{"meta":{"query_hash":"9b02cbf431db","filters":{"topic":"Catalysts for Methane Reforming"},"cohort_total":643,"direct_labels_cover":2,"predictions_cover":643,"exported":643,"export_cap":100000,"truncated":false,"label_status":"direct model label, unvalidated","prediction_status":"machine_predicted_unvalidated (Codex and Gemma teacher distillation)","score_status":"score_only:v0-immature-baseline","snapshot":{"source":"OpenAlex, pinned release, all 482 partitions","release":"2026-06-24","frame_built":"2026-07-12"},"permalink":"https://metacan.xera.ac/q/9b02cbf431db","api":"https://metacan.xera.ac/api/v1/cohort?topic=Catalysts+for+Methane+Reforming"},"results":[{"id":"W1500627386","doi":"10.5539/mas.v9n7p74","title":"The Pyrolysis of Glycerol Using Microwave for the Production of Hydrogen","year":2015,"lang":"en","type":"article","venue":"Modern Applied Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Pyrolysis; Methanol; Hydrogen; Glycerol; Microwave; Activated carbon; Carbon fibers; Materials science; Hydrogen production; Chemical engineering; Nuclear chemistry; Chemistry; Inorganic chemistry; Organic chemistry; Composite material; Adsorption","score_opus":0.037452468666064366,"score_gpt":0.2659913353712067,"score_spread":0.22853886670514237,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1500627386","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8757607,0.0002006867,0.1231404,0.00007548772,0.00012304306,0.00036387812,0.000002255647,0.000020408392,0.00031314488],"genre_scores_gemma":[0.9984153,0.0000023111613,0.0014238271,0.000004046274,0.0000514251,0.000025508209,5.319957e-7,0.000011338111,0.00006569128],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989429,0.0000034771679,0.00022495512,0.00020157955,0.00040219413,0.00022489086],"domain_scores_gemma":[0.99914193,0.00010199612,0.00014360863,0.00043156752,0.00013453969,0.000046356367],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012180714,0.000079072975,0.00013000322,0.000050816125,0.00015493915,0.000010211636,0.00048782787,0.0000270229,3.5432282e-7],"category_scores_gemma":[0.000309554,0.000044763143,0.000058823498,0.0004492479,0.0004239197,0.00008432385,0.000117431555,0.000066480694,8.753135e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000031673873,0.000007668394,0.000005096284,0.0000132369505,0.0000124501985,2.1524283e-8,0.0007012301,0.014856504,0.97467494,0.00047762628,0.0000016719937,0.009217863],"study_design_scores_gemma":[0.00008330254,0.00000483533,0.0000018947409,0.000005455878,0.000022952518,0.0000025665922,0.00016295751,0.29306987,0.70571584,0.0008255745,0.00006541802,0.00003935802],"about_ca_topic_score_codex":0.000043891523,"about_ca_topic_score_gemma":0.0000071175987,"teacher_disagreement_score":0.27821335,"about_ca_system_score_codex":0.000102841725,"about_ca_system_score_gemma":0.00009491787,"threshold_uncertainty_score":0.1825388},"labels":[],"label_agreement":null},{"id":"W1525673254","doi":"10.1002/9783527635603.ch6","title":"German Fischer–Tropsch Facilities","year":2011,"lang":"de","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Fischer–Tropsch process; German; Business; Chemistry; Geography; Archaeology; Catalysis; Organic chemistry","score_opus":0.017959990785107762,"score_gpt":0.23909455746648914,"score_spread":0.22113456668138137,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1525673254","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0026292184,0.0042308653,0.0008786386,0.000025041472,0.0011686472,0.00035335927,0.00016622593,0.00058512005,0.9899629],"genre_scores_gemma":[0.003448866,0.00038151513,0.00092122727,0.00003901447,0.0012891332,0.00004147192,0.00026231975,0.0006848832,0.99293154],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9970698,0.00003214568,0.00069707434,0.0007615067,0.00047025952,0.00096923247],"domain_scores_gemma":[0.99809223,0.00007995297,0.00022455379,0.0012085219,0.00005616337,0.00033857816],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00019256055,0.00090577593,0.0010111535,0.0003693018,0.000058657042,0.00003582441,0.0007132262,0.0010580071,0.25210044],"category_scores_gemma":[0.00012625527,0.00078883104,0.0005509875,0.0002138378,0.00014484081,0.00013473396,0.00036611222,0.0010005675,0.058219813],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00035090762,0.0012128365,0.00042961165,0.022095926,0.014869416,0.0008860102,0.020199548,0.000048107097,0.34507123,0.078326195,0.40920007,0.107310146],"study_design_scores_gemma":[0.00037516947,0.000028732265,0.0000043778264,0.00029725782,0.00018643639,0.000023429991,0.00014463784,0.00014967767,0.06367086,0.0001023527,0.93402207,0.0009950254],"about_ca_topic_score_codex":0.001923907,"about_ca_topic_score_gemma":0.0001017103,"teacher_disagreement_score":0.52482194,"about_ca_system_score_codex":0.00025327553,"about_ca_system_score_gemma":0.00007095455,"threshold_uncertainty_score":0.9994563},"labels":[],"label_agreement":null},{"id":"W1554523783","doi":"10.1002/9783527635603.ch5","title":"Fischer–Tropsch Gas Loop","year":2011,"lang":"de","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Fischer–Tropsch process; Loop (graph theory); Process engineering; Chemistry; Engineering; Mathematics; Combinatorics; Catalysis; Organic chemistry","score_opus":0.016153613126133108,"score_gpt":0.22551470075581145,"score_spread":0.20936108762967834,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1554523783","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0014193141,0.0051238486,0.001584562,0.00004774829,0.001474573,0.00039418545,0.000037355523,0.0006547812,0.98926365],"genre_scores_gemma":[0.0011907442,0.00062132353,0.0023608345,0.00007215035,0.0020081738,0.00003500761,0.0002178145,0.0011822049,0.9923118],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.9968807,0.000030176156,0.00070446363,0.00086553016,0.00048568562,0.0010334187],"domain_scores_gemma":[0.9977965,0.00007963247,0.0002835068,0.0013514645,0.00006370042,0.0004252156],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00023273344,0.0009301469,0.0010469186,0.00037918007,0.000047753838,0.0000317528,0.0008135422,0.0012240274,0.18713441],"category_scores_gemma":[0.00019497488,0.00080349355,0.00057737186,0.00035927712,0.00010150067,0.000107853775,0.00039957598,0.0011643942,0.06899768],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027856202,0.0012423254,0.00045448993,0.0072781085,0.009929532,0.000978468,0.0018217071,0.000053424785,0.49658358,0.028182197,0.30066252,0.15253508],"study_design_scores_gemma":[0.00057461055,0.000037565525,0.000003047498,0.00048617175,0.000369091,0.000039063307,0.000042359407,0.00039959338,0.14258306,0.00007178907,0.85429204,0.0011016149],"about_ca_topic_score_codex":0.0011041949,"about_ca_topic_score_gemma":0.000071881725,"teacher_disagreement_score":0.5536295,"about_ca_system_score_codex":0.00026868214,"about_ca_system_score_gemma":0.00008225086,"threshold_uncertainty_score":0.9994416},"labels":[],"label_agreement":null},{"id":"W1606444741","doi":"10.5539/mas.v9n7p47","title":"Development of Hybrid Fischer-Tropsch Synthesis Catalysts for Direct Production of Synthetic Gasoline from Coal-Based Syngas: An Indonesian Perspective","year":2015,"lang":"en","type":"article","venue":"Modern Applied Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Direktorat Jenderal Pendidikan Tinggi","keywords":"Fischer–Tropsch process; Product distribution; Catalysis; Syngas; Zeolite; Gasoline; Chemical engineering; Coal; Hydrocarbon; Materials science; Chemistry; Organic chemistry; Selectivity","score_opus":0.031314775203788996,"score_gpt":0.26895910010279167,"score_spread":0.23764432489900267,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1606444741","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.900793,0.000045978355,0.0978245,0.00003892888,0.00010934104,0.0004903043,0.000038406954,0.000091860136,0.00056768564],"genre_scores_gemma":[0.96856296,4.5842629e-7,0.031123484,0.000003730621,0.000052382424,0.00017646606,0.000026792895,0.00003743615,0.000016272805],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99765646,0.000015665666,0.0004888001,0.0007088301,0.0007354855,0.00039474785],"domain_scores_gemma":[0.9983991,0.00013240996,0.00026817052,0.00062588585,0.00035534942,0.00021911005],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011613343,0.00023203356,0.00047242257,0.0002658152,0.00010918685,0.000014185734,0.00055130944,0.00005091249,0.0000023548544],"category_scores_gemma":[0.0008366689,0.00021093852,0.000073781586,0.00044807344,0.0003265346,0.00022579833,0.00009995119,0.00011682717,0.0000034919638],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014259668,0.00015725098,0.000036605314,0.00006755497,0.000028325516,7.0139134e-7,0.0022272517,0.0039500277,0.9894711,0.000101041005,0.0000016896976,0.0038158563],"study_design_scores_gemma":[0.00030353773,0.000021104746,0.000054650332,0.0000765056,0.000051992545,0.0000029891278,0.0007894036,0.09896488,0.8992618,0.00023581808,0.000018600378,0.00021872627],"about_ca_topic_score_codex":0.00018288844,"about_ca_topic_score_gemma":0.000042133735,"teacher_disagreement_score":0.09501485,"about_ca_system_score_codex":0.0005574042,"about_ca_system_score_gemma":0.00055014214,"threshold_uncertainty_score":0.86018234},"labels":[],"label_agreement":null},{"id":"W1606995771","doi":"10.1002/9780470974001.f302012","title":"Catalyst development and kinetics for methanol fuel processing","year":2010,"lang":"en","type":"other","venue":"Handbook of Fuel Cells","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Royal Military College of Canada","funders":"","keywords":"Catalysis; Methanol; Steam reforming; Hydrogen; Water-gas shift reaction; Chemistry; Chemical engineering; Elementary reaction; Kinetics; Hydrogen production; Chemical kinetics; Thermodynamics; Organic chemistry; Engineering","score_opus":0.013303604578951344,"score_gpt":0.23684949621232795,"score_spread":0.2235458916333766,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1606995771","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0024819027,0.19550532,0.07608674,0.000045318284,0.0026954454,0.005525949,0.00068648055,0.0015121136,0.7154607],"genre_scores_gemma":[0.0041671894,0.0011489164,0.2273188,0.00004022887,0.0010262846,0.00027719472,0.0005030052,0.0020399783,0.7634784],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984064,0.000006337815,0.00048669532,0.00042995843,0.000280712,0.0003898958],"domain_scores_gemma":[0.9989521,0.00007408891,0.00038975693,0.00036708964,0.00007087149,0.00014612939],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00016863232,0.00042681154,0.0006938951,0.00031420388,0.000021193127,0.00001750389,0.00027022572,0.0005640957,0.00016327867],"category_scores_gemma":[0.000054729877,0.00039032925,0.0001249486,0.000105083134,0.00009773888,0.000042499225,0.00013135225,0.000312867,0.000020620835],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017450962,0.00005288358,0.000001909376,0.009998035,0.00014926195,0.0000040036616,0.0006084484,0.000002187396,0.9489522,0.000014680017,0.0015331404,0.0386658],"study_design_scores_gemma":[0.00039194478,0.000014588071,2.4759515e-7,0.0010031218,0.00009744754,0.000006175383,0.00001750705,0.000055849807,0.6062073,0.000017609354,0.39189065,0.00029754284],"about_ca_topic_score_codex":0.00004769439,"about_ca_topic_score_gemma":0.000121900586,"teacher_disagreement_score":0.39035752,"about_ca_system_score_codex":0.00006361207,"about_ca_system_score_gemma":0.000099948054,"threshold_uncertainty_score":0.99985486},"labels":[],"label_agreement":null},{"id":"W173010916","doi":"10.1016/s0167-2991(01)80331-1","title":"Site reactivity of Fischer-Tropsch synthesis catalysts studied by 12CO → 13CO isotope transients","year":2001,"lang":"en","type":"book-chapter","venue":"Studies in surface science and catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Chemistry; Selectivity; Syngas; Reactivity (psychology); Cobalt; Isotope; Methane; Dispersion (optics); Kinetic isotope effect; Inorganic chemistry; Organic chemistry; Deuterium","score_opus":0.027515510665303042,"score_gpt":0.28000111420057944,"score_spread":0.2524856035352764,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W173010916","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.86738837,0.022992672,0.0000300147,0.00018318852,0.0003721714,0.0007129703,0.0004354503,0.00012428635,0.10776088],"genre_scores_gemma":[0.9532448,0.009909077,0.000121308745,0.000018183133,0.000051114886,0.00003813783,0.00006578159,0.00009477461,0.036456794],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9953985,0.000025346297,0.00094596663,0.0013147636,0.0015331779,0.0007822306],"domain_scores_gemma":[0.9973801,0.0004710731,0.00047061805,0.0009946075,0.000489966,0.00019364829],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0018450904,0.0007269227,0.0018597186,0.00051804224,0.00027166642,0.000024957262,0.00073258183,0.00029049025,0.000029854053],"category_scores_gemma":[0.0009928249,0.0006415197,0.00030395706,0.0010682346,0.0020968784,0.00054302806,0.0006876727,0.00060633203,0.000026549233],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019807386,0.0003552878,0.0025146166,0.0018162038,0.0030630045,0.00015785857,0.011907614,0.00037181276,0.9340409,0.0005063172,0.0009845268,0.044083804],"study_design_scores_gemma":[0.0015184032,0.00017856315,0.0002536911,0.00252194,0.00281282,0.00006372647,0.0050362437,0.00057586853,0.9427854,0.0003631419,0.040531248,0.0033589774],"about_ca_topic_score_codex":0.0008165344,"about_ca_topic_score_gemma":0.00044283216,"teacher_disagreement_score":0.08585646,"about_ca_system_score_codex":0.0007350591,"about_ca_system_score_gemma":0.00013107836,"threshold_uncertainty_score":0.9996036},"labels":[],"label_agreement":null},{"id":"W1739271519","doi":"10.1002/wene.167","title":"Review of catalytic syngas production through steam or dry reforming and partial oxidation of studied liquid compounds","year":2015,"lang":"en","type":"article","venue":"Wiley Interdisciplinary Reviews Energy and Environment","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":59,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Syngas; Partial oxidation; Raw material; Steam reforming; Biodiesel production; Carbon dioxide reforming; Syngas to gasoline plus; Production (economics); Waste management; Hydrogen production; Environmental science; Biodiesel; Process engineering; Biochemical engineering; Catalysis; Chemistry; Engineering; Organic chemistry; Economics","score_opus":0.04213348853108297,"score_gpt":0.292152170181034,"score_spread":0.25001868164995106,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1739271519","genre_codex":"review","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.4916576,0.503568,0.002008949,0.00048827627,0.00037195894,0.00082541193,0.000013701273,0.00004768846,0.0010183693],"genre_scores_gemma":[0.5816696,0.41689566,0.0005685822,0.00005174044,0.00015770546,0.00012563082,0.00011721841,0.000035083867,0.00037871703],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99835384,0.000067825255,0.00086600846,0.00033166437,0.0002013621,0.00017929565],"domain_scores_gemma":[0.9990716,0.000030699986,0.00039274304,0.00039048956,0.000019676012,0.00009481907],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006873809,0.00023091589,0.00073269353,0.000045700002,0.000054049415,0.0000023380624,0.0001108289,0.000056912384,0.000014855434],"category_scores_gemma":[0.000098150456,0.000160891,0.000097674536,0.00010948003,0.00014662197,0.00027699486,0.00057165325,0.000097077114,0.0000030711735],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0020139695,0.0011282014,0.00023198132,0.06519411,0.0008430923,0.000028879285,0.010449066,0.0009330958,0.64102596,0.00088872766,0.0018906362,0.2753723],"study_design_scores_gemma":[0.0016988899,0.0022893285,0.000053384236,0.06813194,0.001110478,0.00037380058,0.0018260324,0.001074543,0.72286975,0.00024333158,0.19919696,0.0011315586],"about_ca_topic_score_codex":0.00003361439,"about_ca_topic_score_gemma":0.00000865409,"teacher_disagreement_score":0.27424073,"about_ca_system_score_codex":0.00015429499,"about_ca_system_score_gemma":0.00001392115,"threshold_uncertainty_score":0.65609443},"labels":[],"label_agreement":null},{"id":"W1755522315","doi":"","title":"Deactivation Behavior of Carbon Nanotubes Supported Cobalt Catalysts in Fischer-Tropsch Synthesis","year":2016,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Cobalt; Fischer–Tropsch process; Catalysis; Sintering; Materials science; Chemical engineering; Chemisorption; Cobalt oxide; Carbon nanotube; Carbon fibers; Space velocity; Metal; Inorganic chemistry; Nanotechnology; Chemistry; Metallurgy; Composite material; Selectivity; Composite number; Organic chemistry","score_opus":0.013267039218100527,"score_gpt":0.24014269691198795,"score_spread":0.22687565769388743,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1755522315","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99715024,0.0000219743,0.00014195479,0.00007483358,0.000062757426,0.00016097931,0.000012465415,0.000092875336,0.002281897],"genre_scores_gemma":[0.9990255,0.0000068695535,0.00023920432,0.0000037444104,0.000030127418,0.000075806565,0.000012353131,0.00003346662,0.00057292165],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99872404,0.000019247056,0.00046805394,0.00024147748,0.00026188683,0.00028528957],"domain_scores_gemma":[0.9991738,0.00025453727,0.0001079609,0.00033346858,0.00005989317,0.00007034236],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021704371,0.00016375678,0.0003235607,0.00021564924,0.000010700258,0.0000029463524,0.00016381544,0.00013888326,0.00011167056],"category_scores_gemma":[0.00056566764,0.00011205252,0.00008774619,0.00030579872,0.00003411288,0.00018961988,0.000058091962,0.0000913586,0.000012137916],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019231342,0.00006680484,0.019486293,0.000034583554,0.000021130028,0.000007145225,0.000054091262,0.0000026964237,0.9687392,0.00014091322,0.0000042886863,0.011423593],"study_design_scores_gemma":[0.00036199373,0.0000119830775,0.0073938877,0.00011791181,0.000044621356,0.000008882471,0.000049562495,0.00015057436,0.99158615,0.000011770558,0.000091382484,0.0001713051],"about_ca_topic_score_codex":0.0023218866,"about_ca_topic_score_gemma":0.00030042572,"teacher_disagreement_score":0.022846894,"about_ca_system_score_codex":0.00022961982,"about_ca_system_score_gemma":0.00003705956,"threshold_uncertainty_score":0.45693693},"labels":[],"label_agreement":null},{"id":"W1820126998","doi":"10.1016/j.crci.2015.07.005","title":"Hydrogenation of CO2 into hydrocarbons over bifunctional system Cu–ZnO/Al2O3 + HZSM-5: Effect of proximity between the acidic and methanol synthesis sites","year":2015,"lang":"en","type":"article","venue":"Comptes Rendus Chimie","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Agence Universitaire de la Francophonie","keywords":"Bifunctional; Catalysis; Chemistry; Zeolite; Hydrocarbon; Methanol; Selectivity; Bifunctional catalyst; Nuclear chemistry; Inorganic chemistry; Organic chemistry","score_opus":0.020134703806329014,"score_gpt":0.24732580664762413,"score_spread":0.22719110284129512,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1820126998","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99692655,0.0014121222,0.00038373514,0.00004254061,0.000109491804,0.00033256205,0.00003805235,0.00011402533,0.0006409051],"genre_scores_gemma":[0.9995001,0.0000103475,0.00018189392,0.0000026261052,0.00013784585,0.000055277105,0.000050342747,0.000038188657,0.000023401366],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982855,0.00014762823,0.0005086049,0.00029163802,0.0005227979,0.00024386632],"domain_scores_gemma":[0.9977266,0.0013330487,0.0002988494,0.00043274392,0.00006635886,0.00014237888],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008894563,0.0002679157,0.0006303168,0.00019392258,0.000066637665,0.00001088298,0.0002802494,0.00016540977,0.000015486208],"category_scores_gemma":[0.0008419029,0.00018306974,0.00017444575,0.00037304388,0.00020343579,0.000161248,0.00020149036,0.00025711794,0.000010436208],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014539399,0.00006338565,0.054534037,0.0014212837,0.000846745,0.0000036401027,0.00052477175,0.00045157206,0.9357813,0.0005755025,0.00011996032,0.0055323914],"study_design_scores_gemma":[0.0005912951,0.00010331456,0.0022657497,0.00026066945,0.00039271443,0.000022139617,0.00007905263,0.019532846,0.97636336,0.00009129906,0.00009577189,0.00020178138],"about_ca_topic_score_codex":0.00027253918,"about_ca_topic_score_gemma":0.0000102233635,"teacher_disagreement_score":0.05226829,"about_ca_system_score_codex":0.00020572524,"about_ca_system_score_gemma":0.000038807768,"threshold_uncertainty_score":0.74653673},"labels":[],"label_agreement":null},{"id":"W1840655355","doi":"10.1016/j.micromeso.2015.08.034","title":"Highly active and stable Ni/SBA-15 catalysts prepared by a “two solvents” method for dry reforming of methane","year":2015,"lang":"en","type":"article","venue":"Microporous and Mesoporous Materials","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":104,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Agence Universitaire de la Francophonie","keywords":"Methane; Catalysis; Carbon dioxide reforming; Chemistry; Chemical engineering; Inorganic chemistry; Materials science; Organic chemistry; Syngas","score_opus":0.014914106908064632,"score_gpt":0.277833041208035,"score_spread":0.2629189342999704,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1840655355","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99196225,0.0023047933,0.0030190651,0.0000497445,0.00038763628,0.00085973565,0.0010557157,0.00013014748,0.00023089224],"genre_scores_gemma":[0.9710521,0.00014029405,0.024400705,0.0000510425,0.00022224433,0.00018181915,0.0007486385,0.00017024213,0.0030329013],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974583,0.00008493131,0.0008809571,0.00062908255,0.00029113126,0.0006556401],"domain_scores_gemma":[0.998382,0.00013256345,0.00050987216,0.0004476419,0.00020754823,0.00032042502],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013694519,0.00044398935,0.0011400864,0.00015237124,0.0000782826,0.000041503896,0.00022617698,0.00021894864,0.000025286643],"category_scores_gemma":[0.0002822685,0.0003827923,0.0000949764,0.00014691318,0.00010583843,0.00043023608,0.0002814134,0.00011837207,0.0000033425974],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004952368,0.00007372717,0.00001935387,0.000516795,0.00022189335,0.0000094601355,0.0021224706,0.0000044096646,0.98698366,0.0001238857,0.0003119504,0.009117182],"study_design_scores_gemma":[0.0027516861,0.00018255941,0.00000411874,0.00010539832,0.00022085679,0.00013276619,0.0010363604,0.00007946149,0.98709947,0.00046004335,0.0074886223,0.0004386713],"about_ca_topic_score_codex":0.008123684,"about_ca_topic_score_gemma":0.00012307214,"teacher_disagreement_score":0.02138164,"about_ca_system_score_codex":0.00022532223,"about_ca_system_score_gemma":0.000102265054,"threshold_uncertainty_score":0.9998624},"labels":[],"label_agreement":null},{"id":"W1843175804","doi":"10.1039/c5ta06184a","title":"Direct confinement of Ru nanoparticles inside nanochannels of large pore mesoporous aluminosilicate for Fischer–Tropsch synthesis","year":2015,"lang":"en","type":"article","venue":"Journal of Materials Chemistry A","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Centre in Green Chemistry and Catalysis","funders":"National Research Foundation of Korea; Korea Research Institute of Chemical Technology; Ministry of Oceans and Fisheries","keywords":"Aluminosilicate; Fischer–Tropsch process; Mesoporous material; Nanoparticle; Materials science; Chemical engineering; Catalysis; Nanotechnology; Chemistry; Organic chemistry","score_opus":0.024263243853464147,"score_gpt":0.26200353210987526,"score_spread":0.2377402882564111,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1843175804","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99872833,0.00032144325,0.000082176484,0.00008775886,0.00015950229,0.00012729842,0.00019671225,0.000017335955,0.00027944843],"genre_scores_gemma":[0.9986715,0.000020760386,0.00086503744,0.000007694356,0.0002299265,0.000019811014,0.000015833702,0.000036784575,0.0001327081],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99786216,0.000029484792,0.0012747635,0.00015075596,0.0003852937,0.00029754962],"domain_scores_gemma":[0.99782205,0.00017591579,0.001143004,0.0002684884,0.00041229517,0.00017826777],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012694624,0.00020668273,0.00086021656,0.000051945015,0.000018983055,0.000010425177,0.00030120098,0.00013695467,0.0001275049],"category_scores_gemma":[0.0015001463,0.0001701684,0.0002133361,0.00009469667,0.000052919928,0.00011441729,0.00009112115,0.000081928454,0.0000012797534],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003730247,0.00015806584,0.000019558747,0.0009218537,0.00021282845,0.000015564747,0.00024780486,0.00009866735,0.9976514,0.00001515947,0.00015309661,0.00013296101],"study_design_scores_gemma":[0.0011426213,0.00007055501,0.000011733927,0.0003618252,0.0001955037,0.00012209515,0.00029335197,0.000043992706,0.9966274,0.000044717264,0.0009262422,0.0001599798],"about_ca_topic_score_codex":0.000023339802,"about_ca_topic_score_gemma":5.4664457e-7,"teacher_disagreement_score":0.0010240327,"about_ca_system_score_codex":0.00009347851,"about_ca_system_score_gemma":0.00011115311,"threshold_uncertainty_score":0.6939266},"labels":[],"label_agreement":null},{"id":"W190462248","doi":"10.1016/b978-008044276-1/50307-x","title":"Processing of Non Purified Ethanol From a Glucose Fermentation Process for Solid Oxide Fuel Cell Application","year":2003,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Ethanol; Fermentation; Chemistry; Process (computing); Oxide; Chromatography; Chemical engineering; Pulp and paper industry; Biochemistry; Organic chemistry; Computer science; Engineering","score_opus":0.014356324669598224,"score_gpt":0.2670230633227873,"score_spread":0.25266673865318906,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W190462248","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.011841469,0.002158614,0.0063077956,0.000018452283,0.00018110572,0.00365589,0.0002323962,0.00021375009,0.97539055],"genre_scores_gemma":[0.24502406,0.000112219,0.0053553116,0.00014597706,0.0005158265,0.0016577537,0.001528739,0.0006614796,0.74499863],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99759364,0.000008233127,0.00091906154,0.0006648205,0.00044382943,0.00037038786],"domain_scores_gemma":[0.99814504,0.00006116834,0.00088246376,0.0005230894,0.00026290934,0.00012530349],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00021913128,0.00054764515,0.00080185785,0.00020865779,0.00006265557,0.000020989652,0.0003345841,0.00057021354,0.000020518464],"category_scores_gemma":[0.000034319815,0.000558868,0.0003119539,0.00003798005,0.000062377745,0.000120184086,0.00005363959,0.00042979774,0.000020398047],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000052265,0.000021036152,6.8889807e-7,0.0029118424,0.00006722366,0.0000012675581,0.0005563295,0.00003193014,0.577218,0.00006507457,0.0000014308855,0.4190729],"study_design_scores_gemma":[0.0010327467,0.000039387054,0.0000013138443,0.00095309166,0.000417129,0.0000047466647,0.000046321584,0.0016967229,0.95418096,0.0070935357,0.033879522,0.00065451284],"about_ca_topic_score_codex":0.0000031863262,"about_ca_topic_score_gemma":0.0000056556228,"teacher_disagreement_score":0.4184184,"about_ca_system_score_codex":0.00025717064,"about_ca_system_score_gemma":0.00012746625,"threshold_uncertainty_score":0.9996863},"labels":[],"label_agreement":null},{"id":"W1963522024","doi":"10.1016/j.ces.2009.05.025","title":"Pure hydrogen generation in a fluidized bed membrane reactor: Application of the generalized comprehensive reactor model","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":44,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Membrane Reactor Technologies (Canada); University of British Columbia","funders":"","keywords":"Membrane reactor; Fluidization; Fluidized bed; Nuclear engineering; Hydrogen production; Steam reforming; Continuous stirred-tank reactor; Mass transfer; Plug flow reactor model; Chemistry; Hydrogen; Process engineering; Mechanics; Thermodynamics; Waste management; Chemical engineering; Engineering; Chromatography; Physics","score_opus":0.015549929189669196,"score_gpt":0.23976146501658105,"score_spread":0.22421153582691186,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1963522024","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9967735,0.000095051975,0.0025293145,0.00010718145,0.00005895537,0.00027717647,0.0000060037833,0.00010770197,0.000045122575],"genre_scores_gemma":[0.996782,0.0000068010913,0.003014153,0.00003856716,0.00008102544,0.000027669212,0.000022120797,0.000021293508,0.0000063382445],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99819636,0.0000070486717,0.00045208816,0.00041780982,0.0005286202,0.00039806517],"domain_scores_gemma":[0.9990348,0.00004166124,0.00010937319,0.0005852704,0.000104645536,0.00012422618],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024996267,0.00021802683,0.00032148114,0.00015461164,0.00003019662,0.000014023588,0.0006593603,0.00013016001,0.0000024845287],"category_scores_gemma":[0.0003813622,0.00017538512,0.00011839025,0.0011365617,0.00010667633,0.0002635772,0.00010087574,0.00028908695,0.0000023446137],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000008551843,0.000027419872,0.0000053639346,0.000028133782,0.0000041584353,5.8686425e-7,0.00016459424,0.04876928,0.94978046,0.00074027607,0.0000022484749,0.0004688947],"study_design_scores_gemma":[0.00025531597,0.0000030101849,0.000007007631,0.000020673166,0.000006209369,0.000006398468,0.0000026123312,0.45324633,0.54629743,0.000030664785,0.000015090508,0.000109298344],"about_ca_topic_score_codex":0.000026188325,"about_ca_topic_score_gemma":6.889439e-7,"teacher_disagreement_score":0.40447703,"about_ca_system_score_codex":0.0003400356,"about_ca_system_score_gemma":0.0000712831,"threshold_uncertainty_score":0.71519977},"labels":[],"label_agreement":null},{"id":"W1963724753","doi":"10.1016/j.jpowsour.2015.03.081","title":"Effect of the porous structure of the support on hydrocarbon distribution in the Fischer–Tropsch reaction","year":2015,"lang":"en","type":"article","venue":"Journal of Power Sources","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":35,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Fischer–Tropsch process; Selectivity; Hydrocarbon; Diesel fuel; Chemical engineering; Porosity; Catalysis; Mesoporous material; Chemistry; Particulates; Carbon dioxide; Polymerization; Carbon fibers; Diesel exhaust; Volume (thermodynamics); Materials science; Organic chemistry; Composite material; Polymer; Thermodynamics","score_opus":0.006127399700225133,"score_gpt":0.23239153464030599,"score_spread":0.22626413494008085,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1963724753","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9988515,0.00008302585,0.000013789792,0.00022491338,0.000353196,0.000104435116,0.000010515682,0.0000037531368,0.0003548999],"genre_scores_gemma":[0.99983233,0.0000020472148,0.0000031971986,0.000012963983,0.000104675055,5.78518e-7,0.0000026434286,0.000010473297,0.00003111712],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998643,0.0001559051,0.0004072052,0.00006681237,0.0005990553,0.00012803292],"domain_scores_gemma":[0.9988891,0.00016673944,0.0005765033,0.00027028896,0.0000642881,0.000033113152],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00095625105,0.00011398585,0.00024154545,0.000044589277,0.00002465793,0.000006527784,0.00040955486,0.00009143341,0.000005108815],"category_scores_gemma":[0.00066069287,0.00004570873,0.0001864008,0.0002576493,0.000050688297,0.000089460256,0.00004877811,0.0005380192,4.5418395e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00044667828,0.000078437275,0.015248046,0.00009336955,0.00011376321,0.000007565914,0.0045182086,0.0024745092,0.9750396,0.00010196623,0.00019079528,0.001687042],"study_design_scores_gemma":[0.00077432574,0.0004577867,0.0114173405,0.00017087991,0.00010110218,0.00022770827,0.0005283403,0.000116333074,0.98458225,0.00009036138,0.0014582456,0.00007533705],"about_ca_topic_score_codex":0.00006508887,"about_ca_topic_score_gemma":0.000011594846,"teacher_disagreement_score":0.009542621,"about_ca_system_score_codex":0.00013207282,"about_ca_system_score_gemma":0.000035949364,"threshold_uncertainty_score":0.23374556},"labels":[],"label_agreement":null},{"id":"W1966473352","doi":"10.1002/cjce.21698","title":"Phenomenological‐based kinetics modelling of dehydrogenation of ethylbenzene to styrene over a Mg<sub>3</sub>Fe<sub>0.25</sub>Mn<sub>0.25</sub>Al<sub>0.5</sub> hydrotalcite catalyst","year":2012,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":true,"ca_institutions":"","funders":"King Abdullah University of Science and Technology","keywords":"Dehydrogenation; Ethylbenzene; Catalysis; Kinetics; Styrene; Activation energy; Chemistry; Thermodynamics; Chemical kinetics; Physical chemistry; Reaction mechanism; Materials science; Organic chemistry; Polymer; Copolymer; Physics","score_opus":0.01733622543312485,"score_gpt":0.2068389770485485,"score_spread":0.18950275161542365,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1966473352","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9786952,0.0015810521,0.018131424,0.00024099697,0.00048503416,0.0005149688,0.0001631227,0.00011081726,0.00007734744],"genre_scores_gemma":[0.9977607,0.0000727857,0.0008657344,0.00015086037,0.00069706526,0.000039861436,0.00011594997,0.00029508627,0.0000019255272],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99354917,0.00008642012,0.0023805797,0.0006247409,0.0013494751,0.0020095916],"domain_scores_gemma":[0.9946061,0.0005671235,0.0010770618,0.0010252631,0.0005614388,0.0021630488],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001473211,0.0010380246,0.0016051161,0.0012433412,0.00014883814,0.00007205032,0.0012642834,0.0006992988,0.000014704118],"category_scores_gemma":[0.0010550302,0.0009599815,0.0008414864,0.0016706171,0.00023818557,0.00060848525,0.00022752701,0.001807798,0.000023251463],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006771339,0.00008988948,0.000021529691,0.00025619759,0.00030573102,0.000033411736,0.00057285023,0.27758428,0.71916205,0.00012140593,0.00002531924,0.0017596099],"study_design_scores_gemma":[0.0011988232,0.00012272384,0.00004063634,0.0006644572,0.00036472298,0.00019812581,0.000043110726,0.10870042,0.88752395,0.00007274886,0.00018168477,0.00088859914],"about_ca_topic_score_codex":0.00028117737,"about_ca_topic_score_gemma":0.00017831364,"teacher_disagreement_score":0.16888386,"about_ca_system_score_codex":0.001811845,"about_ca_system_score_gemma":0.00045533522,"threshold_uncertainty_score":0.99928504},"labels":[],"label_agreement":null},{"id":"W1968050212","doi":"10.1021/ie0341799","title":"Bifurcation Behavior and Efficient Pure Hydrogen Production for Fuel Cells Using a Novel Autothermic Membrane Circulating Fluidized-Bed (CFB) Reformer:  Sequential Debottlenecking and the Contribution of John Grace","year":2004,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"Auburn University","keywords":"Fluidization; Columbia university; Steam reforming; Government (linguistics); Fluidized bed; Engineering; Hydrogen production; Chemical engineering; Chemistry; Management; Hydrogen; Waste management; Philosophy; Economics; Sociology; Organic chemistry","score_opus":0.05923486646488657,"score_gpt":0.31439736536791224,"score_spread":0.25516249890302567,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1968050212","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9971477,0.0004401973,0.0009210565,0.00008533808,0.00015628582,0.0011314783,0.000025335285,0.00008557591,0.0000070666897],"genre_scores_gemma":[0.99897605,0.000023501232,0.00022926845,8.2438316e-7,0.00050231005,0.00014487011,0.000046707002,0.00006313276,0.000013322266],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978542,0.000027435186,0.00055721786,0.00044994862,0.0005501993,0.00056100945],"domain_scores_gemma":[0.9988704,0.00023131215,0.0001700171,0.00032374513,0.00027855366,0.0001260198],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0020061112,0.00025139307,0.00039482594,0.00014803956,0.00019666852,0.000047500263,0.00019232543,0.00034753085,0.000004710849],"category_scores_gemma":[0.0016177621,0.0002173697,0.000115257775,0.00053013297,0.00018845311,0.00013469551,0.00014135928,0.0006771953,3.228689e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016297385,0.000041731106,0.00001647668,0.00035955876,0.00006363861,0.0000015120629,0.00023349073,0.06773609,0.93095267,0.00009451958,1.6629684e-7,0.00033714628],"study_design_scores_gemma":[0.0042436155,0.000016900489,0.0000033819363,0.00034553956,0.000104763305,0.000097383396,0.000096047406,0.06637803,0.9284722,0.000016054351,0.000023610412,0.00020246017],"about_ca_topic_score_codex":0.00026509605,"about_ca_topic_score_gemma":0.0000020089387,"teacher_disagreement_score":0.004080642,"about_ca_system_score_codex":0.0005642234,"about_ca_system_score_gemma":0.00015563743,"threshold_uncertainty_score":0.8864079},"labels":[],"label_agreement":null},{"id":"W1968356698","doi":"10.1021/je900984c","title":"Effects of Confinement in Carbon Nanotubes on the Activity, Selectivity, and Lifetime of Fischer−Tropsch Co/Carbon Nanotube Catalysts","year":2010,"lang":"en","type":"article","venue":"Journal of Chemical & Engineering Data","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":110,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; Université de Sherbrooke","funders":"","keywords":"Cobalt; Fischer–Tropsch process; Catalysis; Chemistry; Carbon nanotube; Sintering; Chemisorption; Chemical engineering; Particle size; Temperature-programmed reduction; Transmission electron microscopy; Nanotechnology; Inorganic chemistry; Selectivity; Materials science; Physical chemistry; Organic chemistry","score_opus":0.009314113267608799,"score_gpt":0.23939851263354683,"score_spread":0.23008439936593802,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1968356698","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9991209,0.0002231328,0.00004281233,0.00013824455,0.00017047292,0.00017028258,0.000021995205,0.000017747063,0.00009442178],"genre_scores_gemma":[0.9994351,0.000025037629,0.0002983447,0.000006012733,0.00017044424,0.0000048557918,0.000011606516,0.000042088916,0.0000064597198],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981736,0.000027250228,0.0006627475,0.00025708924,0.00056285807,0.0003164671],"domain_scores_gemma":[0.9976935,0.0010983164,0.0003475348,0.00063984987,0.00008694124,0.00013386288],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008541143,0.0002787635,0.00070696353,0.00023393886,0.0000091708225,0.000011028828,0.00077218126,0.00019052571,0.00000521102],"category_scores_gemma":[0.0020127734,0.00020647502,0.00010544669,0.00033549409,0.00008312107,0.00015539741,0.0003674559,0.001149102,2.815712e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008687491,0.00016715069,0.00040350397,0.00042999524,0.00014863886,0.000016553937,0.00008797059,0.00015280537,0.997809,0.000062616215,0.00001426646,0.0006206486],"study_design_scores_gemma":[0.00081504753,0.00008337918,0.00052459084,0.00043548245,0.00009768196,0.00007307461,0.000005218545,0.017204992,0.9804386,0.000009467197,0.00012666434,0.00018581082],"about_ca_topic_score_codex":0.00015492974,"about_ca_topic_score_gemma":0.000004921391,"teacher_disagreement_score":0.017370384,"about_ca_system_score_codex":0.00007214143,"about_ca_system_score_gemma":0.00006363605,"threshold_uncertainty_score":0.8419807},"labels":[],"label_agreement":null},{"id":"W1970961051","doi":"10.1007/s10529-006-9114-7","title":"Supersaturation of Dissolved H2 and CO2 During Fermentative Hydrogen Production with N2 Sparging","year":2006,"lang":"en","type":"article","venue":"Biotechnology Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":100,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Sparging; Supersaturation; Fermentative hydrogen production; Chemistry; Hydrogen; Hydrogen production; Environmental chemistry; Organic chemistry; Biohydrogen","score_opus":0.0036802750353156204,"score_gpt":0.18332598024617713,"score_spread":0.1796457052108615,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1970961051","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9965706,0.00006391895,0.00058256136,0.0023786973,0.000037192447,0.00016161481,0.0000027488156,0.00018626043,0.000016430924],"genre_scores_gemma":[0.9989696,0.0000067893798,0.00087852235,0.000011908235,0.000047205005,0.000012375525,0.000022326023,0.000020077396,0.000031179352],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99927884,0.000007450396,0.00017230291,0.00024538112,0.00010052702,0.00019552368],"domain_scores_gemma":[0.9997048,0.000011015888,0.00008389877,0.00017005316,0.00001351239,0.000016713211],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00005476232,0.000126392,0.00016589717,0.00017461891,0.00005098899,0.000003574808,0.000068248584,0.00012053422,0.0000023612827],"category_scores_gemma":[0.000025127698,0.00010942165,0.000025329491,0.00021789686,0.00016844767,0.00013417855,0.000039837745,0.0001703177,0.000001436695],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003287215,0.000011461759,0.0016367545,0.00005088965,0.00003764064,0.0000073483307,0.00011903462,0.00040098303,0.9972932,0.00016819923,0.0000024858346,0.0002391286],"study_design_scores_gemma":[0.00035823297,0.000018027371,0.0021518676,0.00004757084,0.00003067628,0.000075069336,0.00016026844,0.00023316382,0.9967602,0.000013074167,0.000022084589,0.00012978006],"about_ca_topic_score_codex":0.00013933539,"about_ca_topic_score_gemma":0.000022980103,"teacher_disagreement_score":0.0023990418,"about_ca_system_score_codex":0.000097195625,"about_ca_system_score_gemma":0.000003650075,"threshold_uncertainty_score":0.44620854},"labels":[],"label_agreement":null},{"id":"W1971739937","doi":"10.1021/ie070049e","title":"CO<sub>2</sub> Reforming of CH<sub>4</sub> over Xerogel Ni−Ti and Ni−Ti−Al Catalysts","year":2007,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Thermogravimetric analysis; Differential thermal analysis; Materials science; Carbon fibers; Thermal stability; Chemical engineering; Nickel; Deposition (geology); Inorganic chemistry; Diffraction; Metallurgy; Chemistry; Composite material; Organic chemistry; Composite number","score_opus":0.041608692264641284,"score_gpt":0.31354025515613876,"score_spread":0.27193156289149745,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1971739937","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.997425,0.00046972398,0.0000719411,0.00005862663,0.00033946015,0.00044977444,0.000084215084,0.0003091518,0.0007921129],"genre_scores_gemma":[0.99783826,0.00009009574,0.000031808464,0.000006958472,0.0014237516,0.000049582464,0.00018713977,0.00021446646,0.00015794301],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9937551,0.000037898182,0.0012925796,0.0009824085,0.0018745413,0.0020574469],"domain_scores_gemma":[0.99685127,0.0006888831,0.0002375519,0.0010664616,0.0003257129,0.00083009544],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0036112692,0.00070067256,0.0009540104,0.00053524453,0.00019889772,0.000079871665,0.0008087497,0.0010998655,0.000024958905],"category_scores_gemma":[0.0024852664,0.00074145995,0.00026917053,0.00154781,0.00030154092,0.00043842537,0.0005264115,0.003253407,0.000028856033],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001871995,0.00008017715,0.00038575073,0.0005482728,0.00019767096,0.00013434608,0.00017173942,0.0003971787,0.9866427,0.00002073963,0.0002688795,0.0109653305],"study_design_scores_gemma":[0.0020261486,0.000055459415,0.0001294603,0.0005870807,0.00005164509,0.00018737202,0.00016163172,0.0014764986,0.9930661,0.000008470894,0.0015373009,0.00071286253],"about_ca_topic_score_codex":0.00027358043,"about_ca_topic_score_gemma":0.000013037045,"teacher_disagreement_score":0.010252468,"about_ca_system_score_codex":0.0011141454,"about_ca_system_score_gemma":0.00027951636,"threshold_uncertainty_score":0.9995037},"labels":[],"label_agreement":null},{"id":"W1971876886","doi":"10.1016/j.jcat.2011.04.012","title":"Insight into methanol synthesis from CO2 hydrogenation on Cu(1 1 1): Complex reaction network and the effects of H2O","year":2011,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":460,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Pacific Northwest National Laboratory; National Key Research and Development Program of China; Laboratory Directed Research and Development; National Natural Science Foundation of China","keywords":"Chemistry; Methanol; Catalysis; Formate; Methyl formate; Hydrogen; Reaction mechanism; Dimer; Transfer hydrogenation; Combinatorial chemistry; Organic chemistry; Ruthenium","score_opus":0.01384188665439101,"score_gpt":0.22119510172321846,"score_spread":0.20735321506882745,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1971876886","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970169,0.0010090648,0.0009176652,0.00006699549,0.00018191263,0.000100785786,0.0000020913726,0.000014373991,0.00069017505],"genre_scores_gemma":[0.99855196,0.00019801923,0.0009495165,0.000022177996,0.00022224047,0.000006981221,0.000008696494,0.000022837148,0.00001756994],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986675,0.00009991101,0.0005810895,0.00012763082,0.00038257573,0.0001413256],"domain_scores_gemma":[0.9975193,0.0013127589,0.0006983561,0.00027042913,0.000118755896,0.000080356076],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006342847,0.00015380017,0.0005568229,0.00020270837,0.000055142034,0.000008337957,0.00018131663,0.0000944145,0.00002296592],"category_scores_gemma":[0.0010255651,0.000097378914,0.00028958695,0.0003353645,0.00008211782,0.00022186748,0.000054113934,0.00025215463,0.0000047466965],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005495908,0.000085334636,0.00016966484,0.00011236775,0.0013976688,0.000024436269,0.0034596436,0.00016904365,0.9714896,0.00036097548,0.000028401386,0.022153253],"study_design_scores_gemma":[0.0009489509,0.00006501329,0.001408482,0.00024323551,0.0011987721,0.000049477327,0.00009638056,0.001794351,0.99272716,0.0009783404,0.00036131573,0.00012849762],"about_ca_topic_score_codex":0.0006361866,"about_ca_topic_score_gemma":0.000037160127,"teacher_disagreement_score":0.022024756,"about_ca_system_score_codex":0.00010993709,"about_ca_system_score_gemma":0.000015458658,"threshold_uncertainty_score":0.39709967},"labels":[],"label_agreement":null},{"id":"W1975393105","doi":"10.7122/151514-ms","title":"Utilization of Carbon Dioxide as Regenerative Agent for Deactivated Co-Ni Steam Reforming Catalysts","year":2012,"lang":"en","type":"article","venue":"Carbon Management Technology Conference","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Carbon dioxide; Steam reforming; Catalysis; Carbon dioxide reforming; Materials science; Chemical engineering; Waste management; Environmental science; Chemistry; Syngas; Engineering; Organic chemistry; Hydrogen production","score_opus":0.03516284242949182,"score_gpt":0.2905374262320333,"score_spread":0.2553745838025415,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1975393105","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97865206,0.0005157119,0.0026836281,0.00010271678,0.00026443266,0.0009141142,0.000010000095,0.00048417677,0.016373172],"genre_scores_gemma":[0.9978709,0.00008459294,0.0005322556,0.000015619335,0.000050126982,0.00027926877,0.000111524954,0.000053389904,0.0010023266],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981519,0.000021850205,0.0005323409,0.0004085789,0.0002706895,0.0006146128],"domain_scores_gemma":[0.99871325,0.000041910487,0.0003221285,0.0006810752,0.00015933276,0.00008231772],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00033536516,0.00031707864,0.00046919874,0.00061905215,0.000055609664,0.000005205101,0.00042719027,0.0003074035,0.0000071427053],"category_scores_gemma":[0.00020642117,0.0003069181,0.00009096891,0.0006388567,0.00013645714,0.00016961117,0.0002485004,0.00024654332,0.000004765359],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005874675,0.00010638476,0.0016564572,0.00041583378,0.00036373004,0.000008241251,0.00038758846,0.00003795364,0.9220029,0.044114277,0.000010212828,0.030837681],"study_design_scores_gemma":[0.0006456059,0.000064080006,0.00008577818,0.0001706913,0.00016153054,0.000011377451,0.0011811272,0.002541078,0.99285346,0.0003733655,0.0015883634,0.00032355482],"about_ca_topic_score_codex":0.00016642557,"about_ca_topic_score_gemma":0.000018370849,"teacher_disagreement_score":0.07085055,"about_ca_system_score_codex":0.00039367526,"about_ca_system_score_gemma":0.000031829106,"threshold_uncertainty_score":0.9999383},"labels":[],"label_agreement":null},{"id":"W1977350374","doi":"10.1002/cjce.20105","title":"Morphology and deactivation behaviour of Co–Ru/γ‐Al<sub>2</sub>O<sub>3</sub> Fischer–Tropsch synthesis catalyst","year":2008,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Fischer–Tropsch process; Sintering; Chemistry; Chemisorption; Cobalt; Coke; Dispersion (optics); Particle size; Carbon monoxide; Chemical engineering; Inorganic chemistry; Selectivity; Physical chemistry; Organic chemistry; Physics","score_opus":0.010397281043096125,"score_gpt":0.1969683808497183,"score_spread":0.18657109980662218,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1977350374","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99846226,0.00038971598,0.0005197659,0.00026045667,0.00015364724,0.000111825786,0.000031913973,0.000033473712,0.000036952115],"genre_scores_gemma":[0.9993459,0.000035204812,0.00024682542,0.00003913079,0.0002167967,0.000010652962,0.000015988793,0.00008663361,0.00000287696],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99793833,0.0000265852,0.0008087442,0.000232608,0.00039085545,0.0006028897],"domain_scores_gemma":[0.9980907,0.0003852211,0.00034669088,0.00033946594,0.00018201243,0.00065593567],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004876553,0.00033859783,0.0006559861,0.0003985946,0.00010664297,0.000018835412,0.00041898954,0.00026514297,0.00000955218],"category_scores_gemma":[0.0011754652,0.00029568528,0.00024075512,0.0003861132,0.0001959493,0.00027011643,0.000047789465,0.00095298607,0.0000055756327],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000023048919,0.000014338945,0.0004887371,0.00006404273,0.00013272995,0.00013759422,0.00025463538,0.0020677818,0.99544543,0.000044452365,0.00007004259,0.0012571769],"study_design_scores_gemma":[0.00037403166,0.000024149305,0.0008109093,0.00017573644,0.00013314231,0.0022594465,0.00002530182,0.0021360628,0.9936555,0.000012128819,0.000095075295,0.00029849284],"about_ca_topic_score_codex":0.0008289363,"about_ca_topic_score_gemma":0.000105292755,"teacher_disagreement_score":0.0021218522,"about_ca_system_score_codex":0.00052622246,"about_ca_system_score_gemma":0.00029605572,"threshold_uncertainty_score":0.9999495},"labels":[],"label_agreement":null},{"id":"W1977355021","doi":"10.1016/j.apcata.2010.03.006","title":"Effects of nanotubes pore size on the catalytic performances of iron catalysts supported on carbon nanotubes for Fischer–Tropsch synthesis","year":2010,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":115,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Carbon nanotube; Materials science; Fischer–Tropsch process; Incipient wetness impregnation; Chemical engineering; Iron oxide; Selectivity; Oxide; Nanotechnology; Chemistry; Metallurgy; Organic chemistry","score_opus":0.006224100918266994,"score_gpt":0.2126362847927963,"score_spread":0.2064121838745293,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1977355021","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.996679,0.00009408989,0.000018138438,0.00011520135,0.00023462599,0.00087411806,0.00007762494,0.00008887614,0.0018183354],"genre_scores_gemma":[0.99787366,0.00001885112,0.00036998405,0.000050019735,0.00028328312,0.00070207875,0.00026786857,0.000117494885,0.0003167723],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99699533,0.00002944522,0.0008878423,0.00067501835,0.0007467804,0.0006655762],"domain_scores_gemma":[0.99590695,0.002101697,0.00046507717,0.0012516031,0.00012251148,0.00015216532],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00064520125,0.000577281,0.0010497919,0.0002784877,0.00013707827,0.000018327424,0.0008119366,0.00031341176,0.000026259855],"category_scores_gemma":[0.00095750514,0.00040045968,0.0005626184,0.00064071995,0.00023937899,0.00008846354,0.00014414208,0.0004785761,0.000011631544],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023876669,0.00021698217,0.0000911359,0.00062649563,0.00041587724,0.0000034505476,0.0004270674,0.00037935656,0.99051833,0.0020088234,0.000054447373,0.005019245],"study_design_scores_gemma":[0.0007226804,0.00012648257,0.00025332888,0.00010034026,0.00071536296,0.0000070991214,0.000107234875,0.0028666423,0.99437183,0.000053406304,0.00023505381,0.00044056206],"about_ca_topic_score_codex":0.00049780577,"about_ca_topic_score_gemma":0.00009250248,"teacher_disagreement_score":0.004578683,"about_ca_system_score_codex":0.00010495181,"about_ca_system_score_gemma":0.00008817582,"threshold_uncertainty_score":0.99984473},"labels":[],"label_agreement":null},{"id":"W1977666423","doi":"10.1002/apj.411","title":"Hydrogen production by methanol‐steam reforming using NiMoCu/γ‐alumina trimetallic catalysts","year":2009,"lang":"en","type":"article","venue":"Asia-Pacific Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Catalysis; Steam reforming; Methanol; Exothermic reaction; Hydrogen; Hydrogen production; Chemistry; Chemical engineering; Yield (engineering); Enthalpy; Inorganic chemistry; Materials science; Metallurgy; Organic chemistry; Thermodynamics","score_opus":0.00943987796673255,"score_gpt":0.23018238471573216,"score_spread":0.22074250674899962,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1977666423","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.992528,0.0030474241,0.0027662332,0.00021177533,0.0005398628,0.00020616685,0.000006873045,0.000202587,0.00049108104],"genre_scores_gemma":[0.9955069,0.000055768687,0.0032177013,0.000009893049,0.00086662016,0.000003886019,0.000027954206,0.00011420625,0.00019710725],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99625885,0.000025848221,0.0014813314,0.00047527315,0.0008768831,0.0008817848],"domain_scores_gemma":[0.9980643,0.00008552738,0.00061144424,0.0005429865,0.00021876446,0.00047701935],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0009306811,0.0005812292,0.0010160101,0.00054553756,0.00006282461,0.000029824274,0.00061506324,0.00033312556,0.000016898966],"category_scores_gemma":[0.00085706986,0.0005394818,0.0005695337,0.0009853274,0.00005296418,0.0009809551,0.00008148726,0.0011587354,0.0000125738225],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000053847416,0.00009549857,0.0000065978816,0.00008365719,0.00019995666,0.00004468475,0.00018910809,0.0030205944,0.9893088,0.000028054625,0.00008920822,0.00687999],"study_design_scores_gemma":[0.0006486571,0.000079325335,0.0000018194264,0.0003322078,0.0002367451,0.0020433993,0.00017417328,0.0069654924,0.98658717,0.00004298093,0.0023183455,0.0005696812],"about_ca_topic_score_codex":0.0000136103345,"about_ca_topic_score_gemma":7.5615425e-8,"teacher_disagreement_score":0.006310309,"about_ca_system_score_codex":0.0008959657,"about_ca_system_score_gemma":0.00009271121,"threshold_uncertainty_score":0.9997057},"labels":[],"label_agreement":null},{"id":"W1978053790","doi":"10.1016/j.apcata.2014.11.002","title":"Effect of interactions between Ni and Mo on catalytic properties of a bimetallic Ni-Mo/Al2O3 propane reforming catalyst","year":2014,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":73,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Bimetallic strip; Propane; Chemistry; Adsorption; Selectivity; Desorption; Steam reforming; Inorganic chemistry; Oxygen; Chemical engineering; Organic chemistry; Hydrogen production","score_opus":0.011360403992816393,"score_gpt":0.23348963152676228,"score_spread":0.22212922753394587,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1978053790","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99812573,0.00016846032,0.00020702137,0.000017738179,0.000051668376,0.00049348024,0.000028802317,0.00010647993,0.0008006293],"genre_scores_gemma":[0.9986093,0.000007958989,0.00016403274,0.000010264632,0.00022816677,0.00016929205,0.0002923779,0.00009173058,0.00042689336],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99732953,0.000059577942,0.0009539252,0.00063300313,0.00052442,0.0004995149],"domain_scores_gemma":[0.99837,0.00017373322,0.00046037437,0.0007303647,0.00008029974,0.00018523891],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00083849876,0.00049720646,0.0012712153,0.0005280662,0.00010411686,0.00002220344,0.00040683724,0.0001608189,0.000006305963],"category_scores_gemma":[0.00023078074,0.00037114648,0.00028753447,0.0006955971,0.0002004679,0.00019858063,0.0002803191,0.0003826879,0.000033308348],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012296878,0.00005968387,0.00036643303,0.00076603674,0.00051929045,8.629697e-7,0.00047290465,0.00028430656,0.96611714,0.00044775257,0.000003735645,0.030838884],"study_design_scores_gemma":[0.00084093615,0.00020628951,0.00011069651,0.00016979087,0.00082253385,0.000020375803,0.000066675406,0.0033156986,0.99387693,0.000020539757,0.0001630302,0.0003864891],"about_ca_topic_score_codex":0.0018844412,"about_ca_topic_score_gemma":0.00005115548,"teacher_disagreement_score":0.030452395,"about_ca_system_score_codex":0.00018823786,"about_ca_system_score_gemma":0.000026780428,"threshold_uncertainty_score":0.99987406},"labels":[],"label_agreement":null},{"id":"W1979463010","doi":"10.1016/j.fuproc.2009.07.007","title":"Fischer–Tropsch synthesis on mono- and bimetallic Co and Fe catalysts supported on carbon nanotubes","year":2009,"lang":"en","type":"article","venue":"Fuel Processing Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":131,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"","keywords":"Bimetallic strip; Catalysis; Fischer–Tropsch process; Cobalt; Olefin fiber; Selectivity; Carbon nanotube; Chemistry; Inorganic chemistry; Materials science; Chemical engineering; Organic chemistry; Nanotechnology","score_opus":0.01105126682324821,"score_gpt":0.24673916921992065,"score_spread":0.23568790239667242,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1979463010","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9936071,0.0016917533,0.00004115041,0.0011293179,0.00003533222,0.00015594663,0.000005800992,0.0008139574,0.0025196278],"genre_scores_gemma":[0.9988447,0.0000733628,0.00072442857,0.00007392656,0.000046836594,0.000032428947,0.000013035755,0.000049725,0.0001415799],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99840343,0.000013647474,0.0003195949,0.00057610107,0.00021203919,0.00047518988],"domain_scores_gemma":[0.9992263,0.00009118764,0.00012313099,0.00041487758,0.000042348503,0.000102155456],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00017342479,0.0003362884,0.00047585965,0.0006188896,0.00010213882,0.00003322378,0.0002414662,0.000452281,0.000004882418],"category_scores_gemma":[0.0005240801,0.0002957126,0.000044835342,0.00053832936,0.00016309196,0.00011570342,0.000071907976,0.00049204216,0.000009950619],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000676495,0.000100258985,0.0004073399,0.00026773533,0.000056196757,0.000053384665,0.00014777186,0.000008401488,0.8107408,0.0007200332,0.000011698103,0.1874187],"study_design_scores_gemma":[0.00041261056,0.00022939568,0.00034123225,0.00028825802,0.0000822959,0.00014751786,0.00009435348,0.0032797973,0.9925031,0.0013265011,0.0008859214,0.0004089992],"about_ca_topic_score_codex":0.000029952236,"about_ca_topic_score_gemma":0.0000045987713,"teacher_disagreement_score":0.18700969,"about_ca_system_score_codex":0.00009185467,"about_ca_system_score_gemma":0.000032332046,"threshold_uncertainty_score":0.9999495},"labels":[],"label_agreement":null},{"id":"W1980491227","doi":"10.1002/cjce.20110","title":"Notes on the issues of equilibrium in the Fischer–Tropsch synthesis","year":2008,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Fischer–Tropsch process; Product distribution; Chemistry; Thermodynamics; Equilibrium constant; Catalysis; Chemical equilibrium; Product (mathematics); Phase equilibrium; Hydrocarbon; Kinetic energy; Thermodynamic equilibrium; Distribution (mathematics); Phase (matter); Physical chemistry; Organic chemistry; Mathematics; Physics","score_opus":0.020943969255651774,"score_gpt":0.21582721175441816,"score_spread":0.19488324249876637,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1980491227","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99448013,0.00062929967,0.000039052105,0.004298739,0.00008659001,0.00008402501,0.000005744176,0.000010188644,0.00036621874],"genre_scores_gemma":[0.99950063,0.00000705397,0.000113113936,0.000078112185,0.00023924878,0.000006430898,7.303338e-7,0.00003244472,0.000022213933],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986359,0.00003448545,0.00047917466,0.00009363687,0.00037061085,0.0003861843],"domain_scores_gemma":[0.997796,0.0014807917,0.00013281283,0.00036254877,0.00006362226,0.00016422439],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007597478,0.00018787004,0.00032561974,0.00015131912,0.000050111394,0.000016302938,0.0009105766,0.00009701927,0.00004662979],"category_scores_gemma":[0.0028222178,0.00009275926,0.00020738403,0.00039349266,0.00012782471,0.000091009744,0.00002707856,0.00081385934,0.000005458903],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000026354473,0.000019873267,0.00022429932,0.00006449671,0.00011512686,0.00013106763,0.0022220472,0.024418795,0.9696992,0.0024875782,0.00017777765,0.00041338912],"study_design_scores_gemma":[0.0001453374,0.000019373023,0.00014299083,0.00022869659,0.0000341516,0.00039115446,0.00007275156,0.0053184866,0.99236405,0.000068624606,0.0010698171,0.0001445617],"about_ca_topic_score_codex":0.0021031087,"about_ca_topic_score_gemma":0.0001184236,"teacher_disagreement_score":0.02266486,"about_ca_system_score_codex":0.00018419974,"about_ca_system_score_gemma":0.00014571246,"threshold_uncertainty_score":0.37826127},"labels":[],"label_agreement":null},{"id":"W1981369948","doi":"10.1038/418928a","title":"Harnessing hydrogen","year":2002,"lang":"en","type":"letter","venue":"Nature","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":64,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Chemistry","score_opus":0.009785976531304143,"score_gpt":0.2328833863595793,"score_spread":0.22309740982827517,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1981369948","genre_codex":"commentary","genre_gemma":"commentary","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"commentary","genre_consensus":"commentary","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.009839182,0.03329802,0.0001326227,0.8637864,0.005172995,0.000738581,0.00027333596,0.002589229,0.08416962],"genre_scores_gemma":[0.013922669,0.00007033995,0.00062471925,0.8395565,0.029492814,0.000044578715,0.0020995624,0.00063342834,0.11355535],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9982258,0.000014385336,0.00025134019,0.00044055775,0.0005443647,0.000523573],"domain_scores_gemma":[0.9991108,0.00007581943,0.000120678626,0.00058948604,0.000045723256,0.000057498994],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["research_integrity"],"category_scores_codex":[0.0000781562,0.0003920992,0.00043763276,0.00018455143,0.000051310264,0.000026191114,0.00048476402,0.010914327,0.000494148],"category_scores_gemma":[0.00015152508,0.0003462679,0.00030064714,0.00025203003,0.000025679277,0.000110470646,0.000111535475,0.023660611,0.00042929928],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000001590685,0.0000063417688,0.000006259303,0.00038991842,0.00011822922,0.00079871505,0.000053085947,0.000016465567,0.012092884,0.000014050554,0.98206955,0.004432921],"study_design_scores_gemma":[0.00012864351,0.0000029663943,8.6182973e-7,0.0001891593,0.000071670765,0.00013576057,0.0000016839618,0.0006211242,0.038403887,0.000043010965,0.95998394,0.00041726744],"about_ca_topic_score_codex":0.000012386543,"about_ca_topic_score_gemma":6.1664593e-7,"teacher_disagreement_score":0.033227682,"about_ca_system_score_codex":0.00024532242,"about_ca_system_score_gemma":0.000017302582,"threshold_uncertainty_score":0.9998989},"labels":[],"label_agreement":null},{"id":"W1981433091","doi":"10.1021/ie0496333","title":"Coke Formation over a Nickel Catalyst under Methane Dry Reforming Conditions:  Thermodynamic and Kinetic Models","year":2005,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":313,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Imperial Oil (Canada); Western University","funders":"","keywords":"Disproportionation; Coke; Catalysis; Chemistry; Carbon dioxide reforming; Methane; Thermodynamics; Carbon monoxide; Thermodynamic equilibrium; Decomposition; Nickel; Chemical engineering; Syngas; Organic chemistry","score_opus":0.06806138489142088,"score_gpt":0.3252968476475833,"score_spread":0.25723546275616244,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1981433091","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.996257,0.0005285,0.00069352024,0.00015086809,0.000087252745,0.00036841346,0.0000614939,0.00028435813,0.0015686144],"genre_scores_gemma":[0.99739563,0.000057312947,0.000091612776,0.000008371199,0.000810663,0.00012546494,0.00027124933,0.0001019385,0.001137738],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99703604,0.00003395982,0.0006240323,0.0004946931,0.0008609515,0.0009503447],"domain_scores_gemma":[0.9984623,0.0003616952,0.00009518085,0.0005829009,0.00015337719,0.00034451913],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010823618,0.000369517,0.00042133327,0.000289176,0.00013874001,0.00007145542,0.00041603402,0.0005338637,0.00013084416],"category_scores_gemma":[0.0005156489,0.00036943896,0.0001275002,0.00070191105,0.00011627252,0.0008179924,0.00030046204,0.0016550943,0.000030102989],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000032235443,0.000032815078,0.0000064998576,0.00017065303,0.00007592656,0.0000091248485,0.00018769817,0.040580444,0.95615983,0.00027646366,0.00002390341,0.002444424],"study_design_scores_gemma":[0.0011153473,0.0000138411615,0.000009087785,0.00021985266,0.000029655814,0.000068636225,0.00018390636,0.38112944,0.6161086,0.000095911375,0.0007059548,0.00031976777],"about_ca_topic_score_codex":0.00033059635,"about_ca_topic_score_gemma":0.000010486979,"teacher_disagreement_score":0.34054902,"about_ca_system_score_codex":0.0011763194,"about_ca_system_score_gemma":0.00012083517,"threshold_uncertainty_score":0.9998758},"labels":[],"label_agreement":null},{"id":"W1982721472","doi":"10.1002/cjce.21954","title":"Preparation and characterization of palladium–ruthenium composite membrane on alumina‐modified PSS substrate","year":2014,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"NORAM (Canada); University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Ruthenium; Palladium; Permeation; X-ray photoelectron spectroscopy; Membrane; Hydrogen; Materials science; Substrate (aquarium); Alloy; Chemical engineering; Composite number; Metal; Plating (geology); Nuclear chemistry; Chemistry; Inorganic chemistry; Catalysis; Metallurgy; Composite material; Organic chemistry","score_opus":0.008146793653119534,"score_gpt":0.20323992324270995,"score_spread":0.1950931295895904,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1982721472","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99836314,0.00003655811,0.0010395829,0.00015303261,0.00013973235,0.00007170115,0.000006974341,0.000015011847,0.00017425993],"genre_scores_gemma":[0.99958867,0.0000025999639,0.00010950988,0.000020571468,0.00020953586,0.0000018799553,0.0000144262085,0.000028776281,0.000024028],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990109,0.000015956464,0.0004347566,0.00010320835,0.0001950379,0.00024012629],"domain_scores_gemma":[0.9991334,0.00011347916,0.00019846256,0.00017407275,0.000089121575,0.00029142614],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00036546207,0.0001567653,0.00029117372,0.0001564118,0.000035566347,0.000023806591,0.00020645405,0.0000986953,0.000008642436],"category_scores_gemma":[0.00017135758,0.0001237508,0.000083727544,0.00015006067,0.00005050773,0.00012446094,0.000012323487,0.00031079914,0.0000015190786],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003330778,0.0000045458983,0.000023765382,0.000070074435,0.00003846946,0.0000028309244,0.00030712198,0.007998164,0.99027705,0.0008764758,9.891552e-7,0.00036719337],"study_design_scores_gemma":[0.00033515767,0.00003737075,0.00021683626,0.00015729286,0.00004233898,0.00008772586,0.0000033395588,0.05212959,0.9466843,0.00002662826,0.00015328123,0.00012612769],"about_ca_topic_score_codex":0.0002521006,"about_ca_topic_score_gemma":0.000034351146,"teacher_disagreement_score":0.044131428,"about_ca_system_score_codex":0.00012664877,"about_ca_system_score_gemma":0.000060056092,"threshold_uncertainty_score":0.5046411},"labels":[],"label_agreement":null},{"id":"W1982950496","doi":"10.1021/ef010066v","title":"Performance Evaluation of Sulfated-TiO<sub>2</sub> as a Modifier to Co−Ni−ZrO<sub>2</sub> Catalyst in a Dual-Bed Reactor for the Selective Production of C<sub>4</sub> Hydrocarbons from Syngas","year":2001,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina; University of Saskatchewan","funders":"","keywords":"Catalysis; Chemistry; Microreactor; Space velocity; Sulfation; Calcination; Isomerization; Heterogeneous catalysis; Hydrocarbon; Nuclear chemistry; Inorganic chemistry; Selectivity; Organic chemistry","score_opus":0.017566911236117675,"score_gpt":0.24955325064257586,"score_spread":0.2319863394064582,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1982950496","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99681544,0.00039185357,0.00055772,0.00012749706,0.00044581929,0.0011289145,0.00006330075,0.00014016859,0.00032929596],"genre_scores_gemma":[0.99765766,0.0002849218,0.000049043032,0.00003440303,0.00044638314,0.00090415485,0.0004476667,0.00014316213,0.00003258997],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99561363,0.00017120017,0.0011994498,0.00095258834,0.0012533736,0.0008097706],"domain_scores_gemma":[0.9971643,0.00045578825,0.0005969281,0.0010133156,0.0005670865,0.00020259597],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0016327832,0.0005808638,0.00086450763,0.00061136245,0.00014401856,0.000025269299,0.00036886038,0.00036626344,0.0000055450523],"category_scores_gemma":[0.0014484734,0.00052035943,0.00031791136,0.001704033,0.00013118562,0.0005714859,0.00013604986,0.00045888897,0.000019505258],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00047714103,0.00021214932,0.00013365946,0.00007361974,0.0003376185,0.0000048019056,0.0015277655,0.012293902,0.95825064,0.00008937169,0.000035398753,0.0265639],"study_design_scores_gemma":[0.0014714187,0.00018737472,0.0010669035,0.0002945501,0.00045382747,0.000043837124,0.00024445978,0.018457545,0.97688246,0.00028109355,0.00008083468,0.00053570885],"about_ca_topic_score_codex":0.0013646393,"about_ca_topic_score_gemma":0.0011552677,"teacher_disagreement_score":0.026028192,"about_ca_system_score_codex":0.0009196833,"about_ca_system_score_gemma":0.0003270903,"threshold_uncertainty_score":0.9997248},"labels":[],"label_agreement":null},{"id":"W1983477798","doi":"10.1002/cjce.22068","title":"Methanol production by bi‐reforming","year":2014,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Steam reforming; Fossil fuel; Carbon dioxide; Greenhouse gas; Natural gas; Methanol; Methane; Carbon dioxide reforming; Carbon-neutral fuel; Waste management; Environmental science; Biomass (ecology); Syngas; Chemistry; Ecology; Hydrogen production; Engineering; Catalysis; Organic chemistry; Biology","score_opus":0.0065402623761843595,"score_gpt":0.19059486617232765,"score_spread":0.1840546037961433,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1983477798","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9932778,0.00059438497,0.003799664,0.0009280131,0.00083667337,0.00009564173,0.0000042136185,0.00005987386,0.00040373328],"genre_scores_gemma":[0.998564,0.0000016496762,0.0004414719,0.00004159527,0.00073863985,0.0000034912803,0.0000043554082,0.00005395072,0.00015087074],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986068,0.000014211869,0.00047028263,0.0001372978,0.00029009726,0.00048128466],"domain_scores_gemma":[0.99885064,0.0001053003,0.00015609025,0.00026898776,0.000113507725,0.00050549273],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007934821,0.00019995777,0.00030192104,0.00019812371,0.000069732014,0.000028808003,0.00046589805,0.00012324289,0.000029862409],"category_scores_gemma":[0.001527406,0.00014464221,0.0001669252,0.00032921028,0.00005411288,0.00022333678,0.000023945935,0.0006890326,0.000012363995],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000044443673,0.0000035034225,0.000016188542,0.00003726892,0.000054195265,0.0000046156906,0.00019127058,0.005024281,0.99006313,0.0003058233,0.00020949375,0.004085762],"study_design_scores_gemma":[0.00018858745,0.000014691844,0.0000032730725,0.00010815866,0.000045293393,0.00036151186,0.000013219152,0.01057885,0.97537684,0.00007748206,0.013037192,0.00019487612],"about_ca_topic_score_codex":0.0010078589,"about_ca_topic_score_gemma":0.000070693044,"teacher_disagreement_score":0.014686288,"about_ca_system_score_codex":0.00047098327,"about_ca_system_score_gemma":0.00011969157,"threshold_uncertainty_score":0.5898338},"labels":[],"label_agreement":null},{"id":"W1983480124","doi":"10.1007/s10562-006-0193-9","title":"Low-temperature water-gas shift reaction over Mn-promoted Cu/Al2O3 catalysts","year":2006,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Water-gas shift reaction; Catalysis; Chemistry; Activation energy; Water gas; Atmospheric temperature range; Kinetic energy; Space velocity; Redox; Inorganic chemistry; Reaction rate; Analytical Chemistry (journal); Physical chemistry; Syngas; Thermodynamics; Organic chemistry; Selectivity","score_opus":0.004147711252363485,"score_gpt":0.1980930599130052,"score_spread":0.1939453486606417,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1983480124","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9968889,0.00009464786,0.00019874504,0.0012789009,0.00040274448,0.0002235999,0.000043747295,0.00050391065,0.00036480554],"genre_scores_gemma":[0.9925175,0.000004415711,0.00008424006,0.00032954043,0.0008318327,0.000051711242,0.0052421074,0.00013491976,0.00080377026],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99691266,0.000041509975,0.0006966654,0.00081526814,0.00063062354,0.00090328895],"domain_scores_gemma":[0.99843085,0.00005610314,0.0001624065,0.0010977397,0.00006035747,0.00019254124],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00032587358,0.0005476282,0.0006199689,0.00042898854,0.00018039571,0.00008772219,0.00047263593,0.0003222911,0.00008978171],"category_scores_gemma":[0.00006306369,0.00044995768,0.0005159184,0.0007024795,0.000091846814,0.0006806922,0.00016581049,0.0006551836,0.00049413746],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002424819,0.00007795539,0.00009978778,0.00011649017,0.00018268407,0.00010346048,0.00027443934,0.00031293422,0.99698776,0.00002838165,0.0012201903,0.0005716524],"study_design_scores_gemma":[0.0006346639,0.000009885579,0.0004736238,0.00007550301,0.0002652879,0.000056691548,0.00002509026,0.00032770153,0.99319744,0.000030054922,0.004270841,0.00063324394],"about_ca_topic_score_codex":0.0020280613,"about_ca_topic_score_gemma":0.00018265074,"teacher_disagreement_score":0.00519836,"about_ca_system_score_codex":0.00056568027,"about_ca_system_score_gemma":0.000019223737,"threshold_uncertainty_score":0.9997952},"labels":[],"label_agreement":null},{"id":"W1984415459","doi":"10.1002/cjce.5450850109","title":"Hydrogen Yield from Low Temperature Steam Reforming of Ethanol","year":2007,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Saskatchewan Research Council (Canada); University of Saskatchewan","funders":"","keywords":"Steam reforming; Ethanol; Catalysis; Yield (engineering); Hydrogen; Hydrogen production; Atmospheric temperature range; Chemistry; Nuclear chemistry; Ethanol fuel; Chemical engineering; Inorganic chemistry; Materials science; Organic chemistry; Metallurgy; Thermodynamics","score_opus":0.007707480839647615,"score_gpt":0.19712444368088505,"score_spread":0.18941696284123744,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1984415459","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979178,0.0011264168,0.00020151383,0.000119946686,0.00029296568,0.000070707596,0.000018155879,0.00002501898,0.00022748987],"genre_scores_gemma":[0.99894655,0.0000031123311,0.00030681404,0.000036834103,0.0006025372,9.935094e-7,0.0000066002744,0.00005678075,0.000039785267],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99818283,0.0000062232734,0.00075426925,0.00013401722,0.00036911995,0.0005535536],"domain_scores_gemma":[0.9983816,0.00030616767,0.00023579324,0.0003317499,0.00014019996,0.00060445967],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00070430944,0.00023423263,0.00043770703,0.00025434868,0.000044114808,0.000013654227,0.00062957505,0.00026470536,0.000057337245],"category_scores_gemma":[0.00085823954,0.00017490225,0.00026344994,0.00037579113,0.00006544415,0.00017432436,0.000039389535,0.0010529519,0.000004503487],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017387365,0.000005492036,0.00003938405,0.000045706292,0.00011419781,0.00007131788,0.0004598532,0.0036816013,0.99442226,0.00006430182,0.00001193147,0.001066564],"study_design_scores_gemma":[0.00026242668,0.000015414154,0.000019558223,0.0004380802,0.00005540514,0.00019643472,0.000058046564,0.0009996505,0.997329,0.000040877487,0.00038750513,0.00019758116],"about_ca_topic_score_codex":0.0036130573,"about_ca_topic_score_gemma":0.00042285537,"teacher_disagreement_score":0.003190202,"about_ca_system_score_codex":0.00048382688,"about_ca_system_score_gemma":0.00023460688,"threshold_uncertainty_score":0.71323067},"labels":[],"label_agreement":null},{"id":"W1985021226","doi":"10.1002/cjce.21760","title":"Dehydration of methanol to dimethyl ether over γ‐Al<sub>2</sub>O<sub>3</sub> catalyst: Intrinsic kinetics and effectiveness factor","year":2013,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"National Key Research and Development Program of China; Key Technologies Research and Development Program","keywords":"Dimethyl ether; Methanol; Catalysis; Diffusion; Activation energy; Isothermal process; Dehydration; Chemistry; Space velocity; Thermodynamics; Chemical kinetics; Adsorption; Kinetics; Physical chemistry; Materials science; Analytical Chemistry (journal); Chromatography; Organic chemistry; Physics","score_opus":0.00642282636986744,"score_gpt":0.1991661165966107,"score_spread":0.19274329022674327,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1985021226","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.995127,0.00040309163,0.0036977087,0.00016035013,0.00024695264,0.0003042042,0.000017134746,0.000028851067,0.000014661398],"genre_scores_gemma":[0.99927294,0.0000070815663,0.00034451584,0.00005474173,0.00020312931,0.000017966646,0.000006671933,0.000091468675,0.0000014832949],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981155,0.000040938354,0.0006697257,0.00022957764,0.00038957866,0.0005546928],"domain_scores_gemma":[0.9979253,0.0004745404,0.0002216348,0.00033461698,0.00024101709,0.00080290885],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00044591897,0.00035258272,0.0006046267,0.00041887007,0.000043952463,0.000050265466,0.00037747723,0.00021910919,0.000012995626],"category_scores_gemma":[0.0010439456,0.00028671065,0.00020288891,0.00051925343,0.00008353332,0.00029000346,0.00007806396,0.00071946543,0.0000115744615],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000015879812,0.000009897316,0.000073519885,0.00014159948,0.00015662608,0.0000115605235,0.00034786042,0.0057128044,0.9859505,0.000063755324,0.000014324205,0.0075016147],"study_design_scores_gemma":[0.00045682216,0.00005144757,0.0012101445,0.00028993477,0.00008942828,0.00011633336,0.000011880066,0.0034800118,0.9938085,0.00006932043,0.00009740869,0.00031873072],"about_ca_topic_score_codex":0.00076093595,"about_ca_topic_score_gemma":0.00017640014,"teacher_disagreement_score":0.00785798,"about_ca_system_score_codex":0.00053416274,"about_ca_system_score_gemma":0.00013743868,"threshold_uncertainty_score":0.9999585},"labels":[],"label_agreement":null},{"id":"W1985484938","doi":"10.1002/cjce.5450810208","title":"Selective Production of C<sub>4</sub> Hydrocarbons from Syngas Using Fe‐Co/ZrO<sub>2</sub> and SO<sub>4</sub><sup>2—</sup>/ZrO<sub>2</sub> Catalysts","year":2003,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":34,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Isobutane; Syngas; Space velocity; Fischer–Tropsch process; Hydrocarbon; Chemistry; Oxide; Nuclear chemistry; Inorganic chemistry; Organic chemistry; Selectivity","score_opus":0.008794361219135927,"score_gpt":0.198374772803085,"score_spread":0.18958041158394906,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1985484938","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99519885,0.0019411744,0.0011500614,0.00018575093,0.0006702372,0.0005509929,0.00008638926,0.00014724964,0.00006932203],"genre_scores_gemma":[0.99789846,0.00011527522,0.0003803751,0.000054522894,0.0010964703,0.000030258509,0.00006933764,0.0003523054,0.0000029749815],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9937602,0.00014561726,0.0019801932,0.0010030409,0.0011663592,0.0019445451],"domain_scores_gemma":[0.9953285,0.0005274116,0.0008888538,0.000990651,0.00044504125,0.0018195439],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0014259437,0.0011983572,0.0016858209,0.0010934355,0.00040465136,0.00017363255,0.0008908874,0.00075816613,0.0000044757007],"category_scores_gemma":[0.0026164893,0.0011583554,0.00070066785,0.0016551798,0.00047685666,0.00091372005,0.00014094148,0.0027455646,0.000015992176],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000071276394,0.000056559446,0.000083800944,0.0002377235,0.00068091496,0.00012925187,0.0012465785,0.039914746,0.9547378,0.00007909615,0.00007585599,0.0026864416],"study_design_scores_gemma":[0.0011411787,0.000078225334,0.00006023461,0.0009458009,0.00063901686,0.0016286857,0.00015015123,0.022553785,0.97130847,0.0002554188,0.00008672765,0.0011522816],"about_ca_topic_score_codex":0.0010247168,"about_ca_topic_score_gemma":0.00048199817,"teacher_disagreement_score":0.01736096,"about_ca_system_score_codex":0.0023628352,"about_ca_system_score_gemma":0.0013032815,"threshold_uncertainty_score":0.9995552},"labels":[],"label_agreement":null},{"id":"W1985706765","doi":"10.1080/01971520500439401","title":"Biomass for Fuel Cells: A Technical and Economic Assessment","year":2006,"lang":"en","type":"article","venue":"International Journal of Green Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":30,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Queen's University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Biomass (ecology); Hydrogen fuel; Environmental science; Waste management; Greenhouse gas; Fuel cells; Process engineering; Regenerative fuel cell; Engineering; Chemical engineering","score_opus":0.007310419437462839,"score_gpt":0.25932447147818166,"score_spread":0.2520140520407188,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1985706765","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7772519,0.0013901341,0.20790865,0.0031362968,0.0035743776,0.00013333098,0.00013152933,0.00009046073,0.006383344],"genre_scores_gemma":[0.9938934,0.00003306511,0.004442954,0.000033340086,0.00096743135,0.000004615092,0.000013205175,0.0000187597,0.0005932615],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992007,0.000005758494,0.00039692468,0.00009394824,0.00019056436,0.00011213223],"domain_scores_gemma":[0.9994683,0.00009491786,0.00021532124,0.00006295481,0.00010635677,0.000052121817],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00016668106,0.00008945255,0.0001591166,0.00017510685,0.000012581032,0.000019516854,0.00024184615,0.00005780863,0.00002010483],"category_scores_gemma":[0.000012562465,0.000077608136,0.00013307582,0.000024641164,0.000024822992,0.00015106781,0.00006065295,0.00008043313,9.99702e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001004959,0.00007963044,0.00047846843,0.000031944208,0.00024621014,0.000054493936,0.000012637961,0.0010714971,0.9571498,0.02563885,0.0005179357,0.014618055],"study_design_scores_gemma":[0.004080598,0.00023322612,0.0016371626,0.00014633502,0.000119480566,0.0016444115,0.000031458196,0.028793307,0.6974634,0.015203531,0.25015858,0.0004885488],"about_ca_topic_score_codex":0.0014215994,"about_ca_topic_score_gemma":0.00029672246,"teacher_disagreement_score":0.2596864,"about_ca_system_score_codex":0.00029358733,"about_ca_system_score_gemma":0.000041793523,"threshold_uncertainty_score":0.3164768},"labels":[],"label_agreement":null},{"id":"W1986914267","doi":"10.1016/j.cej.2008.04.012","title":"Synthesis of nanocarbons via ethanol dry reforming over a carbon steel catalyst","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":33,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Chemical engineering; Carbon fibers; Materials science; Carbide; Magnetite; Syngas; Activated carbon; Chemistry; Metallurgy; Organic chemistry; Composite material; Composite number","score_opus":0.008941065946458292,"score_gpt":0.20666066081447765,"score_spread":0.19771959486801935,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1986914267","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9932089,0.0006595744,0.004476491,0.00002533908,0.00038363636,0.00010433094,0.000009202131,0.0002252264,0.0009073443],"genre_scores_gemma":[0.9956275,0.000054762117,0.0035273903,0.000008449303,0.0005028913,0.000019974936,0.000007711162,0.00013217081,0.00011909952],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99729943,0.000013807117,0.000936078,0.00033422417,0.00066859747,0.00074787653],"domain_scores_gemma":[0.99843955,0.0002695069,0.00026826907,0.0004921198,0.00010858144,0.0004219429],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00033951574,0.00043658997,0.00075884257,0.00035901065,0.000072496885,0.000010806277,0.0005236136,0.00032562073,0.00004039804],"category_scores_gemma":[0.0009294287,0.00040117977,0.00044564425,0.0005280601,0.00009657098,0.00023928136,0.00017637141,0.0011143556,0.000007706234],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000026663422,0.000051667856,0.00024229934,0.00016854776,0.00017575276,0.0001244018,0.0002744739,0.002075918,0.9953118,0.000020656289,0.0000055815535,0.0015222245],"study_design_scores_gemma":[0.0004926427,0.000017020473,0.00009123886,0.0003557642,0.00009603907,0.0016239374,0.000022128444,0.045914613,0.9507579,0.000009265489,0.00017710925,0.0004423289],"about_ca_topic_score_codex":0.000086774045,"about_ca_topic_score_gemma":4.5680457e-7,"teacher_disagreement_score":0.0445539,"about_ca_system_score_codex":0.00050287606,"about_ca_system_score_gemma":0.00008609583,"threshold_uncertainty_score":0.999844},"labels":[],"label_agreement":null},{"id":"W1988348604","doi":"10.1016/j.jcat.2005.02.010","title":"A kinetic model of CH4 decomposition and filamentous carbon formation on supported Co catalysts","year":2005,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":56,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Nucleation; Catalysis; Carbon fibers; Decomposition; Particle (ecology); Particle size; Chemical engineering; Diffusion; Reaction rate; Metal; Inorganic chemistry; Physical chemistry; Thermodynamics; Organic chemistry; Materials science; Composite material; Composite number","score_opus":0.011610788554487033,"score_gpt":0.2623665653387221,"score_spread":0.25075577678423505,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1988348604","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970218,0.00018806462,0.0020194326,0.000101726415,0.000027826336,0.00006974226,0.000012320314,0.000014905584,0.00054419175],"genre_scores_gemma":[0.99885416,0.00005166658,0.0007713923,0.000017715229,0.000096904,0.000002388696,0.0001189598,0.000019965777,0.00006682011],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984949,0.000014452808,0.00076390203,0.00010986966,0.00043977625,0.00017709174],"domain_scores_gemma":[0.99888176,0.000053056436,0.0005912516,0.00019901697,0.00015481228,0.000120134384],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00030141053,0.00015229422,0.00041876486,0.00044631746,0.000026480664,0.000011105566,0.00011367621,0.000082729304,0.000007706224],"category_scores_gemma":[0.00008089401,0.0001307906,0.00018713337,0.0002131464,0.00002694809,0.00034718405,0.00002641616,0.00019572492,0.0000018289579],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009152643,0.00008850841,0.000036957765,0.000085223146,0.00015129456,0.000007930351,0.00066750014,0.03567262,0.9570305,0.000025233676,0.000024586436,0.0061181565],"study_design_scores_gemma":[0.00062678184,0.000076380995,0.000063861095,0.00008854413,0.00026842966,0.00019289156,0.00004922874,0.24426085,0.7541695,0.000031516705,0.00006419774,0.000107771746],"about_ca_topic_score_codex":0.000032572796,"about_ca_topic_score_gemma":0.000009401155,"teacher_disagreement_score":0.20858823,"about_ca_system_score_codex":0.00022887162,"about_ca_system_score_gemma":0.000027772478,"threshold_uncertainty_score":0.5333486},"labels":[],"label_agreement":null},{"id":"W1988377177","doi":"10.2202/1542-6580.1905","title":"Bioenergy II: Group 8 Metal Complexes as Homogeneous Ionic Hydrogenation and Hydrogenolysis Catalysts for the Deoxygenation of Biomass to Petrochemicals - Opportunities, Challenges, Strategies and the Story so Far","year":2009,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"","keywords":"Deoxygenation; Hydrogenolysis; Catalysis; Petrochemical; Biomass (ecology); Chemistry; Metal; Ruthenium; Organic chemistry; Inorganic chemistry; Chemical engineering; Agronomy","score_opus":0.020583843656623448,"score_gpt":0.24880128999659512,"score_spread":0.22821744633997168,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1988377177","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9823431,0.010517777,0.004130706,0.0025658396,0.00017567161,0.00017726445,0.000022800214,0.000030283934,0.000036580364],"genre_scores_gemma":[0.9978963,0.0011269774,0.0005709737,0.000042205902,0.000280914,0.000016490043,0.000035011937,0.000026045642,0.0000050920753],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99842536,0.000017197588,0.0006028636,0.00018497772,0.0005573931,0.00021219683],"domain_scores_gemma":[0.9983995,0.0006733755,0.00033487106,0.00016331335,0.00029043254,0.00013850635],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005633548,0.00022742378,0.00038683065,0.00025974007,0.000035685116,0.00005488297,0.00045590225,0.00010352615,0.000004358128],"category_scores_gemma":[0.0007210934,0.00015362237,0.00022580056,0.00011870015,0.000104017985,0.00027223106,0.00010864207,0.0002326921,2.2574159e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013067132,0.000036300687,4.9005405e-7,0.0000325031,0.0005238671,0.0000069009316,0.00049411936,0.0002599902,0.9706339,0.008339005,0.0000068591607,0.019535344],"study_design_scores_gemma":[0.001017718,0.00008177607,0.000017692068,0.000094932744,0.0001845714,0.00046803578,0.00035526784,0.007877924,0.9841189,0.00031384814,0.005281066,0.00018831491],"about_ca_topic_score_codex":0.0000465144,"about_ca_topic_score_gemma":0.000003677777,"teacher_disagreement_score":0.01934703,"about_ca_system_score_codex":0.000164266,"about_ca_system_score_gemma":0.000059158494,"threshold_uncertainty_score":0.6264538},"labels":[],"label_agreement":null},{"id":"W1989546555","doi":"10.1021/jp802042s","title":"A First-Principle Study of Chain Propagation Steps in the Fischer−Tropsch Synthesis on Fe(100)","year":2008,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Chain propagation; Exothermic reaction; Isomerization; Methylene; Chemistry; Density functional theory; Potential energy surface; Propane; Fischer–Tropsch process; Reactivity (psychology); Reaction mechanism; Chain termination; Syngas; Ethylene; Polymerization; Photochemistry; Physical chemistry; Computational chemistry; Catalysis; Organic chemistry; Ab initio","score_opus":0.020831223298801365,"score_gpt":0.2571689912839243,"score_spread":0.23633776798512293,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1989546555","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9991313,0.000027122966,0.000030146419,0.0001759671,0.000013654871,0.00014651373,0.0000023198181,0.000008908289,0.0004640427],"genre_scores_gemma":[0.9995402,0.0000058302526,0.000012391182,0.000008944158,0.00032576598,0.000010637199,7.0694216e-7,0.000018817771,0.0000766906],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99854934,0.00007539528,0.00044685067,0.00010215616,0.00063900667,0.00018722535],"domain_scores_gemma":[0.99842656,0.000733634,0.00034675712,0.00036139713,0.00008125337,0.000050402035],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00063901156,0.00015982162,0.00034937073,0.000034031702,0.000070329246,0.000004800571,0.00056461664,0.000047442107,0.000012889232],"category_scores_gemma":[0.00059947214,0.00008468186,0.00015758043,0.00030365854,0.00006152151,0.00008265951,0.000061002174,0.00061376614,0.000003889358],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021322088,0.0012043811,0.00014142839,0.00011389938,0.00008770442,0.000034718967,0.0053163413,0.013041213,0.9795802,0.000019071027,0.000013884046,0.00023394059],"study_design_scores_gemma":[0.0006805444,0.00020313072,0.00084328995,0.00015642254,0.00009490846,0.00013421517,0.0016254816,0.009080759,0.98696077,0.000032436586,0.0000680387,0.00012002267],"about_ca_topic_score_codex":0.00003990853,"about_ca_topic_score_gemma":0.0000030338317,"teacher_disagreement_score":0.007380553,"about_ca_system_score_codex":0.00011866276,"about_ca_system_score_gemma":0.000031763655,"threshold_uncertainty_score":0.3453226},"labels":[],"label_agreement":null},{"id":"W1989565012","doi":"10.1021/ie020780f","title":"Application of the Generic Fluidized-Bed Reactor Model to the Fluidized-Bed Membrane Reactor Process for Steam Methane Reforming with Oxygen Input","year":2003,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Fluidized bed; Membrane reactor; Methane; Plug flow reactor model; Chemistry; Steam reforming; Continuous stirred-tank reactor; Hydrogen; Nuclear engineering; Hydrogen production; Chemical engineering; Materials science; Waste management; Engineering; Organic chemistry","score_opus":0.07583911654688803,"score_gpt":0.32295383852636733,"score_spread":0.2471147219794793,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1989565012","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957868,0.00016680558,0.001074459,0.00028840642,0.00013232413,0.002056859,0.00008253642,0.00017469407,0.00023712452],"genre_scores_gemma":[0.997291,0.000013902127,0.0003036259,0.000010566604,0.00064497016,0.0012062329,0.0000623797,0.00017874759,0.00028852056],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9959243,0.00006398105,0.0007998163,0.0007152358,0.0013907332,0.0011059131],"domain_scores_gemma":[0.9968598,0.000569618,0.00020518972,0.0014350066,0.0005881457,0.00034224824],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0025649203,0.00047563747,0.00063843327,0.0001638657,0.00015086286,0.000040368155,0.0013418964,0.00050311274,0.000014811532],"category_scores_gemma":[0.0040175645,0.00030813727,0.00023108309,0.001947319,0.00010343597,0.00020133163,0.00022640578,0.0013933607,0.00000497773],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028514382,0.00005493585,0.000009710335,0.0004076456,0.00013535342,0.0000012702751,0.00031437847,0.015892042,0.98200196,0.00006530241,0.000041264797,0.0007909912],"study_design_scores_gemma":[0.0016638963,0.0000460695,4.822851e-7,0.00021770243,0.000067562876,0.00002996368,0.00022099387,0.0243956,0.9693219,0.000013901913,0.00364399,0.0003779431],"about_ca_topic_score_codex":0.00014721144,"about_ca_topic_score_gemma":0.0000050012654,"teacher_disagreement_score":0.012680069,"about_ca_system_score_codex":0.0007017545,"about_ca_system_score_gemma":0.0005519022,"threshold_uncertainty_score":0.99993706},"labels":[],"label_agreement":null},{"id":"W1989584302","doi":"10.2202/1542-6580.1000","title":"Modeling of Autothermal Steam Methane Reforming in a Fluidized Bed Membrane Reactor","year":2003,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Membrane Reactor Technologies (Canada); University of British Columbia","funders":"","keywords":"Methane reformer; Steam reforming; Membrane reactor; Hydrogen; Chemical engineering; Hydrogen production; Methane; Fluidized bed; Materials science; Endothermic process; Oxygen; Chemistry; Waste management; Organic chemistry; Adsorption","score_opus":0.012575169647425905,"score_gpt":0.25154820274229167,"score_spread":0.23897303309486576,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1989584302","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99637854,0.00036783007,0.0020890555,0.000031887164,0.00059158436,0.000081408114,0.000007745852,0.000044822995,0.00040711745],"genre_scores_gemma":[0.9962063,0.000053514632,0.00338047,0.000009225067,0.0002601278,0.0000047777276,0.000008925934,0.00007157203,0.000005119864],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971145,0.000022697544,0.0014015193,0.00020919515,0.0008691372,0.00038295743],"domain_scores_gemma":[0.99860954,0.00027960696,0.0003601548,0.00021338515,0.0003404516,0.00019686372],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007875668,0.00029010308,0.0006765874,0.0005713141,0.0000025909767,0.000012490913,0.00058343576,0.00019933502,0.00006969677],"category_scores_gemma":[0.002697885,0.0002648596,0.00035779583,0.00029464974,0.000021939137,0.00049834326,0.000072745774,0.0007201798,0.000002664771],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014653955,0.000086516484,0.000036158966,0.00006455428,0.00021585407,0.00006964707,0.00023821478,0.0042324155,0.99381,0.00034688012,7.9206166e-7,0.0007524032],"study_design_scores_gemma":[0.0016743286,0.000020917036,0.0000014435681,0.0005124509,0.000035465335,0.0003211121,0.00005809888,0.052477937,0.94437605,0.000036802612,0.00025083084,0.00023454375],"about_ca_topic_score_codex":0.00006865183,"about_ca_topic_score_gemma":8.3567113e-7,"teacher_disagreement_score":0.049433954,"about_ca_system_score_codex":0.00064271624,"about_ca_system_score_gemma":0.00012266944,"threshold_uncertainty_score":0.9999804},"labels":[],"label_agreement":null},{"id":"W1990716310","doi":"10.2202/1542-6580.1583","title":"Co-Cu Metal Alloys from LaCo <sub>1-x</sub> Cu <sub>x</sub> O <sub>3</sub> Perovskites as Catalysts for Higher Alcohol Synthesis from Syngas","year":2007,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Syngas; Catalysis; Copper; Bimetallic strip; Calcination; Methanol; Inorganic chemistry; Metal; Dissociation (chemistry); Materials science; Cobalt; Perovskite (structure); Alcohol; Chemistry; Chemical engineering; Physical chemistry; Metallurgy; Crystallography; Organic chemistry","score_opus":0.012795885037336426,"score_gpt":0.2567137893561291,"score_spread":0.24391790431879268,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1990716310","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9903735,0.0007217616,0.005478806,0.00023195395,0.0020178575,0.0002911638,0.0004494853,0.00026697703,0.0001685315],"genre_scores_gemma":[0.993286,0.00015767018,0.0015706957,0.0000929554,0.004005977,0.000051428382,0.0005058857,0.0003234112,0.000005979108],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.993804,0.00003244983,0.002127931,0.0008267123,0.0020624253,0.0011464981],"domain_scores_gemma":[0.9932417,0.003642317,0.0009303212,0.0005709505,0.0007386213,0.0008760608],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00090994773,0.0009873144,0.0013702662,0.0007344967,0.00004342057,0.00016323416,0.0014941941,0.0006818182,0.000042458272],"category_scores_gemma":[0.0038709373,0.0009709112,0.0013349977,0.00036357576,0.00010657005,0.0010989096,0.0002583031,0.0015197548,0.000103669],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00045080492,0.00021237355,0.00013631451,0.00007078974,0.0023557711,0.00033868072,0.0001973623,0.00033121617,0.9849998,0.00009995158,0.00019327545,0.0106137125],"study_design_scores_gemma":[0.0017444234,0.000050054663,0.00031308635,0.0007942744,0.00056368107,0.00028405068,0.000040987565,0.0018890747,0.99178094,0.00016549433,0.001403949,0.00097000523],"about_ca_topic_score_codex":0.0001223851,"about_ca_topic_score_gemma":0.000011149208,"teacher_disagreement_score":0.009643707,"about_ca_system_score_codex":0.001590567,"about_ca_system_score_gemma":0.00014779101,"threshold_uncertainty_score":0.99927413},"labels":[],"label_agreement":null},{"id":"W1990731425","doi":"10.1021/ie100462t","title":"Glycerol Steam Reforming over Bimetallic Co−Ni/Al<sub>2</sub>O<sub>3</sub>","year":2010,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":125,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Australian Research Council; Ryerson University","keywords":"Catalysis; Bimetallic strip; Chemistry; Steam reforming; Glycerol; Adsorption; Reactions on surfaces; Chemisorption; Activation energy; Inorganic chemistry; Water-gas shift reaction; Reaction rate; Physical chemistry; Organic chemistry; Hydrogen production","score_opus":0.0411725654434792,"score_gpt":0.30995702601446895,"score_spread":0.26878446057098976,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1990731425","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9959476,0.00014815682,0.000030588733,0.00013113681,0.0009705108,0.0006220168,0.000090707945,0.0008010021,0.0012582787],"genre_scores_gemma":[0.9952649,0.00006899378,0.000030784406,0.00001563066,0.0035381767,0.00021306337,0.00022434026,0.0003625952,0.0002815228],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9925892,0.00005760664,0.0011973928,0.0012771756,0.0023196326,0.0025590179],"domain_scores_gemma":[0.9959804,0.00067964394,0.00020998894,0.0016990586,0.00035702274,0.0010739279],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["research_integrity"],"category_scores_codex":[0.0027436167,0.0009084348,0.00097643025,0.0005464756,0.00032134596,0.00017641248,0.0014338603,0.0016089224,0.00016399463],"category_scores_gemma":[0.0036950007,0.0009436652,0.00046807327,0.0018583051,0.00026327235,0.0006121005,0.00073811354,0.0080982065,0.00028030665],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000126175,0.0001026328,0.00006928477,0.0002707737,0.00021836981,0.00011565507,0.00007118095,0.0009020319,0.98529273,0.00003133983,0.0004355194,0.012364276],"study_design_scores_gemma":[0.0021436173,0.000052781645,0.000028852572,0.00030263833,0.00005201855,0.00017888437,0.00006114721,0.005562406,0.9749163,0.000013118345,0.01571173,0.0009765122],"about_ca_topic_score_codex":0.00013137088,"about_ca_topic_score_gemma":0.000009952452,"teacher_disagreement_score":0.015276211,"about_ca_system_score_codex":0.0011019153,"about_ca_system_score_gemma":0.00042079057,"threshold_uncertainty_score":0.9996872},"labels":[],"label_agreement":null},{"id":"W1991720249","doi":"10.1021/ie801078p","title":"Kinetic Studies of Carbon Dioxide Reforming of Methane over Ni−Co/Al−Mg−O Bimetallic Catalyst","year":2008,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":87,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Partial pressure; Catalysis; Chemistry; Methane; Partial oxidation; Bimetallic strip; Syngas; Carbon dioxide; Carbon monoxide; Carbon dioxide reforming; Water-gas shift reaction; Hydrogen; Steam reforming; Reaction rate; Catalytic reforming; Methane reformer; Reaction rate constant; Inorganic chemistry; Hydrogen production; Kinetics; Oxygen; Organic chemistry","score_opus":0.1254149519263813,"score_gpt":0.3630331183411076,"score_spread":0.23761816641472627,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1991720249","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99631125,0.0018752192,0.000005194587,0.000031837324,0.00019075185,0.0002869624,0.000035302226,0.00014057172,0.0011229292],"genre_scores_gemma":[0.99778503,0.00022643938,0.0000538871,0.0000015033587,0.00052914297,0.00005710552,0.00005171188,0.00011771981,0.0011774693],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.995591,0.000049902508,0.0011754241,0.000573929,0.0015829086,0.0010268325],"domain_scores_gemma":[0.9973692,0.00070628413,0.000244562,0.000975104,0.00041492935,0.0002899197],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0016767288,0.0004513368,0.0011338621,0.0004538028,0.00006008829,0.0000060544967,0.0007603005,0.000469279,0.0000595197],"category_scores_gemma":[0.004245363,0.00043125043,0.0002938186,0.0016442975,0.00038503873,0.00016069059,0.00043002595,0.0016634462,0.000005619917],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000786076,0.00006396881,0.00034319272,0.00068303436,0.0004412768,0.000066068686,0.00033189083,0.0019819627,0.99548835,0.00001183233,0.000034067503,0.0004757739],"study_design_scores_gemma":[0.0013077208,0.000056757737,0.00004109765,0.00051864376,0.00005930494,0.00010370781,0.0002202934,0.001467468,0.9944072,0.00000505723,0.0014387965,0.00037396766],"about_ca_topic_score_codex":0.0012725735,"about_ca_topic_score_gemma":0.0000026599882,"teacher_disagreement_score":0.0025686345,"about_ca_system_score_codex":0.00062262453,"about_ca_system_score_gemma":0.0002258577,"threshold_uncertainty_score":0.9998139},"labels":[],"label_agreement":null},{"id":"W1996124645","doi":"10.1016/j.molcata.2007.11.014","title":"HMS mesoporous silica as cobalt support for the Fischer–Tropsch Synthesis: Pretreatment, cobalt loading and particle size effects","year":2007,"lang":"en","type":"article","venue":"Journal of Molecular Catalysis A Chemical","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":81,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Fondo Nacional de Ciencia Tecnología e Innovación","keywords":"Cobalt; Fischer–Tropsch process; Catalysis; Chemical engineering; Mesoporous material; Calcination; Materials science; Particle size; Catalyst support; Incipient wetness impregnation; Mesoporous silica; Inorganic chemistry; Chemistry; Selectivity; Organic chemistry","score_opus":0.006088978396966335,"score_gpt":0.24929375945358168,"score_spread":0.24320478105661533,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1996124645","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9896067,0.0025799375,0.0067885695,0.0003546113,0.00011982726,0.00033244278,0.000007593671,0.000041282074,0.00016906876],"genre_scores_gemma":[0.9974136,0.000056615645,0.0019897085,0.00014050594,0.00020040176,0.000037068756,0.000008511419,0.000068020505,0.0000855994],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974678,0.000036807247,0.00088650663,0.0003379807,0.00064127636,0.0006296088],"domain_scores_gemma":[0.9959938,0.002484809,0.00046472403,0.00045215743,0.0001898318,0.00041467816],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0013394611,0.00034439994,0.00071694306,0.00008314396,0.00009944135,0.000050401304,0.00041731106,0.00020682385,0.000028032538],"category_scores_gemma":[0.004474337,0.0002402773,0.00065379794,0.00036621606,0.00010763048,0.00017789075,0.00013610034,0.00042763402,0.000010102903],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002687042,0.00014153584,0.00026320055,0.00012799288,0.0010540534,0.00026351976,0.00020776222,0.000040750376,0.9912414,0.00012565868,0.000055311495,0.0062101246],"study_design_scores_gemma":[0.001228504,0.00013712773,0.000060281734,0.00010006183,0.0016009163,0.0007730704,0.0001568482,0.00093226694,0.9937577,0.00008479637,0.0009069702,0.00026143237],"about_ca_topic_score_codex":0.000031750144,"about_ca_topic_score_gemma":0.0000027521146,"teacher_disagreement_score":0.007806901,"about_ca_system_score_codex":0.0003122148,"about_ca_system_score_gemma":0.00007174319,"threshold_uncertainty_score":0.9798224},"labels":[],"label_agreement":null},{"id":"W1996888809","doi":"10.1021/jp0722206","title":"Density Functional Theory and Kinetic Studies of Methanation on Iron Surface","year":2007,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":56,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Methanation; Kinetic energy; Dissociation (chemistry); Adsorption; Methane; Chemistry; Thermodynamics; Density functional theory; Catalysis; Physical chemistry; Computational chemistry; Organic chemistry; Physics","score_opus":0.017584188733174428,"score_gpt":0.2771337699969828,"score_spread":0.2595495812638084,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1996888809","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99851996,0.00030918745,0.0007199173,0.000041030125,0.000031852196,0.00002157663,0.0000010264632,0.000006405106,0.00034906465],"genre_scores_gemma":[0.99951863,0.000016459839,0.00004009609,0.000008574989,0.00026754622,9.5400424e-8,8.152391e-7,0.000008697719,0.00013905222],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992697,0.000025673367,0.00023579964,0.000059259204,0.00030189342,0.00010763994],"domain_scores_gemma":[0.9983327,0.0011648021,0.0002136027,0.00010655865,0.00013272963,0.0000496454],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011791068,0.00009450638,0.00021990576,0.000015551637,0.000028064378,0.0000017049178,0.00009276659,0.000033929642,0.000007418491],"category_scores_gemma":[0.0004940726,0.00005773117,0.00008704712,0.00008991844,0.00010490119,0.000048896065,0.000042473628,0.00026980828,0.0000010305426],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000269473,0.000046271063,0.000013841551,0.0000923522,0.0000885172,0.0000021318272,0.00036946245,0.0020967352,0.9958355,0.000424516,0.000006015774,0.00075519655],"study_design_scores_gemma":[0.00026337706,0.00004410938,0.0003573135,0.00006145571,0.00010900922,0.000045004363,0.00042338364,0.0003237468,0.9970281,0.0012712694,0.000015155621,0.000058047037],"about_ca_topic_score_codex":0.0000024330068,"about_ca_topic_score_gemma":2.3265349e-7,"teacher_disagreement_score":0.0017729884,"about_ca_system_score_codex":0.00007529525,"about_ca_system_score_gemma":0.000009736445,"threshold_uncertainty_score":0.23542087},"labels":[],"label_agreement":null},{"id":"W1999637463","doi":"10.1205/026387603762878719","title":"Investigation of Methane–Steam Reforming in Fluidized Bed Membrane Reactors","year":2003,"lang":"en","type":"article","venue":"Process Safety and Environmental Protection","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":47,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Membrane Reactor Technologies (Canada)","funders":"","keywords":"Countercurrent exchange; Methane; Fluidized bed; Membrane; Membrane reactor; Flux (metallurgy); Work (physics); Steam reforming; Materials science; Chemical engineering; Nuclear engineering; Waste management; Process engineering; Mechanics; Thermodynamics; Chemistry; Engineering; Catalysis; Physics; Hydrogen production; Organic chemistry; Metallurgy","score_opus":0.01278626518583193,"score_gpt":0.20645248552679224,"score_spread":0.19366622034096032,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1999637463","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99820304,0.00022479249,0.00077140454,0.000018181196,0.000041613395,0.00037028786,0.0000045571446,0.000039695704,0.00032645054],"genre_scores_gemma":[0.999616,0.00015569515,0.00007590564,0.0000052393198,0.000014667553,0.00005003313,0.000030386287,0.00002310673,0.000028913453],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989418,0.00004172244,0.0003948364,0.00023843376,0.00019865415,0.00018456911],"domain_scores_gemma":[0.9996529,0.000022611368,0.00013808074,0.000117762575,0.0000047203084,0.00006390421],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045679,0.00015217437,0.00023196173,0.00012436701,0.000040904877,0.0000021936141,0.000052051564,0.00012793664,0.00003052594],"category_scores_gemma":[0.0001112164,0.00014377353,0.00004142022,0.00020952636,0.00006679517,0.00036277928,0.00002313885,0.00022540888,0.0000029519906],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000121779005,0.000017817818,0.00048766655,0.00025749003,0.000012823616,7.3798805e-7,0.00074745674,0.00031956105,0.99484235,0.000033476812,9.586485e-9,0.0031588268],"study_design_scores_gemma":[0.0008324808,0.000039211733,0.00012346718,0.00009476632,0.000017525643,0.000030085454,0.00072181836,0.0015251851,0.99611145,0.00027175713,0.00007269454,0.0001595428],"about_ca_topic_score_codex":0.00015451046,"about_ca_topic_score_gemma":0.000010325185,"teacher_disagreement_score":0.002999284,"about_ca_system_score_codex":0.00021456351,"about_ca_system_score_gemma":0.000010481095,"threshold_uncertainty_score":0.58629143},"labels":[],"label_agreement":null},{"id":"W2001729075","doi":"10.1016/j.jcat.2003.08.006","title":"Support and rhenium effects on the intrinsic site activity and methane selectivity of cobalt Fischer–Tropsch catalysts","year":2003,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":72,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"ExxonMobil Research and Engineering Company","keywords":"Chemistry; Fischer–Tropsch process; Catalysis; Cobalt; Selectivity; Reactivity (psychology); Inorganic chemistry; Rhenium; Methane; Organic chemistry","score_opus":0.007393263242055275,"score_gpt":0.22821889039413212,"score_spread":0.22082562715207685,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2001729075","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.998319,0.0005314895,0.00030200472,0.00018509287,0.000091427806,0.00012732888,0.000007876598,0.000013143405,0.00042266495],"genre_scores_gemma":[0.99946815,0.000098151286,0.00017545307,0.000031139265,0.00007934989,0.000004263467,0.0000043257573,0.000028683135,0.000110509776],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998313,0.00016782795,0.00048293345,0.00022943571,0.00051295746,0.00029384246],"domain_scores_gemma":[0.99767065,0.0010207185,0.0005785709,0.00035756666,0.00017609287,0.00019637308],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0015466774,0.00025674546,0.00077219604,0.0002873753,0.00006509452,0.000020277075,0.00014672491,0.00012899372,0.000013790824],"category_scores_gemma":[0.0016101549,0.00017118486,0.000252705,0.00060400227,0.00009354098,0.00031763565,0.00008013256,0.00060870574,0.0000036932038],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001632822,0.00010841885,0.0029165566,0.0002349735,0.00073614443,0.000050138027,0.00047574902,0.000033407476,0.9829695,0.00020832483,0.00004637531,0.012057098],"study_design_scores_gemma":[0.00074255635,0.00020285604,0.0035672882,0.00007075547,0.0005609989,0.00047668035,0.0000428909,0.00009425308,0.9935344,0.00005502802,0.00047517734,0.00017709975],"about_ca_topic_score_codex":0.00013892667,"about_ca_topic_score_gemma":0.00003782826,"teacher_disagreement_score":0.011879998,"about_ca_system_score_codex":0.00012922294,"about_ca_system_score_gemma":0.000080734186,"threshold_uncertainty_score":0.6980716},"labels":[],"label_agreement":null},{"id":"W2002061416","doi":"10.2202/1542-6580.1074","title":"Combating Deactivation in Methane Non-Oxidative Dehydrocyclization via Hydrogen Feed Pulsing","year":2003,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Coke; Benzene; Methane; Hydrogen; Hydrogen production; Materials science; Chemical engineering; Incipient wetness impregnation; Chemistry; Inorganic chemistry; Organic chemistry; Metallurgy; Selectivity","score_opus":0.007971934745115076,"score_gpt":0.24582661083539847,"score_spread":0.2378546760902834,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2002061416","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92846906,0.00006984098,0.07052038,0.000052684933,0.00043327452,0.00008192587,0.0000017833662,0.000035783058,0.00033524656],"genre_scores_gemma":[0.99514323,0.000010130858,0.004469182,0.00001851951,0.00027178822,0.0000051059174,0.000025029442,0.000052959633,0.0000040533255],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978577,0.000022822094,0.00092496484,0.00019254355,0.0006981795,0.0003037896],"domain_scores_gemma":[0.99860907,0.00037986372,0.0004560284,0.00012456157,0.00028288053,0.00014761886],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005659003,0.00023916854,0.00038828337,0.00048721058,0.000005375044,0.000025992036,0.00035170847,0.00015408406,0.000029736408],"category_scores_gemma":[0.0028165523,0.00023962371,0.00017607775,0.0003657123,0.000015867987,0.000683334,0.000049685845,0.0005972746,0.000004878913],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000038521794,0.000060477185,0.00047912676,0.000020349613,0.00013117469,0.000038371254,0.00024898033,0.0023934545,0.99459296,0.00029348925,8.0920523e-7,0.0017022814],"study_design_scores_gemma":[0.0009424494,0.000014222238,0.00005132133,0.0002880699,0.000023212357,0.00023766505,0.00003514329,0.038881794,0.95889574,0.00016269927,0.00024635738,0.00022132351],"about_ca_topic_score_codex":0.000028353028,"about_ca_topic_score_gemma":0.0000010238113,"teacher_disagreement_score":0.06667415,"about_ca_system_score_codex":0.0008799085,"about_ca_system_score_gemma":0.000050888113,"threshold_uncertainty_score":0.9771572},"labels":[],"label_agreement":null},{"id":"W2002194155","doi":"10.1021/ie0011425","title":"Permeability, Selectivity, and Testing of Hydrogen Diffusion Membranes Suitable for Use in Steam Reforming","year":2001,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Hydrogen; Permeation; Membrane; Chemical engineering; Permeability (electromagnetism); Steam reforming; Selectivity; Palladium; Argon; Catalysis; Methane; Materials science; Chemistry; Hydrogen production; Organic chemistry","score_opus":0.1267377501655495,"score_gpt":0.33106752677437085,"score_spread":0.20432977660882135,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2002194155","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99896264,0.00016237587,0.000021814569,0.000020658696,0.000044318283,0.00046030674,0.000019649911,0.00010534921,0.00020287558],"genre_scores_gemma":[0.9989124,0.000023298282,0.00011363225,6.196932e-7,0.00032769903,0.0000887636,0.000022236576,0.00006884063,0.00044250916],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974827,0.000031086845,0.00055277324,0.0004911463,0.0005513728,0.00089088327],"domain_scores_gemma":[0.9972774,0.0018367011,0.00007381582,0.00039329252,0.00022163014,0.00019717055],"candidate_categories":["metaresearch","metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0021988514,0.0002554109,0.00047760617,0.00024386846,0.00008822418,0.00003285097,0.00030562954,0.00043050872,0.000015150638],"category_scores_gemma":[0.008437192,0.0002607627,0.000085449465,0.0011772584,0.00007843775,0.00034264295,0.0003705359,0.0010882021,7.4999576e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009174584,0.000070146096,0.012851425,0.0006433941,0.000024822339,0.00001184224,0.00009435017,0.004395738,0.9780199,0.0000051011216,0.0000018610627,0.003789696],"study_design_scores_gemma":[0.001277364,0.00004325146,0.00013657338,0.00040708747,0.000011873005,0.000067372006,0.00010428366,0.06998982,0.9270808,0.00001757878,0.0006218936,0.00024206533],"about_ca_topic_score_codex":0.0012684021,"about_ca_topic_score_gemma":0.000023936538,"teacher_disagreement_score":0.065594085,"about_ca_system_score_codex":0.0004893299,"about_ca_system_score_gemma":0.00011240914,"threshold_uncertainty_score":0.99998444},"labels":[],"label_agreement":null},{"id":"W2004092312","doi":"10.1016/j.jcat.2004.02.001","title":"The effect of surface-active carbon on hydrocarbon selectivity in the cobalt-catalyzed Fischer–Tropsch synthesis","year":2004,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":56,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Chemistry; Catalysis; Fischer–Tropsch process; Carbon monoxide; Cobalt; Hydrocarbon; Syngas; Carbon fibers; Water-gas shift reaction; Hydrogen; Adsorption; Polymerization; Monomer; Selectivity; Inorganic chemistry; Organic chemistry; Polymer","score_opus":0.005585646790000909,"score_gpt":0.2317130967269108,"score_spread":0.2261274499369099,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2004092312","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978986,0.00043805118,0.000044392815,0.0002914562,0.00010330656,0.00018370597,0.00000546789,0.000013725249,0.0010213065],"genre_scores_gemma":[0.9997395,0.000058355585,0.000029356806,0.0000065799923,0.0001035637,0.000011595071,0.0000033895276,0.000033588236,0.000014056076],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99756116,0.00025184834,0.0007510767,0.00019973313,0.0008663937,0.0003698169],"domain_scores_gemma":[0.99618065,0.0024136654,0.0006842278,0.00053680793,0.00010016288,0.00008445516],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0024198932,0.00028256423,0.00077725976,0.00021224904,0.000085317435,0.00002302309,0.00058395945,0.00013402602,0.0000028200536],"category_scores_gemma":[0.0020698125,0.00014869927,0.00053654,0.0010571395,0.000096634176,0.00017311703,0.000057962632,0.00080521475,0.0000032061823],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0017567228,0.00025829495,0.0023539294,0.00014476186,0.0013715402,0.00013103471,0.0017395949,0.041778497,0.9405199,0.00009086607,0.000004861351,0.009849978],"study_design_scores_gemma":[0.0010155406,0.00025168838,0.0011554725,0.00016703087,0.0004655605,0.000116103176,0.00019238194,0.0009405721,0.9954196,0.00006190749,0.000051641073,0.00016249718],"about_ca_topic_score_codex":0.00086927554,"about_ca_topic_score_gemma":0.00016136143,"teacher_disagreement_score":0.05489969,"about_ca_system_score_codex":0.0005854897,"about_ca_system_score_gemma":0.00008555577,"threshold_uncertainty_score":0.606378},"labels":[],"label_agreement":null},{"id":"W2005748778","doi":"10.1002/cjce.21765","title":"Simulation of pellet model with multicomponent mass diffusion closure using least squares spectral element solution method","year":2013,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Norges Forskningsråd","keywords":"Diffusion; Pellet; Mass flux; Diffusion process; Chemistry; Flux (metallurgy); Least-squares function approximation; Closure (psychology); Process (computing); Mechanics; Thermodynamics; Mathematics; Materials science; Physics; Computer science; Statistics","score_opus":0.015513731151129403,"score_gpt":0.23111415642144922,"score_spread":0.2156004252703198,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2005748778","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.70455295,0.00008603361,0.29505655,0.00010074455,0.00005379996,0.0001192116,0.0000045508114,0.000012132045,0.0000140593165],"genre_scores_gemma":[0.96957916,6.4723974e-7,0.030200783,0.000007587436,0.00014903994,0.0000024677588,0.000004831848,0.00004323048,0.000012278048],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99854416,0.000016300508,0.00054385694,0.00012294862,0.00036386657,0.00040885253],"domain_scores_gemma":[0.9989042,0.00013473786,0.00022960245,0.00019571392,0.00018547899,0.0003502204],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00031353458,0.00020879024,0.00033990215,0.00020104462,0.00005249461,0.000023751001,0.00025776587,0.00010253055,0.000037314803],"category_scores_gemma":[0.00015560082,0.00014773874,0.00015363222,0.00018628777,0.000040611103,0.00020322086,0.000022790573,0.00045624434,0.0000014945389],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000097489765,0.0000048585425,0.000033736105,0.000034800203,0.000035641497,0.0000026180533,0.00014725603,0.51743555,0.48204654,0.00004096862,9.710943e-7,0.00020729477],"study_design_scores_gemma":[0.00033857048,0.00001629167,0.000017447186,0.00014144508,0.000056261415,0.000039076305,0.00002558523,0.66831267,0.33088443,0.00003835416,0.000010238598,0.00011959833],"about_ca_topic_score_codex":0.0027766917,"about_ca_topic_score_gemma":0.00008266506,"teacher_disagreement_score":0.2650262,"about_ca_system_score_codex":0.0006227017,"about_ca_system_score_gemma":0.00014960159,"threshold_uncertainty_score":0.6024611},"labels":[],"label_agreement":null},{"id":"W2006513564","doi":"10.1139/v01-032","title":"Kinetic modeling of homogeneous methanol synthesis catalyzed by base-promoted nickel complexes","year":2001,"lang":"en","type":"article","venue":"Canadian Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Electric Power Research Institute; U.S. Department of Energy","keywords":"Chemistry; Syngas; Catalysis; Methanol; Arrhenius equation; Nickel; Alkoxide; Activation energy; Base (topology); Induction period; Homogeneous catalysis; Solvent; Inorganic chemistry; Physical chemistry; Organic chemistry","score_opus":0.014453639577497764,"score_gpt":0.21068214932927337,"score_spread":0.1962285097517756,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2006513564","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9954373,0.0019995356,0.0011773731,0.00009961707,0.0000707092,0.000047744194,0.000094313364,0.000016332746,0.0010570764],"genre_scores_gemma":[0.99892396,0.000031881984,0.00051766855,0.000010392705,0.00012851297,0.0000027564063,0.000027753133,0.000053499294,0.00030358433],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99837285,0.000015553327,0.00071257714,0.00017481703,0.00027484645,0.00044935627],"domain_scores_gemma":[0.9983022,0.0001085221,0.00030118332,0.00034312202,0.00022138077,0.00072354183],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026631815,0.00022675532,0.000530728,0.00014433163,0.000050823295,0.000014931846,0.0005087339,0.00017031463,0.00046416043],"category_scores_gemma":[0.00056599337,0.00022561969,0.00025563635,0.0002852999,0.00007941804,0.000097558965,0.000021883978,0.0003523356,0.0000048433512],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000015553444,0.000015205904,0.00007385331,0.00015260105,0.00012728917,0.00016795071,0.00010142769,0.004247758,0.9938986,0.0000011666675,0.00008054944,0.0011180603],"study_design_scores_gemma":[0.0003341305,0.000008593024,0.0000024446056,0.000258399,0.00011020289,0.0011504438,0.00013615456,0.013692623,0.9835478,0.000029433017,0.00050106534,0.00022868089],"about_ca_topic_score_codex":0.004857564,"about_ca_topic_score_gemma":0.0005241082,"teacher_disagreement_score":0.0103507545,"about_ca_system_score_codex":0.00033347623,"about_ca_system_score_gemma":0.00043123262,"threshold_uncertainty_score":0.92005044},"labels":[],"label_agreement":null},{"id":"W2007686719","doi":"10.1002/cjce.20373","title":"Equilibrium calculations for direct synthesis of dimethyl ether from syngas","year":2010,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":35,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Dimethyl ether; Syngas; Methanol; Catalysis; Chemistry; Dehydration; Partial pressure; Equilibrium constant; Thermodynamics; Chemical equilibrium; Bar (unit); Physical chemistry; Chemical engineering; Organic chemistry","score_opus":0.009668445119418449,"score_gpt":0.21401695102381582,"score_spread":0.20434850590439738,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2007686719","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99674505,0.00022586598,0.0017362933,0.00028935226,0.0004907948,0.000106128755,0.00008251956,0.000023797771,0.0003001764],"genre_scores_gemma":[0.99501806,3.8752236e-7,0.0043933303,0.000011012544,0.00047113598,0.000009192143,0.0000052908317,0.00005801088,0.0000335919],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998819,0.000008540558,0.0005065012,0.00011419504,0.00019841456,0.0003533547],"domain_scores_gemma":[0.99792325,0.0010585092,0.00017447125,0.0002982558,0.00014624432,0.00039924862],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00044946672,0.00017341593,0.00039516666,0.00016171363,0.00003051347,0.000018302155,0.00046227424,0.00017056464,0.00007589731],"category_scores_gemma":[0.0029192935,0.00013279608,0.00030672498,0.00019955977,0.000075744094,0.00011642131,0.00002395591,0.00058210036,0.0000023626117],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000009557704,0.000004973845,0.00003741655,0.000032807042,0.0001305986,0.000003863157,0.00014550227,0.006606273,0.9917084,0.00064096146,0.00001889558,0.000660773],"study_design_scores_gemma":[0.0001886918,0.000007174421,0.000026821568,0.00010136209,0.00012813862,0.000034542532,0.000007869382,0.01862763,0.97920865,0.00019917784,0.0013159147,0.00015403032],"about_ca_topic_score_codex":0.0028913554,"about_ca_topic_score_gemma":0.00039633937,"teacher_disagreement_score":0.012499731,"about_ca_system_score_codex":0.0001325302,"about_ca_system_score_gemma":0.00020011631,"threshold_uncertainty_score":0.5415267},"labels":[],"label_agreement":null},{"id":"W2008483685","doi":"10.1016/j.apcata.2008.05.001","title":"Deactivation behavior of ruthenium promoted Co/γ-Al2O3 catalysts in Fischer–Tropsch synthesis","year":2008,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":96,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Cobalt; Fischer–Tropsch process; Catalysis; Ruthenium; Chemistry; Sintering; Inorganic chemistry; Chemisorption; Coke; Organic chemistry; Selectivity","score_opus":0.017478855393562507,"score_gpt":0.24201134710929095,"score_spread":0.22453249171572845,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2008483685","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99669796,0.000068115616,0.00036835464,0.000022353686,0.000044669097,0.000419896,0.000034035736,0.0001253389,0.0022192616],"genre_scores_gemma":[0.9969578,0.000014599597,0.0012979221,0.000012497231,0.00012670293,0.0005455677,0.00059845403,0.00008770084,0.00035875145],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9973558,0.000032903383,0.00089583773,0.0005819548,0.00059087254,0.0005426222],"domain_scores_gemma":[0.99855417,0.000117117015,0.00031820167,0.00078810565,0.000076857024,0.00014557525],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003632906,0.00037888862,0.0008024339,0.00051711994,0.0000840266,0.000008874115,0.0004136197,0.00025802196,0.00006845169],"category_scores_gemma":[0.00014740849,0.00036962124,0.00027455972,0.0011054114,0.00010946371,0.00020249732,0.000112651236,0.00035117092,0.00006154182],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005647837,0.00026671076,0.0026723254,0.000054739663,0.0001320723,0.000024557738,0.0006458953,0.00035634846,0.9916274,0.00020849842,0.000032904023,0.003922045],"study_design_scores_gemma":[0.0006242598,0.000012812743,0.0039664535,0.000021479023,0.00020113865,0.00004645242,0.00008484009,0.0013168693,0.99311817,0.000013245167,0.00019064438,0.00040366637],"about_ca_topic_score_codex":0.0015802063,"about_ca_topic_score_gemma":0.00009841387,"teacher_disagreement_score":0.003518379,"about_ca_system_score_codex":0.00032055128,"about_ca_system_score_gemma":0.00008163088,"threshold_uncertainty_score":0.99987555},"labels":[],"label_agreement":null},{"id":"W2010707892","doi":"10.4028/www.scientific.net/amr.443-444.671","title":"Optimization of Inlet Temperature of Methanol Synthesis Reactor of LURGI Type","year":2012,"lang":"en","type":"article","venue":"Advanced materials research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Methanol; Inlet; Heat exchanger; Steady state (chemistry); Chemistry; Process engineering; Nuclear engineering; Thermodynamics; Chemical engineering; Mechanical engineering; Organic chemistry; Engineering; Physics","score_opus":0.039172618158424086,"score_gpt":0.34491247407277104,"score_spread":0.30573985591434694,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2010707892","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9987207,0.00032986424,0.00014102155,0.000011239062,0.00016886051,0.00020578418,0.00006860157,0.000021596425,0.0003323438],"genre_scores_gemma":[0.99318045,0.00016911757,0.0063881143,8.1975736e-7,0.000072871975,0.000024474857,0.000031867705,0.000038877828,0.00009341724],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99846196,0.000114486866,0.00047015684,0.0001374486,0.00046706593,0.00034886043],"domain_scores_gemma":[0.99850994,0.0004591065,0.0001276577,0.00039646344,0.0004326616,0.00007413972],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011863993,0.00011185767,0.000438987,0.00024599535,0.000015834185,0.0000033833169,0.00022268452,0.00014204066,0.00036141952],"category_scores_gemma":[0.0026061614,0.000094424,0.000048689402,0.00053531706,0.00008777044,0.000277609,0.00014040414,0.00013314508,0.000006726448],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017284315,0.00005116125,0.00004843438,0.0006333904,0.000040767532,4.181535e-7,0.00018405676,0.0014951524,0.99647397,0.00029776763,0.000004626057,0.00059743423],"study_design_scores_gemma":[0.00016773031,0.00003919302,0.00004226668,0.00020534167,0.000015337884,0.00000336096,0.00009589426,0.000048132133,0.9991141,0.000017374923,0.00016948048,0.00008179899],"about_ca_topic_score_codex":0.000057031695,"about_ca_topic_score_gemma":8.9495035e-7,"teacher_disagreement_score":0.0062470925,"about_ca_system_score_codex":0.00006396811,"about_ca_system_score_gemma":0.000036083893,"threshold_uncertainty_score":0.39572904},"labels":[],"label_agreement":null},{"id":"W2010893236","doi":"10.1002/cjce.20050","title":"Kinetic simulation of a compact reactor system for hydrogen production by steam reforming of higher hydrocarbons","year":2008,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Calgary; University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Steam reforming; Hydrogen production; Membrane reactor; Naphtha; Fluidized bed; Hydrogen; Chemical engineering; Plug flow; Plug flow reactor model; Methane reformer; Bubble column reactor; Chemistry; Waste management; Materials science; Bubble; Thermodynamics; Continuous stirred-tank reactor; Catalysis; Organic chemistry; Engineering; Mechanics","score_opus":0.014212431684576123,"score_gpt":0.21518465250641758,"score_spread":0.20097222082184146,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2010893236","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9982923,0.0006455808,0.0005026699,0.000057122936,0.00022496865,0.0001707051,0.000019207664,0.00002185991,0.00006555276],"genre_scores_gemma":[0.99953896,0.0000015578607,0.000101336394,0.0000024599105,0.00025506824,0.0000029968317,0.0000095254845,0.00004747143,0.000040605497],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99858767,0.000009211957,0.0007184803,0.00011169179,0.0002688154,0.00030413468],"domain_scores_gemma":[0.9988372,0.0001507625,0.00038035505,0.00023248798,0.00013570268,0.0002635074],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029793786,0.00017340512,0.00044815044,0.00019291844,0.000035765064,0.00000302527,0.00027118463,0.00011443857,0.000003554567],"category_scores_gemma":[0.0003981384,0.00013560492,0.00021433133,0.00026641932,0.00006334471,0.00013635616,0.0000103493785,0.00028053438,4.1979897e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000024426245,0.000007524835,0.000028493665,0.00020539042,0.00009083931,0.0000033088177,0.00024319705,0.11534313,0.8838984,0.000034522924,0.000015476815,0.000105294],"study_design_scores_gemma":[0.00035551866,0.00003442557,0.00001072467,0.0003376769,0.00008309298,0.00018205197,0.000019780307,0.04947246,0.94883716,0.000007199246,0.0005281575,0.00013177925],"about_ca_topic_score_codex":0.0011690771,"about_ca_topic_score_gemma":0.00001650073,"teacher_disagreement_score":0.06587067,"about_ca_system_score_codex":0.00058735727,"about_ca_system_score_gemma":0.00014671437,"threshold_uncertainty_score":0.5529808},"labels":[],"label_agreement":null},{"id":"W2010914002","doi":"10.1002/cjce.22103","title":"Modelling and optimization of simultaneous styrene and hydrogen production in an industrial hydrogen‐permselective membrane reactor","year":2014,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Ethylbenzene; Hydrogen production; Dehydrogenation; Membrane reactor; Hydrogen; Styrene; Adiabatic process; Steam reforming; Materials science; Process engineering; Membrane; Chemistry; Chemical engineering; Catalysis; Thermodynamics; Nuclear engineering; Organic chemistry; Engineering; Physics; Copolymer; Composite material; Polymer","score_opus":0.013225602452308307,"score_gpt":0.19528236142880137,"score_spread":0.18205675897649307,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2010914002","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99753356,0.00019134524,0.0020595125,0.000051560688,0.00005455266,0.00008839936,0.0000025575396,0.000010736553,0.000007801289],"genre_scores_gemma":[0.99883646,0.0000069615317,0.0008643089,0.0000034037287,0.00024880804,0.0000015834447,0.000004290213,0.00003136786,0.000002829439],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99905944,0.00001967516,0.0003935202,0.00013626131,0.00015301495,0.00023809935],"domain_scores_gemma":[0.99923205,0.00013433916,0.0001334738,0.00012555286,0.00008586832,0.00028870147],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004405239,0.000144308,0.00029399374,0.00022409127,0.000024480081,0.000013218539,0.00013358357,0.00013660877,0.0000029788848],"category_scores_gemma":[0.00067974656,0.00012204768,0.000038472248,0.00023432057,0.000050967876,0.00020569947,0.000014856727,0.00043888733,8.696481e-8],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001649951,0.000003424212,0.000021073894,0.000019620282,0.000016996915,0.0000031337397,0.00033759014,0.6268152,0.3721181,0.000016647613,6.7777165e-8,0.0006316609],"study_design_scores_gemma":[0.00022208285,0.000019526886,3.4172012e-7,0.00006880071,0.00002187767,0.00010101309,0.000011352502,0.53774756,0.4617125,0.000015209467,0.000006835366,0.000072887495],"about_ca_topic_score_codex":0.001208708,"about_ca_topic_score_gemma":0.00013351552,"teacher_disagreement_score":0.089594424,"about_ca_system_score_codex":0.00020070275,"about_ca_system_score_gemma":0.00008494082,"threshold_uncertainty_score":0.49769598},"labels":[],"label_agreement":null},{"id":"W2012721000","doi":"10.1002/cjce.20223","title":"Steam methane reforming in a Ni/Al<sub>2</sub>O<sub>3</sub> catalyst: Kinetics and diffusional limitations in extrudates","year":2009,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":100,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Isothermal process; Steam reforming; Methane; Sorption; Diffusion; Kinetics; Reaction rate; Chemical engineering; Chemical kinetics; Materials science; Porosity; Chemistry; Thermodynamics; Physical chemistry; Hydrogen production; Organic chemistry; Adsorption; Composite material","score_opus":0.013521221792079572,"score_gpt":0.20456719631428988,"score_spread":0.1910459745222103,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2012721000","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99739087,0.0012728282,0.00012914154,0.0007997531,0.00015772566,0.000142142,0.000012507066,0.000027664348,0.00006734631],"genre_scores_gemma":[0.9992598,0.00007152027,0.00030279753,0.00009396777,0.00018429737,0.000007230229,0.000019523119,0.000056431985,0.0000043727837],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99765426,0.000024183726,0.0009238808,0.00024987687,0.0003853276,0.0007624759],"domain_scores_gemma":[0.99842787,0.00033887388,0.0001945434,0.00027853888,0.00009872479,0.0006614741],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00063324335,0.0003542364,0.00056321063,0.00076869974,0.00004973893,0.000041669995,0.00042554134,0.00021251515,0.0000027965748],"category_scores_gemma":[0.0012299805,0.00030361133,0.00015156076,0.0007815895,0.000079262274,0.00032894823,0.00005617497,0.0012208312,0.000003160291],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019527093,0.000023891911,0.000056769088,0.000040622,0.000031741638,0.0001411898,0.00053422496,0.00886611,0.97848815,0.00013342015,0.0000081967955,0.01165617],"study_design_scores_gemma":[0.0008492709,0.000043652137,0.0006707456,0.00046532115,0.000042379488,0.0006427641,0.000078251636,0.013046551,0.9834047,0.00023204322,0.00015976519,0.00036454631],"about_ca_topic_score_codex":0.00050610467,"about_ca_topic_score_gemma":0.0019686858,"teacher_disagreement_score":0.011291624,"about_ca_system_score_codex":0.00091957534,"about_ca_system_score_gemma":0.00022637911,"threshold_uncertainty_score":0.9999416},"labels":[],"label_agreement":null},{"id":"W2014173745","doi":"10.1016/j.cej.2007.06.024","title":"Staged-separation membrane reactor for steam methane reforming","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":48,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia; Membrane Reactor Technologies (Canada)","funders":"","keywords":"Membrane reactor; Steam reforming; Membrane; Hydrogen production; Methane; Hydrogen; Chemical engineering; Membrane technology; Chemistry; Materials science; Waste management; Engineering; Organic chemistry","score_opus":0.014249551018433698,"score_gpt":0.2752322898575695,"score_spread":0.2609827388391358,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2014173745","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6452371,0.00043976202,0.3522499,0.00006221855,0.0008929928,0.0002814807,0.000013620662,0.00039076305,0.00043220803],"genre_scores_gemma":[0.9631349,0.000027540736,0.033579428,0.000037930742,0.0024500776,0.000025850752,0.00007563667,0.00018196311,0.00048667958],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99744076,0.0000065238496,0.000860017,0.0003132056,0.00047282572,0.00090666534],"domain_scores_gemma":[0.99842715,0.00039936005,0.00020668114,0.00030402304,0.00016595978,0.0004968],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0015478326,0.00036186868,0.0004793362,0.00028805918,0.000067658795,0.00003610122,0.00036068718,0.00028588306,0.000048630543],"category_scores_gemma":[0.0014029513,0.00033016116,0.00034612307,0.0003402631,0.000026240721,0.00044554844,0.000068899564,0.0009424562,0.000015797348],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000098266326,0.000031526026,0.0000058833507,0.00017034925,0.00009106193,0.00002403544,0.00015485112,0.0015317791,0.99130964,0.00026446104,0.000030983138,0.0062871617],"study_design_scores_gemma":[0.0011160007,0.00003842617,0.0000061939113,0.00014476162,0.000056554156,0.0005670124,0.00006628241,0.011763471,0.9777908,0.000034148004,0.007998535,0.0004178538],"about_ca_topic_score_codex":0.000007697745,"about_ca_topic_score_gemma":6.712187e-7,"teacher_disagreement_score":0.31867048,"about_ca_system_score_codex":0.0006703612,"about_ca_system_score_gemma":0.000048580176,"threshold_uncertainty_score":0.99991506},"labels":[],"label_agreement":null},{"id":"W2014457977","doi":"10.1016/j.ijhydene.2014.12.070","title":"Catalytic oxidative steam reforming of bio-ethanol for hydrogen production over Rh promoted Ni/CeO2–ZrO2 catalyst","year":2015,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":131,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"University of Saskatchewan","keywords":"Catalysis; Steam reforming; Chemistry; Hydrogen production; Ethanol; Selectivity; Inorganic chemistry; Oxygen; Space velocity; Hydrogen; Nuclear chemistry; Yield (engineering); Materials science; Organic chemistry; Metallurgy","score_opus":0.01988872682235859,"score_gpt":0.270637739835336,"score_spread":0.2507490130129774,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2014457977","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957438,0.0007419869,0.0014943905,0.00022582448,0.0011136913,0.00017071095,0.00006207783,0.000043853302,0.00040363107],"genre_scores_gemma":[0.997377,0.000040100815,0.0004520811,0.000023055132,0.0010019473,0.000020805184,0.00017178559,0.00007213305,0.0008410927],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99709016,0.00003580758,0.0011661657,0.00030175204,0.0010712915,0.00033479364],"domain_scores_gemma":[0.99698883,0.00007279425,0.0011402515,0.0003136686,0.0012501554,0.00023428428],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00075545895,0.00028909472,0.00053049304,0.00061534805,0.00003589383,0.000014010059,0.0007607533,0.0001528493,0.000013558381],"category_scores_gemma":[0.0009381656,0.00024742528,0.00036670992,0.00032504505,0.00008200177,0.0007670989,0.00016577827,0.00023366128,0.000005933437],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00044321662,0.00022600238,0.000127277,0.00005887665,0.0013461388,0.00005137047,0.0008279759,0.006580205,0.9781652,0.00036101413,0.000088726825,0.011723961],"study_design_scores_gemma":[0.0014573188,0.00018136705,0.000005433275,0.00024161521,0.00015157076,0.0008156292,0.00023115035,0.0037718117,0.98726183,0.0005388639,0.005084389,0.00025904723],"about_ca_topic_score_codex":0.00046288068,"about_ca_topic_score_gemma":0.000056114517,"teacher_disagreement_score":0.011464913,"about_ca_system_score_codex":0.0008700335,"about_ca_system_score_gemma":0.00026169553,"threshold_uncertainty_score":0.9999978},"labels":[],"label_agreement":null},{"id":"W2015081552","doi":"10.1002/apj.2","title":"Development of a novel autothermal reforming process and its economics for clean hydrogen production","year":2006,"lang":"en","type":"article","venue":"Asia-Pacific Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"University of British Columbia; Auburn University","keywords":"Hydrogen production; Methane reformer; Steam reforming; Methane; Hydrogen; Catalysis; Natural gas; Heptane; Fluidized bed; Waste management; Environmental science; Chemistry; Process engineering; Engineering; Organic chemistry","score_opus":0.010012237009500196,"score_gpt":0.2166950498276653,"score_spread":0.2066828128181651,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2015081552","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99358547,0.00023287824,0.005694809,0.000044015927,0.0001356559,0.00015881473,0.000005133922,0.000041697487,0.00010151816],"genre_scores_gemma":[0.9844074,0.000004872838,0.015101325,0.0000010475937,0.00036088083,0.000011315709,0.000008421085,0.00006219372,0.00004252945],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99836177,0.0000018772815,0.00093494495,0.00019717886,0.00017700152,0.00032720497],"domain_scores_gemma":[0.999197,0.000046155496,0.0003807212,0.00011618638,0.00014664738,0.000113262606],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003989848,0.00022491574,0.00044005498,0.0001956341,0.000027502227,0.000008559058,0.00017844654,0.00012824767,0.0000020369996],"category_scores_gemma":[0.00018989916,0.00021105287,0.00013529329,0.0001560543,0.00001978041,0.00033170293,0.00003897008,0.0002499757,4.0288413e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000048689355,0.00005727237,0.000007660281,0.00039115155,0.000079969395,0.0000010658788,0.00036391887,0.016167728,0.9788034,0.00021009063,0.0000014139977,0.0038676406],"study_design_scores_gemma":[0.0006810939,0.000017733226,0.0000060146504,0.00022089342,0.000042013773,0.00028163553,0.00018958838,0.041468393,0.9562513,0.00002368276,0.000596708,0.000220941],"about_ca_topic_score_codex":0.0000012650341,"about_ca_topic_score_gemma":2.5359213e-7,"teacher_disagreement_score":0.025300667,"about_ca_system_score_codex":0.00022058435,"about_ca_system_score_gemma":0.00008758501,"threshold_uncertainty_score":0.86064863},"labels":[],"label_agreement":null},{"id":"W2022768769","doi":"10.1002/cjce.20662","title":"Steam reforming of ethanol on a Ni/Al<sub>2</sub>O<sub>3</sub> catalyst coupled with a hydrotalcite‐like sorbent in a multilayer pattern for co<sub>2</sub> uptake","year":2011,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":68,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Sorbent; Hydrotalcite; Catalysis; Steam reforming; Sorption; Hydrogen; Hydrogen production; Chemical engineering; Materials science; Water-gas shift reaction; Chemistry; Inorganic chemistry; Adsorption; Physical chemistry; Organic chemistry","score_opus":0.015160240976707857,"score_gpt":0.20928569543587672,"score_spread":0.19412545445916887,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2022768769","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99672395,0.00029156555,0.0016181134,0.000108723005,0.00032071362,0.0007230554,0.000091585964,0.00007590206,0.000046383044],"genre_scores_gemma":[0.9989596,0.000022354365,0.00019679799,0.00012292087,0.00026698608,0.000103122606,0.00004478086,0.00027989302,0.0000035231062],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9953991,0.000032225445,0.0016733205,0.0005515371,0.00082922133,0.0015145573],"domain_scores_gemma":[0.99677914,0.00030496827,0.0007067162,0.0007754969,0.0003073934,0.0011262686],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010780547,0.000824422,0.001280069,0.000939312,0.00011277165,0.000040956485,0.0009518163,0.00043431908,0.000007393047],"category_scores_gemma":[0.0005216193,0.00066461076,0.00055384415,0.000753659,0.00017212864,0.00041004928,0.00008972041,0.001713519,0.00001116755],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027278002,0.0000794153,0.000069734124,0.0003456479,0.00034476415,0.00020043096,0.0017065506,0.0089033,0.9810379,0.000019351695,0.000018213697,0.007001908],"study_design_scores_gemma":[0.002513629,0.0002150126,0.00008593463,0.0015164462,0.00018991245,0.0005307756,0.00012948322,0.040380243,0.95358795,0.000017407549,0.00008519303,0.00074800994],"about_ca_topic_score_codex":0.0013845786,"about_ca_topic_score_gemma":0.0022942761,"teacher_disagreement_score":0.03147694,"about_ca_system_score_codex":0.0016384216,"about_ca_system_score_gemma":0.00054925407,"threshold_uncertainty_score":0.9995805},"labels":[],"label_agreement":null},{"id":"W2023610270","doi":"10.1007/s11244-015-0375-z","title":"14C-Labeled Alcohol Tracer Study: Comparison of Reactivity of Alcohols over Cobalt and Ruthenium Fischer–Tropsch Catalysts","year":2015,"lang":"en","type":"article","venue":"Topics in Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Resources Canada","keywords":"Ruthenium; Fischer–Tropsch process; Catalysis; Cobalt; Reactivity (psychology); TRACER; Chemistry; Alcohol; Organic chemistry; Selectivity; Medicine; Physics","score_opus":0.06076429900228013,"score_gpt":0.34786485170566317,"score_spread":0.287100552703383,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2023610270","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9975445,0.00047474104,0.00007244879,0.00004390849,0.00009635261,0.00033063133,0.000028294982,0.000040266626,0.0013688192],"genre_scores_gemma":[0.9990384,0.000007704405,0.00036090656,0.0000045609354,0.00006829709,0.000026692634,0.00006828955,0.000034526594,0.00039063732],"study_design_codex":"observational","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977297,0.00007157191,0.00087624026,0.0004182682,0.0005776873,0.0003265209],"domain_scores_gemma":[0.9984003,0.00016430227,0.00036063328,0.0007773316,0.00013892658,0.00015855081],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007815334,0.00027153123,0.0010471904,0.0002978555,0.000028410792,0.000010367572,0.0003175497,0.00018928018,0.000016792132],"category_scores_gemma":[0.0004889036,0.00025593452,0.0001455821,0.00071620854,0.00013689318,0.00024488324,0.0002540189,0.00038450953,0.000004693079],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00026602534,0.002144819,0.52892315,0.00043112543,0.0008632104,0.000026606218,0.015270518,0.0006525407,0.43876785,0.0003568416,0.00010873443,0.012188588],"study_design_scores_gemma":[0.0037805652,0.00018448663,0.01555049,0.000088991364,0.0005660928,0.000009713663,0.0022554651,0.005408601,0.97073144,0.00013450079,0.00079110824,0.0004985533],"about_ca_topic_score_codex":0.003952456,"about_ca_topic_score_gemma":0.0008311696,"teacher_disagreement_score":0.5319636,"about_ca_system_score_codex":0.00023777616,"about_ca_system_score_gemma":0.0000649881,"threshold_uncertainty_score":0.9999893},"labels":[],"label_agreement":null},{"id":"W2029409669","doi":"10.2202/1542-6580.1103","title":"Conversion of Synthesis Gas into Light Hydrocarbons. Modelling of the Catalytic Reaction Network","year":2004,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Catalysis; Hydrocarbon; Gas phase; Kinetic energy; Chemistry; Chemical engineering; Process engineering; Organic chemistry; Physics; Engineering","score_opus":0.008579352287848306,"score_gpt":0.20736739000645857,"score_spread":0.19878803771861026,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2029409669","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98695296,0.00020120418,0.011682081,0.00019438748,0.00075430056,0.000050429855,0.000002665165,0.000020440759,0.00014151339],"genre_scores_gemma":[0.99784064,0.000040764608,0.0016633738,0.000005359342,0.0004106284,0.000001733466,0.0000029449589,0.000032467044,0.00000210275],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982149,0.0000065454906,0.00077317667,0.00011929396,0.0007041953,0.00018188274],"domain_scores_gemma":[0.9987156,0.0002480646,0.0005385955,0.00019270279,0.0002108141,0.00009424252],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026202822,0.00016737326,0.00035298817,0.0001531992,0.00000554108,0.000006592291,0.00056732853,0.00012377836,0.0000045331994],"category_scores_gemma":[0.00071716786,0.00012991796,0.00035182005,0.00021494951,0.000032972832,0.00023720016,0.00010714805,0.00040876877,0.0000012938916],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000058078436,0.00003866623,0.000041971412,0.00006542094,0.00020486362,0.0000072566727,0.00015625358,0.06654506,0.9322993,0.00025430886,0.0000029571868,0.00032584422],"study_design_scores_gemma":[0.00037023603,0.000011002528,0.0000074141763,0.0009281363,0.00008052775,0.00012100112,0.000016187852,0.023584524,0.97430986,0.00025479903,0.00020353781,0.000112796886],"about_ca_topic_score_codex":0.00008747619,"about_ca_topic_score_gemma":3.416652e-7,"teacher_disagreement_score":0.042960536,"about_ca_system_score_codex":0.0005279814,"about_ca_system_score_gemma":0.00006541951,"threshold_uncertainty_score":0.52979004},"labels":[],"label_agreement":null},{"id":"W2030100158","doi":"10.1002/aic.13979","title":"Hydrogen Production by Sorption‐Enhanced Steam Glycerol Reforming: Sorption Kinetics and Reactor Simulation","year":2012,"lang":"en","type":"article","venue":"AIChE Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":68,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Fonds de recherche du Québec – Nature et technologies; Natural Sciences and Engineering Research Council of Canada; Centre in Green Chemistry and Catalysis","keywords":"Steam reforming; Exothermic reaction; Hydrogen production; Endothermic process; Chemical engineering; Hydrogen; Sorption; Chemistry; Catalysis; Waste management; Process engineering; Adsorption; Materials science; Organic chemistry; Engineering","score_opus":0.01555004256688093,"score_gpt":0.2591641491574776,"score_spread":0.24361410659059668,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2030100158","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9932582,0.0007780009,0.004955864,0.00012329088,0.0004452298,0.00014261852,0.000003241741,0.00008959734,0.00020397267],"genre_scores_gemma":[0.99754506,0.00013960309,0.0001926976,0.000020684376,0.0013908226,0.0000063481375,0.000033070966,0.00004668072,0.0006250078],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99860203,0.000032564483,0.00042937702,0.00017511235,0.00035244477,0.00040844645],"domain_scores_gemma":[0.9991505,0.000042798452,0.0002738793,0.00019575018,0.0001013814,0.0002356684],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005140053,0.00019223952,0.00020346895,0.00012116257,0.0001001421,0.000022450009,0.000093167815,0.00016049037,0.000043066597],"category_scores_gemma":[0.00031893593,0.00016663352,0.000078557954,0.00017002957,0.000028263707,0.0009792277,0.000045258468,0.0004407868,0.000033055712],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000044954395,0.00006145845,0.00023035299,0.000027973647,0.000042196614,3.9287852e-7,0.0005013694,0.0017052171,0.98334247,0.0000070783053,0.00004417645,0.013992375],"study_design_scores_gemma":[0.0005124827,0.000057743,0.00017814612,0.000056169596,0.00008308455,0.00023314898,0.00014464786,0.0050328653,0.98861086,0.00006392729,0.0047920337,0.00023489162],"about_ca_topic_score_codex":0.000010728424,"about_ca_topic_score_gemma":0.0000015770981,"teacher_disagreement_score":0.013757483,"about_ca_system_score_codex":0.00036130034,"about_ca_system_score_gemma":0.000012840663,"threshold_uncertainty_score":0.6795117},"labels":[],"label_agreement":null},{"id":"W2031381388","doi":"10.1016/j.cattod.2012.07.009","title":"Inhibition of carbon formation during steam reforming of methane over ethyldisulfide-impregnated metallic nickel catalysts","year":2012,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Catalysis; Methane; Nickel; Steam reforming; Methane reformer; Carbon fibers; Metal; Materials science; Chemical engineering; Chemistry; Inorganic chemistry; Metallurgy; Hydrogen production; Organic chemistry; Composite material; Composite number","score_opus":0.012612438644884686,"score_gpt":0.24455779183627346,"score_spread":0.2319453531913888,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2031381388","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99648446,0.0015568096,0.00014182464,0.000010222704,0.00015826017,0.00027884493,0.0000372324,0.00012873574,0.0012035834],"genre_scores_gemma":[0.9985731,0.00006225818,0.00013525464,0.0000046868468,0.00011785888,0.000045163797,0.0006678349,0.00007799982,0.00031579073],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99682957,0.000068580965,0.001365338,0.0003387863,0.0007223069,0.0006754406],"domain_scores_gemma":[0.9977143,0.0001232074,0.00084396254,0.00088121736,0.00020247795,0.00023485051],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0009370684,0.00039425446,0.00093468867,0.0007057406,0.00004729891,0.0000056986746,0.00028648792,0.00028952732,0.00004464235],"category_scores_gemma":[0.0004312372,0.00035945507,0.00048351596,0.0012413245,0.000091142516,0.0013243873,0.0002521897,0.00034298984,0.000016617658],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000039009486,0.00012314948,0.00044304944,0.00069693744,0.0003108454,0.0000018865818,0.0020647987,0.00012217274,0.9946121,0.0000829611,0.0000013359769,0.001501742],"study_design_scores_gemma":[0.0009389881,0.000023890068,0.0004933928,0.00028622418,0.0005419354,0.000035565285,0.0006053365,0.0006917423,0.99594706,0.00001856804,0.000045054512,0.00037224698],"about_ca_topic_score_codex":0.00096758467,"about_ca_topic_score_gemma":0.00005010941,"teacher_disagreement_score":0.002088666,"about_ca_system_score_codex":0.00047612193,"about_ca_system_score_gemma":0.000035223507,"threshold_uncertainty_score":0.99988574},"labels":[],"label_agreement":null},{"id":"W2033394827","doi":"10.1115/icone14-89073","title":"Hydrogen: The Fuel That Drill Bits Cannot Reach","year":2006,"lang":"en","type":"article","venue":"Volume 3: Structural Integrity; Nuclear Engineering Advances; Next Generation Systems; Near Term Deployment and Promotion of Nuclear Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"Atomic Energy (Canada)","funders":"","keywords":"Natural gas; Waste management; Environmental science; Hydrogen; Coal; Hydrogen economy; Steam reforming; Hydrogen production; Fossil fuel; Chemistry; Engineering","score_opus":0.024182354839996072,"score_gpt":0.22327963748397,"score_spread":0.19909728264397394,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2033394827","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9947268,0.0023843253,0.00063888245,0.0002226118,0.00092338555,0.00032519744,0.00004114012,0.0004544849,0.00028318627],"genre_scores_gemma":[0.9972917,0.0001635005,0.00082211336,0.000026232457,0.0006944139,0.000024329207,0.00013680449,0.00016749998,0.00067343534],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99760956,0.00008221142,0.00073884195,0.0005363391,0.00055648544,0.00047656224],"domain_scores_gemma":[0.9988518,0.00003637743,0.00032540652,0.0004966673,0.00014327369,0.00014647275],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00026106206,0.00047125426,0.00051236566,0.00018347346,0.00026308064,0.00022728257,0.00033876914,0.00024597518,0.000085075895],"category_scores_gemma":[0.00004224254,0.00037406123,0.0001812274,0.0003239866,0.00010675459,0.00079522864,0.00013819092,0.0004395607,0.00001549652],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000042454398,0.000046831017,0.00019042974,0.00048732743,0.0001583883,0.000013043047,0.0004891175,0.059110247,0.90999603,0.016936524,0.00038191985,0.012147657],"study_design_scores_gemma":[0.00060218776,0.00013982762,0.00033347067,0.0002012938,0.000074514326,0.00024561942,0.00012400659,0.81834835,0.026947469,0.0000407984,0.15231231,0.00063012843],"about_ca_topic_score_codex":0.0015797379,"about_ca_topic_score_gemma":0.00007809674,"teacher_disagreement_score":0.8830486,"about_ca_system_score_codex":0.00023557137,"about_ca_system_score_gemma":0.000019399085,"threshold_uncertainty_score":0.99987113},"labels":[],"label_agreement":null},{"id":"W2033556611","doi":"10.4028/www.scientific.net/ddf.203-205.211","title":"Microstructure Control Factors of H Diffusion through Pd and Pd&lt;sub&gt;77&lt;/sub&gt;Ag&lt;sub&gt;23&lt;/sub&gt; Membranes","year":2002,"lang":"en","type":"article","venue":"Defect and diffusion forum/Diffusion and defect data, solid state data. Part A, Defect and diffusion forum","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Hydro One (Canada); McGill University","funders":"","keywords":"Microstructure; Diffusion; Membrane; Materials science; Chemistry; Metallurgy; Physics; Thermodynamics; Biochemistry","score_opus":0.01837937816574569,"score_gpt":0.24564348074475048,"score_spread":0.22726410257900478,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2033556611","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9579755,0.020386336,0.001019913,0.00029989617,0.0015041927,0.003098013,0.014334521,0.0007565173,0.0006251105],"genre_scores_gemma":[0.93603885,0.04437218,0.00015749226,0.00059636886,0.000433666,0.00012958974,0.01737088,0.00049499585,0.00040595056],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.9853894,0.00062833464,0.003335618,0.004610587,0.0023840752,0.0036519659],"domain_scores_gemma":[0.9893397,0.0018186986,0.00170754,0.0046428675,0.00039960418,0.002091585],"candidate_categories":["metaepi_narrow","sts","open_science","research_integrity"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0016744066,0.0032990891,0.0042648492,0.0013261405,0.0026339367,0.00078272255,0.002048402,0.0017354391,0.0003612163],"category_scores_gemma":[0.001299225,0.0026791156,0.0012381532,0.0014837732,0.0013201137,0.0028654877,0.008409489,0.0017914255,0.00013096115],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0016874203,0.0011867696,0.010180899,0.0016035818,0.0005683011,0.00015210139,0.0015839831,0.000021434105,0.9505169,0.00036396764,0.011116298,0.021018373],"study_design_scores_gemma":[0.05986001,0.0040360945,0.0169429,0.0047422815,0.006425873,0.0026919204,0.0032634048,0.10053268,0.3205978,0.0029865785,0.46427596,0.013644517],"about_ca_topic_score_codex":0.00034217685,"about_ca_topic_score_gemma":0.0016093883,"teacher_disagreement_score":0.62991905,"about_ca_system_score_codex":0.00020883029,"about_ca_system_score_gemma":0.00012247007,"threshold_uncertainty_score":0.9996103},"labels":[],"label_agreement":null},{"id":"W2034447224","doi":"10.1021/ie901726u","title":"Dimethyl Ether Synthesis with in situ H<sub>2</sub>O Removal in Fixed-Bed Membrane Reactor: Model and Simulations","year":2010,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":97,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Permeance; Dimethyl ether; Methanol; Selectivity; Chemistry; Membrane; Yield (engineering); Dehydration; Ether; Membrane reactor; Chemical engineering; Water-gas shift reaction; Organic chemistry; Catalysis; Materials science","score_opus":0.04420868323808333,"score_gpt":0.2943625639690211,"score_spread":0.2501538807309378,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2034447224","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9987337,0.00004721173,0.00001945616,0.00009311845,0.000055093205,0.0002688908,0.000021802516,0.00012176082,0.0006389587],"genre_scores_gemma":[0.99915904,0.00000946479,0.0002276949,0.0000014664133,0.0003142242,0.000070005895,0.000024449018,0.00010435953,0.00008928621],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99741375,0.000032606516,0.0004713659,0.0005539908,0.00067918433,0.0008491011],"domain_scores_gemma":[0.99783516,0.001182816,0.000051924304,0.0005631537,0.00009279743,0.00027413425],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0012958454,0.00032562122,0.00045429982,0.0003719681,0.00005192428,0.00005065971,0.00034581177,0.00069562823,0.000026518543],"category_scores_gemma":[0.0033861883,0.0003185109,0.000061231156,0.0010558711,0.000104341365,0.00023170379,0.00018744153,0.0033958408,0.000004840952],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000098017066,0.00005071901,0.00019747655,0.00011049495,0.000029227393,0.00007006763,0.0001541312,0.05158874,0.9459369,0.000026562328,0.0000029254682,0.0017347065],"study_design_scores_gemma":[0.00098024,0.0000080698555,0.0000228659,0.00022092702,0.0000109874545,0.00004263935,0.000037117865,0.1515964,0.8466474,0.000014254839,0.00011654938,0.00030254462],"about_ca_topic_score_codex":0.0001872059,"about_ca_topic_score_gemma":0.00013421656,"teacher_disagreement_score":0.10000766,"about_ca_system_score_codex":0.00032398387,"about_ca_system_score_gemma":0.00017254308,"threshold_uncertainty_score":0.9999267},"labels":[],"label_agreement":null},{"id":"W2040230400","doi":"10.5539/ijc.v3n3p118","title":"Studies on the Preparation of (S)-3-chloro-phenyl-1-propanol by Catalytic Asymmetric Hydrogenation of B-chloro-propiophenone","year":2011,"lang":"en","type":"article","venue":"International Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Propiophenone; Chemistry; Catalysis; Reaction conditions; Medicinal chemistry; Nuclear chemistry; Organic chemistry; Ketone","score_opus":0.029633160105494938,"score_gpt":0.28579305297136726,"score_spread":0.2561598928658723,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2040230400","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9946974,0.000729936,0.0003004065,0.00010167404,0.00032429615,0.000083278144,0.00002574775,0.000012840955,0.0037244074],"genre_scores_gemma":[0.99924093,0.00007230678,0.00015880744,0.000014396008,0.00019138951,0.000005876063,0.0000166196,0.000021047155,0.00027860375],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978847,0.00001556522,0.0009604309,0.00013905353,0.00086914684,0.00013112287],"domain_scores_gemma":[0.99746805,0.00021498704,0.0011950873,0.00022076587,0.0008461021,0.000055031338],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00047774077,0.00016565714,0.00032560577,0.00014021795,0.000021713007,0.000006855191,0.00060016935,0.00008907656,0.000055264893],"category_scores_gemma":[0.0012191184,0.000117334646,0.00020943313,0.00022573351,0.000102230464,0.00020428754,0.00008762983,0.00026285375,0.000004970526],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024618418,0.00018220283,0.00011470011,0.00011418324,0.0007485296,0.00000886828,0.0009985303,0.00023667293,0.99559534,0.0002654918,0.000086648506,0.0014026402],"study_design_scores_gemma":[0.0004962439,0.000069667134,0.00003308454,0.00022216355,0.00007864263,0.00008720251,0.00034808935,0.0005403702,0.9975361,0.00040446868,0.000079179845,0.000104746905],"about_ca_topic_score_codex":0.000020217158,"about_ca_topic_score_gemma":5.958545e-7,"teacher_disagreement_score":0.0045435405,"about_ca_system_score_codex":0.00025397577,"about_ca_system_score_gemma":0.00006381916,"threshold_uncertainty_score":0.4784768},"labels":[],"label_agreement":null},{"id":"W2040433225","doi":"10.1016/j.enconman.2013.07.023","title":"Combining coal gasification, natural gas reforming, and external carbonless heat for efficient production of gasoline and diesel with CO2 capture and sequestration","year":2013,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":51,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"","keywords":"Syngas; Syngas to gasoline plus; Coal; Diesel fuel; Natural gas; Waste management; Clean coal technology; Gasoline; Environmental science; Substitute natural gas; Coal gasification; Steam reforming; Hydrogen production; Chemistry; Hydrogen; Engineering","score_opus":0.0058510902668865205,"score_gpt":0.1999103423248085,"score_spread":0.194059252057922,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2040433225","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99575025,0.00067705236,0.0029212225,0.00016847427,0.00009252396,0.00025919895,0.0000012796205,0.00002629249,0.00010371518],"genre_scores_gemma":[0.9981276,0.00034171037,0.00059365644,0.000022644474,0.000026687578,0.00003478424,0.000030492116,0.000011293363,0.0008111444],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99937665,0.000007964296,0.00014941474,0.00022687872,0.00011558511,0.00012352614],"domain_scores_gemma":[0.9997152,0.000016160444,0.00006064139,0.00009464398,0.00005248485,0.000060841707],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00009938485,0.00011708208,0.00014158692,0.00007778331,0.00007197374,0.00001778409,0.00002918467,0.000035810015,0.0000019635115],"category_scores_gemma":[0.0000080854525,0.00009002459,0.000012297817,0.000044312226,0.000072509734,0.00011513535,0.00006341975,0.00005135854,7.428706e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00078927807,0.00020681378,0.0043143122,0.004865273,0.00046164024,0.000014879026,0.0041852756,0.0041381624,0.9064353,0.033088848,0.00023350444,0.04126671],"study_design_scores_gemma":[0.0062864837,0.00040963152,0.009473456,0.0010450542,0.0003902636,0.00019482402,0.0065153763,0.4519865,0.5186656,0.00015908481,0.004035951,0.00083779986],"about_ca_topic_score_codex":0.00043878003,"about_ca_topic_score_gemma":0.000024742369,"teacher_disagreement_score":0.44784832,"about_ca_system_score_codex":0.00003589315,"about_ca_system_score_gemma":0.0000041002863,"threshold_uncertainty_score":0.3671096},"labels":[],"label_agreement":null},{"id":"W2042498942","doi":"10.1002/cjce.22202","title":"A numerical study of fixed bed reactor modelling for steam methane reforming process","year":2015,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":29,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Norges Forskningsråd","keywords":"Mass transfer; Steam reforming; Parametric statistics; Particle (ecology); Mechanics; Process (computing); Pellet; Methane; Diffusion; Mixing (physics); Mass flux; Thermodynamics; Nuclear engineering; Chemistry; Process engineering; Materials science; Mathematics; Physics; Catalysis; Computer science; Engineering; Hydrogen production","score_opus":0.03430861503103407,"score_gpt":0.25456229026422217,"score_spread":0.2202536752331881,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2042498942","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9915887,0.00031677884,0.007376922,0.000075653385,0.00024651844,0.00031175202,0.000008287017,0.00002966938,0.00004571295],"genre_scores_gemma":[0.99846953,4.187944e-7,0.0010689598,0.000008711887,0.00034045428,0.000018949255,0.000004583367,0.000074434654,0.000013959885],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99794316,0.000016206013,0.0008659279,0.000171246,0.00046882848,0.00053465704],"domain_scores_gemma":[0.9978797,0.00023197503,0.00033111853,0.000299463,0.00044615747,0.0008115778],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0009813902,0.00025720353,0.00063195283,0.00026990572,0.000033558572,0.000017251234,0.00062477455,0.00013813237,0.000005025879],"category_scores_gemma":[0.0012856442,0.00019063802,0.00020732572,0.0004332414,0.00003579214,0.0002330787,0.000026181979,0.0006182326,9.698061e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018203058,0.00008755157,0.00006865281,0.00025493169,0.00035757886,0.000038141992,0.0071974606,0.6371891,0.3535627,0.000103581166,0.000015548027,0.0009427062],"study_design_scores_gemma":[0.0016852469,0.0001964563,0.0000010619634,0.00019937663,0.00016235403,0.00019026535,0.00073603983,0.25495356,0.7412838,0.00009695252,0.00021328435,0.00028161224],"about_ca_topic_score_codex":0.0025050659,"about_ca_topic_score_gemma":0.00006480331,"teacher_disagreement_score":0.38772106,"about_ca_system_score_codex":0.0005865455,"about_ca_system_score_gemma":0.00051200483,"threshold_uncertainty_score":0.7773993},"labels":[],"label_agreement":null},{"id":"W2046943582","doi":"10.1021/ef000052+","title":"Production of C<sub>4</sub> Hydrocarbons from Modified Fischer−Tropsch Synthesis over Co−Ni−ZrO<sub>2</sub>/Sulfated-ZrO<sub>2</sub> Hybrid Catalysts","year":2000,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; University of Regina","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Isobutane; Selectivity; Space velocity; Hydrocarbon; Microreactor; Chemistry; Sulfate; Inorganic chemistry; Nuclear chemistry; Organic chemistry","score_opus":0.008578339305244266,"score_gpt":0.20595435145339558,"score_spread":0.19737601214815131,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2046943582","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9939703,0.0010267782,0.0004883961,0.00014086411,0.0007734369,0.00041121847,0.00026809628,0.0007763289,0.002144607],"genre_scores_gemma":[0.9959157,0.0008421462,0.00012094867,0.000082848834,0.0011901858,0.00029452954,0.0009003022,0.00039820228,0.0002550984],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9929274,0.00022883104,0.0018057259,0.0019093091,0.0015145579,0.0016141805],"domain_scores_gemma":[0.99592274,0.00045721428,0.00067557755,0.002133175,0.00018037576,0.00063092564],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006580848,0.0012720638,0.0016730889,0.00066781376,0.00029324155,0.00008546514,0.0009840097,0.0006525626,0.000097118835],"category_scores_gemma":[0.00064996834,0.0013108135,0.0008427763,0.0012840261,0.00032226995,0.0009612279,0.0002618761,0.0009786034,0.000237174],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002693363,0.00032575463,0.000057391386,0.0001404736,0.0006837001,0.00009299649,0.00023710265,0.0032207307,0.9384754,0.0001042989,0.00042955668,0.055963296],"study_design_scores_gemma":[0.0010435618,0.000073850984,0.00029555752,0.00040838134,0.00056407583,0.00010973756,0.00004348751,0.0023302655,0.99246204,0.00039030248,0.0008960492,0.0013826936],"about_ca_topic_score_codex":0.0013859376,"about_ca_topic_score_gemma":0.00021679746,"teacher_disagreement_score":0.054580603,"about_ca_system_score_codex":0.0007162028,"about_ca_system_score_gemma":0.00021825903,"threshold_uncertainty_score":0.99893415},"labels":[],"label_agreement":null},{"id":"W2047184906","doi":"10.1016/j.jcat.2015.04.004","title":"Fischer–Tropsch synthesis: Effect of ammonia in syngas on the Fischer–Tropsch synthesis performance of a precipitated iron catalyst","year":2015,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"Western Economic Diversification Canada; Natural Sciences and Engineering Research Council of Canada; University of Saskatchewan; Canadian Light Source; National Research Council Canada; Canada Foundation for Innovation; Canadian Institutes of Health Research; National Research Council; U.S. Department of Energy","keywords":"Syngas; Fischer–Tropsch process; Chemistry; Catalysis; Ammonia; Olefin fiber; Inorganic chemistry; Ammonium hydroxide; Organic chemistry; Selectivity","score_opus":0.01407882605042526,"score_gpt":0.2337769051606256,"score_spread":0.21969807911020034,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2047184906","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99804443,0.0007540693,0.000037186648,0.00021232062,0.00013175172,0.00023298165,0.000024581757,0.00002357595,0.0005391176],"genre_scores_gemma":[0.99925804,0.00009997167,0.00026254114,0.000007507222,0.0001266117,0.00004810729,0.0000098963565,0.00007607578,0.0001112522],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.995828,0.00034475772,0.00174459,0.00031249376,0.0012574526,0.0005127188],"domain_scores_gemma":[0.9945833,0.0024356698,0.0014652461,0.00088817655,0.0003735264,0.00025405386],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0037638277,0.0004645537,0.0016093032,0.0007709874,0.00005168041,0.00002107047,0.00088614924,0.00024547256,0.00004308045],"category_scores_gemma":[0.0063898102,0.00029485027,0.0007102912,0.0013397641,0.00015619582,0.00047536744,0.00015847772,0.0008552704,0.000026264048],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0036704515,0.00067269034,0.020218477,0.001525521,0.0021232932,0.00012998814,0.0024745916,0.020012645,0.93063253,0.000033018987,0.00020537493,0.018301412],"study_design_scores_gemma":[0.00089580385,0.0005111227,0.0015256312,0.001184249,0.0010639392,0.000112987225,0.00034289123,0.00432025,0.98957247,0.000004606653,0.00016638453,0.00029969696],"about_ca_topic_score_codex":0.00037321486,"about_ca_topic_score_gemma":0.000043429136,"teacher_disagreement_score":0.0589399,"about_ca_system_score_codex":0.0004616972,"about_ca_system_score_gemma":0.00015210247,"threshold_uncertainty_score":0.99995035},"labels":[],"label_agreement":null},{"id":"W2048224246","doi":"10.1016/j.ijhydene.2015.03.079","title":"Dry reforming of multiple biogas types for syngas production simulated using Aspen Plus: The use of partial oxidation and hydrogen combustion to achieve thermo-neutrality","year":2015,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":48,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Biogas; Partial oxidation; Syngas to gasoline plus; Process engineering; Combustion; Methane; Hydrogen; Chemistry; Waste management; Chemical engineering; Pulp and paper industry; Environmental science; Hydrogen production; Steam reforming; Organic chemistry; Engineering","score_opus":0.06799389980697738,"score_gpt":0.29662888527293735,"score_spread":0.22863498546595995,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2048224246","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98965234,0.00010170566,0.009623241,0.00019368401,0.0002751308,0.0001206772,0.00001783708,0.000010300403,0.0000051085267],"genre_scores_gemma":[0.99831194,0.000014543566,0.0013146218,0.000016396818,0.00027131435,0.0000023759749,0.00002717818,0.000021367528,0.000020276455],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986364,0.000048057354,0.0006325208,0.00013004534,0.00042473472,0.00012824457],"domain_scores_gemma":[0.99841815,0.0001450702,0.0005776585,0.00013902916,0.0006370431,0.0000830333],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00055987824,0.0001208964,0.00024562294,0.00018980014,0.000030169342,0.000013017069,0.00022542894,0.00006238888,0.0000023139867],"category_scores_gemma":[0.0007474215,0.00008879349,0.00012286744,0.00013796342,0.000045369237,0.00044009121,0.00008323084,0.000092136754,2.8161608e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004953915,0.000028611066,0.00022257325,0.000008225255,0.00022477229,0.0000018664515,0.00032834045,0.44030747,0.5561425,0.000247566,0.000001736462,0.0019909067],"study_design_scores_gemma":[0.0006130724,0.00009711276,0.00002342774,0.000100049576,0.00008502935,0.00006660819,0.0000912398,0.13583827,0.8620866,0.00015628133,0.0007608411,0.000081488404],"about_ca_topic_score_codex":0.0008881083,"about_ca_topic_score_gemma":0.00007246873,"teacher_disagreement_score":0.30594406,"about_ca_system_score_codex":0.00024367608,"about_ca_system_score_gemma":0.00007010401,"threshold_uncertainty_score":0.36208934},"labels":[],"label_agreement":null},{"id":"W2049163448","doi":"10.1002/cjce.5450790515","title":"Rate equations for the fischer‐tropsch reaction on a promoted iron catalyst","year":2001,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Fischer–Tropsch process; Carbon monoxide; Catalysis; Space velocity; Hydrogen; Chemistry; Reaction rate; Water-gas shift reaction; Reaction rate constant; Thermodynamics; Atmospheric temperature range; Carbon fibers; Diffusion; Activation energy; Inorganic chemistry; Chemical engineering; Physical chemistry; Materials science; Organic chemistry; Kinetics; Physics; Composite material","score_opus":0.017747940566730812,"score_gpt":0.22514448491622394,"score_spread":0.20739654434949312,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2049163448","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9785754,0.0004564597,0.015001196,0.004531856,0.00064003497,0.0004462678,0.000020288153,0.0000632619,0.0002652535],"genre_scores_gemma":[0.9988866,0.0000038073056,0.00017078762,0.00005744155,0.0006156782,0.000022798333,0.000013334425,0.000050557333,0.00017903688],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99884385,0.000012252121,0.00040447357,0.00011887328,0.0002029865,0.00041756683],"domain_scores_gemma":[0.9984707,0.0006372712,0.00015082659,0.0002961986,0.00013081353,0.00031418377],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00066047563,0.00018450427,0.00022006285,0.00014916087,0.00014241376,0.000042333715,0.00042594734,0.00010895144,0.000019385863],"category_scores_gemma":[0.0017337557,0.00011537237,0.00020533401,0.00034038187,0.000043509728,0.00013993696,0.000014280132,0.0006490277,0.00000928035],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000041642244,0.000009383963,0.000005615559,0.000030923486,0.00010848322,0.00001721589,0.00028927464,0.035472777,0.9607826,0.00093146856,0.0000891237,0.002221497],"study_design_scores_gemma":[0.000986607,0.00007474034,0.000056903165,0.00023570217,0.00025371157,0.00046666389,0.000058378122,0.20871407,0.7705367,0.00013448727,0.01810781,0.00037422922],"about_ca_topic_score_codex":0.0012427269,"about_ca_topic_score_gemma":0.00030910238,"teacher_disagreement_score":0.1902459,"about_ca_system_score_codex":0.00056319864,"about_ca_system_score_gemma":0.00018266436,"threshold_uncertainty_score":0.47047487},"labels":[],"label_agreement":null},{"id":"W2051310579","doi":"10.1021/ie0504295","title":"Economics of the Clean Fuel Hydrogen in a Novel Autothermal Reforming Process","year":2005,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Auburn University","keywords":"Methane reformer; Steam reforming; Hydrogen production; Methane; Capital cost; Hydrogen; Waste management; Environmental science; Process engineering; Chemistry; Engineering","score_opus":0.06307801850017396,"score_gpt":0.31200962772336766,"score_spread":0.24893160922319368,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2051310579","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9977435,0.00007029832,0.0000060912125,0.00015145197,0.00007241012,0.00024505172,0.00001968433,0.00007490637,0.001616609],"genre_scores_gemma":[0.99832916,0.0000058868654,0.00002554834,0.0000028945517,0.0007806072,0.00004530271,0.000008201846,0.00007365333,0.00072875974],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99780655,0.000013343765,0.00061125605,0.00034883636,0.00045399627,0.0007659964],"domain_scores_gemma":[0.99893814,0.00016094804,0.000098207616,0.000569346,0.000084532425,0.00014884358],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00114904,0.0002345523,0.00033991938,0.00014592365,0.00004779763,0.000017669858,0.000864911,0.0003890336,0.000052607556],"category_scores_gemma":[0.0008946322,0.00020343368,0.00014292734,0.00080328446,0.000087990455,0.00020625268,0.00029312604,0.0016223105,0.0000072792536],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000030014737,0.00005478588,0.00020868688,0.0001818518,0.000030979485,0.000001951796,0.00035542526,0.10358353,0.8922798,0.000032407417,0.00000226973,0.0032383145],"study_design_scores_gemma":[0.0010160648,0.000007484634,0.000032331995,0.00023604053,0.0000067382975,0.000027403945,0.00015045857,0.06060978,0.93570876,0.000007853451,0.0019928769,0.00020420716],"about_ca_topic_score_codex":0.0001578883,"about_ca_topic_score_gemma":0.000011699994,"teacher_disagreement_score":0.04342898,"about_ca_system_score_codex":0.001004467,"about_ca_system_score_gemma":0.00038017717,"threshold_uncertainty_score":0.82957846},"labels":[],"label_agreement":null},{"id":"W2051614995","doi":"10.1016/j.apcata.2015.04.004","title":"Oxidative and non-oxidative steam reforming of crude bio-ethanol for hydrogen production over Rh promoted Ni/CeO2-ZrO2 catalyst","year":2015,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":83,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Steam reforming; Chemistry; Hydrogen production; XANES; Extended X-ray absorption fine structure; Inorganic chemistry; Nuclear chemistry; Organic chemistry; Absorption spectroscopy; Spectroscopy","score_opus":0.016657477427665938,"score_gpt":0.2516752904941501,"score_spread":0.23501781306648417,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2051614995","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99567914,0.0002607211,0.00176084,0.000056447,0.00014700662,0.0012858107,0.00010263881,0.00014176918,0.0005656303],"genre_scores_gemma":[0.99451417,0.000015772592,0.0020185686,0.000019020805,0.00042398315,0.00052075455,0.0014188219,0.0001200905,0.00094883976],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9969074,0.0000271195,0.0008654981,0.00095396355,0.00058955664,0.00065647194],"domain_scores_gemma":[0.99793994,0.00005612364,0.0005425616,0.0008622421,0.00028662023,0.00031249062],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007873193,0.00053113827,0.0009393215,0.00042837855,0.00012452282,0.000019932444,0.0003770138,0.00026995107,0.000009378615],"category_scores_gemma":[0.00027396923,0.00047360428,0.00024026445,0.00091873383,0.0001802743,0.00042953284,0.00031196556,0.00028477763,0.00001675483],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018859959,0.00012141705,0.000099417135,0.00017834023,0.0005974997,0.0000021264216,0.0029673602,0.00026688288,0.98904383,0.00013249293,0.000050680155,0.0063513336],"study_design_scores_gemma":[0.0015887871,0.00009831748,0.000037997757,0.000050213366,0.00047320753,0.000022527063,0.0009154359,0.0022456972,0.99336594,0.00019984289,0.00043693924,0.00056510844],"about_ca_topic_score_codex":0.0008333807,"about_ca_topic_score_gemma":0.00010167965,"teacher_disagreement_score":0.005786225,"about_ca_system_score_codex":0.0004749535,"about_ca_system_score_gemma":0.0001271537,"threshold_uncertainty_score":0.99977154},"labels":[],"label_agreement":null},{"id":"W2053118934","doi":"10.1016/j.memsci.2009.04.047","title":"Methane steam reforming with a novel catalytic nickel membrane for effective hydrogen production","year":2009,"lang":"en","type":"article","venue":"Journal of Membrane Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":70,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Nickel; Steam reforming; Catalysis; Methane; Catalytic reforming; Methane reformer; Hydrogen production; Hydrogen; Space velocity; Methanation; Carbon dioxide reforming; Membrane reactor; Materials science; Chemical engineering; Methanizer; Chemistry; Syngas; Inorganic chemistry; Waste management; Metallurgy; Carbon monoxide; Organic chemistry; Electrochemical reduction of carbon dioxide; Selectivity","score_opus":0.011760306609994513,"score_gpt":0.2619492685417887,"score_spread":0.2501889619317942,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2053118934","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99563515,0.00020181606,0.00228581,0.00047644248,0.00036578724,0.00058623904,0.0000060776993,0.00005181871,0.00039085717],"genre_scores_gemma":[0.9963458,0.000017344002,0.0027699845,0.000044818313,0.000417831,0.000012652686,0.0000027723017,0.000030737792,0.00035803686],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99715525,0.000015354339,0.00066435797,0.0004232569,0.0011188851,0.0006229117],"domain_scores_gemma":[0.9979276,0.00014790181,0.00062488916,0.00040861146,0.0005863455,0.00030465043],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0030940345,0.00027592215,0.000574736,0.0005970504,0.00017486369,0.000024329538,0.0007024132,0.00008176105,0.0000039693864],"category_scores_gemma":[0.0016273862,0.00018967535,0.00021042435,0.0014032817,0.00022596505,0.0015837529,0.000048959744,0.00043378604,0.0000036733818],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00031087754,0.00010332159,0.000004386389,0.00010786652,0.000051068226,0.000012147475,0.00042237935,0.0048984066,0.98027,0.00008388854,0.0000011708478,0.013734485],"study_design_scores_gemma":[0.0015864556,0.0006314558,0.000043521733,0.00034793644,0.00014942004,0.0022163712,0.0002272361,0.0026170923,0.9915895,0.000047833804,0.00027470468,0.00026849023],"about_ca_topic_score_codex":0.000022533948,"about_ca_topic_score_gemma":0.000006207484,"teacher_disagreement_score":0.013465995,"about_ca_system_score_codex":0.0005990818,"about_ca_system_score_gemma":0.0003338882,"threshold_uncertainty_score":0.7734736},"labels":[],"label_agreement":null},{"id":"W2054121618","doi":"10.1002/cjce.20068","title":"Simulation of autothermal reforming in a staged‐separation membrane reactor for pure hydrogen production","year":2008,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of British Columbia; Membrane Reactor Technologies (Canada)","funders":"","keywords":"Methane reformer; Hydrogen production; Steam reforming; Membrane reactor; Hydrogen; Methane; Membrane; Oxygen; Chemical engineering; Yield (engineering); Catalysis; Materials science; Chemistry; Process engineering; Waste management; Engineering; Organic chemistry; Composite material","score_opus":0.01707325567535499,"score_gpt":0.23700164347448102,"score_spread":0.21992838779912605,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2054121618","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99847037,0.00015279111,0.0009070919,0.00009928643,0.00014262751,0.0001819972,0.0000062046265,0.000015237765,0.000024392786],"genre_scores_gemma":[0.9993123,0.0000017089665,0.00029906895,0.000005363579,0.0002959979,0.0000070374213,0.000008076417,0.00003614565,0.000034292334],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99882805,0.000008797493,0.0005704543,0.00010527301,0.00020227574,0.00028512467],"domain_scores_gemma":[0.99918646,0.00013912021,0.00021195017,0.00016210043,0.00013216866,0.00016822017],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004526229,0.00013881322,0.00028552444,0.00025682183,0.00003694804,0.000004922215,0.00019699082,0.000114936825,0.000009194997],"category_scores_gemma":[0.0011446468,0.000112265734,0.00013386451,0.00028342573,0.00003856647,0.00026545778,0.00000895783,0.0003379352,6.357152e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000021349835,0.0000042035654,0.000029315517,0.00005886473,0.000020446125,0.0000054631987,0.0005115251,0.41659492,0.5825236,0.000031718453,0.0000014312612,0.00019714472],"study_design_scores_gemma":[0.00033230684,0.000017371425,0.000018920267,0.00012886572,0.00001945736,0.00011460591,0.000015062302,0.17084202,0.8282101,0.000020656666,0.00017328205,0.0001073398],"about_ca_topic_score_codex":0.00045295534,"about_ca_topic_score_gemma":0.0001230667,"teacher_disagreement_score":0.24575292,"about_ca_system_score_codex":0.00051352836,"about_ca_system_score_gemma":0.00025043954,"threshold_uncertainty_score":0.45780635},"labels":[],"label_agreement":null},{"id":"W2055027950","doi":"10.1002/cjce.20498","title":"Kinetics study on cnt‐supported RuKCo FTS catalyst in a fixed bed reactor","year":2011,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"Enerkem","keywords":"Microreactor; Catalysis; Space velocity; Fischer–Tropsch process; Thermodynamics; Kinetics; Activation energy; Syngas; Chemistry; Rate equation; Kinetic energy; Reaction rate; Chemical kinetics; Physical chemistry; Materials science; Physics; Organic chemistry; Classical mechanics","score_opus":0.02382060847351422,"score_gpt":0.2164536665277206,"score_spread":0.19263305805420639,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2055027950","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99886626,0.0000866753,0.00005270191,0.00007302569,0.0002708279,0.00018362753,0.0000082452225,0.000031304495,0.00042733055],"genre_scores_gemma":[0.9994855,5.99891e-7,0.00018449464,0.000027458456,0.00019177512,0.000007718465,0.000006138766,0.00006903048,0.000027313852],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981282,0.000018765822,0.00073774817,0.00018167098,0.00034539244,0.000588267],"domain_scores_gemma":[0.998572,0.00013492155,0.0001783727,0.0004078893,0.000093412134,0.00061344064],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00042898802,0.00028476462,0.00046076206,0.00044368193,0.000025871926,0.00002198293,0.00064770906,0.00014622984,0.00007400227],"category_scores_gemma":[0.00079656526,0.000221468,0.00016622576,0.0005021877,0.000046072422,0.000128241,0.000037721155,0.00097490667,0.000014411085],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000055808443,0.0001156139,0.0010079063,0.0000340265,0.00015941833,0.00056864443,0.0040079514,0.0011387933,0.9922936,0.000120489785,0.000027566386,0.0004701693],"study_design_scores_gemma":[0.0010391334,0.00013742626,0.0013024535,0.00018747133,0.00008780076,0.00023648363,0.00017441584,0.0016301185,0.99457943,0.000025372978,0.00026160653,0.00033831148],"about_ca_topic_score_codex":0.0039599454,"about_ca_topic_score_gemma":0.0009796468,"teacher_disagreement_score":0.0038335354,"about_ca_system_score_codex":0.0006721322,"about_ca_system_score_gemma":0.00015235855,"threshold_uncertainty_score":0.9031203},"labels":[],"label_agreement":null},{"id":"W2057038141","doi":"10.1515/1542-6580.2793","title":"The Role of Catalytic Site Deposition on Cobalt Catalysts Supported on Carbon Nanotubes for Fisher-Trospch Synthesis","year":2012,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; York University","funders":"","keywords":"Catalysis; Cobalt; Carbon nanotube; Incipient wetness impregnation; Chemical engineering; Materials science; Deposition (geology); Fischer–Tropsch process; Carbon nanotube supported catalyst; Selectivity; Catalyst support; Nanotechnology; Inorganic chemistry; Chemistry; Organic chemistry; Carbon nanofiber; Metallurgy","score_opus":0.006979243078669291,"score_gpt":0.23239416230495824,"score_spread":0.22541491922628895,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2057038141","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979879,0.0003039346,0.0002792042,0.00010632387,0.0007500137,0.000109073044,0.00004271377,0.00003305573,0.00038773628],"genre_scores_gemma":[0.9987739,0.000018603725,0.0002981407,0.000011153045,0.0007849257,0.000018245419,0.000036328773,0.00005186236,0.000006861746],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99809766,0.000008642738,0.00068394816,0.00013204386,0.00072647916,0.0003512245],"domain_scores_gemma":[0.99769086,0.0013036336,0.00035122118,0.00020131562,0.00027643185,0.00017654456],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00037836336,0.00022288473,0.0003333603,0.00017918578,0.000010726879,0.000022385671,0.0004464163,0.00012726196,0.0000039408646],"category_scores_gemma":[0.0020205167,0.00016808597,0.0003138077,0.000112043956,0.000026617327,0.00020706796,0.00004917186,0.00033497362,0.0000030841],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024108675,0.00009622482,0.00026866663,0.00003097087,0.00029750718,0.000004308255,0.00011006325,0.00021059012,0.9929598,0.0004344307,0.000013336056,0.005333026],"study_design_scores_gemma":[0.00035854155,0.0000467019,0.00008109579,0.00030695682,0.00008658245,0.00009816907,0.000022508959,0.006425195,0.99101186,0.000023294868,0.0013771561,0.00016196749],"about_ca_topic_score_codex":0.000031231077,"about_ca_topic_score_gemma":7.1888473e-7,"teacher_disagreement_score":0.0062146047,"about_ca_system_score_codex":0.0005094165,"about_ca_system_score_gemma":0.000031745265,"threshold_uncertainty_score":0.6854347},"labels":[],"label_agreement":null},{"id":"W2060251087","doi":"10.1016/j.ces.2005.02.062","title":"Bifurcation and its implications for a novel autothermal circulating fluidized bed membrane reformer for the efficient pure hydrogen production","year":2005,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Auburn University","keywords":"Hydrogen production; Steam reforming; Methane reformer; Bifurcation; Hydrogen; Steady state (chemistry); Materials science; Fluidized bed; Mechanics; Chemical engineering; Thermodynamics; Chemistry; Engineering; Nonlinear system; Physics; Organic chemistry","score_opus":0.01753346636032435,"score_gpt":0.25552462198763637,"score_spread":0.23799115562731202,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2060251087","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.94677806,0.0002544039,0.050429314,0.0012812187,0.0001252086,0.0008788146,0.000018539891,0.00021966864,0.0000147583005],"genre_scores_gemma":[0.991766,0.0000028544505,0.007316194,0.000021090382,0.00034737153,0.0004570367,0.00001623587,0.000039524763,0.000033712626],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985569,0.0000013924061,0.0003090067,0.00045843297,0.00020840453,0.00046583865],"domain_scores_gemma":[0.99913293,0.00019930326,0.00007771336,0.00030942654,0.00015706618,0.00012354614],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00059798843,0.00018400134,0.00017405143,0.00010835524,0.0002338127,0.000031594318,0.00033681944,0.000079542166,0.0000017188403],"category_scores_gemma":[0.0016442523,0.00014208702,0.000090065616,0.00056638365,0.00008649895,0.0002448154,0.00007424612,0.00013833061,0.0000017544528],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000077206805,0.000019590303,0.0000015300121,0.00009007725,0.000012555066,1.3818143e-8,0.00015720444,0.06309083,0.9328593,0.0013826721,0.0000011676151,0.0023773229],"study_design_scores_gemma":[0.00023574593,0.0000037927703,0.000013196263,0.000023919556,0.000021886257,0.00001836061,0.0000065541235,0.43410683,0.56527007,0.000005358589,0.00018082527,0.00011345994],"about_ca_topic_score_codex":0.0000025609384,"about_ca_topic_score_gemma":1.47284e-7,"teacher_disagreement_score":0.371016,"about_ca_system_score_codex":0.00028973108,"about_ca_system_score_gemma":0.000058120568,"threshold_uncertainty_score":0.57941407},"labels":[],"label_agreement":null},{"id":"W2060658794","doi":"10.1016/j.jpowsour.2007.06.018","title":"K (Na)-promoted Ni, Al layered double hydroxide catalysts for the steam reforming of methanol","year":2007,"lang":"en","type":"article","venue":"Journal of Power Sources","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":42,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Royal Military College of Canada","funders":"Ministère de la Défense Nationale","keywords":"Catalysis; Steam reforming; Methanol; Potassium hydroxide; Hydroxide; Chemistry; Inorganic chemistry; Hydrogen production; Sodium hydroxide; Hydrogen; Syngas; Organic chemistry","score_opus":0.01711199938232561,"score_gpt":0.28081263174613746,"score_spread":0.26370063236381186,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2060658794","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98706985,0.0017165788,0.0094471825,0.00023607416,0.0005650605,0.00024361668,0.000007726187,0.00003545834,0.00067842763],"genre_scores_gemma":[0.998079,0.000020617621,0.0010471944,0.000044006905,0.00025534595,0.000003837718,0.0000036020397,0.000057352565,0.0004890326],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997545,0.000016943435,0.0011421955,0.00017107485,0.00063375226,0.00049105124],"domain_scores_gemma":[0.9976687,0.0004859307,0.000992802,0.00038932078,0.0002957985,0.00016747609],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0025878984,0.00024175674,0.0005759011,0.00031714016,0.00009911637,0.00001584927,0.0006554161,0.00014590888,0.000021760246],"category_scores_gemma":[0.00040165012,0.00015101884,0.0005012249,0.0003764809,0.00007872117,0.00033421867,0.000112178306,0.0004618879,0.0000038513986],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00051743374,0.000079267265,0.00023340384,0.000093366114,0.00058309216,0.000026034268,0.0027835951,0.0004932105,0.98804164,0.00008199975,0.0001276044,0.006939349],"study_design_scores_gemma":[0.0017643964,0.00016741702,0.00011972184,0.00016361396,0.00017137872,0.00030006323,0.0019046504,0.00043303816,0.9822843,0.000044390574,0.01245292,0.00019411616],"about_ca_topic_score_codex":0.00015201785,"about_ca_topic_score_gemma":0.00003457868,"teacher_disagreement_score":0.012325316,"about_ca_system_score_codex":0.00018303099,"about_ca_system_score_gemma":0.000061046856,"threshold_uncertainty_score":0.615837},"labels":[],"label_agreement":null},{"id":"W2061274662","doi":"10.1016/j.fuel.2012.06.116","title":"CuZn/ZrO2 catalytic honeycombs for dimethyl ether steam reforming and autothermal reforming","year":2012,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":18,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Ministerio de Ciencia e Innovación; European Regional Development Fund; Institució Catalana de Recerca i Estudis Avançats; Ministerio de Economía y Competitividad; Mountain Equipment Co-operative","keywords":"Catalysis; Methane reformer; X-ray photoelectron spectroscopy; Steam reforming; Dimethyl ether; Methane; Chemical engineering; Materials science; Yield (engineering); Fourier transform infrared spectroscopy; Nuclear chemistry; Chemistry; Hydrogen production; Organic chemistry; Composite material","score_opus":0.018409833113650822,"score_gpt":0.2627959344339861,"score_spread":0.24438610132033525,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2061274662","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9828337,0.004236323,0.002246967,0.00010749062,0.000738711,0.0005774733,0.00004320471,0.00043801495,0.008778123],"genre_scores_gemma":[0.99183565,0.000025252102,0.0021209754,0.00008512457,0.00073712284,0.00009151239,0.000054250035,0.00015047002,0.0048996457],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980596,0.00001564361,0.00043369006,0.00032528647,0.00025533073,0.00091048196],"domain_scores_gemma":[0.9988612,0.00017198846,0.00014277727,0.00047498939,0.00004482016,0.0003042521],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006862505,0.00033048601,0.00042085577,0.00016120398,0.00012587322,0.000016861199,0.00023724216,0.00022437196,0.000040189247],"category_scores_gemma":[0.00025432586,0.00027320313,0.00017059942,0.00020024633,0.00006257961,0.00074671116,0.00019664003,0.00032313663,0.00007141015],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018003129,0.00021038718,0.00242381,0.0019423261,0.00039323847,0.000009226464,0.009749514,0.0000767451,0.8595417,0.0038145194,0.0001274479,0.121531054],"study_design_scores_gemma":[0.0032573752,0.00014672148,0.0011336209,0.00040518303,0.00032954305,0.00030427155,0.0019461281,0.007034058,0.8661769,0.0006423575,0.11690464,0.001719174],"about_ca_topic_score_codex":0.00021866993,"about_ca_topic_score_gemma":0.00001109376,"teacher_disagreement_score":0.11981188,"about_ca_system_score_codex":0.0002735725,"about_ca_system_score_gemma":0.000031215204,"threshold_uncertainty_score":0.999972},"labels":[],"label_agreement":null},{"id":"W2062232284","doi":"10.1080/00908310600625285","title":"Enhancing CO<sub>2</sub>Conversion to Methanol Using Dynamic Optimization, Applied on Shell Temperature and Inlet Hydrogen During Four Years Operation of Methanol Plant","year":2007,"lang":"en","type":"article","venue":"Energy Sources Part A Recovery Utilization and Environmental Effects","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University; University of Waterloo","funders":"","keywords":"Methanol; Mole fraction; Exothermic reaction; Inlet; Hydrogen; Hydrogen production; Fraction (chemistry); Materials science; Chemistry; Thermodynamics; Process engineering; Mechanical engineering; Engineering; Organic chemistry; Physical chemistry; Physics","score_opus":0.005986340080535898,"score_gpt":0.19730073492662242,"score_spread":0.19131439484608653,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2062232284","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9823721,0.00021141888,0.016966663,0.0000034449415,0.0000894728,0.0002542551,0.000023412678,0.000049533417,0.000029695937],"genre_scores_gemma":[0.99866134,0.0002691122,0.00052036624,0.00006262743,0.00005081024,0.000013333733,0.00032783687,0.00005666342,0.0000379202],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99863654,0.000047716254,0.00035001684,0.0004094582,0.0002777346,0.00027854563],"domain_scores_gemma":[0.9994055,0.00012459396,0.00013401578,0.00016921575,0.000005515682,0.0001611562],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00026293652,0.00026497716,0.00030908914,0.00027963804,0.00012479424,0.000021832873,0.00006971961,0.00019594628,0.000011473689],"category_scores_gemma":[0.00003472158,0.0002756251,0.00005710028,0.00018190964,0.00004460173,0.00018487613,0.00009202346,0.00012350704,0.0000031638665],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011236513,0.000023844394,0.0001376449,0.00009155252,0.000045773948,0.0000059884856,0.00033467158,0.22483577,0.77247566,0.000008491817,5.834796e-7,0.0019276687],"study_design_scores_gemma":[0.00065571937,0.0000802877,0.00033237893,0.00014852344,0.000049188744,0.000027726754,0.00015951642,0.06060664,0.93757,0.0000021408794,0.00010144009,0.0002664589],"about_ca_topic_score_codex":0.000012899031,"about_ca_topic_score_gemma":0.000016968866,"teacher_disagreement_score":0.16509433,"about_ca_system_score_codex":0.00023138033,"about_ca_system_score_gemma":0.000007865443,"threshold_uncertainty_score":0.9999696},"labels":[],"label_agreement":null},{"id":"W2064469073","doi":"10.1016/j.ces.2007.05.029","title":"Selective hydrogenation of 1,3-butadiene in mixture with isobutene on a Pd/<mml:math xmlns:mml=\"http://www.w3.org/1998/Math/MathML\" altimg=\"si52.gif\" display=\"inline\" overflow=\"scroll\"><mml:mi>α</mml:mi></mml:math>-alumina catalyst in a semi-batch reactor","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":39,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Raffinate; Chemistry; Catalysis; Naphtha; Chemical engineering; Isobutylene; Hydrogen; Organic chemistry; Extraction (chemistry); Copolymer","score_opus":0.0074087515526968205,"score_gpt":0.22084751417520926,"score_spread":0.21343876262251243,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2064469073","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9982005,0.00008558857,0.0010324076,0.000031760155,0.0001416839,0.00007639305,0.000022832442,0.000115294766,0.00029358728],"genre_scores_gemma":[0.99781924,0.000011555244,0.0017816114,0.000030188945,0.0001274279,0.00006507749,0.00006965919,0.00008156206,0.000013682073],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99707764,0.0000073730967,0.0005903166,0.0006687966,0.0008231523,0.00083270343],"domain_scores_gemma":[0.9986114,0.00030915652,0.00022555547,0.00051955547,0.000081333295,0.00025303656],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00084725826,0.00033611135,0.00030163693,0.0003526767,0.000062284096,0.000040203246,0.0005676777,0.00030997215,0.0000036077747],"category_scores_gemma":[0.0011500162,0.00035775718,0.00015369688,0.0016829764,0.00023518877,0.00046971333,0.00020899902,0.00072945806,0.000024003426],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015070527,0.00010642614,0.000034156517,0.000257415,0.000036328114,0.000095105876,0.0007635598,0.013347132,0.861171,0.12376685,0.000002769203,0.00026857542],"study_design_scores_gemma":[0.00034975648,0.00006332994,0.00008021795,0.000352338,0.000019883915,0.000083886676,0.000052962423,0.45655718,0.5422071,0.0000076228803,0.000025445648,0.00020023981],"about_ca_topic_score_codex":0.00025387848,"about_ca_topic_score_gemma":0.000044156128,"teacher_disagreement_score":0.44321007,"about_ca_system_score_codex":0.00022801936,"about_ca_system_score_gemma":0.00018996211,"threshold_uncertainty_score":0.99988747},"labels":[],"label_agreement":null},{"id":"W2066989322","doi":"10.1016/j.fuel.2009.09.034","title":"Kinetic studies of the autothermal reforming of tetradecane over Pt/Al2O3 catalyst in a fixed-bed reactor","year":2009,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":34,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Royal Military College of Canada; Queen's University","funders":"National Energy Technology Laboratory; Natural Sciences and Engineering Research Council of Canada; Astellas Pharma US; U.S. Department of Energy","keywords":"Tetradecane; Catalysis; Thermodynamics; Chemistry; Kinetics; Hydrocarbon; Materials science; Organic chemistry; Physics","score_opus":0.018906056146829837,"score_gpt":0.27298912079026055,"score_spread":0.2540830646434307,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2066989322","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99638397,0.0014004153,0.000003887655,0.00008487509,0.00010400503,0.00014894169,0.000013541114,0.0000358271,0.0018245192],"genre_scores_gemma":[0.99937993,0.000036244553,0.00009380055,0.000023045382,0.000062709085,0.0000060019047,0.000005443077,0.000021871065,0.00037094456],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987102,0.00001712629,0.0005240484,0.00018265824,0.00028820048,0.00027777965],"domain_scores_gemma":[0.99915224,0.00010086476,0.00019700106,0.00046627515,0.000043173197,0.0000404545],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00020529912,0.00017314096,0.00043153626,0.00013454356,0.000014517381,0.0000022356212,0.00030225024,0.00008997796,0.00001824614],"category_scores_gemma":[0.00039740477,0.00011548962,0.0001545454,0.00046953704,0.0000735178,0.00011388728,0.0000916105,0.00022586538,0.0000027496312],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000024786768,0.00006289983,0.00078628666,0.000263505,0.000054448916,0.0000053237536,0.0021150187,0.000087770604,0.9937059,0.00023582688,0.000012990587,0.002645214],"study_design_scores_gemma":[0.0007950991,0.00005336395,0.018140819,0.00049704773,0.000051088293,0.000017556345,0.0004293336,0.00074592215,0.9783649,0.00015553227,0.00054577773,0.00020359151],"about_ca_topic_score_codex":0.00045986188,"about_ca_topic_score_gemma":0.00009462696,"teacher_disagreement_score":0.017354533,"about_ca_system_score_codex":0.00016958236,"about_ca_system_score_gemma":0.00003352859,"threshold_uncertainty_score":0.47095302},"labels":[],"label_agreement":null},{"id":"W2067383332","doi":"10.1021/jp8038219","title":"Chemisorption and Reactivity of CH<sub><i>x</i></sub> (<i>x</i> = 0−4) on Fe−Co Alloy Surfaces","year":2008,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Methanation; Chemisorption; Catalysis; Adsorption; Exothermic reaction; Chemistry; Density functional theory; Alloy; Reactivity (psychology); Physical chemistry; Materials science; Computational chemistry; Organic chemistry","score_opus":0.011485795402416656,"score_gpt":0.22707743139258113,"score_spread":0.21559163599016448,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2067383332","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9986511,0.000101066675,0.000016296846,0.00007395377,0.000020363237,0.000042570737,0.000007705165,0.000019769433,0.0010671662],"genre_scores_gemma":[0.99938554,0.00013826521,0.0000141700775,0.000011364596,0.00036258658,9.843699e-7,0.0000033671276,0.000025818594,0.000057893467],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99880695,0.000022858385,0.00035410927,0.00012726815,0.0004746287,0.00021420361],"domain_scores_gemma":[0.9987424,0.00035933047,0.00042029642,0.0002586854,0.000094415685,0.00012488372],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003366132,0.00019974148,0.00042444194,0.000021537826,0.000059886253,0.000004208782,0.00024842087,0.000085810556,0.0000054224315],"category_scores_gemma":[0.00019709245,0.00013734557,0.00019575619,0.00013897511,0.00017690205,0.000157631,0.000057822177,0.00058167265,0.000004093174],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016034355,0.0001613549,0.000031908094,0.000122046586,0.000065289,0.000008020886,0.00030505113,0.0005942954,0.9977246,0.00000528393,0.000041144107,0.0007806778],"study_design_scores_gemma":[0.00048962876,0.00006335645,0.0001611163,0.00010601741,0.000069997826,0.0002974742,0.000048700775,0.00086770084,0.9975825,0.00006379893,0.00010742772,0.00014231312],"about_ca_topic_score_codex":0.0000083974755,"about_ca_topic_score_gemma":1.7643805e-7,"teacher_disagreement_score":0.0010092728,"about_ca_system_score_codex":0.00008208402,"about_ca_system_score_gemma":0.000035376186,"threshold_uncertainty_score":0.56007904},"labels":[],"label_agreement":null},{"id":"W2068105925","doi":"10.1016/j.ijhydene.2012.04.082","title":"Hydrogen production by methane cracking using Ni-supported catalysts in a fluidized bed","year":2012,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":51,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Methane; Fluidized bed; Space velocity; Chemical engineering; Materials science; Hydrogen production; Fluidization; Carbon fibers; Hydrogen; Catalysis; Chemistry; Composite material; Organic chemistry","score_opus":0.01662082410844124,"score_gpt":0.2737814000283054,"score_spread":0.2571605759198642,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2068105925","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9961729,0.0017956482,0.0004884047,0.00014732055,0.0011824582,0.000054070428,0.000010519173,0.000033415196,0.00011527963],"genre_scores_gemma":[0.99801075,0.000069689486,0.0004900106,0.000048448714,0.0011244295,0.000005419661,0.00007362909,0.000060135488,0.00011750121],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9973417,0.000070405134,0.0010310287,0.0002104167,0.0008881694,0.0004582993],"domain_scores_gemma":[0.99862224,0.00005981367,0.0006238518,0.00019725467,0.0002824246,0.00021444283],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00089648797,0.00024877844,0.00043425657,0.00063627586,0.000027477321,0.00001650174,0.0005093938,0.00013586895,0.000070995986],"category_scores_gemma":[0.00044462425,0.000234982,0.00024676556,0.0003676555,0.000035668654,0.0009948779,0.000121767465,0.00030194045,0.000007772117],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011291141,0.00016380691,0.0012694552,0.000008619383,0.00044864937,0.00007478545,0.00030406562,0.0012786203,0.9934052,0.00006895032,0.000045965608,0.002818957],"study_design_scores_gemma":[0.0009585021,0.000016896909,0.000010561028,0.000116121424,0.00008323653,0.001846207,0.00006519545,0.002094044,0.9920042,0.00007971345,0.0024879768,0.00023732535],"about_ca_topic_score_codex":0.00076997833,"about_ca_topic_score_gemma":0.000031775533,"teacher_disagreement_score":0.0025816318,"about_ca_system_score_codex":0.0007675945,"about_ca_system_score_gemma":0.000089570305,"threshold_uncertainty_score":0.95822877},"labels":[],"label_agreement":null},{"id":"W2068385046","doi":"10.2202/1542-6580.1241","title":"Hydrogen from an Internally Circulating Fluidized Bed Membrane Reactor","year":2005,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":27,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Membrane Reactor Technologies (Canada); University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Membrane reactor; Endothermic process; Hydrogen; Chemical looping combustion; Fluidized bed; Steam reforming; Hydrogen production; Chemical engineering; Water-gas shift reaction; Catalysis; Chemistry; Methane reformer; Materials science; Waste management; Organic chemistry; Adsorption","score_opus":0.010365350213715364,"score_gpt":0.2559715628520132,"score_spread":0.24560621263829785,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2068385046","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99666965,0.00021957642,0.0017251163,0.00025550643,0.0007361583,0.00006328004,0.000027797225,0.00014164003,0.00016126968],"genre_scores_gemma":[0.9903704,0.000017699234,0.00582239,0.000067590256,0.0035369752,0.000003858505,0.00007613126,0.000098388125,0.000006604121],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9970847,0.000015442287,0.0011719752,0.0002899698,0.0010553086,0.0003826063],"domain_scores_gemma":[0.9981453,0.00034123813,0.00045587504,0.00028606685,0.00036543075,0.00040609585],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00034385122,0.00034586707,0.00053563574,0.0002979903,0.000006018299,0.000064149346,0.0010714699,0.0002039929,0.00022911263],"category_scores_gemma":[0.0013012607,0.00032715301,0.00040761364,0.00014446175,0.000024286306,0.0010327644,0.00014977927,0.0007833258,0.000026897098],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011933185,0.00008822445,0.00010190005,0.000011679044,0.00046675673,0.00011391326,0.0003008946,0.00049876334,0.99196005,0.00006568486,0.000009351051,0.0062634316],"study_design_scores_gemma":[0.0012114762,0.000020568643,0.000013875854,0.00027969002,0.00006675005,0.00040818506,0.000018561701,0.026749402,0.9677153,0.00002938313,0.0031612108,0.00032557722],"about_ca_topic_score_codex":0.00007532101,"about_ca_topic_score_gemma":0.0000017581409,"teacher_disagreement_score":0.026250638,"about_ca_system_score_codex":0.00076302764,"about_ca_system_score_gemma":0.000057931506,"threshold_uncertainty_score":0.99991804},"labels":[],"label_agreement":null},{"id":"W2069890507","doi":"10.1016/j.ijhydene.2008.06.058","title":"Thermal and catalytic dry reforming and cracking of ethanol for hydrogen and carbon nanofilaments' production","year":2008,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":83,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Cracking; Catalysis; Carbon fibers; Fluid catalytic cracking; Hydrogen; Chemical engineering; Ethanol; Carbon dioxide reforming; Materials science; Hydrogen production; Chemistry; Syngas; Organic chemistry; Composite material; Composite number","score_opus":0.012289137149658055,"score_gpt":0.23958641869057332,"score_spread":0.22729728154091527,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2069890507","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979316,0.0014717137,0.00015214004,0.000099355486,0.00019205452,0.000049315564,0.00000521409,0.000009746111,0.00008886716],"genre_scores_gemma":[0.99886835,0.0002897018,0.00035433876,0.000017460565,0.0003153692,0.000004237066,0.0000070575206,0.000025674515,0.00011783508],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989145,0.000011573505,0.00045686337,0.00015529964,0.00031747762,0.00014430434],"domain_scores_gemma":[0.999248,0.00006078962,0.00034929594,0.000083490486,0.00018046147,0.0000779432],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00022946796,0.00013211253,0.00024663613,0.00022561797,0.000038831113,0.0000068307213,0.00013518213,0.00006747186,0.0000016466756],"category_scores_gemma":[0.00014093569,0.00011363666,0.0000731611,0.000058460002,0.00008090141,0.0003292311,0.00008998949,0.000098367906,6.323872e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001078623,0.000027116697,0.001602416,0.000036788962,0.00032049313,0.000032240154,0.00053574145,0.000800097,0.9840289,0.00014099042,6.658261e-7,0.012366723],"study_design_scores_gemma":[0.000674484,0.00006373814,0.00013790787,0.00013322795,0.000057178317,0.0013539811,0.000067616034,0.0063592787,0.9905875,0.00012344407,0.00032213575,0.00011955481],"about_ca_topic_score_codex":0.00019124537,"about_ca_topic_score_gemma":0.000007737931,"teacher_disagreement_score":0.012247168,"about_ca_system_score_codex":0.00009431624,"about_ca_system_score_gemma":0.000034348934,"threshold_uncertainty_score":0.46339685},"labels":[],"label_agreement":null},{"id":"W2070015515","doi":"10.1021/ef700361m","title":"Dynamic Optimization Strategies of a Heterogeneous Reactor for CO<sub>2</sub>Conversion to Methanol","year":2007,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Methanol; Process engineering; Renewable energy; Mole fraction; Steady state (chemistry); Environmental science; Computer science; Chemistry; Engineering","score_opus":0.009206476290515068,"score_gpt":0.24799128440335605,"score_spread":0.23878480811284097,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2070015515","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6577841,0.000098431214,0.34139284,0.000013736752,0.00013383829,0.0001196738,0.000018870416,0.00009255163,0.0003459706],"genre_scores_gemma":[0.9924864,0.000028334227,0.0070748483,0.00002526133,0.00006515334,0.000025910611,0.00014017134,0.000060759463,0.00009316429],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99873704,0.0000111263025,0.00038884557,0.00027588726,0.00022350272,0.0003635915],"domain_scores_gemma":[0.9991903,0.00015614997,0.00013112173,0.00028665925,0.0000985576,0.00013721999],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024892692,0.00019722218,0.0002938634,0.00023752585,0.000031849526,0.000011566738,0.00017788024,0.0001550501,0.000016235748],"category_scores_gemma":[0.00009351601,0.00019506284,0.00016687595,0.000252944,0.00002327724,0.00017970832,0.000051293086,0.0000748648,0.000005283186],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000082153805,0.000026156946,0.0000018322868,0.0000840376,0.000058917693,0.0000052088667,0.00011271748,0.044578306,0.9483758,0.0004461411,0.000004771703,0.006223963],"study_design_scores_gemma":[0.00037412666,0.0000909211,0.0000037973882,0.00004699732,0.000036391684,0.0000134693355,0.000120872646,0.010217816,0.9879264,0.000060861166,0.0009132022,0.00019510464],"about_ca_topic_score_codex":0.000065145294,"about_ca_topic_score_gemma":0.000043558382,"teacher_disagreement_score":0.3347023,"about_ca_system_score_codex":0.00018884624,"about_ca_system_score_gemma":0.00003507953,"threshold_uncertainty_score":0.7954431},"labels":[],"label_agreement":null},{"id":"W2071640534","doi":"10.1007/s11244-011-9704-z","title":"Computational Investigation of the Thermochemistry and Kinetics of Steam Methane Reforming Over a Multi-Faceted Nickel Catalyst","year":2011,"lang":"en","type":"article","venue":"Topics in Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":111,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dow Chemical (Canada)","funders":"","keywords":"Thermochemistry; Chemisorption; Catalysis; Methane; Nickel; Steam reforming; Hydrogen; Chemistry; Thermodynamics; Methanation; Physical chemistry; Materials science; Inorganic chemistry; Hydrogen production; Organic chemistry","score_opus":0.02791763104760409,"score_gpt":0.24854789459409266,"score_spread":0.22063026354648857,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2071640534","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99895287,0.00018311344,0.0003976861,0.000017357057,0.00003586167,0.00009921674,0.000018390489,0.00001472105,0.00028079975],"genre_scores_gemma":[0.99685335,0.000008294166,0.0028466461,0.000007975353,0.000018435541,0.000007734517,0.000061004925,0.00001612237,0.00018042473],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99890935,0.000021215712,0.00049818197,0.0001869122,0.00023892352,0.00014540584],"domain_scores_gemma":[0.9991845,0.00006629867,0.00025071044,0.00037794263,0.00007408907,0.00004645878],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002036737,0.00013506849,0.0002958009,0.00010805574,0.00001327637,0.0000019124127,0.00023749757,0.00011533119,0.000020264462],"category_scores_gemma":[0.000197795,0.00010524867,0.00010099548,0.00043782286,0.00015247572,0.00008334195,0.00017503007,0.0001778147,6.170463e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012594097,0.000057462308,0.018549517,0.0002602065,0.0001081013,0.0000012145962,0.0032737034,0.0005073994,0.9748591,0.00014459911,6.6612614e-7,0.0022254174],"study_design_scores_gemma":[0.00045799633,0.000009026724,0.014567397,0.00008537282,0.00008841839,0.000006409536,0.0002637249,0.0054501607,0.978719,0.00022902194,0.000007828494,0.00011565188],"about_ca_topic_score_codex":0.0008901426,"about_ca_topic_score_gemma":0.000072188115,"teacher_disagreement_score":0.0049427613,"about_ca_system_score_codex":0.000090180336,"about_ca_system_score_gemma":0.000025442474,"threshold_uncertainty_score":0.42919162},"labels":[],"label_agreement":null},{"id":"W2072957130","doi":"10.1016/j.fuel.2013.12.016","title":"Evaluating the performance of non-precious metal based catalysts for sulfur-tolerance during the dry reforming of biogas","year":2013,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":61,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Bimetallic strip; Metal; Dispersion (optics); Cobalt; Surface-area-to-volume ratio; Materials science; Carbon dioxide reforming; Chemical engineering; Biogas; Chemistry; Inorganic chemistry; Metallurgy; Syngas; Organic chemistry; Waste management","score_opus":0.01900626121245363,"score_gpt":0.27844688119999556,"score_spread":0.2594406199875419,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2072957130","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9981851,0.00034017657,0.00023141809,0.000059575974,0.0001677945,0.00068265485,0.00002172921,0.00004011105,0.00027143673],"genre_scores_gemma":[0.9977283,0.000010384654,0.001491471,0.000015550251,0.00013305376,0.00022183139,0.000018765502,0.000045858134,0.0003348111],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998327,0.00002490026,0.000602206,0.00023853408,0.00041236024,0.00039499713],"domain_scores_gemma":[0.9982961,0.00037387945,0.00034974428,0.0007222598,0.00020783345,0.000050181072],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007440773,0.00021271591,0.0003702549,0.00009133036,0.00014198221,0.000010217948,0.000577874,0.00008309878,0.000028306993],"category_scores_gemma":[0.0003404811,0.00012234478,0.00025617707,0.000328438,0.00010969776,0.00026612022,0.00013550607,0.00022712976,0.000017383967],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047157104,0.000022939206,0.0009349312,0.00074325054,0.000068398454,2.446693e-7,0.00069499586,0.0040346496,0.9890201,0.000016499647,0.00000308512,0.0044137104],"study_design_scores_gemma":[0.0006652616,0.00006373474,0.0018146508,0.00016626883,0.000067671586,0.000005385091,0.00021215675,0.17086388,0.8259346,0.000012245465,0.00005574527,0.00013842538],"about_ca_topic_score_codex":0.0005175275,"about_ca_topic_score_gemma":0.000017080329,"teacher_disagreement_score":0.16682924,"about_ca_system_score_codex":0.000098222015,"about_ca_system_score_gemma":0.000053044838,"threshold_uncertainty_score":0.4989075},"labels":[],"label_agreement":null},{"id":"W2073075401","doi":"10.1002/cjce.5450850610","title":"Dry Reforming of Methane with a Ni/Al<sub>2</sub>O<sub>3</sub>‐YSZ Catalyst: The Role of the Catalyst Preparation Protocol","year":2007,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Calcination; Materials science; Carbon dioxide reforming; Chemical engineering; Methane; Nickel; Ceramic; Syngas; Catalyst support; Porosity; Yttria-stabilized zirconia; Cubic zirconia; Pellets; Metallurgy; Composite material; Chemistry; Metal; Organic chemistry","score_opus":0.005286698603545784,"score_gpt":0.21066206987860303,"score_spread":0.20537537127505726,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073075401","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99513036,0.0002374246,0.00055381074,0.00014640292,0.00013060434,0.0035750084,0.000018267445,0.000028867365,0.00017927254],"genre_scores_gemma":[0.99905276,0.0000020122525,0.00016239323,0.00002841417,0.00025436157,0.00039401182,0.00000884486,0.000090702466,0.0000065193017],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99695355,0.00003525979,0.0012341886,0.00024019132,0.0007928573,0.00074398326],"domain_scores_gemma":[0.99733377,0.0002862548,0.00080465374,0.0007801914,0.00033433357,0.0004608012],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0017205463,0.00040286774,0.00065509195,0.0003091938,0.000109650566,0.000026637876,0.0010650482,0.00021282134,0.0000038967733],"category_scores_gemma":[0.00070899574,0.00022544115,0.00037802276,0.00097631,0.00024183646,0.00030718336,0.000106354586,0.0011405149,0.0000024016504],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000121184945,0.000017005366,0.00011296963,0.0001738358,0.00022795123,0.000016302401,0.0009919191,0.007046778,0.98772275,0.00012782047,0.0000073253364,0.0034341388],"study_design_scores_gemma":[0.0006246017,0.000057367928,0.000091632355,0.00062618824,0.00017456962,0.00036820187,0.0001648882,0.0033912621,0.9936522,0.00005159508,0.00052173925,0.0002757023],"about_ca_topic_score_codex":0.0017771063,"about_ca_topic_score_gemma":0.002376634,"teacher_disagreement_score":0.0059294826,"about_ca_system_score_codex":0.0007620266,"about_ca_system_score_gemma":0.00061230303,"threshold_uncertainty_score":0.9193223},"labels":[],"label_agreement":null},{"id":"W2073264481","doi":"10.1002/cjce.20680","title":"Multicomponent mass diffusion in porous pellets: Effects of flux models on the pellet level and impacts on the reactor level. Application to methanol synthesis","year":2011,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":true,"ca_institutions":"","funders":"Norges Forskningsråd","keywords":"Pellet; Knudsen diffusion; Diffusion; Pellets; Knudsen number; Flux (metallurgy); Particle (ecology); Chemistry; Thermodynamics; Mass flux; Mechanics; Chemical engineering; Materials science; Physics; Engineering; Composite material; Organic chemistry","score_opus":0.03072857426694784,"score_gpt":0.20531982423267076,"score_spread":0.17459124996572292,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073264481","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9963855,0.000103665065,0.0021034621,0.0008245309,0.000069888214,0.00033625631,0.000014033259,0.000011110665,0.00015153969],"genre_scores_gemma":[0.99939924,0.0000055557234,0.00036133087,0.00007990533,0.00006695231,0.00002528708,0.0000011853729,0.000047465666,0.000013046952],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99864703,0.000038881288,0.00045486956,0.00015640727,0.00031676577,0.00038604863],"domain_scores_gemma":[0.9976708,0.001368066,0.00016482486,0.00038646994,0.00005713559,0.00035268886],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00066560745,0.00024317765,0.00035565387,0.0002224518,0.00004404897,0.000015092932,0.0005223098,0.00011612644,0.000014740789],"category_scores_gemma":[0.0014260309,0.00013190691,0.00011547102,0.00024000985,0.00005095826,0.00007208993,0.000043521377,0.0006270671,0.000004666452],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000045692927,0.00002000587,0.000009259695,0.00006133832,0.000055790304,0.000014181804,0.0013387594,0.0045687826,0.99112236,0.0015557279,0.000012169021,0.0011958977],"study_design_scores_gemma":[0.00023322186,0.000035890695,0.00023545127,0.00053606625,0.000044608892,0.000037487436,0.00006249195,0.025969306,0.9724549,0.00019519057,0.00003429866,0.0001610882],"about_ca_topic_score_codex":0.0030374022,"about_ca_topic_score_gemma":0.00018820885,"teacher_disagreement_score":0.021400522,"about_ca_system_score_codex":0.00042441496,"about_ca_system_score_gemma":0.00007845682,"threshold_uncertainty_score":0.5379008},"labels":[],"label_agreement":null},{"id":"W2073812893","doi":"10.1021/jp073757m","title":"Theoretical Studies of the Formation and Reactivity of C<sub>2</sub>Hydrocarbon Species on the Fe(100) Surface","year":2007,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":44,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Chemistry; Reactivity (psychology); Hydrocarbon; Ethylene; Hydride; Adsorption; Catalysis; Density functional theory; Hydrogen atom; Hydrogen; Atom (system on chip); Computational chemistry; Physical chemistry; Photochemistry; Organic chemistry","score_opus":0.015139599373240865,"score_gpt":0.24886276133136118,"score_spread":0.23372316195812032,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073812893","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99801576,0.00013819452,0.000057256533,0.00033696304,0.00002685825,0.0000593628,0.0000032838993,0.000005540507,0.0013567886],"genre_scores_gemma":[0.9997364,0.000037377595,0.0000051723714,0.000009737474,0.00018609464,3.0253435e-7,3.1609386e-7,0.0000110650235,0.000013493004],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989097,0.000041167943,0.000367762,0.00006277772,0.00046017108,0.00015839259],"domain_scores_gemma":[0.9976324,0.0015091555,0.0004370209,0.0002625072,0.00011800172,0.000040920644],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010700396,0.00013449069,0.0003136863,0.000011231838,0.00005650961,0.0000039374913,0.000284338,0.00004787693,0.0000025979443],"category_scores_gemma":[0.00069864816,0.000058145277,0.00017928325,0.00015934459,0.0005033765,0.000085028725,0.00010221045,0.00048874674,4.2956978e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001223673,0.00006397421,0.0000073800775,0.00011345323,0.00008449094,7.7416377e-7,0.0010880511,0.00033915462,0.995772,0.0020147304,0.000007141402,0.0003865079],"study_design_scores_gemma":[0.000183607,0.000041172996,0.00012478277,0.00018169479,0.00010349792,0.00003933877,0.0009996284,0.00150288,0.9947325,0.002016811,0.00001120698,0.00006290776],"about_ca_topic_score_codex":0.0000022346908,"about_ca_topic_score_gemma":4.377491e-7,"teacher_disagreement_score":0.0017206894,"about_ca_system_score_codex":0.00008456971,"about_ca_system_score_gemma":0.000014744147,"threshold_uncertainty_score":0.23710956},"labels":[],"label_agreement":null},{"id":"W2075698096","doi":"10.1021/ie901861y","title":"Fischer−Tropsch Synthesis in a Slurry Reactor Using a Nanoiron Carbide Catalyst Produced by a Plasma Spray Technique","year":2010,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":33,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Resources Canada; Natural Sciences and Engineering Research Council of Canada","keywords":"Fischer–Tropsch process; Slurry; Catalysis; Carbide; Chemical engineering; Materials science; Syngas; Chemistry; Metallurgy; Organic chemistry; Engineering; Composite material","score_opus":0.053822841016923896,"score_gpt":0.31332928417272515,"score_spread":0.25950644315580124,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2075698096","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9981693,0.00006270618,0.000019221363,0.00011038328,0.0002233513,0.0006851631,0.00007653888,0.00030099155,0.00035232026],"genre_scores_gemma":[0.99751586,0.0000045296797,0.00027811396,0.0000012538569,0.0010812548,0.00051488396,0.00005915581,0.00019140611,0.00035354646],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99569607,0.000058810405,0.0007956471,0.00091838575,0.0010712118,0.0014598656],"domain_scores_gemma":[0.99744654,0.0007264103,0.00012193274,0.0010857154,0.00017018167,0.00044921],"candidate_categories":["metaresearch","metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0024730803,0.000521299,0.0006843221,0.00039349083,0.000107299784,0.000087149645,0.0009043383,0.001155878,0.00013105955],"category_scores_gemma":[0.009166175,0.00055052346,0.00017958056,0.0016065558,0.00013526059,0.0002906913,0.00037526194,0.005347057,0.00001819427],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007841606,0.00009251934,0.00021292019,0.00025056666,0.000058189435,0.000081529215,0.000076901015,0.00045190757,0.998108,0.000006876831,0.00008149169,0.0005006243],"study_design_scores_gemma":[0.00069681974,0.000014576709,0.000004453827,0.00041603355,0.00002576281,0.000114208524,0.000054177137,0.0073887184,0.9867245,0.0000014184684,0.0040023476,0.0005570171],"about_ca_topic_score_codex":0.0014441189,"about_ca_topic_score_gemma":0.000016932805,"teacher_disagreement_score":0.011383591,"about_ca_system_score_codex":0.0009904677,"about_ca_system_score_gemma":0.00040747924,"threshold_uncertainty_score":0.99969465},"labels":[],"label_agreement":null},{"id":"W2076098989","doi":"10.1021/ie701764y","title":"Comparative Simulations of Cobalt- and Iron-Based Fischer-Tropsch Synthesis Slurry Bubble Column Reactors","year":2008,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Fischer–Tropsch process; Cobalt; Catalysis; Chemistry; Slurry; Bubble column reactor; Water gas; Isothermal process; Syngas; Space velocity; Water-gas shift reaction; Chemical engineering; Thermodynamics; Bubble; Inorganic chemistry; Organic chemistry; Mechanics; Selectivity; Gas bubble","score_opus":0.13911642168280478,"score_gpt":0.34003367270594803,"score_spread":0.20091725102314326,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2076098989","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985095,0.00013551205,0.000042926313,0.00005309373,0.00006561356,0.00025764122,0.000105480096,0.0001334276,0.0006968071],"genre_scores_gemma":[0.9989616,0.000008022775,0.0001260845,0.000001105074,0.00032033262,0.000049565246,0.00005448904,0.00005488689,0.00042389418],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976316,0.000044974928,0.0005130653,0.0004049906,0.0007709988,0.0006343418],"domain_scores_gemma":[0.9969354,0.0019392365,0.000093804716,0.00047940476,0.0002460311,0.00030607148],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005612538,0.00027650606,0.0005644528,0.00017529674,0.0001662875,0.000020530451,0.0003395834,0.00041681447,0.00015945389],"category_scores_gemma":[0.0026501003,0.00029741778,0.00010941406,0.0008421589,0.00024332872,0.00013637403,0.00015119147,0.0012342753,0.0000073674037],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006328612,0.00006919941,0.0008077949,0.00018871146,0.00006667533,0.00001679944,0.00015928959,0.054260023,0.94412863,0.0000103985885,0.00010394429,0.00012525773],"study_design_scores_gemma":[0.0007537099,0.000025343825,0.00009047805,0.00018984325,0.000023855577,0.000022031765,0.00008408663,0.09180892,0.90515995,0.0000015858251,0.0015829604,0.00025722844],"about_ca_topic_score_codex":0.0003298644,"about_ca_topic_score_gemma":0.0000024473495,"teacher_disagreement_score":0.038968664,"about_ca_system_score_codex":0.00033688985,"about_ca_system_score_gemma":0.0002692491,"threshold_uncertainty_score":0.9999478},"labels":[],"label_agreement":null},{"id":"W2077202413","doi":"10.3390/en20200180","title":"Optimal Fixed Bed Reactor Network Configuration for the Efficient Recycling of CO2 into Methanol","year":2009,"lang":"en","type":"article","venue":"Energies","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University; University of Waterloo","funders":"","keywords":"Methanol; Production (economics); Process engineering; Profit (economics); Environmental science; Computer science; Mathematical optimization; Mathematics; Engineering; Chemistry","score_opus":0.01354877003916303,"score_gpt":0.25863114660845365,"score_spread":0.24508237656929063,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2077202413","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9679171,0.00091062364,0.02976628,0.00023567313,0.0003261579,0.000250416,0.0000042823326,0.00012375857,0.00046571894],"genre_scores_gemma":[0.9926824,0.000016972526,0.00668369,0.00002365435,0.00032632903,0.000030661926,0.00003275966,0.000019021494,0.00018450845],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99910134,0.000014889203,0.00032098932,0.00015825099,0.00017127772,0.00023323605],"domain_scores_gemma":[0.9989626,0.0005365122,0.00013358463,0.00026286274,0.00007019171,0.000034272936],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035174485,0.00013197877,0.00022870029,0.000043426455,0.00007053123,0.00001197055,0.0001807998,0.00008129026,0.000012603903],"category_scores_gemma":[0.00037867378,0.00009260578,0.0001372192,0.00017575781,0.00003263223,0.000059592756,0.000027234115,0.00010870159,0.0000018608735],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000043992273,0.000010233008,0.000001939568,0.000016087768,0.000031433956,2.9217966e-7,0.00041580215,0.4204006,0.5715963,0.0017371527,0.00003848457,0.005707636],"study_design_scores_gemma":[0.00028502787,0.000042409683,0.000026181235,0.00005048137,0.000049253184,0.0000016694365,0.00018229445,0.09989192,0.8966531,0.0000902402,0.0026155894,0.00011183673],"about_ca_topic_score_codex":0.00006382987,"about_ca_topic_score_gemma":0.00000389107,"teacher_disagreement_score":0.32505676,"about_ca_system_score_codex":0.000058877904,"about_ca_system_score_gemma":0.000018259449,"threshold_uncertainty_score":0.37763542},"labels":[],"label_agreement":null},{"id":"W2077415362","doi":"10.1016/j.biortech.2012.07.019","title":"Hydrogen production from steam reforming of acetic acid over Cu–Zn supported calcium aluminate","year":2012,"lang":"en","type":"article","venue":"Bioresource Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":51,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Steam reforming; Catalysis; Hydrogen production; Acetic acid; Aluminate; Nuclear chemistry; Coke; Scanning electron microscope; Hydrogen; Materials science; Yield (engineering); Chemistry; Inorganic chemistry; Chemical engineering; Metallurgy; Cement; Organic chemistry; Composite material","score_opus":0.014386976398994927,"score_gpt":0.2489380163478223,"score_spread":0.2345510399488274,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2077415362","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9969344,0.0013389853,0.0001203568,0.00017723849,0.00023536282,0.00023656727,0.000024591078,0.0006681401,0.00026432466],"genre_scores_gemma":[0.99881804,0.000012292224,0.00035475256,0.0000103355815,0.00025199176,0.00003532528,0.00006683981,0.00007320104,0.00037723788],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99811715,0.000018082925,0.0005130468,0.00037806653,0.0002751161,0.0006985493],"domain_scores_gemma":[0.9986921,0.000024922403,0.00025789987,0.00084692816,0.00005555244,0.00012259142],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00027715467,0.0002767523,0.00045239308,0.0005008452,0.00005458564,0.0000022705133,0.00040704018,0.00052896584,0.00011025804],"category_scores_gemma":[0.00037155827,0.00025093625,0.00013153834,0.0007225611,0.00022233282,0.000188258,0.00031993788,0.0004188842,0.00007555861],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000023729284,0.00007500749,0.006225228,0.00004571765,0.000084389925,0.0000039753886,0.00038169426,0.000007850042,0.98233926,0.00011260831,0.000018000637,0.010682515],"study_design_scores_gemma":[0.00036610095,0.000037561415,0.0005621592,0.00006397982,0.00009746738,0.00006327754,0.00053577364,0.00023979532,0.9898655,0.00006975363,0.007821381,0.00027728305],"about_ca_topic_score_codex":0.0003693294,"about_ca_topic_score_gemma":0.000011642705,"teacher_disagreement_score":0.010405231,"about_ca_system_score_codex":0.00023887168,"about_ca_system_score_gemma":0.00001921861,"threshold_uncertainty_score":0.9999943},"labels":[],"label_agreement":null},{"id":"W2079232284","doi":"10.1021/jp8058273","title":"CO<sub>2</sub> + CH<sub>4</sub> Chemistry over Pd: Results of Kinetic Simulations Relevant to Environmental Issues","year":2009,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Chemistry; Formic acid; Carbon monoxide; Plug flow reactor model; Formaldehyde; Arrhenius equation; Bar (unit); Methanol; Hydrogen; Thermodynamics; Plug flow; Methane; Catalysis; Syngas; Physical chemistry; Organic chemistry; Continuous stirred-tank reactor; Activation energy","score_opus":0.006713869542387669,"score_gpt":0.24113351857897222,"score_spread":0.23441964903658455,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2079232284","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99880177,0.00014885043,0.000062023326,0.00027115934,0.000026045851,0.00009998963,0.00010005195,0.00003037413,0.0004597363],"genre_scores_gemma":[0.9987789,0.000046553996,0.00003832044,0.00003155038,0.000931138,0.0000013607739,0.000041201398,0.00004185781,0.00008911513],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977289,0.000024056922,0.00083533657,0.0002367144,0.00076921,0.00040582113],"domain_scores_gemma":[0.9982801,0.00030425462,0.0005199177,0.0005437242,0.00006421772,0.00028778252],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00027657716,0.00033927566,0.0005698576,0.00003443991,0.00006865192,0.000014317234,0.00052125717,0.00013944205,0.000025986872],"category_scores_gemma":[0.00036090318,0.0002607952,0.00035605958,0.00022963996,0.00011625805,0.00015192397,0.00008464356,0.0007112329,0.000020388237],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028966996,0.00028099594,0.000003697029,0.000081489925,0.000082028,0.000012830451,0.00041273117,0.013905453,0.98295236,0.0000022642707,0.00013782275,0.0018386627],"study_design_scores_gemma":[0.0010329023,0.000093983035,0.00017363709,0.00020130392,0.00016320686,0.00008366587,0.000074614916,0.003483129,0.9939357,0.00014227592,0.00033246944,0.00028311127],"about_ca_topic_score_codex":0.0000037442462,"about_ca_topic_score_gemma":1.9778389e-7,"teacher_disagreement_score":0.010983345,"about_ca_system_score_codex":0.00026453898,"about_ca_system_score_gemma":0.00003772302,"threshold_uncertainty_score":0.99998444},"labels":[],"label_agreement":null},{"id":"W2079322546","doi":"10.1016/j.ijhydene.2010.03.136","title":"Steam reforming of propane in a fluidized bed membrane reactor for hydrogen production","year":2010,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":101,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Steam reforming; Hydrogen production; Propane; Fluidized bed; Membrane reactor; Hydrogen; Methane reformer; Methane; Raw material; Chemical engineering; Chemistry; Catalysis; Waste management; Materials science; Organic chemistry; Engineering","score_opus":0.01069615838801053,"score_gpt":0.254022281383787,"score_spread":0.2433261229957765,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2079322546","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9982985,0.00015742582,0.000104337385,0.00021416048,0.000960037,0.00010513455,0.000012749837,0.000019551322,0.00012809364],"genre_scores_gemma":[0.9981222,0.00004847035,0.000734018,0.00001413223,0.0008737642,0.000017217417,0.000028740029,0.00004221437,0.00011921283],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979888,0.000018606539,0.0009901128,0.00018376297,0.00059371284,0.00022499276],"domain_scores_gemma":[0.99849856,0.00008300838,0.0006407109,0.00019544462,0.0004886586,0.00009364392],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006685742,0.00016891476,0.00039392876,0.0005155274,0.000015178187,0.0000063971015,0.0005157941,0.00012310306,0.00003079764],"category_scores_gemma":[0.0008015534,0.00014229704,0.00027148658,0.00018449774,0.000040506202,0.00040309227,0.00006747492,0.00029008035,0.0000012103209],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003860316,0.00012953648,0.00007313336,0.000029942667,0.00023237258,0.000026932781,0.00017412289,0.00043823326,0.98954564,0.0005124959,0.0000038504854,0.008447718],"study_design_scores_gemma":[0.0013911398,0.00006731597,0.0000037191805,0.00012797472,0.000039131603,0.0006821656,0.00004862537,0.0013133327,0.9918539,0.0003030937,0.0040268702,0.000142713],"about_ca_topic_score_codex":0.00023201459,"about_ca_topic_score_gemma":0.00014305545,"teacher_disagreement_score":0.008305005,"about_ca_system_score_codex":0.00020941133,"about_ca_system_score_gemma":0.00010872048,"threshold_uncertainty_score":0.58027047},"labels":[],"label_agreement":null},{"id":"W2080614180","doi":"10.2202/1542-6580.1303","title":"Hydrogen Production in Fluidized Beds with In-Situ Membranes","year":2005,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":40,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"King Saud University; Auburn University","keywords":"Hydrogen production; Steam reforming; Process engineering; Fluidized bed; Membrane reactor; Flexibility (engineering); Hydrogen; Process (computing); Waste management; Environmental science; Materials science; Engineering; Computer science; Chemistry","score_opus":0.007106988075431524,"score_gpt":0.2304624020243123,"score_spread":0.22335541394888078,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2080614180","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9986249,0.00033490147,0.00013597314,0.00038533317,0.0002480768,0.000058329017,0.0000010167747,0.000033622673,0.00017780646],"genre_scores_gemma":[0.99779075,0.00004007767,0.0013114605,0.000010230722,0.00079194276,0.000005278549,0.000006683549,0.000036539328,0.000007044892],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99841946,0.0000060387815,0.00062308327,0.0001595588,0.0005541491,0.00023770149],"domain_scores_gemma":[0.9994028,0.00009383793,0.00015367744,0.00011226458,0.00013760789,0.0000998184],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00027980778,0.0001767455,0.00030471678,0.00045423664,0.000001932164,0.000012804713,0.0003469149,0.000093956965,0.000017168122],"category_scores_gemma":[0.00056000083,0.0001510179,0.00010299256,0.0002485113,0.000015296448,0.0005169296,0.00004387958,0.0005005576,0.000004912469],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015049102,0.00007204543,0.00030385578,0.000025010075,0.00007474041,0.00008154293,0.0002225762,0.003247931,0.9923907,0.00003354806,0.0000020626126,0.0033954808],"study_design_scores_gemma":[0.0010805521,0.000012328171,0.00005597772,0.00035213653,0.00001205455,0.00051126216,0.000017170136,0.0025613506,0.9941405,0.00000957308,0.0010814987,0.00016559851],"about_ca_topic_score_codex":0.000015572197,"about_ca_topic_score_gemma":0.000008975697,"teacher_disagreement_score":0.0032298823,"about_ca_system_score_codex":0.00066571444,"about_ca_system_score_gemma":0.000038525282,"threshold_uncertainty_score":0.6158331},"labels":[],"label_agreement":null},{"id":"W2082121289","doi":"10.1016/j.ijhydene.2011.10.064","title":"Life cycle assessment of various hydrogen production methods","year":2011,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":571,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"","keywords":"Hydrogen production; Life-cycle assessment; Natural gas; Environmental science; Hydrogen; Thermochemical cycle; Coal gasification; Electrolysis of water; Renewable energy; Steam reforming; Water splitting; Coal; Waste management; Electrolysis; Hydrogen economy; Carbon dioxide; Methane; Chemistry; Production (economics); Engineering; Catalysis","score_opus":0.022633451071799888,"score_gpt":0.3137468421556037,"score_spread":0.29111339108380385,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2082121289","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9488753,0.00043412347,0.04445219,0.00014173519,0.0013300809,0.000040365423,0.0000059030153,0.000033414304,0.004686877],"genre_scores_gemma":[0.9791829,0.00006452649,0.019975869,0.00004686958,0.0005098077,0.000003735668,0.0000069159287,0.00003218739,0.00017721741],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99817884,0.000065327244,0.0008141747,0.00015399266,0.0006173725,0.00017030281],"domain_scores_gemma":[0.99847263,0.000055633696,0.0006752602,0.00019296561,0.00042631335,0.00017720417],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00068605796,0.00014841308,0.00031891905,0.00033577235,0.000018607989,0.0000058172322,0.00055690634,0.000079725476,0.00019917834],"category_scores_gemma":[0.00044885837,0.00012966747,0.00028013324,0.0001534997,0.00004067726,0.0002983679,0.00011403891,0.0001953627,0.0000025700535],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009096626,0.00029350424,0.00038444012,0.000016563394,0.0014589952,0.00007853648,0.00041777772,0.023064304,0.9405459,0.005311053,0.00002210183,0.028315835],"study_design_scores_gemma":[0.00039739613,0.00006861581,0.0001051705,0.000056039615,0.000083862375,0.0006046383,0.000042155396,0.012407757,0.98168975,0.001652724,0.002754714,0.00013717676],"about_ca_topic_score_codex":0.00028203332,"about_ca_topic_score_gemma":0.0000075469443,"teacher_disagreement_score":0.041143827,"about_ca_system_score_codex":0.00021560898,"about_ca_system_score_gemma":0.00016125709,"threshold_uncertainty_score":0.5287686},"labels":[],"label_agreement":null},{"id":"W2082545179","doi":"10.1002/ange.200990103","title":"Titelbild: Nanoscale Chemical Imaging of the Reduction Behavior of a Single Catalyst Particle (Angew. Chem. 20/2009)","year":2009,"lang":"de","type":"article","venue":"Angewandte Chemie","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); University of Saskatchewan","funders":"","keywords":"Chemistry; Particle (ecology); Physical chemistry","score_opus":0.012720360390830755,"score_gpt":0.23619245532278846,"score_spread":0.22347209493195772,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2082545179","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99026954,0.006945645,0.000023340086,0.0004852475,0.0005879278,0.0004258671,0.00011833414,0.000097752,0.0010463694],"genre_scores_gemma":[0.99807674,0.000074126256,0.0001949148,0.000035307818,0.00059382454,0.000024992676,0.00012710472,0.00007501363,0.00079795683],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968813,0.000026574226,0.0010832916,0.00058809953,0.00068295386,0.0007377516],"domain_scores_gemma":[0.99775803,0.00006896852,0.0005870075,0.0011402373,0.000222205,0.00022357781],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003192712,0.00048218778,0.0007798495,0.000097464144,0.00008356033,0.000024109837,0.00064688,0.00030421326,0.0000896309],"category_scores_gemma":[0.0002862187,0.00041272322,0.000618211,0.0009343723,0.00035550847,0.00029743454,0.00023640592,0.0004997156,0.000022702925],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006236712,0.00072724547,0.000487695,0.00025204677,0.00009887076,0.000008876172,0.0009781605,0.000012735405,0.9942026,0.000028313989,0.00027207966,0.0028690037],"study_design_scores_gemma":[0.0009167199,0.00005154687,0.00016314883,0.00047846808,0.0007932903,0.000081613776,0.00025015423,0.00009918845,0.9951805,0.000041395244,0.0015112016,0.00043280574],"about_ca_topic_score_codex":0.00016308612,"about_ca_topic_score_gemma":0.000003655317,"teacher_disagreement_score":0.0078072418,"about_ca_system_score_codex":0.0004393562,"about_ca_system_score_gemma":0.000093488336,"threshold_uncertainty_score":0.99983245},"labels":[],"label_agreement":null},{"id":"W2083109696","doi":"10.6000/1929-6002.2015.04.01.3","title":"Solvent Isotope Effect on Hydrogen-Transfer Reduction of CO2 into Formate with Glycerine by Alkaline Hydrothermal Reaction","year":2015,"lang":"en","type":"article","venue":"Journal of Technology Innovations in Renewable Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Fundamental Research Funds for the Central Universities; Tongji University; China Postdoctoral Science Foundation; National Natural Science Foundation of China","keywords":"Chemistry; Formate; Dehydrogenation; Hydrothermal circulation; Solvent; Abiogenic petroleum origin; Hydrogen; Ketone; Inorganic chemistry; Organic chemistry; Catalysis; Methane","score_opus":0.007752247999114105,"score_gpt":0.23495019666185282,"score_spread":0.2271979486627387,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2083109696","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98965234,0.00016166033,0.009028653,0.00038234412,0.00017052155,0.000086485525,0.0000033037459,0.00006324478,0.00045144756],"genre_scores_gemma":[0.99866027,0.000040211475,0.0009209513,0.000014195997,0.00006897234,0.000024609411,0.000027435892,0.000034542278,0.00020884197],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984694,0.00002082891,0.00082968903,0.00014620749,0.00030909083,0.00022475117],"domain_scores_gemma":[0.9990008,0.000025173593,0.0003512026,0.00027575082,0.0002979177,0.00004916121],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005215383,0.00018627009,0.00042036644,0.0013572766,0.00003220313,0.0000043410487,0.00022998315,0.00025547968,0.000007696542],"category_scores_gemma":[0.00013271012,0.00014829141,0.00006341959,0.001852286,0.0000881289,0.00030254063,0.00003535882,0.0003761502,0.0000011954216],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00041520243,0.00013438212,0.00010597423,0.000031556992,0.000103703685,0.00001174276,0.00004285939,0.053679638,0.93976897,0.0012898488,0.000105843246,0.004310295],"study_design_scores_gemma":[0.001809246,0.0011442992,0.0000022545887,0.00019645903,0.000032951553,0.0004943759,0.00011057211,0.0015955426,0.9844,0.0006111119,0.009462141,0.0001410488],"about_ca_topic_score_codex":0.00085036556,"about_ca_topic_score_gemma":0.00009636558,"teacher_disagreement_score":0.052084092,"about_ca_system_score_codex":0.0004358912,"about_ca_system_score_gemma":0.000076941724,"threshold_uncertainty_score":0.6047148},"labels":[],"label_agreement":null},{"id":"W2083129892","doi":"10.1039/b105703k","title":"Production of ultra highly pure H2 and higher hydrocarbons from methane in one step at mild temperatures and development of the catalyst under non-equilibrium reaction conditions","year":2001,"lang":"en","type":"article","venue":"Chemical Communications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":26,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Dehydrogenation; Catalysis; Methane; Hydrogen; Chemistry; Hydrogen production; Thermodynamic equilibrium; Chemical equilibrium; Chemical engineering; Thermodynamics; Organic chemistry","score_opus":0.02967195218759539,"score_gpt":0.25783103148398606,"score_spread":0.22815907929639068,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2083129892","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9974097,0.0007792782,0.000015109685,0.0009952453,0.00004975736,0.0002175692,0.000025800593,0.000029183782,0.00047837826],"genre_scores_gemma":[0.9977447,0.00011705983,0.0014660915,0.000013041813,0.00002526873,0.000048966223,0.00039931003,0.000020548603,0.0001650118],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99897975,0.000034520574,0.00044474786,0.00022075252,0.00017183638,0.00014838252],"domain_scores_gemma":[0.99860287,0.0002108125,0.00015855362,0.00091585884,0.00004869255,0.000063207764],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013473564,0.00014325077,0.0002683345,0.00008525231,0.000073618576,0.000005230145,0.00032288447,0.00013092319,0.0000056331273],"category_scores_gemma":[0.00010785768,0.00012253945,0.000045529043,0.00035713371,0.00026404895,0.0001277063,0.0003089248,0.00034338,0.000001193662],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017155844,0.00010853178,0.001045209,0.000038089533,0.00006506898,1.0196335e-7,0.0004560633,0.000006022624,0.9979866,0.0001496746,0.000010221202,0.000117219424],"study_design_scores_gemma":[0.0003822123,0.0000039387987,0.012810244,0.00016477061,0.000064235406,0.000009727303,0.0001653323,0.000098049895,0.98557085,0.00018098539,0.00041824725,0.00013143805],"about_ca_topic_score_codex":0.00039663925,"about_ca_topic_score_gemma":0.0002868192,"teacher_disagreement_score":0.0124158235,"about_ca_system_score_codex":0.00017637493,"about_ca_system_score_gemma":0.000038101865,"threshold_uncertainty_score":0.49970138},"labels":[],"label_agreement":null},{"id":"W2083306660","doi":"10.1021/ef1007227","title":"Intrinsic Reaction Kinetics of Higher Alcohol Synthesis from Synthesis Gas over a Sulfided Alkali-Promoted Co−Rh−Mo Trimetallic Catalyst Supported on Multiwalled Carbon Nanotubes (MWCNTs)","year":2010,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":44,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Space velocity; Methanol; Chemistry; Alcohol; Kinetics; Alkali metal; Activation energy; Carbon fibers; Chemical engineering; Carbon dioxide; Materials science; Inorganic chemistry; Physical chemistry; Composite material; Organic chemistry; Composite number","score_opus":0.013180745003235511,"score_gpt":0.2406568570520949,"score_spread":0.2274761120488594,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2083306660","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9958658,0.00012413113,0.00003046853,0.000065784494,0.0006245598,0.00022799705,0.00015219291,0.00034577175,0.0025632568],"genre_scores_gemma":[0.9975398,0.000058934856,0.0003854464,0.00003404331,0.00045248828,0.0001462141,0.00026151803,0.00020428405,0.0009172749],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9964028,0.00011966805,0.0010938065,0.0008828631,0.0008045229,0.00069631025],"domain_scores_gemma":[0.99650276,0.0012784139,0.0005108735,0.0012663449,0.00013801114,0.00030362484],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003254503,0.0006783186,0.0011818205,0.0005487605,0.000062899664,0.00003073983,0.00056465453,0.0006511775,0.0005973227],"category_scores_gemma":[0.0014068602,0.00062596623,0.00048447627,0.0006388419,0.00013857837,0.00020902588,0.00013161881,0.00058797287,0.00004308149],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00025665906,0.00034507297,0.00006391516,0.000052595413,0.000658953,0.00003919984,0.00011638246,0.000018387092,0.9772945,0.00021203204,0.00002078046,0.020921487],"study_design_scores_gemma":[0.00114208,0.000057653313,0.0015408563,0.00016252576,0.00058711367,0.000015154486,0.000027067896,0.00054420467,0.9914441,0.000111071306,0.0037250933,0.0006430489],"about_ca_topic_score_codex":0.012512239,"about_ca_topic_score_gemma":0.0004469202,"teacher_disagreement_score":0.020278439,"about_ca_system_score_codex":0.0002612535,"about_ca_system_score_gemma":0.000055960387,"threshold_uncertainty_score":0.9996192},"labels":[],"label_agreement":null},{"id":"W2083312036","doi":"10.1016/j.biortech.2011.09.088","title":"Dry reforming of methane with CO2 on an electron-activated iron catalytic bed","year":2011,"lang":"en","type":"article","venue":"Bioresource Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Syngas; Methane; Carbon dioxide reforming; Carbon dioxide; Chemistry; Catalysis; Syngas to gasoline plus; Saturation (graph theory); Chemical engineering; Inorganic chemistry; Steam reforming; Organic chemistry; Hydrogen production","score_opus":0.01376733499548861,"score_gpt":0.23027628064461012,"score_spread":0.21650894564912151,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2083312036","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970556,0.000090617694,0.00013027029,0.000033454195,0.000025310792,0.00020672688,0.0000069824478,0.00073610514,0.0017149446],"genre_scores_gemma":[0.9984841,0.000004335485,0.0011818344,0.0000119592105,0.000028040404,0.000030693787,0.000036256937,0.000084218176,0.00013858153],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983888,0.00001682498,0.0003617997,0.0004292782,0.00022863274,0.0005746564],"domain_scores_gemma":[0.99869186,0.000035221365,0.00021919316,0.0008885241,0.000059145103,0.00010605195],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018483325,0.0002977299,0.00046636324,0.00068357,0.000035718414,0.0000022602192,0.0005227497,0.00040814411,0.000030510566],"category_scores_gemma":[0.00012513636,0.00023234455,0.00006930644,0.00085975893,0.00024373735,0.00010767475,0.0001156316,0.0005056628,0.000023588145],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027219357,0.00012924743,0.00093800377,0.0000511668,0.00007162204,0.000023152514,0.00041835458,0.000014728795,0.9894138,0.0014222744,6.518285e-7,0.0072447984],"study_design_scores_gemma":[0.00065835926,0.00085627084,0.00013787208,0.00007941864,0.00005905036,0.000048234728,0.00043851376,0.00017808794,0.9967494,0.000101424135,0.0003980902,0.00029528103],"about_ca_topic_score_codex":0.00058628013,"about_ca_topic_score_gemma":0.000058012272,"teacher_disagreement_score":0.007335591,"about_ca_system_score_codex":0.00020394154,"about_ca_system_score_gemma":0.000034651715,"threshold_uncertainty_score":0.9474736},"labels":[],"label_agreement":null},{"id":"W2083388200","doi":"10.1007/s11244-006-0015-8","title":"Catalytic Decomposition of Methane for Hydrogen Production","year":2006,"lang":"en","type":"article","venue":"Topics in Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":77,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Methane; Decomposition; Hydrogen; Hydrogen production; Carbon fibers; Cracking; Chemical engineering; Chemistry; Materials science; Physical chemistry; Organic chemistry; Composite number; Composite material","score_opus":0.012246057489020724,"score_gpt":0.27171554369246276,"score_spread":0.259469486203442,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2083388200","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9962616,0.00021508677,0.0020431774,0.00014330541,0.00011554962,0.00024322078,0.000014203257,0.000050897925,0.00091296516],"genre_scores_gemma":[0.9966827,0.0000045553625,0.0014600718,0.0000034946945,0.00025373918,0.000058340782,0.00044498238,0.000021429189,0.001070657],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989804,0.00000875621,0.0004133359,0.00023869918,0.00015746735,0.00020136351],"domain_scores_gemma":[0.99942464,0.000052399453,0.0001110142,0.0003282015,0.000057755526,0.00002601171],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00027527427,0.00011665288,0.00028125552,0.0002341445,0.00001609034,0.0000028426368,0.00013547143,0.000083526684,0.0000071456834],"category_scores_gemma":[0.000134617,0.00011877237,0.00014969427,0.0004241059,0.00002692566,0.00012020146,0.00003524621,0.00008621248,0.000005388201],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000036408503,0.00015522707,0.0013673233,0.00034747602,0.0000861704,0.0000029775106,0.00020177236,0.00944481,0.97318214,0.0016675545,0.000021265287,0.013486885],"study_design_scores_gemma":[0.00028408496,0.000012308845,0.00018218148,0.000028480465,0.00009819116,0.000008430052,0.000021030448,0.0034274228,0.993961,0.0012734706,0.0005739953,0.00012945542],"about_ca_topic_score_codex":0.00095641945,"about_ca_topic_score_gemma":0.00026400256,"teacher_disagreement_score":0.020778818,"about_ca_system_score_codex":0.00018399999,"about_ca_system_score_gemma":0.000016724263,"threshold_uncertainty_score":0.48433965},"labels":[],"label_agreement":null},{"id":"W2086037957","doi":"10.1016/j.apcata.2015.01.027","title":"Selectivity control of Cu promoted iron-based Fischer-Tropsch catalyst by tuning the oxidation state of Cu to mimic K","year":2015,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":30,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"Western Economic Diversification Canada; Natural Sciences and Engineering Research Council of Canada; University of Wyoming; Canadian Institutes of Health Research; University of Saskatchewan; National Research Council Canada; Canada Foundation for Innovation","keywords":"Syngas; Catalysis; Fischer–Tropsch process; Chemistry; Copper; Selectivity; XANES; Hydrocarbon; Inorganic chemistry; Oxidation state; Partial oxidation; Organic chemistry; Spectroscopy","score_opus":0.010130572907226264,"score_gpt":0.22581181535514852,"score_spread":0.21568124244792225,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2086037957","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9577665,0.00012252618,0.040945515,0.0001319077,0.000042407813,0.00057965395,0.00010296779,0.000085044594,0.00022352785],"genre_scores_gemma":[0.9977289,0.0000014806955,0.0010695544,0.000057669808,0.00007147118,0.00016525516,0.0006626062,0.000068764806,0.00017433162],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99757344,0.0000664105,0.00073017424,0.00048266616,0.0006648311,0.00048249643],"domain_scores_gemma":[0.9981627,0.0001316407,0.00041764663,0.00082600955,0.00022871622,0.000233285],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00089767826,0.00034340422,0.00071544724,0.0002179299,0.00006760415,0.000018325183,0.00049472955,0.000114809896,0.000011193276],"category_scores_gemma":[0.00021323567,0.00027385278,0.00021418542,0.0011181888,0.00008930162,0.000118107724,0.00011114531,0.00028131815,0.000019855315],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014927739,0.00011324764,0.00023194822,0.00006705154,0.00021363661,8.2272936e-7,0.00063485757,0.03296249,0.95971286,0.00004064703,0.00012367695,0.0057494896],"study_design_scores_gemma":[0.0013966074,0.00005334297,0.00010454457,0.000016471682,0.000266051,0.0000024883027,0.00007617963,0.06446006,0.93299747,0.000021506277,0.0003137219,0.00029158653],"about_ca_topic_score_codex":0.0022037416,"about_ca_topic_score_gemma":0.00016692537,"teacher_disagreement_score":0.03996242,"about_ca_system_score_codex":0.0002975206,"about_ca_system_score_gemma":0.00014931573,"threshold_uncertainty_score":0.9999714},"labels":[],"label_agreement":null},{"id":"W2086082904","doi":"10.1115/1.4026599","title":"Cascade Utilization of Fuel Gas Energy in Gas-to-Liquids Plant","year":2014,"lang":"en","type":"article","venue":"Journal of Engineering for Gas Turbines and Power","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Hatch (Canada)","funders":"","keywords":"Air preheater; Combined cycle; Natural gas; Waste management; Syngas; Fuel gas; Environmental science; Renewable natural gas; Exergy; Gas engine; Industrial gas; Producer gas; Gas to liquids; Electricity generation; Power station; Process engineering; Exhaust gas; Gas turbines; Engineering; Power (physics); Chemistry; Automotive engineering; Combustion; Mechanical engineering","score_opus":0.010613874691850282,"score_gpt":0.2301443514401986,"score_spread":0.2195304767483483,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2086082904","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96162343,0.00087162235,0.036669243,0.00011966768,0.0004848383,0.00007389735,0.000013519869,0.00002061369,0.00012318128],"genre_scores_gemma":[0.9977747,0.00012609425,0.0017430293,0.00002314377,0.00022399693,0.000004124081,0.000007746004,0.000039231516,0.000057898815],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989216,0.0000065985737,0.0005440906,0.00011200983,0.0001717596,0.00024396823],"domain_scores_gemma":[0.9993647,0.0001372741,0.00014792212,0.000119017364,0.00009465288,0.00013648898],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034162542,0.00016771365,0.00038951365,0.00034255756,0.000011052709,0.0000093405115,0.00012466472,0.00009847886,0.00000889336],"category_scores_gemma":[0.00035332257,0.00013896004,0.00012638659,0.00019117443,0.000009755928,0.00013071894,0.00003307494,0.00014382775,3.053603e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00039482024,0.00010111779,0.00048727734,0.00090286334,0.0001604345,0.00002348159,0.0011828617,0.119979404,0.8613578,0.008270691,0.00023470489,0.00690456],"study_design_scores_gemma":[0.0031266802,0.0009542153,0.0010178672,0.0014586909,0.00012390008,0.00070903613,0.00010887666,0.2431753,0.63466954,0.0004557308,0.1134775,0.0007226831],"about_ca_topic_score_codex":0.00003125869,"about_ca_topic_score_gemma":0.0000092033715,"teacher_disagreement_score":0.22668827,"about_ca_system_score_codex":0.000056339748,"about_ca_system_score_gemma":0.000013929655,"threshold_uncertainty_score":0.5666626},"labels":[],"label_agreement":null},{"id":"W2086308243","doi":"10.1021/ie071547q","title":"Kinetics and Reactor Modeling of a High Temperature Water−Gas Shift Reaction (WGSR) for Hydrogen Production in a Packed Bed Tubular Reactor (PBTR)","year":2008,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Water-gas shift reaction; Hydrogen production; Packed bed; Kinetics; Chemistry; Hydrogen; Chemical engineering; Catalysis; Chemical kinetics; Chromatography; Organic chemistry","score_opus":0.06081098517769412,"score_gpt":0.28545544312645993,"score_spread":0.2246444579487658,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2086308243","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9987502,0.000096954085,0.000009542774,0.00018851768,0.00015895121,0.00062176574,0.000034089713,0.00012217584,0.000017774464],"genre_scores_gemma":[0.9981987,0.000051061383,0.000085223604,7.545225e-7,0.0010851324,0.00013940218,0.00022914236,0.0001008349,0.0001097903],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972734,0.00002953933,0.0006675618,0.00059951894,0.00064655585,0.0007834214],"domain_scores_gemma":[0.99881065,0.0001776639,0.00007084985,0.0005064388,0.0002267172,0.00020765165],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0009320683,0.00032312152,0.000529679,0.00028248027,0.00006371475,0.000019207833,0.0002561408,0.00068991253,0.000008397591],"category_scores_gemma":[0.002136705,0.00030072054,0.00010999085,0.0005626306,0.00007893985,0.00022662774,0.00013914808,0.0014555464,0.0000015671678],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024505574,0.000081359365,0.000046075438,0.00036873657,0.000059691854,0.00001925378,0.00042750215,0.0066213575,0.9919322,0.0000064857086,0.000009573093,0.0001826786],"study_design_scores_gemma":[0.0013960165,0.000061143764,0.000008708871,0.00030847522,0.000022974064,0.0000865668,0.00006764472,0.014188177,0.98327655,0.000037252856,0.00024590295,0.00030061742],"about_ca_topic_score_codex":0.0004266795,"about_ca_topic_score_gemma":0.000003802515,"teacher_disagreement_score":0.00865571,"about_ca_system_score_codex":0.00049680856,"about_ca_system_score_gemma":0.00007827085,"threshold_uncertainty_score":0.9999445},"labels":[],"label_agreement":null},{"id":"W2087067515","doi":"10.4028/www.scientific.net/amr.324.197","title":"From Nanoparticles to Process: An Aberration-Corrected TEM Study of Fischer-Tropsch Catalysts at Various Steps of the Process","year":2011,"lang":"en","type":"article","venue":"Advanced materials research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University; Université de Sherbrooke","funders":"","keywords":"Carbide; Materials science; Nanoparticle; Transmission electron microscopy; Amorphous solid; Amorphous carbon; Fischer–Tropsch process; High-resolution transmission electron microscopy; Microstructure; Chemical engineering; Carbon fibers; Nanostructure; Catalysis; Nanotechnology; Particle (ecology); Metallurgy; Crystallography; Composite material; Composite number; Chemistry; Organic chemistry; Selectivity","score_opus":0.052446218052395896,"score_gpt":0.35185426590516405,"score_spread":0.29940804785276814,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2087067515","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99835694,0.00002713865,0.000012750472,0.000011219168,0.00017009884,0.001149711,0.000066647015,0.00006420821,0.00014131391],"genre_scores_gemma":[0.9991356,0.000002336124,0.00025074795,0.0000024481305,0.00005768637,0.0003056786,0.000029191813,0.00005549192,0.00016083421],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974019,0.00019110068,0.00065220596,0.0004431225,0.0008484297,0.00046325335],"domain_scores_gemma":[0.9981824,0.0001307322,0.00019050586,0.0008438368,0.00051055494,0.00014198273],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006749462,0.00019208119,0.00043182226,0.0001457023,0.00012162406,0.000014772747,0.0007636428,0.00008992916,0.00018178538],"category_scores_gemma":[0.00074492866,0.00013842764,0.00003751524,0.000815468,0.000084400395,0.00034837998,0.00036778048,0.00017799939,0.000026568303],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00047755093,0.00047195947,0.00100458,0.00019325061,0.00005301776,0.0000024668789,0.019673241,0.0003176979,0.97716385,0.000008774202,0.0000024101012,0.00063122663],"study_design_scores_gemma":[0.00064920296,0.0003187706,0.0026505482,0.00011622629,0.000025014058,0.0000020909288,0.00449867,0.000066117485,0.9912576,0.00025212095,0.00000979818,0.00015385327],"about_ca_topic_score_codex":0.0028322518,"about_ca_topic_score_gemma":0.0011691432,"teacher_disagreement_score":0.015174571,"about_ca_system_score_codex":0.00012421513,"about_ca_system_score_gemma":0.000079940066,"threshold_uncertainty_score":0.5644915},"labels":[],"label_agreement":null},{"id":"W2095969913","doi":"10.1002/cjce.21773","title":"Simplified kinetic model for steam reforming of ethanol on a Ni/Al<sub>2</sub>O<sub>3</sub> catalyst","year":2013,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":57,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Kinetic energy; Thermodynamics; Chemistry; Steam reforming; Methane; Activation energy; Order of reaction; Adsorption; Reaction rate; Nickel; Physical chemistry; Hydrogen; Kinetics; Reaction rate constant; Hydrogen production; Organic chemistry; Physics","score_opus":0.012371695154474826,"score_gpt":0.206150180484366,"score_spread":0.19377848532989117,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2095969913","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99499387,0.00027486013,0.00346862,0.0003783719,0.0002799626,0.00042679138,0.00004547435,0.000054016236,0.0000780657],"genre_scores_gemma":[0.99892485,0.000010313914,0.000375713,0.000119837336,0.00032084325,0.0000519678,0.00002300921,0.00016016328,0.000013323809],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9969868,0.00001445631,0.0011578106,0.00030316098,0.0005271466,0.0010106477],"domain_scores_gemma":[0.9973872,0.0003269286,0.0004258401,0.0005814906,0.00034791636,0.0009306376],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005682782,0.00048752193,0.0008007258,0.0004993465,0.00009274961,0.000040538103,0.0008219424,0.00030365927,0.000006361454],"category_scores_gemma":[0.0010246828,0.00039290206,0.00048055133,0.00044665358,0.00010495086,0.00031933165,0.00007006313,0.0010842204,0.000014556006],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000030274356,0.000015701911,0.0000024987528,0.00019062155,0.00014452498,0.000010783409,0.0003477784,0.08701751,0.90753776,0.00016008732,0.00010011757,0.0044423444],"study_design_scores_gemma":[0.0006507127,0.00005143781,0.0000054069224,0.00040216703,0.0001002138,0.00015016425,0.000028514845,0.20307924,0.7949445,0.00015370552,0.00008184947,0.00035209197],"about_ca_topic_score_codex":0.0006784691,"about_ca_topic_score_gemma":0.00016730672,"teacher_disagreement_score":0.11606173,"about_ca_system_score_codex":0.0009631152,"about_ca_system_score_gemma":0.0003872281,"threshold_uncertainty_score":0.9998523},"labels":[],"label_agreement":null},{"id":"W2097658184","doi":"10.3906/kim-0809-33","title":"Partial regeneration of Ni-based catalysts for hydrogen production via methane cracking part II: modeling and optimization","year":2009,"lang":"en","type":"article","venue":"TURKISH JOURNAL OF CHEMISTRY","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Chemistry; Catalysis; Methane; Carbon monoxide; Chemical engineering; Hydrogen; Reaction rate constant; Reaction rate; Thermodynamics; Kinetics; Organic chemistry","score_opus":0.014135581007624633,"score_gpt":0.2426216425801184,"score_spread":0.22848606157249376,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2097658184","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92267567,0.0005801896,0.07621733,0.0002358471,0.00011698286,0.00010850681,0.0000044955063,0.00002393101,0.000037057187],"genre_scores_gemma":[0.99345726,0.000027273112,0.005607609,0.00001093079,0.0007356559,0.000004008461,0.00007635764,0.000021758751,0.000059166672],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99867827,0.000010518293,0.0006776874,0.00017558999,0.0002757345,0.00018218983],"domain_scores_gemma":[0.9988999,0.000023650784,0.00050542376,0.00016290968,0.0003134202,0.00009472586],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005267347,0.00015286294,0.00032610653,0.0000577759,0.00009208924,0.000013910862,0.000108771506,0.0001267527,0.0000054156303],"category_scores_gemma":[0.00041167962,0.00014721451,0.00012882707,0.00013953866,0.000020682039,0.00028293562,0.000016071872,0.00018023247,8.0476106e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007454192,0.000028460136,0.000004284476,0.00008631528,0.000026466629,0.0000013198253,0.00004561615,0.42007816,0.5778315,7.8156893e-7,0.000008420283,0.0018141315],"study_design_scores_gemma":[0.0004517487,0.000034546047,2.2766095e-7,0.00012423331,0.00009661601,0.000103186554,0.000013197688,0.3317085,0.6672973,0.00004714222,0.000027294138,0.000096034026],"about_ca_topic_score_codex":0.0000056248005,"about_ca_topic_score_gemma":3.9673773e-7,"teacher_disagreement_score":0.089465775,"about_ca_system_score_codex":0.00009753769,"about_ca_system_score_gemma":0.00006240674,"threshold_uncertainty_score":0.6003234},"labels":[],"label_agreement":null},{"id":"W2097727844","doi":"10.1002/cjce.5450830607","title":"Dry‐Reforming of Ethanol in the Presence of a 316 Stainless Steel Catalyst","year":2005,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":46,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Carbon dioxide reforming; Biomass (ecology); Yield (engineering); Chemical engineering; Hydrogen; Carbon fibers; Catalytic reforming; Natural gas; Materials science; Syngas to gasoline plus; Fossil fuel; Hydrogen production; Chemistry; Syngas; Waste management; Steam reforming; Organic chemistry; Metallurgy; Engineering; Composite material","score_opus":0.009898966753772819,"score_gpt":0.2144314098524544,"score_spread":0.20453244309868157,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2097727844","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99802816,0.0008264777,0.00030360997,0.00038158984,0.0000900564,0.00012393876,0.000012255663,0.00000811694,0.00022576857],"genre_scores_gemma":[0.9993535,0.000004304266,0.00036035388,0.000019404803,0.00020091522,0.0000046092005,0.0000024997546,0.00003124884,0.000023123332],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981154,0.000022498498,0.0008478847,0.000110434186,0.0004425772,0.00046116297],"domain_scores_gemma":[0.9985963,0.00036606393,0.00029369735,0.00037610283,0.00013653004,0.00023130298],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010530084,0.00019404455,0.00043928841,0.00030079496,0.000028234179,0.000012253047,0.0010226137,0.0001236885,0.00001571361],"category_scores_gemma":[0.000840149,0.0001234766,0.00020322092,0.0005472882,0.00011469156,0.00022218826,0.0000452561,0.00077646325,0.000001338513],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019001307,0.000019311407,0.00022881095,0.0002038731,0.00007825705,0.000032944678,0.0042587267,0.05849296,0.9329027,0.00069688825,0.000008461103,0.0030580906],"study_design_scores_gemma":[0.00042513132,0.000018999215,0.000081939885,0.00041078046,0.000046640573,0.00014665496,0.00026528846,0.017682865,0.980157,0.00003623916,0.0005676842,0.00016074916],"about_ca_topic_score_codex":0.0038259109,"about_ca_topic_score_gemma":0.0011139434,"teacher_disagreement_score":0.047254354,"about_ca_system_score_codex":0.00038836827,"about_ca_system_score_gemma":0.00029961616,"threshold_uncertainty_score":0.5783658},"labels":[],"label_agreement":null},{"id":"W2097915338","doi":"10.3389/fchem.2014.00081","title":"Review on dry reforming of methane, a potentially more environmentally-friendly approach to the increasing natural gas exploitation","year":2014,"lang":"en","type":"review","venue":"Frontiers in Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":526,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Carbon dioxide reforming; Methane; Syngas; Syngas to gasoline plus; Fossil fuel; Natural gas; Environmental science; Methane reformer; Renewable energy; Environmentally friendly; Waste management; Carbon footprint; Carbon dioxide; Steam reforming; Biomass (ecology); Greenhouse gas; Chemistry; Hydrogen production; Engineering; Hydrogen; Ecology","score_opus":0.013110374545547272,"score_gpt":0.2655171495261466,"score_spread":0.2524067749805993,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2097915338","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00021868075,0.9944231,0.001981266,0.000027129783,0.0003497333,0.0009700292,0.000036374917,0.000057347504,0.0019363364],"genre_scores_gemma":[0.00012444131,0.9875335,0.010304076,0.00007787827,0.0002913915,0.00033853608,0.000749195,0.00016227964,0.0004186786],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99651796,0.00013152418,0.0013660295,0.00076975237,0.000659047,0.0005556928],"domain_scores_gemma":[0.997754,0.00016322637,0.0007537804,0.0011437761,0.000029939329,0.00015527109],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013873118,0.00072943716,0.0023646092,0.00018158469,0.000049245566,0.000013299242,0.0011004588,0.00042969943,0.000012812403],"category_scores_gemma":[0.0008357571,0.0005234942,0.00078573567,0.00057552557,0.00009663303,0.0001223081,0.00032250586,0.0012723224,0.000010318799],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002824627,0.00007469741,0.0000019666427,0.11460951,0.00025138046,0.00000641478,0.00015987614,0.000084849795,0.0017757735,0.0000042008755,0.00041141157,0.88259166],"study_design_scores_gemma":[0.00036775085,0.000019993466,5.6594934e-7,0.10774155,0.0010752847,0.00012104806,0.0004077976,0.00047285744,0.009784672,0.000008138055,0.8790032,0.0009971292],"about_ca_topic_score_codex":0.00005227687,"about_ca_topic_score_gemma":7.6510213e-7,"teacher_disagreement_score":0.88159454,"about_ca_system_score_codex":0.0011029707,"about_ca_system_score_gemma":0.00009287405,"threshold_uncertainty_score":0.99972165},"labels":[],"label_agreement":null},{"id":"W2101442387","doi":"10.1002/0471238961.fiscdekl.a01","title":"Fischer–Tropsch Process","year":2013,"lang":"en","type":"other","venue":"Kirk-Othmer Encyclopedia of Chemical Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":50,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Fischer–Tropsch process; Syngas; Gas to liquids; Syngas to gasoline plus; Oxygenate; Refining (metallurgy); Liquefaction; Catalysis; Coal liquefaction; Chemistry; Chemical engineering; Process engineering; Waste management; Organic chemistry; Steam reforming; Engineering; Hydrogen production; Selectivity","score_opus":0.005027316509376621,"score_gpt":0.23621502842572556,"score_spread":0.23118771191634893,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2101442387","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.023048338,0.0031530014,0.00030363488,0.000358104,0.00046289703,0.00074206025,0.00007614716,0.0026031157,0.9692527],"genre_scores_gemma":[0.03996619,0.00120997,0.008390075,0.00007242078,0.0018860032,0.0009181179,0.00045464016,0.0034599686,0.9436426],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.99688554,0.000012437796,0.0008386659,0.0008639952,0.0005176766,0.00088171597],"domain_scores_gemma":[0.9978404,0.00007615185,0.0005728771,0.0011894455,0.00012382043,0.00019728446],"candidate_categories":["metaepi_narrow","research_integrity","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.000091125265,0.00076520024,0.0013852604,0.0009429091,0.000015927335,0.000006664849,0.0012892615,0.0026631376,0.0028027268],"category_scores_gemma":[0.0005916245,0.0007044514,0.00031133916,0.0010792244,0.000532674,0.000087189335,0.0004206405,0.0013641549,0.00068815605],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003759328,0.0005075853,0.00085246225,0.003862916,0.0012517435,0.00007555693,0.00019455844,0.00000500837,0.7520897,0.00630173,0.16211893,0.072702244],"study_design_scores_gemma":[0.0005908521,0.000029051267,9.3200276e-7,0.00043000697,0.00015100885,0.00006214112,0.000043457323,0.000076009914,0.47374502,0.0010358772,0.5229733,0.00086233736],"about_ca_topic_score_codex":0.0001465382,"about_ca_topic_score_gemma":0.0000056551517,"teacher_disagreement_score":0.3608544,"about_ca_system_score_codex":0.00014285547,"about_ca_system_score_gemma":0.000093714756,"threshold_uncertainty_score":0.9995407},"labels":[],"label_agreement":null},{"id":"W2103296909","doi":"10.1016/j.cherd.2015.05.006","title":"Dynamic simulation and control of an integrated gasifier/reformer system. Part I: Agile case design and control","year":2015,"lang":"en","type":"article","venue":"Process Safety and Environmental Protection","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Wood gas generator; Syngas; Process engineering; Natural gas; Engineering; Automotive engineering; Environmental science; Waste management; Coal; Chemistry","score_opus":0.013956643429596011,"score_gpt":0.2233338832345812,"score_spread":0.20937723980498518,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2103296909","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.48545334,0.00026626704,0.5135209,0.000009428247,0.000029397619,0.00062412757,0.00003415367,0.000047572645,0.00001479179],"genre_scores_gemma":[0.99967974,0.000016599412,0.00014357147,0.000004738178,0.000019308636,0.0000646102,0.000031538973,0.000021389737,0.000018498153],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9991474,0.000051665575,0.00027941022,0.00023741275,0.00013382194,0.00015028246],"domain_scores_gemma":[0.99960226,0.000034621396,0.00012480783,0.00008978607,0.000014191493,0.00013435032],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00036972205,0.00016004895,0.0002335036,0.000055073953,0.00009382874,0.000010901797,0.000027104565,0.00011557335,0.0000043111727],"category_scores_gemma":[0.00004160033,0.00013487265,0.000018659657,0.00005782386,0.00008315623,0.00040498257,0.000015771824,0.00014620218,0.000001106689],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.003619997,0.00015675447,0.00032203272,0.0013605576,0.00016777817,0.000055604032,0.0015823621,0.69333375,0.22764474,0.000017795452,8.019546e-8,0.071738556],"study_design_scores_gemma":[0.0023587686,0.00021657012,0.000059634964,0.00007364873,0.00007747678,0.00066469057,0.0015772391,0.98038507,0.014353639,0.000031609045,0.00004302132,0.00015862078],"about_ca_topic_score_codex":0.00013584504,"about_ca_topic_score_gemma":0.000006958763,"teacher_disagreement_score":0.5142264,"about_ca_system_score_codex":0.0001705719,"about_ca_system_score_gemma":0.000007696366,"threshold_uncertainty_score":0.5499947},"labels":[],"label_agreement":null},{"id":"W2106962368","doi":"10.1002/ceat.201500105","title":"Kinetics and Reactor Modeling of the Steam Reforming of Methanol over a Mn‐Promoted Cu/Al Catalyst","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Methanol; Catalysis; Chemistry; Steam reforming; Mass transfer; Kinetics; Chemical engineering; Packed bed; Thermodynamics; Chemical kinetics; Adsorption; Physical chemistry; Chromatography; Organic chemistry; Hydrogen production","score_opus":0.013355551639594579,"score_gpt":0.22702917281542914,"score_spread":0.21367362117583455,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2106962368","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.994647,0.00050196075,0.0040452685,0.000114429036,0.00012923822,0.00016559541,0.00001812647,0.00028539638,0.00009294518],"genre_scores_gemma":[0.99758196,0.00001041152,0.0022412145,0.0000066374755,0.00004035175,0.000017593473,0.000013089217,0.00006869592,0.000020045014],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983106,0.0000060604657,0.0006248782,0.00032646224,0.00031806072,0.0004138951],"domain_scores_gemma":[0.9987904,0.000063109925,0.0001721438,0.00071242085,0.00013344048,0.00012847886],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00019598227,0.00028597534,0.0005741346,0.0002850634,0.000011946431,0.0000030721103,0.0005300044,0.00043325947,0.0000028353782],"category_scores_gemma":[0.0013568394,0.0002275068,0.00013049862,0.0008012609,0.00015152241,0.00009635382,0.00056245027,0.00060967426,0.0000011079884],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012663232,0.00003648444,0.000045657314,0.00016714908,0.00006884052,0.000002281588,0.00013195166,0.0047396817,0.993408,0.00032447564,0.0000036561903,0.0010591634],"study_design_scores_gemma":[0.000474706,0.000028353326,0.0000027699307,0.00017109957,0.000056321045,0.00006380055,0.00005889467,0.19060123,0.8079938,0.0001099712,0.00024545868,0.0001935838],"about_ca_topic_score_codex":0.00009176488,"about_ca_topic_score_gemma":0.000001723844,"teacher_disagreement_score":0.18586154,"about_ca_system_score_codex":0.00021753433,"about_ca_system_score_gemma":0.000030395418,"threshold_uncertainty_score":0.9277458},"labels":[],"label_agreement":null},{"id":"W2108861055","doi":"10.1007/978-3-319-07896-0_9","title":"Thermodynamic Analysis of a Cycle Intergrating a Solid-Oxide Fuel Cell and Micro Gas Turbine with Biomass Gasification","year":2014,"lang":"en","type":"book-chapter","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Gas turbines; Biomass (ecology); Solid oxide fuel cell; Syngas; Biomass gasification; Fuel cells; Combined cycle; Waste management; Process engineering; Environmental science; Nuclear engineering; Chemical engineering; Chemistry; Biofuel; Engineering; Mechanical engineering; Hydrogen; Organic chemistry; Biology","score_opus":0.006363668378893858,"score_gpt":0.21116817148037192,"score_spread":0.20480450310147807,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2108861055","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6490557,0.0011352411,0.040752314,0.000059414746,0.00006333043,0.0005606745,0.000112205686,0.00032875533,0.30793232],"genre_scores_gemma":[0.948428,0.00005979729,0.0018935468,0.000011533234,0.000037167614,0.0000105850795,0.00029897701,0.00011804519,0.049142357],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99841726,0.000008574644,0.00059677137,0.0004858427,0.00024676984,0.00024478522],"domain_scores_gemma":[0.99861574,0.000119087075,0.00048459086,0.00057473383,0.000105840496,0.00009998645],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001826858,0.00042106275,0.0008819685,0.00067296973,0.000025275747,0.000017163142,0.00020963367,0.00026339863,0.0000938416],"category_scores_gemma":[0.00002369751,0.00032194526,0.0002827832,0.0001834409,0.00008584979,0.000059398404,0.00011097982,0.00026522923,0.000008650968],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000036525595,0.000014711103,0.000040555326,0.0006880354,0.0014360297,0.0000046644973,0.00019952934,0.00021422097,0.99377686,0.0021001613,0.0000018195134,0.0014869076],"study_design_scores_gemma":[0.0012534087,0.00015693258,0.00011779345,0.00101976,0.007552339,0.00005913768,0.00013588951,0.3548754,0.6312899,0.00089539186,0.0010464729,0.0015976146],"about_ca_topic_score_codex":0.0003413631,"about_ca_topic_score_gemma":0.00037293584,"teacher_disagreement_score":0.36248696,"about_ca_system_score_codex":0.00013148063,"about_ca_system_score_gemma":0.000020423862,"threshold_uncertainty_score":0.9999233},"labels":[],"label_agreement":null},{"id":"W2109344869","doi":"10.1016/j.jpowsour.2013.08.106","title":"Single-stage temperature-controllable water gas shift reactor with catalytic nickel plates","year":2013,"lang":"en","type":"article","venue":"Journal of Power Sources","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Ministry of Knowledge Economy","keywords":"Exothermic reaction; Space velocity; Water-gas shift reaction; Coolant; Catalysis; Chemistry; Heat exchanger; Volumetric flow rate; Thermodynamics; Materials science; Nuclear engineering; Chemical engineering; Selectivity; Organic chemistry","score_opus":0.006564859963075631,"score_gpt":0.1936315015907576,"score_spread":0.18706664162768197,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2109344869","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99751204,0.00051864644,0.000048649774,0.00043907372,0.00021763344,0.00012635125,0.0000046812693,0.00004769982,0.001085207],"genre_scores_gemma":[0.9965281,0.0000059642134,0.0002753347,0.00006491801,0.00027287044,0.00000414423,0.0000071518693,0.0000647307,0.0027767716],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99822354,0.000019534456,0.0005927148,0.00018362042,0.00047157408,0.0005089847],"domain_scores_gemma":[0.99887025,0.000117353055,0.00030078873,0.00028471742,0.0001779346,0.00024896374],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002939961,0.00028249976,0.00053087535,0.00021099961,0.000057067824,0.00013001235,0.00034779575,0.00014267201,0.00048865925],"category_scores_gemma":[0.00011699801,0.00015279753,0.00020000426,0.00013815502,0.000061733546,0.00075947604,0.00006225512,0.0005473221,0.00014890872],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010510472,0.000072633586,0.00063669943,0.00004873844,0.0002500239,0.000077347504,0.0022982797,0.00036928427,0.995798,0.000013398067,0.00016194487,0.00016857474],"study_design_scores_gemma":[0.0013734873,0.00027569255,0.00013350845,0.0001813273,0.00009302582,0.00030631412,0.0006575419,0.00016275476,0.9847644,0.000045714212,0.011697341,0.00030888282],"about_ca_topic_score_codex":0.00015060355,"about_ca_topic_score_gemma":0.00001374166,"teacher_disagreement_score":0.011535396,"about_ca_system_score_codex":0.00014183352,"about_ca_system_score_gemma":0.00003372662,"threshold_uncertainty_score":0.6230902},"labels":[],"label_agreement":null},{"id":"W2121142228","doi":"10.1002/cjce.22370","title":"Kinetics of reverse water‐gas shift reaction over Pt/Al<sub>2</sub>O<sub>3</sub> catalyst","year":2015,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":25,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"University Grants Commission","keywords":"Water-gas shift reaction; Catalysis; Methanol; Space velocity; Chemistry; Redox; Chemical kinetics; Reaction rate; Carbon dioxide; Kinetics; Water gas; Syngas; Chemical engineering; Inorganic chemistry; Selectivity; Organic chemistry","score_opus":0.01079305853865413,"score_gpt":0.19742820610000472,"score_spread":0.18663514756135058,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2121142228","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978459,0.00028258623,0.00047962277,0.00049907126,0.0006148857,0.00012156439,0.000022517708,0.000046659712,0.000087231514],"genre_scores_gemma":[0.9991193,0.000012640087,0.0001344438,0.000063423286,0.0005193377,0.000004581873,0.00003270849,0.00010783282,0.0000057687857],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99740267,0.000022530483,0.00094634737,0.00023101643,0.00062012055,0.00077733473],"domain_scores_gemma":[0.99766415,0.000120902,0.0002921764,0.0004927115,0.00025843462,0.0011716447],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00066128856,0.0003867326,0.0006216542,0.00039476383,0.000038119077,0.0000364967,0.0005778889,0.00026799212,0.000007556379],"category_scores_gemma":[0.000802275,0.0002976739,0.00033606298,0.00041225555,0.00011250174,0.00033841142,0.00007988218,0.0010662953,0.000022520384],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003379762,0.000015929229,0.0000132628875,0.00009753427,0.00013355455,0.00007970244,0.0006709921,0.009384473,0.9884175,0.00006223735,0.00020929766,0.0008816901],"study_design_scores_gemma":[0.00068673695,0.00004274865,0.000023276232,0.00028647523,0.00015100461,0.000459013,0.000034524677,0.0031710665,0.9926731,0.00008986397,0.0020271444,0.00035502392],"about_ca_topic_score_codex":0.0011156296,"about_ca_topic_score_gemma":0.00033121277,"teacher_disagreement_score":0.0062134066,"about_ca_system_score_codex":0.00118885,"about_ca_system_score_gemma":0.000211447,"threshold_uncertainty_score":0.99994755},"labels":[],"label_agreement":null},{"id":"W2125012649","doi":"10.1007/s10562-007-9194-6","title":"Fischer–Tropsch Synthesis: Morphology, Phase Transformation and Particle Size Growth of Nano-scale Particles","year":2007,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":70,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"U.S. Department of Energy","keywords":"Fischer–Tropsch process; Catalysis; Syngas; Chemistry; Nucleation; Magnetite; Particle size; Chemical engineering; Particle (ecology); Hematite; Phase (matter); Inorganic chemistry; Mineralogy; Metallurgy; Materials science; Physical chemistry; Organic chemistry; Selectivity","score_opus":0.009183202781477108,"score_gpt":0.23577778002898914,"score_spread":0.22659457724751203,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2125012649","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99169403,0.0001304828,0.0070209415,0.0008271642,0.00004327462,0.000112665,0.000014422413,0.00008679863,0.00007020365],"genre_scores_gemma":[0.9989066,0.000011179039,0.0007942174,0.00015898528,0.0000483584,0.000021117794,0.00002011569,0.000027081343,0.0000123196505],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99860084,0.00002475326,0.0005187854,0.00024179854,0.00021896268,0.00039488447],"domain_scores_gemma":[0.9990487,0.0003638655,0.00012297712,0.000277906,0.000040516392,0.00014603267],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00058979605,0.00017639277,0.00034175965,0.000090136986,0.000055563374,0.000011080248,0.00015244789,0.000086278924,0.000035712357],"category_scores_gemma":[0.00032096717,0.00016216382,0.00014938989,0.0003767416,0.00012538367,0.00034152617,0.000035050714,0.00013339169,0.000015854375],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000066449735,0.000080630045,0.000973891,0.00009022078,0.000101219135,0.000009415985,0.0010449644,0.000031931995,0.9911937,0.00007803943,0.000014544054,0.006314994],"study_design_scores_gemma":[0.00077598233,0.000019772066,0.00063955697,0.000028545774,0.00022789558,0.000020962556,0.000337195,0.0012378684,0.99642533,0.000012812687,0.00008920095,0.0001848874],"about_ca_topic_score_codex":0.0001315071,"about_ca_topic_score_gemma":0.000018102353,"teacher_disagreement_score":0.007212578,"about_ca_system_score_codex":0.00006252002,"about_ca_system_score_gemma":0.000006645331,"threshold_uncertainty_score":0.66128486},"labels":[],"label_agreement":null},{"id":"W2128036416","doi":"10.1002/aic.11242","title":"Multicomponent multicompartment model for Fischer–Tropsch SCBR","year":2007,"lang":"en","type":"article","venue":"AIChE Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Fischer–Tropsch process; Syngas; Chemistry; Water gas; Thermodynamics; Mass transfer; Gas to liquids; Water-gas shift reaction; Oxygenate; Bubble column reactor; Bubble; Chemical engineering; Catalysis; Mechanics; Organic chemistry; Chromatography; Physics; Engineering","score_opus":0.03672438479806741,"score_gpt":0.30703257419889135,"score_spread":0.27030818940082396,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2128036416","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5580908,0.00023581083,0.44063148,0.00015288062,0.00028989007,0.00019352403,0.00000635046,0.000075427335,0.0003238504],"genre_scores_gemma":[0.9473788,0.000013970293,0.05086009,0.00009080925,0.0005759887,0.000012258535,0.0000141139935,0.00005879995,0.0009951859],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99815774,0.000010840744,0.00059833704,0.00020035767,0.00036708734,0.0006656561],"domain_scores_gemma":[0.99894243,0.0001751999,0.00017100431,0.00023962164,0.0001225726,0.00034917478],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010818843,0.00022331538,0.00030335414,0.00014406585,0.00015654898,0.00002965561,0.0002656466,0.000115851326,0.00003523274],"category_scores_gemma":[0.0001926435,0.00018337963,0.00027955743,0.000099665696,0.000025393996,0.00019345146,0.00007133585,0.00050897175,0.0000362722],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019338922,0.00021395957,0.00030806984,0.00006050098,0.00019646008,0.000028281596,0.0007404017,0.042178746,0.94304246,0.00043736325,0.0002862303,0.012314112],"study_design_scores_gemma":[0.0017914105,0.00003208434,0.0001737133,0.00004676906,0.000072271694,0.00016735031,0.00009604528,0.7298087,0.26262942,0.00015730725,0.0047721406,0.0002527758],"about_ca_topic_score_codex":0.000012264918,"about_ca_topic_score_gemma":0.000010241548,"teacher_disagreement_score":0.68762994,"about_ca_system_score_codex":0.00038691907,"about_ca_system_score_gemma":0.000037903632,"threshold_uncertainty_score":0.7478004},"labels":[],"label_agreement":null},{"id":"W2128817243","doi":"10.1002/ceat.201200029","title":"Simulation of a Compact Multichannel Membrane Reactor for the Production of Pure Hydrogen via Steam Methane Reforming","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":23,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Fonds de recherche du Québec – Nature et technologies; Natural Sciences and Engineering Research Council of Canada","keywords":"Steam reforming; Membrane reactor; Isothermal process; Hydrogen production; Methane; Methane reformer; Hydrogen; Chemistry; Combustion; Catalysis; Plug flow reactor model; Chemical engineering; Nuclear engineering; Syngas; Thermodynamics; Materials science; Waste management; Continuous stirred-tank reactor; Engineering; Organic chemistry; Physical chemistry; Physics","score_opus":0.014594544571841958,"score_gpt":0.24973616788175484,"score_spread":0.2351416233099129,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2128817243","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97320545,0.00094225403,0.024546383,0.00012166063,0.00029601046,0.000517601,0.000011642175,0.00034866924,0.000010303621],"genre_scores_gemma":[0.9983467,0.000008167654,0.0012498819,0.000002221012,0.00021891539,0.000056848072,0.000024763549,0.000068188565,0.000024355151],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99849266,0.0000050834983,0.00056640053,0.00023535716,0.00020982216,0.0004906615],"domain_scores_gemma":[0.9985106,0.0005040234,0.0002304681,0.00054561056,0.00012998696,0.000079305726],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00039031327,0.00025135995,0.0005120538,0.00027452884,0.000020650617,0.0000013668429,0.00034102376,0.00036937743,0.0000060254015],"category_scores_gemma":[0.0027308222,0.00019459084,0.00018687484,0.00059561234,0.00008906374,0.00017399107,0.00009379421,0.00037133004,0.0000020069815],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000036213038,0.000058583955,0.000020114969,0.00036953783,0.00012905929,1.6630192e-7,0.00018131013,0.11874787,0.8775592,0.0001324624,8.5036055e-7,0.0027646625],"study_design_scores_gemma":[0.00025227768,0.000021033717,0.0000028785585,0.000089742134,0.00009641148,0.00001841079,0.00006024581,0.25308794,0.7459335,0.000021857944,0.0002685552,0.000147191],"about_ca_topic_score_codex":0.000020751371,"about_ca_topic_score_gemma":3.7679914e-7,"teacher_disagreement_score":0.13434008,"about_ca_system_score_codex":0.00017889182,"about_ca_system_score_gemma":0.000012490383,"threshold_uncertainty_score":0.7935184},"labels":[],"label_agreement":null},{"id":"W2129248796","doi":"10.1016/j.jpowsour.2005.09.019","title":"Steam reforming of methane over unsupported nickel catalysts","year":2005,"lang":"en","type":"article","venue":"Journal of Power Sources","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":109,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Methane; Catalysis; Steam reforming; Methane reformer; Nickel; Coke; Syngas; Hydrogen; Carbon dioxide reforming; Chemical engineering; Materials science; Chemistry; Inorganic chemistry; Hydrogen production; Metallurgy; Organic chemistry","score_opus":0.00938002073757146,"score_gpt":0.25420059954884167,"score_spread":0.2448205788112702,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2129248796","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99617904,0.0015932588,0.00025765246,0.00011348096,0.0002766863,0.000059384303,0.000007935202,0.000030875843,0.0014816964],"genre_scores_gemma":[0.99750173,0.000043390082,0.0007944086,0.000033630848,0.00047024054,9.1653527e-7,0.0000045515744,0.000046749716,0.0011043943],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976037,0.000027092587,0.0011658517,0.00015289566,0.00068702985,0.0003633897],"domain_scores_gemma":[0.99813235,0.00011724612,0.0010035476,0.00032801734,0.00020496096,0.00021389831],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008431463,0.00022709591,0.0006419095,0.00040766617,0.000026062055,0.00000839771,0.0004488236,0.00014647408,0.00019475442],"category_scores_gemma":[0.00032953173,0.00017265865,0.00042628456,0.00034367488,0.000062563995,0.00055217766,0.000103671984,0.00046819032,0.00002017542],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013069628,0.00015183061,0.0010941672,0.00010433355,0.0004951868,0.000040716644,0.0031938187,0.0006700288,0.9795633,0.00005981903,0.000203012,0.014293087],"study_design_scores_gemma":[0.0011521323,0.00012445779,0.00040500716,0.00021106072,0.00016001797,0.00037024476,0.00090740476,0.00021057787,0.96861017,0.00002342441,0.027586292,0.00023921201],"about_ca_topic_score_codex":0.000073719035,"about_ca_topic_score_gemma":0.00001540054,"teacher_disagreement_score":0.02738328,"about_ca_system_score_codex":0.00020537055,"about_ca_system_score_gemma":0.00007853278,"threshold_uncertainty_score":0.70408154},"labels":[],"label_agreement":null},{"id":"W2145172547","doi":"10.1016/j.ijhydene.2006.01.001","title":"Kinetic modeling of hydrogen production by the catalytic reforming of crude ethanol over a co-precipitated Ni-Al2O3Ni-Al2O3 catalyst in a packed bed tubular reactor","year":2006,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":117,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Hydrogenics (Canada); University of Saskatchewan; University of Regina","funders":"","keywords":"Catalysis; Dissociation (chemistry); Chemistry; Packed bed; Hydrogen; Kinetic energy; Adsorption; Hydrogen production; Kinetics; Chemical engineering; Atmospheric pressure; Work (physics); Atmospheric temperature range; Thermodynamics; Physical chemistry; Chromatography; Organic chemistry","score_opus":0.010059008566489848,"score_gpt":0.2448120438058023,"score_spread":0.23475303523931246,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2145172547","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99766773,0.0011345005,0.00034029115,0.00014210513,0.00034006612,0.00011007939,0.000047862755,0.000020991756,0.0001964013],"genre_scores_gemma":[0.99902487,0.00006986161,0.000084304,0.000016913216,0.00039846014,0.00001105923,0.00019113913,0.00006325907,0.00014012434],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99647886,0.000065739536,0.0016908898,0.000281742,0.0011438718,0.0003388941],"domain_scores_gemma":[0.99784166,0.00010232496,0.0010572425,0.0003710088,0.0005429365,0.00008485618],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000668324,0.00029258107,0.000584936,0.000606409,0.000026620575,0.000012778319,0.0008207353,0.00015769924,0.000020984178],"category_scores_gemma":[0.0004081596,0.00022742456,0.00032846662,0.0004346573,0.00009543575,0.00042543115,0.000116460964,0.00037119692,0.000001945071],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018357093,0.00017934476,0.0003523847,0.00003299304,0.0003988537,0.000042588552,0.00042210738,0.042885114,0.95460725,0.0001268173,0.00003266378,0.0007363388],"study_design_scores_gemma":[0.0010278499,0.000052299605,0.000021397087,0.00030416346,0.00010401293,0.00041521745,0.00011923862,0.039898578,0.9571224,0.0004190126,0.00030258665,0.00021327808],"about_ca_topic_score_codex":0.0066339304,"about_ca_topic_score_gemma":0.00026804462,"teacher_disagreement_score":0.006365886,"about_ca_system_score_codex":0.00056529377,"about_ca_system_score_gemma":0.00011404918,"threshold_uncertainty_score":0.999981},"labels":[],"label_agreement":null},{"id":"W2146262263","doi":"10.5539/eer.v3n2p90","title":"Co-Production of Liquid and Gaseous Fuels from Polyethylene and Polystyrene in a Continuous Sequential Pyrolysis and Catalytic Reforming System","year":2013,"lang":"en","type":"article","venue":"Energy and Environment Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"National Institute of Advanced Industrial Science and Technology","keywords":"Pyrolysis; Catalysis; Space velocity; Diesel fuel; Polystyrene; Materials science; Polyethylene; High-density polyethylene; Chemical engineering; Raw material; Catalytic reforming; Methane; Liquid fuel; Chemistry; Organic chemistry; Combustion; Composite material; Polymer","score_opus":0.016299487958979893,"score_gpt":0.24743789998445578,"score_spread":0.2311384120254759,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2146262263","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99492043,0.004615377,0.000050324245,0.000110120505,0.000024668141,0.00013000562,0.000008995841,0.000017495713,0.00012255371],"genre_scores_gemma":[0.99741596,0.0018830304,0.00008943077,0.000003261286,0.00007896267,0.00004348913,0.00003357437,0.000023498294,0.00042879058],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998492,0.00007721082,0.00031349057,0.00042920205,0.00032797654,0.00036014122],"domain_scores_gemma":[0.9994021,0.000115105795,0.00005931241,0.00024776402,0.000012877203,0.00016285082],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005779411,0.0001615856,0.00033245882,0.00024601212,0.00009324595,0.000020077689,0.000070791735,0.00012938875,0.000022467864],"category_scores_gemma":[0.00005628915,0.000141768,0.000024007973,0.00011012201,0.00027276567,0.00025136812,0.00018748673,0.00020394352,0.0000022473407],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000084797524,0.000024729981,0.0006797599,0.00014599932,0.000052199175,0.000014354426,0.00042986393,0.000053621006,0.97957623,0.00013325659,0.0000014872184,0.018803684],"study_design_scores_gemma":[0.0006214778,0.00013501919,0.0014072028,0.00016296521,0.000030136362,0.00007450203,0.0011411279,0.001578527,0.99437034,0.000067197405,0.00022505435,0.00018645864],"about_ca_topic_score_codex":0.018002499,"about_ca_topic_score_gemma":0.000084764186,"teacher_disagreement_score":0.018617226,"about_ca_system_score_codex":0.00014756066,"about_ca_system_score_gemma":0.0000089937885,"threshold_uncertainty_score":0.9885367},"labels":[{"model":"gemma","categories":[],"domain":null,"study_design":"bench_or_experimental","genre":"empirical","about_ca_system":false,"about_ca_topic":false,"confidence":"low"},{"model":"gpt","categories":[],"domain":null,"study_design":"bench_or_experimental","genre":"empirical","about_ca_system":false,"about_ca_topic":false,"confidence":"high"}],"label_agreement":"agree"},{"id":"W2154815692","doi":"10.1002/cjce.5450810219","title":"Hydrogen Production from Partial Oxidation and Steam Reforming of N‐octane Over Alumina‐supported Ni and Ni‐Pd Catalysts","year":2003,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Jet Propulsion Laboratory; National Natural Science Foundation of China","keywords":"Catalysis; Steam reforming; Hydrogen production; Nickel; Partial oxidation; Hydrogen; Selectivity; Palladium; Inorganic chemistry; Octane; Materials science; Chemistry; Metallurgy; Organic chemistry","score_opus":0.007504644431404741,"score_gpt":0.1961685032613692,"score_spread":0.18866385882996445,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2154815692","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985311,0.0009592706,0.00006407488,0.00008300539,0.0002072192,0.00009197217,0.000008745622,0.00001483855,0.000039784205],"genre_scores_gemma":[0.999471,0.000011007376,0.00022548507,0.000007727365,0.00020284635,0.0000025765949,0.000013485922,0.000036063033,0.000029780826],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987321,0.000014837027,0.0005308855,0.0001671664,0.00023758992,0.00031741915],"domain_scores_gemma":[0.9990451,0.00005786968,0.00022067424,0.00021300862,0.000086215005,0.00037714466],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00044092277,0.00018915192,0.00034154803,0.00016912204,0.000048535352,0.000014375468,0.00014799245,0.0001239198,0.000016663835],"category_scores_gemma":[0.00079696527,0.0001536208,0.00006917709,0.00021342713,0.000081216094,0.0002720566,0.000021993157,0.00037930516,7.221539e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012930365,0.0000051136235,0.0002976979,0.000051771,0.000098672725,0.000015235253,0.00047799488,0.00060996716,0.99723196,0.00009812035,0.0000072298617,0.00109331],"study_design_scores_gemma":[0.00035772746,0.00001679055,0.0001234401,0.00015323715,0.00011753223,0.00042433143,0.00006566112,0.0020463122,0.9961133,0.000060497332,0.0003489456,0.0001722418],"about_ca_topic_score_codex":0.00324833,"about_ca_topic_score_gemma":0.000280042,"teacher_disagreement_score":0.0029682878,"about_ca_system_score_codex":0.00025240055,"about_ca_system_score_gemma":0.00013751851,"threshold_uncertainty_score":0.62644744},"labels":[],"label_agreement":null},{"id":"W2155545694","doi":"10.1002/ceat.201000282","title":"Optimization of Methanol Yield from a Lurgi Reactor","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":128,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Methanol; Yield (engineering); Chemistry; Syngas; Methanol reformer; Steam reforming; Chemical engineering; Waste management; Process engineering; Catalysis; Thermodynamics; Organic chemistry; Hydrogen production; Engineering","score_opus":0.015550475319962192,"score_gpt":0.20085526151411429,"score_spread":0.18530478619415208,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2155545694","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7353251,0.00040506132,0.26084787,0.000057009765,0.00026060353,0.00018654406,0.00002531059,0.0016625918,0.0012299228],"genre_scores_gemma":[0.9482146,0.000011956414,0.05153877,0.000006183654,0.00006368385,0.000036571597,0.000029912426,0.000070779395,0.000027527265],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986833,0.0000025940233,0.00044861675,0.0003371889,0.00015594813,0.00037238834],"domain_scores_gemma":[0.99906313,0.000113545364,0.000111048204,0.000556697,0.00006231242,0.00009326727],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000074785436,0.00024957056,0.00044448668,0.00033240387,0.000008685045,0.0000023858597,0.0004526117,0.000545558,0.00024237284],"category_scores_gemma":[0.0009537838,0.00025306205,0.00012826922,0.0006203927,0.00007277307,0.00010320427,0.00019482325,0.00046647462,0.00001841395],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000129845075,0.000042593423,0.00004748351,0.000047987083,0.000084561565,0.000007925389,0.00010360495,0.0039031748,0.99366754,0.0008991541,0.0000050185586,0.0011779648],"study_design_scores_gemma":[0.0002300793,0.00001816344,0.0000051190364,0.00009928438,0.000046793743,0.000015791835,0.000020413976,0.063812025,0.9351652,0.00015591238,0.00019178659,0.0002393907],"about_ca_topic_score_codex":0.00010645098,"about_ca_topic_score_gemma":3.5207663e-7,"teacher_disagreement_score":0.21288954,"about_ca_system_score_codex":0.00011007744,"about_ca_system_score_gemma":0.000015020119,"threshold_uncertainty_score":0.99999213},"labels":[],"label_agreement":null},{"id":"W2160646440","doi":"10.1007/s10973-008-9834-0","title":"Optimal synthesis of heat exchanger network for thermochemical S-I cycle","year":2009,"lang":"en","type":"article","venue":"Journal of Thermal Analysis and Calorimetry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Heat exchanger; Thermochemical cycle; Process engineering; Thermodynamics; Chemistry; Environmental science; Engineering; Hydrogen production; Hydrogen; Physics; Organic chemistry","score_opus":0.008199853645013876,"score_gpt":0.23841692610132115,"score_spread":0.23021707245630726,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2160646440","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9877464,0.0019870307,0.009829312,0.00010801176,0.00006054221,0.000045525598,0.000005903383,0.0000094649395,0.0002077962],"genre_scores_gemma":[0.9952313,0.000055072323,0.0040491894,0.000035844125,0.000563677,0.0000015567324,0.0000028243699,0.000014739387,0.0000458426],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987079,0.000022997163,0.0006042217,0.00013607182,0.00026947382,0.00025931554],"domain_scores_gemma":[0.9990418,0.0002498974,0.0002669298,0.00017270526,0.00012690411,0.00014178106],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00057316216,0.00016041873,0.0007545018,0.00024068676,0.000042385425,0.000011290724,0.00019862552,0.00011627853,0.00006911777],"category_scores_gemma":[0.00014804114,0.00011468185,0.00080376875,0.00058013876,0.000036294365,0.00012003988,0.000030289524,0.00018694316,5.9853073e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00045784807,0.00012766235,0.0010618869,0.000064349224,0.0024621675,0.0000092885675,0.00011315423,0.02512295,0.94227105,0.00009278338,0.000043931857,0.028172942],"study_design_scores_gemma":[0.0006388143,0.00023562035,0.0035997329,0.00011507591,0.004177097,0.000040299863,0.00010038314,0.031278014,0.9591896,0.00014765598,0.00019171872,0.00028601207],"about_ca_topic_score_codex":0.000022210868,"about_ca_topic_score_gemma":7.5968524e-7,"teacher_disagreement_score":0.027886929,"about_ca_system_score_codex":0.000045798715,"about_ca_system_score_gemma":0.000013307591,"threshold_uncertainty_score":0.467659},"labels":[],"label_agreement":null},{"id":"W2165183987","doi":"10.1093/chromsci/45.3.153","title":"Gas Chromatography Method for the Characterization of Ethanol Steam Reforming Products","year":2007,"lang":"en","type":"article","venue":"Journal of Chromatographic Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Chemistry; Steam reforming; Ethanol; Gas chromatography; Chromatography; Hydrogen; Catalysis; Organic chemistry; Hydrogen production","score_opus":0.014956025035311385,"score_gpt":0.2878598804699344,"score_spread":0.272903855434623,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2165183987","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9037698,0.00038469132,0.094655305,0.00019147304,0.0005329738,0.00031849038,0.000004529434,0.00003286678,0.00010987516],"genre_scores_gemma":[0.9860312,0.00010828061,0.01348384,0.000030026811,0.00029607903,0.000006338022,0.0000019557256,0.000029021385,0.000013301087],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99706733,0.000021527529,0.001070021,0.0002488624,0.0010720262,0.0005202264],"domain_scores_gemma":[0.9969263,0.00038318965,0.001199144,0.00043079807,0.0009004821,0.00016007194],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0076766214,0.00019563336,0.00042448178,0.0012567765,0.00021532622,0.000026114814,0.000981113,0.000088601955,0.000005580672],"category_scores_gemma":[0.0007617376,0.00012342629,0.00034774502,0.00407755,0.00044810516,0.0008422226,0.000088966626,0.0002948395,5.269869e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004629163,0.000042640062,0.00032743413,0.00013669545,0.000060942974,0.000003304429,0.00045202035,0.000024260064,0.97895664,0.0004689472,0.0000020080688,0.019478787],"study_design_scores_gemma":[0.00045620243,0.00012702867,0.0027680187,0.00023688373,0.000087516404,0.00047586477,0.0002754788,0.0015715263,0.99266136,0.00012627894,0.0010624822,0.00015138276],"about_ca_topic_score_codex":0.000018013989,"about_ca_topic_score_gemma":0.0000026169223,"teacher_disagreement_score":0.08226136,"about_ca_system_score_codex":0.00008103947,"about_ca_system_score_gemma":0.00019939158,"threshold_uncertainty_score":0.50331783},"labels":[],"label_agreement":null},{"id":"W2173199915","doi":"10.1002/cjce.22357","title":"High‐loaded Fe‐supported catalyst for the thermochemical BtL‐FT process: Experimental results and modelling","year":2015,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Syngas; Catalysis; Fischer–Tropsch process; Yield (engineering); Selectivity; Chemical engineering; Materials science; Chemistry; Biomass (ecology); Analytical Chemistry (journal); Chromatography; Metallurgy; Organic chemistry","score_opus":0.02523560480165751,"score_gpt":0.2345468479542133,"score_spread":0.20931124315255578,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2173199915","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9911267,0.0020192119,0.0052298866,0.0009006005,0.00033162683,0.00026128683,0.00002996394,0.00004351246,0.000057165875],"genre_scores_gemma":[0.9984447,0.0000020608354,0.00077208155,0.000042068805,0.0005938007,0.000021730708,0.000020256482,0.000067892,0.00003544307],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99818003,0.000009423073,0.00064932817,0.00020383856,0.00035398392,0.0006033736],"domain_scores_gemma":[0.99816704,0.00033610445,0.00020166265,0.00030172797,0.0002080367,0.0007854151],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008089805,0.0002812881,0.0003867271,0.000120074044,0.000117885844,0.0000658631,0.000593558,0.00016457496,0.0000060280327],"category_scores_gemma":[0.0008192851,0.0001787984,0.0001649637,0.00023135336,0.00013380189,0.00019194734,0.0000464281,0.00064107525,0.0000019273423],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015695521,0.000013567338,0.0000037712541,0.000056827725,0.00019383644,0.00002588381,0.0022932265,0.10645296,0.8899838,0.0003620016,0.00016111662,0.0002961096],"study_design_scores_gemma":[0.00117031,0.000028165603,7.2069906e-7,0.000093352384,0.00009402524,0.0003510021,0.00025702824,0.16030385,0.8368693,0.000115559415,0.0004983798,0.00021831706],"about_ca_topic_score_codex":0.0012007976,"about_ca_topic_score_gemma":0.00002911623,"teacher_disagreement_score":0.053850885,"about_ca_system_score_codex":0.00042950877,"about_ca_system_score_gemma":0.0003522232,"threshold_uncertainty_score":0.72911865},"labels":[],"label_agreement":null},{"id":"W2184864151","doi":"","title":"ETHANOL REFORMING FOR HYDROGEN PRODUCTION IN HIGH PRESSURE CONDITION: EFFECT OF DIFFERENT SUPPORT ON COBALT BASED CATALYST","year":2009,"lang":"en","type":"article","venue":"RASAYAN Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Catalysis; Cobalt; Hydrogen production; Steam reforming; Hydrogen; Cobalt oxide; Supercritical fluid; Inorganic chemistry; Materials science; Chemistry; Catalyst support; Chemical engineering; Organic chemistry","score_opus":0.005983430073272602,"score_gpt":0.2441500959172539,"score_spread":0.2381666658439813,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2184864151","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9990145,0.0001116513,0.000092957715,0.00018286884,0.00013207679,0.00022106551,0.000027433594,0.000022128872,0.00019533529],"genre_scores_gemma":[0.99922764,0.000005092483,0.00005623577,0.000012271099,0.00037011702,0.000010937159,0.000103254184,0.000026763379,0.0001876826],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99830776,0.000023156594,0.00076637004,0.00021057815,0.0004132573,0.00027886924],"domain_scores_gemma":[0.9987406,0.00013725532,0.0005845355,0.00028927883,0.000121695455,0.00012663673],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00060266437,0.0002443699,0.00062579825,0.0001213251,0.000027944036,0.0000061207697,0.00024310475,0.00017643416,0.000044512883],"category_scores_gemma":[0.000503018,0.00019115138,0.0002791997,0.00016475223,0.000032511965,0.00016106284,0.00001484288,0.00041516154,9.175577e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00054108887,0.00011872574,0.00028405708,0.00084069825,0.00008312042,0.00002078754,0.00005631657,0.0021140536,0.9932012,0.000003508227,0.000033049695,0.002703411],"study_design_scores_gemma":[0.0022400054,0.0003997287,0.0001239918,0.0006208351,0.0001644163,0.00015114702,0.000016458154,0.00029964256,0.99562776,0.000053023636,0.00012575794,0.00017720355],"about_ca_topic_score_codex":0.0000040514024,"about_ca_topic_score_gemma":4.972952e-7,"teacher_disagreement_score":0.0025262074,"about_ca_system_score_codex":0.00024109465,"about_ca_system_score_gemma":0.000060013776,"threshold_uncertainty_score":0.7794927},"labels":[],"label_agreement":null},{"id":"W2198074607","doi":"10.1016/j.solener.2015.11.038","title":"Solar molten salt heated membrane reformer for natural gas upgrading and hydrogen generation: A CFD model","year":2015,"lang":"en","type":"article","venue":"Solar Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":48,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"King Fahd University of Petroleum and Minerals","keywords":"Molten salt; Materials science; Hydrogen; Endothermic process; Volumetric flow rate; Isothermal process; Methane; Heat transfer; Steam reforming; Natural gas; Hydrogen production; Chemical engineering; Thermodynamics; Chemistry; Organic chemistry; Metallurgy","score_opus":0.027768996977635123,"score_gpt":0.24566633964374865,"score_spread":0.21789734266611352,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2198074607","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.94444203,0.0031902741,0.048979446,0.00041398202,0.00044347017,0.00030609107,0.000055482364,0.000467249,0.0017019605],"genre_scores_gemma":[0.99198836,0.00005224562,0.0048148297,0.00013696792,0.0005083465,0.00006928516,0.00037799482,0.00009557724,0.0019563797],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99851143,0.000017481174,0.00033510223,0.00038734276,0.00026543293,0.0004831809],"domain_scores_gemma":[0.99919456,0.000029085075,0.00007512897,0.00031385603,0.00011661522,0.00027072546],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029006443,0.00026926657,0.00034052326,0.00013206298,0.0001138791,0.000033066815,0.00017311895,0.00017826709,0.0000050013177],"category_scores_gemma":[0.00013770029,0.00023488057,0.00013050038,0.00018935502,0.00003242074,0.00037654737,0.00010068169,0.0001844262,0.0000034448444],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000054139688,0.000018925042,0.0000061974933,0.00005001317,0.00012386659,0.0000068447557,0.0003184621,0.039801642,0.9535733,0.0023537343,0.00014505767,0.0035478037],"study_design_scores_gemma":[0.00057125476,0.000019971496,1.1594835e-7,0.0000131268025,0.0000337475,0.00004026762,0.00002045786,0.5328564,0.46314254,0.0003793225,0.0027324527,0.00019035682],"about_ca_topic_score_codex":0.00030663534,"about_ca_topic_score_gemma":0.00008379271,"teacher_disagreement_score":0.49305475,"about_ca_system_score_codex":0.00022942947,"about_ca_system_score_gemma":0.00006533727,"threshold_uncertainty_score":0.9578152},"labels":[],"label_agreement":null},{"id":"W2203094417","doi":"10.1016/s0167-2991(01)80330-x","title":"Methane to syngas: Development of non-coking catalyst and hydrogen-permselective membrane","year":2001,"lang":"en","type":"book-chapter","venue":"Studies in surface science and catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Natural Resources Canada","funders":"","keywords":"Syngas; Syngas to gasoline plus; Methane; Catalysis; Chemistry; Hydrogen; Chemical engineering; Steam reforming; Hydrogen production; Organic chemistry; Engineering","score_opus":0.026355355035471668,"score_gpt":0.29078468599593194,"score_spread":0.2644293309604603,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2203094417","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95498544,0.008317855,0.00008061778,0.000049668688,0.00014229809,0.00053676794,0.000025168354,0.000052858453,0.03580931],"genre_scores_gemma":[0.97615594,0.0022438378,0.0019192923,0.000029510236,0.00005116744,0.00003543519,0.000026215326,0.00008149319,0.019457106],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9965715,0.0000080673635,0.00078374223,0.0010340014,0.0009921313,0.00061055954],"domain_scores_gemma":[0.99843496,0.00018232135,0.00025950526,0.00049380166,0.00041093904,0.00021848395],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0017751053,0.0005301419,0.0012991528,0.000781903,0.00023262878,0.000018053155,0.00046472735,0.00016466535,0.000012088909],"category_scores_gemma":[0.00048448166,0.00047237787,0.00010260621,0.0010895429,0.0009776367,0.00027563714,0.000999925,0.0003574282,0.000011638481],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000059076974,0.000045113717,0.00019990891,0.0010673907,0.0014840468,0.00007912498,0.032705247,0.0014272513,0.92323714,0.00032451065,0.000010721716,0.039360475],"study_design_scores_gemma":[0.00039882126,0.00004988077,0.00003114037,0.0010498684,0.00037667982,0.000058169797,0.0036640696,0.00041565314,0.99022615,0.00010959893,0.002668661,0.00095127925],"about_ca_topic_score_codex":0.000206466,"about_ca_topic_score_gemma":0.00046536746,"teacher_disagreement_score":0.06698904,"about_ca_system_score_codex":0.0007007749,"about_ca_system_score_gemma":0.00023698031,"threshold_uncertainty_score":0.9997728},"labels":[],"label_agreement":null},{"id":"W2203450406","doi":"","title":"Preparation of a Novel Super Active Fischer-Tropsch Cobalt Catalyst Supported on Carbon Nanotubes","year":2009,"lang":"en","type":"article","venue":"DOAJ (DOAJ: Directory of Open Access Journals)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Fischer–Tropsch process; Cobalt; Catalysis; Carbon nanotube; Materials science; Chemical engineering; Nanotechnology; Chemistry; Organic chemistry; Metallurgy; Selectivity; Engineering","score_opus":0.1300917017539628,"score_gpt":0.4983312702232264,"score_spread":0.36823956846926353,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2203450406","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.988549,0.0012924414,0.0002128111,0.000071989445,0.00025231577,0.0005336549,0.00009722397,0.00006972126,0.008920843],"genre_scores_gemma":[0.998703,0.00037498394,0.00019204144,0.000063414256,0.00015745327,0.000027131397,0.00010509736,0.00006321863,0.00031366304],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99676853,0.00007589793,0.0011716299,0.0005253488,0.0009686859,0.00048989366],"domain_scores_gemma":[0.9975987,0.0002554732,0.0008003618,0.00069959497,0.00038504714,0.0002607891],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007269298,0.0004408185,0.0010582202,0.0007657807,0.000096887285,0.0001637183,0.0016011178,0.00022518563,0.0008832098],"category_scores_gemma":[0.00064352783,0.00039511267,0.0003109697,0.0010992155,0.00008286035,0.0016786671,0.0003229296,0.00055027247,0.0000061172414],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005909326,0.0005037832,0.0042237095,0.00008434568,0.00027282626,0.0000142592,0.00041407405,0.0010304847,0.9874038,0.000106391744,0.0003257409,0.005029636],"study_design_scores_gemma":[0.0010070651,0.000046746547,0.028372282,0.00044556273,0.00015251235,0.000024556304,0.00007889526,0.0016637163,0.96691626,0.00017093137,0.0006865177,0.0004349727],"about_ca_topic_score_codex":0.0015875982,"about_ca_topic_score_gemma":0.000058366437,"teacher_disagreement_score":0.024148572,"about_ca_system_score_codex":0.0003202943,"about_ca_system_score_gemma":0.00015170171,"threshold_uncertainty_score":0.9998501},"labels":[],"label_agreement":null},{"id":"W2224553560","doi":"10.1002/cjce.22426","title":"Fischer‐Tropsch synthesis: Effect of solvent on the H<sub>2</sub>‐D<sub>2</sub> isotopic exchange rate over an activated cobalt catalyst","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Cobalt; Chemistry; Solvent; Fischer–Tropsch process; Pentane; Hexadecane; Hydrogen; Inorganic chemistry; Hydrogen–deuterium exchange; Organic chemistry; Selectivity","score_opus":0.008416262647070547,"score_gpt":0.19754652911308052,"score_spread":0.18913026646600997,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2224553560","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99827045,0.00026897228,0.00021184271,0.0005629542,0.00029634804,0.00025656348,0.000040672567,0.000048492544,0.000043718926],"genre_scores_gemma":[0.99927944,0.00002178644,0.000013896433,0.00005071559,0.00047312156,0.000033798588,0.000005918152,0.00011358203,0.000007722089],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99756354,0.00011163151,0.0007416318,0.00028056346,0.00048837566,0.00081424357],"domain_scores_gemma":[0.9967518,0.0013466239,0.00036579123,0.0006697548,0.00013327925,0.000732745],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012962156,0.0004780681,0.00071773434,0.00028787972,0.000101358615,0.000041480194,0.0008692742,0.00025889525,0.000036706613],"category_scores_gemma":[0.0019369649,0.00026084835,0.00041051165,0.00043088096,0.00014138041,0.00028832143,0.00006942029,0.00087218103,0.000018532144],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000086576125,0.00001548878,0.000029440898,0.00013986437,0.00026476404,0.000046238394,0.00015006853,0.00095350866,0.99363244,0.00011214056,0.000062026695,0.0045074658],"study_design_scores_gemma":[0.0006480378,0.00010389356,0.00007960131,0.0009066992,0.00017366138,0.000110443216,0.000010662348,0.001492083,0.99589515,0.000021520169,0.00022326101,0.0003350011],"about_ca_topic_score_codex":0.00037179198,"about_ca_topic_score_gemma":0.00016076342,"teacher_disagreement_score":0.004172465,"about_ca_system_score_codex":0.0009004218,"about_ca_system_score_gemma":0.00021681454,"threshold_uncertainty_score":0.9999844},"labels":[],"label_agreement":null},{"id":"W2229105327","doi":"10.1002/cjce.22425","title":"Gas‐to‐liquids processes: Preface","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada; Sasol","keywords":"Syngas; Syngas to gasoline plus; Natural gas; Gasoline; Waste management; Coal; Environmental science; Gas to liquids; Fossil fuel; Biomass (ecology); Chemistry; Engineering; Organic chemistry; Catalysis; Geology","score_opus":0.008325367269559113,"score_gpt":0.2015577418872732,"score_spread":0.1932323746177141,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2229105327","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9905418,0.00037046257,0.005812422,0.0024536366,0.0003215186,0.000119202436,0.000011680832,0.00005436861,0.00031489602],"genre_scores_gemma":[0.99865085,0.0000024693513,0.0005762021,0.000066618246,0.0004462189,0.0000059534605,6.346629e-7,0.000055606182,0.0001954519],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99859136,0.000006551559,0.0004360032,0.0001338565,0.00028259566,0.0005496245],"domain_scores_gemma":[0.99832165,0.00020763453,0.00009391146,0.0002680955,0.00020015419,0.0009085558],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00037470937,0.00019935159,0.00027940675,0.00020598434,0.000042642925,0.000027441441,0.00066045177,0.00010273736,0.00007867828],"category_scores_gemma":[0.002192947,0.00011407067,0.0001236343,0.00042987659,0.000046964647,0.00019406207,0.000038271697,0.00034150816,0.000042151212],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001284102,0.0000035393066,0.000028868215,0.00006522324,0.000053558597,0.000031236847,0.0003033755,0.0022184765,0.99467796,0.00032561948,0.00012930574,0.002149998],"study_design_scores_gemma":[0.0003051791,0.000026846761,0.0000069495873,0.00043227425,0.000030944153,0.00034059142,0.000008716533,0.00044589938,0.9881283,0.000072862334,0.009986136,0.00021529026],"about_ca_topic_score_codex":0.00036172528,"about_ca_topic_score_gemma":0.00013984645,"teacher_disagreement_score":0.00985683,"about_ca_system_score_codex":0.00058255077,"about_ca_system_score_gemma":0.0004593958,"threshold_uncertainty_score":0.4651667},"labels":[],"label_agreement":null},{"id":"W2229843803","doi":"10.2495/esus130021","title":"Interaction of CO<sub>2</sub>/CH<sub>4</sub>with steel wool in an electrocatalytic dry reforming reactor","year":2013,"lang":"en","type":"article","venue":"WIT transactions on ecology and the environment","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Hydro-Québec; Université de Sherbrooke","funders":"CRB Innovations; Natural Sciences and Engineering Research Council of Canada; Enerkem","keywords":"Syngas; Oxidizing agent; Carbon dioxide reforming; Methane; Catalysis; Chemical engineering; Materials science; Chemistry; Inorganic chemistry; Organic chemistry","score_opus":0.005753944966944392,"score_gpt":0.19520093409294334,"score_spread":0.18944698912599894,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2229843803","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9953221,0.000033492503,0.0038066604,0.00012816257,0.00006411408,0.0004958777,0.000005958051,0.00003740419,0.00010621701],"genre_scores_gemma":[0.99936426,0.00017901295,0.0000495435,0.000039497212,0.000021450796,0.00025358456,0.000022353577,0.00003653552,0.000033782522],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987362,0.00006628064,0.0003825605,0.0003156646,0.00016021688,0.0003390794],"domain_scores_gemma":[0.9992123,0.00020268024,0.00013502411,0.00035170923,0.000009676109,0.00008860727],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025334817,0.00023069355,0.00034128316,0.00017715772,0.00010052256,0.000008433219,0.00013079164,0.00016769812,0.00005120503],"category_scores_gemma":[0.000010457657,0.00016390573,0.00007538885,0.000113957045,0.00020664434,0.00036875764,0.0000087601,0.00056980475,0.00006238589],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030523294,0.0002565913,0.00033377123,0.0000360793,0.000121867015,0.0000037142993,0.0005224165,0.0030238805,0.9732415,0.000051364623,4.1087668e-7,0.022103183],"study_design_scores_gemma":[0.0016710475,0.0003094106,0.0054821,0.00004705715,0.000099841105,0.00004000621,0.00043390025,0.004207332,0.98739094,0.00007984189,0.00003475257,0.00020374687],"about_ca_topic_score_codex":0.00006419216,"about_ca_topic_score_gemma":0.0002520152,"teacher_disagreement_score":0.021899436,"about_ca_system_score_codex":0.000367193,"about_ca_system_score_gemma":0.000017089733,"threshold_uncertainty_score":0.6683881},"labels":[],"label_agreement":null},{"id":"W2249330846","doi":"10.14447/jnmes.v16i3.25","title":"Thermodynamic Analysis of the Absorption Enhanced Steam Reforming of Biofuel Model Compounds","year":2013,"lang":"en","type":"article","venue":"Journal of New Materials for Electrochemical Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Stoichiometry; Furfural; Chemistry; Vanillin; Steam reforming; Methanol; Nuclear chemistry; Biofuel; Carbon fibers; Chemical engineering; Hydrogen; Hydrogen production; Organic chemistry; Materials science; Catalysis; Waste management","score_opus":0.011773599251090486,"score_gpt":0.24166112607235818,"score_spread":0.2298875268212677,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2249330846","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9861806,0.00022183899,0.012851239,0.000026450243,0.000244714,0.00035237815,0.000022441376,0.000014973298,0.0000853861],"genre_scores_gemma":[0.9993857,0.000019402893,0.00015725217,0.0000052795435,0.00019920847,0.000016674632,0.000016250573,0.00003588875,0.00016430239],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99734414,0.000033576704,0.0015875575,0.00015774577,0.0005468185,0.0003301655],"domain_scores_gemma":[0.9972781,0.000106194355,0.0016720896,0.00033370833,0.00050325546,0.00010666223],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00059297006,0.00021478329,0.0010898955,0.00026143316,0.000029855479,0.000018101666,0.0005125679,0.0001886661,0.000017820561],"category_scores_gemma":[0.00020807142,0.00013511599,0.0005849651,0.0005189062,0.00004119127,0.00022811681,0.000060018665,0.00016173134,0.0000010973802],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011638867,0.00004067122,0.0000099858025,0.00030287768,0.00082950265,7.83212e-8,0.0001528206,0.0015162094,0.99672896,0.0001399059,0.000015501946,0.00014709022],"study_design_scores_gemma":[0.0005628256,0.00007317621,0.000031286403,0.00022082204,0.00068572146,0.000021741063,0.00007449575,0.037099592,0.96064425,0.00043880905,0.00001127876,0.00013602611],"about_ca_topic_score_codex":0.00027323622,"about_ca_topic_score_gemma":0.0000055852493,"teacher_disagreement_score":0.03608474,"about_ca_system_score_codex":0.0003883228,"about_ca_system_score_gemma":0.0001023926,"threshold_uncertainty_score":0.550987},"labels":[],"label_agreement":null},{"id":"W2253706778","doi":"10.1021/acs.iecr.5b03828","title":"Mechanistic Kinetic Modeling of Oxidative Steam Reforming of Bioethanol for Hydrogen Production over Rh–Ni/CeO<sub>2</sub>–ZrO<sub>2</sub> Catalyst","year":2015,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Steam reforming; Catalysis; Chemistry; Dehydrogenation; Kinetic energy; Hydrogen production; Decomposition; Activation energy; Reactions on surfaces; Hydrogen; Inorganic chemistry; Chemical engineering; Physical chemistry; Organic chemistry","score_opus":0.09443083511130913,"score_gpt":0.31559965509002497,"score_spread":0.22116881997871585,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2253706778","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99660176,0.00030187695,0.0012020551,0.000032150092,0.0003913289,0.001025395,0.00014027258,0.00020178941,0.00010338406],"genre_scores_gemma":[0.9978424,0.000034861696,0.00013088039,8.9690474e-7,0.00123078,0.00024290763,0.00025759588,0.00019523043,0.000064469335],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99485,0.00005573427,0.0013218613,0.00090313697,0.0016201681,0.0012490916],"domain_scores_gemma":[0.996801,0.00033593888,0.00034353833,0.001011534,0.0010090192,0.00049897854],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002789203,0.0005728377,0.0009660338,0.00051313743,0.00010382009,0.000026129153,0.0007697588,0.0007720306,0.0000059178606],"category_scores_gemma":[0.0066250325,0.0006000912,0.0003068854,0.0015302082,0.00016298138,0.00037272656,0.00045424554,0.0015020815,0.000008005995],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00025654017,0.00010362185,0.0000074466684,0.00089040503,0.00021733959,0.000007937021,0.00026896637,0.09107278,0.9050102,0.00003172329,0.000023572515,0.0021094657],"study_design_scores_gemma":[0.0015516202,0.000121923775,3.603401e-7,0.00070045935,0.000107647706,0.000038827133,0.00034231547,0.13225356,0.864271,0.00007720689,0.00005514528,0.00047995578],"about_ca_topic_score_codex":0.0003031966,"about_ca_topic_score_gemma":0.000005759668,"teacher_disagreement_score":0.04118078,"about_ca_system_score_codex":0.0012118318,"about_ca_system_score_gemma":0.00049899245,"threshold_uncertainty_score":0.99964505},"labels":[],"label_agreement":null},{"id":"W2254612158","doi":"10.1039/c6cy00032k","title":"Factors affecting the long-term stability of mesoporous nickel-based catalysts in combined steam and dry reforming of methane","year":2016,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":80,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Agence Universitaire de la Francophonie","keywords":"Catalysis; Carbon dioxide reforming; Methane; Mesoporous material; Sintering; Steam reforming; Coke; Nickel; Methane reformer; Chemical engineering; Materials science; Syngas; Chemistry; Metallurgy; Hydrogen production; Organic chemistry","score_opus":0.017608337104954543,"score_gpt":0.26134624507513526,"score_spread":0.24373790797018072,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2254612158","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9983646,0.00035236948,0.0006392848,0.00013004437,0.00006677339,0.0002805835,0.000011029496,0.00011417112,0.0000411169],"genre_scores_gemma":[0.99983525,0.000010473549,0.00008326349,0.000002699064,0.0000062621457,0.000017833709,0.000008318868,0.000021272508,0.000014629886],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974498,0.0000391909,0.0007896845,0.0006282839,0.00049079524,0.0006022118],"domain_scores_gemma":[0.9974103,0.00054885884,0.0004816255,0.0012824647,0.00018100442,0.00009577138],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0020928846,0.00027270312,0.00075323245,0.0014277343,0.00009021718,0.000006219582,0.0011383684,0.00021792388,0.000008853866],"category_scores_gemma":[0.0027150032,0.0001534634,0.00014427064,0.0039137304,0.0026410595,0.00038200538,0.0005533045,0.00029337732,0.000001405251],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000013993041,0.000051741332,0.21399708,0.00008705223,0.000022867618,0.0000025572913,0.0003912521,0.000010512454,0.7731163,0.00008001885,3.2905955e-8,0.012226612],"study_design_scores_gemma":[0.0005755288,0.0000727111,0.012391852,0.00015041303,0.00006485097,0.0000066901966,0.0009974091,0.00020033281,0.9852891,0.000064693406,0.0000011381455,0.00018529149],"about_ca_topic_score_codex":0.00034501558,"about_ca_topic_score_gemma":0.00034061182,"teacher_disagreement_score":0.21217282,"about_ca_system_score_codex":0.00046068477,"about_ca_system_score_gemma":0.00017967758,"threshold_uncertainty_score":0.97310936},"labels":[],"label_agreement":null},{"id":"W2258881133","doi":"10.1002/cjce.22413","title":"Slurry reactor system with inertial separation for Fischer‐Tropsch synthesis and other three‐phase hydrogenation processes","year":2015,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":23,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Slurry; Fischer–Tropsch process; Catalysis; Materials science; Chemical engineering; Continuous stirred-tank reactor; Phase (matter); Chemical reactor; Chemistry; Organic chemistry; Engineering; Composite material","score_opus":0.01921193644295281,"score_gpt":0.2356702843249776,"score_spread":0.2164583478820248,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2258881133","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98644525,0.00043342594,0.012548136,0.00017627134,0.000094360796,0.00017393591,0.000020384121,0.000036571466,0.00007165816],"genre_scores_gemma":[0.9986523,3.3986143e-7,0.000850742,0.000012298578,0.00039825248,0.00002435397,0.000004143046,0.000049832077,0.000007787772],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990664,0.000006893953,0.00032627114,0.00011216058,0.00021928891,0.0002689847],"domain_scores_gemma":[0.998857,0.00017423215,0.00014872555,0.00012783078,0.00023680212,0.000455364],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00038892703,0.00016850144,0.00025901743,0.00012912565,0.000042659125,0.00004405998,0.00018086693,0.00010051415,0.0000026744847],"category_scores_gemma":[0.0010442368,0.000113829716,0.00005440412,0.00020216223,0.000036703914,0.0002107405,0.000009867549,0.0002253828,9.844197e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002868022,0.000020657964,0.00013034453,0.0007541759,0.00030314014,0.000032317206,0.0011780385,0.0204576,0.973897,0.0011964546,0.00006377146,0.0016797172],"study_design_scores_gemma":[0.0010063353,0.00006703468,0.000002115615,0.00035196065,0.00013618376,0.0004933479,0.000070101276,0.1283557,0.867749,0.0000136602785,0.0015401121,0.00021444629],"about_ca_topic_score_codex":0.0007437776,"about_ca_topic_score_gemma":0.000436848,"teacher_disagreement_score":0.1078981,"about_ca_system_score_codex":0.0004186307,"about_ca_system_score_gemma":0.00039544993,"threshold_uncertainty_score":0.4641841},"labels":[],"label_agreement":null},{"id":"W2267462256","doi":"","title":"Extensive Analysis of Hydrogen Costs","year":2010,"lang":"en","type":"article","venue":"JuSER (Forschungszentrum Jülich)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Fossil fuel; Gasoline; Subsidy; Hydrogen; Hydrogen fuel; Automotive industry; Waste management; Hydrogen economy; Diesel fuel; Coal; Environmental science; Natural resource economics; Economics; Engineering; Chemistry","score_opus":0.006925119897219684,"score_gpt":0.23824160655651827,"score_spread":0.23131648665929858,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2267462256","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9945454,0.00009084009,0.00029867588,0.0001185655,0.000334282,0.00020107547,0.00007176126,0.00020864744,0.0041307383],"genre_scores_gemma":[0.9979451,0.000012320218,0.0004591316,0.00009044916,0.00015553372,0.000018514582,0.00016089909,0.00007261144,0.0010854597],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977658,0.00001886587,0.0006489675,0.00045988834,0.0005108989,0.0005955777],"domain_scores_gemma":[0.9981303,0.00014854495,0.00027057322,0.0009839656,0.00018983579,0.00027675988],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00032437828,0.00031999339,0.00075323536,0.00065637124,0.00006682811,0.000016711865,0.0005108027,0.00026292494,0.00060757605],"category_scores_gemma":[0.00040767572,0.00029258404,0.00061696925,0.0017274561,0.00009833818,0.0002552927,0.00022068185,0.0005433984,0.00015154565],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003169606,0.00007346798,0.005006315,0.00004176645,0.0015649239,0.000014569555,0.00033031308,0.00038661677,0.9869528,0.0030937416,0.00007593432,0.0024278967],"study_design_scores_gemma":[0.0006495706,0.000032589764,0.0065634046,0.000028676743,0.0022106033,0.00002681786,0.00014345192,0.019571552,0.9598334,0.00010118864,0.0103243515,0.0005144307],"about_ca_topic_score_codex":0.00051585794,"about_ca_topic_score_gemma":0.00040382202,"teacher_disagreement_score":0.027119394,"about_ca_system_score_codex":0.00010952126,"about_ca_system_score_gemma":0.000035362013,"threshold_uncertainty_score":0.9999526},"labels":[],"label_agreement":null},{"id":"W2275312861","doi":"10.1139/cjc-2015-0499","title":"Fischer–Tropsch synthesis over alumina-supported cobalt catalysts: effects of different spray temperature of aluminum slurry","year":2016,"lang":"en","type":"article","venue":"Canadian Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Fischer–Tropsch process; Calcination; Catalysis; Cobalt; Chemistry; Slurry; Particle size; Aluminium; Chemical engineering; Inorganic chemistry; Nuclear chemistry; Organic chemistry; Materials science; Physical chemistry","score_opus":0.0038338362559142626,"score_gpt":0.19123063814807587,"score_spread":0.1873968018921616,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2275312861","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9980367,0.000751251,0.000020666519,0.00014308952,0.00021778517,0.00008147906,0.00011119018,0.000010476772,0.0006273978],"genre_scores_gemma":[0.9987589,0.000025736615,0.000055073087,0.000012678276,0.00024401219,0.000005427764,0.000011030863,0.000054173935,0.0008329407],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980032,0.000025567457,0.00085968943,0.00021438068,0.00041188148,0.00048529345],"domain_scores_gemma":[0.99736965,0.00037473682,0.00065993314,0.00048465462,0.00028015143,0.000830849],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00022927126,0.00031456543,0.0008039563,0.00015998425,0.00003910355,0.000010066121,0.00052683265,0.00032216994,0.00038095968],"category_scores_gemma":[0.0017342372,0.00022214052,0.00039910834,0.00023271726,0.00019066116,0.0001737452,0.000036490314,0.00040447133,0.00000286285],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000032153424,0.000031451484,0.002038752,0.00096398825,0.00030422688,0.00019383068,0.00014064668,0.0000026254777,0.9946246,0.000008986653,0.00056774827,0.0010909499],"study_design_scores_gemma":[0.0007857298,0.00003213412,0.00085806503,0.0016492337,0.00019696957,0.00024508275,0.00009255945,0.00000547783,0.9949557,0.000014454174,0.00091306044,0.00025153646],"about_ca_topic_score_codex":0.00060969085,"about_ca_topic_score_gemma":0.00027325907,"teacher_disagreement_score":0.0015049659,"about_ca_system_score_codex":0.00048926036,"about_ca_system_score_gemma":0.00069121417,"threshold_uncertainty_score":0.9058627},"labels":[],"label_agreement":null},{"id":"W2278516120","doi":"10.1021/acscatal.5b02060","title":"Surface-Bound Intermediates in Low-Temperature Methanol Synthesis on Copper: Participants and Spectators","year":2015,"lang":"en","type":"article","venue":"ACS Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":107,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Biological and Environmental Research; Basic Energy Sciences; Natural Sciences and Engineering Research Council of Canada; U.S. Department of Energy","keywords":"Formate; Formic acid; Chemistry; Methanol; Catalysis; Titration; Inorganic chemistry; Adsorption; Photochemistry; Organic chemistry","score_opus":0.022749578277725887,"score_gpt":0.263363678581896,"score_spread":0.24061410030417013,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2278516120","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9986564,0.00047996885,0.0000014505584,0.00013491134,0.00013962603,0.00012833203,0.000023299943,0.00010838546,0.00032763707],"genre_scores_gemma":[0.99941224,0.000050808503,0.00006373905,0.000036822967,0.00008151449,0.000034142802,0.000053294694,0.000057098427,0.00021031412],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981593,0.000050566785,0.0004110191,0.00046374803,0.00036559644,0.0005497693],"domain_scores_gemma":[0.998666,0.00037578534,0.000090747606,0.00048766637,0.000052823973,0.00032696704],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00052666175,0.00030460762,0.00056127424,0.00025706555,0.00003759391,0.00004579421,0.0002536899,0.0001867056,0.000022673332],"category_scores_gemma":[0.0015050778,0.00026073083,0.00010366064,0.0006517003,0.00008839104,0.0002594215,0.00015352543,0.00034358248,0.00012369703],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014966947,0.00020822225,0.013662262,0.00018685019,0.0004481604,0.00016029262,0.0046103816,0.001815456,0.97528815,0.00010463415,0.00013511421,0.003230834],"study_design_scores_gemma":[0.0004698278,0.000025772537,0.0010983779,0.00016966138,0.0001441368,0.000012215366,0.0008667214,0.0006392669,0.99608815,0.000048458027,0.000093728304,0.00034370078],"about_ca_topic_score_codex":0.00042919957,"about_ca_topic_score_gemma":0.00028844757,"teacher_disagreement_score":0.02080001,"about_ca_system_score_codex":0.00030545561,"about_ca_system_score_gemma":0.00004655382,"threshold_uncertainty_score":0.9999845},"labels":[],"label_agreement":null},{"id":"W2278590875","doi":"10.1016/j.apcata.2016.02.017","title":"Fischer-Tropsch synthesis: Cobalt catalysts on alumina having partially pre-filled pores exhibit higher C5+ and lower light gas selectivities","year":2016,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"National Research Council Canada; Western Economic Diversification Canada; Natural Sciences and Engineering Research Council of Canada; University of Wyoming; Canadian Institutes of Health Research; University of Saskatchewan; Canadian Light Source","keywords":"Cobalt; Catalysis; Fischer–Tropsch process; Calcination; Chemical engineering; Carbon monoxide; Chemistry; Selectivity; Hydrogen; Cobalt oxide; Materials science; Inorganic chemistry; Organic chemistry","score_opus":0.007697071853476254,"score_gpt":0.21247179554546142,"score_spread":0.20477472369198516,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2278590875","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9918847,0.00040733704,0.00034051997,0.00054045103,0.00020084398,0.00038819123,0.00004235636,0.00039075583,0.005804818],"genre_scores_gemma":[0.99228626,0.0000620679,0.00040134383,0.00009662797,0.0006584014,0.0005156348,0.00008389159,0.0001699082,0.0057258746],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9963115,0.000054944092,0.000746306,0.0011436301,0.0007178657,0.0010257881],"domain_scores_gemma":[0.99788517,0.00033329372,0.0002790356,0.0010551384,0.000084852196,0.00036253128],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00045184288,0.00071632396,0.000972417,0.00031903436,0.00022146656,0.00008467532,0.000457228,0.0003179226,0.0002210321],"category_scores_gemma":[0.00018359904,0.00051817094,0.00033676514,0.00048904517,0.00014771883,0.00031059695,0.00030676433,0.00031794317,0.0001483703],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002505152,0.00014601105,0.00032703564,0.00008102595,0.0005919916,0.00003538833,0.00034406112,0.00010932058,0.9794351,0.0021222718,0.0006981765,0.015859125],"study_design_scores_gemma":[0.00094473985,0.00006174272,0.0005183542,0.00015898258,0.00045871307,0.000030014187,0.00004933986,0.00027799496,0.9908258,0.00012014412,0.0057010306,0.0008531561],"about_ca_topic_score_codex":0.00030316686,"about_ca_topic_score_gemma":0.00015374942,"teacher_disagreement_score":0.0150059685,"about_ca_system_score_codex":0.00039107763,"about_ca_system_score_gemma":0.00007001375,"threshold_uncertainty_score":0.999727},"labels":[],"label_agreement":null},{"id":"W2281005715","doi":"10.5539/jmsr.v5n2p33","title":"H2-TPR, XPS and TEM Study of the Reduction of Ru and Re promoted Co/γ-Al2O3, Co/TiO2 and Co/SiC Catalysts","year":2016,"lang":"en","type":"article","venue":"Journal of Materials Science Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Interreg; Sasol","keywords":"X-ray photoelectron spectroscopy; Catalysis; Metal; Materials science; Chemisorption; Nuclear chemistry; Chemistry; Chemical engineering; Metallurgy","score_opus":0.06213546368032863,"score_gpt":0.3802220440502758,"score_spread":0.3180865803699472,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2281005715","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99921185,0.00011421087,0.0000051074303,0.00017159923,0.00011116915,0.0002954406,0.000014285651,0.000004762659,0.00007159556],"genre_scores_gemma":[0.9996396,0.000104203595,0.000052176027,6.1101565e-7,0.000077784294,0.000003270924,3.2770606e-7,0.0000110665305,0.00011097548],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974853,0.00017416607,0.000590094,0.00021615025,0.0012212844,0.00031299551],"domain_scores_gemma":[0.9985887,0.000168488,0.00036376232,0.00027641607,0.00045166156,0.0001509685],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.007328766,0.00010382374,0.00036248052,0.00039279778,0.00016810055,0.00005731234,0.00037778824,0.000058111316,0.000016912447],"category_scores_gemma":[0.0011759293,0.00005431055,0.000026785252,0.00048633653,0.0009897853,0.00049936416,0.00022594827,0.00018103055,9.510093e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000104923965,0.000069471695,0.0007791081,0.00013785844,0.000019639474,0.000004090436,0.0009956966,0.000001298251,0.9966064,0.00001491391,0.000018215489,0.0012483755],"study_design_scores_gemma":[0.0007776483,0.00035821143,0.0058655827,0.00033670344,0.000016615135,0.00028903855,0.0013600561,0.000018128187,0.9908227,0.000063779764,0.000027357562,0.000064230306],"about_ca_topic_score_codex":0.00012551091,"about_ca_topic_score_gemma":0.000004558666,"teacher_disagreement_score":0.0061528366,"about_ca_system_score_codex":0.00012521693,"about_ca_system_score_gemma":0.00016441516,"threshold_uncertainty_score":0.3646905},"labels":[],"label_agreement":null},{"id":"W2281093366","doi":"10.1039/c5cy01524c","title":"Active phase distribution changes within a catalyst particle during Fischer–Tropsch synthesis as revealed by multi-scale microscopy","year":2016,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":54,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); Saskatoon Medical Imaging","funders":"National Research Council Canada; Nederlandse Organisatie voor Wetenschappelijk Onderzoek; Western Economic Diversification Canada; Canadian Institutes of Health Research; Office of Science; U.S. Department of Energy; European Commission; Universiteit Utrecht; Canadian Light Source; Natural Sciences and Engineering Research Council of Canada; University of Saskatchewan; SLAC National Accelerator Laboratory; Shell","keywords":"Fischer–Tropsch process; Catalysis; Chemical engineering; Particle (ecology); Phase (matter); Materials science; Particle-size distribution; Chemistry; Nanotechnology; Particle size; Organic chemistry; Geology; Engineering; Selectivity","score_opus":0.00924776180872025,"score_gpt":0.27470995079219324,"score_spread":0.26546218898347296,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2281093366","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.989916,0.00019978316,0.0072891386,0.0013281783,0.0001004221,0.00026917894,0.0002604934,0.00060913234,0.00002762338],"genre_scores_gemma":[0.9982211,0.000033358567,0.0005599259,0.000013832296,0.000036317437,0.00028240873,0.00006540507,0.000043735385,0.0007439175],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968138,0.000026279788,0.000501649,0.0010913283,0.0004925635,0.001074394],"domain_scores_gemma":[0.9979254,0.00010871229,0.00031248256,0.0011657017,0.00020265905,0.00028503488],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00060182804,0.00037372185,0.0005668176,0.0005455805,0.000453746,0.00004118513,0.0011659974,0.00030244933,0.00006494741],"category_scores_gemma":[0.002154115,0.0002817565,0.00013958018,0.0032936325,0.0015501113,0.0006955068,0.0004992105,0.00031132862,0.0002764751],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000052565123,0.00017517676,0.0005569378,0.000022973587,0.000050933628,0.000013661577,0.00026374814,0.0000047752733,0.98993415,0.00006607063,0.000007868871,0.008851158],"study_design_scores_gemma":[0.0010853192,0.00005504537,0.000069314956,0.000100201745,0.00013036988,0.000088902016,0.00062932767,0.00094186503,0.9961533,0.000024396244,0.00030955774,0.00041242168],"about_ca_topic_score_codex":0.00017902257,"about_ca_topic_score_gemma":0.000094259456,"teacher_disagreement_score":0.008438736,"about_ca_system_score_codex":0.001067664,"about_ca_system_score_gemma":0.00010910302,"threshold_uncertainty_score":0.99996346},"labels":[],"label_agreement":null},{"id":"W2291385635","doi":"10.1002/cjce.22472","title":"Preparation of nanocrystalline Ni/Al<sub>2</sub>O<sub>3</sub> catalysts with the microemulsion method for dry reforming of methane","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"University of Kashan; Iran National Science Foundation","keywords":"Nanocrystalline material; Catalysis; Carbon dioxide reforming; Syngas; Materials science; Mesoporous material; Microemulsion; Methane; Specific surface area; Space velocity; Scanning electron microscope; Crystallite; Temperature-programmed reduction; Chemical engineering; Nickel; BET theory; Inorganic chemistry; Nuclear chemistry; Nanotechnology; Chemistry; Metallurgy; Selectivity; Organic chemistry; Pulmonary surfactant; Composite material","score_opus":0.007392407240218501,"score_gpt":0.23155216109218668,"score_spread":0.22415975385196818,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2291385635","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9571147,0.00050005445,0.04114685,0.00066500565,0.00015710958,0.00032029866,0.000056912402,0.000024367664,0.000014713999],"genre_scores_gemma":[0.9962714,0.000017510489,0.0033071956,0.000030469277,0.00023071229,0.000020340882,0.000014221146,0.00009540165,0.000012750125],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976274,0.000037817044,0.0010106252,0.00024300715,0.00047044863,0.0006107082],"domain_scores_gemma":[0.9973077,0.00066864904,0.00068416685,0.00050073094,0.0004355427,0.00040321742],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0014222525,0.0003581149,0.0007121969,0.00031637956,0.000065122156,0.000014903499,0.00064479583,0.00019198026,0.000002971352],"category_scores_gemma":[0.0008547106,0.00019295169,0.00035046233,0.00047042928,0.00013555714,0.00035096792,0.000059513815,0.0004605373,0.0000011274016],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001702949,0.000011657203,0.0000065297186,0.00020782468,0.00024063326,0.000008466752,0.00039582682,0.0044873822,0.98635644,0.00010718317,0.000032434775,0.00797532],"study_design_scores_gemma":[0.00097558374,0.00010326297,0.000006643769,0.0007079804,0.000201397,0.00023301847,0.00003724607,0.005128328,0.9917528,0.00005707094,0.0005294061,0.00026725244],"about_ca_topic_score_codex":0.00043034903,"about_ca_topic_score_gemma":0.0005336109,"teacher_disagreement_score":0.03915671,"about_ca_system_score_codex":0.0005908266,"about_ca_system_score_gemma":0.00037416304,"threshold_uncertainty_score":0.7868341},"labels":[],"label_agreement":null},{"id":"W2292236732","doi":"10.1002/cjce.22453","title":"Synthesis gas technology large‐scale applications","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":74,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Syngas; Synthetic fuel; Natural gas; Raw material; Production (economics); Gasoline; Steam reforming; Process engineering; Fischer–Tropsch process; Substitute natural gas; Waste management; Environmental science; Engineering; Chemistry; Hydrogen production; Organic chemistry; Economics; Catalysis","score_opus":0.004880277637035635,"score_gpt":0.1876933771406775,"score_spread":0.18281309950364186,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2292236732","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95036834,0.0010972426,0.04036964,0.006776572,0.0003038316,0.00022060689,0.000047636266,0.00016186478,0.0006542615],"genre_scores_gemma":[0.99867386,0.000004431789,0.00084805134,0.000019836929,0.00030941164,0.000025210327,6.479913e-7,0.000043128402,0.000075454554],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988277,0.0000054999205,0.00038117936,0.00011754105,0.00017465377,0.0004934334],"domain_scores_gemma":[0.9988173,0.00022808948,0.000109393346,0.00032264262,0.0001081353,0.00041441945],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00031246385,0.00015741111,0.00026039188,0.0003056067,0.000061023744,0.000014129733,0.00059845595,0.00015592258,0.00009527638],"category_scores_gemma":[0.00068314857,0.000094906456,0.00014984213,0.00041233253,0.000081444334,0.00010976248,0.000035753714,0.0003698044,0.000037364487],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00000349296,0.000006146849,0.000084392675,0.000022449465,0.000062668994,0.00001604959,0.000074488766,0.00027920876,0.9886238,0.0024452456,0.00004981693,0.008332217],"study_design_scores_gemma":[0.00020808303,0.0000057857987,0.000005092197,0.00015793892,0.00004812511,0.00040077072,0.00002049977,0.0008643615,0.9783279,0.00038330661,0.01941386,0.00016432353],"about_ca_topic_score_codex":0.000100547986,"about_ca_topic_score_gemma":0.000099090066,"teacher_disagreement_score":0.048305485,"about_ca_system_score_codex":0.00044300465,"about_ca_system_score_gemma":0.00016857858,"threshold_uncertainty_score":0.38701728},"labels":[],"label_agreement":null},{"id":"W2316312089","doi":"10.11159/ijepr.2015.002","title":"Nano-Iron Carbide-Catalyzed Fischer-Tropsch Synthesis of Green Fuel: Surface Reaction Kinetics-controlled Regimes in a 3-φ Slurry-Continuous Stirred Tank Reactor","year":2015,"lang":"en","type":"article","venue":"International Journal of Environmental Pollution and Remediation","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Université de Sherbrooke; Natural Sciences and Engineering Research Council of Canada; Enerkem","keywords":"Fischer–Tropsch process; Catalysis; Slurry; Carbide; Chemical engineering; Continuous stirred-tank reactor; Kinetics; Materials science; Nano-; Microreactor; Chemistry; Metallurgy; Organic chemistry; Engineering; Composite material; Selectivity","score_opus":0.009128847030396028,"score_gpt":0.22409314342874148,"score_spread":0.21496429639834547,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2316312089","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99765074,0.0005542164,0.00009921433,0.00073558534,0.00056095916,0.00015896445,0.000037669008,0.000012590626,0.00019008685],"genre_scores_gemma":[0.9987329,0.00029743506,0.00038956729,0.000014070506,0.0002670887,0.0000040201503,0.00003851103,0.000021997164,0.00023440317],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980368,0.000071725386,0.0008577558,0.00016076326,0.0007209719,0.00015199902],"domain_scores_gemma":[0.9987356,0.000120117016,0.00083056814,0.000113460635,0.000073702526,0.00012657211],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00058185164,0.00016686694,0.00040926554,0.00028134583,0.000012849061,0.000013048212,0.00017194671,0.00013840395,0.000019323455],"category_scores_gemma":[0.000618902,0.00014573868,0.00013762008,0.00009350604,0.00006878573,0.00043665053,0.000053631862,0.00020974441,0.0000048508705],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0009278678,0.00016156181,0.00186415,0.00001529093,0.00011275223,0.00001295806,0.00051647646,0.00042944934,0.99103373,0.000021003128,0.000014607109,0.0048901434],"study_design_scores_gemma":[0.01549903,0.0002890171,0.03927472,0.00037288567,0.00028598582,0.00032786,0.0020531311,0.007058276,0.93291456,0.00022452285,0.0012066198,0.0004933992],"about_ca_topic_score_codex":0.000345956,"about_ca_topic_score_gemma":0.00004004155,"teacher_disagreement_score":0.058119185,"about_ca_system_score_codex":0.00067351793,"about_ca_system_score_gemma":0.00003572473,"threshold_uncertainty_score":0.5943051},"labels":[],"label_agreement":null},{"id":"W2316508361","doi":"10.1021/ie100954a","title":"Modeling of a Fluidized Bed Membrane Reactor for Hydrogen Production by Steam Reforming of Hydrocarbons","year":2011,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Steam reforming; Fluidized bed; Fluidization; Methane; Mass transfer; Hydrogen production; Plug flow; Chemistry; Membrane reactor; Thermodynamics; Propane; Plug flow reactor model; Chemical engineering; Hydrogen; Continuous stirred-tank reactor; Chromatography; Organic chemistry","score_opus":0.11521084432627442,"score_gpt":0.3089653497526575,"score_spread":0.19375450542638306,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2316508361","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9983393,0.0002482079,0.00010250729,0.000016955797,0.00013705326,0.00058002124,0.000060799648,0.00013804533,0.00037710482],"genre_scores_gemma":[0.99882793,0.000024653742,0.00014809021,3.3001785e-7,0.00045547757,0.00014376773,0.00009452522,0.00010734878,0.00019786408],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997089,0.00002299665,0.0008992144,0.0004865229,0.0007525909,0.000749627],"domain_scores_gemma":[0.9985373,0.0001835647,0.00014332998,0.0006588022,0.00026128677,0.00021574264],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0017129269,0.00029400858,0.00062264525,0.0002173385,0.000050200375,0.0000053318513,0.00053135847,0.00048452333,0.00002782196],"category_scores_gemma":[0.0030026687,0.00029998124,0.00023461063,0.00072470534,0.000079986465,0.00020047103,0.00016480531,0.00088270684,0.0000013952784],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028286182,0.00009558913,0.000007687826,0.000548824,0.00016006776,0.0000016962907,0.00032432628,0.0019110598,0.99611485,0.000011955499,0.000012924754,0.0005281421],"study_design_scores_gemma":[0.001158819,0.000055407243,5.3139303e-8,0.0003509119,0.00004895661,0.000013304692,0.0001680675,0.05463774,0.943153,0.000015913383,0.0001456275,0.0002521691],"about_ca_topic_score_codex":0.00056765147,"about_ca_topic_score_gemma":0.0000010781424,"teacher_disagreement_score":0.052961838,"about_ca_system_score_codex":0.0003370389,"about_ca_system_score_gemma":0.00015369555,"threshold_uncertainty_score":0.9999452},"labels":[],"label_agreement":null},{"id":"W2319312898","doi":"10.1515/1542-6580.2697","title":"Effect of Operating Conditions for Higher Alcohols Synthesis from Synthesis Gas over Alkali-Modified Co-Rh-Mo Trimetallic Catalyst Supported on Multi-Walled Carbon Nanotubes","year":2011,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"York University; University of Saskatchewan","funders":"","keywords":"Selectivity; Catalysis; Space velocity; Molar ratio; Ethanol; Alkali metal; Carbon nanotube; Chemistry; Chemical engineering; Materials science; Carbon fibers; Inorganic chemistry; Nuclear chemistry; Nanotechnology; Organic chemistry; Composite material","score_opus":0.025064369489425226,"score_gpt":0.2879689537255198,"score_spread":0.26290458423609453,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2319312898","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978576,0.000086680666,0.0006478954,0.000023977736,0.00055857643,0.00023207774,0.00027635793,0.000071278555,0.00024558004],"genre_scores_gemma":[0.9979152,0.000013404851,0.0013249607,0.000010019752,0.00046316182,0.00007612203,0.00007964898,0.00010451766,0.000012932582],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99742204,0.000037361195,0.0011530246,0.0003105969,0.0007178888,0.00035910882],"domain_scores_gemma":[0.99503165,0.0037162704,0.0005283967,0.00024990333,0.00024649967,0.00022728626],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005207162,0.0004177645,0.00090124796,0.0004003525,0.000012272969,0.000027048209,0.0006750026,0.00025551615,0.00014505563],"category_scores_gemma":[0.0048167543,0.00035476332,0.0006476953,0.00014127092,0.000045919718,0.0002658107,0.00006680018,0.0004506657,0.0000041057283],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00041913803,0.00015166185,0.000100914345,0.000075896955,0.0014005791,0.00003647064,0.00014169715,0.0002230236,0.99615234,0.00007974561,0.000007684785,0.0012108268],"study_design_scores_gemma":[0.0016841915,0.00008578443,0.00010073382,0.0006832013,0.00039613774,0.000038874452,0.000010041491,0.01527807,0.98128647,0.000012604761,0.00010229332,0.00032157896],"about_ca_topic_score_codex":0.00021167568,"about_ca_topic_score_gemma":7.4929153e-7,"teacher_disagreement_score":0.015055046,"about_ca_system_score_codex":0.00040903612,"about_ca_system_score_gemma":0.000046058256,"threshold_uncertainty_score":0.99989045},"labels":[],"label_agreement":null},{"id":"W2321539943","doi":"10.1021/jp402421q","title":"Effect of Metal–Support Interface During CH<sub>4</sub>and H<sub>2</sub>Dissociation on Ni/γ-Al<sub>2</sub>O<sub>3</sub>: A Density Functional Theory Study","year":2013,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":83,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Density functional theory; Dissociation (chemistry); Nickel; Metal; Oxide; Chemistry; Adsorption; Hydrogen; Atom (system on chip); Cluster (spacecraft); Hydrogen atom; Physical chemistry; Charge density; Crystallography; Materials science; Computational chemistry","score_opus":0.0051949564678659315,"score_gpt":0.2207758234873451,"score_spread":0.21558086701947915,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2321539943","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985027,0.00012607349,0.00020012727,0.00009659408,0.00023102119,0.00057515356,0.000024575364,0.00011009658,0.00013370269],"genre_scores_gemma":[0.99867314,0.00005566876,0.000005041459,0.00003206353,0.0010001977,0.000040756036,0.000027125052,0.00014437626,0.000021653332],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9952783,0.00036856622,0.0013098683,0.0006199907,0.0015769721,0.00084630074],"domain_scores_gemma":[0.99558145,0.0014175882,0.0013493652,0.0007458496,0.00043993027,0.0004658116],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002253285,0.0008730164,0.0014830338,0.0001578,0.00028599444,0.000071036564,0.0006417672,0.00027980545,0.000020117315],"category_scores_gemma":[0.0010773819,0.00065939006,0.0008297415,0.0005054836,0.0002641087,0.0006310682,0.00046131262,0.0020330793,0.00008989922],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0012077551,0.0007098097,0.00015625196,0.00051900087,0.0011112905,0.000029472381,0.00084578985,0.0010725659,0.9888142,0.000010604527,0.000066239336,0.005457052],"study_design_scores_gemma":[0.0025135183,0.0005841736,0.0027136514,0.0003633596,0.0010245086,0.00027356972,0.00035177506,0.0008954727,0.9903653,0.0002965969,0.0000037531302,0.00061428174],"about_ca_topic_score_codex":0.000010196469,"about_ca_topic_score_gemma":0.000003089198,"teacher_disagreement_score":0.0048427708,"about_ca_system_score_codex":0.0007477064,"about_ca_system_score_gemma":0.00010951938,"threshold_uncertainty_score":0.99958575},"labels":[],"label_agreement":null},{"id":"W2324578673","doi":"10.1515/ijcre-2012-0002","title":"Ethanol Steam Reforming for Hydrogen Production in Microchannel Reactors: Experimental Design and Optimization","year":2013,"lang":"en","type":"article","venue":"International Journal of Chemical Reactor Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Steam reforming; Multi-objective optimization; Hydrogen production; Range (aeronautics); Pareto principle; Optimal design; Process engineering; Mathematical optimization; Computer science; Hydrogen; Chemistry; Engineering; Mathematics; Organic chemistry","score_opus":0.013423781540148798,"score_gpt":0.2464890928375345,"score_spread":0.2330653112973857,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2324578673","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9692787,0.00034422785,0.029451868,0.00013448806,0.0004644812,0.00027315007,0.0000021517872,0.00003900582,0.000011944475],"genre_scores_gemma":[0.9824269,0.000029990222,0.016881097,0.000010067175,0.00053887104,0.000042444513,0.000013861566,0.00004936859,0.0000074106383],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99863255,0.00000794716,0.00060842256,0.00018770939,0.0003265906,0.00023675445],"domain_scores_gemma":[0.9991586,0.00015809844,0.00022808996,0.000093692346,0.00024006295,0.00012143655],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00028598137,0.00018995823,0.00026443324,0.0003127254,0.00000499981,0.00002364646,0.00024748876,0.00012709126,0.00001385821],"category_scores_gemma":[0.000818161,0.00017618368,0.00010727129,0.000111628746,0.000016861553,0.0007679278,0.000060650014,0.00027940626,0.0000015160915],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006432647,0.000052294636,0.0000130740245,0.000024586367,0.00007300528,0.000004974907,0.00029979312,0.024387088,0.9735962,0.000009754856,0.000006878274,0.0014680253],"study_design_scores_gemma":[0.00063044485,0.00003142541,0.0000025325016,0.00023126825,0.000012104766,0.00021159108,0.000078104,0.087876774,0.91064286,0.000021928274,0.00009648967,0.00016445594],"about_ca_topic_score_codex":0.000022447588,"about_ca_topic_score_gemma":8.664809e-8,"teacher_disagreement_score":0.06348968,"about_ca_system_score_codex":0.0005361561,"about_ca_system_score_gemma":0.00002578498,"threshold_uncertainty_score":0.71845615},"labels":[],"label_agreement":null},{"id":"W2325289499","doi":"10.1021/ef201854t","title":"Evaluation of the Catalytic Activity of Various 5Ni/Ce<sub>0.5</sub>Zr<sub>0.33</sub>M<sub>0.17</sub>O<sub>2-δ</sub> Catalysts for Hydrogen Production by the Steam Reforming of a Mixture of Oxygenated Hydrocarbons","year":2012,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Nickel; Dispersion (optics); Chemistry; Nuclear chemistry; Hydrogen; Ethylene glycol; Metal; Hydrogen production; Chemical engineering; Materials science; Inorganic chemistry; Organic chemistry","score_opus":0.013609498419347619,"score_gpt":0.23265861221679693,"score_spread":0.21904911379744932,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2325289499","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99453914,0.0018315106,0.0004997165,0.00011527261,0.00069632597,0.0015921426,0.00034235232,0.00014689422,0.00023666541],"genre_scores_gemma":[0.99814063,0.00018851536,0.000023056686,0.000026591302,0.0004278366,0.00041740917,0.0005015049,0.00025184362,0.000022623313],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9927372,0.00045933414,0.001963479,0.0010483322,0.0024681534,0.0013235025],"domain_scores_gemma":[0.9937197,0.00046887613,0.0023159978,0.002277252,0.00089812774,0.00032006943],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0040220874,0.000983605,0.0015473646,0.00053097005,0.00028049137,0.000017792858,0.0010766496,0.00073796976,0.000002593861],"category_scores_gemma":[0.0017232094,0.0007549598,0.0010246438,0.0019387058,0.00044332485,0.00092893664,0.0005116363,0.0007806388,0.000004536394],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022519061,0.0005968344,0.000053410004,0.00064134225,0.0009713641,0.0000010845183,0.0015637494,0.0026425044,0.95279795,0.000073053256,0.000086393964,0.040347114],"study_design_scores_gemma":[0.0015614697,0.00015106867,0.00032759501,0.00044707194,0.0019684646,0.00009221244,0.00022443406,0.0036420953,0.9904194,0.0003428765,0.00009523841,0.0007280861],"about_ca_topic_score_codex":0.00046595652,"about_ca_topic_score_gemma":0.0006361762,"teacher_disagreement_score":0.03961903,"about_ca_system_score_codex":0.0011540982,"about_ca_system_score_gemma":0.0005301917,"threshold_uncertainty_score":0.99949014},"labels":[],"label_agreement":null},{"id":"W2326278724","doi":"10.1021/ie500294k","title":"Hydrogen Production in a Sorption-Enhanced Fluidized-Bed Membrane Reactor: Operating Parameter Investigation","year":2014,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":31,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"University of British Columbia; China Scholarship Council","keywords":"Sorbent; Sorption; Fluidized bed; Membrane reactor; Membrane; Chemical engineering; Steam reforming; Hydrogen production; Chemistry; Materials science; Chromatography; Waste management; Hydrogen; Adsorption; Organic chemistry","score_opus":0.06654508653070451,"score_gpt":0.3054585626572522,"score_spread":0.23891347612654767,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2326278724","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985339,0.000036898884,0.000033017594,0.00016404722,0.00022279758,0.00039532463,0.0000038722706,0.000276738,0.0003333787],"genre_scores_gemma":[0.99758697,0.000008938667,0.000093238225,0.000003744811,0.0016244488,0.00019087478,0.000104262144,0.00008919932,0.0002983065],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99687207,0.00009198713,0.00067265745,0.000668185,0.0008343487,0.00086073],"domain_scores_gemma":[0.9983948,0.00048734967,0.000081086175,0.0006035917,0.00016952805,0.00026364662],"candidate_categories":["metaresearch","metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002600223,0.0003159115,0.00042012584,0.00026583517,0.00008104559,0.0000634839,0.00039045027,0.00051253184,0.00006993884],"category_scores_gemma":[0.0101988185,0.00033570672,0.00010302173,0.0011741441,0.00007717593,0.00036036497,0.00015426932,0.0018607439,0.000038172144],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000030309455,0.000026341275,0.00008540312,0.0001581941,0.00002857287,0.0000035845235,0.00023040596,0.009866628,0.98803186,0.000012901644,0.000016753609,0.0015090441],"study_design_scores_gemma":[0.00097017916,0.00002021496,0.0000052196447,0.000353653,0.0000098742,0.00001729876,0.000057259935,0.031053305,0.9668453,0.000022896245,0.00031379206,0.00033102502],"about_ca_topic_score_codex":0.00022949008,"about_ca_topic_score_gemma":0.0000042534793,"teacher_disagreement_score":0.021186676,"about_ca_system_score_codex":0.0007126254,"about_ca_system_score_gemma":0.000120564866,"threshold_uncertainty_score":0.9999095},"labels":[],"label_agreement":null},{"id":"W2329304768","doi":"10.1021/ie502082q","title":"Kinetic Study of Hydrogen Production by the High Temperature Water Gas Shift Reaction of Reformate Gas in Conventional and Membrane Packed Bed Reactors over Ca-Promoted CeO<sub>2</sub>–ZrO<sub>2</sub> Supported Ni–Cu Catalyst","year":2014,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Hydrogen; Chemistry; Catalytic reforming; Activation energy; Water-gas shift reaction; Packed bed; Hydrogen production; Permeation; Membrane reactor; Yield (engineering); Atmospheric temperature range; Reaction rate; Membrane; Analytical Chemistry (journal); Nuclear chemistry; Chemical engineering; Chromatography; Materials science; Physical chemistry; Thermodynamics; Organic chemistry; Metallurgy","score_opus":0.018447061811769555,"score_gpt":0.2525812668350311,"score_spread":0.23413420502326157,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2329304768","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9986169,0.000034479057,6.545776e-7,0.00012884675,0.00020081611,0.00084802066,0.000060841685,0.00009159525,0.000017900848],"genre_scores_gemma":[0.9984602,0.000025631321,0.0000016475321,0.0000010082305,0.00041955753,0.00010900701,0.0008516414,0.00009265691,0.00003866965],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9960458,0.00014307136,0.0010653795,0.0006674055,0.0012489439,0.000829381],"domain_scores_gemma":[0.99833083,0.00019638424,0.00022035968,0.0007807602,0.00025417595,0.00021747312],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00242039,0.0004423622,0.00068706437,0.00032131493,0.000101246136,0.000036278732,0.00040767997,0.0005879341,0.00001787294],"category_scores_gemma":[0.0010938032,0.00034312354,0.0001187625,0.0009760629,0.00016995565,0.0003026956,0.00024642746,0.0019133415,0.0000042647266],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00026726033,0.0002562312,0.00027904168,0.00042685447,0.00018298964,0.000010067862,0.0004695194,0.0005783258,0.9970413,0.0000027675387,0.000042474803,0.00044320658],"study_design_scores_gemma":[0.0026555264,0.00012246927,0.00028189184,0.0002834925,0.000078251614,0.000053719665,0.00021217826,0.0011891837,0.99471635,0.000010477026,0.000059282018,0.0003371917],"about_ca_topic_score_codex":0.0013986477,"about_ca_topic_score_gemma":0.000044210603,"teacher_disagreement_score":0.002388266,"about_ca_system_score_codex":0.0004455288,"about_ca_system_score_gemma":0.00008387825,"threshold_uncertainty_score":0.99990207},"labels":[],"label_agreement":null},{"id":"W2329446590","doi":"10.1021/ef502073b","title":"Multiobjective Optimization of Methanol Synthesis Loop from Synthesis Gas via a Multibed Adiabatic Reactor with Additional Interstage CO<sub>2</sub>Quenching","year":2014,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Flue gas; Syngas; Natural gas; Methanol; Environmental science; Process engineering; Carbon dioxide; Waste management; Greenhouse gas; Combustion; Methanol reformer; Steam reforming; Chemistry; Hydrogen production; Catalysis; Engineering; Organic chemistry","score_opus":0.0067414005233339515,"score_gpt":0.19822631382373607,"score_spread":0.19148491330040213,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2329446590","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.78162736,0.000048638627,0.21628591,0.000019330395,0.00008883772,0.00014581301,0.0006761501,0.00020191484,0.0009060261],"genre_scores_gemma":[0.9870056,0.000020468344,0.011732242,0.000026730122,0.00017580875,0.00034671402,0.000544774,0.00011550692,0.000032185406],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99792755,0.00015842411,0.00054621353,0.0005206444,0.00045963732,0.00038753916],"domain_scores_gemma":[0.99556774,0.0032370917,0.00040033532,0.00048070206,0.0001410673,0.00017303968],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00025413578,0.00039070315,0.00065049337,0.00031838828,0.000066877416,0.000021076828,0.0002748534,0.00019887237,0.0009413215],"category_scores_gemma":[0.0020681736,0.00034738152,0.00021795406,0.00031107044,0.0001049355,0.0003986005,0.00006854964,0.00023220554,0.000023541454],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000101257945,0.000091525304,0.000016983815,0.0000698909,0.0004152737,0.0000073778365,0.0003021621,0.0154535035,0.9662802,0.00007465561,0.000015339128,0.017171837],"study_design_scores_gemma":[0.00037602973,0.00004121773,0.00004246746,0.00060322206,0.00020438693,0.0000102738195,0.00010526954,0.077919945,0.92015994,0.000059249716,0.000099494646,0.00037848737],"about_ca_topic_score_codex":0.00062813226,"about_ca_topic_score_gemma":0.00012886948,"teacher_disagreement_score":0.2053782,"about_ca_system_score_codex":0.00032938767,"about_ca_system_score_gemma":0.000048263144,"threshold_uncertainty_score":0.9999719},"labels":[],"label_agreement":null},{"id":"W2331619376","doi":"10.1021/ie4006589","title":"Steady-State Simulation of a Novel Annular Multitubular Reactor for Enhanced Methanol Production","year":2013,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Methanol; Syngas; Exothermic reaction; Air preheater; Chemical engineering; Catalysis; Methanol reformer; Materials science; Chemistry; Steam reforming; Organic chemistry; Hydrogen production","score_opus":0.1016950518601607,"score_gpt":0.3486410382856815,"score_spread":0.2469459864255208,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2331619376","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9894281,0.00005850652,0.008568712,0.000059678026,0.00025916917,0.001270704,0.000045186585,0.00019209883,0.00011786319],"genre_scores_gemma":[0.996908,0.0000039951096,0.0005355904,7.54121e-7,0.00087285414,0.0003821215,0.00008671531,0.000095587064,0.0011143482],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99737436,0.00001871392,0.0006252737,0.0005115447,0.00073217385,0.00073791196],"domain_scores_gemma":[0.9977681,0.0005681484,0.0001317925,0.0005791299,0.0007469385,0.00020589773],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0011067551,0.00027756218,0.00042588997,0.00020444846,0.00005612407,0.00003402776,0.00036457556,0.0003898369,0.000067760026],"category_scores_gemma":[0.0062349318,0.0002853931,0.00016270936,0.000715462,0.00006525557,0.00035099496,0.0001262146,0.00089572737,0.000012177827],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000051550574,0.00007108705,0.000004949132,0.0003279365,0.00007488951,6.0533364e-7,0.0001430875,0.20693213,0.79036003,0.00000419162,0.000018911413,0.0020106172],"study_design_scores_gemma":[0.0010727204,0.000029519011,0.000003682747,0.00018619996,0.000015534288,0.0000029964408,0.000057943875,0.20061208,0.7968429,0.0000083074965,0.0009475237,0.00022061958],"about_ca_topic_score_codex":0.0001812239,"about_ca_topic_score_gemma":4.8822943e-7,"teacher_disagreement_score":0.008033122,"about_ca_system_score_codex":0.00038617055,"about_ca_system_score_gemma":0.00010402562,"threshold_uncertainty_score":0.9999598},"labels":[],"label_agreement":null},{"id":"W2332730727","doi":"10.1021/acs.iecr.5b02918","title":"Dynamic Optimization of Lurgi Type Methanol Reactor Using Hybrid GA-GPS Algorithm: The Optimal Shell Temperature Trajectory and Carbon Dioxide Utilization","year":2015,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":34,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Syngas; Process engineering; Computer science; Natural gas; Methane; Methanol; Raw material; Space velocity; Environmental science; Algorithm; Materials science; Chemistry; Engineering; Catalysis; Organic chemistry","score_opus":0.09709378651913127,"score_gpt":0.32829385141087697,"score_spread":0.23120006489174572,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2332730727","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99739516,0.0008173902,0.000811512,0.000032471857,0.00027376667,0.00033768316,0.00003557472,0.00012805608,0.0001683757],"genre_scores_gemma":[0.99762684,0.000058947455,0.0012690936,0.000001197779,0.0005158547,0.000019902196,0.00013377385,0.00010914661,0.0002652501],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977314,0.00006449679,0.00045130728,0.00039774386,0.0008089338,0.00054610096],"domain_scores_gemma":[0.99851143,0.00026437943,0.0000996655,0.0004640806,0.00040666407,0.0002537746],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013440411,0.0002850602,0.0003707733,0.00016664095,0.000056688306,0.000041502277,0.0003545328,0.00039531343,0.000019008352],"category_scores_gemma":[0.0018878963,0.00024833105,0.00007384322,0.0009094648,0.00011183995,0.0001698954,0.00019939494,0.001337118,8.0351595e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047564306,0.000017948381,0.0000110656065,0.00007929145,0.00005583527,0.000010581996,0.00010373598,0.23472689,0.76440567,0.0000014054883,0.0000081929675,0.0005318061],"study_design_scores_gemma":[0.00043170244,0.000019428408,0.0000011664379,0.000099925266,0.000025992147,0.000047309164,0.0001023355,0.45204622,0.5469436,9.1906736e-7,0.00014300075,0.00013844052],"about_ca_topic_score_codex":0.00019644019,"about_ca_topic_score_gemma":4.6611538e-7,"teacher_disagreement_score":0.21746211,"about_ca_system_score_codex":0.00055743026,"about_ca_system_score_gemma":0.0002898812,"threshold_uncertainty_score":0.9999969},"labels":[],"label_agreement":null},{"id":"W2332846523","doi":"10.1021/ie503496m","title":"Conversion of CO<sub>2</sub>over a Co-Based Fischer–Tropsch Catalyst","year":2015,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":47,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Resources Canada; Helmholtz-Alberta Initiative; Helmholtz-Gemeinschaft; University of Alberta","keywords":"Fischer–Tropsch process; Syngas; Catalysis; Carbon dioxide; Water-gas shift reaction; Methane; Chemistry; Hydrocarbon; Carbon fibers; Chemical engineering; Selectivity; Inorganic chemistry; Organic chemistry; Materials science","score_opus":0.0891492441152462,"score_gpt":0.3321487211507758,"score_spread":0.2429994770355296,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2332846523","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99762595,0.0001300925,0.00009413107,0.000055579112,0.00018165995,0.00029343428,0.00010236499,0.00022421195,0.0012925623],"genre_scores_gemma":[0.998486,0.0000055274454,0.000030694944,0.0000034404047,0.00078831107,0.000048089685,0.00028971877,0.000109149085,0.0002390981],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9961555,0.000050949213,0.0006489762,0.0005297494,0.0016397139,0.00097511464],"domain_scores_gemma":[0.99753207,0.0004942612,0.0001275252,0.00079346506,0.00038473195,0.0006679352],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0019018833,0.00037834607,0.00058631157,0.000274028,0.00006619816,0.00004017726,0.00069372344,0.00069744955,0.00009787866],"category_scores_gemma":[0.0027560468,0.0003960818,0.0002186716,0.0010376072,0.00017366499,0.00019520329,0.0001978277,0.0019314357,0.00008163185],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017975048,0.00007612826,0.0003596194,0.00037534806,0.00009006684,0.00004712681,0.000070304406,0.006836934,0.99022996,0.000006249129,0.0013603051,0.0003682157],"study_design_scores_gemma":[0.0028306432,0.000055637585,0.000012425779,0.0002343347,0.000027132455,0.00001953289,0.000089741676,0.016748533,0.9715793,0.0000017164467,0.008027953,0.00037305287],"about_ca_topic_score_codex":0.00019412306,"about_ca_topic_score_gemma":5.908934e-7,"teacher_disagreement_score":0.018650655,"about_ca_system_score_codex":0.0008906136,"about_ca_system_score_gemma":0.00055641145,"threshold_uncertainty_score":0.9998491},"labels":[],"label_agreement":null},{"id":"W2333272809","doi":"10.1021/cs500918c","title":"Nanocast LaNiO<sub>3</sub> Perovskites as Precursors for the Preparation of Coke-Resistant Dry Reforming Catalysts","year":2014,"lang":"en","type":"article","venue":"ACS Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":182,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada; Fonds Québécois de la Recherche sur la Nature et les Technologies","keywords":"Catalysis; Perovskite (structure); Lanio; Carbon dioxide reforming; Materials science; Coke; Mesoporous material; Chemical engineering; Hydrogen; Specific surface area; Syngas; Methane; Steam reforming; Mesoporous silica; Hydrogen production; Chemistry; Metallurgy; Organic chemistry","score_opus":0.008393412339782393,"score_gpt":0.24739543536770528,"score_spread":0.2390020230279229,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2333272809","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99492073,0.00054834515,0.0028887922,0.00013417233,0.00016363585,0.0005315712,0.00006145406,0.00014928062,0.0006019995],"genre_scores_gemma":[0.9982858,0.000040684306,0.00025707931,0.000035757206,0.00021120807,0.00020748486,0.00056534354,0.00008153262,0.00031514931],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977048,0.000039079154,0.000745764,0.00049629685,0.0005115245,0.0005025401],"domain_scores_gemma":[0.9973921,0.00079455745,0.0004149532,0.0010720604,0.00021886933,0.00010742913],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00091106334,0.0003473516,0.0005748837,0.00021442185,0.00022559454,0.0000328649,0.00057945313,0.0001834288,0.0000063991415],"category_scores_gemma":[0.0013720148,0.00025352064,0.00041999455,0.000607107,0.00011576374,0.00038324978,0.00017936713,0.00020187697,0.000050193874],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001370204,0.000046997455,0.00012453277,0.0002357946,0.0003466854,9.957098e-7,0.0011128833,0.00069858617,0.9826084,0.00051381753,0.000064394066,0.014109907],"study_design_scores_gemma":[0.0004711992,0.00009958069,0.000095526666,0.00009728854,0.00056134677,0.000011225405,0.00035539904,0.0069826087,0.98842764,0.00010747622,0.0024688311,0.00032189878],"about_ca_topic_score_codex":0.0007564409,"about_ca_topic_score_gemma":0.0005737139,"teacher_disagreement_score":0.013788008,"about_ca_system_score_codex":0.00020581554,"about_ca_system_score_gemma":0.000057008074,"threshold_uncertainty_score":0.9999917},"labels":[],"label_agreement":null},{"id":"W2336768476","doi":"10.1002/cjce.22429","title":"Kinetics of low‐temperature Fischer‐Tropsch synthesis on cobalt catalysts: Are both slurry autoclave and tubular packed‐bed reactors adequate to collect relevant data at lab‐scale?","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Fischer–Tropsch process; Autoclave; Packed bed; Slurry; Syngas; Plug flow; Cobalt; Chemical engineering; Plug flow reactor model; Product distribution; Catalysis; Volumetric flow rate; Materials science; Chemistry; Space velocity; Continuous stirred-tank reactor; Waste management; Thermodynamics; Chromatography; Metallurgy; Organic chemistry; Composite material; Engineering","score_opus":0.011470836486324895,"score_gpt":0.20576912633548575,"score_spread":0.19429828984916087,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2336768476","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99703556,0.0005235353,0.00005582526,0.0016022952,0.00019332164,0.0001803936,0.00032776664,0.000031419324,0.00004987418],"genre_scores_gemma":[0.9990233,0.000017659273,0.00038453646,0.00005148463,0.00026103575,0.0000075741714,0.00001542382,0.00009626567,0.00014270016],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99778944,0.000031566244,0.0007383893,0.0003387976,0.00046827187,0.00063354115],"domain_scores_gemma":[0.9969786,0.0006691011,0.000289682,0.00090601,0.00015416327,0.0010024348],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045435963,0.00037851065,0.0006921778,0.0002869871,0.00006479378,0.000033290828,0.000915784,0.00025717544,0.000040457355],"category_scores_gemma":[0.0028881049,0.00024474825,0.00014759315,0.0004457241,0.0001088978,0.0001720746,0.00018616376,0.0006016573,0.000007947024],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000078655095,0.000012836249,0.00006110769,0.00012779006,0.00018575265,0.00009057969,0.00026044037,0.0005009608,0.9977142,0.00007952241,0.00054349983,0.0003446267],"study_design_scores_gemma":[0.00045489214,0.00005773332,0.00009640678,0.0015161058,0.00013749229,0.00025032816,0.000044597662,0.00066688936,0.9946891,0.000008843305,0.0017350732,0.00034253037],"about_ca_topic_score_codex":0.00055757177,"about_ca_topic_score_gemma":0.000465455,"teacher_disagreement_score":0.0030251208,"about_ca_system_score_codex":0.0010102796,"about_ca_system_score_gemma":0.00016114293,"threshold_uncertainty_score":0.99805444},"labels":[],"label_agreement":null},{"id":"W2338828269","doi":"10.1002/cjce.22519","title":"Effects of particle size on the catalytic performance of MWCNTs supported alkalized MoS<sub>2</sub> catalysts promoted by Ni and Co in higher alcohols synthesis","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Microemulsion; Particle size; Selectivity; Materials science; Chemical engineering; Syngas; Chemisorption; Carbon nanotube; Incipient wetness impregnation; Particle (ecology); Metal; Pulmonary surfactant; Nuclear chemistry; Chemistry; Nanotechnology; Organic chemistry; Metallurgy","score_opus":0.007769422745933759,"score_gpt":0.18858498316839964,"score_spread":0.18081556042246588,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2338828269","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9989637,0.00022931842,0.0000099328,0.0005001556,0.00006018144,0.00018386007,0.000019144562,0.000011518719,0.000022150944],"genre_scores_gemma":[0.99983263,0.0000120834675,0.00001789146,0.000017445203,0.00003641301,0.00001430964,0.0000014935313,0.00004228963,0.000025442348],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998474,0.0000276791,0.0006126494,0.00014364292,0.00030270885,0.00043933495],"domain_scores_gemma":[0.99782574,0.001273761,0.00024261902,0.00027348893,0.000070880036,0.00031350987],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005462582,0.0002211983,0.000483466,0.000117020216,0.00002741829,0.000009726843,0.00037818548,0.000118844684,0.000014895827],"category_scores_gemma":[0.001673633,0.00012561862,0.00010909415,0.00032996587,0.00014112258,0.00013972039,0.000028402974,0.0003238963,0.0000024156298],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000489018,0.000017068518,0.00024880213,0.00019075988,0.00010265854,0.000018031826,0.00015199452,0.00011746942,0.9979632,0.000052768908,0.000028744344,0.0010596255],"study_design_scores_gemma":[0.000746198,0.000037414673,0.0005979564,0.0008462683,0.00007895528,0.00005034155,0.000005133869,0.0014664417,0.9959831,0.000010839337,0.000020587162,0.0001567273],"about_ca_topic_score_codex":0.0004024392,"about_ca_topic_score_gemma":0.000031578373,"teacher_disagreement_score":0.0019800381,"about_ca_system_score_codex":0.00026997598,"about_ca_system_score_gemma":0.0001183795,"threshold_uncertainty_score":0.5122579},"labels":[],"label_agreement":null},{"id":"W2339802542","doi":"10.1007/s10562-016-1747-0","title":"Effect of H2S in Syngas on the Fischer–Tropsch Synthesis Performance of a 0.5%Pt–25%Co–Al2O3 Catalyst","year":2016,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"U.S. Department of Energy","keywords":"Syngas; Chemistry; Fischer–Tropsch process; Catalysis; Selectivity; Cobalt; Hydrocarbon; Sulfur; Space velocity; Inorganic chemistry; Organic chemistry","score_opus":0.006486047009096363,"score_gpt":0.21656509075872443,"score_spread":0.21007904374962807,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2339802542","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9982078,0.00007067703,0.00007982051,0.00080635224,0.000059334994,0.00024108554,0.000032870008,0.000045785317,0.00045625126],"genre_scores_gemma":[0.9995244,0.000022008971,0.000025126954,0.000068162204,0.00006220503,0.000115931165,0.000022123308,0.000055962602,0.0001040749],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99778414,0.00013753452,0.0006860682,0.00040807994,0.0005118264,0.00047237656],"domain_scores_gemma":[0.9963021,0.0021769432,0.00030637038,0.001095474,0.000036507197,0.00008255231],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012469303,0.00034781135,0.00078306533,0.00039410513,0.000046332814,0.000006974386,0.00068507186,0.0001238406,0.00007996878],"category_scores_gemma":[0.0012470568,0.00018947946,0.00041191964,0.00070412847,0.00021282572,0.00022006652,0.00011184324,0.00027613618,0.000093655115],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013045606,0.000037524485,0.0049121547,0.00031266548,0.0001985355,0.000008657336,0.00018640471,0.00018347365,0.98230964,0.000027152608,0.000061649334,0.011631674],"study_design_scores_gemma":[0.00046713225,0.000082647435,0.0007702436,0.00053709507,0.00018311097,0.000008363246,0.000024109586,0.00045927824,0.99698067,6.4667125e-7,0.00025246997,0.00023425347],"about_ca_topic_score_codex":0.00021430495,"about_ca_topic_score_gemma":0.000011807127,"teacher_disagreement_score":0.014670998,"about_ca_system_score_codex":0.00024417078,"about_ca_system_score_gemma":0.000019037243,"threshold_uncertainty_score":0.7726748},"labels":[],"label_agreement":null},{"id":"W2343119552","doi":"10.14447/jnmes.v15i3.60","title":"Effect of WO&lt;sub&gt;x&lt;/sub&gt; Over Ni/Hydrotalcite Catalysts to Produce Hydrogen from Ethanol","year":2012,"lang":"en","type":"article","venue":"Journal of New Materials for Electrochemical Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Hydrotalcite; Catalysis; Physisorption; Hydrogen production; Ethanol; Hydrogen; Nuclear chemistry; Chemistry; Inorganic chemistry; Materials science; Organic chemistry","score_opus":0.00825315776338012,"score_gpt":0.24946832842486008,"score_spread":0.24121517066147996,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2343119552","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99377215,0.00246812,0.0006562795,0.000055138833,0.0015746556,0.001244378,0.00009670332,0.00008379325,0.000048766306],"genre_scores_gemma":[0.99471694,0.000026620331,0.000111379755,0.000020687505,0.0046048644,0.00009626477,0.00009870419,0.00017778852,0.00014674597],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99483514,0.00015598585,0.0021119965,0.00047494555,0.0011851555,0.0012367626],"domain_scores_gemma":[0.9963925,0.00048253816,0.001349049,0.00064081367,0.00030061902,0.00083450077],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0023446574,0.0006573833,0.002016086,0.00032335558,0.00005583935,0.00006395658,0.0007510989,0.0004744841,0.000033152046],"category_scores_gemma":[0.0015716867,0.00052399345,0.00057967275,0.00045739952,0.000038404487,0.0005415162,0.00018017959,0.00036225814,0.000041052914],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0013183124,0.00009287402,0.00005311606,0.000905553,0.0005807459,0.000006845344,0.00026974126,0.000039860268,0.9953986,0.000023977856,0.00095690624,0.0003534738],"study_design_scores_gemma":[0.0019159499,0.0005844845,0.000014517291,0.00078864413,0.0004639727,0.00035593082,0.0000055977584,0.00007160089,0.992288,0.000031628737,0.002945808,0.00053386344],"about_ca_topic_score_codex":0.00012774218,"about_ca_topic_score_gemma":0.000003417121,"teacher_disagreement_score":0.003110592,"about_ca_system_score_codex":0.00078674406,"about_ca_system_score_gemma":0.00013127581,"threshold_uncertainty_score":0.99972117},"labels":[],"label_agreement":null},{"id":"W2346500448","doi":"10.14447/jnmes.v16i3.23","title":"Thermodynamic Analysis of the Absorption Enhanced Autothermal Reforming of Ethanol","year":2013,"lang":"en","type":"article","venue":"Journal of New Materials for Electrochemical Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Methane reformer; Stoichiometry; Ethanol; Chemistry; Hydrogen; Hydrogen production; Absorption (acoustics); Oxygen; Steam reforming; Carbon fibers; Nuclear chemistry; Inorganic chemistry; Materials science; Organic chemistry","score_opus":0.009089888084133753,"score_gpt":0.23791785592574938,"score_spread":0.22882796784161563,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2346500448","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99199116,0.0001904271,0.0069729956,0.00003585434,0.00033380653,0.0003708104,0.000013372612,0.000015704509,0.00007587945],"genre_scores_gemma":[0.99932575,0.000011321138,0.00009208614,0.0000054236048,0.00028269688,0.000018744659,0.000008925785,0.00003641186,0.00021865568],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99751335,0.000044006418,0.0014660322,0.00014377666,0.00050768023,0.00032516007],"domain_scores_gemma":[0.99740565,0.00012929358,0.0016500357,0.00030504825,0.00041542717,0.00009455742],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006107674,0.00019822443,0.0009875161,0.00023596047,0.000024176705,0.000016587734,0.00047797605,0.00019393986,0.00007454016],"category_scores_gemma":[0.0002979475,0.00012278238,0.0005795277,0.00051665166,0.00003748478,0.00020225202,0.000049059698,0.00016033505,0.000001831061],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001075692,0.000029346973,0.0000112109665,0.0002460959,0.0009110345,1.360954e-7,0.0001989383,0.00032663977,0.99775845,0.00010168499,0.000011279949,0.00029760753],"study_design_scores_gemma":[0.00052890234,0.00008307477,0.00012781912,0.00023941453,0.00065984897,0.000027824215,0.000058912065,0.0038372355,0.99415314,0.00012582265,0.000030634223,0.0001273473],"about_ca_topic_score_codex":0.00032540888,"about_ca_topic_score_gemma":0.000002956746,"teacher_disagreement_score":0.007334585,"about_ca_system_score_codex":0.00030294576,"about_ca_system_score_gemma":0.00010429934,"threshold_uncertainty_score":0.500692},"labels":[],"label_agreement":null},{"id":"W2346691260","doi":"10.1021/acs.iecr.5b04381","title":"Effect of Pretreatment on Physicochemical Properties and Performance of Multiwalled Carbon Nanotube Supported Cobalt Catalyst for Fischer–Tropsch Synthesis","year":2016,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":45,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"Social Sciences and Humanities Research Council of Canada; Natural Sciences and Engineering Research Council of Canada; Canadian Institutes of Health Research; University of Saskatchewan","keywords":"Catalysis; Fischer–Tropsch process; Cobalt; Carbon nanotube; Nitric acid; Chemical engineering; Materials science; Space velocity; Nanotube; Dispersion (optics); Raman spectroscopy; Crystallite; Chemisorption; Nuclear chemistry; Chemistry; Inorganic chemistry; Nanotechnology; Organic chemistry; Metallurgy; Selectivity","score_opus":0.04967906362001121,"score_gpt":0.2893946400281882,"score_spread":0.239715576408177,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2346691260","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9989299,0.00009883204,0.0000032356422,0.00003548128,0.000050190876,0.000640004,0.00007018158,0.000068299596,0.00010388273],"genre_scores_gemma":[0.99898696,0.000021945838,0.000016799751,2.2608472e-7,0.00022863064,0.00036819806,0.000018982288,0.00006738724,0.00029089514],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978074,0.000038292532,0.0005034215,0.0004318099,0.00061772065,0.0006013659],"domain_scores_gemma":[0.99749666,0.0015528275,0.000108905006,0.0004854023,0.00018208913,0.00017413084],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00096743926,0.00032526415,0.00067008985,0.00011904889,0.000039219423,0.000008959401,0.00030465054,0.00035404455,0.000014051491],"category_scores_gemma":[0.0034657337,0.00021963756,0.00015372639,0.0003002421,0.00016079006,0.00007851648,0.00014560563,0.0004152268,0.0000012265714],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0013483664,0.00007394256,0.00056618155,0.0016290105,0.00020698943,0.0000023847567,0.00005342959,0.0001990791,0.9899343,0.000002317334,0.000006849645,0.0059771193],"study_design_scores_gemma":[0.0023611358,0.00046272366,0.000020242835,0.0013731024,0.00007390193,0.000007082654,0.000011824535,0.009083627,0.98633146,3.0597445e-7,0.00005121402,0.00022336747],"about_ca_topic_score_codex":0.000097379794,"about_ca_topic_score_gemma":2.637269e-7,"teacher_disagreement_score":0.008884548,"about_ca_system_score_codex":0.00034284318,"about_ca_system_score_gemma":0.000088193054,"threshold_uncertainty_score":0.895656},"labels":[],"label_agreement":null},{"id":"W2347384734","doi":"10.1002/cjce.22537","title":"Low‐temperature Fischer‐Tropsch synthesis using plasma‐synthesized nanometric Co/C and Fe/C catalysts","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; Université de Sherbrooke","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Space velocity; Cobalt; Chemistry; Particle size; Materials science; Metal; Transmission electron microscopy; Chemical engineering; Analytical Chemistry (journal); Nuclear chemistry; Inorganic chemistry; Physical chemistry; Metallurgy; Nanotechnology; Selectivity; Organic chemistry","score_opus":0.009438036620815795,"score_gpt":0.19933232641183285,"score_spread":0.18989428979101705,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2347384734","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9983716,0.0006812602,0.00020714186,0.0003350535,0.00019934955,0.00008801997,0.00002853895,0.000033927154,0.00005509472],"genre_scores_gemma":[0.9988581,0.000011250919,0.000605904,0.000018487943,0.00035757673,0.0000047790863,0.0000015555343,0.000083404695,0.000058960457],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99817413,0.000024614277,0.00058686675,0.0002164913,0.00034771988,0.000650157],"domain_scores_gemma":[0.9978572,0.0006679816,0.00019799275,0.00032731038,0.00012187814,0.00082765054],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00057754817,0.00033128064,0.00055452005,0.0005371716,0.0001042137,0.000065390224,0.0005251552,0.00024727642,0.00004085814],"category_scores_gemma":[0.0028357143,0.00020329254,0.00022124195,0.00059080514,0.00012294661,0.0002941563,0.000043295055,0.00057090534,0.000008422212],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000020033118,0.00000535163,0.00005259564,0.00006936416,0.0001421933,0.00006654566,0.00010351094,0.0005203154,0.9965013,0.00006036865,0.000020939042,0.002437457],"study_design_scores_gemma":[0.0004608204,0.000010296218,0.000032755084,0.00053633354,0.000113969356,0.00090140256,0.000014993584,0.0028726787,0.9943697,0.000011425069,0.00036893124,0.0003067131],"about_ca_topic_score_codex":0.00070220174,"about_ca_topic_score_gemma":0.0000533426,"teacher_disagreement_score":0.0023523632,"about_ca_system_score_codex":0.00072292984,"about_ca_system_score_gemma":0.000308284,"threshold_uncertainty_score":0.8290029},"labels":[],"label_agreement":null},{"id":"W2372074758","doi":"","title":"Study on Three-phase Methanol Synthesis I. The Global Kinetics of Methanol Synthesis for CO-rich Synthesis Gas in Slurry Reactor","year":2000,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"CAE (Canada)","funders":"","keywords":"Methanol; Slurry; Catalysis; Methanol reformer; Hydrogen; Chemical engineering; Chemistry; Carbon monoxide; Syngas; Kinetics; Carbon dioxide; Hydrogen production; Materials science; Organic chemistry; Steam reforming; Composite material","score_opus":0.034224542421222845,"score_gpt":0.3181465473508673,"score_spread":0.2839220049296444,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2372074758","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9872514,0.00011806329,0.0006544579,0.00028185247,0.00010331718,0.0017694366,0.00033726022,0.00022592701,0.009258279],"genre_scores_gemma":[0.99697816,0.000030602223,0.00125993,0.000036662426,0.00012664348,0.0012513684,0.000007886251,0.00012347463,0.00018524854],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9960189,0.00020932023,0.0012552227,0.0007868978,0.0008536776,0.0008760165],"domain_scores_gemma":[0.99080116,0.007205157,0.00027116155,0.0014130522,0.00011156745,0.00019792593],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013609496,0.0006524796,0.0012696055,0.00029413938,0.00008043683,0.000033657063,0.0010408422,0.0003087013,0.00090884464],"category_scores_gemma":[0.005079785,0.0004567919,0.00048515724,0.0010247927,0.00012643299,0.00018686111,0.00010616983,0.0003432572,0.00008697992],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0016154012,0.0060881916,0.002415694,0.00043627294,0.0017492233,0.000077410616,0.0011837081,0.00066416943,0.5458549,0.00089049205,0.00010825553,0.43891624],"study_design_scores_gemma":[0.0010304915,0.00029792936,0.00081736903,0.00022986601,0.0007193499,0.000020131736,0.0011013784,0.0014663559,0.9928203,0.00015272753,0.0007668918,0.0005771818],"about_ca_topic_score_codex":0.00062233367,"about_ca_topic_score_gemma":0.00056519744,"teacher_disagreement_score":0.44696537,"about_ca_system_score_codex":0.00054665975,"about_ca_system_score_gemma":0.00005405243,"threshold_uncertainty_score":0.9997884},"labels":[],"label_agreement":null},{"id":"W2375679711","doi":"","title":"DIMETHYL ETHER SYNTHESIS FROM SYNGAS DERIVED FROM BIOMASS GASIFICATION AND REFORMING","year":2004,"lang":"en","type":"article","venue":"Ranliao huaxue xuebao","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Syngas; Chemistry; Dimethyl ether; Biomass (ecology); Syngas to gasoline plus; Sawdust; Methanol; Organic chemistry; Ether; Chemical engineering; Hydrogen; Steam reforming; Hydrogen production","score_opus":0.014516313922356352,"score_gpt":0.2297617114417471,"score_spread":0.21524539751939073,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2375679711","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9892134,0.0014146107,0.0073826034,0.00034974486,0.00022853489,0.00022072354,0.00010819605,0.00035095186,0.00073122204],"genre_scores_gemma":[0.99161285,0.00006353774,0.007470642,0.000045779943,0.0003031737,0.00006376646,0.00012844909,0.00010929186,0.00020248986],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99801356,0.000032212654,0.00049575587,0.0006248612,0.000344349,0.0004892604],"domain_scores_gemma":[0.99847364,0.00040849703,0.00016932515,0.00067614234,0.000052565025,0.00021982477],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00025252238,0.00036898628,0.00050060195,0.00016088353,0.000146759,0.000050095307,0.00031572956,0.00029707127,0.0001373894],"category_scores_gemma":[0.00045034743,0.00033455054,0.00016282815,0.00029226387,0.000091360474,0.00043350374,0.00012735902,0.000322539,0.00018720646],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000046314868,0.00004487469,0.00020310907,0.000036507077,0.0001491737,0.000017838933,0.00080985465,0.000067705,0.9842077,0.00030900852,0.0000022289,0.0141056925],"study_design_scores_gemma":[0.0009267778,0.000014131976,0.0014217425,0.00025807886,0.0001535898,0.000010110631,0.00032149555,0.00071947224,0.9918691,0.0026876903,0.0011598237,0.00045798346],"about_ca_topic_score_codex":0.008487042,"about_ca_topic_score_gemma":0.00020390486,"teacher_disagreement_score":0.013647709,"about_ca_system_score_codex":0.0003578364,"about_ca_system_score_gemma":0.000033618213,"threshold_uncertainty_score":0.99991065},"labels":[],"label_agreement":null},{"id":"W2397956406","doi":"10.1039/c6ta02809h","title":"Toward highly efficient in situ dry reforming of H<sub>2</sub>S contaminated methane in solid oxide fuel cells via incorporating a coke/sulfur resistant bimetallic catalyst layer","year":2016,"lang":"en","type":"article","venue":"Journal of Materials Chemistry A","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":33,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Alberta Innovates; National Institute for Nanotechnology; Alberta Hospital Edmonton; University of Alberta","funders":"Universiteit van Amsterdam; Climate Change and Emissions Management Corporation","keywords":"Bimetallic strip; Coke; Methane; Catalysis; Sulfur; Materials science; Oxide; In situ; Methane reformer; Carbon dioxide reforming; Contamination; Chemical engineering; Layer (electronics); Waste management; Chemistry; Metallurgy; Syngas; Nanotechnology; Steam reforming; Organic chemistry; Engineering; Hydrogen production","score_opus":0.011488795212504208,"score_gpt":0.22655443359709376,"score_spread":0.21506563838458956,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2397956406","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99892116,0.00024928537,0.0002248027,0.000058017373,0.00019822438,0.0001726573,0.000049106442,0.000030699324,0.000096029304],"genre_scores_gemma":[0.99920183,0.00005120444,0.00044532504,0.000007681889,0.00015121486,0.000012572742,0.000017172177,0.00007148006,0.000041533232],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.995723,0.00009556432,0.0026007786,0.0003589448,0.000632839,0.0005888823],"domain_scores_gemma":[0.9969761,0.0002427243,0.0018983764,0.00041184723,0.00025903163,0.00021196956],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0023376243,0.00042686614,0.0013893639,0.00034679144,0.000021011643,0.00002203712,0.00050882954,0.00032307132,0.000026657171],"category_scores_gemma":[0.00067474536,0.00031289083,0.00023761675,0.0005096188,0.00009868417,0.00028048703,0.00023024979,0.00037324085,0.000009285378],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006490038,0.0001628394,0.00002353918,0.0011510636,0.00010556491,0.0004671417,0.00033902552,0.0003422094,0.9963669,0.000004898411,0.0000010084918,0.00038680207],"study_design_scores_gemma":[0.0026341681,0.000052820353,0.000080037156,0.0021227049,0.00007946552,0.00020151073,0.00023018956,0.0000684368,0.9940844,0.000058372338,0.000013326532,0.00037457974],"about_ca_topic_score_codex":0.000170328,"about_ca_topic_score_gemma":0.000029501747,"teacher_disagreement_score":0.0022825152,"about_ca_system_score_codex":0.0008907779,"about_ca_system_score_gemma":0.00017625009,"threshold_uncertainty_score":0.9999323},"labels":[],"label_agreement":null},{"id":"W2400221730","doi":"10.1007/978-3-319-17031-2_44","title":"Hydrogen Production from Nuclear Energy: Comparative Cost Assessment","year":2015,"lang":"en","type":"book-chapter","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Production (economics); Hydrogen production; Environmental science; Hydrogen; Nuclear engineering; Chemistry; Economics; Engineering; Macroeconomics","score_opus":0.055633691559386876,"score_gpt":0.2857331890256632,"score_spread":0.2300994974662763,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2400221730","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0008171566,0.00037295822,0.000374043,0.00007252815,0.00045694894,0.00026755148,0.00008957912,0.0004015356,0.9971477],"genre_scores_gemma":[0.048334636,0.000054592605,0.0010679321,0.000041148618,0.0013472389,0.000027018199,0.0015185028,0.0002228338,0.9473861],"study_design_codex":"theoretical_or_conceptual","study_design_gemma":"not_applicable","domain_scores_codex":[0.99826294,0.000008304164,0.0004037719,0.00055669085,0.00052499655,0.00024331406],"domain_scores_gemma":[0.9988637,0.000033732667,0.00019868359,0.0005762737,0.00013641243,0.00019119501],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00012506143,0.00043298004,0.00063757936,0.000120597724,0.000043647065,0.00001580706,0.0002419514,0.0003514496,0.0018137674],"category_scores_gemma":[0.000015852798,0.00038805194,0.00018453292,0.000032941367,0.000052999607,0.00014797512,0.00018551348,0.00047991695,0.0005094798],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000121466095,0.00013359376,0.0000036247409,0.00012095922,0.0027460423,0.00007664798,0.00093267043,0.001825508,0.20810406,0.73791575,0.023081116,0.024938589],"study_design_scores_gemma":[0.00026824328,0.000025473219,5.015398e-7,0.00014605407,0.00017411225,0.000015780495,0.000049575207,0.0031530038,0.041638147,0.004244204,0.9496722,0.0006126855],"about_ca_topic_score_codex":0.00043493055,"about_ca_topic_score_gemma":0.00007321576,"teacher_disagreement_score":0.9265911,"about_ca_system_score_codex":0.000877424,"about_ca_system_score_gemma":0.000070932496,"threshold_uncertainty_score":0.9998571},"labels":[],"label_agreement":null},{"id":"W2467066661","doi":"10.1002/aic.15391","title":"A comparative computational study of diesel steam reforming in a catalytic plate heat‐exchange reactor","year":2016,"lang":"en","type":"article","venue":"AIChE Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Queen's University; Royal Military College of Canada","funders":"Natural Sciences and Engineering Research Council of Canada; Ministère de la Défense Nationale","keywords":"Steam reforming; Space velocity; Flue gas; Diesel fuel; Catalysis; Chemistry; Endothermic process; Methane reformer; Combustor; Thermodynamics; Hydrogen production; Chemical engineering; Nuclear engineering; Waste management; Combustion; Engineering; Physical chemistry; Organic chemistry; Physics","score_opus":0.03500400365411119,"score_gpt":0.29603516481284814,"score_spread":0.2610311611587369,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2467066661","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99848515,0.00019319911,0.0005192903,0.00007661934,0.00010010816,0.00019006028,0.000010923581,0.000025962323,0.00039868156],"genre_scores_gemma":[0.99947613,0.000015168759,0.00015891665,0.000008406968,0.00012287592,0.000010127111,0.0000043388227,0.00002343232,0.00018060778],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983359,0.00004918995,0.0006663326,0.00018158589,0.00043647573,0.00033050094],"domain_scores_gemma":[0.99908704,0.00027282955,0.00020941948,0.00018134475,0.00011834863,0.0001310276],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005687435,0.00018514878,0.00048590897,0.00030850523,0.000047916976,0.000008055787,0.00022619983,0.0000679106,0.000042099895],"category_scores_gemma":[0.00014288747,0.00011881212,0.000091986054,0.00029670153,0.000038676262,0.0003894283,0.000107788816,0.00037738986,0.000019914605],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008573544,0.0022119917,0.01849992,0.00026582653,0.0011322446,0.0003839622,0.067953356,0.008363384,0.87996036,0.0001224203,0.00014168106,0.020107474],"study_design_scores_gemma":[0.059177235,0.0046669426,0.07775123,0.0066803433,0.00075323076,0.004881332,0.058898438,0.055602558,0.7223095,0.0024891633,0.0029811105,0.003808894],"about_ca_topic_score_codex":0.000244607,"about_ca_topic_score_gemma":0.00018565798,"teacher_disagreement_score":0.15765086,"about_ca_system_score_codex":0.00047877562,"about_ca_system_score_gemma":0.000060394486,"threshold_uncertainty_score":0.48450175},"labels":[],"label_agreement":null},{"id":"W2467601336","doi":"10.1021/acscatal.6b01464","title":"Zinc Hinders Deactivation of Copper-Mordenite: Dimethyl Ether Carbonylation","year":2016,"lang":"en","type":"article","venue":"ACS Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":55,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Canada Foundation for Innovation; Natural Sciences and Engineering Research Council of Canada; Enerkem","keywords":"Mordenite; Dimethyl ether; Chemistry; Carbonylation; Catalysis; Zinc; Methanol; Acetic acid; Copper; Inorganic chemistry; Methane; Organic chemistry; Zeolite; Carbon monoxide","score_opus":0.011886733528662298,"score_gpt":0.23644003860027668,"score_spread":0.2245533050716144,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2467601336","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99171376,0.000103239196,0.0062172906,0.00021166218,0.00008824619,0.00010081175,0.000008632041,0.00010382099,0.0014525094],"genre_scores_gemma":[0.9983988,0.000013942469,0.0003329124,0.000013628122,0.00007826333,0.000015689067,0.00007713402,0.000042807726,0.0010268616],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99873877,0.000023009969,0.0003848571,0.00025766337,0.00036031986,0.00023541362],"domain_scores_gemma":[0.99890405,0.00025040813,0.00019745031,0.00047787005,0.00009990403,0.00007033102],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026449468,0.00016806799,0.00029804566,0.00023199775,0.00003344754,0.00000550235,0.00018724677,0.00014233841,0.00007278847],"category_scores_gemma":[0.0004895671,0.00012139574,0.0001559424,0.0004937128,0.000053066502,0.00033188335,0.00007022327,0.00010519043,0.000047903563],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017052525,0.000022123306,0.0013089922,0.00002677642,0.00013984377,0.0000010202011,0.0002991195,0.000098200144,0.9669934,0.00028480025,0.000017319422,0.030791363],"study_design_scores_gemma":[0.00040701567,0.000012447673,0.0006502597,0.00004920326,0.00013149297,0.0000035672042,0.00007577974,0.0003592249,0.9972194,0.00019977542,0.0007033822,0.0001884494],"about_ca_topic_score_codex":0.00055250386,"about_ca_topic_score_gemma":0.000039989038,"teacher_disagreement_score":0.030602913,"about_ca_system_score_codex":0.0002284271,"about_ca_system_score_gemma":0.000023774319,"threshold_uncertainty_score":0.49503744},"labels":[],"label_agreement":null},{"id":"W2468361866","doi":"10.1039/c6ra10150j","title":"Fischer–Tropsch synthesis: effect of Cu, Mn and Zn addition on activity and product selectivity of cobalt ferrite","year":2016,"lang":"en","type":"article","venue":"RSC Advances","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); Saskatoon Medical Imaging","funders":"","keywords":"Fischer–Tropsch process; Cobalt; Selectivity; Catalysis; Ferrite (magnet); Cobalt ferrite; Chemistry; Manganese; Inorganic chemistry; Materials science; Nuclear chemistry; Organic chemistry","score_opus":0.007049504921287424,"score_gpt":0.2436594125763722,"score_spread":0.23660990765508477,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2468361866","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99823374,0.00083379576,0.00032346245,0.000055046108,0.00004034268,0.00016252663,0.0000772528,0.00004145249,0.00023235937],"genre_scores_gemma":[0.9994527,0.00021762484,0.00017371692,0.000001174801,0.000053722488,0.00002774272,0.0000023247298,0.000016112685,0.00005487278],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992117,0.000055997545,0.00014520479,0.0002595214,0.0001647971,0.00016272615],"domain_scores_gemma":[0.9987845,0.0008221293,0.00013200565,0.00018044333,0.000031420266,0.000049490027],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026397774,0.00014862788,0.0003512078,0.00006235766,0.000027269587,0.0000027148994,0.000057093683,0.00005034559,0.000009102737],"category_scores_gemma":[0.0009736905,0.00009574921,0.000045300327,0.000115665,0.00008925466,0.00034435443,0.000039530965,0.000092324706,0.0000012724909],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018849877,0.000026749893,0.0013709349,0.00043593056,0.000032690798,7.526292e-7,0.00001839088,0.000011925646,0.7987139,0.000055877794,0.0000030054673,0.19914131],"study_design_scores_gemma":[0.00033550162,0.00017270674,0.002557298,0.00040429365,0.000040618514,0.000008490909,0.0000035215742,0.00011755983,0.99579424,0.000068425776,0.00037938516,0.000117938835],"about_ca_topic_score_codex":0.00003873908,"about_ca_topic_score_gemma":0.000018383142,"teacher_disagreement_score":0.19902337,"about_ca_system_score_codex":0.000046732923,"about_ca_system_score_gemma":0.000008773662,"threshold_uncertainty_score":0.39045393},"labels":[],"label_agreement":null},{"id":"W247007988","doi":"","title":"Green diesel from Fischer-Tropsch Synthesis: challenges and hurdles.","year":2007,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Fischer–Tropsch process; Diesel fuel; Renewable energy; Syngas; Context (archaeology); Vegetable oil refining; Waste management; Renewable fuels; Fossil fuel; Biogas; Environmental science; Engineering; Biodiesel; Chemistry","score_opus":0.02447759603075375,"score_gpt":0.23878344813942862,"score_spread":0.21430585210867487,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W247007988","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.93242204,0.0118082,0.0019086476,0.00058460725,0.00010268512,0.0001122452,0.000010903613,0.00041024946,0.052640397],"genre_scores_gemma":[0.99505156,0.0005796077,0.0024756135,0.00003815675,0.00027278744,0.000009909878,0.0000063134407,0.000044063756,0.0015219705],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998977,0.0000075263874,0.00022530553,0.00027338846,0.00018530704,0.00033146332],"domain_scores_gemma":[0.9991297,0.0003876697,0.000037142192,0.00027869444,0.000020924956,0.00014583085],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002769726,0.00017140644,0.00024253488,0.00007355132,0.000032009408,0.0000071689597,0.00014500409,0.00013128223,0.00013294572],"category_scores_gemma":[0.00018915684,0.00013937397,0.00006273565,0.00006410542,0.00003755074,0.00013711705,0.00012449526,0.00017478767,0.00006155464],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000048305836,0.0000557027,0.00045617032,0.0001553253,0.0002564748,0.000051349994,0.0014618626,0.000003341145,0.54922605,0.0044307513,0.000041922496,0.44381276],"study_design_scores_gemma":[0.00047665727,0.00002286071,0.0063049975,0.0001374683,0.00009936493,0.000017128203,0.0022418513,0.0010808546,0.9734716,0.0011695971,0.014382161,0.00059548306],"about_ca_topic_score_codex":0.0011010291,"about_ca_topic_score_gemma":0.00035399388,"teacher_disagreement_score":0.44321728,"about_ca_system_score_codex":0.00006202823,"about_ca_system_score_gemma":0.0000051081556,"threshold_uncertainty_score":0.56835055},"labels":[],"label_agreement":null},{"id":"W2474239512","doi":"10.1002/cjce.22433","title":"Micro‐syngas technology options for GtL","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Natural gas; Syngas; Methane; Refinery; Gas to liquids; Chemistry; Steam reforming; Hydrocarbon; Waste management; Liquefied natural gas; Syngas to gasoline plus; Renewable natural gas; Environmental science; Fuel gas; Organic chemistry; Engineering; Catalysis","score_opus":0.008664895226914405,"score_gpt":0.2047022120418541,"score_spread":0.1960373168149397,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2474239512","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9682034,0.0011179367,0.023570875,0.0061350903,0.000564112,0.00018543648,0.000039269868,0.00008428818,0.000099562676],"genre_scores_gemma":[0.9966468,0.0000035029575,0.0027226612,0.000025635078,0.00038148195,0.000011730544,0.0000014734325,0.000048441354,0.00015825496],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989065,0.000003108785,0.0003855512,0.00010733409,0.0001198823,0.00047764424],"domain_scores_gemma":[0.9989367,0.00021274245,0.000105877676,0.00023478449,0.00014586996,0.00036402105],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002986196,0.00015712884,0.00025327443,0.0003082832,0.000058289883,0.000015451473,0.0005053173,0.00015906304,0.00003477094],"category_scores_gemma":[0.0010774743,0.000095115975,0.00019315354,0.00026805446,0.00008671558,0.00011443232,0.000024750174,0.00031683067,0.0000107918995],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000005870267,0.0000026485907,0.000017205233,0.000019014231,0.00005893435,0.000009771611,0.00003522607,0.00056015776,0.99363977,0.0032982435,0.00008651527,0.0022666398],"study_design_scores_gemma":[0.00047776074,0.000017957966,0.0000034755858,0.00017209238,0.000043740692,0.00047237455,0.000007883352,0.0006875004,0.98417556,0.000567458,0.013214756,0.0001594481],"about_ca_topic_score_codex":0.00011240672,"about_ca_topic_score_gemma":0.00005306539,"teacher_disagreement_score":0.028443389,"about_ca_system_score_codex":0.0004763349,"about_ca_system_score_gemma":0.00020853945,"threshold_uncertainty_score":0.38787168},"labels":[],"label_agreement":null},{"id":"W2478702769","doi":"10.1007/s10562-016-1820-8","title":"Fischer–Tropsch Synthesis: XANES Investigation of Hydrogen Chloride Poisoned Iron and Cobalt-Based Catalysts at the K-Edges of Cl, Fe, and Co","year":2016,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"U.S. Department of Energy","keywords":"Catalysis; Chemistry; Cobalt; Fischer–Tropsch process; XANES; Syngas; Inorganic chemistry; Adsorption; Hydrogen chloride; Hydrogen; Selectivity; Spectroscopy; Organic chemistry","score_opus":0.011125056520491361,"score_gpt":0.20987994590642356,"score_spread":0.1987548893859322,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2478702769","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9966886,0.000570363,0.00017031853,0.0022498884,0.00002675147,0.000162882,0.000062005856,0.000043562042,0.000025604571],"genre_scores_gemma":[0.99950427,0.00003837959,0.00006748168,0.00012130789,0.00004565247,0.000041141466,0.00008094958,0.00003818035,0.00006263229],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984966,0.000052812997,0.0004949087,0.00036056858,0.0003230491,0.00027205594],"domain_scores_gemma":[0.99825954,0.0006674754,0.00033110788,0.00056994933,0.000048617025,0.0001233203],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00041191792,0.00025098084,0.0004901401,0.00017309692,0.00007952276,0.000009453477,0.00023590948,0.000104102044,0.000011833815],"category_scores_gemma":[0.00044047556,0.00015672081,0.00014368446,0.00027654652,0.0005077137,0.00019857353,0.00011644692,0.00009591454,0.0000073125075],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005969681,0.00000878441,0.008454188,0.00023631674,0.00016215378,0.0000028625461,0.00030075767,0.000047559734,0.98724955,0.000009445965,0.000055453642,0.00341325],"study_design_scores_gemma":[0.00046722702,0.0000135707705,0.0017786528,0.0001671694,0.00035074784,0.000013730605,0.00008236171,0.00018532183,0.9965796,0.0000055400587,0.00015284002,0.00020327495],"about_ca_topic_score_codex":0.00031616128,"about_ca_topic_score_gemma":0.000055598597,"teacher_disagreement_score":0.009330031,"about_ca_system_score_codex":0.00012470798,"about_ca_system_score_gemma":0.000022005095,"threshold_uncertainty_score":0.63908887},"labels":[],"label_agreement":null},{"id":"W2487673092","doi":"10.1021/bk-2012-1092.ch012","title":"Design and Preparation of Ni-Co Bimetallic Nanocatalyst for Carbon Dioxide Reforming of Methane","year":2012,"lang":"en","type":"book-chapter","venue":"ACS symposium series","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; Canadian Light Source (Canada); Saskatchewan Research Council (Canada)","funders":"Argonne National Laboratory; Purdue University","keywords":"Catalysis; Bimetallic strip; Materials science; Nickel; Oxide; Carbon dioxide reforming; Methane; Transition metal; Chemical engineering; Syngas; Carbon fibers; Sintering; Metal; Inorganic chemistry; Metallurgy; Chemistry; Composite material; Organic chemistry","score_opus":0.01959103941892012,"score_gpt":0.25285754426878504,"score_spread":0.23326650484986491,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2487673092","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.66734177,0.058125854,0.010373046,0.00029486755,0.002616672,0.012590571,0.0010684452,0.0012758644,0.24631293],"genre_scores_gemma":[0.7639487,0.0032775681,0.009837764,0.000012450298,0.00075881736,0.0003603711,0.0012463355,0.0007374951,0.2198205],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99797267,0.000016907432,0.00090741477,0.00039236713,0.00034881305,0.00036185034],"domain_scores_gemma":[0.99815834,0.00021217465,0.0007513551,0.000600437,0.0001704748,0.00010725242],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00055215135,0.000494012,0.0010712154,0.00029723247,0.000033146407,0.0000065270633,0.0002467853,0.0004927605,0.000009433087],"category_scores_gemma":[0.00008165334,0.0004537731,0.00020944509,0.00006621064,0.00017182187,0.00042584242,0.00013764146,0.0002084154,0.0000020782559],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027233225,0.000013367143,0.000004130392,0.0014419291,0.00039687834,0.0000011572005,0.0008036668,0.000067645466,0.990582,0.005610654,0.0000018555501,0.00080439483],"study_design_scores_gemma":[0.00034532862,0.00020667179,6.836748e-7,0.00038378182,0.00061206165,0.000056576926,0.00004013956,0.000083602914,0.9928649,0.0006427556,0.004328638,0.00043484409],"about_ca_topic_score_codex":0.00013445651,"about_ca_topic_score_gemma":0.000012321831,"teacher_disagreement_score":0.09660695,"about_ca_system_score_codex":0.00013731328,"about_ca_system_score_gemma":0.000069878675,"threshold_uncertainty_score":0.9997914},"labels":[],"label_agreement":null},{"id":"W2494513745","doi":"10.1002/cjce.22602","title":"Modelling of binary fluidized bed reactors for the sorption‐enhanced steam methane reforming process","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Norges Forskningsråd","keywords":"Sorbent; Fluidized bed; Steam reforming; Methane; Packed bed; Sorption; Hydrogen; Chemistry; Waste management; Superficial velocity; Trickle-bed reactor; Residence time (fluid dynamics); Hydrogen production; Chemical engineering; Materials science; Catalysis; Chromatography; Adsorption; Mechanics; Engineering; Organic chemistry; Flow (mathematics); Physics","score_opus":0.020847941700655695,"score_gpt":0.2292581639276121,"score_spread":0.20841022222695643,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2494513745","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97195685,0.00084157556,0.026150633,0.00045254474,0.0002987396,0.00023085889,0.000018812058,0.0000299459,0.000020015745],"genre_scores_gemma":[0.9988996,0.000017758277,0.0005780898,0.000011939572,0.0003649875,0.0000202833,0.000002755343,0.0000697507,0.000034830642],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99818295,0.000011961686,0.000774911,0.00015348919,0.00033667663,0.0005400266],"domain_scores_gemma":[0.99789613,0.0007639126,0.00033911958,0.00033787603,0.00030920215,0.0003537437],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00091335236,0.0002459965,0.00046611056,0.00021373891,0.00007228166,0.000012858283,0.0007180809,0.00014874693,0.000019685573],"category_scores_gemma":[0.0010306597,0.00012563712,0.00032743887,0.00032743756,0.00009770168,0.00026895804,0.000029233197,0.00039919137,0.0000015297115],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006352462,0.000005110622,0.0000018750643,0.00010328188,0.00014042671,0.0000028910158,0.00043169994,0.050783772,0.9468695,0.00014158865,0.000005090403,0.0014512246],"study_design_scores_gemma":[0.000772663,0.000029576806,4.46202e-7,0.0004606339,0.000118740405,0.0000708729,0.00007029369,0.042885028,0.95508933,0.00014086481,0.00017564626,0.00018593173],"about_ca_topic_score_codex":0.00055764045,"about_ca_topic_score_gemma":0.000031250584,"teacher_disagreement_score":0.02694273,"about_ca_system_score_codex":0.00047878086,"about_ca_system_score_gemma":0.00033813348,"threshold_uncertainty_score":0.5123333},"labels":[],"label_agreement":null},{"id":"W2497232582","doi":"10.1016/b978-0-444-63428-3.50243-5","title":"Optimal Design of an Integrated Radiant Syngas Cooler and Steam Methane Reformer using NLP and Meta-heuristic Algorithms","year":2016,"lang":"en","type":"book-chapter","venue":"Computer-aided chemical engineering/Computer aided chemical engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"","keywords":"Solver; Syngas; Computer science; Heuristic; Meta heuristic; Particle swarm optimization; Mathematical optimization; Algorithm; Process engineering; Artificial intelligence; Mathematics; Engineering; Chemistry","score_opus":0.02423486818410183,"score_gpt":0.22280677484556127,"score_spread":0.19857190666145944,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2497232582","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.03295891,0.002658668,0.9605744,0.00003657643,0.0008343421,0.0011200568,0.00031343952,0.001376322,0.00012732609],"genre_scores_gemma":[0.045854613,0.00026425454,0.94570386,0.00009995212,0.0036932998,0.00016955835,0.0006022023,0.0019909055,0.0016213713],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99211687,0.000040896874,0.0025987327,0.0023595141,0.001067751,0.0018162362],"domain_scores_gemma":[0.9947986,0.0010891341,0.0006653287,0.0015166099,0.0003645809,0.001565722],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.0006851549,0.0028015773,0.0043760366,0.00097455166,0.00006859477,0.00012438862,0.0012432405,0.001863752,0.000104522755],"category_scores_gemma":[0.00023577755,0.0024810166,0.0009114496,0.00036042667,0.00034685872,0.000671844,0.0014095894,0.0025083905,0.000014127008],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012432547,0.00010171829,1.7337743e-7,0.0018358179,0.004297774,0.00024677376,0.00018168049,0.19937097,0.78180987,0.0016840936,0.000026893194,0.01031991],"study_design_scores_gemma":[0.0014848887,0.00016728323,4.6509857e-7,0.0009530858,0.0022842768,0.00086310087,0.0000022912695,0.68506336,0.30617633,0.000083822415,0.0008418177,0.0020792831],"about_ca_topic_score_codex":0.000032510397,"about_ca_topic_score_gemma":1.3827352e-7,"teacher_disagreement_score":0.48569238,"about_ca_system_score_codex":0.00088340463,"about_ca_system_score_gemma":0.00013144556,"threshold_uncertainty_score":0.9997929},"labels":[],"label_agreement":null},{"id":"W2500407566","doi":"10.1007/s11090-016-9734-1","title":"Synthesis of Nano-catalysts by Induction Suspension Plasma Technology (SPS) for Fischer–Tropsch Reaction","year":2016,"lang":"en","type":"article","venue":"Plasma Chemistry and Plasma Processing","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Catalysis; Bimetallic strip; Materials science; Fischer–Tropsch process; Nanoparticle; Chemical engineering; Carbon fibers; Amorphous carbon; Cobalt; Scanning electron microscope; Carbide; Metal; Amorphous solid; Nanotechnology; Chemistry; Metallurgy; Composite material; Crystallography; Composite number; Organic chemistry","score_opus":0.00944260207444673,"score_gpt":0.22435338195815827,"score_spread":0.21491077988371154,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2500407566","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99762917,0.00016099027,0.00064083183,0.00031198649,0.00009740861,0.00017218017,0.00007503665,0.00022383778,0.0006885506],"genre_scores_gemma":[0.997013,0.0000735798,0.0016281023,0.0000024722153,0.00012010887,0.000094436866,0.00006917528,0.0000642102,0.00093492743],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980932,0.000011396862,0.0005687359,0.00059651,0.00026036747,0.0004697928],"domain_scores_gemma":[0.998569,0.00042427977,0.0004094598,0.00029753393,0.000166079,0.00013365092],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00029073222,0.00035460232,0.0004952937,0.00011066659,0.00018071337,0.00002255496,0.00021823504,0.00060169806,0.000018474686],"category_scores_gemma":[0.0012191338,0.00028440126,0.00010199197,0.0003685108,0.00016841297,0.00049148285,0.000093801675,0.00026888202,0.000006951432],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00020529893,0.000046150068,0.00010677096,0.000986374,0.00005317458,0.0000018955695,0.000049426035,0.0000058080495,0.87533796,0.000014856067,0.000053698794,0.1231386],"study_design_scores_gemma":[0.00093779125,0.000026865497,0.000004347329,0.00082902267,0.00011668883,0.00024636782,0.00021410498,0.00393931,0.99051046,0.00007880271,0.002720235,0.00037599602],"about_ca_topic_score_codex":0.000013403792,"about_ca_topic_score_gemma":0.0000028738516,"teacher_disagreement_score":0.122762606,"about_ca_system_score_codex":0.00016249405,"about_ca_system_score_gemma":0.00006654821,"threshold_uncertainty_score":0.99996084},"labels":[],"label_agreement":null},{"id":"W2506408881","doi":"10.3389/fmicb.2016.01188","title":"Biomethanation of Syngas Using Anaerobic Sludge: Shift in the Catabolic Routes with the CO Partial Pressure Increase","year":2016,"lang":"en","type":"article","venue":"Frontiers in Microbiology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":87,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Montréal; National Research Council Canada","funders":"Natural Resources Canada; Office of Energy Research and Development; Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Anaerobic exercise; Chemistry; Pulp and paper industry; Waste management; Environmental science; Biochemical engineering; Biology; Catalysis; Biochemistry; Engineering","score_opus":0.008976331475513374,"score_gpt":0.23502648648815366,"score_spread":0.22605015501264028,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2506408881","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9887501,0.0011015185,0.009198576,0.00037546267,0.00017110136,0.00027670723,0.00008094091,0.000017594997,0.00002797573],"genre_scores_gemma":[0.99875575,0.000021189726,0.0009962061,0.000044921046,0.000059255446,0.000022030325,0.00004598762,0.000019544754,0.000035099045],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988467,0.00019873836,0.00030154467,0.0002374648,0.00006954573,0.00034598503],"domain_scores_gemma":[0.99927205,0.00018291884,0.00014416194,0.00035152683,0.000024451601,0.000024863299],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006719686,0.0001640236,0.0003161418,0.00025432455,0.000034931665,0.000005310036,0.00042725547,0.0001509776,0.000010830687],"category_scores_gemma":[0.00013620207,0.00007679801,0.000053562555,0.0004701039,0.00026322878,0.00010965907,0.000061299346,0.00020597642,0.0000022169081],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009935276,0.000035051016,0.010575667,0.000030622443,0.00006688031,0.0000058778246,0.0009244412,0.0002489003,0.9866221,0.00013376134,0.00020681859,0.0010505128],"study_design_scores_gemma":[0.0020927645,0.00007755357,0.0030117847,0.00017713342,0.0001317939,0.00009295347,0.00071551703,0.00087973673,0.98006225,0.00010992027,0.01229707,0.00035152337],"about_ca_topic_score_codex":0.00084075786,"about_ca_topic_score_gemma":0.0002039089,"teacher_disagreement_score":0.012090251,"about_ca_system_score_codex":0.00009427354,"about_ca_system_score_gemma":0.00004392991,"threshold_uncertainty_score":0.3131732},"labels":[],"label_agreement":null},{"id":"W2507825755","doi":"10.1021/acs.energyfuels.5b00624","title":"Syngas Purification in Cryogenic Packed Beds Using a One-Dimensional Pseudo-homogenous Model","year":2015,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"Natural Sciences and Engineering Research Council of Canada; Ontario Ministry of Agriculture, Food and Rural Affairs","keywords":"Biogas; Syngas; Flue gas; Heat of combustion; Environmental science; Waste management; Process engineering; Hydrogen; Pulp and paper industry; Materials science; Chemistry; Engineering; Organic chemistry; Combustion","score_opus":0.04731919655533958,"score_gpt":0.2582492150983099,"score_spread":0.2109300185429703,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2507825755","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9901171,0.00058143307,0.008142824,0.00004862858,0.00014042525,0.00007939305,0.000008054383,0.00014286507,0.0007392929],"genre_scores_gemma":[0.99241656,0.000010663001,0.0065367874,0.000060705315,0.0001615976,0.000028936707,0.000074208554,0.000072827024,0.0006377074],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99822634,0.000034757577,0.0004432125,0.00037997036,0.00044440554,0.0004713015],"domain_scores_gemma":[0.9990585,0.000044959357,0.00010817488,0.000459081,0.00009781141,0.00023150249],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034806688,0.0002363084,0.0003292689,0.00023882314,0.000047062746,0.000015782809,0.0002303342,0.0001942219,0.000022467319],"category_scores_gemma":[0.00013195397,0.00024429438,0.000120390345,0.00040239704,0.00003606772,0.00024930705,0.00011474503,0.0002179016,0.000027225455],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003248401,0.00008568302,0.00002903039,0.000015151365,0.000036702888,0.000015104671,0.0003140971,0.081914544,0.9136981,0.002595065,0.0000076171477,0.0012564136],"study_design_scores_gemma":[0.0006765731,0.000019490451,0.0000121903195,0.000056218934,0.000038145456,0.000060389313,0.000041863157,0.25130934,0.744924,0.0023435887,0.00020800406,0.00031018583],"about_ca_topic_score_codex":0.0007634791,"about_ca_topic_score_gemma":0.00009484052,"teacher_disagreement_score":0.16939478,"about_ca_system_score_codex":0.0005707802,"about_ca_system_score_gemma":0.00017396655,"threshold_uncertainty_score":0.9962036},"labels":[],"label_agreement":null},{"id":"W2509371109","doi":"10.1007/s11164-016-2701-x","title":"Novel Co/graphene oxide and Co/nanoporous graphene catalysts for Fischer–Tropsch reaction","year":2016,"lang":"en","type":"article","venue":"Research on Chemical Intermediates","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Graphene; Nanoporous; Catalysis; Oxide; Materials science; Selectivity; Hydrocarbon; Chemical engineering; Fischer–Tropsch process; Hydrogen; Carbon fibers; Nanotechnology; Inorganic chemistry; Chemistry; Organic chemistry; Composite material; Composite number","score_opus":0.06118462881011682,"score_gpt":0.36985556447640117,"score_spread":0.30867093566628434,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2509371109","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.997011,0.00017158281,0.0005326252,0.000521548,0.000097743745,0.0004677738,0.00018516737,0.00019696317,0.00081561663],"genre_scores_gemma":[0.9978495,0.000180284,0.00050092954,0.000032945194,0.000346991,0.00029106956,0.00019888887,0.00009984817,0.0004995221],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968543,0.000039708044,0.00051208306,0.00075121166,0.00078569935,0.0010569933],"domain_scores_gemma":[0.99639046,0.002216552,0.000105069754,0.0005361389,0.00026643145,0.00048535265],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0009975529,0.0003425616,0.00046530497,0.00045505792,0.00011399863,0.00004179806,0.00044968774,0.0003249011,0.000029410652],"category_scores_gemma":[0.002110373,0.00023855807,0.00021767938,0.0003886285,0.00049913966,0.0002765836,0.00017548296,0.0006077563,0.00008751548],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033790438,0.00014031376,0.00026824654,0.00015149015,0.000104906554,0.0000072840858,0.00007017241,2.8295014e-7,0.99084145,0.0006095729,0.00087943644,0.006588954],"study_design_scores_gemma":[0.0016274825,0.00014138184,0.00022827851,0.00030169333,0.000020277686,0.000039727467,0.00008049995,0.000150184,0.9933107,0.0005632128,0.0032073024,0.00032926127],"about_ca_topic_score_codex":0.00018787145,"about_ca_topic_score_gemma":0.000014489589,"teacher_disagreement_score":0.006259693,"about_ca_system_score_codex":0.00037097634,"about_ca_system_score_gemma":0.000051123156,"threshold_uncertainty_score":0.9728116},"labels":[],"label_agreement":null},{"id":"W2515334437","doi":"10.1007/s11356-016-7480-9","title":"Steam reforming of ethanol for hydrogen production over Cu/Co-Mg-Al-based catalysts prepared by hydrotalcite route","year":2016,"lang":"en","type":"article","venue":"Environmental Science and Pollution Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Agence Universitaire de la Francophonie; Université du Littoral Côte d'Opale","keywords":"Catalysis; Hydrotalcite; Thermogravimetry; Hydrogen production; Steam reforming; Hydrogen; Ethanol; Chemistry; Coke; Differential scanning calorimetry; Magnesium; Inorganic chemistry; Nuclear chemistry; Chemical engineering; Materials science; Organic chemistry","score_opus":0.02410834094717458,"score_gpt":0.32440080088185425,"score_spread":0.3002924599346797,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2515334437","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.998048,0.00018682324,0.00013814718,0.0005032716,0.00005726662,0.00061345834,0.00018057517,0.0000331193,0.00023934976],"genre_scores_gemma":[0.99828136,0.00005479897,0.000056683628,0.000022343687,0.00005297182,0.00009602775,0.000036375717,0.000021343862,0.0013781115],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99718034,0.000040376985,0.00030456122,0.00056056253,0.0012755226,0.00063861685],"domain_scores_gemma":[0.99920166,0.0000673257,0.00009744753,0.0003949384,0.000032098014,0.00020656254],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0023856242,0.0001491793,0.00017717932,0.0003025857,0.0003264106,0.000012760363,0.00030553856,0.000082762424,0.000039825954],"category_scores_gemma":[0.00036742986,0.000107559456,0.00006881943,0.00047853612,0.0010031135,0.000698581,0.00016315111,0.0001400408,0.00001977674],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006582176,0.000053518554,0.0006703596,0.000029377336,0.000009999396,4.5197316e-7,0.00016318112,0.000023563833,0.9847201,0.000012470472,0.00010719019,0.014143963],"study_design_scores_gemma":[0.00058625883,0.00010600526,0.0005488173,0.00007227152,0.0000074889726,0.0000073078563,0.00011811319,0.0014296509,0.9902646,0.000025485731,0.006678036,0.0001559432],"about_ca_topic_score_codex":0.00021672886,"about_ca_topic_score_gemma":0.000007183809,"teacher_disagreement_score":0.01398802,"about_ca_system_score_codex":0.0010369198,"about_ca_system_score_gemma":0.00009482288,"threshold_uncertainty_score":0.43861473},"labels":[],"label_agreement":null},{"id":"W2517838794","doi":"10.1021/acs.iecr.5b03003","title":"Synthesis and Characterization of Co/C and Fe/C Nanocatalysts for Fischer–Tropsch Synthesis: A Comparative Study Using a Fixed-Bed Reactor","year":2015,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); University of Saskatchewan; Université de Sherbrooke","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Space velocity; Nanomaterial-based catalyst; Syngas; Chemical engineering; Materials science; Coprecipitation; Chemistry; Bar (unit); Inorganic chemistry; Organic chemistry; Selectivity","score_opus":0.1919577340466624,"score_gpt":0.3703997824420644,"score_spread":0.178442048395402,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2517838794","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9987671,0.00008187625,0.00006667072,0.000022567283,0.000058683603,0.000754097,0.00011772679,0.00007979475,0.000051504438],"genre_scores_gemma":[0.9990974,0.0000056889075,0.000100765916,4.382003e-7,0.00035962253,0.00026320576,0.00004491571,0.00006416477,0.000063815125],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977803,0.00006584879,0.0005334791,0.00048083707,0.0006038939,0.00053560786],"domain_scores_gemma":[0.9977904,0.0010504768,0.00013827624,0.00037505678,0.00030914374,0.00033662372],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0016140111,0.00030245192,0.0006811093,0.00019717983,0.00007305638,0.000059960512,0.00025809504,0.00032124974,0.000008956271],"category_scores_gemma":[0.0036892684,0.0003019157,0.00006970466,0.0004940404,0.00010560979,0.00023800679,0.00018779816,0.0005896263,0.0000010877012],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023816785,0.000103184175,0.00048522567,0.00029472503,0.00019687257,0.00000635108,0.0008356136,0.00009799806,0.997149,0.0000042445868,0.00000736753,0.00058126316],"study_design_scores_gemma":[0.0011330879,0.00006499738,0.00006362918,0.00033001215,0.00009157206,0.00002475647,0.0011888414,0.019234143,0.97737896,0.000001453551,0.0002127746,0.0002757408],"about_ca_topic_score_codex":0.000162254,"about_ca_topic_score_gemma":0.0000011545707,"teacher_disagreement_score":0.019769996,"about_ca_system_score_codex":0.00029455216,"about_ca_system_score_gemma":0.00016089612,"threshold_uncertainty_score":0.9999433},"labels":[],"label_agreement":null},{"id":"W2518408394","doi":"10.1021/acs.iecr.5b01402","title":"Fischer–Tropsch Mechanism: <sup>13</sup>C<sup>18</sup>O Tracer Studies on a Ceria–Silica Supported Cobalt Catalyst and a Doubly Promoted Iron Catalyst","year":2015,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Resources Canada; Helmholtz-Alberta Initiative; Helmholtz-Gemeinschaft; University of Alberta","keywords":"Fischer–Tropsch process; Catalysis; Cobalt; Chemistry; Methanol; Syngas; Water-gas shift reaction; Inorganic chemistry; Organic chemistry; Selectivity","score_opus":0.13353214453346748,"score_gpt":0.3467096935499581,"score_spread":0.21317754901649064,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2518408394","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957466,0.00055962085,0.000022367823,0.00041854783,0.00018921483,0.0011931646,0.00021812074,0.0007115604,0.00094080134],"genre_scores_gemma":[0.9936435,0.000043157463,0.00009522107,0.000009787435,0.0018656676,0.0004432924,0.00057238434,0.00029489762,0.0030320608],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99255526,0.00013648624,0.0013378451,0.0015808477,0.002261655,0.0021278814],"domain_scores_gemma":[0.99547386,0.0006978094,0.00021190544,0.0014922546,0.00070681825,0.0014173354],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.003260308,0.0010600955,0.0013944426,0.00049763854,0.00027636864,0.00020820435,0.0010638927,0.0012673346,0.00016314951],"category_scores_gemma":[0.0064370753,0.0010242679,0.00028699162,0.0018829802,0.0003114062,0.00045237434,0.0008782127,0.0038213867,0.00010667717],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00060923945,0.0002572052,0.00006266725,0.0008446533,0.000709038,0.0003713304,0.0026186784,0.049077976,0.9429504,0.00006321256,0.0015606066,0.00087498745],"study_design_scores_gemma":[0.0048461817,0.0002458411,0.0000038950143,0.00058152457,0.0001647722,0.00029694228,0.0023843255,0.081488706,0.9046964,0.000033889297,0.004188413,0.0010690812],"about_ca_topic_score_codex":0.0006251926,"about_ca_topic_score_gemma":0.0000071199142,"teacher_disagreement_score":0.03825398,"about_ca_system_score_codex":0.0017460858,"about_ca_system_score_gemma":0.000575384,"threshold_uncertainty_score":0.9992208},"labels":[],"label_agreement":null},{"id":"W2521088471","doi":"10.1021/acs.energyfuels.6b01981","title":"Effects of Co Particle Size on the Stability of Co/Al<sub>2</sub>O<sub>3</sub> and Re–Co/Al<sub>2</sub>O<sub>3</sub> Catalysts in a Slurry-Phase Fischer-Tropsch Reactor","year":2016,"lang":"ar","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Fischer–Tropsch process; Particle size; Carbon fibers; Deposition (geology); Particle (ecology); Chemistry; Volumetric flow rate; Chemical engineering; Carbon monoxide; Materials science; Analytical Chemistry (journal); Selectivity; Physical chemistry; Organic chemistry; Thermodynamics; Composite material","score_opus":0.011355233774437758,"score_gpt":0.24175408690865638,"score_spread":0.23039885313421862,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2521088471","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.993188,0.0020319691,0.00017016692,0.0008755669,0.00067547965,0.0016013894,0.0007229012,0.00037587836,0.00035860064],"genre_scores_gemma":[0.99559295,0.0022110902,0.00004876635,0.0003919322,0.00047951413,0.000510626,0.0002114006,0.00053381064,0.000019922307],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9865848,0.0013331871,0.003742255,0.002852554,0.0024142186,0.0030729957],"domain_scores_gemma":[0.98446494,0.007981579,0.0019070243,0.0036768,0.0005685377,0.0014011336],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.003495392,0.0022751603,0.0033964594,0.0006527385,0.00042645438,0.00014047869,0.001511362,0.0013268834,0.000051703384],"category_scores_gemma":[0.0063702385,0.0018123504,0.0012909495,0.0020764028,0.0013994963,0.0012599743,0.00083310035,0.0018711685,0.00019590801],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.001810887,0.0019619025,0.0006813327,0.0018100496,0.00086294115,0.00024909087,0.0017197154,0.000051040468,0.95417994,0.00044602025,0.0004031274,0.035823938],"study_design_scores_gemma":[0.008679244,0.001061876,0.0013306455,0.002172144,0.00070935895,0.0000665165,0.0003374029,0.0004158518,0.9818218,0.00028269735,0.0011573407,0.0019651442],"about_ca_topic_score_codex":0.0003578825,"about_ca_topic_score_gemma":0.0004806656,"teacher_disagreement_score":0.033858795,"about_ca_system_score_codex":0.0014962454,"about_ca_system_score_gemma":0.00057696353,"threshold_uncertainty_score":0.9999696},"labels":[],"label_agreement":null},{"id":"W2525338126","doi":"10.1109/redec.2016.7577544","title":"Preparation and characterization of Ni-Co-Mg-Al mixed oxides derived from layered double hydroxides and their performance in the dry reforming of methane","year":2016,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Agence Universitaire de la Francophonie; Université du Littoral Côte d'Opale","keywords":"Hydrotalcite; Calcination; Catalysis; Thermogravimetric analysis; Carbon dioxide reforming; Methane; Materials science; Differential scanning calorimetry; Nuclear chemistry; Fourier transform infrared spectroscopy; Chemical engineering; Syngas; Chemistry; Analytical Chemistry (journal); Organic chemistry; Physics; Thermodynamics","score_opus":0.014382843299454195,"score_gpt":0.2432102241036122,"score_spread":0.22882738080415801,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2525338126","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985973,0.00007032586,0.00083758426,0.000057370256,0.000025703104,0.00018919724,0.000014459211,0.00002633099,0.00018169095],"genre_scores_gemma":[0.9994706,0.00013143901,0.00024083104,0.000010206575,0.000021034084,0.000017474804,0.00003850401,0.000014107005,0.00005581846],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99913055,0.000026244948,0.0003853365,0.00017994436,0.00012958758,0.00014833988],"domain_scores_gemma":[0.9994008,0.0001542052,0.00016880904,0.00021415245,0.000033168766,0.000028882665],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003643244,0.00013653382,0.0002667956,0.000097059674,0.00001923319,0.00000598366,0.00011056981,0.000074154064,0.000011208759],"category_scores_gemma":[0.000048800805,0.00007063194,0.000031331485,0.0001232652,0.00006214237,0.00047161317,0.000052911582,0.000064509906,7.6392683e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014355005,0.000014887431,0.0039979233,0.000058598413,0.000024149816,2.0972318e-7,0.0017234264,0.0000042531933,0.9859645,0.00004833226,1.1626368e-7,0.0080200825],"study_design_scores_gemma":[0.0009122806,0.00003580933,0.017230794,0.00014773221,0.000010766864,0.0000038588714,0.0003442958,0.002990499,0.9781546,0.000032923024,0.000034836394,0.00010157757],"about_ca_topic_score_codex":0.00035942747,"about_ca_topic_score_gemma":0.00008540527,"teacher_disagreement_score":0.013232871,"about_ca_system_score_codex":0.000032632608,"about_ca_system_score_gemma":0.000011947297,"threshold_uncertainty_score":0.2880287},"labels":[],"label_agreement":null},{"id":"W2527555069","doi":"10.14447/jnmes.v15i3.68","title":"Production of Hydrogen from Ethanol Using Pt/Hydrotalcite Catalysts Stabilized with Tungsten Oxides","year":2012,"lang":"en","type":"article","venue":"Journal of New Materials for Electrochemical Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Hydrotalcite; Crystallinity; Catalysis; Sintering; Hydrogen production; Materials science; Steam reforming; Hydrogen; Chemical engineering; Inorganic chemistry; Nuclear chemistry; Chemistry; Metallurgy; Organic chemistry; Composite material","score_opus":0.02237652706386313,"score_gpt":0.25911681218434446,"score_spread":0.23674028512048134,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2527555069","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99523604,0.0014742713,0.0019324844,0.000027814984,0.00071841426,0.0005355101,0.000023511331,0.00003984288,0.000012130474],"genre_scores_gemma":[0.9965495,0.00001171624,0.0010208704,0.0000035178298,0.0021874595,0.000017486367,0.000039883525,0.00008934817,0.00008020153],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99708503,0.000055676668,0.0013486793,0.00023556077,0.0006688186,0.00060623814],"domain_scores_gemma":[0.9975357,0.00013324813,0.001355442,0.00031243678,0.0003605781,0.00030260705],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00095576333,0.00032396035,0.0011034021,0.00017026238,0.0000379491,0.000028032195,0.00029730605,0.00021803386,0.000015600355],"category_scores_gemma":[0.00052615005,0.00023749894,0.00023569388,0.00026150286,0.000043553813,0.00058330793,0.00004775929,0.00019593151,0.0000020130824],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000863208,0.0000770158,0.00014033781,0.00039256262,0.00043988746,0.0000016948304,0.00035682952,0.00014330841,0.9974936,0.000015971707,0.000028552062,0.00004701548],"study_design_scores_gemma":[0.0012391792,0.00014518348,0.000008863482,0.0005546022,0.00038769483,0.0006023076,0.000091243885,0.00018000294,0.99613917,0.000049862523,0.00032713826,0.00027476516],"about_ca_topic_score_codex":0.00043958295,"about_ca_topic_score_gemma":0.0000023852313,"teacher_disagreement_score":0.0014690452,"about_ca_system_score_codex":0.0005266302,"about_ca_system_score_gemma":0.00015123373,"threshold_uncertainty_score":0.96849257},"labels":[],"label_agreement":null},{"id":"W2528285034","doi":"10.1109/sege.2016.7589528","title":"Economic and environmental impact of using hydrogen enriched natural gas and renewable natural gas for residential heating","year":2016,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Natural gas; Renewable natural gas; Renewable energy; Greenhouse gas; Biogas; Power to gas; Electricity; Methane; Coal; Environmental science; Hydrogen; Waste management; Process engineering; Computer science; Chemistry; Fuel gas; Engineering; Electrical engineering; Organic chemistry; Electrolysis","score_opus":0.007677894206265486,"score_gpt":0.2422388815019406,"score_spread":0.2345609872956751,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2528285034","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9987992,0.0005073439,0.0003434679,0.000012466459,0.00006888179,0.00016787561,0.00003105564,0.00003095058,0.00003878255],"genre_scores_gemma":[0.9983612,0.000025149948,0.0010007513,0.0000024046697,0.000108641245,0.000004413132,0.000017682216,0.00003270292,0.00044706493],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990591,0.00000914288,0.00029089325,0.0002547253,0.00008253311,0.000303605],"domain_scores_gemma":[0.9995142,0.00014527675,0.0001034176,0.00013972627,0.0000057685693,0.00009157505],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014890023,0.00017662614,0.00027381984,0.00008291891,0.00005361249,0.000012443795,0.00007577847,0.00007379415,0.000047599136],"category_scores_gemma":[0.000060948245,0.0001199555,0.00012958323,0.000026392569,0.0000748147,0.0003409819,0.000120245815,0.00006886149,9.736627e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000057652058,0.0000050056074,0.00408938,0.00003126524,0.000085777836,8.4564675e-7,0.000067439374,0.00030798547,0.99396557,0.00002052199,0.0000040238792,0.0013645403],"study_design_scores_gemma":[0.0012237102,0.000037229656,0.00063320564,0.000047658956,0.00004604774,0.00007818733,0.00006339336,0.085133046,0.9123186,0.00019547789,0.0000088562,0.00021457268],"about_ca_topic_score_codex":0.002108006,"about_ca_topic_score_gemma":0.000097337484,"teacher_disagreement_score":0.08482506,"about_ca_system_score_codex":0.00035120483,"about_ca_system_score_gemma":0.000019626383,"threshold_uncertainty_score":0.48916432},"labels":[],"label_agreement":null},{"id":"W2528397815","doi":"10.1002/cjce.22706","title":"Modelling and experimental validation of a CO<sub>2</sub> methanation annular cooled fixed‐bed reactor exchanger","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":60,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Association Instituts Carnot","keywords":"Methanation; Nusselt number; Thermodynamics; Coolant; Heat transfer; Materials science; Heat exchanger; Reynolds number; Heat transfer coefficient; Thermal conductivity; Prandtl number; Particle (ecology); Chemistry; Turbulence; Catalysis; Physics","score_opus":0.014745992805161852,"score_gpt":0.21731647626559644,"score_spread":0.2025704834604346,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2528397815","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99065024,0.00052910263,0.00844682,0.00012722508,0.000114380106,0.00008456814,0.000013146673,0.000016850623,0.000017698962],"genre_scores_gemma":[0.999331,0.000007183001,0.0004225582,0.0000075705157,0.00017676545,0.0000043877967,0.0000051150123,0.00004010184,0.0000053434333],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99885154,0.000015530744,0.00045622015,0.00012176905,0.00026599024,0.0002889395],"domain_scores_gemma":[0.99899644,0.00017554537,0.00019907753,0.00016307304,0.00012823069,0.00033762748],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00043798465,0.00017235702,0.00030144074,0.00019199954,0.00002845584,0.000015746386,0.00019610592,0.0001190102,0.000015764033],"category_scores_gemma":[0.00030788803,0.0001185851,0.000114380215,0.00016506782,0.000059308364,0.0002672796,0.000020043468,0.00022792687,0.0000017310897],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000018584846,0.0000050739,0.0000150906135,0.000032236323,0.00006117816,0.000007777046,0.0003853648,0.010522318,0.9883969,0.00008764778,0.0000071612058,0.00046067158],"study_design_scores_gemma":[0.0005070163,0.00001988336,0.000002267649,0.00021541535,0.000042339463,0.00009500924,0.00002213159,0.02083039,0.97800255,0.00003299031,0.00008003449,0.00014996841],"about_ca_topic_score_codex":0.00029169634,"about_ca_topic_score_gemma":0.000008742149,"teacher_disagreement_score":0.01039434,"about_ca_system_score_codex":0.00037416557,"about_ca_system_score_gemma":0.000095784846,"threshold_uncertainty_score":0.483576},"labels":[],"label_agreement":null},{"id":"W2529943023","doi":"10.1002/cjce.22428","title":"Partial oxidation of methane to syngas over Pt/Rh/MgO catalyst supported on FeCralloy woven fibre","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Syngas; Coke; Partial oxidation; Catalysis; Methane; Chemical engineering; Chemistry; Partial pressure; Yield (engineering); Fischer–Tropsch process; Materials science; Selectivity; Organic chemistry; Metallurgy; Oxygen","score_opus":0.01034485373896299,"score_gpt":0.21733600560418664,"score_spread":0.20699115186522365,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2529943023","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9971616,0.00007173721,0.001334777,0.0008932359,0.00027388646,0.000119368444,0.000030012921,0.000027181599,0.00008818048],"genre_scores_gemma":[0.9991193,0.000001425433,0.0002771417,0.00004943203,0.00036212543,0.0000052512455,0.000009072359,0.000059095335,0.00011716836],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981791,0.000016925984,0.0006751893,0.00017482995,0.0004191672,0.00053481007],"domain_scores_gemma":[0.99821514,0.0002744755,0.00021859017,0.00037615874,0.00013675836,0.0007789061],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00052090705,0.00025053913,0.00045753326,0.00032304061,0.00002651467,0.000016630516,0.000519374,0.00015263162,0.00015563793],"category_scores_gemma":[0.0013418552,0.00016198402,0.0002450749,0.00036673367,0.00005170364,0.00019213025,0.000041197105,0.00037507096,0.000022007418],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000043265252,0.000007902813,0.00004608449,0.000038684804,0.00011450548,0.000031003412,0.00015962245,0.0027102714,0.99494416,0.00031394057,0.000103483304,0.0014870765],"study_design_scores_gemma":[0.0005333935,0.000053511456,0.000075250966,0.0003967294,0.000071183764,0.0001171297,0.000007414273,0.00073423213,0.99610764,0.000028685505,0.0016577999,0.00021704771],"about_ca_topic_score_codex":0.001063108,"about_ca_topic_score_gemma":0.00014794171,"teacher_disagreement_score":0.0019760393,"about_ca_system_score_codex":0.0006098241,"about_ca_system_score_gemma":0.0002540039,"threshold_uncertainty_score":0.66055167},"labels":[],"label_agreement":null},{"id":"W2534687563","doi":"10.1039/c6fd00198j","title":"Structural and elemental influence from various MOFs on the performance of Fe@C catalysts for Fischer–Tropsch synthesis","year":2016,"lang":"en","type":"article","venue":"Faraday Discussions","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":46,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Carbon Engineering (Canada)","funders":"","keywords":"Catalysis; Porosity; Fischer–Tropsch process; Carbonization; Specific surface area; Chemical engineering; Particle size; Nanoparticle; Pyrolysis; Materials science; Crystallite; Carbon fibers; Particle (ecology); Thermal stability; Heteroatom; Selectivity; Chemistry; Nanotechnology; Physical chemistry; Adsorption; Organic chemistry; Metallurgy; Composite material","score_opus":0.011082412629034416,"score_gpt":0.23013263514426546,"score_spread":0.21905022251523104,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2534687563","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9982916,0.000054192547,0.00009507193,0.00069409335,0.00007635101,0.00024446961,0.00041821803,0.000042104566,0.00008389982],"genre_scores_gemma":[0.9991545,0.000014675019,0.00029268835,0.000021948304,0.00006310788,0.00009340298,0.000022168499,0.000028478995,0.00030904496],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989317,0.000019683666,0.00029105332,0.0002571544,0.0002215017,0.00027889825],"domain_scores_gemma":[0.9988236,0.00054309133,0.00010959678,0.00040471318,0.000029134353,0.00008985597],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012177704,0.00018936933,0.00023734973,0.000050862407,0.00015397253,0.000009754671,0.0002721809,0.000072154806,0.00004957987],"category_scores_gemma":[0.00040838178,0.00007844866,0.00009988032,0.000102555576,0.00009479215,0.00017875145,0.00012366117,0.00011692606,0.000009872838],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006836548,0.000020742675,0.0034087822,0.00004288782,0.00007825798,9.082748e-7,0.00036411476,0.00006497841,0.9807451,0.0010007118,0.000056540186,0.014148646],"study_design_scores_gemma":[0.00048927986,0.00006008456,0.014902533,0.00036186757,0.000088363166,0.0000063831835,0.00017851128,0.0031981023,0.9795482,0.00015161213,0.00075345737,0.00026157443],"about_ca_topic_score_codex":0.00016939,"about_ca_topic_score_gemma":0.00002400104,"teacher_disagreement_score":0.013887071,"about_ca_system_score_codex":0.000074500866,"about_ca_system_score_gemma":0.00002015285,"threshold_uncertainty_score":0.31990436},"labels":[],"label_agreement":null},{"id":"W2550023360","doi":"10.1002/cjce.22438","title":"H<sub>2</sub>S poisoning of NiAl<sub>2</sub>O<sub>4</sub>/Al<sub>2</sub>O<sub>3</sub>‐YSZ catalyst during methane dry reforming","year":2016,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"AllerGen; BioFuelNet Canada","keywords":"Catalysis; Carbon dioxide reforming; Space velocity; Nial; Methane; Steam reforming; Calcination; Nickel; Methane reformer; Hydrogen; Syngas; Spinel; Materials science; Analytical Chemistry (journal); Inorganic chemistry; Nuclear chemistry; Chemistry; Metallurgy; Hydrogen production; Intermetallic; Environmental chemistry; Organic chemistry","score_opus":0.00679814697267228,"score_gpt":0.19391028908141553,"score_spread":0.18711214210874325,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2550023360","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9919255,0.0022433666,0.0017240626,0.00077530753,0.0016807009,0.0008042215,0.0002485128,0.00045898944,0.00013937258],"genre_scores_gemma":[0.9954853,0.0005279978,0.00038181755,0.00016347072,0.0023214903,0.00009736737,0.000111073445,0.0008990504,0.000012408603],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.98680484,0.0002012113,0.0044021397,0.0016697852,0.002488152,0.004433875],"domain_scores_gemma":[0.98951226,0.0013116121,0.0021156596,0.0022432357,0.00094072655,0.0038764793],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.0030663575,0.0024012527,0.0033958398,0.002403886,0.0005991627,0.00024763535,0.0028821377,0.0014388683,0.000022079705],"category_scores_gemma":[0.0037705062,0.002051233,0.002060636,0.0025528332,0.00065067847,0.001978779,0.00073999015,0.0043806606,0.00014140498],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002443108,0.00008262877,0.00009776898,0.00090579083,0.0011323745,0.00070017844,0.0009090998,0.0057453024,0.96741843,0.00011045031,0.00010540046,0.022548279],"study_design_scores_gemma":[0.0032702142,0.0001408786,0.00018016566,0.004404757,0.00076570344,0.00219755,0.00019670516,0.0030576303,0.98284745,0.00014745786,0.00031659362,0.002474919],"about_ca_topic_score_codex":0.0006642951,"about_ca_topic_score_gemma":0.0011162751,"teacher_disagreement_score":0.02007336,"about_ca_system_score_codex":0.0056165066,"about_ca_system_score_gemma":0.0015258581,"threshold_uncertainty_score":0.9998575},"labels":[],"label_agreement":null},{"id":"W2551401459","doi":"10.20286/nova-jeas-050105","title":"Hydrogenation of Carbon Monoxide and Carbon Dioxide over Nano γ-Alumina Supported Cobalt (III)/Molybdenum Catalyst","year":2016,"lang":"en","type":"article","venue":"Nova Journal of Engineering and Applied Sciences","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Carbon monoxide; Cobalt; Molybdenum; Electrochemical reduction of carbon dioxide; Inorganic chemistry; Materials science; Carbon nanotube supported catalyst; Methanizer; Carbon dioxide; Methane; Molybdate; Catalyst support; Cobalt oxide; Carbon fibers; Chemistry; Carbon nanofiber; Organic chemistry; Composite material; Composite number","score_opus":0.012412535680443612,"score_gpt":0.2288377058530604,"score_spread":0.21642517017261678,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2551401459","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99836755,0.0005775658,0.00042890702,0.00003434258,0.00013573946,0.000059682814,0.0000028829184,0.000022525968,0.00037083367],"genre_scores_gemma":[0.9994449,0.000054606207,0.00036747733,0.000002998296,0.00008802041,0.000001727117,5.8054445e-7,0.00001626057,0.000023439712],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986349,0.0000054485026,0.00049949734,0.00019510838,0.00039998972,0.0002651109],"domain_scores_gemma":[0.9992861,0.00013187827,0.00027068032,0.00011649671,0.000057115893,0.00013773717],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006874084,0.00017357229,0.00036018246,0.000299866,0.00003150338,0.000012836278,0.0001819565,0.0000793461,0.0000039450097],"category_scores_gemma":[0.0001226527,0.000118593816,0.00005631676,0.0003446741,0.00013750428,0.00014805899,0.00005944491,0.00013214521,1.7674911e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000015242628,0.000010238887,0.0008492395,0.000045002453,0.000047086363,0.0000047666026,0.00014222441,0.0010204859,0.9960518,0.00031606012,7.184185e-7,0.0014971672],"study_design_scores_gemma":[0.0006673953,0.000052033258,0.00091093004,0.00018097804,0.000055228422,0.0001527322,0.000074831005,0.0042415094,0.9934108,0.00003371903,0.000047102447,0.00017269033],"about_ca_topic_score_codex":0.000088168585,"about_ca_topic_score_gemma":0.000005386118,"teacher_disagreement_score":0.0032210234,"about_ca_system_score_codex":0.00006012114,"about_ca_system_score_gemma":0.000042903128,"threshold_uncertainty_score":0.48361155},"labels":[],"label_agreement":null},{"id":"W2555669281","doi":"10.1002/aic.15582","title":"Simulation of dry reforming of methane in a conventional downfired reformer","year":2016,"lang":"en","type":"article","venue":"AIChE Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; GreenField Specialty Alcolhols (Canada); Process Research Ortech (Canada); Queen's University","funders":"Natural Sciences and Engineering Research Council of Canada; Queen's University","keywords":"Methane; Steam reforming; Carbon dioxide reforming; Process engineering; Methane reformer; Syngas; Solver; Dry gas; Process (computing); Gas composition; Nuclear engineering; Thermodynamics; Waste management; Environmental science; Mechanics; Chemistry; Engineering; Hydrogen production; Catalysis; Computer science; Physics","score_opus":0.01856310888314506,"score_gpt":0.2790582480514491,"score_spread":0.260495139168304,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2555669281","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9909746,0.0001741024,0.008006725,0.000073775875,0.0001216381,0.0000603542,0.000006550499,0.000012312458,0.00056996295],"genre_scores_gemma":[0.9986637,0.000025171543,0.00082904677,0.000005135564,0.000095387215,0.0000019220686,0.0000031125326,0.000017477272,0.00035901056],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985394,0.000028957562,0.0007565731,0.0001024618,0.000352058,0.00022054049],"domain_scores_gemma":[0.9989931,0.00024054946,0.00039678242,0.00015707285,0.00013924224,0.00007327206],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008082647,0.00010845286,0.00030068832,0.00027747214,0.000013435042,0.0000019003162,0.00015416132,0.00010031786,0.00019709514],"category_scores_gemma":[0.0006414075,0.00006784,0.00016748878,0.00023779797,0.000043122935,0.0003488083,0.000047103975,0.0001949606,0.0000072612593],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000103696104,0.00004141155,0.0036375222,0.000058867874,0.00006169485,0.0000056519093,0.00018328032,0.0030081915,0.97234136,0.00017652326,0.0000010960705,0.020380713],"study_design_scores_gemma":[0.0022411996,0.000060262428,0.0024180897,0.0006521337,0.00003642983,0.000034106823,0.00011493012,0.0077997893,0.98528475,0.0007942621,0.0004101708,0.00015390832],"about_ca_topic_score_codex":0.00006336817,"about_ca_topic_score_gemma":0.000012434628,"teacher_disagreement_score":0.020226805,"about_ca_system_score_codex":0.00022528158,"about_ca_system_score_gemma":0.00005554842,"threshold_uncertainty_score":0.27664348},"labels":[],"label_agreement":null},{"id":"W2561341519","doi":"10.6000/1929-6002.2016.05.04.1","title":"Dehydrogenation Catalyst for Organic Hydride on the Basis of Superheated Liquid-Film Concept","year":2016,"lang":"en","type":"article","venue":"Journal of Technology Innovations in Renewable Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Dehydrogenation; Superheating; Methylcyclohexane; Catalysis; Hydrogen; Chemistry; Chemical engineering; Boiling; Hydride; Coke; Materials science; Organic chemistry; Inorganic chemistry; Thermodynamics","score_opus":0.011586364551939515,"score_gpt":0.23554521652908655,"score_spread":0.22395885197714704,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2561341519","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96198636,0.00014766991,0.03203121,0.0052845725,0.00017702895,0.00009395702,0.000017170536,0.00005122518,0.00021079426],"genre_scores_gemma":[0.9986883,0.000042753858,0.0006959325,0.000066360866,0.00006401674,0.000029842617,0.000010294558,0.00002923471,0.00037325537],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985016,0.00001668395,0.00090672594,0.00013961243,0.00020275135,0.00023264604],"domain_scores_gemma":[0.9981732,0.0004413867,0.0004994757,0.00034920825,0.00051339384,0.000023381912],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00047086822,0.00014204989,0.00033134938,0.0013017425,0.000053276086,0.0000035535181,0.00045185644,0.0002489984,0.00005047942],"category_scores_gemma":[0.0026153638,0.00008545231,0.00009967263,0.0022146585,0.00012349198,0.00015628345,0.00006130812,0.00017572082,9.512449e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000053476655,0.000057701647,0.000120231474,0.000008004932,0.00009929393,0.000003010635,0.00002754408,0.0037519406,0.97313064,0.019383067,0.00021915152,0.0031459383],"study_design_scores_gemma":[0.0007517338,0.00018635977,0.0000067005953,0.00018064167,0.000025295341,0.000061896855,0.00012973158,0.00071932835,0.99206966,0.0020996355,0.0036673965,0.000101622594],"about_ca_topic_score_codex":0.00013332278,"about_ca_topic_score_gemma":0.00015567146,"teacher_disagreement_score":0.036701936,"about_ca_system_score_codex":0.00032631264,"about_ca_system_score_gemma":0.00011189924,"threshold_uncertainty_score":0.3484644},"labels":[],"label_agreement":null},{"id":"W2562501361","doi":"10.82308/18169","title":"Effect of aeration strategy on the performance of a very high gravity continuous fuel ethanol fermentation process","year":2006,"lang":"en","type":"article","venue":"eScholarship@McGill (McGill)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada; Fonds Québécois de la Recherche sur la Nature et les Technologies","keywords":"Aeration; High Gravity; Fermentation; Process (computing); Environmental science; Process engineering; Pulp and paper industry; Waste management; Chemistry; Food science; Computer science; Engineering","score_opus":0.00791303199559371,"score_gpt":0.22878318231638542,"score_spread":0.2208701503207917,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2562501361","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99533737,0.000032987395,8.5434584e-7,0.0000074106906,0.00013494438,0.0005808137,0.00012996604,0.00010253296,0.0036730971],"genre_scores_gemma":[0.99949336,0.000010112707,0.000026728801,0.000014276643,0.000031579173,0.00009044711,0.00009889479,0.00005652959,0.00017805764],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978183,0.00017747,0.0006638608,0.00036212264,0.00061827915,0.00035996232],"domain_scores_gemma":[0.9985386,0.00036869512,0.00041532135,0.0004285807,0.00018540837,0.000063388325],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010867562,0.00033256423,0.00048164764,0.0001521931,0.00018828639,0.000014817086,0.00031146052,0.00020379397,0.0000310812],"category_scores_gemma":[0.0003268785,0.0002502792,0.00017428288,0.00046082638,0.000074708936,0.0005232313,0.00005878501,0.00053383043,0.000021810216],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028577287,0.000109784,0.00023980925,0.00078204315,0.00005432944,0.0000033020333,0.0000056479266,0.0034308534,0.9678066,0.009641114,1.5295547e-7,0.017640641],"study_design_scores_gemma":[0.000977251,0.0005836413,0.00092470006,0.00022476492,0.00008623864,0.0000088878105,0.000025667252,0.0008644168,0.99513274,0.00089447794,0.000029777548,0.0002474399],"about_ca_topic_score_codex":0.00041560497,"about_ca_topic_score_gemma":0.00004020764,"teacher_disagreement_score":0.027326185,"about_ca_system_score_codex":0.00027747476,"about_ca_system_score_gemma":0.000015274747,"threshold_uncertainty_score":0.99999493},"labels":[],"label_agreement":null},{"id":"W2566988826","doi":"10.1021/acs.iecr.6b03861","title":"Oligomerization of Fischer–Tropsch Tail Gas over H-ZSM-5","year":2016,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":29,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Canada-Israel Industrial Research and Development Foundation","keywords":"Fischer–Tropsch process; Space velocity; Olefin fiber; Catalysis; Chemistry; Dry gas; ZSM-5; Fraction (chemistry); Ethylene; Partial pressure; Organic chemistry; Syngas; Distillation; Chemical engineering; Zeolite; Oxygen; Selectivity","score_opus":0.06357401269044406,"score_gpt":0.3167119916734593,"score_spread":0.25313797898301527,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2566988826","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970388,0.00009844498,0.0003271738,0.00016197776,0.00018170627,0.0001938915,0.000050478848,0.00019949031,0.0017480281],"genre_scores_gemma":[0.99599904,0.000031438052,0.00004416954,0.0000012885077,0.0010448832,0.000043723336,0.000025745418,0.000090832575,0.0027189043],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99719584,0.000029571467,0.00055736984,0.00042183878,0.0009776716,0.0008176941],"domain_scores_gemma":[0.9983468,0.00048631887,0.000094914256,0.00063098076,0.00016922507,0.00027175923],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0009351119,0.00026809864,0.00039219213,0.00018862408,0.00005077386,0.000021588314,0.00053236284,0.00048616133,0.0006025402],"category_scores_gemma":[0.0030723698,0.0002175923,0.00015330968,0.0009231071,0.000108849425,0.00022178052,0.00025546306,0.000846872,0.0000444827],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000051097046,0.00003277128,0.00027916534,0.00011996837,0.00006906647,0.00001024037,0.000035826826,0.00048165797,0.9926621,0.00008735379,0.000084313004,0.0060864533],"study_design_scores_gemma":[0.0012347597,0.000024122906,0.000037801383,0.0003413853,0.000013432365,0.00001318118,0.000019792937,0.0020326367,0.9879648,0.000016638178,0.008042013,0.00025940826],"about_ca_topic_score_codex":0.00008872665,"about_ca_topic_score_gemma":4.805787e-7,"teacher_disagreement_score":0.007957701,"about_ca_system_score_codex":0.00043799277,"about_ca_system_score_gemma":0.00015244744,"threshold_uncertainty_score":0.88731563},"labels":[],"label_agreement":null},{"id":"W2567295735","doi":"10.1016/j.fuproc.2016.12.002","title":"Numerical study of methane steam reforming and methane combustion over the segmented and continuously coated layers of catalysts in a plate reactor","year":2016,"lang":"en","type":"article","venue":"Fuel Processing Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":60,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Royal Military College of Canada","funders":"Ministère de la Défense Nationale","keywords":"Steam reforming; Methane; Methane reformer; Catalysis; Catalytic combustion; Combustion; Hydrogen; Hydrogen production; Endothermic process; Materials science; Chemical engineering; Catalytic reforming; Chemistry; Organic chemistry; Engineering","score_opus":0.011456997828978471,"score_gpt":0.25538957230849463,"score_spread":0.24393257447951616,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2567295735","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9981497,0.0008579389,0.00031291734,0.00013232621,0.000030218564,0.00034867824,0.000006195705,0.00013669394,0.000025347394],"genre_scores_gemma":[0.99967366,0.000025446867,0.00019439236,0.0000041149347,0.000008896351,0.000031825526,0.000004311058,0.00003161048,0.000025737007],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984988,0.00004358799,0.0006001191,0.00033726767,0.00021607385,0.0003041305],"domain_scores_gemma":[0.9989703,0.00016922539,0.00039709054,0.00032228738,0.0000951489,0.00004590103],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00053013733,0.00020976705,0.0005931444,0.0004724528,0.000022645092,0.000003704753,0.00022931938,0.00023839125,0.0000026272608],"category_scores_gemma":[0.0005879907,0.000126664,0.000029901435,0.0008077899,0.00024287966,0.00019225078,0.00020729419,0.00029741533,4.5906097e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015022147,0.00014744737,0.0073221936,0.00029860358,0.000078732606,0.00001127261,0.0012176445,0.0000053503904,0.9658283,0.000030938576,5.509475e-7,0.024908742],"study_design_scores_gemma":[0.0034760002,0.00030682082,0.0014375784,0.00054939114,0.000105363644,0.000095083284,0.002547365,0.00092658354,0.9901313,0.0001746054,0.00002947972,0.00022042304],"about_ca_topic_score_codex":0.00052046997,"about_ca_topic_score_gemma":0.000057533107,"teacher_disagreement_score":0.02468832,"about_ca_system_score_codex":0.00009341316,"about_ca_system_score_gemma":0.00003338977,"threshold_uncertainty_score":0.5165208},"labels":[],"label_agreement":null},{"id":"W2582857696","doi":"10.1002/cjce.22787","title":"Modelling and optimization of hydrogen yield in membrane steam reforming reactors","year":2017,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Steam reforming; Hydrogen production; Membrane reactor; Hydrogen; Yield (engineering); Work (physics); Permeation; Process engineering; Chemical reaction engineering; Scaling; Chemistry; Nuclear engineering; Thermodynamics; Membrane; Materials science; Chemical engineering; Engineering; Physics; Mathematics; Catalysis","score_opus":0.016949162915375925,"score_gpt":0.20667422935358407,"score_spread":0.18972506643820813,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2582857696","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9971282,0.00036848205,0.0020704863,0.00011262499,0.000090838876,0.000055060977,0.0000028821362,0.000007473921,0.00016396568],"genre_scores_gemma":[0.99887276,0.000015052269,0.0009585516,0.0000042286,0.00010507808,0.0000010939776,0.0000012990064,0.000030041703,0.000011915845],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998988,0.0000043751243,0.00046614,0.00009271503,0.00017001586,0.00027880966],"domain_scores_gemma":[0.9990569,0.00009139125,0.00025571242,0.00027384472,0.00006087332,0.00026130606],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045705552,0.00013646144,0.00030737332,0.00020257643,0.000060992483,0.000022951828,0.0004091578,0.00011516398,0.000008338033],"category_scores_gemma":[0.00067953934,0.00010815639,0.00008261947,0.00009224599,0.00006202032,0.00029985464,0.000038698505,0.00044952956,2.551596e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000065827267,0.0000020501438,0.00005980762,0.00004751438,0.000023426197,0.000013952603,0.0002521775,0.73369634,0.26554608,0.00006697537,2.62156e-7,0.00028481078],"study_design_scores_gemma":[0.00018690148,0.0000061828478,0.000003555934,0.00029181017,0.000020248683,0.00008880154,0.00001863777,0.4477568,0.5514921,0.000017384638,0.000026214506,0.000091367925],"about_ca_topic_score_codex":0.0058714417,"about_ca_topic_score_gemma":0.00021420869,"teacher_disagreement_score":0.285946,"about_ca_system_score_codex":0.00023163647,"about_ca_system_score_gemma":0.00010721826,"threshold_uncertainty_score":0.8875903},"labels":[],"label_agreement":null},{"id":"W2582988119","doi":"10.1016/j.cattod.2017.01.027","title":"Steam reforming of ethanol over cerium-promoted Ni-Mg-Al hydrotalcite catalysts","year":2017,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":81,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Hydrotalcite; Space velocity; Chemistry; Steam reforming; Cerium; Ethanol; Yield (engineering); Hydrogen; Inorganic chemistry; Nuclear chemistry; Hydrogen production; Materials science; Organic chemistry; Metallurgy; Selectivity","score_opus":0.01540808081032042,"score_gpt":0.2777629901671438,"score_spread":0.2623549093568234,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2582988119","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99003094,0.00033006628,0.00016096202,0.000203509,0.00047993605,0.00031757983,0.0000825491,0.00024099468,0.008153443],"genre_scores_gemma":[0.99511164,0.000034572797,0.00017545484,0.0000467418,0.00023830752,0.000051045186,0.00041088095,0.00013740854,0.0037939528],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9964276,0.00003474618,0.00103497,0.00081772136,0.000830862,0.0008540962],"domain_scores_gemma":[0.9952066,0.00008790668,0.0009104919,0.0032833787,0.00018294822,0.00032869336],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00072481384,0.0005630874,0.0010968238,0.00041657657,0.00037833577,0.000064731306,0.0015797024,0.0003484063,0.00014592995],"category_scores_gemma":[0.0009144087,0.00050799054,0.00065395125,0.0004331274,0.00027930952,0.0011035652,0.00084944995,0.0005736259,0.00017828985],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000038840473,0.00010142257,0.00084140524,0.0001900361,0.0004480276,0.000035986588,0.00065237615,0.000052514468,0.9844184,0.000076437194,0.000115108436,0.0130294245],"study_design_scores_gemma":[0.0011078937,0.000039253806,0.0010315385,0.00020236927,0.0003199748,0.000051710307,0.00009585118,0.0030409838,0.98974097,0.00004165469,0.0036760678,0.0006517518],"about_ca_topic_score_codex":0.002046039,"about_ca_topic_score_gemma":0.00012395934,"teacher_disagreement_score":0.012377672,"about_ca_system_score_codex":0.00038870118,"about_ca_system_score_gemma":0.0000806428,"threshold_uncertainty_score":0.99973714},"labels":[],"label_agreement":null},{"id":"W2588269415","doi":"10.1002/cjce.22812","title":"Highly selective Fischer‐Tropsch synthesis for C<sub>10</sub>‐C<sub>20</sub> diesel fuel under low pressure","year":2017,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Atlantic Hydrogen (Canada); University of New Brunswick","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Fischer–Tropsch process; Syngas; Selectivity; Catalysis; Diesel fuel; Hydrocarbon; Chemistry; Hydrogen; Dissociation (chemistry); Chemical engineering; Organic chemistry","score_opus":0.009968212890241093,"score_gpt":0.20580324717635565,"score_spread":0.19583503428611454,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2588269415","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.993804,0.0012104233,0.0022432231,0.0012033472,0.00060229877,0.00035266508,0.00010994128,0.00008404489,0.00039010402],"genre_scores_gemma":[0.9983109,0.000014927667,0.00030015357,0.00004218531,0.0010311148,0.00004882108,0.00000934319,0.00016410099,0.00007844556],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974619,0.000021231142,0.0006963153,0.0003313935,0.00044817664,0.0010409526],"domain_scores_gemma":[0.99690455,0.0005944799,0.00044755047,0.00073516037,0.0003818411,0.000936413],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00064671965,0.0004914357,0.00073759403,0.00025725976,0.00033448808,0.00019511973,0.0013166433,0.00036888287,0.000017371716],"category_scores_gemma":[0.0030755927,0.0004046107,0.0005112491,0.00019903704,0.00017098481,0.00048768357,0.000102286365,0.0011051083,0.000016468455],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006173024,0.000014421892,0.000015815705,0.00027464196,0.00055111793,0.00003138265,0.00017954732,0.014996454,0.9819247,0.00035669658,0.00035959852,0.0012338967],"study_design_scores_gemma":[0.00064155547,0.00003135951,0.00006590743,0.0004037228,0.00034848615,0.00016946429,0.000021126807,0.015048989,0.98123115,0.0002320189,0.0013167999,0.0004894051],"about_ca_topic_score_codex":0.00033989007,"about_ca_topic_score_gemma":0.0003408862,"teacher_disagreement_score":0.0045069554,"about_ca_system_score_codex":0.00074074056,"about_ca_system_score_gemma":0.0004719582,"threshold_uncertainty_score":0.99984056},"labels":[],"label_agreement":null},{"id":"W2588308942","doi":"10.1016/j.ijhydene.2017.01.120","title":"Syngas production by the CO 2 reforming of CH 4 over Ni–Co–Mg–Al catalysts obtained from hydrotalcite precursors","year":2017,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":64,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Centre National de la Recherche Scientifique; Agence Universitaire de la Francophonie; Université du Littoral Côte d'Opale","keywords":"Hydrotalcite; Catalysis; Syngas; Calcination; Methane; Carbon dioxide reforming; Hydrogen; Hydrogen production; Chemistry; Methane reformer; Carbon monoxide; Inorganic chemistry; Temperature-programmed reduction; Cobalt; Materials science; Steam reforming; Organic chemistry","score_opus":0.010593104938734317,"score_gpt":0.2748329275184289,"score_spread":0.2642398225796946,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2588308942","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9961587,0.00051603705,0.00019908327,0.00067975087,0.0010631816,0.00005890885,0.00007502208,0.000020698664,0.0012285799],"genre_scores_gemma":[0.9977791,0.00010181249,0.00007044573,0.000052931784,0.0008923407,0.000005856225,0.00010954882,0.0000455582,0.0009424106],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99756926,0.00003699446,0.0008320587,0.00023973585,0.0010656329,0.000256322],"domain_scores_gemma":[0.9975574,0.00008294625,0.001406547,0.0005308573,0.00030886673,0.000113383336],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005088781,0.00023255026,0.00037456187,0.00019402218,0.00013980902,0.000055832956,0.0014284548,0.0000921724,0.000060209724],"category_scores_gemma":[0.00055555656,0.00016708582,0.00031711694,0.00007030428,0.00013441664,0.00080596487,0.00016127739,0.00032441085,0.0000064572],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001978788,0.000087729284,0.0010966165,0.000008558712,0.0010137396,0.00005772854,0.00036308146,0.0011294779,0.98780274,0.00017169605,0.0006506017,0.007420126],"study_design_scores_gemma":[0.000723595,0.000038115293,0.00020720458,0.00016930637,0.00007583629,0.0004562806,0.00007425033,0.0017979492,0.9809523,0.00024419563,0.015078056,0.0001829173],"about_ca_topic_score_codex":0.002522679,"about_ca_topic_score_gemma":0.00008733859,"teacher_disagreement_score":0.014427454,"about_ca_system_score_codex":0.00034678864,"about_ca_system_score_gemma":0.00007147355,"threshold_uncertainty_score":0.6813562},"labels":[],"label_agreement":null},{"id":"W2589799508","doi":"10.1002/bbb.1758","title":"Techno‐economic assessment of biogas to liquid fuels conversion technology via Fischer‐Tropsch synthesis","year":2017,"lang":"en","type":"article","venue":"Biofuels Bioproducts and Biorefining","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":66,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Institute of Food and Agriculture; McMaster University","keywords":"Biogas; Diesel fuel; Fischer–Tropsch process; Syngas; Waste management; Environmental science; Gasoline; Anaerobic digestion; Biofuel; Renewable energy; Liquid fuel; Pulp and paper industry; Engineering; Chemistry; Combustion; Hydrogen; Methane","score_opus":0.01502011410482924,"score_gpt":0.27369193787329293,"score_spread":0.2586718237684637,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2589799508","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99589723,0.00035492665,0.00020473974,0.0018731578,0.00027526854,0.00021572008,0.000052380627,0.00018035014,0.0009462294],"genre_scores_gemma":[0.9903623,0.00010280906,0.009160118,0.000019939887,0.0001582503,0.000025352754,0.000007721182,0.000045110355,0.000118403674],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99821335,0.00001063383,0.00045811269,0.0006899731,0.00017256163,0.00045538245],"domain_scores_gemma":[0.99844116,0.00004776321,0.00034952312,0.0009658441,0.00006611425,0.00012958933],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00049330224,0.00031048016,0.0005383976,0.00048299955,0.00033030528,0.000046321213,0.0005844421,0.0003060776,0.000045059805],"category_scores_gemma":[0.00036782026,0.00026445897,0.00009330555,0.00019910799,0.00033532857,0.00021115299,0.00068935426,0.0002331357,0.00003519568],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000034469154,0.000028398294,0.0031895651,0.00011993223,0.00007104968,0.0000058762294,0.000026288231,0.000005279358,0.97381884,0.0019697875,0.000005511751,0.020724995],"study_design_scores_gemma":[0.00029012057,0.00024635936,0.0007254194,0.00020124954,0.000058463265,0.000027199389,0.00008389911,0.000289268,0.9938178,0.00006301241,0.0038424395,0.00035478096],"about_ca_topic_score_codex":0.0003734783,"about_ca_topic_score_gemma":0.0000060819275,"teacher_disagreement_score":0.020370213,"about_ca_system_score_codex":0.00012498898,"about_ca_system_score_gemma":0.000052250976,"threshold_uncertainty_score":0.99998075},"labels":[],"label_agreement":null},{"id":"W2590207156","doi":"10.1002/9781119251101.ch10","title":"NATURAL GAS CONVERSION","year":2017,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Methane reformer; Steam reforming; Exothermic reaction; Partial oxidation; Endothermic process; Methane; Natural gas; Carbon dioxide reforming; Water-gas shift reaction; Sorbent; Chemical engineering; Chemistry; Catalysis; Waste management; Process engineering; Environmental science; Hydrogen production; Syngas; Engineering; Organic chemistry","score_opus":0.008597204206708535,"score_gpt":0.23829048242506223,"score_spread":0.2296932782183537,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2590207156","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00004757402,0.00075336825,0.000095356525,0.0000190448,0.0008421768,0.000077916535,0.0000069720722,0.00050303765,0.99765456],"genre_scores_gemma":[0.0016272335,0.00005572034,0.00024570245,0.000014179106,0.00045732153,0.0000025816682,0.00007806242,0.0003332191,0.997186],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9993981,0.0000023422635,0.00007204059,0.00018845803,0.00015065003,0.00018839931],"domain_scores_gemma":[0.99933434,0.000011493812,0.00009292631,0.00049597915,0.000007850709,0.00005742371],"candidate_categories":["insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.000036676753,0.00018047408,0.00023406577,0.0001062045,0.000021209687,0.000008827364,0.00028778767,0.0002376948,0.0040760487],"category_scores_gemma":[0.000054544147,0.00014053001,0.000114907765,0.000020404294,0.000026643245,0.000035212703,0.000113316804,0.0002504861,0.0010694715],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000057367242,0.000009486197,0.000007458775,0.00037165673,0.00015799975,0.000041343068,0.000014974593,4.556014e-7,0.04088881,0.0004779526,0.9450087,0.013015443],"study_design_scores_gemma":[0.00017746903,0.0000021742032,3.6823604e-7,0.0002009433,0.00002151198,0.000010977153,0.0000026101582,0.00029947757,0.04577174,0.000003787106,0.9533038,0.00020512585],"about_ca_topic_score_codex":0.0007387739,"about_ca_topic_score_gemma":0.00005077771,"teacher_disagreement_score":0.012810317,"about_ca_system_score_codex":0.00006313327,"about_ca_system_score_gemma":0.000010858203,"threshold_uncertainty_score":0.9997083},"labels":[],"label_agreement":null},{"id":"W2591425530","doi":"10.3390/catal7020069","title":"Effect of CO Concentration on the α-Value of Plasma-Synthesized Co/C Catalyst in Fischer-Tropsch Synthesis","year":2017,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); Université de Sherbrooke","funders":"","keywords":"Fischer–Tropsch process; Syngas; Catalysis; Space velocity; Hydrocarbon; Chemistry; Isothermal process; Selectivity; Wax; Diesel fuel; Molar ratio; Cobalt; Nuclear chemistry; Organic chemistry; Physics","score_opus":0.013685773940320828,"score_gpt":0.27678711092949093,"score_spread":0.2631013369891701,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2591425530","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99303037,0.000068177476,0.000018020239,0.000106271895,0.00010299357,0.0004443625,0.0000749994,0.000036858113,0.0061179344],"genre_scores_gemma":[0.9996017,0.000013202714,0.00002180912,0.00000558002,0.000056865938,0.000099841265,0.0000603306,0.000045311466,0.00009532973],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99805856,0.00015393956,0.0006335311,0.00033895794,0.000456753,0.00035827895],"domain_scores_gemma":[0.9956481,0.0022446637,0.00057072897,0.0014005683,0.00005026691,0.0000856915],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001383518,0.00029599434,0.0007578971,0.00011634286,0.00012337553,0.00002299022,0.00084513106,0.00018569583,0.000033044114],"category_scores_gemma":[0.005158475,0.00020427987,0.0002568485,0.0001488137,0.0002693537,0.0002138164,0.00008772991,0.00030379518,0.000053326094],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00039078036,0.00006829423,0.0033710133,0.00044454337,0.0001590816,0.000015101343,0.00035390595,0.00018710799,0.9889081,0.0009072043,0.000046700523,0.005148141],"study_design_scores_gemma":[0.00082255364,0.00007345912,0.0010719155,0.00042142667,0.00011033355,0.000007757206,0.00004219373,0.0029142494,0.9942001,0.0000073919036,0.00013747888,0.00019113766],"about_ca_topic_score_codex":0.00060256216,"about_ca_topic_score_gemma":0.000033501878,"teacher_disagreement_score":0.006571347,"about_ca_system_score_codex":0.0001625691,"about_ca_system_score_gemma":0.000050556446,"threshold_uncertainty_score":0.83302915},"labels":[],"label_agreement":null},{"id":"W2594663065","doi":"10.1039/c7cy00101k","title":"Steam methane reforming on a Ni-based bimetallic catalyst: density functional theory and experimental studies of the catalytic consequence of surface alloying of Ni with Ag","year":2017,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":69,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dow Chemical (Canada)","funders":"","keywords":"Bimetallic strip; Methane; Catalysis; Steam reforming; Alloy; Density functional theory; Materials science; Methane reformer; Chemical engineering; Inorganic chemistry; Chemistry; Metallurgy; Hydrogen production; Computational chemistry; Organic chemistry","score_opus":0.026975760518793985,"score_gpt":0.2871462203317104,"score_spread":0.2601704598129164,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2594663065","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9981321,0.0010109952,0.0002593161,0.0001030131,0.00009653179,0.0002291047,0.000012489298,0.00005268994,0.000103721795],"genre_scores_gemma":[0.9993916,0.000011965661,0.00044408845,0.000008919056,0.0000070227557,0.000016455257,0.0000052733267,0.000019811167,0.0000948381],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977238,0.00003545105,0.00055633864,0.00058954465,0.0006939072,0.00040096967],"domain_scores_gemma":[0.99667543,0.00024801926,0.000917862,0.0017249271,0.00036171032,0.0000720793],"candidate_categories":["sts"],"consensus_categories":[],"category_scores_codex":[0.0016903346,0.00027958298,0.0007893572,0.0005440482,0.00057134335,0.000016507933,0.001265893,0.00013715721,0.0000030833983],"category_scores_gemma":[0.0021261077,0.00018247019,0.00013289596,0.0013104003,0.00815841,0.00035376067,0.00075550226,0.00028948067,0.0000014324348],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000100069534,0.00006812213,0.0024448421,0.00010658009,0.0001783082,0.000008862808,0.0002934934,0.00070633,0.99390167,0.001567055,2.3110474e-7,0.00062443246],"study_design_scores_gemma":[0.00052322575,0.00012664555,0.00043503416,0.0002579946,0.00020199637,0.00011417685,0.0026449175,0.00039342867,0.99488,0.00022843106,0.000002782666,0.00019132263],"about_ca_topic_score_codex":0.0005192862,"about_ca_topic_score_gemma":0.00009735695,"teacher_disagreement_score":0.0075870664,"about_ca_system_score_codex":0.00028025862,"about_ca_system_score_gemma":0.00027627416,"threshold_uncertainty_score":0.9945408},"labels":[],"label_agreement":null},{"id":"W2600093336","doi":"10.1149/ma2011-01/43/2000","title":"Evaluation of Thermodynamic and Kinetic Parameters for Hydrogen Permeation through Palladium-Copper Alloys","year":2011,"lang":"en","type":"article","venue":"ECS Meeting Abstracts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut National de la Recherche Scientifique","funders":"","keywords":"Palladium; Copper; Hydrogen; Kinetic energy; Permeation; Materials science; Thermodynamics; Metallurgy; Chemistry; Inorganic chemistry; Catalysis; Organic chemistry; Membrane; Physics","score_opus":0.04814037718842241,"score_gpt":0.27225810281329516,"score_spread":0.22411772562487275,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2600093336","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9775364,0.00023598436,0.000084024556,0.0000117794525,0.00008396705,0.00038112016,0.000006650412,0.000059212885,0.02160087],"genre_scores_gemma":[0.9956141,0.000010118154,0.0041893567,0.0000075979096,0.000039585557,0.000047835725,0.00002699214,0.00004086785,0.000023553055],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99870104,0.000033815904,0.00038679037,0.00024190938,0.00039276315,0.00024365618],"domain_scores_gemma":[0.9991941,0.00015754653,0.00021558993,0.00020880773,0.00016984757,0.00005413064],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0013297035,0.00015644412,0.00020381744,0.000060084814,0.000041776504,0.0000067771357,0.000104034465,0.00010985601,0.0000138671185],"category_scores_gemma":[0.00089904293,0.00014631196,0.0000818788,0.00007834074,0.00004019298,0.00014500046,0.00002796991,0.00009748985,0.0000052984146],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000022776658,0.000033690103,0.00016540459,0.00010894728,0.00008025237,5.71985e-7,0.0021494033,0.021937715,0.97263175,0.000024371278,0.0000018268565,0.0028432833],"study_design_scores_gemma":[0.0006560379,0.00004350254,0.0026698115,0.00013816309,0.00027573152,0.000009002389,0.00015560145,0.13125467,0.86346394,0.0011312814,0.000022775526,0.00017947287],"about_ca_topic_score_codex":0.0004499552,"about_ca_topic_score_gemma":0.000020022911,"teacher_disagreement_score":0.10931696,"about_ca_system_score_codex":0.00010780232,"about_ca_system_score_gemma":0.000031178595,"threshold_uncertainty_score":0.59664285},"labels":[],"label_agreement":null},{"id":"W2602084074","doi":"10.1016/j.cattod.2017.03.006","title":"Activation mechanism and microstructural evolution of a YSZ/Ni-alumina catalyst for dry reforming of methane","year":2017,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":33,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Catalysis; Methane; Materials science; Carbon dioxide reforming; Yttria-stabilized zirconia; Chemical engineering; Mechanism (biology); Heterogeneous catalysis; Nanotechnology; Metallurgy; Chemistry; Cubic zirconia; Syngas; Ceramic; Organic chemistry; Engineering; Physics","score_opus":0.01239692681734231,"score_gpt":0.25737231903739227,"score_spread":0.24497539222004996,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2602084074","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9903857,0.00020207913,0.008649838,0.00004553188,0.00014606287,0.00030230786,0.00008516281,0.000036245838,0.00014707283],"genre_scores_gemma":[0.9970726,0.000010458287,0.0020474407,0.0000026746154,0.000092780014,0.000036879814,0.00021608974,0.000040878247,0.0004802252],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99845594,0.000013881172,0.00059005164,0.00036735655,0.00026270872,0.0003100717],"domain_scores_gemma":[0.99791044,0.0001056403,0.0007774965,0.0009065286,0.00020768626,0.000092190676],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005171648,0.00023918395,0.0006237935,0.00026148095,0.00015272609,0.000016416268,0.00040977242,0.00018229657,0.000008607693],"category_scores_gemma":[0.00095656264,0.00021483056,0.00024425506,0.00016205997,0.00015839176,0.00075205916,0.0002270834,0.00014181566,0.000001497629],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006507605,0.000018298804,0.0002519833,0.00042355832,0.00017202021,5.809445e-7,0.0005070776,0.000011383097,0.9877657,0.0022701856,0.000001520853,0.008512604],"study_design_scores_gemma":[0.000812102,0.000041704145,0.0007972959,0.00013840433,0.00026365547,0.000011041705,0.00038250684,0.0020427837,0.9938334,0.0013639608,0.00008376336,0.00022935917],"about_ca_topic_score_codex":0.0019096755,"about_ca_topic_score_gemma":0.00007834966,"teacher_disagreement_score":0.008283244,"about_ca_system_score_codex":0.00026199754,"about_ca_system_score_gemma":0.0000489783,"threshold_uncertainty_score":0.87605363},"labels":[],"label_agreement":null},{"id":"W2604976286","doi":"10.1039/c7ra00940b","title":"Bimodal NdNiAl and NdFeB hybrid catalytic and magnetic nanoparticles laminated on Fe foam: catalytic conversion of CO + 3H<sub>2</sub> to CH<sub>4</sub>","year":2017,"lang":"en","type":"article","venue":"RSC Advances","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Korea Institute of Materials Science","keywords":"Catalysis; Neodymium magnet; Sintering; Materials science; Nanoparticle; Chemical engineering; Composite material; Nanotechnology; Magnet; Chemistry; Organic chemistry; Mechanical engineering","score_opus":0.00896720534774667,"score_gpt":0.23991113780618842,"score_spread":0.23094393245844175,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2604976286","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99782723,0.0010648074,0.00005377448,0.000119633136,0.00021073484,0.00036106724,0.000081277074,0.00009682958,0.00018464534],"genre_scores_gemma":[0.999308,0.00031045268,0.00007916443,0.00002916717,0.000099934936,0.000024283883,0.000044472996,0.00005935988,0.000045157056],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980015,0.000021806121,0.00044125522,0.00059031765,0.00039430498,0.0005508171],"domain_scores_gemma":[0.99852115,0.00020405866,0.00024845861,0.0006377833,0.0000786231,0.00030991258],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00023699176,0.00037466997,0.0005608373,0.00019384727,0.00025226834,0.000061114835,0.00033357716,0.00010293449,0.000004908899],"category_scores_gemma":[0.0004844832,0.00035020412,0.00008665122,0.00013994171,0.0003340165,0.0005680007,0.00027895003,0.0002258404,0.000064732085],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015991686,0.000051918556,0.0005127256,0.0003888811,0.000030244762,0.000044159242,0.00017851751,0.00008655752,0.93861306,0.000058084268,0.00001178994,0.059864163],"study_design_scores_gemma":[0.0012741748,0.0003049304,0.0017895824,0.00028267296,0.00009612579,0.000072113566,0.000089146946,0.002392465,0.9927937,0.0001015375,0.00038133014,0.00042223008],"about_ca_topic_score_codex":0.00007865866,"about_ca_topic_score_gemma":0.000043994383,"teacher_disagreement_score":0.05944193,"about_ca_system_score_codex":0.00011778026,"about_ca_system_score_gemma":0.000037294034,"threshold_uncertainty_score":0.999895},"labels":[],"label_agreement":null},{"id":"W2605368857","doi":"10.1007/s13404-017-0205-0","title":"Gold-promoted plasma-synthesized Ni-Co-Fe/C catalyst for Fischer-Tropsch synthesis","year":2017,"lang":"en","type":"article","venue":"Gold bulletin","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Materials science; Plasma; Chemical engineering; Chemistry; Organic chemistry; Engineering; Physics","score_opus":0.02160530178344509,"score_gpt":0.2581755910418959,"score_spread":0.23657028925845083,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2605368857","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96586,0.00023576223,0.0007735396,0.0043015624,0.0007266494,0.0012432651,0.00037860466,0.0008160887,0.025664523],"genre_scores_gemma":[0.9676016,0.000024073523,0.005065283,0.00006240681,0.00070395746,0.00061746466,0.00011335665,0.00023304061,0.025578808],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99722475,0.000038468483,0.0006346481,0.0007488845,0.0004274074,0.0009258679],"domain_scores_gemma":[0.9967181,0.00067903026,0.0004163083,0.0018036411,0.0001116905,0.00027119456],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0007554761,0.00051667914,0.0008045601,0.00015512554,0.00032047383,0.00015876746,0.001318128,0.00037542838,0.0005142776],"category_scores_gemma":[0.0051042098,0.00047711993,0.0004586199,0.00009217673,0.00014667003,0.00015972462,0.0002764575,0.0004144015,0.0012307444],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00036665733,0.00016572552,0.00018837553,0.0005416657,0.00042589993,0.00006057012,0.00019339027,0.00003611919,0.95041215,0.00044954254,0.012553367,0.034606513],"study_design_scores_gemma":[0.0011686949,0.000028980017,0.000117092546,0.00020162172,0.00017591579,0.00003758461,0.000053568103,0.0014779434,0.7610518,0.000031926636,0.23504655,0.0006083433],"about_ca_topic_score_codex":0.00070332474,"about_ca_topic_score_gemma":0.00003582237,"teacher_disagreement_score":0.22249319,"about_ca_system_score_codex":0.00022517514,"about_ca_system_score_gemma":0.000046849495,"threshold_uncertainty_score":0.9997681},"labels":[],"label_agreement":null},{"id":"W2607109465","doi":"10.1021/jacs.7b01632","title":"Consequences of Surface Oxophilicity of Ni, Ni-Co, and Co Clusters on Methane Activation","year":2017,"lang":"en","type":"article","venue":"Journal of the American Chemical Society","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":151,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada; Government of Canada; Canada Foundation for Innovation; Ontario Centres of Excellence","keywords":"Chemistry; Methane; Chemical engineering; Organic chemistry","score_opus":0.020035845449096697,"score_gpt":0.29280121939696596,"score_spread":0.27276537394786926,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2607109465","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99866366,0.00003131566,0.000059071437,0.0008410699,0.00005829699,0.000060224862,0.000012040719,0.0000060778184,0.0002682133],"genre_scores_gemma":[0.99886715,0.00005943779,0.000854702,0.00007983347,0.00007530331,4.406814e-7,9.392204e-7,0.000013614338,0.000048553553],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99879926,0.000025584712,0.0004568578,0.00011833227,0.0004308724,0.00016907416],"domain_scores_gemma":[0.9973625,0.00028164967,0.0018269169,0.00033522208,0.0001103276,0.00008337161],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00048088573,0.00013673659,0.00053635566,0.000017208366,0.00006329898,0.000009460358,0.000512848,0.00006874011,0.0000062364747],"category_scores_gemma":[0.00065081986,0.00008977003,0.00035613336,0.000103371975,0.0010784601,0.00014669773,0.00010874885,0.00041531445,2.998048e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010250056,0.000037827434,0.002156693,0.000058129437,0.00016169819,4.2668117e-7,0.00030884898,0.00012653231,0.9962761,0.000017185592,0.00007952925,0.0006745647],"study_design_scores_gemma":[0.00043040904,0.0000630874,0.0011914523,0.00014278537,0.000054520446,0.000025308063,0.0003762628,0.00021276779,0.9972412,0.00012042876,0.000048524565,0.000093276765],"about_ca_topic_score_codex":0.0003798965,"about_ca_topic_score_gemma":5.060827e-7,"teacher_disagreement_score":0.0014367665,"about_ca_system_score_codex":0.00014541551,"about_ca_system_score_gemma":0.000046202367,"threshold_uncertainty_score":0.39736316},"labels":[],"label_agreement":null},{"id":"W2618517203","doi":"10.1039/c7se00212b","title":"Insights on pathways for hydrogen generation from ethanol","year":2017,"lang":"en","type":"article","venue":"Sustainable Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":158,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"York University; Saskatoon Medical Imaging; University of Saskatchewan; Toronto Public Health","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Hydrogen; Ethanol; Chemistry; Computer science; Environmental science; Biochemistry; Organic chemistry","score_opus":0.021382243989104783,"score_gpt":0.24226365782476755,"score_spread":0.22088141383566276,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2618517203","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97964245,0.0004760353,0.006300655,0.00015516825,0.00033177156,0.00024654224,0.000028028511,0.00019786131,0.012621476],"genre_scores_gemma":[0.9848197,0.000021553613,0.0002761757,0.00009152281,0.0011260733,0.00022504924,0.00027061003,0.00008231928,0.01308697],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99844015,0.000015308908,0.0002799807,0.00045686797,0.00025299026,0.00055469456],"domain_scores_gemma":[0.99841917,0.000093264636,0.00018319923,0.0010014181,0.00015547537,0.00014744846],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001253757,0.0002668561,0.0003040624,0.00011629155,0.00053701585,0.00010115065,0.0004906819,0.00022553885,0.00003234345],"category_scores_gemma":[0.0004387923,0.0002451608,0.00018207717,0.00006854894,0.0000409602,0.00046351683,0.00017671102,0.00014385558,0.00001425848],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003859459,0.000037897476,0.0000053911763,0.00004118225,0.000076799646,0.000049750073,0.00020329171,0.0012774748,0.8442088,0.14836143,0.00010823786,0.005591201],"study_design_scores_gemma":[0.0006876924,0.000059714617,0.0000097423235,0.0000235475,0.00003399469,0.0000013467252,0.00014570958,0.0050391247,0.9089201,0.018296571,0.06648342,0.00029899867],"about_ca_topic_score_codex":0.0017145163,"about_ca_topic_score_gemma":0.000064118925,"teacher_disagreement_score":0.13006486,"about_ca_system_score_codex":0.0003587676,"about_ca_system_score_gemma":0.00008092344,"threshold_uncertainty_score":0.99973667},"labels":[],"label_agreement":null},{"id":"W2622092165","doi":"10.1007/s10562-017-2090-9","title":"Fischer–Tropsch Synthesis: XANES Spectra of Potassium in Promoted Precipitated Iron Catalysts as a Function of Time On-stream","year":2017,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"","keywords":"XANES; Catalysis; Chemistry; Potassium; Inorganic chemistry; Oxidizing agent; Heterogeneous catalysis; Sintering; Spectral line; Organic chemistry","score_opus":0.0086180046523884,"score_gpt":0.22543773914876367,"score_spread":0.21681973449637526,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2622092165","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9977991,0.000057217396,0.00004914287,0.0004862065,0.00009076038,0.0002671107,0.000038987975,0.00007673338,0.001134745],"genre_scores_gemma":[0.9991536,0.0000069071175,0.00011359226,0.000026164069,0.00007947076,0.000056001725,0.00021358722,0.000063471016,0.00028716953],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99780834,0.00005083469,0.0007280218,0.0005133926,0.00047028434,0.00042911278],"domain_scores_gemma":[0.99757165,0.0001806889,0.0006363649,0.0014308876,0.00006922521,0.00011119769],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00039507422,0.0003477592,0.0007871386,0.00047338533,0.00007723942,0.000025451187,0.00064531615,0.00017921753,0.00008381102],"category_scores_gemma":[0.0009565311,0.00032206695,0.0003243679,0.0003589983,0.00016982823,0.0003653184,0.00012876317,0.00032310365,0.00011884542],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018069783,0.0001737274,0.0011021079,0.00023070286,0.00028324738,0.000029157287,0.0003347957,0.0005881592,0.99331933,0.0000120509785,0.00006161142,0.003684417],"study_design_scores_gemma":[0.00059929205,0.00007071052,0.006486443,0.00033812385,0.0003542973,0.000010480201,0.000057405996,0.00086337974,0.9908255,0.0000090830035,0.00006443167,0.00032087238],"about_ca_topic_score_codex":0.0012552238,"about_ca_topic_score_gemma":0.000059882885,"teacher_disagreement_score":0.005384335,"about_ca_system_score_codex":0.00022385543,"about_ca_system_score_gemma":0.00003659432,"threshold_uncertainty_score":0.9999231},"labels":[],"label_agreement":null},{"id":"W2623378581","doi":"10.14447/jnmes.v13i3.167","title":"Tungsten effect over co-hydrotalcite catalysts to produce hydrogen from bio-ethanol","year":2010,"lang":"en","type":"article","venue":"Journal of New Materials for Electrochemical Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Hydrotalcite; Catalysis; Physisorption; Hydrogen production; Tungsten; Hydrogen; Chemistry; Inorganic chemistry; Mesoporous material; Nuclear chemistry; Materials science; Chemical engineering; Organic chemistry","score_opus":0.00777136811967007,"score_gpt":0.26250190765154285,"score_spread":0.2547305395318728,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2623378581","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99617016,0.00026526387,0.0005773605,0.00011965056,0.0016303213,0.0009909153,0.0000882007,0.00009560748,0.00006249175],"genre_scores_gemma":[0.994167,0.0000039955285,0.00021199037,0.000035266068,0.004918668,0.00007135561,0.00010995375,0.00013543981,0.00034637103],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9964377,0.00005265678,0.0014124752,0.00047835658,0.00081910304,0.0007996661],"domain_scores_gemma":[0.9974779,0.00031479532,0.0007446554,0.0005528608,0.00024294095,0.0006668333],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012236547,0.0004905023,0.0013129272,0.0002523153,0.000059704635,0.00011724865,0.00075190084,0.00040971496,0.00006782317],"category_scores_gemma":[0.0013118773,0.00038180227,0.000411711,0.00029329475,0.000030143927,0.00030082001,0.00009365035,0.0005044817,0.00006715967],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000610681,0.000039916944,0.00006223893,0.00022805194,0.00032722673,0.000013998279,0.00013117158,0.00001436012,0.99729097,0.000016981518,0.0010396211,0.00022478467],"study_design_scores_gemma":[0.0015670757,0.00034156832,0.000014768326,0.00025362975,0.00021033389,0.00046797647,0.0000071735344,0.000089626614,0.98805875,0.00006926627,0.008481369,0.00043845622],"about_ca_topic_score_codex":0.00033900118,"about_ca_topic_score_gemma":0.0000075891867,"teacher_disagreement_score":0.009232211,"about_ca_system_score_codex":0.00035678537,"about_ca_system_score_gemma":0.00014630926,"threshold_uncertainty_score":0.9998634},"labels":[],"label_agreement":null},{"id":"W2670226855","doi":"10.1039/c7cs00026j","title":"Heterogeneous catalytic hydrogenation of CO<sub>2</sub>by metal oxides: defect engineering – perfecting imperfection","year":2017,"lang":"en","type":"review","venue":"Chemical Society Reviews","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":390,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto; Toronto Public Health","funders":"Engineering and Physical Sciences Research Council","keywords":"Catalysis; Metal; Catalytic hydrogenation; Materials science; Chemistry; Nanotechnology; Metallurgy; Organic chemistry","score_opus":0.04358468711400098,"score_gpt":0.3106885341483419,"score_spread":0.2671038470343409,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2670226855","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0057158973,0.9918118,0.0003504889,0.0000020067268,0.00025671546,0.0014571394,0.0000865584,0.0002376934,0.000081688784],"genre_scores_gemma":[0.0020581794,0.99534345,0.0002092812,0.0000072310722,0.00045748756,0.00041952354,0.001179994,0.00028758243,0.000037271693],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9952591,0.0000906723,0.0022017576,0.001063235,0.0005383488,0.00084687985],"domain_scores_gemma":[0.99609065,0.0004262408,0.0017994667,0.0012851092,0.000090528345,0.00030803305],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0014905438,0.0012160286,0.004718652,0.000106028754,0.00015861061,0.000054398075,0.0008675791,0.0011117196,0.000015818126],"category_scores_gemma":[0.0016567265,0.0010409093,0.007120067,0.00046311214,0.0001246933,0.00028136803,0.00030788413,0.0014362334,0.00013362186],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000011895511,0.000042588665,4.683072e-7,0.041859943,0.0006462063,0.000002230233,0.00005406379,0.000010429907,0.51008767,0.0000018338584,0.00013097952,0.44716236],"study_design_scores_gemma":[0.00017500491,0.000020330792,1.1667216e-8,0.009811405,0.0019931896,0.00022488256,0.0000027350875,0.0005647996,0.54508656,0.0000012389804,0.44136024,0.00075963023],"about_ca_topic_score_codex":0.000023541908,"about_ca_topic_score_gemma":6.225862e-7,"teacher_disagreement_score":0.44640273,"about_ca_system_score_codex":0.0013367864,"about_ca_system_score_gemma":0.00010404486,"threshold_uncertainty_score":0.9992041},"labels":[],"label_agreement":null},{"id":"W2733910078","doi":"10.1016/b978-0-08-101031-0.00011-9","title":"Advancements and confinements in hydrogen production technologies","year":2017,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":31,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; Université de Sherbrooke; York University","funders":"","keywords":"Hydrogen production; Steam reforming; Raw material; Syngas; Hydrogen; Hydrogen fuel; Energy carrier; Hydrogen technologies; Waste management; Fuel cells; Biochemical engineering; Environmental science; Process engineering; Chemistry; Hydrogen economy; Engineering; Chemical engineering; Organic chemistry","score_opus":0.01530109506305122,"score_gpt":0.24663667782282264,"score_spread":0.23133558275977142,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2733910078","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0043033105,0.0021260853,0.0000011713093,0.00004917014,0.00025064955,0.0006125585,0.000013469856,0.0002239329,0.99241966],"genre_scores_gemma":[0.013217602,0.0003363968,0.00010647713,0.000006957422,0.00009512602,0.00006712642,0.000032388616,0.00008033635,0.9860576],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99863845,0.0000029744815,0.0003684177,0.00048589936,0.00022948865,0.00027477017],"domain_scores_gemma":[0.99897635,0.000011092562,0.00025008005,0.0006909472,0.000031686435,0.00003982604],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001606083,0.0003474214,0.00046083948,0.00023711026,0.000065989494,0.0000139831545,0.00027674073,0.00031771557,0.000024876803],"category_scores_gemma":[0.00010797164,0.00033366244,0.000074270836,0.0000064702476,0.00013322958,0.00008052464,0.000296965,0.00047383897,0.000037571514],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000008821078,0.000003886633,0.000016793789,0.00017020985,0.0000665881,0.000027984519,0.00005453147,0.0000015992401,0.012108763,0.0004853006,0.0000018334815,0.9870537],"study_design_scores_gemma":[0.000466603,0.000023536702,0.0000042262864,0.0012198669,0.00007506098,0.00004361067,0.000016476111,0.000021977878,0.08378639,0.004975094,0.9088429,0.00052425364],"about_ca_topic_score_codex":0.0000019777578,"about_ca_topic_score_gemma":0.000035059653,"teacher_disagreement_score":0.9865294,"about_ca_system_score_codex":0.00016020657,"about_ca_system_score_gemma":0.000022023625,"threshold_uncertainty_score":0.99991155},"labels":[],"label_agreement":null},{"id":"W2734562633","doi":"10.1134/s0965544117070040","title":"Catalysis in the dispersed phase: Slurry technology in the synthesis of dimethyl ether (Review)","year":2017,"lang":"en","type":"article","venue":"Petroleum Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Institute of Coal Chemistry, Chinese Academy of Sciences; Dalian Institute of Chemical Physics; University of Calgary","keywords":"Dimethyl ether; Slurry; Syngas; Methanol; Catalysis; Ether; Chemical engineering; Inert; Materials science; Organic chemistry; Chemistry; Engineering; Composite material","score_opus":0.011781966230849556,"score_gpt":0.28679742022715776,"score_spread":0.2750154539963082,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2734562633","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9817161,0.005456955,0.00002072989,0.0029761111,0.000027553722,0.00012841419,0.000017606659,0.000034188473,0.00962237],"genre_scores_gemma":[0.9990058,0.00046676534,0.00004542317,0.000044398967,0.00005341087,0.00016410547,0.000016040261,0.000024165178,0.0001799214],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985752,0.000035159406,0.00044381866,0.0002801746,0.00033145558,0.0003341672],"domain_scores_gemma":[0.99766374,0.00032694134,0.0002624365,0.0016959475,0.000022978276,0.000027958104],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001067086,0.00021359227,0.0004760358,0.00007317745,0.000080640406,0.000013231194,0.0017372102,0.00018243399,0.00008536506],"category_scores_gemma":[0.0019698665,0.00013001842,0.00019792024,0.00029315494,0.00020640141,0.00008557794,0.00014910239,0.00059517036,0.000010231972],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000018383505,0.00023866097,0.0010571027,0.0010469721,0.00006533437,0.00004112872,0.00032712947,0.000024945795,0.9870937,0.00007223005,0.00004591345,0.009968541],"study_design_scores_gemma":[0.0006973841,0.000007261067,0.00018799963,0.0007251368,0.0001428156,0.00004714179,0.0009318996,0.00081585377,0.99347687,0.00008458845,0.0026537157,0.0002293082],"about_ca_topic_score_codex":0.0002450946,"about_ca_topic_score_gemma":0.000026933405,"teacher_disagreement_score":0.017289698,"about_ca_system_score_codex":0.00008804547,"about_ca_system_score_gemma":0.00002466793,"threshold_uncertainty_score":0.5301997},"labels":[],"label_agreement":null},{"id":"W2736729186","doi":"10.1039/c7cy01436h","title":"Insight into the preferred formation mechanism of long-chain hydrocarbons in Fischer–Tropsch synthesis on Hcp Co(10−11) surfaces from DFT and microkinetic modeling","year":2017,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":43,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China; Santen; University of Windsor","keywords":"Fischer–Tropsch process; Hydrocarbon; Chemistry; Catalysis; Mechanism (biology); Chain (unit); Chemical engineering; Organic chemistry; Selectivity; Physics","score_opus":0.01604591679277856,"score_gpt":0.24857594786823164,"score_spread":0.2325300310754531,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2736729186","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99356514,0.00028313755,0.004965234,0.00055179006,0.00004477858,0.0001912834,0.0000062129684,0.000088181696,0.00030426713],"genre_scores_gemma":[0.99934137,0.000051692725,0.00047249554,0.000007329252,0.0000116076635,0.000052307852,0.000012069258,0.000019431318,0.00003168783],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982385,0.000020677287,0.00046109463,0.0005182035,0.00036436683,0.00039715302],"domain_scores_gemma":[0.9981386,0.00014142574,0.0002970048,0.0013070707,0.000051659914,0.00006420528],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00070625875,0.00022421694,0.00042727977,0.0009141766,0.00036458403,0.000060154453,0.0014406289,0.00023908919,0.0000061365586],"category_scores_gemma":[0.0015071962,0.00016866256,0.00007088555,0.0008125031,0.0008128805,0.0005301893,0.00047361632,0.00026882184,0.000008550555],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001067977,0.000028529348,0.0005665592,0.000018217099,0.000021752165,0.000004249695,0.0012152295,0.0019599504,0.9892481,0.0006765049,3.7781177e-7,0.006249882],"study_design_scores_gemma":[0.00014797674,0.0000144229425,0.00009348011,0.000082089,0.000042733405,0.000005626292,0.00033636438,0.3000315,0.69799834,0.0010941257,0.00001657917,0.00013674457],"about_ca_topic_score_codex":0.0012467351,"about_ca_topic_score_gemma":0.0009791543,"teacher_disagreement_score":0.29807156,"about_ca_system_score_codex":0.00019393617,"about_ca_system_score_gemma":0.0000478049,"threshold_uncertainty_score":0.687786},"labels":[],"label_agreement":null},{"id":"W2737437113","doi":"10.1007/978-3-319-61112-9","title":"Renewable Synthetic Fuels and Chemicals from Carbon Dioxide","year":2017,"lang":"en","type":"book","venue":"SpringerBriefs in energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":48,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Renewable energy; Carbon dioxide; Renewable fuels; Environmental science; Carbon-neutral fuel; Waste management; Fossil fuel; Natural resource economics; Biochemical engineering; Engineering; Chemistry; Syngas; Economics; Organic chemistry","score_opus":0.00966257293223489,"score_gpt":0.2150028812769297,"score_spread":0.20534030834469483,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2737437113","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.04103221,0.017141825,0.00012691489,0.0000657325,0.000885129,0.00020954447,0.00008899208,0.00038018386,0.9400695],"genre_scores_gemma":[0.095077604,0.0024400319,0.00048733247,0.00006422367,0.0017688351,0.00010515177,0.0002790581,0.00048881874,0.89928895],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9973143,0.000018700352,0.000642762,0.0009587216,0.00041415557,0.00065136375],"domain_scores_gemma":[0.99764156,0.0002397406,0.00034794016,0.0015017039,0.00003578844,0.00023325284],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00023706628,0.00063452014,0.0011123521,0.00024513385,0.000056342775,0.000042962238,0.0007111996,0.00087215484,0.000064363296],"category_scores_gemma":[0.0004030174,0.00066894916,0.00020052145,0.00005993666,0.00017858761,0.00011664248,0.0006535143,0.0006666621,0.000009495473],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009332781,0.00007465531,0.00012460494,0.00086259237,0.00055121444,0.0005792208,0.0002804859,0.0009252238,0.9570674,0.006348295,0.00036484038,0.032728154],"study_design_scores_gemma":[0.0005630249,0.000012741717,0.000014641184,0.0020391543,0.00012590086,0.000024606326,0.0000048556108,0.00077311177,0.62571037,0.009276603,0.36043066,0.0010243403],"about_ca_topic_score_codex":0.015660306,"about_ca_topic_score_gemma":0.0010688051,"teacher_disagreement_score":0.36006582,"about_ca_system_score_codex":0.00072499685,"about_ca_system_score_gemma":0.00014413227,"threshold_uncertainty_score":0.99957615},"labels":[],"label_agreement":null},{"id":"W2747069120","doi":"10.1016/j.apcata.2017.08.032","title":"Performances of promoted cobalt catalysts supported on mesoporous alumina for Fischer-Tropsch synthesis","year":2017,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); Université de Sherbrooke; University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; BioFuelNet Canada; University of Saskatchewan","keywords":"Fischer–Tropsch process; Cobalt; Catalysis; Space velocity; Syngas; Mesoporous material; Selectivity; Inorganic chemistry; Materials science; Dispersion (optics); Transition metal; Chemistry; Chemical engineering; Organic chemistry","score_opus":0.019561567771780232,"score_gpt":0.27288108828020036,"score_spread":0.2533195205084201,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2747069120","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99186414,0.00008674307,0.0003184028,0.00009977946,0.00014127453,0.0006687378,0.00015309254,0.00013625761,0.0065315776],"genre_scores_gemma":[0.99522924,0.000015968333,0.0018911784,0.000020170977,0.00030644215,0.00058722653,0.0006594487,0.00009041517,0.0011999193],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972315,0.000014430981,0.0007829577,0.0007097327,0.0005662457,0.0006951721],"domain_scores_gemma":[0.99694985,0.0001463239,0.0007149423,0.001841521,0.00014202301,0.0002053266],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005861299,0.00047456188,0.0010295649,0.00024602516,0.0003909895,0.0000565873,0.0010584962,0.00024345687,0.000055143206],"category_scores_gemma":[0.00031675465,0.00041732163,0.0004685168,0.0002269664,0.00019185519,0.00023195794,0.00022149991,0.00024213198,0.00005055182],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002816154,0.00022944463,0.00031964143,0.00036023074,0.00086114666,0.000007917145,0.0004827406,0.00037138135,0.965699,0.0014657959,0.00032169127,0.029599402],"study_design_scores_gemma":[0.00090906135,0.00006874299,0.00048434202,0.000048805192,0.00055878883,0.000011709477,0.000108615284,0.006611259,0.98908705,0.000054883203,0.0015605645,0.0004961689],"about_ca_topic_score_codex":0.00059883774,"about_ca_topic_score_gemma":0.00009004877,"teacher_disagreement_score":0.029103234,"about_ca_system_score_codex":0.00017063167,"about_ca_system_score_gemma":0.0000811008,"threshold_uncertainty_score":0.99982786},"labels":[],"label_agreement":null},{"id":"W2749887736","doi":"10.1002/cjce.23005","title":"Utilization of sol‐gel CuO‐ZnO‐Al<sub>2</sub>O<sub>3</sub> catalysts in the methanol steam reforming for hydrogen production","year":2017,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Coordenação de Aperfeiçoamento de Pessoal de Nível Superior","keywords":"Catalysis; Hydrogen production; Steam reforming; Calcination; Sintering; Methanol; Materials science; Chemical engineering; Hydrogen; Dispersion (optics); Electrolyte; Metal; Inorganic chemistry; Metallurgy; Chemistry; Electrode; Organic chemistry","score_opus":0.02259026524933171,"score_gpt":0.24324936245811793,"score_spread":0.2206590972087862,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2749887736","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9973124,0.00052449934,0.0005735908,0.000670212,0.0004210142,0.0004047322,0.000019814477,0.000025297022,0.000048399208],"genre_scores_gemma":[0.9991714,0.000026073465,0.00011985776,0.000031651005,0.00050486025,0.000032504468,0.000022200174,0.00008652998,0.00000495407],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997597,0.000028238228,0.0009365273,0.00026787515,0.0004851177,0.00068526395],"domain_scores_gemma":[0.99783075,0.00018158891,0.0006334111,0.00078055967,0.00024509578,0.0003286066],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0017295604,0.0003381697,0.0005609784,0.00038304247,0.0002181101,0.00005365235,0.0011296181,0.00021495843,0.0000012553071],"category_scores_gemma":[0.0026134276,0.0002476131,0.00033215628,0.00030137956,0.00012999763,0.0005551896,0.00007030239,0.00080010394,0.0000024147935],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000029779607,0.0000150963115,0.00003223184,0.00017257694,0.00010598066,0.000015482687,0.00085935503,0.007554752,0.9823494,0.00008692358,0.000029233153,0.00874919],"study_design_scores_gemma":[0.00052416284,0.000028529565,0.000048865622,0.00041554074,0.00012490516,0.0003086779,0.00009854507,0.010116093,0.98759174,0.00012445262,0.00034426808,0.00027422313],"about_ca_topic_score_codex":0.0006688844,"about_ca_topic_score_gemma":0.0009422557,"teacher_disagreement_score":0.0084749665,"about_ca_system_score_codex":0.00073261483,"about_ca_system_score_gemma":0.00032539683,"threshold_uncertainty_score":0.9999976},"labels":[],"label_agreement":null},{"id":"W2754924817","doi":"","title":"Plant Performance Test for the Deethanizer Overhead Recycle (DOR) Process","year":2006,"lang":"en","type":"article","venue":"Chemeca 2006: Knowledge and Innovation","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Operability; Methane; Waste management; Overhead (engineering); Extraction (chemistry); Recovery rate; Process (computing); Process engineering; Engineering; Environmental science; Chemistry; Environmental engineering; Chromatography; Computer science; Reliability engineering; Organic chemistry; Electrical engineering","score_opus":0.01674492842273151,"score_gpt":0.2599464079627273,"score_spread":0.24320147953999577,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2754924817","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.984238,0.0009179438,0.0025118697,0.00013573407,0.00021017356,0.00040609878,0.00003789404,0.00013202883,0.011410225],"genre_scores_gemma":[0.9948858,0.000028213559,0.00015161626,0.00003440981,0.00062117697,0.00012042138,0.00023133469,0.000036149577,0.0038909009],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99903506,0.000002814097,0.00035571586,0.00022061332,0.000115685194,0.0002701268],"domain_scores_gemma":[0.9992468,0.00017792535,0.00010707532,0.00018410647,0.00026292788,0.000021161168],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002949558,0.00016861998,0.00015959467,0.00014239672,0.0001613021,0.00002224456,0.0001302663,0.00010644131,0.000018641716],"category_scores_gemma":[0.00021902237,0.00012314795,0.000033022137,0.0009170054,0.000038434093,0.00024178455,0.00003699105,0.00015625215,0.000017135697],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009270337,0.0002658704,0.0062369537,0.0012648583,0.000057068784,9.5192036e-7,0.00067929237,0.00014372465,0.90583193,0.00926196,0.0054182736,0.070746414],"study_design_scores_gemma":[0.0007014207,0.000038589627,0.0013607179,0.00009456425,0.00003010036,0.000015362148,0.000051399427,0.03778288,0.9065162,0.00034905042,0.052815508,0.00024421854],"about_ca_topic_score_codex":0.000017792694,"about_ca_topic_score_gemma":0.000014516485,"teacher_disagreement_score":0.0705022,"about_ca_system_score_codex":0.00007686534,"about_ca_system_score_gemma":0.000033853663,"threshold_uncertainty_score":0.5021828},"labels":[],"label_agreement":null},{"id":"W2761826041","doi":"10.1016/j.cattod.2017.10.008","title":"A study of CO 2 reforming of CH 4 for coal delivered gases over Ni-based catalysts","year":2017,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs","keywords":"Catalysis; Coal; Chemistry; Carbon dioxide reforming; Carbon fibers; Syngas; Methane; Chemical engineering; Alloy; Metal; Carbon dioxide; Inorganic chemistry; Materials science; Organic chemistry; Composite material; Composite number","score_opus":0.027801160116794895,"score_gpt":0.3074364477965279,"score_spread":0.279635287679733,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2761826041","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979459,0.00011457904,0.00035743607,0.000012732714,0.00011961198,0.00058921595,0.00017089154,0.000058736103,0.00063092064],"genre_scores_gemma":[0.9987222,0.000002854068,0.00021197475,0.0000063962225,0.00008889435,0.00010713705,0.00037093577,0.000064756285,0.0004248758],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997726,0.000020790712,0.00085433066,0.00046705082,0.00050962,0.000422166],"domain_scores_gemma":[0.99674034,0.00021549778,0.00085677777,0.0018348453,0.00021423535,0.00013828858],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005356017,0.00031873173,0.0009441753,0.00024841155,0.00035307964,0.00003865664,0.00089788064,0.0001455622,0.00002440876],"category_scores_gemma":[0.00084167556,0.00028132397,0.00042583223,0.00018335239,0.00014082274,0.00030919572,0.00019182499,0.00015789263,0.0000071723603],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005333955,0.0017492183,0.030584265,0.0011478402,0.0016319196,0.000028503411,0.0030228903,0.0014492607,0.95270735,0.000066276465,0.00023392013,0.006845158],"study_design_scores_gemma":[0.0034505988,0.00022041259,0.0022492984,0.0001474804,0.0006174118,0.000005389849,0.000982221,0.0027024772,0.9889278,0.0000072323214,0.00033651147,0.00035315807],"about_ca_topic_score_codex":0.003958831,"about_ca_topic_score_gemma":0.00064460095,"teacher_disagreement_score":0.036220454,"about_ca_system_score_codex":0.00017549812,"about_ca_system_score_gemma":0.00007763484,"threshold_uncertainty_score":0.9999639},"labels":[],"label_agreement":null},{"id":"W2762198910","doi":"10.1021/acs.energyfuels.7b01318","title":"Performance of Promoted Iron/CNT Catalyst for Fischer–Tropsch Synthesis: Influence of Pellet Shapes and Binder Loading","year":2017,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Mitacs; BioFuelNet Canada","keywords":"Pellets; Pellet; Fischer–Tropsch process; Bentonite; Catalysis; Materials science; Dispersion (optics); Chemical engineering; Syngas; Composite material; Chemistry; Selectivity; Organic chemistry","score_opus":0.01266260093450172,"score_gpt":0.23265808095630133,"score_spread":0.2199954800217996,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2762198910","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99873465,0.00030036113,0.00016282737,0.00003549413,0.000034598328,0.00010368163,0.00002426507,0.000033704535,0.00057040696],"genre_scores_gemma":[0.9987003,0.000076292374,0.000672299,0.000005422854,0.0000605896,0.000052735017,0.000008828775,0.00003976254,0.0003837701],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988178,0.000009755131,0.00040032133,0.00027345435,0.00020250988,0.0002961426],"domain_scores_gemma":[0.9988241,0.0001496128,0.00035203627,0.0004914356,0.00009790284,0.00008490302],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00023971521,0.00020037711,0.00042544914,0.00010626693,0.00012378492,0.000016398231,0.00040045672,0.00012652455,0.000012921197],"category_scores_gemma":[0.00053504284,0.00017615441,0.000104246545,0.0000724478,0.0001364789,0.00035410296,0.00017510851,0.00010197518,0.000001625212],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000048205267,0.000026606855,0.0012595063,0.00065232586,0.00008046952,0.000001353928,0.0001845543,0.00079005543,0.9912571,0.0002556186,0.0000026298158,0.0054415846],"study_design_scores_gemma":[0.00034632254,0.000049679995,0.0021387443,0.00035256497,0.000076020966,0.000009479918,0.000033976692,0.0051289103,0.99121,0.000021324126,0.00043424277,0.00019872942],"about_ca_topic_score_codex":0.0003521682,"about_ca_topic_score_gemma":0.000019137646,"teacher_disagreement_score":0.005242855,"about_ca_system_score_codex":0.000039957933,"about_ca_system_score_gemma":0.00003059965,"threshold_uncertainty_score":0.7183369},"labels":[],"label_agreement":null},{"id":"W2764326561","doi":"10.1002/cjce.23032","title":"Iridium promoted Ni‐Co/Al<sub>2</sub>O<sub>3</sub>‐ZrO<sub>2</sub> catalyst for dry reforming of methane","year":2017,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Deanship of Scientific Research, King Saud University; King Saud University","keywords":"Catalysis; Methane; Cobalt; Nickel; Iridium; Carbon dioxide reforming; Chemistry; Syngas; Inorganic chemistry; Cobalt oxide; Nuclear chemistry; Methane reformer; Hydrogen production; Steam reforming; Organic chemistry","score_opus":0.013074006502137947,"score_gpt":0.23032012623422515,"score_spread":0.2172461197320872,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2764326561","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9951812,0.00070728775,0.0016314083,0.0006505488,0.0008949211,0.0005583394,0.00015519651,0.000102668826,0.00011840522],"genre_scores_gemma":[0.99791765,0.00004449486,0.0005270677,0.000064662214,0.0010227602,0.0000471338,0.00007350693,0.0002880701,0.000014666803],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99497867,0.000037188434,0.0017964374,0.0005738425,0.00089792704,0.0017159365],"domain_scores_gemma":[0.9948321,0.0003926196,0.0012382542,0.0014274505,0.0005469157,0.0015626873],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0018765414,0.00085084577,0.0014789752,0.0007180681,0.00035087776,0.0001456706,0.0020429518,0.00056119094,0.0000070410492],"category_scores_gemma":[0.0032676656,0.0007339237,0.0009023676,0.00048430782,0.00033765825,0.00095051917,0.0002093157,0.0018271505,0.000017992299],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000088085006,0.000029908811,0.000027506707,0.0005157676,0.0004577313,0.00011068899,0.00038844242,0.0017670252,0.9872415,0.00010558474,0.0001048452,0.009162922],"study_design_scores_gemma":[0.0014954191,0.0000852174,0.000050386436,0.0008969424,0.0003321026,0.0005279017,0.000050391984,0.008375133,0.98638016,0.00012442433,0.0008590397,0.0008228772],"about_ca_topic_score_codex":0.0010000211,"about_ca_topic_score_gemma":0.0006965334,"teacher_disagreement_score":0.008340045,"about_ca_system_score_codex":0.0015685916,"about_ca_system_score_gemma":0.0008995153,"threshold_uncertainty_score":0.9995112},"labels":[],"label_agreement":null},{"id":"W2774271116","doi":"10.2495/eq-v3-n1-44-56","title":"Is dry reforming the solution to reduce natural gas carbon footprint?","year":2018,"lang":"en","type":"article","venue":"International Journal of Energy Production and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"CRB Innovations; Natural Sciences and Engineering Research Council of Canada; Mitacs; Enerkem","keywords":"Carbon footprint; Natural gas; Environmental science; Carbon dioxide reforming; Natural (archaeology); Carbon fibers; Footprint; Waste management; Greenhouse gas; Natural resource economics; Chemistry; Economics; Materials science; Syngas; Engineering; Geology; Hydrogen","score_opus":0.012263498850167346,"score_gpt":0.26274066569686877,"score_spread":0.2504771668467014,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2774271116","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96415734,0.00033801774,0.003174364,0.018020216,0.007666628,0.00011316862,7.1736696e-7,0.00004012985,0.006489428],"genre_scores_gemma":[0.99338317,0.00022051824,0.0007043613,0.00020170749,0.0019671624,0.0000047411822,0.0000013116143,0.000011101446,0.0035059245],"study_design_codex":"design_other","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990459,0.000011743,0.00028310416,0.00014711174,0.00038881414,0.00012328956],"domain_scores_gemma":[0.99936885,0.000007450466,0.00015331822,0.00013465212,0.00028591885,0.000049841005],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00032178973,0.0000900532,0.00008914803,0.00021965096,0.00005566655,0.000023565344,0.00024182323,0.000022642236,0.000007775998],"category_scores_gemma":[0.000086288666,0.00006245448,0.000060287628,0.00012510389,0.000036775466,0.00009854834,0.00016808214,0.000109568464,0.000001977246],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00038680783,0.000072891155,0.000089436006,0.00003569604,0.00086577714,0.0000274894,0.0012187011,0.00052621163,0.37920457,0.012319373,0.0006376162,0.60461545],"study_design_scores_gemma":[0.00035846178,0.00007122067,0.00039312209,0.00020818386,0.00006106977,0.0002563962,0.0003750491,0.0014049364,0.84128684,0.0005031571,0.1549216,0.00015992524],"about_ca_topic_score_codex":0.00010764385,"about_ca_topic_score_gemma":0.00003717388,"teacher_disagreement_score":0.6044555,"about_ca_system_score_codex":0.00020397277,"about_ca_system_score_gemma":0.000007983959,"threshold_uncertainty_score":0.25468197},"labels":[],"label_agreement":null},{"id":"W2774922515","doi":"10.1016/j.cherd.2017.12.008","title":"System development of integrated high temperature and low temperature Fischer–Tropsch synthesis for high value chemicals","year":2017,"lang":"en","type":"article","venue":"Process Safety and Environmental Protection","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China; Syncrude","keywords":"Fischer–Tropsch process; Process engineering; Coal; Investment (military); Coal gasification; Coproduction; Process integration; Syngas; Capital investment; Engineering; Environmental science; Waste management; Business; Chemistry; Catalysis","score_opus":0.005791826447950785,"score_gpt":0.19629687370704405,"score_spread":0.19050504725909326,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2774922515","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99696994,0.00017066851,0.0018571584,0.00006991388,0.00006858008,0.00066812494,0.000109606386,0.00006105665,0.000024982697],"genre_scores_gemma":[0.9984483,0.00004256004,0.0009206485,0.0000039489146,0.00006778988,0.0002863293,0.00009623629,0.00003734425,0.00009680961],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988745,0.000013521516,0.0003515215,0.0003674588,0.00018034955,0.00021268897],"domain_scores_gemma":[0.9994273,0.000030450507,0.0002194608,0.00022202524,0.00001646096,0.000084280255],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002386619,0.00024621445,0.0003476279,0.00004525756,0.00046861183,0.000036787653,0.00013827185,0.0002817269,0.000009739367],"category_scores_gemma":[0.00012622289,0.00020281159,0.00004390946,0.000042650427,0.00009982924,0.0002838741,0.000088192384,0.00027155812,0.0000013368419],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030238475,0.000039986466,0.00007474762,0.0018642201,0.00007949958,7.4459865e-7,0.00019308084,0.000250969,0.9893745,0.00006290025,3.229401e-7,0.0077566314],"study_design_scores_gemma":[0.0006052399,0.00003132073,0.0008876816,0.0005434909,0.000053557374,0.000027299717,0.00043691354,0.0027621984,0.99429244,0.000032750148,0.00007836587,0.00024872238],"about_ca_topic_score_codex":0.00006518679,"about_ca_topic_score_gemma":0.000002517382,"teacher_disagreement_score":0.0075079086,"about_ca_system_score_codex":0.00022548612,"about_ca_system_score_gemma":0.000018869338,"threshold_uncertainty_score":0.8270416},"labels":[],"label_agreement":null},{"id":"W2780827044","doi":"10.3390/catal8010001","title":"Bio-Oil Steam Reforming over a Mining Residue Functionalized with Ni as Catalyst: Ni-UGSO","year":2017,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":89,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Catalysis; Space velocity; Physisorption; Steam reforming; Thermogravimetric analysis; Syngas; Chemistry; Chemical engineering; Nuclear chemistry; Selectivity; Materials science; Organic chemistry; Hydrogen production","score_opus":0.014817457682977401,"score_gpt":0.2595131803485551,"score_spread":0.24469572266557768,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2780827044","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96336097,0.000683862,0.000065119566,0.00017973414,0.00066150125,0.00019370583,0.0000471865,0.00041520988,0.03439271],"genre_scores_gemma":[0.958594,0.000030959898,0.0003541131,0.000080531914,0.00066056335,0.000110494606,0.00046553568,0.00019365322,0.03951012],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99644345,0.000028429451,0.0007055891,0.00095177646,0.00090673135,0.00096400094],"domain_scores_gemma":[0.9961889,0.00011276305,0.0006173281,0.0024725825,0.00018561183,0.00042282237],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005926021,0.0006307976,0.0008033073,0.00034272482,0.0008082043,0.00014951256,0.0010987549,0.00032505798,0.00023734948],"category_scores_gemma":[0.000862805,0.00051698426,0.00026722348,0.00033806972,0.00026323853,0.0012489147,0.0005255464,0.00054013554,0.0004317129],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.002012882,0.00041772999,0.02307055,0.0016899586,0.0027642706,0.0017930479,0.0050588325,0.0003025128,0.8440521,0.0018785796,0.0023794214,0.11458016],"study_design_scores_gemma":[0.0077851615,0.00023050264,0.006029713,0.0017364345,0.0008255166,0.0016573219,0.0014390812,0.0008876255,0.92825675,0.00013096757,0.048225224,0.0027956788],"about_ca_topic_score_codex":0.004492509,"about_ca_topic_score_gemma":0.00096652756,"teacher_disagreement_score":0.11178448,"about_ca_system_score_codex":0.00056314346,"about_ca_system_score_gemma":0.00019484591,"threshold_uncertainty_score":0.9997282},"labels":[],"label_agreement":null},{"id":"W2784162584","doi":"10.14447/jnmes.v17i4.399","title":"Catalytic Performance of Oxidized Ni3Sn2 for Hydrogen Production from Methanol Decomposition","year":2014,"lang":"en","type":"article","venue":"Journal of New Materials for Electrochemical Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Methanol; Methanation; Decomposition; Isothermal process; Hydrogen; Hydrogen production; Materials science; Water-gas shift reaction; Chemical engineering; Inorganic chemistry; Chemistry; Thermodynamics; Organic chemistry; Physics","score_opus":0.01204821768377616,"score_gpt":0.25460354368274307,"score_spread":0.2425553259989669,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2784162584","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9834345,0.0002918375,0.014768798,0.000055347744,0.0008122916,0.0005670864,0.00002479149,0.000033513,0.000011818297],"genre_scores_gemma":[0.99622875,0.000013934151,0.0012034388,0.000005653556,0.0022503005,0.000045001227,0.00010105312,0.000057233134,0.000094630384],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977579,0.000034407723,0.0012452188,0.00022590712,0.0003810383,0.0003555328],"domain_scores_gemma":[0.99798787,0.00022064606,0.0010338803,0.0002311576,0.00038087217,0.00014560415],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001052537,0.00022618941,0.00087971706,0.00013269464,0.00003874605,0.000020538035,0.0002865551,0.00018251067,0.000005671933],"category_scores_gemma":[0.0007599022,0.00018826366,0.00026422145,0.00012633669,0.000020500938,0.0002512818,0.000025152109,0.00011642603,0.000002611512],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010556492,0.000039409246,0.000007395771,0.0006167278,0.00020294072,1.655279e-7,0.00006502688,0.00016621477,0.9973607,0.000046741574,0.00010239005,0.00033664922],"study_design_scores_gemma":[0.0015813846,0.0003760156,0.0000032730811,0.0003944453,0.00025894222,0.00012275531,0.000012215757,0.0026183133,0.99323285,0.00028735743,0.0009154278,0.00019703222],"about_ca_topic_score_codex":0.000068716756,"about_ca_topic_score_gemma":0.000001010461,"teacher_disagreement_score":0.013565359,"about_ca_system_score_codex":0.0003108351,"about_ca_system_score_gemma":0.00007726588,"threshold_uncertainty_score":0.76771694},"labels":[],"label_agreement":null},{"id":"W2784492610","doi":"10.1021/acs.iecr.7b04582","title":"Metal Oxide-Based Catalysts for the Autothermal Reforming of Glycerol","year":2018,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation; Faculty of Graduate Studies and Research, University of Regina","keywords":"Glycerol; Catalysis; Chemistry; Catalytic reforming; Methane reformer; Dilution; Hydrogen; Metal; Selectivity; Steam reforming; Oxide; Oxygen; Hydrogen production; Chemical engineering; Inorganic chemistry; Nuclear chemistry; Organic chemistry","score_opus":0.10118859842812396,"score_gpt":0.347775545355907,"score_spread":0.24658694692778305,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2784492610","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9964637,0.00022945674,0.0008692484,0.00021032373,0.0003360498,0.00071880943,0.000082054976,0.00024234045,0.00084799016],"genre_scores_gemma":[0.9967786,0.00000209339,0.00012856656,0.0000039873644,0.0018235998,0.00018544839,0.000042443393,0.0001053006,0.00092995976],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971406,0.000021982261,0.0006032874,0.00041908826,0.00085692736,0.00095813145],"domain_scores_gemma":[0.99727136,0.0011609666,0.000117557756,0.00084192096,0.00040763887,0.00020053322],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0021255715,0.0002977852,0.00042416362,0.00015651034,0.00019066465,0.000030418087,0.0009344067,0.00040806102,0.000075078264],"category_scores_gemma":[0.0028805586,0.00023154814,0.00028237884,0.0008582225,0.00027948062,0.00013742763,0.00021592743,0.0010571261,0.00001618829],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017541397,0.00003114836,0.000025666253,0.00019844266,0.00015289168,0.0000037094148,0.000071794806,0.002664151,0.9937734,0.000041601903,0.0001305938,0.0027311908],"study_design_scores_gemma":[0.0012847297,0.00005723139,0.00000877896,0.00015485918,0.000049877326,0.000015033957,0.00007177003,0.05126708,0.9378954,0.000005346085,0.008958414,0.00023147915],"about_ca_topic_score_codex":0.00037639734,"about_ca_topic_score_gemma":0.0000030765536,"teacher_disagreement_score":0.055877995,"about_ca_system_score_codex":0.0003931986,"about_ca_system_score_gemma":0.00031123645,"threshold_uncertainty_score":0.9442259},"labels":[],"label_agreement":null},{"id":"W2787090555","doi":"10.3390/en11020362","title":"Simulation-Optimization Framework for Synthesis and Design of Natural Gas Downstream Utilization Networks","year":2018,"lang":"en","type":"article","venue":"Energies","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada; Qatar University","keywords":"Natural gas; Upgrade; Syngas; Liquefied natural gas; Downstream (manufacturing); Process engineering; Operating cost; Renewable natural gas; Computer science; Environmental science; Engineering; Waste management; Fuel gas; Hydrogen; Operations management; Chemistry","score_opus":0.025282840120351906,"score_gpt":0.2730043328007253,"score_spread":0.24772149268037338,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2787090555","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"methods","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.052115362,0.00030490494,0.9471924,0.000011861506,0.00013969888,0.00011872293,0.000003008494,0.00007699435,0.000037073612],"genre_scores_gemma":[0.9123722,0.000036659396,0.08728587,0.0000060471457,0.00020042094,0.000021257889,0.000019857542,0.00002181307,0.000035899273],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9994454,0.000013221402,0.00018317708,0.00013547513,0.00008725427,0.0001354965],"domain_scores_gemma":[0.9985534,0.0010965918,0.000085187894,0.000134542,0.00010457015,0.000025738735],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001123593,0.00009957586,0.00014752368,0.00006816792,0.000055429166,0.00001072129,0.00006213791,0.00010486897,0.000020508216],"category_scores_gemma":[0.0012187448,0.00008890802,0.000036907368,0.00015899967,0.000057649566,0.0001392289,0.000026029511,0.000050380157,4.631712e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000038911232,0.000006203173,0.000027683633,0.00002796366,0.000024190123,7.292903e-8,0.00011463732,0.98362863,0.0037057507,0.001776302,0.0000034831558,0.010646171],"study_design_scores_gemma":[0.0000819575,0.000016780818,0.000010180768,0.00006643818,0.000029747995,5.6668637e-7,0.000033937904,0.8122052,0.18710928,0.00032445352,0.000040671588,0.00008077198],"about_ca_topic_score_codex":0.000011205282,"about_ca_topic_score_gemma":0.0000012870597,"teacher_disagreement_score":0.8602568,"about_ca_system_score_codex":0.000026077376,"about_ca_system_score_gemma":0.0000076196943,"threshold_uncertainty_score":0.36255637},"labels":[],"label_agreement":null},{"id":"W2789944399","doi":"10.1002/aic.16094","title":"Highly efficient methane reforming over a low‐loading Ru/γ‐Al<sub>2</sub>O<sub>3</sub> catalyst in a Pd‐Ag membrane reactor","year":2018,"lang":"en","type":"article","venue":"AIChE Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"King Fahd University of Petroleum and Minerals","keywords":"Syngas; Methane; Catalysis; Steam reforming; Membrane reactor; Chemistry; Hydrogen; Bar (unit); Catalytic reforming; Methane reformer; Carbon fibers; Chemical engineering; Nuclear chemistry; Hydrogen production; Materials science; Organic chemistry; Physics","score_opus":0.009621538347741314,"score_gpt":0.23953898150090133,"score_spread":0.22991744315316,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2789944399","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9959383,0.00056955963,0.000759539,0.0002445937,0.0012297325,0.00034682156,0.000024225095,0.00023801353,0.0006491937],"genre_scores_gemma":[0.9972348,0.0002020949,0.00033234648,0.0002411183,0.0016374949,0.00003086402,0.000045997152,0.00022766864,0.00004761678],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99409795,0.0001390461,0.0017377812,0.00084405893,0.0013731439,0.0018080394],"domain_scores_gemma":[0.9968525,0.0003637007,0.0007522107,0.0009172713,0.00030957247,0.0008047497],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0026929576,0.0008164459,0.0011534715,0.00114876,0.0002825451,0.00012928798,0.0008410187,0.00049149967,0.00005542401],"category_scores_gemma":[0.0012825303,0.000719225,0.0005980855,0.0015962565,0.00018713133,0.0008502201,0.00043843707,0.002278032,0.0003265335],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021972269,0.00017233306,0.00008654223,0.00015454368,0.00022821777,0.00035104848,0.0014782859,0.00044820894,0.9891594,0.000040807092,0.000101176556,0.007559704],"study_design_scores_gemma":[0.0024022523,0.00012845948,0.00025056145,0.0010551995,0.00017636272,0.0016474656,0.00030881364,0.005641978,0.9862025,0.000046383368,0.001245677,0.0008943408],"about_ca_topic_score_codex":0.00020429307,"about_ca_topic_score_gemma":0.00020040401,"teacher_disagreement_score":0.0066653634,"about_ca_system_score_codex":0.0019868652,"about_ca_system_score_gemma":0.00025732405,"threshold_uncertainty_score":0.9995259},"labels":[],"label_agreement":null},{"id":"W2791935119","doi":"10.1002/cjce.23140","title":"Performance evaluation of fixed‐bed, millistructured, and metallic foam reactor channels for CO<sub>2</sub> methanation","year":2018,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":31,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Association Instituts Carnot","keywords":"Methanation; Materials science; Substitute natural gas; Power to gas; Methane; Space velocity; Chemical engineering; Hydrogen; Catalysis; Process engineering; Waste management; Electrolysis; Syngas; Chemistry; Engineering; Organic chemistry","score_opus":0.02008686712560494,"score_gpt":0.24228896195655034,"score_spread":0.22220209483094538,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2791935119","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9982928,0.00043944558,0.0005984456,0.00008392969,0.00032397342,0.000197598,0.000017510572,0.000011324305,0.00003498334],"genre_scores_gemma":[0.99880373,0.000006152457,0.00057649496,0.0000118243115,0.00053575065,0.000010922338,0.000013611794,0.000038285893,0.0000032184528],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99866897,0.00001527413,0.00047156058,0.00012757424,0.00039989495,0.00031672462],"domain_scores_gemma":[0.9986059,0.00015440997,0.00023669147,0.0001798731,0.0005363873,0.00028675538],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012632125,0.00017853809,0.0003216185,0.00023178254,0.000051414518,0.00001975179,0.00024781268,0.00012991694,0.000012510643],"category_scores_gemma":[0.0011468469,0.00014099348,0.00012914618,0.00022148922,0.000096381795,0.000210997,0.000015578114,0.00026852364,9.772191e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019088942,0.0000023043751,0.000012302139,0.00008001812,0.0001029056,6.296817e-7,0.00031556273,0.0016830829,0.99147207,0.000120847675,0.000014080333,0.0061771255],"study_design_scores_gemma":[0.0005126216,0.000040409133,0.000026828353,0.00010850692,0.00017975479,0.00009816232,0.000012413985,0.11064822,0.8879024,0.000094237126,0.00023943392,0.00013701462],"about_ca_topic_score_codex":0.00014173509,"about_ca_topic_score_gemma":0.00006582765,"teacher_disagreement_score":0.10896514,"about_ca_system_score_codex":0.00037784016,"about_ca_system_score_gemma":0.00021458535,"threshold_uncertainty_score":0.5749547},"labels":[],"label_agreement":null},{"id":"W2792438255","doi":"10.3390/chemengineering2010009","title":"Recent Advances in Supported Metal Catalysts for Syngas Production from Methane","year":2018,"lang":"en","type":"article","venue":"ChemEngineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":63,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation; Faculty of Graduate Studies and Research, University of Regina; University of Regina","keywords":"Syngas; Methane; Catalysis; Coke; Bimetallic strip; Carbon dioxide reforming; Methane reformer; Environmental science; Steam reforming; Process engineering; Materials science; Chemistry; Hydrogen production; Engineering; Metallurgy; Organic chemistry","score_opus":0.015404426742861412,"score_gpt":0.26577328243335135,"score_spread":0.25036885569048994,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2792438255","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9794143,0.007071751,0.0102195265,0.00012756302,0.0015024927,0.00061589427,0.000038065602,0.00046269762,0.000547725],"genre_scores_gemma":[0.9927122,0.0004801103,0.0048284875,0.000010325746,0.001021477,0.00020881784,0.00034578642,0.000097696466,0.00029511328],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99836415,0.00000636307,0.00044317998,0.00047313375,0.00021043047,0.00050273736],"domain_scores_gemma":[0.99925834,0.0000727449,0.00008274744,0.00037486322,0.00010374278,0.000107587235],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003217032,0.00026687232,0.0003743471,0.00020721449,0.00003154472,0.000009228746,0.0002003292,0.00008861355,0.000060489925],"category_scores_gemma":[0.0006254388,0.000271225,0.00009915258,0.0004995586,0.000033772532,0.0004657929,0.00006517343,0.00019148257,0.000025292868],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000038263628,0.000031855845,0.000050781702,0.00010504722,0.00006804054,0.0000042349075,0.0002653903,0.0007654998,0.95499843,0.000037155725,0.000020476355,0.043614794],"study_design_scores_gemma":[0.00053295493,0.000028373062,0.0000404178,0.000088083885,0.000046591926,0.000010462412,0.00007287579,0.008246673,0.942718,0.000074028496,0.04783325,0.00030828646],"about_ca_topic_score_codex":0.000042194897,"about_ca_topic_score_gemma":0.000081329024,"teacher_disagreement_score":0.04781277,"about_ca_system_score_codex":0.00026372873,"about_ca_system_score_gemma":0.000025325871,"threshold_uncertainty_score":0.999974},"labels":[],"label_agreement":null},{"id":"W2793043757","doi":"10.1016/j.joule.2018.02.017","title":"Green Syngas by Solar Dry Reforming","year":2018,"lang":"en","type":"article","venue":"Joule","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":64,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Ontario Ministry of Research and Innovation; Natural Sciences and Engineering Research Council of Canada; Ministero dello Sviluppo Economico","keywords":"Syngas; Carbon dioxide reforming; Methane; Greenhouse gas; Renewable energy; Solar energy; Syngas to gasoline plus; Environmental science; Carbon fibers; Fossil fuel; Waste management; Catalysis; Materials science; Chemical engineering; Chemistry; Steam reforming; Engineering; Hydrogen production; Organic chemistry; Composite number; Composite material; Geology","score_opus":0.00969437784380846,"score_gpt":0.24017818962367446,"score_spread":0.230483811779866,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2793043757","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9709554,0.00022314842,0.0023103098,0.00019970401,0.0003850647,0.00010982162,0.000017350236,0.00037833367,0.025420887],"genre_scores_gemma":[0.98302865,0.000008804638,0.00084014045,0.0001379111,0.00092788297,0.000011420788,0.000034351342,0.00007232588,0.0149385305],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99893177,0.000008158138,0.00023737765,0.00021505839,0.000221699,0.00038596115],"domain_scores_gemma":[0.99938405,0.000028675455,0.00006208063,0.00035403547,0.00004518252,0.00012599825],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021619092,0.00014815468,0.00019059368,0.00006575846,0.000095916825,0.000011348844,0.00022987278,0.0001205584,0.00023229109],"category_scores_gemma":[0.00010098662,0.00012658746,0.000093332514,0.0001850325,0.00004927166,0.00024447555,0.00012503527,0.0002327538,0.0006595625],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000009938331,0.000021826843,0.00029364522,0.000040838106,0.000039009075,0.000005572831,0.00029251495,0.000001658679,0.98032475,0.00011877434,0.00084967125,0.018001778],"study_design_scores_gemma":[0.0002474685,0.000035967798,0.000033193162,0.0000395828,0.000018947832,0.000012075536,0.000079245794,0.0020656453,0.8810929,0.00010167681,0.11606452,0.00020878621],"about_ca_topic_score_codex":0.000580926,"about_ca_topic_score_gemma":0.000037146707,"teacher_disagreement_score":0.11521485,"about_ca_system_score_codex":0.00015543208,"about_ca_system_score_gemma":0.000015204069,"threshold_uncertainty_score":0.8477561},"labels":[],"label_agreement":null},{"id":"W2793736982","doi":"10.1039/c8cy00250a","title":"Methanol synthesis <i>via</i> CO<sub>2</sub> hydrogenation over CuO–ZrO<sub>2</sub> prepared by two-nozzle flame spray pyrolysis","year":2018,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":54,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institute of Particle Physics","funders":"Japan Society for the Promotion of Science; Eidgenössische Technische Hochschule Zürich","keywords":"Methanol; Catalysis; Pyrolysis; Nozzle; Spray pyrolysis; Materials science; Particle (ecology); Particle size; Chemical engineering; Formaldehyde; Inorganic chemistry; Chemistry; Organic chemistry; Nanotechnology; Thermodynamics","score_opus":0.0063455233026966625,"score_gpt":0.24163562135486258,"score_spread":0.2352900980521659,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2793736982","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9875535,0.00044016488,0.0083629405,0.0003370846,0.0003038333,0.00049522275,0.000070104456,0.0015343915,0.0009027732],"genre_scores_gemma":[0.99836034,0.00007357702,0.0005872404,0.00010141294,0.00019421756,0.00036189062,0.00011845835,0.00013587714,0.00006701629],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9930911,0.00006901437,0.0011879187,0.0021770461,0.0015765255,0.001898385],"domain_scores_gemma":[0.9954494,0.00028767367,0.0006714979,0.0026084639,0.0005400109,0.00044290777],"candidate_categories":["metaepi_narrow","sts"],"consensus_categories":[],"category_scores_codex":[0.0019292613,0.0008057622,0.0011817222,0.0032602546,0.00074125174,0.00012234905,0.0026455033,0.0007220749,0.000054369226],"category_scores_gemma":[0.00265036,0.00079322746,0.0005144549,0.010393446,0.0032472212,0.0014468962,0.00092950615,0.00072064967,0.00076665496],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000023333487,0.0001247409,0.00018766201,0.000029108605,0.00019012495,0.000015166087,0.00019634828,0.00014196773,0.9637041,0.00017103397,0.0001526644,0.03506373],"study_design_scores_gemma":[0.0004913713,0.00007555327,0.000012654623,0.000059995353,0.00045861676,0.00013258605,0.0001478501,0.008194046,0.9879084,0.00036260902,0.0012456297,0.0009106454],"about_ca_topic_score_codex":0.00008989635,"about_ca_topic_score_gemma":0.00012422181,"teacher_disagreement_score":0.03415308,"about_ca_system_score_codex":0.0013341004,"about_ca_system_score_gemma":0.00026575007,"threshold_uncertainty_score":0.99946535},"labels":[],"label_agreement":null},{"id":"W2794128586","doi":"10.1002/ijch.201700134","title":"CO<sub>2</sub> Conversion Enhancement in a Periodically Operated Sabatier Reactor: Nonlinear Frequency Response Analysis and Simulation‐based Study","year":2018,"lang":"en","type":"article","venue":"Israel Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Chemistry; Nonlinear system; Energy conversion efficiency; Volumetric flow rate; Space velocity; Frequency conversion; Mechanics; Modulation (music); Energy transformation; Steady state (chemistry); Bar (unit); Continuous flow; Control theory (sociology); Nuclear engineering; Analytical Chemistry (journal); Catalysis; Thermodynamics; Physical chemistry; Physics; Selectivity; Computer science; Meteorology; Chromatography","score_opus":0.009842732898500052,"score_gpt":0.2730251186773584,"score_spread":0.26318238577885833,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2794128586","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985145,0.00007500367,0.0011285725,0.000053885993,0.0000377553,0.00010279684,0.000010553832,0.000016334458,0.00006062815],"genre_scores_gemma":[0.9992238,0.000005849224,0.0005439492,0.000032656488,0.0001264327,0.0000026508264,0.000017549826,0.00002194897,0.00002510998],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981712,0.00006774335,0.00078526844,0.00023377621,0.00050380826,0.00023821858],"domain_scores_gemma":[0.9986244,0.00027309734,0.00034049898,0.00026458816,0.0003068524,0.00019059461],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00091295043,0.00020713576,0.00047516148,0.00026013987,0.000052425003,0.000033560245,0.00020204882,0.00013826978,0.00013667595],"category_scores_gemma":[0.0007721313,0.00018456274,0.00015138304,0.0005879167,0.00008431037,0.00018855346,0.000037515812,0.0003899289,0.000007056428],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008877938,0.00024907402,0.010939092,0.000041320814,0.00029031278,0.000081118815,0.0004976884,0.001218622,0.98545605,5.3523014e-8,0.0000019815895,0.00033688275],"study_design_scores_gemma":[0.0020844084,0.00017935176,0.0019598175,0.00008947346,0.00025794783,0.000012175857,0.00041712727,0.028680326,0.96607107,8.804151e-7,0.00005401432,0.00019341875],"about_ca_topic_score_codex":0.00002464394,"about_ca_topic_score_gemma":0.000007994999,"teacher_disagreement_score":0.027461704,"about_ca_system_score_codex":0.00036691036,"about_ca_system_score_gemma":0.00017607486,"threshold_uncertainty_score":0.752625},"labels":[],"label_agreement":null},{"id":"W2796069345","doi":"10.1016/j.joule.2018.03.007","title":"Photocatalytic Hydrogenation of Carbon Dioxide with High Selectivity to Methanol at Atmospheric Pressure","year":2018,"lang":"en","type":"article","venue":"Joule","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":226,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada; Qinglan Project of Jiangsu Province of China; Collaborative Innovation Center of Suzhou Nano Science and Technology; Environment and Climate Change Canada; Materials Research Institute, Pennsylvania State University; Ministero dello Sviluppo Economico; Priority Academic Program Development of Jiangsu Higher Education Institutions; National Natural Science Foundation of China; Connaught Fund; National Key Research and Development Program of China; Higher Education Discipline Innovation Project; Natural Science Foundation of Jiangsu Province; Ontario Ministry of Research, Innovation and Science","keywords":"Photocatalysis; Carbon dioxide; Methanol; Atmospheric pressure; Selectivity; High pressure; Materials science; Chemical engineering; Photochemistry; Environmental science; Environmental chemistry; Chemistry; Organic chemistry; Catalysis; Meteorology; Engineering physics; Engineering","score_opus":0.006584584400491617,"score_gpt":0.2215010555146241,"score_spread":0.21491647111413248,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2796069345","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9962138,0.00005943337,0.0008427256,0.000025902289,0.0000717777,0.00030718933,0.000006409333,0.00010778764,0.0023649912],"genre_scores_gemma":[0.9963735,0.0000010048492,0.0013827186,0.000014137114,0.00012117662,0.00003888522,0.000008056428,0.00004595601,0.0020145667],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989248,0.000015434603,0.00020696275,0.00026804357,0.0003152276,0.00026951983],"domain_scores_gemma":[0.9992617,0.000048458674,0.00010536429,0.0003699108,0.00010754701,0.0001070246],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00016547374,0.00016135423,0.00027900605,0.000028109123,0.00003454045,0.0000036937101,0.00015578308,0.00008930889,0.00005944708],"category_scores_gemma":[0.00011505019,0.00013185386,0.00005617522,0.0005496718,0.00003933842,0.0000964443,0.00010394963,0.000114261195,0.000029673643],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008601425,0.000034335328,0.0007021464,0.00007763002,0.00011617828,0.0000022661427,0.00027905358,0.0009996501,0.9971926,0.000028787503,0.000011302543,0.00046998725],"study_design_scores_gemma":[0.0003314828,0.00013170294,0.00048117808,0.00004563242,0.00009676139,0.000016385531,0.000011599047,0.010336397,0.98716897,0.000017446211,0.0011878968,0.00017456824],"about_ca_topic_score_codex":0.0010329173,"about_ca_topic_score_gemma":0.00022448268,"teacher_disagreement_score":0.010023699,"about_ca_system_score_codex":0.00020959826,"about_ca_system_score_gemma":0.000028896804,"threshold_uncertainty_score":0.53768444},"labels":[],"label_agreement":null},{"id":"W2797945086","doi":"10.1002/cctc.201800327","title":"How do Core–Shell Structure Features Impact on the Activity/Stability of the Co‐based Catalyst in Dry Reforming of Methane?","year":2018,"lang":"en","type":"article","venue":"ChemCatChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":37,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"National Natural Science Foundation of China","keywords":"Catalysis; X-ray photoelectron spectroscopy; Carbon dioxide reforming; Methane; Particle size; Chemical engineering; Chemistry; Materials science; Particle (ecology); Syngas; Physical chemistry; Organic chemistry","score_opus":0.02110837817375516,"score_gpt":0.27327053928578265,"score_spread":0.2521621611120275,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2797945086","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9981744,0.00008596598,0.000012888944,0.00025996385,0.00011124824,0.00034367671,0.00012525024,0.000036078258,0.0008504809],"genre_scores_gemma":[0.999608,0.0000016813224,0.000074636584,0.000023223838,0.00012256422,0.00001321831,0.000024051107,0.000046764286,0.000085885375],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982611,0.000050109535,0.00035781864,0.00037911368,0.00052242645,0.00042942233],"domain_scores_gemma":[0.9974747,0.0005014371,0.00037178618,0.0014327343,0.00013553443,0.000083847044],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00058845675,0.00035555314,0.0005755888,0.000108583714,0.00005288206,0.000013536832,0.00078927353,0.00025798375,0.000071825205],"category_scores_gemma":[0.00087578053,0.00018157891,0.00037618875,0.0007789986,0.00041507313,0.00014636606,0.0001666885,0.0007071615,0.0000019136564],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015648706,0.00006547182,0.0030970024,0.00019902407,0.000065115055,9.2004484e-7,0.0012229581,0.000018557332,0.9931736,0.000059413993,0.000016174718,0.0019252722],"study_design_scores_gemma":[0.00046772632,0.000045144876,0.004041643,0.00015881145,0.000041452837,0.00000502055,0.00054001744,0.000326999,0.9939926,0.00011655941,0.000064823034,0.00019914912],"about_ca_topic_score_codex":0.00067920226,"about_ca_topic_score_gemma":0.00018684354,"teacher_disagreement_score":0.001726123,"about_ca_system_score_codex":0.00045742965,"about_ca_system_score_gemma":0.00013787384,"threshold_uncertainty_score":0.7404573},"labels":[],"label_agreement":null},{"id":"W2800521107","doi":"10.1039/c8re00013a","title":"Improved performance of a catalytic plate reactor coated with distributed layers of reforming and combustion catalysts for hydrogen production","year":2018,"lang":"en","type":"article","venue":"Reaction Chemistry & Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Royal Military College of Canada","funders":"Ministère de la Défense Nationale","keywords":"Hydrogen production; Steam reforming; Catalysis; Combustion; Methane reformer; Hydrogen; Methane; Catalytic combustion; Materials science; Chemical engineering; Chemical looping combustion; Waste management; Chemistry; Engineering; Organic chemistry","score_opus":0.007478160297689137,"score_gpt":0.20762781264986926,"score_spread":0.20014965235218013,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2800521107","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979449,0.000039637387,0.0014555377,0.000009609154,0.00007689931,0.00025621208,0.00004851923,0.00013731878,0.000031347863],"genre_scores_gemma":[0.9989634,0.000013612931,0.0003568198,5.02232e-7,0.0001457646,0.000037130394,0.000377778,0.00005021089,0.00005476785],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988292,0.0000022787417,0.00042530271,0.00030190658,0.00017083938,0.0002704903],"domain_scores_gemma":[0.99906,0.00004186327,0.00028749582,0.0002995945,0.00022134003,0.00008971411],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00019717774,0.0002281542,0.0003445169,0.0000819352,0.00004156798,0.0000042728498,0.00009492714,0.00013766467,0.0000013021073],"category_scores_gemma":[0.00021978815,0.0002133706,0.00006218105,0.00032955536,0.00006859305,0.0002953826,0.000034052027,0.00017097611,4.274249e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002000997,0.00002959549,0.00009803218,0.0011853405,0.00011060373,4.0554534e-7,0.000118584016,0.0008886567,0.99677116,0.0000029591545,0.0000011314211,0.0005934283],"study_design_scores_gemma":[0.0005508642,0.00008833205,0.000077383134,0.00034266856,0.00010843407,0.00009828221,0.000071895156,0.07796299,0.9203666,3.0959484e-7,0.00012131589,0.00021096118],"about_ca_topic_score_codex":0.00009877444,"about_ca_topic_score_gemma":0.0000034136635,"teacher_disagreement_score":0.07707433,"about_ca_system_score_codex":0.00023330185,"about_ca_system_score_gemma":0.0000383773,"threshold_uncertainty_score":0.8701001},"labels":[],"label_agreement":null},{"id":"W2800976884","doi":"10.1002/cjce.23231","title":"Biomass‐gas‐and‐nuclear‐to‐liquids (BGNTL) processes part I: Model development and simulation","year":2018,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":true,"ca_institutions":"McMaster University","funders":"Atomic Energy of Canada Limited; Natural Sciences and Engineering Research Council of Canada; Ontario Ministry of Research, Innovation and Science","keywords":"Biomass (ecology); Process engineering; Dimethyl ether; Process (computing); Process simulation; Natural gas; Electricity; Electricity generation; Environmental science; Methanol; Fischer–Tropsch process; Waste management; Nuclear engineering; Engineering; Computer science; Chemistry; Power (physics); Thermodynamics; Organic chemistry; Physics","score_opus":0.0153203272066521,"score_gpt":0.2169787609894323,"score_spread":0.2016584337827802,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2800976884","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99657357,0.00021247445,0.0026623823,0.00028543215,0.00008390322,0.000065497414,0.0000024460303,0.00002683986,0.000087437824],"genre_scores_gemma":[0.9967181,0.0000014222658,0.0028916805,0.000054793614,0.00026681926,0.0000021544563,0.0000012973123,0.000039497194,0.000024238545],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990184,0.00000304338,0.00034398882,0.00012424185,0.00017971132,0.00033061916],"domain_scores_gemma":[0.9989926,0.00007907529,0.0000676126,0.00011708631,0.00015698295,0.00058659463],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026533494,0.00016073664,0.00020564406,0.00017197045,0.000087414686,0.000042761556,0.00019387658,0.00008733986,0.0000103245075],"category_scores_gemma":[0.00061498175,0.0001257432,0.000032757656,0.00023529795,0.00006448273,0.00014462015,0.00004438405,0.00023416028,0.000004591553],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047371635,0.000009862697,0.000048571037,0.00034436808,0.00016167949,0.000024811827,0.0062049916,0.12812112,0.85618186,0.000701491,0.00005574189,0.0080981385],"study_design_scores_gemma":[0.00027128082,0.00003116163,0.000009434871,0.00027200402,0.000039428076,0.00015335105,0.00002772498,0.4088853,0.58231634,0.00006607988,0.00765559,0.00027230073],"about_ca_topic_score_codex":0.00012593003,"about_ca_topic_score_gemma":0.00011259502,"teacher_disagreement_score":0.2807642,"about_ca_system_score_codex":0.00021978343,"about_ca_system_score_gemma":0.00023052609,"threshold_uncertainty_score":0.51276594},"labels":[],"label_agreement":null},{"id":"W2802342746","doi":"","title":"Transition Metal Carbides for Thermocatalytic Conversion of Carbon Dioxide via Reverse Water Gas Shift and Sabatier Reactions","year":2018,"lang":"en","type":"dissertation","venue":"UWSpace (University of Waterloo)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Water-gas shift reaction; Carbon dioxide; Carbide; Transition metal; Chemistry; Materials science; Inorganic chemistry; Metallurgy; Catalysis; Organic chemistry","score_opus":0.007813315598677961,"score_gpt":0.1962734773183815,"score_spread":0.18846016171970353,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2802342746","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9989208,0.000057866742,0.00008299964,0.00008473353,0.00019401837,0.0003541571,0.00006455839,0.00004795944,0.0001928788],"genre_scores_gemma":[0.9559836,0.000046965273,0.0004954869,0.0000023146922,0.0000515542,0.0000016577819,0.0013918991,0.00005435149,0.041972164],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99894375,0.000021418029,0.00021713415,0.00033541676,0.00022407496,0.00025822714],"domain_scores_gemma":[0.99923384,0.00004498038,0.00020761653,0.00027441615,0.00015235525,0.00008679658],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00016192294,0.00025981345,0.0005312015,0.00028707276,0.00008323394,0.000003593119,0.00016811618,0.00032980958,0.00005816218],"category_scores_gemma":[0.000015262554,0.00024995115,0.00027070785,0.000100019875,0.00012744391,0.00023077951,0.000035169716,0.00018310572,0.0000047612803],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003835835,0.00003343416,0.000009274251,0.0018048416,0.00029384956,0.0000058666687,0.06664593,0.000018381063,0.9304444,0.00001467769,0.000007392297,0.00033836422],"study_design_scores_gemma":[0.0008674379,0.00012090727,0.00006308152,0.0003375113,0.0009114915,0.000007659444,0.030007303,0.0017344299,0.9653542,0.00008072399,0.00020940883,0.00030582992],"about_ca_topic_score_codex":0.04088494,"about_ca_topic_score_gemma":0.003455287,"teacher_disagreement_score":0.04293722,"about_ca_system_score_codex":0.00012300837,"about_ca_system_score_gemma":0.000026331854,"threshold_uncertainty_score":0.9999953},"labels":[],"label_agreement":null},{"id":"W2803628314","doi":"10.1007/s10562-018-2428-y","title":"Phase Quantification of Carbon Support by X-Ray Photoelectron Spectroscopy (XPS) in Plasma-Synthesized Fischer–Tropsch Nanocatalysts","year":2018,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Fischer–Tropsch process; Nanomaterial-based catalyst; X-ray photoelectron spectroscopy; Catalysis; Chemistry; Carbon fibers; Nanoparticle; Analytical Chemistry (journal); Chemical engineering; Phase (matter); Nanotechnology; Materials science; Organic chemistry; Selectivity","score_opus":0.010400822233724369,"score_gpt":0.2551975294457938,"score_spread":0.24479670721206945,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2803628314","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.996684,0.00009896934,0.0017592248,0.0003249014,0.00015174129,0.00031405562,0.00004114071,0.00013454622,0.0004914126],"genre_scores_gemma":[0.9980057,0.00001576144,0.00055004325,0.000090234986,0.0001506725,0.00008655578,0.0007987641,0.00009544691,0.00020684341],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.996914,0.00006909531,0.0009774696,0.00074610463,0.00053629244,0.00075703405],"domain_scores_gemma":[0.99819326,0.00014955198,0.00039751784,0.0010190489,0.00008249573,0.00015814134],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006423296,0.00042538307,0.00080964476,0.0005358848,0.000057533685,0.000022393935,0.00057930924,0.00019330194,0.00010309088],"category_scores_gemma":[0.000294686,0.0004279102,0.00027527078,0.0012011139,0.00022823655,0.00027802342,0.000079386366,0.0003795877,0.000078997415],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021440585,0.00029453656,0.00022545063,0.00007714105,0.00017188328,0.000011269106,0.00046953236,0.00004704784,0.99699324,0.0000125462175,0.0003163345,0.0011665912],"study_design_scores_gemma":[0.0021063662,0.00013773404,0.000025088606,0.00005354073,0.00018955249,0.000009715157,0.00007062923,0.005881909,0.9896219,0.0000030042027,0.0014707681,0.0004298096],"about_ca_topic_score_codex":0.0008836188,"about_ca_topic_score_gemma":0.000102809536,"teacher_disagreement_score":0.0073713786,"about_ca_system_score_codex":0.00050335866,"about_ca_system_score_gemma":0.00006226297,"threshold_uncertainty_score":0.99981725},"labels":[],"label_agreement":null},{"id":"W2806356795","doi":"10.1038/s41598-018-27381-6","title":"Microwave Heating-Assisted Catalytic Dry Reforming of Methane to Syngas","year":2018,"lang":"en","type":"article","venue":"Scientific Reports","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":69,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Carbon dioxide reforming; Commodity chemicals; Methane; Natural gas; Renewable energy; Environmental science; Raw material; Capital cost; Greenhouse gas; Waste management; Process engineering; Chemical engineering; Catalysis; Materials science; Chemistry; Organic chemistry","score_opus":0.017449562453350703,"score_gpt":0.2662401912580657,"score_spread":0.248790628804715,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2806356795","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.987559,0.00008967613,0.0011956419,0.000027264276,0.00498955,0.00028723435,0.000003899524,0.00015916533,0.005688539],"genre_scores_gemma":[0.9877575,2.8985443e-7,0.003104596,0.000016028362,0.00018854176,0.000016729593,0.000058781046,0.00004744774,0.008810069],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9969032,0.000018900078,0.0010055294,0.0008086746,0.0006785151,0.00058518146],"domain_scores_gemma":[0.99744433,0.000058417118,0.00039288684,0.0014485002,0.0003697752,0.0002860672],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0019687982,0.00023450573,0.00044372366,0.00043584828,0.00013625735,0.000043123884,0.00028374937,0.00011206487,0.00008646398],"category_scores_gemma":[0.001192859,0.0002057856,0.0001941248,0.0013428257,0.00026824474,0.0002256038,0.0002899463,0.00017293687,0.000105428415],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000010924111,0.00003273005,0.0002972193,0.0000903556,0.000037387945,0.00009836965,0.00076518167,0.000022391825,0.9882296,0.00003132656,0.0001778664,0.010206651],"study_design_scores_gemma":[0.00010768303,0.00004021925,0.00010812756,0.0002119369,0.000043805354,0.0003752034,0.0001539781,0.00037694778,0.9926402,0.00029488394,0.005402781,0.0002442399],"about_ca_topic_score_codex":0.00053919415,"about_ca_topic_score_gemma":0.00018989378,"teacher_disagreement_score":0.009962411,"about_ca_system_score_codex":0.00025777705,"about_ca_system_score_gemma":0.00013659941,"threshold_uncertainty_score":0.8391693},"labels":[],"label_agreement":null},{"id":"W2809277978","doi":"10.1002/cjce.23259","title":"Activation and deactivation scenarios in a plasma‐synthesized Co/C catalyst for Fischer‐Tropsch synthesis","year":2018,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Catalysis; Fischer–Tropsch process; Squalane; Chemistry; Space velocity; Cobalt; Phase (matter); Nuclear chemistry; Analytical Chemistry (journal); Chemical engineering; Chromatography; Inorganic chemistry; Organic chemistry; Selectivity","score_opus":0.012377451278147163,"score_gpt":0.21922072494332667,"score_spread":0.20684327366517952,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2809277978","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99708855,0.00004547801,0.0020312541,0.00049269985,0.000076414675,0.00015502679,0.0000064168808,0.000017196737,0.00008695712],"genre_scores_gemma":[0.9984975,0.0000010460868,0.0010882873,0.00002094896,0.00031052434,0.000019572508,0.0000046148607,0.00004243947,0.000015054117],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99888176,0.000011836785,0.00043402394,0.0001343877,0.00017218792,0.00036583553],"domain_scores_gemma":[0.99862456,0.0006771697,0.0001538945,0.00015615502,0.00011537946,0.00027284623],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005528863,0.00017346056,0.00031215596,0.0002947288,0.000067337816,0.000035869365,0.00023515626,0.00014200073,0.000014546937],"category_scores_gemma":[0.003032832,0.000139845,0.000091554226,0.00025478486,0.000073176445,0.0002502654,0.0000138653,0.00037236998,0.000002127021],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000064648855,0.0000059661397,0.000110168054,0.000053987787,0.000059032627,0.000004163328,0.00042576907,0.001111543,0.99566,0.00024042744,0.00001750075,0.0022467747],"study_design_scores_gemma":[0.00045896275,0.000017792107,0.000082481674,0.00025112453,0.00003737125,0.00008419991,0.00003796114,0.04179902,0.9563426,0.000042511838,0.0006839882,0.00016201955],"about_ca_topic_score_codex":0.0013566319,"about_ca_topic_score_gemma":0.00042072326,"teacher_disagreement_score":0.04068748,"about_ca_system_score_codex":0.00052748644,"about_ca_system_score_gemma":0.00018951147,"threshold_uncertainty_score":0.5702713},"labels":[],"label_agreement":null},{"id":"W2810969569","doi":"10.1016/j.ultsonch.2018.06.017","title":"Ultrasound-assisted impregnation for high temperature Fischer-Tropsch catalysts","year":2018,"lang":"en","type":"article","venue":"Ultrasonics Sonochemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":27,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Syngas; Fischer–Tropsch process; Catalysis; Chemical engineering; Methane; Partial oxidation; Yield (engineering); Natural gas; Chemistry; Carbon dioxide reforming; Materials science; Bimetallic strip; Organic chemistry; Metallurgy","score_opus":0.009375325147083525,"score_gpt":0.2464163593909439,"score_spread":0.23704103424386036,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2810969569","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9949149,0.0002980068,0.0012691207,0.00014319159,0.0004487904,0.00034903322,0.00024792418,0.000469139,0.0018598766],"genre_scores_gemma":[0.98859906,0.000021675507,0.005215862,0.00005943851,0.0011946274,0.00013019278,0.0014727511,0.00011674937,0.0031896604],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977335,0.00001293057,0.0005040444,0.0006771446,0.00035766262,0.0007147169],"domain_scores_gemma":[0.99802047,0.00038212587,0.00020385857,0.00078037474,0.00037437852,0.0002388177],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00028020205,0.000431552,0.00041262136,0.00007072042,0.00023341643,0.00007177232,0.0005078282,0.00056323904,0.0001338071],"category_scores_gemma":[0.0014112154,0.0004265866,0.00025413494,0.0004018607,0.00013021185,0.00023439527,0.00006323864,0.00048652224,0.00006232198],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000044857326,0.00006358413,0.00012301578,0.00020963693,0.00012355862,0.000002258606,0.00015120777,0.000012632966,0.9967472,0.00038598877,0.00093700906,0.0011990645],"study_design_scores_gemma":[0.000982153,0.000042714804,0.00014396568,0.0001187375,0.000104009945,0.00016639395,0.00015048841,0.0003487273,0.9948909,0.00016654725,0.002349208,0.00053613586],"about_ca_topic_score_codex":0.00007143327,"about_ca_topic_score_gemma":0.000020693107,"teacher_disagreement_score":0.0063158744,"about_ca_system_score_codex":0.00043376503,"about_ca_system_score_gemma":0.00013274027,"threshold_uncertainty_score":0.9998186},"labels":[],"label_agreement":null},{"id":"W2811252372","doi":"10.1016/b978-0-444-64235-6.50245-x","title":"Combining Biomass, Natural Gas, and Carbonless Heat to Produce Liquid Fuels and Electricity","year":2018,"lang":"en","type":"book-chapter","venue":"Computer-aided chemical engineering/Computer aided chemical engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"McMaster University","keywords":"Greenhouse gas; Waste management; Environmental science; Biomass (ecology); Natural gas; Methane; Liquid fuel; Combined cycle; Fossil fuel; Life-cycle assessment; Carbon capture and storage (timeline); Nuclear engineering; Process engineering; Engineering; Environmental engineering; Chemistry; Mechanical engineering; Gas turbines; Climate change; Production (economics)","score_opus":0.007087228471987956,"score_gpt":0.1947496538619887,"score_spread":0.18766242539000075,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2811252372","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8326926,0.0045538074,0.15010175,0.0003728926,0.0038821301,0.0023805802,0.00014804935,0.005177619,0.0006905517],"genre_scores_gemma":[0.782738,0.00022835493,0.1893373,0.0006350222,0.019141104,0.00038054064,0.001232419,0.0032606535,0.0030466681],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99126554,0.000018486395,0.0020757504,0.003115332,0.0011504435,0.0023744341],"domain_scores_gemma":[0.99522746,0.00071525126,0.00029385573,0.0016093829,0.00034754918,0.0018065134],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.00047747302,0.0028466054,0.0030261036,0.0010585596,0.00012196405,0.0002664055,0.0014246256,0.0016603682,0.00003914029],"category_scores_gemma":[0.0003046261,0.0031322858,0.00066411216,0.0006096912,0.00023592687,0.00044255363,0.0028484543,0.0032540718,0.000055397853],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013510833,0.000067039524,0.0000015453412,0.0022377165,0.0007113333,0.00015756726,0.0004176635,0.0043861554,0.98539513,0.001454932,0.00029608913,0.0047396915],"study_design_scores_gemma":[0.0012582705,0.00024349181,0.0000023846264,0.0017619886,0.00023970279,0.00074941467,0.0000016311985,0.37766412,0.6101715,0.000098884935,0.0049423343,0.0028662656],"about_ca_topic_score_codex":0.000034506586,"about_ca_topic_score_gemma":6.899682e-7,"teacher_disagreement_score":0.37522364,"about_ca_system_score_codex":0.0010516745,"about_ca_system_score_gemma":0.00008916711,"threshold_uncertainty_score":0.9996357},"labels":[],"label_agreement":null},{"id":"W2886141776","doi":"10.1002/cctc.201800608","title":"Effect of Phosphorus on the Activity and Stability of Supported Cobalt Catalysts for Fischer‐Tropsch Synthesis","year":2018,"lang":"en","type":"article","venue":"ChemCatChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Cobalt; Sintering; Chemistry; Selectivity; Methane; Heterogeneous catalysis; Inorganic chemistry; Chemical engineering; Organic chemistry","score_opus":0.014504608588728474,"score_gpt":0.2582958105969423,"score_spread":0.2437912020082138,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2886141776","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9983916,0.00007323127,0.00008415741,0.00009376443,0.000055624427,0.0004542283,0.00007840345,0.000044821805,0.0007241591],"genre_scores_gemma":[0.9996489,0.000006743701,0.00009464633,0.000005789398,0.00006148665,0.00010207291,0.000011316026,0.000034202636,0.000034809687],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988396,0.000037723268,0.0003015809,0.0003104882,0.00022562523,0.00028499484],"domain_scores_gemma":[0.9968221,0.002126358,0.00020228911,0.00064051116,0.00012514992,0.00008357437],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010103837,0.00022523323,0.00051983824,0.000037118425,0.000051714436,0.000004652952,0.00024269031,0.00014089074,0.000032589473],"category_scores_gemma":[0.0023178966,0.00014985248,0.00017914356,0.00022497054,0.00028108247,0.00006991271,0.00010182364,0.00015916047,0.000004290889],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004501725,0.00007671593,0.0008275658,0.00052774104,0.00011423235,2.9849812e-7,0.00029517987,1.3065261e-7,0.9814507,0.000050458275,0.00004282746,0.016164001],"study_design_scores_gemma":[0.0004863323,0.00021776512,0.00033872787,0.00007841988,0.00012951154,0.0000027622254,0.000056890425,0.00041350757,0.9979656,0.000017832008,0.00015053738,0.00014211617],"about_ca_topic_score_codex":0.00022572296,"about_ca_topic_score_gemma":0.000009744814,"teacher_disagreement_score":0.01651492,"about_ca_system_score_codex":0.00009543839,"about_ca_system_score_gemma":0.00003516223,"threshold_uncertainty_score":0.6110807},"labels":[],"label_agreement":null},{"id":"W2886158192","doi":"10.1016/j.fuel.2018.07.146","title":"Ternary oxide-supported bimetallic nickel-copper catalysts for a single step high temperature water gas shift of biogas reformate","year":2018,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Catalytic reforming; Atmospheric pressure; Bimetallic strip; Calcination; Syngas; Chemistry; Ternary operation; Water-gas shift reaction; Carbon dioxide reforming; Nickel; Oxide; Inorganic chemistry; Chemical engineering; Organic chemistry","score_opus":0.011880549611664758,"score_gpt":0.2312052398653896,"score_spread":0.21932469025372484,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2886158192","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99716663,0.00015823441,0.000073690164,0.0001687797,0.00041180916,0.00040116077,0.0001580709,0.00022234974,0.0012392608],"genre_scores_gemma":[0.995428,0.000008542289,0.0017232065,0.000067637055,0.00035985807,0.000052573694,0.00067836535,0.00010866924,0.0015731171],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978615,0.000016562355,0.00065972324,0.00042470306,0.00032739536,0.000710141],"domain_scores_gemma":[0.9987194,0.00004497497,0.00015863593,0.0007360155,0.00016494891,0.00017602122],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00028179187,0.00036386523,0.0005444301,0.00024838897,0.00007608057,0.000025488316,0.00042591753,0.0002831744,0.000090316535],"category_scores_gemma":[0.00007768957,0.00025088122,0.00029248782,0.00026545196,0.00012794725,0.00038866972,0.0002185491,0.00022600761,0.0002453503],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001201068,0.00008921419,0.000077497556,0.00032889526,0.00018303294,0.000012926423,0.00047156936,0.000004029483,0.9978222,0.00015864699,0.00041294048,0.00031891192],"study_design_scores_gemma":[0.0010189179,0.00017035604,0.000068566886,0.00011753083,0.00011866175,0.00007000745,0.00006498568,0.00017402988,0.9879097,0.00015968872,0.009766565,0.00036101215],"about_ca_topic_score_codex":0.00044535447,"about_ca_topic_score_gemma":0.000053254502,"teacher_disagreement_score":0.00991255,"about_ca_system_score_codex":0.00015556302,"about_ca_system_score_gemma":0.00003059697,"threshold_uncertainty_score":0.99999434},"labels":[],"label_agreement":null},{"id":"W2886652686","doi":"10.1016/j.energy.2018.08.058","title":"Combining petroleum coke and natural gas for efficient liquid fuels production","year":2018,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":43,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"Natural Sciences and Engineering Research Council of Canada; U.S. Department of Energy","keywords":"Petroleum coke; Natural gas; Wood gas generator; Waste management; Substitute natural gas; Greenhouse gas; Syngas; Process engineering; Environmental science; Engineering; Coke; Coal; Chemistry","score_opus":0.007938109169921402,"score_gpt":0.2272439001785938,"score_spread":0.2193057910086724,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2886652686","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9948883,0.00034902108,0.0028931345,0.00013054704,0.00093142333,0.000053628595,0.0000022143824,0.00012865273,0.0006230797],"genre_scores_gemma":[0.996962,0.000005879981,0.00037247615,0.000026341648,0.0007306668,0.000025593272,0.000022841772,0.000029147903,0.0018250189],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992459,0.0000068007635,0.00014998436,0.00023473486,0.000116361836,0.0002462189],"domain_scores_gemma":[0.9996303,0.000041074396,0.000046582758,0.0001658837,0.000057108497,0.000059092097],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013241505,0.000114046394,0.0001419201,0.00007089517,0.000083273204,0.0000099584395,0.00007238696,0.000051614024,0.000007501072],"category_scores_gemma":[0.00015978544,0.00010125068,0.000049417064,0.00008879929,0.00005217218,0.000057834837,0.00005784752,0.000076805205,0.000004018697],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000110810375,0.000019605128,0.0000043992645,0.000038167494,0.00002855211,9.559549e-7,0.00021895858,0.0006790245,0.98975724,0.0040959367,0.00004575752,0.0050005703],"study_design_scores_gemma":[0.00033903707,0.000117608055,0.0000069088933,0.00003499583,0.000016305647,0.000032086835,0.000044431505,0.028687047,0.9522422,0.00005270528,0.018283777,0.00014290317],"about_ca_topic_score_codex":0.000050418872,"about_ca_topic_score_gemma":0.00001638952,"teacher_disagreement_score":0.03751507,"about_ca_system_score_codex":0.000064574066,"about_ca_system_score_gemma":0.00000953038,"threshold_uncertainty_score":0.4128883},"labels":[],"label_agreement":null},{"id":"W2887540809","doi":"10.3390/catal8080319","title":"Investigation of Ni/SiO2 Fiber Catalysts Prepared by Different Methods on Hydrogen production from Ethanol Steam Reforming","year":2018,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Chulalongkorn University","keywords":"Catalysis; Steam reforming; Materials science; Hydrogen production; Chemical engineering; Nuclear chemistry; Adsorption; Fiber; Chemistry; Composite material; Organic chemistry","score_opus":0.022994340472213378,"score_gpt":0.2857375865951361,"score_spread":0.2627432461229227,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2887540809","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.996658,0.00038632346,0.00016976811,0.000086557724,0.0005935208,0.0005016237,0.000103298626,0.00028839824,0.0012125068],"genre_scores_gemma":[0.99401957,0.000011518741,0.0009589483,0.000028343255,0.00058879115,0.00009572261,0.0015429882,0.00011609419,0.0026380194],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9969041,0.00013664117,0.0009084963,0.00089983933,0.0006190789,0.00053185655],"domain_scores_gemma":[0.9975241,0.00016254954,0.00050433894,0.0013391603,0.00020314855,0.00026670567],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00061581074,0.00048428273,0.00070620567,0.0002838356,0.00012533812,0.0000124604685,0.00048426058,0.00032201633,0.000066600864],"category_scores_gemma":[0.0007707519,0.00041503328,0.00022198806,0.0005780045,0.00022260637,0.00042201922,0.00023384872,0.0003672178,0.00014050944],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000082934384,0.000046290006,0.0001752612,0.00011204391,0.00020356652,0.0000017645826,0.0017113712,0.000015814923,0.9795252,0.000007758308,0.00036354444,0.017754458],"study_design_scores_gemma":[0.00047510333,0.00010625087,0.00013509148,0.00031402416,0.00017876034,0.000013948987,0.000117011674,0.00045649087,0.99607277,0.00014204929,0.0015399267,0.00044854873],"about_ca_topic_score_codex":0.00091281463,"about_ca_topic_score_gemma":0.000054665346,"teacher_disagreement_score":0.01730591,"about_ca_system_score_codex":0.00055829284,"about_ca_system_score_gemma":0.000055926314,"threshold_uncertainty_score":0.9998301},"labels":[],"label_agreement":null},{"id":"W2888928184","doi":"10.1021/acs.iecr.8b00246","title":"Optimization of Coke Oven Gas Desulfurization and Combined Cycle Power Plant Electricity Generation","year":2018,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"","keywords":"Refinery; Power station; Oil refinery; Flue-gas desulfurization; Waste management; Process engineering; Environmental science; Electricity generation; Combined cycle; Electricity; Petroleum coke; Coke; Engineering; Power (physics); Mechanical engineering; Electrical engineering","score_opus":0.05316365762225857,"score_gpt":0.29409558344515935,"score_spread":0.2409319258229008,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2888928184","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99558985,0.000050835315,0.0029871098,0.00004967592,0.00012692444,0.0002353941,0.000030153833,0.000117111136,0.00081297115],"genre_scores_gemma":[0.9986634,0.00001633315,0.00020704848,0.0000016492273,0.00068438007,0.000018773499,0.00018077673,0.000044139582,0.00018344718],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983567,0.000028569824,0.00037805815,0.00029856368,0.00051178585,0.0004263507],"domain_scores_gemma":[0.99908435,0.0001658965,0.000076207805,0.0002713335,0.00027572722,0.0001264678],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00081551686,0.00017006161,0.00024132579,0.00015118967,0.00008666081,0.00003341073,0.0001852686,0.00032271136,0.000097454795],"category_scores_gemma":[0.0015484598,0.0001807102,0.000042730906,0.00070037553,0.00008398322,0.0001497312,0.0001106658,0.00053921144,0.000003516615],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000064456915,0.000030803523,0.000058660804,0.000053582044,0.000034483124,0.0000025609975,0.00007787622,0.03331384,0.9658445,0.000094873874,0.00007005829,0.00035428655],"study_design_scores_gemma":[0.0005707502,0.000053290656,0.0000057951293,0.000051335846,0.000008142702,0.000009892422,0.0000085386755,0.33876535,0.66021794,0.0000062359004,0.00018967947,0.00011304726],"about_ca_topic_score_codex":0.000057716465,"about_ca_topic_score_gemma":6.9215366e-7,"teacher_disagreement_score":0.30562657,"about_ca_system_score_codex":0.00022329492,"about_ca_system_score_gemma":0.00007858131,"threshold_uncertainty_score":0.73691475},"labels":[],"label_agreement":null},{"id":"W2897274758","doi":"10.3390/nano8100822","title":"Use of Plasma-Synthesized Nano-Catalysts for CO Hydrogenation in Low-Temperature Fischer–Tropsch Synthesis: Effect of Catalyst Pre-Treatment","year":2018,"lang":"en","type":"article","venue":"Nanomaterials","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Social Sciences and Humanities Research Council of Canada; Natural Sciences and Engineering Research Council of Canada; Networks of Centres of Excellence of Canada; Université de Sherbrooke","keywords":"Fischer–Tropsch process; Catalysis; Space velocity; X-ray photoelectron spectroscopy; Diesel fuel; Scanning electron microscope; Materials science; Analytical Chemistry (journal); Transmission electron microscopy; Selectivity; Particle size; Ultra-low-sulfur diesel; Gasoline; Nanoparticle; Nuclear chemistry; Chemical engineering; Chemistry; Nanotechnology; Organic chemistry; Physical chemistry; Composite material","score_opus":0.014775042906218441,"score_gpt":0.2646012176964636,"score_spread":0.24982617479024516,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2897274758","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978372,0.000074585856,0.000009965311,0.000009220954,0.0002747067,0.0011896004,0.0004770661,0.000082617065,0.000045038367],"genre_scores_gemma":[0.9983584,0.000016539338,0.00041617107,0.000002198157,0.00017851933,0.00056577614,0.0002499173,0.00007979309,0.00013267327],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977267,0.00014851162,0.0009970553,0.0004288279,0.00028729305,0.00041162389],"domain_scores_gemma":[0.9975919,0.0011596709,0.00045202416,0.00058827514,0.00012403748,0.000084087624],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007468474,0.00039502146,0.001183351,0.00029878443,0.00004600334,0.000025307316,0.0002577795,0.00034195094,0.000038011985],"category_scores_gemma":[0.0016049455,0.00030313135,0.00027124738,0.00028099192,0.000099155965,0.00031286734,0.000056305413,0.000048628328,0.000016903665],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0012353724,0.000120155586,0.0002502394,0.0009114053,0.00023548941,0.000003415648,0.0003157774,0.00004726342,0.99595594,0.000017652917,0.000011952802,0.00089532876],"study_design_scores_gemma":[0.0015416378,0.00033862726,0.000087637825,0.0006044155,0.00020389886,0.000013704323,0.000010049106,0.00040798774,0.99630004,0.0000033796362,0.00022226787,0.00026632595],"about_ca_topic_score_codex":0.00032939672,"about_ca_topic_score_gemma":0.000048813272,"teacher_disagreement_score":0.0010111593,"about_ca_system_score_codex":0.00029027366,"about_ca_system_score_gemma":0.00006479354,"threshold_uncertainty_score":0.99994206},"labels":[],"label_agreement":null},{"id":"W2899832184","doi":"10.1002/cjce.23384","title":"Enhanced CO selectivity for reverse water‐gas shift reaction using Ti<sub>4</sub>O<sub>7</sub>‐doped SrCe<sub>0.9</sub>Y<sub>0.1</sub>O<sub>3‐δ</sub> hollow fibre membrane reactor","year":2018,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Natural Science Foundation of Shandong Province; National Natural Science Foundation of China","keywords":"Analytical Chemistry (journal); Chemistry; Carbon monoxide; Desorption; Carbon dioxide; Yield (engineering); Adsorption; Hydrogen; Isotopologue; Methane; Nuclear chemistry; Materials science; Catalysis; Chromatography; Molecule; Physical chemistry; Organic chemistry","score_opus":0.01202012334484294,"score_gpt":0.21659340833842067,"score_spread":0.20457328499357774,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2899832184","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9908537,0.0002547326,0.0048799296,0.00043564013,0.0017318475,0.0011432751,0.00020462854,0.00041619362,0.00008004785],"genre_scores_gemma":[0.99478495,0.00012727446,0.00038475593,0.00016668318,0.0035365648,0.00006081935,0.00023343683,0.00069866865,0.000006829638],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99086,0.00017441038,0.0025118513,0.0014464904,0.0015520147,0.0034552724],"domain_scores_gemma":[0.99295706,0.000808872,0.001137043,0.0014896584,0.0008891583,0.0027182107],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.002294046,0.001860007,0.0023263313,0.0012496271,0.00060854293,0.00033594688,0.0014692276,0.0013991016,0.000016663904],"category_scores_gemma":[0.0021754946,0.0017141824,0.0014175788,0.0015781056,0.00043145285,0.0017513027,0.00026043988,0.0036097206,0.000116570896],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00048879255,0.00008900721,0.000009454363,0.000638393,0.00073804235,0.00019058686,0.0013558035,0.004539043,0.983908,0.0000286646,0.00018425904,0.007829959],"study_design_scores_gemma":[0.0026466388,0.00023381389,0.00005871706,0.0014373267,0.0007390021,0.0011780919,0.00009163062,0.0150482,0.9758981,0.0001222578,0.00054476934,0.0020014506],"about_ca_topic_score_codex":0.0005550681,"about_ca_topic_score_gemma":0.0013544641,"teacher_disagreement_score":0.010509157,"about_ca_system_score_codex":0.0050049317,"about_ca_system_score_gemma":0.0012441853,"threshold_uncertainty_score":0.9998973},"labels":[],"label_agreement":null},{"id":"W2900537794","doi":"10.1007/s13203-018-0218-5","title":"Dry reforming of methane for syngas production over Ni–Co-supported Al2O3–MgO catalysts","year":2018,"lang":"en","type":"article","venue":"Applied Petrochemical Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":39,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Memorial University of Newfoundland","funders":"Universiti Teknologi Petronas","keywords":"Catalysis; Syngas; Carbon dioxide reforming; Nanomaterial-based catalyst; Calcination; Materials science; Chemical engineering; Methane; Catalyst support; BET theory; Bimetallic strip; Methane reformer; Inorganic chemistry; Hydrogen production; Chemistry; Steam reforming; Organic chemistry","score_opus":0.053590225862605846,"score_gpt":0.38131745275016,"score_spread":0.3277272268875541,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2900537794","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9883784,0.0000935573,0.00087091734,0.00010240203,0.00018071513,0.00089637097,0.000036523405,0.00018014904,0.009260986],"genre_scores_gemma":[0.99377483,0.000015038456,0.0020866338,0.0000146684,0.0011467092,0.00036608716,0.0003577834,0.000120554345,0.002117666],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9955191,0.000036965404,0.0008054285,0.00090934435,0.001420108,0.0013090539],"domain_scores_gemma":[0.9972585,0.00055091135,0.00018591853,0.0010233772,0.0006361272,0.00034515507],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0025059301,0.000342486,0.00063247513,0.00052921905,0.00015188211,0.000017922019,0.0007030536,0.0003146629,0.0001642797],"category_scores_gemma":[0.002648007,0.0003096028,0.00022028516,0.0011868419,0.0005600495,0.00024653747,0.0003559167,0.0009010536,0.00013130302],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00046429163,0.00011327929,0.00009215393,0.00041898375,0.00012929698,0.0000027289498,0.00030412342,0.0000014633825,0.9913608,0.0011995999,0.0005309799,0.005382291],"study_design_scores_gemma":[0.00083176635,0.00010659205,0.00003930827,0.000096689546,0.000046129826,0.000012941969,0.0002665295,0.0004607405,0.9916122,0.0008000412,0.0054000868,0.00032698957],"about_ca_topic_score_codex":0.00029284073,"about_ca_topic_score_gemma":0.000027682943,"teacher_disagreement_score":0.0071433196,"about_ca_system_score_codex":0.0005387136,"about_ca_system_score_gemma":0.0001747918,"threshold_uncertainty_score":0.9999356},"labels":[],"label_agreement":null},{"id":"W2907671670","doi":"10.1201/b19455-7","title":"Fischer-Tropsch Synthesis: Comparisons of Al2O3- and TiO2-Supported Co Catalysts Prepared by Aqueous Impregnation and CVD Methods","year":2016,"lang":"en","type":"book-chapter","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Canadian Light Source","keywords":"Fischer–Tropsch process; Catalysis; Aqueous solution; Chemical engineering; Materials science; Chemistry; Organic chemistry; Selectivity; Engineering","score_opus":0.01768611882998369,"score_gpt":0.29056788296672265,"score_spread":0.272881764136739,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2907671670","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.010352625,0.012211034,0.050918348,0.00026600738,0.00027959305,0.0017227735,0.0015570468,0.00080135965,0.9218912],"genre_scores_gemma":[0.14687146,0.0015473897,0.039661128,0.000055857323,0.00028879519,0.00020940058,0.0014010498,0.000684772,0.80928016],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99774784,0.000040151226,0.0008484292,0.00065391615,0.00035906778,0.00035058294],"domain_scores_gemma":[0.99791783,0.0006083222,0.00050525786,0.00060318166,0.00012899465,0.00023643246],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00045789473,0.00056283467,0.0011207146,0.00026185036,0.000054584936,0.00002002681,0.0002252741,0.00065464235,0.0003029574],"category_scores_gemma":[0.0002317714,0.00045183007,0.00018174207,0.000045366327,0.0001866243,0.00018690502,0.00019587157,0.00034413353,0.000017796574],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007719581,0.000037684815,0.000031564403,0.00080873055,0.001137613,0.000010638298,0.00027028023,0.0000011187755,0.918684,0.0056262175,0.0026912556,0.07062367],"study_design_scores_gemma":[0.00080643373,0.00006656966,0.0000112154685,0.0009143106,0.0007536194,0.0001446816,0.00006808694,0.0013760052,0.90641904,0.0007898047,0.08758544,0.0010647711],"about_ca_topic_score_codex":0.00011898862,"about_ca_topic_score_gemma":0.000020389514,"teacher_disagreement_score":0.13651884,"about_ca_system_score_codex":0.00015792764,"about_ca_system_score_gemma":0.000055166453,"threshold_uncertainty_score":0.99979335},"labels":[],"label_agreement":null},{"id":"W2910245529","doi":"10.1149/ma2018-02/48/1685","title":"Electrochemical Promotion of Catalysis for CO<sub>2</sub> Hydrogenation on Ru-Based Catalyst Using Ionically Conducting Ceramics","year":2018,"lang":"en","type":"article","venue":"ECS Meeting Abstracts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Catalysis; Syngas; Materials science; Water-gas shift reaction; Nanoparticle; Chemical engineering; Carbon fibers; Yttria-stabilized zirconia; Electrochemistry; Inorganic chemistry; Cubic zirconia; Ceramic; Nanotechnology; Chemistry; Organic chemistry; Electrode; Metallurgy","score_opus":0.033429998262479776,"score_gpt":0.2812593861200372,"score_spread":0.24782938785755743,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2910245529","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9963317,0.000021899377,0.0017039356,0.000055838707,0.00015553055,0.00038727155,0.000020380352,0.00018087142,0.0011425588],"genre_scores_gemma":[0.9949205,0.0000012154403,0.0040070284,0.000019467783,0.0004719102,0.000025519963,0.00045091286,0.000095017494,0.00000841486],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9973902,0.000032401498,0.00092927524,0.00053888554,0.0005097505,0.00059948966],"domain_scores_gemma":[0.99786264,0.00048360278,0.00067889504,0.00042149296,0.0003975822,0.0001557973],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0011116664,0.0003248323,0.00046403348,0.00026584827,0.00019916991,0.000029540883,0.00025229403,0.0002873351,0.0000039172864],"category_scores_gemma":[0.0026670652,0.00033961632,0.00026206172,0.00042913228,0.00011730899,0.00018730495,0.00004009652,0.00035743142,0.000016917787],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000079242855,0.00015224192,0.00004697979,0.00020360827,0.000081185084,0.0000018163829,0.00012930088,0.015564162,0.98326325,0.000012243527,0.0000034695195,0.00046247116],"study_design_scores_gemma":[0.0006266796,0.000134173,0.000018675682,0.00032391542,0.00013767707,0.000017850229,0.00003448917,0.096138634,0.9021957,0.00003840536,0.000025421743,0.00030840255],"about_ca_topic_score_codex":0.00007488524,"about_ca_topic_score_gemma":0.000016969787,"teacher_disagreement_score":0.0810676,"about_ca_system_score_codex":0.00049845455,"about_ca_system_score_gemma":0.00013869262,"threshold_uncertainty_score":0.9999056},"labels":[],"label_agreement":null},{"id":"W2913381384","doi":"10.1016/j.renene.2019.01.125","title":"Autothermal dry reforming of methane with a nickel spinellized catalyst prepared from a negative value metallurgical residue","year":2019,"lang":"en","type":"article","venue":"Renewable Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":25,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Fonds de recherche du Québec – Nature et technologies","keywords":"Carbon dioxide reforming; Methane; Residue (chemistry); Nickel; Methane reformer; Catalysis; Metallurgy; Materials science; Waste management; Environmental science; Chemistry; Syngas; Engineering; Steam reforming; Organic chemistry; Hydrogen production","score_opus":0.007071236554291142,"score_gpt":0.214108322842008,"score_spread":0.20703708628771686,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2913381384","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9690185,0.00072801573,0.0142683955,0.0000235875,0.00015672008,0.00025598006,0.00005676465,0.00026419872,0.015227809],"genre_scores_gemma":[0.9779688,0.00003798751,0.0065713655,0.000027117527,0.00015248338,0.00005986225,0.00023915635,0.00013556363,0.014807626],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972571,0.000086400934,0.0007244813,0.00068796123,0.00062381465,0.0006202503],"domain_scores_gemma":[0.9979683,0.0003055325,0.00039072917,0.000998383,0.000111447924,0.0002255718],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00030460765,0.00044916425,0.0010597308,0.00022907303,0.000036309088,0.000014072947,0.00048988167,0.00025966138,0.00041773848],"category_scores_gemma":[0.00015363183,0.0003435833,0.00029443126,0.0006589006,0.00009222854,0.00036621687,0.00022426657,0.00022605465,0.00003101531],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000512378,0.000071366485,0.00006996732,0.00008985502,0.0005837144,0.000029346715,0.00039139227,0.25804457,0.7393163,0.00041090426,0.000004973659,0.00047523802],"study_design_scores_gemma":[0.0023589865,0.00012307712,0.000035987934,0.00030717926,0.00019205971,0.000021976222,0.00025606522,0.07774336,0.91648835,0.0002358455,0.001776738,0.00046037548],"about_ca_topic_score_codex":0.12738627,"about_ca_topic_score_gemma":0.0014740118,"teacher_disagreement_score":0.1803012,"about_ca_system_score_codex":0.00027805715,"about_ca_system_score_gemma":0.00021289616,"threshold_uncertainty_score":0.9999016},"labels":[],"label_agreement":null},{"id":"W2913533270","doi":"10.1016/j.fuel.2019.02.024","title":"Highly selective production of C5-C12 hydrocarbons over efficient Ru/heteropoly-acid catalysts","year":2019,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"National Natural Science Foundation of China","keywords":"Selectivity; Catalysis; Syngas; Chemistry; Gasoline; Hydrocarbon; Fischer–Tropsch process; Heteropoly acid; Organic chemistry; Chemical engineering","score_opus":0.005742881020019203,"score_gpt":0.21821201342151456,"score_spread":0.21246913240149534,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2913533270","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9939201,0.00030735612,0.00011109783,0.00003472042,0.00086994155,0.00029337272,0.000009534638,0.00014095807,0.004312955],"genre_scores_gemma":[0.9981714,0.0000045889897,0.00013136359,0.000008226011,0.0001663161,0.000018299952,0.000042094347,0.00004814236,0.0014095681],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986062,0.000015090818,0.00031978707,0.00038274168,0.0003414545,0.00033473416],"domain_scores_gemma":[0.99920183,0.00003008367,0.0001377651,0.00049704185,0.000049691324,0.000083590036],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00015498397,0.00020000471,0.00032319914,0.00016388335,0.000025176158,0.0000063258203,0.00017835795,0.00010931429,0.000031992546],"category_scores_gemma":[0.00012548258,0.00018351602,0.00014765962,0.00042301384,0.0000411006,0.000116089956,0.00009602608,0.00022612874,0.00016497546],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003547677,0.00007563982,0.0005160606,0.00018222409,0.00007956024,0.0000018862361,0.00059717393,0.00083607476,0.9970901,0.00016688262,0.000042651893,0.00037625918],"study_design_scores_gemma":[0.00039050684,0.00004909038,0.00065027317,0.00007258933,0.00004534818,0.000022177699,0.000052957534,0.003220297,0.9946528,0.00004217065,0.00057500857,0.0002267814],"about_ca_topic_score_codex":0.0002781549,"about_ca_topic_score_gemma":0.000012924385,"teacher_disagreement_score":0.0042513367,"about_ca_system_score_codex":0.00025311328,"about_ca_system_score_gemma":0.000034431072,"threshold_uncertainty_score":0.74835664},"labels":[],"label_agreement":null},{"id":"W2913832126","doi":"10.1039/c8re00334c","title":"Syn-gas from waste: the reduction of CO<sub>2</sub> with H<sub>2</sub>S","year":2019,"lang":"en","type":"article","venue":"Reaction Chemistry & Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"Saudi Basic Industries Corporation","keywords":"Syngas; Waste management; Materials science; Chemistry; Environmental science; Hydrogen; Engineering; Organic chemistry","score_opus":0.004788659912632059,"score_gpt":0.18827421003610406,"score_spread":0.183485550123472,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2913832126","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99726224,0.00016641138,0.0010603995,0.000044146283,0.00033783438,0.00021834444,0.000024716304,0.00033086282,0.0005550214],"genre_scores_gemma":[0.99883527,0.00008236883,0.00010488076,0.0000032556086,0.00058811915,0.000039958206,0.00016258802,0.00011734621,0.00006620421],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980928,0.000008929376,0.0004888892,0.00047081074,0.0004984063,0.00044016592],"domain_scores_gemma":[0.99864876,0.00013390748,0.00024642108,0.000731579,0.00009745776,0.00014187944],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00020672365,0.00039269557,0.00043286063,0.00007828148,0.00005244437,0.000023842556,0.0002620089,0.0002533437,0.00002235011],"category_scores_gemma":[0.000101717465,0.00033104845,0.00018862213,0.00040638057,0.00004240121,0.0003216542,0.000064426065,0.0006960401,0.000053878826],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047821235,0.000029478342,0.000025460358,0.00026852297,0.00016694563,0.0000042373736,0.00011591288,0.022707121,0.9743151,0.0000120286395,0.000016337508,0.0022910049],"study_design_scores_gemma":[0.00049450865,0.000016242877,0.000044752745,0.0003354389,0.00009808689,0.00016521743,0.00027176007,0.011672769,0.9858866,0.000004488151,0.0006312621,0.00037887634],"about_ca_topic_score_codex":0.000048778387,"about_ca_topic_score_gemma":9.900039e-7,"teacher_disagreement_score":0.011571469,"about_ca_system_score_codex":0.0004005118,"about_ca_system_score_gemma":0.000046680892,"threshold_uncertainty_score":0.99991417},"labels":[],"label_agreement":null},{"id":"W2914256782","doi":"10.1002/cjce.23458","title":"Role of promoters and catalyst supports for selective synthesis of higher alcohols over molybdenum carbides","year":2019,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"University of Queensland","keywords":"Syngas; Catalysis; Molybdenum; Selectivity; Chemistry; Methanol; Inorganic chemistry; Dissociation (chemistry); Carbon monoxide; Carbide; Organic chemistry","score_opus":0.0044054602943696935,"score_gpt":0.195290183271127,"score_spread":0.1908847229767573,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2914256782","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99901515,0.00048384568,0.000025701314,0.00004938765,0.00009198443,0.00016630892,0.000033329117,0.0000074391455,0.00012683652],"genre_scores_gemma":[0.9995912,0.0000013984929,0.00022627926,0.000005784067,0.00008410094,0.0000065789654,0.0000029080445,0.000041394254,0.00004039552],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989384,0.0000061994588,0.00045056076,0.00011458844,0.00018567487,0.00030457965],"domain_scores_gemma":[0.9989447,0.00027010852,0.0002195225,0.00018549,0.00012504793,0.00025513515],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029438632,0.00016104965,0.00045246497,0.00017743453,0.000015220837,0.00000879138,0.00024357384,0.000109513276,0.000022299613],"category_scores_gemma":[0.00035034123,0.00012642928,0.00017769061,0.0001705843,0.000055138265,0.000118476746,0.000023457402,0.0002475197,5.0005275e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000020622787,0.000005057573,0.000421844,0.00021115568,0.00018510778,0.0000030928668,0.00032819816,0.0013249584,0.9968664,0.000178218,0.000014056859,0.00044128488],"study_design_scores_gemma":[0.0002738449,0.000025641475,0.00024049387,0.00023333517,0.00011157763,0.00007857448,0.00002722781,0.0023371757,0.99627876,0.00007047357,0.0001873771,0.00013553856],"about_ca_topic_score_codex":0.0015463367,"about_ca_topic_score_gemma":0.00005169712,"teacher_disagreement_score":0.0014946396,"about_ca_system_score_codex":0.00020241443,"about_ca_system_score_gemma":0.00015586354,"threshold_uncertainty_score":0.51556367},"labels":[],"label_agreement":null},{"id":"W2918203453","doi":"","title":"Life Cycle and Techno-Economic Analysis of Fischer-Tropsch Renewable Diesel and Jet Fuel Production","year":2016,"lang":"en","type":"dissertation","venue":"TSpace","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada; University of Toronto","keywords":"Fischer–Tropsch process; Jet fuel; Diesel fuel; Renewable energy; Production (economics); Environmental science; Waste management; Engineering; Economics; Chemistry; Catalysis","score_opus":0.00879484358785439,"score_gpt":0.27471800620455633,"score_spread":0.26592316261670196,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2918203453","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9939196,0.0020623102,0.000047493006,0.00014059618,0.0001488473,0.00015415948,0.000020927024,0.000088509136,0.0034175687],"genre_scores_gemma":[0.9748153,0.000860693,0.00026411714,0.0000030598894,0.00014426209,0.000034597088,0.000315026,0.00006323961,0.023499696],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998935,0.000009462532,0.00030331526,0.00041592188,0.00013228938,0.00020403106],"domain_scores_gemma":[0.999151,0.000049631704,0.00026173063,0.00037375826,0.000050040813,0.000113828086],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017764897,0.0002416668,0.00060277246,0.00044150188,0.000038909922,0.000012094829,0.00010239152,0.00025839504,0.00006233529],"category_scores_gemma":[0.00037353026,0.00020239472,0.00011380539,0.00029081397,0.00003758026,0.00012373278,0.000047087353,0.00016549046,0.000005239876],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013201385,0.000028302204,0.0012222212,0.0014042737,0.0021840553,0.0000014471315,0.0025909273,0.0015561718,0.98560375,0.00010274932,0.000097542645,0.0050765304],"study_design_scores_gemma":[0.0006018508,0.000049319908,0.0023310638,0.00043727245,0.003378377,0.000006974877,0.00335393,0.00850491,0.9778331,0.00021352108,0.0024608152,0.00082889834],"about_ca_topic_score_codex":0.0028710351,"about_ca_topic_score_gemma":0.00093192083,"teacher_disagreement_score":0.020082127,"about_ca_system_score_codex":0.00010421312,"about_ca_system_score_gemma":0.000048917736,"threshold_uncertainty_score":0.8253417},"labels":[],"label_agreement":null},{"id":"W2921187386","doi":"10.3390/en12061031","title":"Is the Fischer-Tropsch Conversion of Biogas-Derived Syngas to Liquid Fuels Feasible at Atmospheric Pressure?","year":2019,"lang":"en","type":"article","venue":"Energies","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Seventh Framework Programme; Queen's University; Queen's University Belfast; European Commission","keywords":"Fischer–Tropsch process; Syngas; Biogas; Gas to liquids; Methane; Waste management; Liquid fuel; Atmospheric pressure; Renewable fuels; Environmental science; Synthetic fuel; Renewable energy; Fossil fuel; Chemistry; Catalysis; Engineering; Selectivity; Organic chemistry","score_opus":0.009602550122427193,"score_gpt":0.22430799526721007,"score_spread":0.21470544514478287,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2921187386","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9959964,0.0010375454,0.000055103916,0.00029708043,0.0002654343,0.00020555181,0.00001398945,0.00010985204,0.0020190105],"genre_scores_gemma":[0.9863699,0.00005793987,0.00064661365,0.00010034327,0.00006780858,0.00001778344,0.000010550762,0.000042616008,0.012686429],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998846,0.000024037654,0.00024789863,0.00026853808,0.0003042446,0.00030930215],"domain_scores_gemma":[0.99902743,0.00013282186,0.00009844184,0.0005946988,0.00006322258,0.000083391715],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013837655,0.00019458515,0.0003006484,0.000021933125,0.000058117606,0.000010505909,0.00037698608,0.00010556979,0.000656328],"category_scores_gemma":[0.00008038312,0.0001369909,0.00016569163,0.00029900682,0.000045276767,0.00013909901,0.00039977184,0.00013259385,0.00028340073],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000119676806,0.000014549584,0.00050487794,0.00012768983,0.00010430673,0.0000013233432,0.00079773035,0.010309691,0.9873119,0.00020521923,0.00042861004,0.00007442923],"study_design_scores_gemma":[0.0003087896,0.000084120016,0.000199518,0.00006225346,0.000047783946,0.0000050374097,0.00026443318,0.0008362878,0.9370224,0.000004923599,0.060995523,0.00016894132],"about_ca_topic_score_codex":0.0003163494,"about_ca_topic_score_gemma":0.0000054199822,"teacher_disagreement_score":0.060566913,"about_ca_system_score_codex":0.000078751655,"about_ca_system_score_gemma":0.00002120567,"threshold_uncertainty_score":0.7186332},"labels":[],"label_agreement":null},{"id":"W2923766510","doi":"10.1002/er.4440","title":"An overview of the methanol reforming process: Comparison of fuels, catalysts, reformers, and systems","year":2019,"lang":"en","type":"article","venue":"International Journal of Energy Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":140,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Catalytic reforming; Methanol; Methane reformer; Steam reforming; Process engineering; Fuel cells; Hydrogen; Methanol fuel; Hydrogen production; Waste management; Chemistry; Engineering; Chemical engineering; Organic chemistry","score_opus":0.09591798077029426,"score_gpt":0.42965085628283195,"score_spread":0.3337328755125377,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2923766510","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99227154,0.0058986037,0.00007121774,0.000101134996,0.00039595485,0.00007443192,0.000011286473,0.0000051888383,0.0011706217],"genre_scores_gemma":[0.9992478,0.00030328045,0.000055724002,0.0000042666193,0.0001303992,0.0000032422752,0.0000069700877,0.000021004382,0.00022732464],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99696416,0.00011070789,0.00084603846,0.00013983401,0.0017192366,0.00022001663],"domain_scores_gemma":[0.9973782,0.00019567645,0.00059611356,0.00029120196,0.0014419128,0.00009692956],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0016233837,0.000112759546,0.0004145937,0.00043369667,0.000026352336,0.000019177305,0.001052153,0.00009268342,0.000018055818],"category_scores_gemma":[0.00031494067,0.00007054034,0.00013573172,0.00036477268,0.00010014841,0.00043165704,0.00020312489,0.0004359916,0.0000011331146],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017767094,0.00013864844,0.007843014,0.00048786393,0.00042125848,0.000007759421,0.0008541665,0.0023775334,0.9703354,0.009461857,0.000011268575,0.0078835115],"study_design_scores_gemma":[0.0006104274,0.00016820345,0.00031532452,0.0012282276,0.000025811627,0.00018139332,0.0021118983,0.0053198957,0.9882022,0.0003068282,0.0014249871,0.00010479734],"about_ca_topic_score_codex":0.0006827657,"about_ca_topic_score_gemma":0.00002728035,"teacher_disagreement_score":0.017866759,"about_ca_system_score_codex":0.00026465557,"about_ca_system_score_gemma":0.00017836347,"threshold_uncertainty_score":0.28765517},"labels":[],"label_agreement":null},{"id":"W2925723235","doi":"10.1007/s10562-019-02770-2","title":"H2S Poisoning and Regeneration of a Nickel Spinellized Catalyst Prepared from Waste Metallurgical Residues, During Dry Autothermal Methane Reforming","year":2019,"lang":"en","type":"article","venue":"Catalysis Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Calcination; Catalysis; Methane; Chemistry; Nickel; Methane reformer; Space velocity; Carbon dioxide reforming; Syngas; Steam reforming; Metallurgy; Inorganic chemistry; Materials science; Organic chemistry; Hydrogen production; Selectivity","score_opus":0.006434529702147624,"score_gpt":0.20981599129893932,"score_spread":0.2033814615967917,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2925723235","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9958871,0.0016989743,0.0014103632,0.00022893162,0.00013976109,0.00030799213,0.00003431687,0.00016398398,0.00012859197],"genre_scores_gemma":[0.99623036,0.00004470401,0.0016632548,0.00010079313,0.00020943939,0.000035529552,0.0007154759,0.00010105839,0.0008994087],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99709564,0.00007473069,0.00095327897,0.0007955854,0.0005347147,0.00054604374],"domain_scores_gemma":[0.9981883,0.00014739894,0.0004476964,0.0009657334,0.000061102466,0.00018973199],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00044060312,0.0004360085,0.0009882448,0.00037522902,0.00008210916,0.00003314397,0.0003772258,0.00020056908,0.00013087962],"category_scores_gemma":[0.00017650262,0.0003993112,0.00036969848,0.0005209123,0.000097510645,0.00063693407,0.00028427638,0.0003604229,0.000043797878],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013197659,0.000023867358,0.00044980514,0.00018963042,0.00053100474,0.00002315394,0.00092649134,0.005267709,0.9918177,0.000014555174,0.000007761063,0.0006163219],"study_design_scores_gemma":[0.001627848,0.000018379198,0.00039139815,0.00020733986,0.00042035233,0.000024172567,0.00032445884,0.020555273,0.9757494,0.0000046120526,0.0002015212,0.00047528063],"about_ca_topic_score_codex":0.0017207717,"about_ca_topic_score_gemma":0.000055117976,"teacher_disagreement_score":0.01606836,"about_ca_system_score_codex":0.00026587004,"about_ca_system_score_gemma":0.00003578235,"threshold_uncertainty_score":0.99984586},"labels":[],"label_agreement":null},{"id":"W2935997349","doi":"10.1016/j.enconman.2019.04.026","title":"Nonthermal plasma-catalytic conversion of biogas to liquid chemicals with low coke formation","year":2019,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":58,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Institute for Oil Sands Innovation, University of Alberta; Natural Sciences and Engineering Research Council of Canada; University of Alberta","keywords":"Coke; Catalysis; Biogas; Nonthermal plasma; Waste management; Chemistry; Plasma; Chemical engineering; Environmental science; Engineering; Organic chemistry; Physics","score_opus":0.0038501876555363163,"score_gpt":0.18316065860324907,"score_spread":0.17931047094771274,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2935997349","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9907798,0.000026261141,0.0019788134,0.00012315664,0.00011941653,0.00022385208,0.0000044303556,0.00006346605,0.006680792],"genre_scores_gemma":[0.99663174,0.00007063227,0.00025181717,0.00012758936,0.000016385793,0.000010519978,0.00005767613,0.000019052368,0.0028145714],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990932,0.000007632593,0.0002090783,0.00022907043,0.00025235716,0.0002086601],"domain_scores_gemma":[0.9994871,0.000026029458,0.000085689164,0.00024602193,0.000035296347,0.00011985171],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000101425656,0.00015449706,0.00021549981,0.0001772076,0.000026740645,0.0000070890796,0.00013474503,0.00006008309,0.00014125733],"category_scores_gemma":[0.0000050582726,0.00012852733,0.00005158266,0.00017923996,0.000025347525,0.00019062233,0.00021311104,0.000054449858,0.00008204773],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0015389159,0.00012343682,0.00009113705,0.0019824947,0.00028426398,0.00002767015,0.0005758823,0.0022726976,0.9769645,0.009940896,0.0005208995,0.005677211],"study_design_scores_gemma":[0.0014668675,0.00015844055,0.000021826836,0.00020680435,0.000048819973,0.0000065721038,0.0003217909,0.008441723,0.94861835,0.0000013671712,0.040517047,0.00019040766],"about_ca_topic_score_codex":0.00009406339,"about_ca_topic_score_gemma":0.0000025742504,"teacher_disagreement_score":0.039996147,"about_ca_system_score_codex":0.00009365539,"about_ca_system_score_gemma":0.0000057654393,"threshold_uncertainty_score":0.5241192},"labels":[],"label_agreement":null},{"id":"W2941872841","doi":"10.3390/ma12091362","title":"Evaluation of a Catalyst Durability in Absence and Presence of Toluene Impurity: Case of the Material Co2Ni2Mg2Al2 Mixed Oxide Prepared by Hydrotalcite Route in Methane Dry Reforming to Produce Energy","year":2019,"lang":"en","type":"article","venue":"Materials","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Université Libanaise; Centre National de la Recherche Scientifique; Agence Universitaire de la Francophonie","keywords":"Catalysis; Toluene; Hydrotalcite; Methane; Carbon dioxide reforming; Adsorption; Carbon fibers; Inorganic chemistry; Calcination; Chemistry; Chemical engineering; Oxide; Materials science; Syngas; Organic chemistry; Composite material; Composite number","score_opus":0.011402049485074492,"score_gpt":0.2572501982365659,"score_spread":0.2458481487514914,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2941872841","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99847424,0.00007351391,0.0000056118415,0.000015931444,0.00022820072,0.00089457695,0.0002672128,0.000013062601,0.000027619859],"genre_scores_gemma":[0.9996598,0.0000038384683,0.00013311466,0.0000025568147,0.000016387714,0.000098794284,0.00003391218,0.000022379429,0.000029235547],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99746907,0.0002904634,0.0010671793,0.00040470067,0.0005000903,0.00026851404],"domain_scores_gemma":[0.99852103,0.00010783284,0.00041903922,0.0007380289,0.00016281554,0.00005125951],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0034694339,0.00019274738,0.00067882484,0.0001440544,0.00001119677,0.00000856795,0.00026192877,0.00011510186,0.000030416966],"category_scores_gemma":[0.001217318,0.00015226127,0.000050983035,0.0003825791,0.00006689073,0.00023640637,0.0003547279,0.00005972651,6.1699285e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024605208,0.000053343316,0.0012707898,0.0005609051,0.000023646277,0.0000043718924,0.0010291162,0.00053131854,0.99549484,0.000019179264,4.29491e-7,0.00076598726],"study_design_scores_gemma":[0.00074339565,0.000038812734,0.0018788422,0.00035981246,0.00004157301,0.000044721222,0.00015517187,0.0011133713,0.99537283,0.00009714596,0.000005508127,0.00014881772],"about_ca_topic_score_codex":0.029323108,"about_ca_topic_score_gemma":0.0017133902,"teacher_disagreement_score":0.027609719,"about_ca_system_score_codex":0.00029161802,"about_ca_system_score_gemma":0.00007973594,"threshold_uncertainty_score":0.9771407},"labels":[],"label_agreement":null},{"id":"W2943336806","doi":"10.1016/j.cej.2019.04.214","title":"Catalytic membrane reactor for CO2 hydrogenation using renewable streams: Model-based feasibility analysis","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":23,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Membrane reactor; Catalysis; Membrane; Renewable energy; Yield (engineering); Chemical engineering; Materials science; Process engineering; Biomass (ecology); Heat exchanger; Waste management; Chemistry; Environmental science; Nuclear engineering; Engineering; Mechanical engineering; Organic chemistry; Composite material","score_opus":0.019792713421852386,"score_gpt":0.2533350881672652,"score_spread":0.2335423747454128,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2943336806","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6368544,0.00007724129,0.36248228,0.000016304024,0.00013868132,0.00021106041,0.000029764555,0.00012942587,0.00006082483],"genre_scores_gemma":[0.9698703,0.000002349755,0.02951522,0.000013799354,0.00021884423,0.0000130246435,0.00015634956,0.00009047829,0.00011960441],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99777913,0.000008654535,0.0006815259,0.00044221355,0.00045614524,0.00063232315],"domain_scores_gemma":[0.99851054,0.00021703746,0.00021216922,0.000512656,0.0001886358,0.00035893836],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000546197,0.0003594423,0.0006666988,0.00041245317,0.00005199512,0.000054781674,0.000357153,0.0002482741,0.0000423322],"category_scores_gemma":[0.0005571792,0.0003481681,0.00067864393,0.00078212284,0.000022631913,0.00032100466,0.000055089517,0.0005075898,0.000007460745],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000028527387,0.00002889643,0.00008697748,0.00012477396,0.00019843051,0.0000016427218,0.000017260032,0.49765652,0.5017767,0.000011529608,0.0000022060046,0.000066518405],"study_design_scores_gemma":[0.0006181556,0.000009097077,0.0000019317752,0.00005093034,0.00033308237,0.000023972962,0.000004739857,0.52004844,0.47864592,0.00001559976,0.000032986347,0.0002151404],"about_ca_topic_score_codex":0.000037622136,"about_ca_topic_score_gemma":0.0000011054173,"teacher_disagreement_score":0.3330159,"about_ca_system_score_codex":0.001013767,"about_ca_system_score_gemma":0.000133785,"threshold_uncertainty_score":0.999897},"labels":[],"label_agreement":null},{"id":"W2947260425","doi":"10.1002/cjce.23518","title":"Importance of proper hydrodynamics modelling in fixed‐bed reactors: Fischer‐Tropsch synthesis study case","year":2019,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Instituto Mexicano del Petróleo; Consejo Nacional de Ciencia y Tecnología","keywords":"Fischer–Tropsch process; Isothermal process; Syngas; Continuous stirred-tank reactor; Nuclear engineering; Materials science; Mechanics; Thermodynamics; Catalysis; Process engineering; Chemistry; Selectivity; Chemical engineering; Engineering; Physics; Organic chemistry","score_opus":0.01125227070623872,"score_gpt":0.20053545675288634,"score_spread":0.18928318604664762,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2947260425","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99907845,0.00018119901,0.0002011127,0.00005139763,0.00013966527,0.00022877232,0.000007469934,0.000015445634,0.00009646139],"genre_scores_gemma":[0.9992623,0.0000014509454,0.0005321326,0.000005148352,0.000101830025,0.0000071008744,0.0000014987447,0.00006580944,0.000022744693],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9981433,0.000020871006,0.0008815027,0.00018230961,0.00030418253,0.00046783604],"domain_scores_gemma":[0.99862456,0.00025860433,0.00025416305,0.00041023732,0.00012124686,0.00033121434],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007793349,0.00024569745,0.0005634273,0.00030283863,0.000022707267,0.000021269838,0.00046406334,0.00012183618,0.000035486184],"category_scores_gemma":[0.00062594324,0.0001870084,0.0001762602,0.00043839394,0.000036607456,0.00023830899,0.00003889641,0.0008709915,0.0000037431728],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000032041193,0.000044828575,0.00678752,0.00016386979,0.0001566857,0.00097409583,0.0012713852,0.60722136,0.3830306,0.00008176767,0.0000020778498,0.00023375441],"study_design_scores_gemma":[0.0007233802,0.000053138032,0.00006758614,0.00048268112,0.00011532553,0.0018633126,0.00030822706,0.69277227,0.3031318,0.000018475472,0.000050203627,0.00041358796],"about_ca_topic_score_codex":0.0048769573,"about_ca_topic_score_gemma":0.0009959065,"teacher_disagreement_score":0.08555091,"about_ca_system_score_codex":0.00060886424,"about_ca_system_score_gemma":0.00022668476,"threshold_uncertainty_score":0.7625981},"labels":[],"label_agreement":null},{"id":"W2948737247","doi":"","title":"Design and Simulation of Novel Sabatier Reactors for the Thermocatalytic Conversion of CO2 into Renewable Natural Gas","year":2019,"lang":"en","type":"dissertation","venue":"UWSpace (University of Waterloo)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Natural gas; Renewable energy; Environmental science; Waste management; Engineering; Biochemical engineering","score_opus":0.01301266249351186,"score_gpt":0.21695290635840483,"score_spread":0.20394024386489298,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2948737247","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957868,0.0001945705,0.0032320064,0.000026863152,0.00017251009,0.00052424736,0.000016316026,0.000016136033,0.00003058047],"genre_scores_gemma":[0.95648193,0.00003686712,0.0012046541,8.593064e-7,0.000010665338,4.334322e-7,0.00034866697,0.000027840764,0.041888062],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992597,0.000013134685,0.00016782498,0.00020264453,0.0002158052,0.00014089597],"domain_scores_gemma":[0.99869925,0.00038798165,0.00041163652,0.00026408586,0.0002050221,0.000032002707],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017941682,0.00017392171,0.0004042846,0.00016082393,0.00006106987,0.000003152022,0.00023684136,0.00021323725,0.0000119441365],"category_scores_gemma":[0.000057992962,0.00014949487,0.00014860845,0.00013039415,0.00007551361,0.0001784508,0.00004947742,0.00013608955,8.8272765e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0007225545,0.000037173624,0.000030738465,0.002044761,0.00026219414,4.9006115e-7,0.04503445,0.062065605,0.88903785,0.000028360699,0.0000138469995,0.0007219669],"study_design_scores_gemma":[0.0011243455,0.000084370804,0.000055400596,0.00033942054,0.0003686644,8.1900583e-7,0.033505775,0.41781592,0.54647326,0.000019165616,0.000033989312,0.00017885641],"about_ca_topic_score_codex":0.020677406,"about_ca_topic_score_gemma":0.0005100011,"teacher_disagreement_score":0.35575032,"about_ca_system_score_codex":0.00008960285,"about_ca_system_score_gemma":0.00004742736,"threshold_uncertainty_score":0.985844},"labels":[],"label_agreement":null},{"id":"W2954207334","doi":"10.1016/j.jclepro.2019.06.027","title":"Analysis and optimization for energy, cost and carbon emission of a solar driven steam-autothermal hybrid methane reforming for hydrogen, ammonia and power production","year":2019,"lang":"en","type":"article","venue":"Journal of Cleaner Production","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":55,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"","keywords":"Methane reformer; Steam reforming; Hydrogen production; Methane; Exergy; Process engineering; Waste management; Ammonia production; Hydrogen; Water-gas shift reaction; Environmental science; Chemistry; Ammonia; Engineering; Organic chemistry","score_opus":0.007115641300170306,"score_gpt":0.22992082582504053,"score_spread":0.22280518452487022,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2954207334","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9905288,0.000546669,0.008086748,0.00016411829,0.00024077989,0.00040383858,0.0000057994193,0.000014143329,0.000009070735],"genre_scores_gemma":[0.9952543,0.0001975911,0.003941692,0.0000041994886,0.0002746632,0.000011637084,0.000024348905,0.00003779282,0.0002538158],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986772,0.00002932606,0.00058944797,0.0003012694,0.00021631748,0.00018643998],"domain_scores_gemma":[0.9987354,0.000047145648,0.00064741296,0.00017830236,0.0002993515,0.000092382405],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00086064,0.00016696073,0.00047637257,0.00043293228,0.000048291153,0.000011871407,0.000057624813,0.00008693608,0.0000033553456],"category_scores_gemma":[0.00034620016,0.00013830497,0.00012668845,0.00022209057,0.000040097173,0.00044903992,0.00003432978,0.0001313208,2.331033e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00055587286,0.000043352964,0.0014794859,0.00032238264,0.00046696234,6.61737e-7,0.00034699345,0.06229323,0.9142623,0.000004413025,0.0000039934685,0.020220332],"study_design_scores_gemma":[0.000834973,0.00023365146,0.00013448807,0.00012277332,0.00072423706,0.00023496097,0.00023190743,0.10254937,0.89425,0.000028528462,0.00049477996,0.00016033782],"about_ca_topic_score_codex":0.000040197676,"about_ca_topic_score_gemma":0.0000074456393,"teacher_disagreement_score":0.04025613,"about_ca_system_score_codex":0.00009681373,"about_ca_system_score_gemma":0.000029838158,"threshold_uncertainty_score":0.5639913},"labels":[],"label_agreement":null},{"id":"W2956016710","doi":"10.1021/acs.iecr.9b01426","title":"Design of an Air-Cooled Sabatier Reactor for Thermocatalytic Hydrogenation of CO<sub>2</sub>: Experimental Proof-of-Concept and Model-Based Feasibility Analysis","year":2019,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Coolant; Process engineering; Chemistry; Nuclear engineering; Environmental science; Thermodynamics; Engineering; Physics","score_opus":0.07751728830517665,"score_gpt":0.3341737538276151,"score_spread":0.2566564655224385,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2956016710","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99237823,0.00008397907,0.00644907,0.0000054756283,0.00002404144,0.0009049207,0.000090048416,0.000036804737,0.000027409162],"genre_scores_gemma":[0.99933535,4.927988e-7,0.00026944207,4.1140785e-7,0.00006341122,0.00007905639,0.00018004994,0.00004975871,0.000022036687],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99784386,0.000041333235,0.0006369427,0.00043270452,0.00064970856,0.00039543185],"domain_scores_gemma":[0.9982811,0.0005118785,0.0001887888,0.00058776134,0.00027089834,0.0001595797],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012117794,0.00023323181,0.000629437,0.0002446212,0.000024257233,0.000008813393,0.00031996038,0.00034766505,0.000015319085],"category_scores_gemma":[0.00063723914,0.00023549558,0.00019340892,0.00074157625,0.00012767653,0.00016518896,0.000068549205,0.00041659042,2.4226128e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022850488,0.00011964164,0.000055750676,0.00025505509,0.0001915286,4.20466e-7,0.00014827623,0.30139884,0.6972236,0.0000031630746,8.547274e-7,0.00037434977],"study_design_scores_gemma":[0.0009964367,0.00008189351,0.0000036154076,0.00005601987,0.00006181767,8.1209356e-7,0.000043574033,0.44443175,0.5542074,0.000003182629,6.5234747e-7,0.00011285327],"about_ca_topic_score_codex":0.00003128721,"about_ca_topic_score_gemma":1.878504e-7,"teacher_disagreement_score":0.14303291,"about_ca_system_score_codex":0.0003097245,"about_ca_system_score_gemma":0.00022428516,"threshold_uncertainty_score":0.96032315},"labels":[],"label_agreement":null},{"id":"W2963736778","doi":"10.3390/catal9070618","title":"Application of Microwave in Hydrogen Production from Methane Dry Reforming: Comparison Between the Conventional and Microwave-Assisted Catalytic Reforming on Improving the Energy Efficiency","year":2019,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":39,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University; University of New Brunswick","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Carbon dioxide reforming; Catalysis; Methane; Hydrogen; Microwave; Selectivity; Hydrogen production; Methane reformer; Materials science; Syngas; Steam reforming; Chemical engineering; Energy carrier; Chemistry; Organic chemistry","score_opus":0.012849041572152756,"score_gpt":0.23897825849358986,"score_spread":0.22612921692143712,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2963736778","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970128,0.00074780505,0.0011696764,0.000115736984,0.00014796955,0.000506981,0.000025535574,0.000049796454,0.00022373056],"genre_scores_gemma":[0.998883,0.000008102988,0.00007875117,0.000017343948,0.00016393304,0.000061257524,0.0005739325,0.00004603681,0.00016765104],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99773663,0.000061632774,0.0008177996,0.0005900441,0.00041257314,0.0003813266],"domain_scores_gemma":[0.9981548,0.00030355153,0.00050492655,0.0008846637,0.00007794616,0.000074114185],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008346203,0.0002925181,0.0005116005,0.0002114492,0.00010378722,0.00001392745,0.0004785809,0.00016988772,0.000002521756],"category_scores_gemma":[0.00018071367,0.00019134402,0.00014848092,0.0005858328,0.0001479904,0.00020286193,0.00022139376,0.0004072278,0.000021604039],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004387268,0.000051425395,0.004862243,0.00010138964,0.00008067659,9.1897914e-7,0.00077827316,0.00015666794,0.9404314,0.00015772777,0.0000013553494,0.053334042],"study_design_scores_gemma":[0.0005601003,0.000035044763,0.0043409835,0.00014091883,0.0001125723,0.000015622436,0.00061995984,0.0065464852,0.9871023,0.00009085522,0.00019587747,0.00023925804],"about_ca_topic_score_codex":0.003248403,"about_ca_topic_score_gemma":0.00025781422,"teacher_disagreement_score":0.053094786,"about_ca_system_score_codex":0.00038308388,"about_ca_system_score_gemma":0.0000581193,"threshold_uncertainty_score":0.78027827},"labels":[],"label_agreement":null},{"id":"W2965607392","doi":"10.1002/cjce.23607","title":"Effect of hydrogen addition on formation of hydrogen and carbon from methane decomposition over Ni/Al<sub>2</sub>O<sub>3</sub>","year":2019,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China","keywords":"Hydrogen; Methane; Decomposition; Carbon fibers; Chemistry; Hydrogen production; Inorganic chemistry; Catalysis; Cryo-adsorption; Chemical engineering; Materials science; Hydrogen storage; Organic chemistry; Composite number","score_opus":0.0035265663807164515,"score_gpt":0.1918205037338595,"score_spread":0.18829393735314306,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2965607392","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99902475,0.00034576893,0.00009137842,0.00004547004,0.0001554398,0.0002083088,0.00006415769,0.000020527204,0.000044210872],"genre_scores_gemma":[0.9996485,0.000013107057,0.0000409618,0.000018619661,0.00014698369,0.000005923762,0.000069530615,0.000055783836,6.055265e-7],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983537,0.000042696654,0.0006735885,0.00016794121,0.00040156906,0.00036045664],"domain_scores_gemma":[0.99852127,0.00039959338,0.00037467928,0.00026787844,0.00008372606,0.00035283336],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00056748866,0.00028025347,0.0005851334,0.00032585472,0.000023614137,0.00001244101,0.00024131188,0.0001971205,0.000009414838],"category_scores_gemma":[0.0002592942,0.00023407949,0.00022155323,0.00025547028,0.00004633324,0.00025008974,0.000033192613,0.0005348599,0.0000037367436],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009583921,0.0000073659025,0.00003775434,0.00018505068,0.00013249443,0.000009415749,0.00016250167,0.011139581,0.98570293,0.000019910012,0.000005731652,0.0025014451],"study_design_scores_gemma":[0.0008995979,0.00014714082,0.00004117295,0.0005961129,0.00015784115,0.000107033135,0.0000056775534,0.043918155,0.9538597,0.000042953474,0.000017237506,0.00020740152],"about_ca_topic_score_codex":0.00058195676,"about_ca_topic_score_gemma":0.000065154134,"teacher_disagreement_score":0.032778572,"about_ca_system_score_codex":0.00048735138,"about_ca_system_score_gemma":0.00007702921,"threshold_uncertainty_score":0.9545485},"labels":[],"label_agreement":null},{"id":"W2967050251","doi":"10.1016/j.cattod.2019.08.014","title":"Interaction effects between CuO-ZnO-ZrO2 methanol phase and zeolite surface affecting stability of hybrid systems during one-step CO2 hydrogenation to DME","year":2019,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":66,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Mount Allison University; Magyar Tudományos Akadémia; Consiglio Nazionale delle Ricerche; Hawaii Academy of Science","keywords":"Catalysis; Zeolite; Selectivity; Methanol; Metal; Chemical engineering; Phase (matter); Materials science; Drop (telecommunication); Inorganic chemistry; Chemistry; Organic chemistry; Metallurgy","score_opus":0.013394942864583027,"score_gpt":0.2649306000002378,"score_spread":0.2515356571356548,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2967050251","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957173,0.0003235939,0.0023120465,0.000016748356,0.00030967218,0.0009222164,0.000055168144,0.00016836423,0.00017489704],"genre_scores_gemma":[0.9992276,0.0000066809757,0.00018745284,0.0000030983633,0.0001292293,0.000029583027,0.00022903491,0.00006695616,0.00012038684],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99754524,0.00013343917,0.0007401029,0.0006608276,0.0004723405,0.0004480265],"domain_scores_gemma":[0.9977586,0.000752113,0.00036398307,0.00073680363,0.0001477579,0.00024071212],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010367426,0.00033978638,0.00093133183,0.00030563018,0.00007356897,0.00003885276,0.00022497594,0.00011390916,0.000022654594],"category_scores_gemma":[0.00063470745,0.00034511066,0.00022198212,0.00059593335,0.000031255007,0.0005528669,0.0002306953,0.0003203271,0.00006149209],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000059110855,0.00008129473,0.005397055,0.0017758367,0.00035438722,0.0000038282624,0.0006856945,0.002451273,0.98726374,0.000009303232,9.844938e-7,0.0019174812],"study_design_scores_gemma":[0.0012243469,0.000081097605,0.00046288752,0.0004169705,0.00032316637,0.000018426805,0.00025915023,0.012727277,0.98405135,0.0000030784647,0.00008403683,0.00034820253],"about_ca_topic_score_codex":0.000552262,"about_ca_topic_score_gemma":0.000009751387,"teacher_disagreement_score":0.010276005,"about_ca_system_score_codex":0.00052360917,"about_ca_system_score_gemma":0.0000204029,"threshold_uncertainty_score":0.9999001},"labels":[],"label_agreement":null},{"id":"W2971685565","doi":"10.1016/j.ijhydene.2019.08.068","title":"Highly-efficient hydroxyapatite-supported nickel catalysts for dry reforming of methane","year":2019,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":58,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Association Nationale de la Recherche et de la Technologie","keywords":"Catalysis; Nickel; Methane; Carbon dioxide reforming; Materials science; Selectivity; Chemical engineering; Steam reforming; Chemistry; Inorganic chemistry; Syngas; Hydrogen production; Metallurgy; Organic chemistry","score_opus":0.009401881433044407,"score_gpt":0.2513330075220541,"score_spread":0.2419311260890097,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2971685565","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99261266,0.00040069365,0.0047932165,0.00010012054,0.0010910105,0.00009112615,0.000050648174,0.000024363186,0.000836159],"genre_scores_gemma":[0.99723744,0.000029736999,0.0010591263,0.00004218722,0.0003575273,0.0000074458217,0.00008274989,0.00005174469,0.0011320348],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974622,0.000020666746,0.0011402342,0.00020680162,0.00087792997,0.0002921371],"domain_scores_gemma":[0.99779063,0.00019457295,0.0009611593,0.0002671351,0.0006449601,0.00014153613],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005444688,0.00021495466,0.000514747,0.0005401898,0.000014675993,0.000009115179,0.0007707724,0.00012126617,0.00007145561],"category_scores_gemma":[0.0002466236,0.0001816526,0.00052061654,0.0002011954,0.00003506612,0.00029165536,0.00013386409,0.00018055488,0.00001242248],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021448392,0.00012954556,0.00021580682,0.000050745446,0.00079961785,0.000035721492,0.00020761554,0.022527087,0.96677643,0.0021551694,0.000018796552,0.006868967],"study_design_scores_gemma":[0.0014465132,0.000106096464,0.000010498343,0.00015569352,0.00007612104,0.00021165688,0.00008223053,0.02972416,0.95894843,0.000202952,0.008843825,0.0001918076],"about_ca_topic_score_codex":0.00029123874,"about_ca_topic_score_gemma":0.000016517148,"teacher_disagreement_score":0.008825028,"about_ca_system_score_codex":0.00034591352,"about_ca_system_score_gemma":0.00012824796,"threshold_uncertainty_score":0.7407578},"labels":[],"label_agreement":null},{"id":"W2984220203","doi":"10.3390/catal9110922","title":"Atomic Layer Deposition ZnO Over-Coated Cu/SiO2 Catalysts for Methanol Synthesis from CO2 Hydrogenation","year":2019,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; China Scholarship Council","keywords":"Catalysis; XANES; Methanol; Chemisorption; Atomic layer deposition; Materials science; Adsorption; Atomic layer epitaxy; Extended X-ray absorption fine structure; Chemical engineering; Inorganic chemistry; Temperature-programmed reduction; Layer (electronics); Chemistry; Absorption spectroscopy; Nanotechnology; Spectroscopy; Physical chemistry","score_opus":0.012678001128277834,"score_gpt":0.2456031054391592,"score_spread":0.23292510431088137,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2984220203","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9947234,0.0004411321,0.001601094,0.000065433866,0.00056111946,0.0009400745,0.00033169505,0.00045316768,0.0008828773],"genre_scores_gemma":[0.9948831,0.0000136692315,0.0006957975,0.000055389948,0.00026467984,0.00030853684,0.0029927043,0.00016920798,0.0006168789],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997157,0.000047780406,0.0007259175,0.0008618061,0.0005324886,0.0006750337],"domain_scores_gemma":[0.997598,0.0006724813,0.00032602038,0.0010071512,0.00015499958,0.00024136958],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00039308835,0.00049422996,0.0007382805,0.00034817425,0.00011153479,0.000049768758,0.0005099814,0.00041062976,0.00011010798],"category_scores_gemma":[0.0004884473,0.00048804286,0.0004608674,0.0005255164,0.000039415096,0.00060746324,0.00016254594,0.00028505494,0.00084727147],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010553524,0.0000620906,0.0005807893,0.00017723092,0.00035144654,0.000009535728,0.00023222371,0.00009202714,0.995031,0.00013311296,0.00022667782,0.0029983148],"study_design_scores_gemma":[0.0011203664,0.00002441367,0.00040167227,0.00020039314,0.00037973587,0.000025236335,0.000053648393,0.020442571,0.97577745,0.00013555626,0.0008232674,0.00061567716],"about_ca_topic_score_codex":0.0015987947,"about_ca_topic_score_gemma":0.00014638364,"teacher_disagreement_score":0.020350544,"about_ca_system_score_codex":0.0006838662,"about_ca_system_score_gemma":0.00007518151,"threshold_uncertainty_score":0.9999307},"labels":[],"label_agreement":null},{"id":"W2992313182","doi":"10.1039/c9ra08385e","title":"Oxidative steam reforming of ethanol over M<sub>x</sub>La<sub>2−x</sub>Ce<sub>1.8</sub>Ru<sub>0.2</sub>O<sub>7−δ</sub> (M = Mg, Ca) catalysts: effect of alkaline earth metal substitution and support on stability and activity","year":2019,"lang":"en","type":"article","venue":"RSC Advances","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"National Chiao Tung University; Ministry of Science and Technology, Taiwan; Ministry of Education, India; Shanghai Educational Development Foundation","keywords":"Steam reforming; Ethanol; Oxidative phosphorylation; Analytical Chemistry (journal); Chemistry; Physical chemistry; Materials science; Nuclear chemistry; Hydrogen; Hydrogen production; Environmental chemistry; Organic chemistry","score_opus":0.00750479794190155,"score_gpt":0.2420718513801569,"score_spread":0.23456705343825535,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2992313182","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99350727,0.0013175393,0.00061344384,0.000034955552,0.00067439495,0.0022464294,0.00086427666,0.00037548158,0.0003662077],"genre_scores_gemma":[0.99657375,0.0018594214,0.00008631632,0.000035719342,0.00029397465,0.000208705,0.00065974414,0.00027181322,0.000010540959],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9910656,0.0006231566,0.0020956462,0.002400814,0.0019904487,0.0018243428],"domain_scores_gemma":[0.99306846,0.002123339,0.0017646438,0.0018708874,0.00047693646,0.000695728],"candidate_categories":["metaepi_narrow"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0029708412,0.0018284705,0.0031256047,0.00087151007,0.0003466085,0.00007849593,0.0006940983,0.00096584146,0.000016351196],"category_scores_gemma":[0.0015747562,0.0016636639,0.0008536204,0.0014722823,0.0011003581,0.0034373787,0.00075248576,0.0018258245,0.00006702293],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0015126992,0.0004272312,0.0013182908,0.0027046779,0.0006453315,0.000056996596,0.0007187305,0.00054354314,0.9398171,0.00008516125,0.00000700657,0.05216325],"study_design_scores_gemma":[0.0040221955,0.0011487752,0.002285967,0.00094916235,0.00071479223,0.00015587953,0.00029712755,0.0012377293,0.98715454,0.00012068023,0.0002441417,0.0016690141],"about_ca_topic_score_codex":0.00013440524,"about_ca_topic_score_gemma":0.00059832324,"teacher_disagreement_score":0.050494235,"about_ca_system_score_codex":0.00095806835,"about_ca_system_score_gemma":0.00035299093,"threshold_uncertainty_score":0.99944603},"labels":[],"label_agreement":null},{"id":"W2995022540","doi":"10.1016/j.apcatb.2019.118535","title":"A novel synthesis of NiAl2O4 spinel from a Ni-Al mixed-metal alkoxide as a highly efficient catalyst for hydrogen production by glycerol steam reforming","year":2019,"lang":"en","type":"article","venue":"Applied Catalysis B: Environmental","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":109,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Calcination; Steam reforming; Hydrogen production; Alkoxide; Materials science; Spinel; Physisorption; Chemical engineering; Nickel; Coke; Hydrogen; X-ray photoelectron spectroscopy; Inorganic chemistry; Metallurgy; Chemistry; Organic chemistry","score_opus":0.003925551398891057,"score_gpt":0.18790364772831722,"score_spread":0.18397809632942616,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2995022540","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99606955,0.0002900389,0.0006054593,0.00005871536,0.00023077114,0.0013118136,0.0009558126,0.00013788558,0.0003399369],"genre_scores_gemma":[0.9950429,0.000020714446,0.0006330062,0.000038203838,0.00017296204,0.00060236163,0.002846807,0.00018466024,0.0004583426],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9958961,0.000017148477,0.0010855752,0.0013077225,0.00093180087,0.00076162664],"domain_scores_gemma":[0.9977568,0.00016363934,0.0005827634,0.0012445237,0.00001508621,0.0002371922],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004383166,0.0006614603,0.0010895303,0.00022887107,0.00012991209,0.000014342309,0.0006026789,0.00026917926,0.00011742449],"category_scores_gemma":[0.000099806995,0.00064240984,0.0005810458,0.00036450126,0.00016332722,0.00022479876,0.00036890406,0.00030209986,0.000372218],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002907206,0.0005668004,0.0000846172,0.00009442234,0.0008118519,0.0000016466498,0.00034882373,0.0024637522,0.98870796,0.000026595912,0.00003076022,0.0065720514],"study_design_scores_gemma":[0.0015532764,0.00006526432,0.00005454643,0.00005579053,0.00082354766,0.00003303963,0.0012054936,0.002403928,0.9915689,0.000011266431,0.0015233371,0.00070158154],"about_ca_topic_score_codex":0.0011542611,"about_ca_topic_score_gemma":0.000022241977,"teacher_disagreement_score":0.00587047,"about_ca_system_score_codex":0.00092312467,"about_ca_system_score_gemma":0.000034874196,"threshold_uncertainty_score":0.99960274},"labels":[],"label_agreement":null},{"id":"W2995359311","doi":"10.3390/catal9121069","title":"Catalytic Dry Reforming and Cracking of Ethylene for Carbon Nanofilaments and Hydrogen Production Using a Catalyst Derived from a Mining Residue","year":2019,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Space velocity; Materials science; Carbon fibers; Hydrogen; Chemical engineering; Temperature-programmed reduction; Thermogravimetric analysis; Scanning electron microscope; Syngas; Fluid catalytic cracking; Chemistry; Nuclear chemistry; Organic chemistry; Composite material","score_opus":0.01673957353829507,"score_gpt":0.24734901491269276,"score_spread":0.2306094413743977,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2995359311","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99730605,0.0014976438,0.00006707747,0.000020029189,0.00021078838,0.00067663257,0.00004941851,0.00008158292,0.00009080282],"genre_scores_gemma":[0.99763906,0.000021034646,0.0016106867,0.0000069806115,0.0001603375,0.0000366575,0.0002813669,0.000098284334,0.00014558651],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997785,0.000022941273,0.0006521357,0.0007593982,0.0003029744,0.0004775623],"domain_scores_gemma":[0.99856883,0.00016615631,0.00038569423,0.0006150374,0.000109940425,0.00015435954],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00043537698,0.00035791085,0.000686543,0.00028477935,0.000098887576,0.000019408399,0.00019133149,0.00020855908,0.000001746583],"category_scores_gemma":[0.00038954426,0.00035516272,0.00011147435,0.00030800604,0.000095948904,0.000407653,0.00026384092,0.0001753603,0.0000018303921],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007782536,0.000019172592,0.007542412,0.0005796267,0.00019011484,0.000004842339,0.0023300448,0.00015760913,0.986078,0.0000051011516,3.852858e-7,0.0030148425],"study_design_scores_gemma":[0.0009474407,0.000037895126,0.0007627841,0.00066796306,0.00027882232,0.00004872629,0.0009153851,0.013840475,0.98205334,0.000034147044,0.000016072561,0.00039692761],"about_ca_topic_score_codex":0.003006248,"about_ca_topic_score_gemma":0.0001348755,"teacher_disagreement_score":0.013682866,"about_ca_system_score_codex":0.00026651754,"about_ca_system_score_gemma":0.00006594682,"threshold_uncertainty_score":0.99989},"labels":[],"label_agreement":null},{"id":"W3005725725","doi":"10.1016/j.jcou.2019.12.022","title":"Methanol production from water electrolysis and tri-reforming: Process design and technical-economic analysis","year":2020,"lang":"en","type":"article","venue":"Journal of CO2 Utilization","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":73,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Operating expense; Environmental science; Process engineering; Waste management; Electrolysis; Methanol; Operating cost; Environmental engineering; Engineering; Economics; Chemistry; Finance","score_opus":0.02895013240803851,"score_gpt":0.2663400529399203,"score_spread":0.2373899205318818,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3005725725","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8423674,0.0005092322,0.15647136,0.0004507549,0.000038223137,0.000112273825,0.0000016717678,0.00003244282,0.000016660579],"genre_scores_gemma":[0.9983128,0.00017788271,0.001236327,0.000022715558,0.00019178736,0.0000038791004,0.000018207335,0.000019717956,0.000016682367],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989261,0.000034868437,0.0005074576,0.00019985618,0.00018167261,0.00015002042],"domain_scores_gemma":[0.99937594,0.000047588554,0.00025842714,0.000093679235,0.00010223172,0.00012215822],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00039813138,0.0001325324,0.0003976776,0.0002587058,0.000042044343,0.000024685427,0.00009329163,0.00009216757,0.000028779128],"category_scores_gemma":[0.00023726493,0.000094170944,0.00010072173,0.00035742242,0.00002399902,0.0004550623,0.000027793638,0.00018453605,0.0000017791621],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001851245,0.000015474463,0.0005199484,0.0000424995,0.0005279727,0.0000028859808,0.0006524995,0.021049201,0.97035545,0.000009522275,0.00000586126,0.006633564],"study_design_scores_gemma":[0.0003516046,0.000074596726,0.00015421784,0.000017356739,0.0010900511,0.00004066019,0.00007986738,0.10019931,0.89759225,0.00016272697,0.000119700904,0.00011763415],"about_ca_topic_score_codex":0.000011838562,"about_ca_topic_score_gemma":0.0000031954155,"teacher_disagreement_score":0.1559454,"about_ca_system_score_codex":0.00010031896,"about_ca_system_score_gemma":0.000026645588,"threshold_uncertainty_score":0.38401797},"labels":[],"label_agreement":null},{"id":"W3012389036","doi":"10.11575/prism/32945","title":"Catalytic Upgrading of Low Cost Carbon Resources Under Methane Environment","year":2018,"lang":"en","type":"dissertation","venue":"PRISM (University of Calgary)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Methane; Catalysis; Carbon fibers; Environmental science; Waste management; Chemistry; Environmental chemistry; Business; Engineering; Materials science; Organic chemistry","score_opus":0.008123020950120763,"score_gpt":0.19761065262653585,"score_spread":0.18948763167641508,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3012389036","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9786929,0.00048524197,0.005313343,0.000014469132,0.00019377556,0.00033061896,0.0000037049695,0.000060443243,0.014905534],"genre_scores_gemma":[0.9433245,0.00039365556,0.0071388567,0.0000073770025,0.000104308994,0.0000029300963,0.0016480489,0.00018885458,0.04719144],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99847776,0.000025678246,0.0002981617,0.00038919423,0.00050625973,0.00030293796],"domain_scores_gemma":[0.9987663,0.00008016638,0.00047977976,0.00048474682,0.000050179293,0.00013885232],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00019258015,0.00029549625,0.0006587397,0.00037204026,0.000051211064,0.0000029651294,0.00048238126,0.00041497615,0.00013029308],"category_scores_gemma":[0.000042564436,0.0003631027,0.0002870138,0.00017600635,0.00013621885,0.00009777833,0.00012552267,0.00037401935,0.000020719319],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010279557,0.0004940934,0.00048093157,0.007042806,0.0025514744,0.00015888934,0.03388467,0.00010908502,0.73247856,0.0007193348,0.00014903018,0.22090314],"study_design_scores_gemma":[0.0023044783,0.00015678305,0.0022077772,0.0017176748,0.0016259593,0.000014827711,0.0032119735,0.03218272,0.9474302,0.0002693736,0.007468443,0.0014098127],"about_ca_topic_score_codex":0.002970212,"about_ca_topic_score_gemma":0.000058858743,"teacher_disagreement_score":0.21949333,"about_ca_system_score_codex":0.00036637107,"about_ca_system_score_gemma":0.000061644474,"threshold_uncertainty_score":0.9998821},"labels":[],"label_agreement":null},{"id":"W3020480227","doi":"10.1002/cjce.23769","title":"Effects of metal support interaction on dry reforming of methane over Ni/<scp>Ce‐Al<sub>2</sub>O<sub>3</sub></scp>catalysts","year":2020,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Carbon dioxide reforming; Syngas; Catalysis; Methane; Thermogravimetric analysis; Nickel; Crystallite; Materials science; Temperature-programmed reduction; Methane reformer; Chemistry; Chemical engineering; Inorganic chemistry; Steam reforming; Metallurgy; Hydrogen production; Organic chemistry","score_opus":0.00796181749002618,"score_gpt":0.20690946595293389,"score_spread":0.19894764846290772,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3020480227","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99817,0.00039163852,0.00038395452,0.00013413664,0.000518533,0.00020662752,0.000024633562,0.00004935511,0.00012109423],"genre_scores_gemma":[0.99913013,0.000021415042,0.00013648451,0.000118361684,0.0004269945,0.00000876984,0.000023402608,0.00012971043,0.0000047130907],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99691904,0.000038195158,0.00124982,0.00031203034,0.0007272697,0.00075364567],"domain_scores_gemma":[0.99699676,0.0007279301,0.00067599805,0.00037816865,0.00020716785,0.0010139772],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006531769,0.00049098703,0.0010421079,0.00050119753,0.000042599248,0.00002216621,0.00068921794,0.00027074266,0.000007707083],"category_scores_gemma":[0.0029207517,0.0004123052,0.00061338505,0.00074411,0.00010767654,0.0004378875,0.00010181161,0.0014590515,0.000012758868],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000041790125,0.000024450377,0.000019849904,0.00058500504,0.0004473631,0.00012551087,0.00078985514,0.004752414,0.9900081,0.00006189513,0.000079472986,0.0030642904],"study_design_scores_gemma":[0.0008672467,0.00014252367,0.000049101123,0.00060263154,0.00030918964,0.00020013325,0.000063779196,0.004449862,0.99272734,0.000018376617,0.0003571483,0.00021269631],"about_ca_topic_score_codex":0.0003727591,"about_ca_topic_score_gemma":0.000059191272,"teacher_disagreement_score":0.002851594,"about_ca_system_score_codex":0.0007161264,"about_ca_system_score_gemma":0.00034206331,"threshold_uncertainty_score":0.99983287},"labels":[],"label_agreement":null},{"id":"W3020932224","doi":"10.1002/cjce.23775","title":"Microreactor technology for synthesis of ethyl methyl oxalate from diethyl oxalate with methanol and its kinectics","year":2020,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Fundamental Research Funds for the Central Universities; National Natural Science Foundation of China","keywords":"Oxalate; Microreactor; Transesterification; Methanol; Chemistry; Catalysis; Selectivity; Nuclear chemistry; Inorganic chemistry; Organic chemistry","score_opus":0.012450030519685192,"score_gpt":0.1989399193765351,"score_spread":0.18648988885684992,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3020932224","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99356353,0.0015977336,0.0022733493,0.002151164,0.00009260426,0.0001777966,0.00008126526,0.00004055095,0.000022008307],"genre_scores_gemma":[0.9942567,0.000013091081,0.005398842,0.00004003726,0.00019332931,0.000010730477,0.0000036025317,0.000079191246,0.0000044815492],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986157,0.000011048296,0.00054737413,0.00019587061,0.00019860701,0.00043140375],"domain_scores_gemma":[0.9981902,0.0006004229,0.0002670576,0.00019582931,0.0002032586,0.00054323475],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00027618237,0.00027113198,0.0006426345,0.00022677769,0.000038143942,0.000018103428,0.00046960538,0.00023833352,0.000013260774],"category_scores_gemma":[0.0023394108,0.00019674667,0.00015870211,0.00043386666,0.000087239336,0.00012226985,0.00004794697,0.00070359523,0.0000010939443],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004970539,0.0000041004296,0.000029834253,0.0001512373,0.0003440656,0.000021336671,0.00037107326,0.001610526,0.99606055,0.00023248035,0.0000062461377,0.0011188396],"study_design_scores_gemma":[0.0004741085,0.00005838214,0.000012451445,0.00023022025,0.00027869115,0.0000869332,0.000035149544,0.015680173,0.9822719,0.00009315097,0.0005509752,0.0002278477],"about_ca_topic_score_codex":0.00044788665,"about_ca_topic_score_gemma":0.000034722525,"teacher_disagreement_score":0.0140696475,"about_ca_system_score_codex":0.00015948422,"about_ca_system_score_gemma":0.00017754978,"threshold_uncertainty_score":0.8023096},"labels":[],"label_agreement":null},{"id":"W3023481340","doi":"10.1021/acs.energyfuels.0c01275","title":"Preface to the PetroPhase 2019 Special Issue","year":2020,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"University of Alberta","funders":"","keywords":"Computer science","score_opus":0.01077931018639359,"score_gpt":0.22897826231076915,"score_spread":0.21819895212437557,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3023481340","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.83241767,0.0015108555,0.016767517,0.025927434,0.003023511,0.00042872046,0.000107451,0.00091356086,0.11890327],"genre_scores_gemma":[0.9268635,0.000046529258,0.0007540007,0.003590614,0.0286034,0.000043265874,0.00005857077,0.00012557,0.039914533],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.99898046,0.000015035364,0.00019623066,0.00025961257,0.00024827378,0.00030035982],"domain_scores_gemma":[0.99934494,0.000047111855,0.00003616828,0.000319259,0.000023593591,0.0002289101],"candidate_categories":["insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00006956803,0.00016069926,0.00018821821,0.000032874013,0.000053409618,0.000019432913,0.00038047813,0.000059493683,0.0011038315],"category_scores_gemma":[0.00016543332,0.00011564801,0.000108317996,0.0002952447,0.000015675732,0.0000874602,0.00018644173,0.00016523483,0.0010212939],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000054670567,0.000021300535,0.000005237399,0.000020833699,0.00005441235,0.00003153124,0.0009888045,0.0022363022,0.933289,0.002274212,0.02952627,0.03149743],"study_design_scores_gemma":[0.000125768,0.000022489614,0.0000044723965,0.000005583497,0.000009389275,0.0000035980393,0.000028964976,0.0001501995,0.45192546,0.000012825272,0.5476149,0.00009638609],"about_ca_topic_score_codex":0.00016156565,"about_ca_topic_score_gemma":0.00002107384,"teacher_disagreement_score":0.5180886,"about_ca_system_score_codex":0.000064445594,"about_ca_system_score_gemma":0.000018602354,"threshold_uncertainty_score":0.99980927},"labels":[],"label_agreement":null},{"id":"W3025264384","doi":"10.11575/prism/37848","title":"Process Simulation of Methanol Production from Water Electrolysis and Tri-Reforming","year":2020,"lang":"en","type":"dissertation","venue":"PRISM (University of Calgary)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Electrolysis; Process engineering; Environmental science; Process (computing); Production (economics); Methanol; Hydrogen production; Process simulation; Electrolysis of water; Waste management; Engineering; Computer science; Chemistry; Economics; Catalysis; Operating system; Microeconomics","score_opus":0.0075945447567808905,"score_gpt":0.21193086644145928,"score_spread":0.20433632168467838,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3025264384","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98389864,0.00026337008,0.014707735,0.00004252413,0.000097335105,0.00026095353,0.0000015714184,0.00007000072,0.0006578531],"genre_scores_gemma":[0.99581075,0.00006231818,0.0012323974,0.0000017711436,0.00003933749,9.76013e-7,0.001166564,0.00004048348,0.0016454022],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99882907,0.000020064957,0.00025962753,0.00037363401,0.00033224994,0.00018536285],"domain_scores_gemma":[0.99926186,0.000041280025,0.00029825352,0.00019127592,0.00013335742,0.0000739944],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010314095,0.00021331052,0.00054851064,0.00025738662,0.00005989989,0.0000029166597,0.00018530765,0.0002953449,0.000054936892],"category_scores_gemma":[0.00009815689,0.00021391355,0.00016382836,0.000199707,0.000031491814,0.0003035032,0.000044908043,0.0003195979,0.0000043694977],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003561249,0.000031684474,0.000039807623,0.00094134675,0.00034090597,0.000005345401,0.010048494,0.00020606625,0.90416974,0.000010321631,0.0000014443636,0.08384869],"study_design_scores_gemma":[0.00042245816,0.000035537178,0.00014021428,0.00015018215,0.00054469565,8.0203273e-7,0.00046873323,0.09987406,0.89773226,0.00016090873,0.00023425091,0.00023591006],"about_ca_topic_score_codex":0.00068552716,"about_ca_topic_score_gemma":0.000022527416,"teacher_disagreement_score":0.09966799,"about_ca_system_score_codex":0.00008664455,"about_ca_system_score_gemma":0.00003830855,"threshold_uncertainty_score":0.8723141},"labels":[],"label_agreement":null},{"id":"W30303683","doi":"10.17660/actahortic.2008.797.38","title":"TOWARDS A PLANT-BASED METHOD OF CO2 MANAGEMENT","year":2008,"lang":"en","type":"article","venue":"Acta Horticulturae","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Agriculture and Agri-Food Canada; University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Computer science; Environmental science","score_opus":0.018624029515221997,"score_gpt":0.25474703160770856,"score_spread":0.23612300209248657,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W30303683","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9810704,0.00008834721,0.007813956,0.00017297913,0.00013930057,0.0002709129,0.000038237074,0.00021679814,0.010189072],"genre_scores_gemma":[0.9814678,0.00002400598,0.017641991,0.000038868053,0.000046516354,0.000025384228,0.000071794886,0.000022539101,0.00066111214],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99883944,0.000016352265,0.00033444253,0.00021285398,0.00032247402,0.0002744655],"domain_scores_gemma":[0.9993943,0.00005300735,0.00009889233,0.00030891554,0.0000483387,0.000096533535],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001306718,0.00016851818,0.0002890385,0.00007512842,0.000042492728,0.0000038206713,0.00021671504,0.000077034565,0.000073766176],"category_scores_gemma":[0.000068342706,0.00012411523,0.00015400528,0.00024806405,0.000036127374,0.00009580142,0.00007375954,0.00013089506,0.000020224828],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006712979,0.00013993474,0.0002076758,0.0003208555,0.00031070554,0.0001407012,0.00075000135,0.00083623535,0.9868826,0.00083775655,0.00068423175,0.008822126],"study_design_scores_gemma":[0.0006121522,0.000029458522,0.002215412,0.000066016575,0.000097435564,0.00011772048,0.00014484697,0.004238926,0.985183,0.000012170243,0.0070432695,0.00023956553],"about_ca_topic_score_codex":0.000121333134,"about_ca_topic_score_gemma":0.000005133252,"teacher_disagreement_score":0.009828036,"about_ca_system_score_codex":0.00008561954,"about_ca_system_score_gemma":0.000015762227,"threshold_uncertainty_score":0.50612724},"labels":[],"label_agreement":null},{"id":"W3036972046","doi":"10.1002/cjce.23828","title":"<scp>CO<sub>2</sub></scp> conversion through combined steam and <scp>CO<sub>2</sub></scp> reforming of methane reactions over Ni and Co catalysts","year":2020,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"GreenField Specialty Alcolhols (Canada); Canadian Light Source (Canada); University of Saskatchewan","funders":"","keywords":"Steam reforming; Bimetallic strip; Catalysis; Syngas; Methane reformer; Chemistry; Methane; Water-gas shift reaction; Carbon dioxide reforming; Hydrogen production; Inorganic chemistry; Nuclear chemistry; Organic chemistry","score_opus":0.012116807145872781,"score_gpt":0.2160443808151204,"score_spread":0.2039275736692476,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3036972046","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9971111,0.001481034,0.00028236568,0.00019130748,0.00024039033,0.000244909,0.000080700825,0.0000798559,0.0002883675],"genre_scores_gemma":[0.99893177,0.0001613765,0.0001903304,0.00011356444,0.00037816362,0.0000080923055,0.000056472665,0.0001379032,0.00002230519],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968465,0.000043209864,0.0011403695,0.00041643906,0.00063469715,0.0009187936],"domain_scores_gemma":[0.99651676,0.00089511817,0.00056462054,0.00041545226,0.00019368735,0.0014143444],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00069245737,0.0005639449,0.0010072148,0.00036073397,0.00014018748,0.00006175829,0.0005429805,0.000397137,0.000004754147],"category_scores_gemma":[0.0023864198,0.00049976894,0.0003084617,0.0006366824,0.00025780432,0.0006742964,0.00011325503,0.0015313519,0.000008803104],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000014440322,0.000016112957,0.00013045938,0.0004575851,0.00032112957,0.00008748749,0.0019461754,0.00086985,0.9950679,0.00007561065,0.0004781948,0.0005350459],"study_design_scores_gemma":[0.0014152853,0.000098317316,0.00009421675,0.00039246667,0.00024528668,0.00061546045,0.00045284443,0.0042652464,0.9892866,0.00004673963,0.0029086887,0.00017886076],"about_ca_topic_score_codex":0.0008175904,"about_ca_topic_score_gemma":0.00006542463,"teacher_disagreement_score":0.005781322,"about_ca_system_score_codex":0.0005945987,"about_ca_system_score_gemma":0.00032372162,"threshold_uncertainty_score":0.99974537},"labels":[],"label_agreement":null},{"id":"W3046640427","doi":"10.1016/j.ijhydene.2020.06.142","title":"Improvements in hydrogen production from methane dry reforming on filament-shaped mesoporous alumina-supported cobalt nanocatalyst","year":2020,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":26,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Cobalt; Carbon dioxide reforming; Catalysis; Methane; Fischer–Tropsch process; Chemical engineering; Mesoporous material; Materials science; Crystallite; Amorphous solid; Hydrogen production; Syngas; Selectivity; Chemistry; Metallurgy; Organic chemistry","score_opus":0.014971602069692747,"score_gpt":0.2504857192344803,"score_spread":0.23551411716478757,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3046640427","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.997055,0.0003609756,0.00036921786,0.00092368084,0.0007603785,0.00009487791,0.000046273657,0.000052117968,0.00033747574],"genre_scores_gemma":[0.99747556,0.000084410036,0.00030234092,0.0004556435,0.0011292087,0.000012466356,0.00024342844,0.00006567496,0.00023128101],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.996735,0.000052152984,0.0012487345,0.00041361098,0.0011902783,0.00036023746],"domain_scores_gemma":[0.99838006,0.000066200926,0.0008062506,0.00023772754,0.00024868757,0.00026106078],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00038092947,0.0003194867,0.00051824667,0.00040097468,0.000029353694,0.000020241048,0.0008001102,0.00013908937,0.00016458637],"category_scores_gemma":[0.00045459904,0.00029085553,0.00029442713,0.00033357277,0.000037995564,0.0005201231,0.00018459084,0.00040953959,0.000027599912],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00044156038,0.00016354585,0.0003270065,0.00001227675,0.0007417882,0.0005185703,0.0004592866,0.0044926023,0.9727959,0.00008824306,0.000020873711,0.019938333],"study_design_scores_gemma":[0.0016479349,0.00015869216,0.00003528817,0.00016556762,0.0000806015,0.00012783833,0.00020671966,0.010551656,0.9825985,0.0001727165,0.0039743762,0.00028014317],"about_ca_topic_score_codex":0.0010996088,"about_ca_topic_score_gemma":0.0000906544,"teacher_disagreement_score":0.01965819,"about_ca_system_score_codex":0.0007520926,"about_ca_system_score_gemma":0.00011480463,"threshold_uncertainty_score":0.99995434},"labels":[],"label_agreement":null},{"id":"W3047893492","doi":"10.5383/swes.7.01.006","title":"Fe Supported Alumina Catalyst for Methane Decomposition: Effect of Co Coupling","year":2015,"lang":"en","type":"article","venue":"International Journal of Sustainable Water and Environmental Systems","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"King Abdulaziz City for Science and Technology","keywords":"Catalysis; Methane; Decomposition; Hydrogen; Hydrogen production; Oxidative coupling of methane; Materials science; Chemical engineering; Chemistry; Inorganic chemistry; Organic chemistry; Engineering","score_opus":0.008187079612780805,"score_gpt":0.2552076740912719,"score_spread":0.24702059447849106,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3047893492","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9960138,0.0005313165,0.002656402,0.00004625556,0.00037644373,0.0002427191,0.000031045376,0.000008184061,0.00009379339],"genre_scores_gemma":[0.99878764,0.000016293883,0.00005305876,0.000004347243,0.00025253143,0.000015229415,0.00021905988,0.000023116832,0.0006287303],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99858123,0.00002061559,0.00056517316,0.00011940616,0.00045606203,0.00025751122],"domain_scores_gemma":[0.9993408,0.00008474854,0.00023657449,0.000085616375,0.00009705031,0.00015520844],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010617529,0.00014837967,0.0003633431,0.00017710205,0.000029043471,0.000025924985,0.00020409995,0.00006680034,0.000010836068],"category_scores_gemma":[0.000043749737,0.00010378767,0.00013183705,0.000027675109,0.000053076295,0.00033425752,0.00008710032,0.000105661544,0.0000023826876],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0011205507,0.00010329438,0.0051399325,0.00051489373,0.0007929522,0.00034579524,0.0012572361,0.011444266,0.9786178,0.00015484559,0.00009028703,0.00041817265],"study_design_scores_gemma":[0.002967587,0.00041771887,0.000045755543,0.00010153002,0.00012587478,0.0011541037,0.004388233,0.0062418645,0.9807029,0.00003966066,0.0036556975,0.00015909913],"about_ca_topic_score_codex":0.00015813675,"about_ca_topic_score_gemma":2.4959087e-7,"teacher_disagreement_score":0.005202401,"about_ca_system_score_codex":0.00048341908,"about_ca_system_score_gemma":0.000016808906,"threshold_uncertainty_score":0.42323384},"labels":[],"label_agreement":null},{"id":"W3080736653","doi":"10.1002/cjce.23868","title":"Working diagrams to identify the operating range of a bubbling fluidized bed reactor for the <scp>CO<sub>2</sub></scp> methanation","year":2020,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Natural Sciences and Engineering Research Council of Canada; Consejo Nacional de Ciencia y Tecnología","keywords":"Methanation; Fluidized bed; Nuclear engineering; Fluidization; Materials science; Waste management; Environmental science; Hydrogen; Chemistry; Process engineering; Engineering","score_opus":0.027367786833683908,"score_gpt":0.25118692395390274,"score_spread":0.22381913712021884,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3080736653","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9855575,0.001116207,0.010725758,0.0017078738,0.00037319484,0.0004481508,0.000012903656,0.000035729932,0.0000227048],"genre_scores_gemma":[0.99797523,0.000009334473,0.00071322155,0.0002023822,0.0009745343,0.00003409816,0.0000059229556,0.000082149585,0.0000031034238],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997963,0.00003258963,0.0008039096,0.00018721673,0.00044913407,0.0005641325],"domain_scores_gemma":[0.9965626,0.002087147,0.00028704724,0.00029455,0.000225007,0.000543626],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0014637931,0.00027010636,0.00046792976,0.00015430863,0.00014907126,0.00010102385,0.0009450825,0.00013397218,0.00000411434],"category_scores_gemma":[0.007706958,0.00016415076,0.00037925693,0.0006991074,0.000058653695,0.00016766395,0.00006286336,0.00080743874,0.0000030550284],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000008339203,0.0000030988672,0.000038692455,0.00006693827,0.00018186624,0.0000061421756,0.002588113,0.011202051,0.9836964,0.00013083497,0.0000991797,0.0019783478],"study_design_scores_gemma":[0.00049526384,0.000022641212,0.00001717474,0.00021735465,0.00015494417,0.000044814282,0.00021616856,0.034221996,0.96333516,0.00002004477,0.0011605574,0.00009387],"about_ca_topic_score_codex":0.00027753133,"about_ca_topic_score_gemma":0.000110921865,"teacher_disagreement_score":0.023019947,"about_ca_system_score_codex":0.0003219298,"about_ca_system_score_gemma":0.00019840278,"threshold_uncertainty_score":0.9226505},"labels":[],"label_agreement":null},{"id":"W3081469068","doi":"10.1039/d0cy00939c","title":"Investigating methane dry reforming on Ni and B promoted Ni surfaces: DFT assisted microkinetic analysis and addressing the coking problem","year":2020,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":42,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Alberta Hospital Edmonton; University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Cambridge Trust; Nanyang Technological University; National Research Foundation Singapore","keywords":"Carbon dioxide reforming; Methane; Catalysis; Density functional theory; Coke; Chemistry; Chemical engineering; Materials science; Metallurgy; Computational chemistry; Syngas; Organic chemistry; Engineering","score_opus":0.03373084657542447,"score_gpt":0.2721541367703415,"score_spread":0.23842329019491704,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3081469068","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99470514,0.00068697013,0.0012266566,0.0023567304,0.000034702225,0.00031028295,0.000007124747,0.00045546528,0.00021694117],"genre_scores_gemma":[0.99459285,0.00002262265,0.005060549,0.00014737839,0.00003039452,0.00003854092,0.000024237725,0.00003675556,0.000046696176],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968275,0.000046398527,0.0006453593,0.0011174426,0.00058098097,0.0007823492],"domain_scores_gemma":[0.9982686,0.00016138294,0.0004002566,0.0007421879,0.00015926862,0.00026828234],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001290504,0.00038189878,0.0007316224,0.0014771717,0.0006082939,0.00012954218,0.0009510221,0.00025174246,0.000007567294],"category_scores_gemma":[0.0021043438,0.00027580766,0.00011340639,0.01241986,0.0020128652,0.00042369193,0.00085626467,0.000783431,0.000005936645],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000047135004,0.00001363843,0.0062006745,0.00008203404,0.00020563131,0.000009429653,0.0012667136,0.00044366793,0.9608553,0.0001573203,7.339688e-7,0.03076012],"study_design_scores_gemma":[0.00035158123,0.00007193956,0.0012698108,0.00017607775,0.00086037215,0.00005962749,0.0017786443,0.062576964,0.9321256,0.00016898748,0.00011655636,0.000443786],"about_ca_topic_score_codex":0.00028648673,"about_ca_topic_score_gemma":0.000085880594,"teacher_disagreement_score":0.062133297,"about_ca_system_score_codex":0.00024048067,"about_ca_system_score_gemma":0.000107163956,"threshold_uncertainty_score":0.9999694},"labels":[],"label_agreement":null},{"id":"W3081872212","doi":"10.1039/d0se00996b","title":"The use of supercritical water for the catalyst-free oxidation of coarse aluminum for hydrogen production","year":2020,"lang":"en","type":"article","venue":"Sustainable Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":47,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Fonds de recherche du Québec – Nature et technologies; Natural Sciences and Engineering Research Council of Canada","keywords":"Supercritical fluid; Aluminium; Scrap; Catalysis; Hydrogen production; Materials science; Supercritical water oxidation; Chemical engineering; Hydrogen; Metallurgy; Chemistry; Organic chemistry; Engineering","score_opus":0.025469835233563092,"score_gpt":0.23382308920386347,"score_spread":0.20835325397030038,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3081872212","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9731756,0.0003898893,0.020602314,0.00461979,0.00016423463,0.0009007637,0.000039501807,0.00006816217,0.000039776183],"genre_scores_gemma":[0.99658084,0.000029210747,0.0003799874,0.0000526492,0.00030326843,0.0003488363,0.00014775063,0.000053671996,0.002103767],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985876,0.000020774445,0.00043415398,0.0002527582,0.00022838938,0.0004763237],"domain_scores_gemma":[0.9983524,0.0005171771,0.000035288856,0.00057955703,0.0004446658,0.000070893955],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00041030924,0.00015702179,0.00025441227,0.000045830802,0.00017123381,0.000018418199,0.0003926333,0.00008949042,0.000006546868],"category_scores_gemma":[0.0026607914,0.000089076886,0.00021087009,0.00019098053,0.00013384086,0.00032273197,0.00018979661,0.000082696555,5.3338476e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021881622,0.000026756159,0.0000045184993,0.0005674422,0.00012710955,0.0000010261267,0.00054246647,0.0031482596,0.97630745,0.017142782,0.00039230406,0.0015210602],"study_design_scores_gemma":[0.0003868337,0.000073053554,6.171684e-7,0.0000115344665,0.00013055811,0.000003638391,0.0014102889,0.005118584,0.90462667,0.0010367378,0.08709294,0.0001085262],"about_ca_topic_score_codex":0.00047973162,"about_ca_topic_score_gemma":0.000028674685,"teacher_disagreement_score":0.08670064,"about_ca_system_score_codex":0.000098649,"about_ca_system_score_gemma":0.00005506524,"threshold_uncertainty_score":0.363245},"labels":[],"label_agreement":null},{"id":"W3088649029","doi":"10.1021/acs.iecr.0c02213","title":"Intensification of the Reverse Water Gas Shift Reaction by Water-Permeable Packed-Bed Membrane Reactors","year":2020,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":33,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada; Lakehead University","keywords":"Packed bed; Water-gas shift reaction; Membrane; Chemistry; Chromatography; Environmental science; Chemical engineering; Catalysis; Organic chemistry","score_opus":0.07073097392164426,"score_gpt":0.27991256995276403,"score_spread":0.20918159603111977,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3088649029","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9968727,0.000025722104,0.000011220489,0.0020443741,0.00020287638,0.00029610386,0.000028351764,0.00016723116,0.00035139752],"genre_scores_gemma":[0.99844056,0.000011593375,0.000006090727,0.00000900506,0.00064766064,0.000035913105,0.00020390378,0.00007789128,0.0005673591],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972934,0.000046298792,0.0005597204,0.00045406225,0.0008691523,0.00077735574],"domain_scores_gemma":[0.99868405,0.00014446586,0.00006459883,0.000633592,0.00020033206,0.00027294658],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0009629028,0.0002710618,0.0003695671,0.00006640546,0.000078506724,0.000032525026,0.00061721687,0.0004504914,0.00016343301],"category_scores_gemma":[0.001615882,0.00017735374,0.0001746936,0.0005183266,0.000101198944,0.00020748445,0.0003085508,0.0017851015,0.00004887334],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000105540734,0.000027018243,0.000021758266,0.00023188358,0.000059625836,0.0000042771208,0.0006654534,0.00060344435,0.99760056,0.0000070378783,0.00046884036,0.00020454734],"study_design_scores_gemma":[0.0006287676,0.000018868803,0.0000020209538,0.00012461003,0.000025210016,0.000010165255,0.00016310094,0.0033539934,0.9752028,0.000005394654,0.020248337,0.00021672396],"about_ca_topic_score_codex":0.00036161323,"about_ca_topic_score_gemma":5.644365e-7,"teacher_disagreement_score":0.022397764,"about_ca_system_score_codex":0.00037740613,"about_ca_system_score_gemma":0.000054733464,"threshold_uncertainty_score":0.7755477},"labels":[],"label_agreement":null},{"id":"W3089041858","doi":"10.1016/j.jcou.2020.101272","title":"Evaluation of CO2 utilization for methanol production via tri-reforming of methane","year":2020,"lang":"en","type":"article","venue":"Journal of CO2 Utilization","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":40,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Lakehead University","keywords":"Syngas; Methanol; Pressure swing adsorption; Methane; Steam reforming; Tonne; Gas composition; Methane reformer; Environmental science; Pulp and paper industry; Hydrogen; Methanol reformer; Waste management; Hydrogen production; Chemistry; Materials science; Thermodynamics; Engineering; Organic chemistry; Physics","score_opus":0.14748380124219945,"score_gpt":0.3505667827569696,"score_spread":0.20308298151477017,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3089041858","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.68332404,0.0011198897,0.31393418,0.00021433731,0.0005061926,0.0007199512,0.000012593428,0.000032310203,0.00013650376],"genre_scores_gemma":[0.9974856,0.00009933338,0.0018885831,0.000013011895,0.00036295,0.000013080588,0.000065633016,0.000044608776,0.000027201355],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99675184,0.0001401869,0.0014048759,0.00019961121,0.0013136804,0.00018979849],"domain_scores_gemma":[0.9948337,0.0001260661,0.001735257,0.00019081938,0.0030069593,0.00010718744],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0032942866,0.00018645344,0.0005708991,0.0003538527,0.000030894826,0.0000054971683,0.00019449586,0.00015662756,0.000049989936],"category_scores_gemma":[0.005544147,0.00016664944,0.00026044573,0.00086629315,0.00003788429,0.0006611539,0.00003200569,0.000172461,0.0000011345419],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030045985,0.00007995789,0.000093005394,0.0004822136,0.00018347264,3.3339325e-7,0.0010260816,0.024989901,0.89012957,0.0001424361,0.000016539754,0.08255606],"study_design_scores_gemma":[0.0013833246,0.00023209935,0.00006717854,0.0001769251,0.0007271631,0.000022714252,0.0002803142,0.19072905,0.8054816,0.00037880056,0.00040383093,0.00011695503],"about_ca_topic_score_codex":0.000011188009,"about_ca_topic_score_gemma":0.0000041508733,"teacher_disagreement_score":0.31416157,"about_ca_system_score_codex":0.0002571751,"about_ca_system_score_gemma":0.00021909621,"threshold_uncertainty_score":0.6795767},"labels":[],"label_agreement":null},{"id":"W3095575079","doi":"10.1515/cppm-2020-0038","title":"Carbon dioxide utilization in methanol synthesis plant: process modeling","year":2020,"lang":"en","type":"article","venue":"Chemical Product and Process Modeling","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia, Okanagan Campus; University of British Columbia","funders":"","keywords":"Methanol; Inert gas; Inert; Raw material; Carbon dioxide; Syngas; Hydrogen; Methanol reformer; Separator (oil production); Natural gas; Chemistry; Chemical engineering; Hydrogen production; Materials science; Waste management; Organic chemistry; Thermodynamics; Steam reforming; Engineering","score_opus":0.05301573341755665,"score_gpt":0.2709444923614264,"score_spread":0.21792875894386976,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3095575079","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98939866,0.0016722932,0.007479527,0.00039865487,0.000039806244,0.00029037325,0.000007670365,0.00027412645,0.0004388982],"genre_scores_gemma":[0.999022,0.00008380684,0.00030191033,0.000050387625,0.00032097203,0.00009244893,0.000042042182,0.00008155093,0.0000048845905],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99768406,0.000016595712,0.000599435,0.00083314214,0.0003656816,0.0005011119],"domain_scores_gemma":[0.9992999,0.000056017623,0.00008306866,0.0002170563,0.000118298565,0.00022564655],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0002890044,0.00035131045,0.00052085455,0.0001213065,0.0000499282,0.000023152832,0.00028259994,0.00017677282,0.00000634451],"category_scores_gemma":[0.0013953024,0.00033364404,0.00006504657,0.00058277854,0.00003056941,0.00033885217,0.00010072372,0.0005253106,0.0000020569046],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013256774,0.00003585294,0.00011501633,0.0018435046,0.000028276325,0.0000062962235,0.0029233969,0.2809621,0.7103142,0.000020191283,2.3742723e-7,0.0036183116],"study_design_scores_gemma":[0.00015502104,0.0000036330441,8.39286e-8,0.00016724924,0.000029565912,0.0000075449866,0.00019178052,0.52263457,0.47628108,0.00029907818,0.0000018073627,0.00022859333],"about_ca_topic_score_codex":0.00005435474,"about_ca_topic_score_gemma":0.0000023942782,"teacher_disagreement_score":0.24167246,"about_ca_system_score_codex":0.00007398156,"about_ca_system_score_gemma":0.000057726338,"threshold_uncertainty_score":0.99991155},"labels":[],"label_agreement":null},{"id":"W3096464077","doi":"10.1039/d0gc03115a","title":"Continuous reactor for renewable methanol","year":2020,"lang":"en","type":"article","venue":"Green Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto; Toronto Public Health","funders":"Connaught Fund; University of Toronto; Ontario Ministry of Research and Innovation; Imperial Oil Limited; Natural Sciences and Engineering Research Council of Canada; Ontario Ministry of Research, Innovation and Science","keywords":"Renewable energy; Methanol; Fossil fuel; Waste management; Renewable resource; Natural resource economics; Renewable fuels; Carbon fibers; Environmental science; Business; Chemistry; Economics; Materials science; Engineering; Organic chemistry","score_opus":0.022104695625211144,"score_gpt":0.2377664015753174,"score_spread":0.21566170595010625,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3096464077","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9254321,0.0008669823,0.019265553,0.0032925694,0.00026541535,0.0008199407,0.0003553897,0.001735119,0.047966965],"genre_scores_gemma":[0.98309857,0.000006666684,0.0030353428,0.0002829889,0.0014256581,0.00010413363,0.00023369721,0.0001219629,0.011690968],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99891174,0.000002965243,0.0002532629,0.00032729664,0.0001624174,0.00034230447],"domain_scores_gemma":[0.9992798,0.000084502724,0.00008174403,0.0002749667,0.0000529594,0.00022604415],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00008923228,0.00018380943,0.0002995825,0.0000103210505,0.000027912849,0.000010263022,0.00027705703,0.00015627123,0.00018639286],"category_scores_gemma":[0.00039132455,0.00018159524,0.00017524186,0.00014295644,0.00002256068,0.00007964622,0.00008935073,0.00017352687,0.000035083074],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003522711,0.000009590266,0.000033864482,0.00037839048,0.000051445113,0.000006536153,0.00011451742,0.000021361153,0.9965909,0.0000063958437,0.00055581174,0.0021959268],"study_design_scores_gemma":[0.00053962704,0.0000116951815,0.0000010218911,0.000024059304,0.00004043962,0.000012245312,0.00006482142,0.0026605614,0.9332407,0.000042585467,0.06314298,0.00021924273],"about_ca_topic_score_codex":0.00016805164,"about_ca_topic_score_gemma":0.0000018144978,"teacher_disagreement_score":0.06335021,"about_ca_system_score_codex":0.0000706629,"about_ca_system_score_gemma":0.000029266388,"threshold_uncertainty_score":0.7405239},"labels":[],"label_agreement":null},{"id":"W3097210817","doi":"10.1016/j.seppur.2020.117945","title":"Design of hydrogen separatinwg Nb-Ti-Fe membranes with high permeability and low cost","year":2020,"lang":"en","type":"article","venue":"Separation and Purification Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut National de la Recherche Scientifique","funders":"","keywords":"Materials science; Alloy; CALPHAD; Eutectic system; Hydrogen; Liquidus; Microstructure; Permeation; Hydrogen embrittlement; Phase diagram; Chemical engineering; Ternary operation; Metallurgy; Permeability (electromagnetism); Phase (matter); Membrane; Thermodynamics; Corrosion; Chemistry","score_opus":0.01727003795814846,"score_gpt":0.24990059402427145,"score_spread":0.23263055606612298,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3097210817","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95895755,0.00034563814,0.03806507,0.0017355023,0.000013733053,0.0005270317,0.000011227093,0.00023683051,0.000107403335],"genre_scores_gemma":[0.9978333,0.00008094574,0.001843365,0.00004174694,0.00001905889,0.0000688647,0.000044488752,0.0000150950855,0.000053146105],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991336,0.000027544502,0.00028787035,0.000302135,0.00011410855,0.0001347601],"domain_scores_gemma":[0.9994273,0.000057683425,0.00013671424,0.00022379233,0.00008333955,0.0000711793],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014121467,0.00013653157,0.00024713838,0.00010630675,0.000055226654,0.000008955904,0.000099588084,0.00017932327,0.00002617266],"category_scores_gemma":[0.0001190396,0.00011806633,0.000017167733,0.00036931742,0.00017675644,0.00013341646,0.000029300465,0.00014328686,0.000008781851],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009674278,0.000027305337,0.00044031764,0.00016648273,0.00003313946,9.984203e-7,0.0005119857,0.0014148512,0.9876923,0.0042138766,0.0000089989135,0.0053930096],"study_design_scores_gemma":[0.000523501,0.0001018211,0.00012445958,0.000014392207,0.000030506028,0.00002426663,0.00016313353,0.04878512,0.94908744,0.00030235236,0.0006967879,0.00014620436],"about_ca_topic_score_codex":0.000013757535,"about_ca_topic_score_gemma":0.0000029229216,"teacher_disagreement_score":0.04737027,"about_ca_system_score_codex":0.000022554557,"about_ca_system_score_gemma":0.00002873416,"threshold_uncertainty_score":0.48146054},"labels":[],"label_agreement":null},{"id":"W3097355211","doi":"10.1021/acsomega.0c03251","title":"Numerical Investigation of the Effects of Coke on Transport Properties in an Oxidative Fuel Cell Reformer","year":2020,"lang":"en","type":"article","venue":"ACS Omega","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"Natural Sciences and Engineering Research Council of Canada; Government of Canada","keywords":"Coke; Catalysis; Combustion; Chemical engineering; Steam reforming; Materials science; Hydrogen; Heat transfer; Porosity; Oxide; Chemistry; Packed bed; Mass transfer; Hydrogen production; Metallurgy; Composite material; Organic chemistry; Chromatography; Thermodynamics","score_opus":0.016998861902968038,"score_gpt":0.2122061007106154,"score_spread":0.19520723880764737,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3097355211","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99914914,0.00006906764,0.000017664954,0.00010317147,0.0000357415,0.00019665239,0.0000027510164,0.000021339047,0.00040445474],"genre_scores_gemma":[0.9997712,0.000005067903,0.000042376643,0.00008388659,0.000021429307,0.0000138621335,0.000008703174,0.000017848148,0.000035635905],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99926746,0.000023789975,0.00024865754,0.00013587822,0.00020400659,0.000120184224],"domain_scores_gemma":[0.99960846,0.000047988557,0.0000899719,0.00017540112,0.000028579041,0.000049581522],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00006432776,0.00010211415,0.00021010166,0.0000382861,0.000009533654,0.0000012377224,0.00017823715,0.00006137962,0.0000012332777],"category_scores_gemma":[0.0001368006,0.00006405502,0.00005529001,0.00031338385,0.0000570617,0.00013768021,0.000020179235,0.00018145591,0.0000024896162],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000045659253,0.000035731544,0.0046361736,0.00092594355,0.0000095369805,0.0000013445009,0.004071771,0.00040678843,0.98962593,0.000037618072,0.0000012934239,0.00020222271],"study_design_scores_gemma":[0.00035949115,0.00014143658,0.005607719,0.00014635184,0.0000144561955,3.4641002e-7,0.000092710245,0.00071080524,0.9927953,0.000021602633,0.000030510404,0.000079284866],"about_ca_topic_score_codex":0.00010920712,"about_ca_topic_score_gemma":0.000006287822,"teacher_disagreement_score":0.0039790613,"about_ca_system_score_codex":0.000044329816,"about_ca_system_score_gemma":0.000023780065,"threshold_uncertainty_score":0.2612088},"labels":[],"label_agreement":null},{"id":"W3101807566","doi":"10.1038/s41467-020-19438-w","title":"Copper-zirconia interfaces in UiO-66 enable selective catalytic hydrogenation of CO2 to methanol","year":2020,"lang":"en","type":"article","venue":"Nature Communications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":201,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Pacific Northwest National Laboratory; Argonne National Laboratory; Basic Energy Sciences; Biological and Environmental Research; Office of Science; Canadian Light Source; U.S. Department of Energy","keywords":"Catalysis; Methanol; Selectivity; Cubic zirconia; Adsorption; Copper; Metal-organic framework; Linker; Water-gas shift reaction; Nanoparticle; Metal; Chemical engineering; Materials science; Chemistry; Inorganic chemistry; Nanotechnology; Organic chemistry; Metallurgy; Ceramic","score_opus":0.022094913841652145,"score_gpt":0.2909554397862813,"score_spread":0.26886052594462917,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3101807566","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9761532,0.004993037,0.0006172077,0.00858354,0.00012042197,0.0009081002,0.00008864206,0.00026163747,0.008274201],"genre_scores_gemma":[0.9964304,0.000044695822,0.0030796598,0.00017151864,0.000021537275,0.000057834055,0.00010543666,0.000030401445,0.000058526235],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99893373,0.000057148187,0.00038041422,0.00022095237,0.00019645649,0.00021132083],"domain_scores_gemma":[0.99845904,0.00029765232,0.00011127228,0.00086319615,0.00015667897,0.00011217282],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00022516567,0.00015036472,0.00029348503,0.00019963384,0.00005221781,0.000009215681,0.0010332906,0.00022564545,0.000011186308],"category_scores_gemma":[0.0011580082,0.00015296954,0.000070859336,0.0012611055,0.00004898032,0.00017882352,0.00047669682,0.00095842587,0.00004492901],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000025916035,0.000081463484,0.00044854786,0.00007778944,0.00008139397,9.065695e-7,0.0043639923,0.001195709,0.989419,0.0030232414,0.00026664755,0.0010153977],"study_design_scores_gemma":[0.0003008644,0.00003488569,0.00009045795,0.00007855523,0.000033057568,0.000004050847,0.00028187074,0.011260467,0.98169,0.00010279255,0.005952199,0.00017080708],"about_ca_topic_score_codex":0.00023497219,"about_ca_topic_score_gemma":0.00043483256,"teacher_disagreement_score":0.020277178,"about_ca_system_score_codex":0.00025325234,"about_ca_system_score_gemma":0.000061692874,"threshold_uncertainty_score":0.6237917},"labels":[],"label_agreement":null},{"id":"W3102923747","doi":"10.1002/er.6203","title":"Using the analytical heirarchy process to select specific methanation catalysts based on their extraction impacts","year":2020,"lang":"en","type":"article","venue":"International Journal of Energy Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Methanation; Catalysis; Substitute natural gas; Methane; Industrial catalysts; Environmental science; Chemistry; Ruthenium; Biogas; Waste management; Chemical engineering; Process engineering; Catalyst support; Syngas; Organic chemistry; Engineering","score_opus":0.1616656990639605,"score_gpt":0.4377305151022665,"score_spread":0.276064816038306,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3102923747","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9014338,0.00020444678,0.08229718,0.012669198,0.0005284248,0.00017313052,0.00001916093,0.00004209981,0.0026325388],"genre_scores_gemma":[0.9980636,0.000017519355,0.00029888196,0.0002427728,0.0012823193,0.000004386655,0.000013217201,0.00003333967,0.000043966316],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9967842,0.00015964855,0.00049122743,0.00021782247,0.0020111494,0.00033593902],"domain_scores_gemma":[0.99723554,0.0006435057,0.00017264135,0.0001673896,0.0014665155,0.0003144358],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0014942781,0.00015018551,0.00021729825,0.0007057321,0.00008474334,0.000094021634,0.0008532768,0.000076975506,0.000068091314],"category_scores_gemma":[0.0015749531,0.000098554905,0.00018319611,0.0010191351,0.000050702765,0.00031077958,0.000087985,0.00078186573,0.000010834394],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0014412411,0.00014603348,0.00019617256,0.000028095794,0.00038084254,0.0001931152,0.001173704,0.1995143,0.78250575,0.0019391297,0.0004560824,0.012025537],"study_design_scores_gemma":[0.0005065553,0.00020542482,0.00009674582,0.00014635772,0.0000142842755,0.00014197646,0.00035312356,0.3041418,0.68806857,0.00017651802,0.006011706,0.00013694144],"about_ca_topic_score_codex":0.00008033835,"about_ca_topic_score_gemma":0.000011018229,"teacher_disagreement_score":0.10462749,"about_ca_system_score_codex":0.0006388103,"about_ca_system_score_gemma":0.00024817532,"threshold_uncertainty_score":0.40189525},"labels":[],"label_agreement":null},{"id":"W3110841868","doi":"10.3390/catal10121450","title":"The Effects of CeO2 and Co Doping on the Properties and the Performance of the Ni/Al2O3-MgO Catalyst for the Combined Steam and CO2 Reforming of Methane Using Ultra-Low Steam to Carbon Ratio","year":2020,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":29,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Thailand Science Research and Innovation; PTT Public Company Limited","keywords":"Catalysis; Thermogravimetric analysis; Steam reforming; Oxygen; Materials science; Dissociation (chemistry); Desorption; Adsorption; Methane; Inorganic chemistry; Temperature-programmed reduction; Chemistry; Chemical engineering; Hydrogen production; Organic chemistry","score_opus":0.017395093918990405,"score_gpt":0.2212441707751046,"score_spread":0.2038490768561142,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3110841868","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9941348,0.0029850441,0.00002594672,0.00076159515,0.00013263723,0.001858172,0.000018541285,0.000018986277,0.00006426418],"genre_scores_gemma":[0.99943477,0.00019358599,0.000012701248,0.00008373122,0.00006744086,0.00010725587,0.000005690518,0.000040850664,0.00005395712],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99829715,0.00010995601,0.0005902457,0.00028797908,0.0003966595,0.00031801988],"domain_scores_gemma":[0.9967078,0.0020155243,0.0003981763,0.00067517394,0.00012340631,0.00007989641],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011225145,0.00028675853,0.00057214213,0.000048156213,0.00032982245,0.000026974116,0.0005351644,0.00008336868,2.7992436e-7],"category_scores_gemma":[0.0015893508,0.00011035689,0.00012777143,0.00036568675,0.00065406493,0.000121411846,0.00025258842,0.00029972792,1.7258755e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00054290507,0.00001500609,0.0002772378,0.0017010946,0.0002525594,3.64849e-7,0.007447048,0.00036166332,0.98702925,0.0002502275,0.000004910726,0.0021177111],"study_design_scores_gemma":[0.0013358701,0.00016709327,0.00018272692,0.00070187123,0.0002685136,0.000015371003,0.001905729,0.022763982,0.9724407,0.000007817297,0.000057404806,0.0001529201],"about_ca_topic_score_codex":0.00042174163,"about_ca_topic_score_gemma":0.000039679046,"teacher_disagreement_score":0.02240232,"about_ca_system_score_codex":0.000062063235,"about_ca_system_score_gemma":0.000059516926,"threshold_uncertainty_score":0.4500223},"labels":[],"label_agreement":null},{"id":"W3111062068","doi":"10.1016/j.ces.2020.116364","title":"Process design and simulation study: CO2 utilization through mixed reforming of methane for methanol synthesis","year":2020,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":43,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Methanol; Methane; Steam reforming; Methanol reformer; Methane reformer; Process engineering; Syngas to gasoline plus; Volume (thermodynamics); Yield (engineering); Chemical engineering; Process simulation; Chemistry; Waste management; Catalysis; Process (computing); Materials science; Hydrogen production; Engineering; Organic chemistry; Thermodynamics; Computer science; Metallurgy","score_opus":0.06194431279471683,"score_gpt":0.31202232593582924,"score_spread":0.2500780131411124,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3111062068","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6464201,0.00006583157,0.3528421,0.000028538578,0.000043503234,0.00044464358,0.0000039115193,0.00013970552,0.000011650828],"genre_scores_gemma":[0.9792719,0.000002450124,0.020527195,0.000009247368,0.00005382713,0.00009095034,0.000003447538,0.000038429243,0.0000025651575],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99830145,0.000009312197,0.00041635308,0.0004764086,0.0004353845,0.00036110962],"domain_scores_gemma":[0.99868685,0.0006422648,0.00011867527,0.00020720338,0.00017825801,0.00016676672],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00063832273,0.00021370863,0.0003826143,0.00010338163,0.000043075648,0.000014981703,0.00036212525,0.00008535111,0.0000033386655],"category_scores_gemma":[0.0061179134,0.00019737825,0.00006078279,0.0010642109,0.00011042826,0.00053521985,0.00010768015,0.00013898904,8.3646825e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000030044432,0.00002511183,0.000010362805,0.00028659546,0.000016969207,5.184135e-7,0.0010984922,0.22121969,0.7750702,0.00005321817,1.6862008e-7,0.0021886178],"study_design_scores_gemma":[0.00019516874,0.000030537194,0.000006947726,0.000042679312,0.00003513442,0.0000015358588,0.00013153299,0.4559601,0.54344386,0.000019380404,0.000009591649,0.00012353533],"about_ca_topic_score_codex":0.0000057949455,"about_ca_topic_score_gemma":6.193083e-8,"teacher_disagreement_score":0.33285177,"about_ca_system_score_codex":0.00010982004,"about_ca_system_score_gemma":0.000054453423,"threshold_uncertainty_score":0.8048851},"labels":[],"label_agreement":null},{"id":"W3116393989","doi":"10.1016/j.arabjc.2020.102955","title":"Catalyzed-like water enhanced mechanism of CO2 conversion to methanol","year":2020,"lang":"en","type":"article","venue":"Arabian Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Nemzeti Kutatási, Fejlesztési és Innovaciós Alap; European Regional Development Fund; Innovációs és Technológiai Minisztérium; European Commission","keywords":"Chemistry; Methanol; Catalysis; Hydrogen; Chemical engineering; Aqueous solution; Carbon dioxide; Inorganic chemistry; Organic chemistry","score_opus":0.010512753428857548,"score_gpt":0.2175740674251867,"score_spread":0.20706131399632915,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3116393989","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9915269,0.000064894986,0.0068584313,0.00058991613,0.00013812426,0.000060461196,0.000008249709,0.000025089725,0.0007279104],"genre_scores_gemma":[0.998601,0.000008659944,0.0008143707,0.00011663226,0.00021149506,0.0000014544652,0.000009930009,0.00003316838,0.00020328833],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99852633,0.000010440239,0.0006225978,0.00017517821,0.00038895654,0.00027650385],"domain_scores_gemma":[0.99891925,0.000041348692,0.00024590298,0.00020965154,0.00018251754,0.00040134502],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00023076273,0.00018207352,0.00047177178,0.000045935732,0.000020693387,0.000006857644,0.00041190584,0.00011969565,0.00035399426],"category_scores_gemma":[0.00020577524,0.00014250378,0.00025373636,0.0001592687,0.000028607237,0.00015090578,0.00012259632,0.0003435164,0.000041978943],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011047871,0.000018978551,0.0000043131986,0.00027830634,0.000099758116,0.00003429476,0.0011750272,0.0001742336,0.9976775,0.000006602539,0.00004873479,0.00037176773],"study_design_scores_gemma":[0.000724222,0.000047369464,9.0673797e-7,0.00013291542,0.00007059832,0.00009502234,0.00027003704,0.00014504355,0.99742514,0.0000428127,0.0008736006,0.00017231934],"about_ca_topic_score_codex":0.0000047497297,"about_ca_topic_score_gemma":1.0746287e-7,"teacher_disagreement_score":0.0070740785,"about_ca_system_score_codex":0.0000861619,"about_ca_system_score_gemma":0.000043120144,"threshold_uncertainty_score":0.5811135},"labels":[],"label_agreement":null},{"id":"W3122597187","doi":"10.1016/j.compchemeng.2021.107234","title":"Investigation and optimization of a new hybrid natural gas reforming system for cascaded hydrogen, ammonia and methanol synthesis","year":2021,"lang":"en","type":"article","venue":"Computers & Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"Mitacs","keywords":"Ammonia production; Natural gas; Steam reforming; Ammonia; Hydrogen production; Hydrogen; Pressure swing adsorption; Chemistry; Methanol; Methane reformer; Methane; Syngas; Methanol reformer; Chemical engineering; Waste management; Process engineering; Organic chemistry; Engineering","score_opus":0.01085179398493687,"score_gpt":0.20003714692028038,"score_spread":0.1891853529353435,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3122597187","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.84814256,0.0010586323,0.1502042,0.000055445234,0.00015131476,0.00018285068,0.000007758828,0.00019240154,0.000004851661],"genre_scores_gemma":[0.88340664,0.00001606239,0.116287515,0.000008649302,0.00014155505,0.000025215812,0.000046184654,0.00005549392,0.0000126701825],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99875194,0.000008249942,0.00041914094,0.0003617874,0.00016567623,0.00029323556],"domain_scores_gemma":[0.99910766,0.00030454015,0.00010465801,0.00020368943,0.00007347125,0.00020599025],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00013887737,0.00024434092,0.00044423967,0.00011735659,0.000030913892,0.000020818497,0.0001139202,0.00010979487,8.801971e-7],"category_scores_gemma":[0.0004374863,0.0002542274,0.00010254618,0.00022497206,0.000029616313,0.00019805304,0.00015226591,0.0001803044,2.5893422e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012292791,0.0000036405513,0.0000069152547,0.0009787334,0.000091361566,0.0000079689835,0.00019036687,0.044895157,0.94751215,0.00011498837,0.0000033484487,0.00618306],"study_design_scores_gemma":[0.00027850314,0.000003955863,0.0000015509846,0.00033249884,0.00005469536,0.00016230541,0.000025593312,0.4561694,0.54280066,0.0000062192435,0.000020783431,0.00014384718],"about_ca_topic_score_codex":0.00003125032,"about_ca_topic_score_gemma":5.377718e-7,"teacher_disagreement_score":0.41127425,"about_ca_system_score_codex":0.00018139453,"about_ca_system_score_gemma":0.00003416155,"threshold_uncertainty_score":0.999991},"labels":[],"label_agreement":null},{"id":"W3129979464","doi":"","title":"Development of Technologies for RNG Utilization","year":2018,"lang":"en","type":"article","venue":"eScholarship (California Digital Library)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"University of California, Riverside; Yeungnam University; Climate Change and Emissions Management Corporation; Louisiana State University; California Energy Commission","keywords":"Syngas; Steam reforming; Methane; Methane reformer; Renewable energy; Tonne; Coke; Waste management; Methanol; Integrated gasification combined cycle; Syngas to gasoline plus; Catalysis; Environmental science; Process engineering; Chemical engineering; Chemistry; Hydrogen production; Engineering; Organic chemistry","score_opus":0.02937350378020644,"score_gpt":0.24611489316733853,"score_spread":0.21674138938713208,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3129979464","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9581059,0.0001969685,0.029469442,0.00011436822,0.00015023787,0.000480712,0.0007641787,0.0016415167,0.009076683],"genre_scores_gemma":[0.97583467,0.0000025410143,0.022982642,0.000017994234,0.00007982699,0.000041772848,0.0005320268,0.00007457425,0.00043398186],"study_design_codex":"design_other","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986513,0.000004719201,0.00050338847,0.00027946854,0.00021755687,0.00034352217],"domain_scores_gemma":[0.99934447,0.000082804116,0.00013663054,0.0002994975,0.000063777385,0.00007285113],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001269697,0.00020257996,0.00024351299,0.0001934455,0.000085047184,0.00008924059,0.00038480674,0.00017014316,0.00006838312],"category_scores_gemma":[0.0006055147,0.00018017238,0.00011270572,0.00043615684,0.0001032863,0.0014973141,0.00024878015,0.00014955508,0.00026105216],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002949648,0.00026696388,0.008701176,0.0008073754,0.00021939952,0.0000040398854,0.0002821456,0.000009508036,0.4117575,0.012454803,0.00036762597,0.56483454],"study_design_scores_gemma":[0.0002601615,0.000027507733,0.000056987035,0.00009030819,0.000008473227,0.0000029014057,0.00007446685,0.00044082457,0.8167737,0.0017701976,0.18029447,0.0001999878],"about_ca_topic_score_codex":2.8515637e-7,"about_ca_topic_score_gemma":5.116889e-7,"teacher_disagreement_score":0.5646345,"about_ca_system_score_codex":0.000047342084,"about_ca_system_score_gemma":0.0000677064,"threshold_uncertainty_score":0.73472166},"labels":[],"label_agreement":null},{"id":"W3132569453","doi":"10.1016/j.apcatb.2021.119958","title":"Development of residue coal fly ash supported nickel catalyst for H2 production via glycerol steam reforming","year":2021,"lang":"en","type":"article","venue":"Applied Catalysis B: Environmental","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":68,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada; China Scholarship Council","keywords":"Catalysis; Materials science; Physisorption; Chemisorption; Sintering; Steam reforming; Chemical engineering; Nickel; Coke; Nuclear chemistry; Metallurgy; Hydrogen production; Chemistry; Organic chemistry","score_opus":0.009835213345527645,"score_gpt":0.213577482237224,"score_spread":0.20374226889169636,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3132569453","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9940935,0.00017825564,0.0041127373,0.000034960376,0.00016437918,0.000628321,0.000089591034,0.00011753621,0.0005807557],"genre_scores_gemma":[0.98591566,0.000016165603,0.005464398,0.000021050326,0.00017672093,0.00034407873,0.00631254,0.00012457192,0.0016247885],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9964965,0.000015834517,0.0011672919,0.000946639,0.00071396,0.00065978745],"domain_scores_gemma":[0.99834144,0.00005860891,0.00041759084,0.0009524942,0.000027236274,0.0002026296],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00046604825,0.0004681629,0.0007407227,0.00019879993,0.00022758884,0.000011403322,0.00035413634,0.00023591568,0.00014797226],"category_scores_gemma":[0.000050100476,0.000487133,0.00032761725,0.00035522343,0.00012577456,0.00024364932,0.00036223923,0.00028308763,0.00011264943],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001146159,0.00027306052,0.00015592956,0.00017093187,0.0004942431,0.000007808447,0.0010264827,0.00034439683,0.97592795,0.000026371286,0.00002237467,0.02143582],"study_design_scores_gemma":[0.0010889842,0.000019999976,0.0003005483,0.000031087766,0.00036764872,0.00007159262,0.0020065522,0.0002690532,0.99057233,0.000020057509,0.0047149574,0.00053716195],"about_ca_topic_score_codex":0.00004634757,"about_ca_topic_score_gemma":0.00013329252,"teacher_disagreement_score":0.020898659,"about_ca_system_score_codex":0.00093826774,"about_ca_system_score_gemma":0.000107916174,"threshold_uncertainty_score":0.999758},"labels":[],"label_agreement":null},{"id":"W3134647224","doi":"10.3390/catal11030330","title":"Kinetics and Selectivity Study of Fischer–Tropsch Synthesis to C5+ Hydrocarbons: A Review","year":2021,"lang":"en","type":"review","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":109,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"","keywords":"Fischer–Tropsch process; Syngas; Catalysis; Gas to liquids; Selectivity; Methane; Process engineering; Chemistry; Chemical engineering; Materials science; Organic chemistry; Engineering","score_opus":0.03878829924100211,"score_gpt":0.32549624980994074,"score_spread":0.2867079505689386,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3134647224","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00071208365,0.9970862,0.00002964995,0.000012593883,0.000093709874,0.0016007223,0.000049259892,0.00008721082,0.00032856333],"genre_scores_gemma":[0.0025945487,0.9961162,0.00012612143,0.000014929937,0.000114800074,0.0005787757,0.00009215631,0.00015964749,0.00020278317],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9966763,0.00020816694,0.0012410107,0.00090518704,0.00051026634,0.00045905908],"domain_scores_gemma":[0.99699384,0.00078925985,0.0004687218,0.0013555245,0.00009925087,0.00029340337],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005430193,0.0007207318,0.004384445,0.00031680558,0.0000379116,0.000017458138,0.0005241562,0.00030689806,0.000018206501],"category_scores_gemma":[0.0037018375,0.000617706,0.00056744553,0.0016031283,0.00003484787,0.0000800407,0.0005892928,0.0006104021,0.000027450873],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000002817692,0.00041692762,0.000004773049,0.11553315,0.0011132932,0.000083866915,0.00017696824,0.000001406147,0.00066652085,0.000009044182,0.00017482246,0.8818164],"study_design_scores_gemma":[0.0002554172,0.00020957508,0.000003220815,0.24488907,0.012303007,0.00045013093,0.00008908959,0.000017725915,0.006990129,0.0000018806546,0.73319024,0.0016005452],"about_ca_topic_score_codex":0.0001429312,"about_ca_topic_score_gemma":0.000043936318,"teacher_disagreement_score":0.8802159,"about_ca_system_score_codex":0.00029446807,"about_ca_system_score_gemma":0.000110254856,"threshold_uncertainty_score":0.9996274},"labels":[],"label_agreement":null},{"id":"W3135432231","doi":"10.1002/cctc.202100073","title":"Investigating CO<sub>2</sub> Methanation on Ni and Ru: DFT Assisted Microkinetic Analysis","year":2021,"lang":"en","type":"article","venue":"ChemCatChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":47,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Cambridge Trust; University of Alberta","keywords":"Methanation; Dissociation (chemistry); Chemistry; Density functional theory; Catalysis; Ruthenium; Selectivity; Reaction mechanism; Physical chemistry; Kinetics; Photochemistry; Chemical kinetics; Inorganic chemistry; Computational chemistry; Organic chemistry","score_opus":0.017580400709939478,"score_gpt":0.254029193974857,"score_spread":0.23644879326491752,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3135432231","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99698055,0.00035676998,0.000488564,0.00025103227,0.00006714388,0.000083269326,0.000014499284,0.0001680828,0.0015900886],"genre_scores_gemma":[0.99728644,0.000028333092,0.0016729374,0.00014178282,0.00011745308,0.000022842716,0.0003822384,0.000052914747,0.0002950666],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983037,0.00003253035,0.0004152026,0.0005411118,0.00034306248,0.00036438237],"domain_scores_gemma":[0.9988219,0.00021060057,0.00015622114,0.00046886885,0.00012954495,0.00021284843],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00028833243,0.0002793324,0.00047994597,0.00023807978,0.000080641614,0.0000436872,0.0001439587,0.00019492595,0.000034037465],"category_scores_gemma":[0.0007565207,0.0002891031,0.00020155185,0.0014478277,0.0000672781,0.00011698894,0.00010448066,0.00035809985,0.000035117024],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000032810713,0.000035541256,0.00077481207,0.00010845037,0.0004164618,0.000013935939,0.00032680156,0.000064888874,0.9872341,0.00006206638,0.00004117231,0.010918502],"study_design_scores_gemma":[0.00042243733,0.0000094405505,0.0020831798,0.00006990219,0.00051076146,0.0000301914,0.00019825094,0.002972767,0.9931002,0.00007236277,0.00020702204,0.00032346262],"about_ca_topic_score_codex":0.000035852936,"about_ca_topic_score_gemma":0.000026402338,"teacher_disagreement_score":0.010595039,"about_ca_system_score_codex":0.0002200096,"about_ca_system_score_gemma":0.000050251303,"threshold_uncertainty_score":0.99995613},"labels":[],"label_agreement":null},{"id":"W3136907192","doi":"10.3390/reactions2010006","title":"Effects of Structure and Particle Size of Iron, Cobalt and Ruthenium Catalysts on Fischer–Tropsch Synthesis","year":2021,"lang":"en","type":"article","venue":"Reactions","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Fischer–Tropsch process; Particle size; Ruthenium; Cobalt; Chemical engineering; Particle (ecology); Materials science; Metal; Syngas; Crystal (programming language); Chemistry; Metallurgy; Organic chemistry; Selectivity","score_opus":0.004811226874864412,"score_gpt":0.21392107986955308,"score_spread":0.20910985299468868,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3136907192","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99914885,0.00038295827,0.000027715758,0.00007506778,0.000053703607,0.00006382254,0.00002797366,0.000024418985,0.0001954655],"genre_scores_gemma":[0.99948883,0.00005435934,0.00023317452,0.000005002152,0.000028115128,0.0000069461644,0.0000044362255,0.000015844635,0.00016331728],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99939823,0.000019687126,0.00018453298,0.00015549632,0.00011652145,0.00012551893],"domain_scores_gemma":[0.9988298,0.0007894304,0.000072386225,0.00019547615,0.00004155747,0.000071390554],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000049210157,0.00009576315,0.00022069902,0.000027342969,0.00003063523,0.0000043831865,0.000037320948,0.000073313335,0.000016444801],"category_scores_gemma":[0.0009830797,0.00008574514,0.0000480957,0.00016123183,0.00003844623,0.00006756007,0.000041318246,0.000121518024,0.0000012679501],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000011795396,0.000036968268,0.00037284647,0.00041943556,0.000056543908,0.0000046995447,0.00013931404,0.000031701893,0.9969196,0.0004431653,0.0000047110593,0.0015592655],"study_design_scores_gemma":[0.00021482623,0.000014861337,0.0041853916,0.00011530299,0.0001196863,0.00003003138,0.00007716407,0.00026429628,0.9946443,0.000048957885,0.00020619898,0.000079014506],"about_ca_topic_score_codex":0.00012318582,"about_ca_topic_score_gemma":0.000015489923,"teacher_disagreement_score":0.0038125452,"about_ca_system_score_codex":0.000030184352,"about_ca_system_score_gemma":0.00001703191,"threshold_uncertainty_score":0.34965852},"labels":[],"label_agreement":null},{"id":"W3139697717","doi":"10.1021/acs.jpcc.1c00928","title":"Application of Ni–Spinel in the Chemical-Looping Conversion of CO<sub>2</sub> to CO via Induction-Generated Oxygen Vacancies","year":2021,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut interdisciplinaire d'innovation technologique; Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Catalysis; Spinel; Induction heating; Oxygen; Water-gas shift reaction; Ferrite (magnet); Chemical engineering; Materials science; Hydrogen; Nanoparticle; Octahedron; Chemistry; Metallurgy; Nanotechnology; Crystallography; Composite material; Crystal structure; Organic chemistry","score_opus":0.010092589259732037,"score_gpt":0.24250822713080902,"score_spread":0.232415637871077,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3139697717","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9983486,0.00008790347,0.0011359012,0.00019979071,0.000022968363,0.000074442425,0.000007840077,0.000007345039,0.00011520682],"genre_scores_gemma":[0.99955446,0.000013219329,0.000042778905,0.000028759621,0.00031171754,0.0000041644694,0.00002033847,0.000015703208,0.000008840664],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987635,0.00003481662,0.00050061016,0.00011396117,0.00041845636,0.00016863433],"domain_scores_gemma":[0.99884826,0.00017135644,0.0003707678,0.00029225159,0.00024975705,0.00006759017],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00037619553,0.00013899546,0.00035583982,0.000031959953,0.000027904176,0.0000049159403,0.00037206552,0.00007890344,0.000007136354],"category_scores_gemma":[0.00020880392,0.000092813105,0.00014844752,0.0005140438,0.00007173513,0.000082912484,0.00006321896,0.00042637187,0.0000029727414],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000053607913,0.00011171141,0.000021847465,0.00020892847,0.000051385312,0.0000021347262,0.00061665894,0.0016534633,0.9965181,0.000009312132,0.000037402096,0.0007155001],"study_design_scores_gemma":[0.000359231,0.00001865941,0.00008920565,0.00011031438,0.00006091956,0.00006606721,0.00042561325,0.0024883156,0.99616516,0.00005944329,0.000060596296,0.00009648412],"about_ca_topic_score_codex":0.000021784223,"about_ca_topic_score_gemma":3.9169132e-7,"teacher_disagreement_score":0.0012058759,"about_ca_system_score_codex":0.00012347597,"about_ca_system_score_gemma":0.0000696757,"threshold_uncertainty_score":0.37848085},"labels":[],"label_agreement":null},{"id":"W3140497392","doi":"10.1016/j.apcata.2021.118119","title":"Efficient approaches to overcome challenges in material development for conventional and intensified CO2 catalytic hydrogenation to CO, methanol, and DME","year":2021,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":85,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Catalysis; Dimethyl ether; Methanol; Greenhouse gas; Raw material; Petrochemical; Process engineering; Waste management; Organic chemistry","score_opus":0.08281913374498258,"score_gpt":0.2552247826605743,"score_spread":0.17240564891559174,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3140497392","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.996261,0.00032118717,0.0021652107,0.00030494126,0.00008809885,0.00050006586,0.000038532395,0.000041916883,0.00027905864],"genre_scores_gemma":[0.99163556,0.000010389823,0.0067357062,0.00006714344,0.00011195163,0.0004720897,0.00079452514,0.000039282888,0.00013336343],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982945,0.000013477153,0.00043027767,0.00063915673,0.00026105953,0.00036155683],"domain_scores_gemma":[0.99938464,0.000065198765,0.000060779937,0.00024194593,0.00005157546,0.00019583706],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00042266477,0.00024407604,0.0004490949,0.00027869802,0.0000621773,0.000034995497,0.00010694318,0.00010643182,0.000009992406],"category_scores_gemma":[0.00007523614,0.00024970973,0.0000643509,0.00028470802,0.000026351872,0.00003479585,0.00022583698,0.00008442478,0.000011641856],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013637748,0.000109564724,0.000029512883,0.00024423364,0.00022927257,0.0000057423786,0.0028348265,0.0055545084,0.9664081,0.00637742,0.0000118514945,0.018058605],"study_design_scores_gemma":[0.000882843,0.000016570677,0.0004218296,0.00002834448,0.00007039291,0.000028692159,0.000416499,0.009369244,0.9870877,0.0000954991,0.001217881,0.0003644739],"about_ca_topic_score_codex":0.00003311761,"about_ca_topic_score_gemma":0.00007492025,"teacher_disagreement_score":0.020679645,"about_ca_system_score_codex":0.0002325322,"about_ca_system_score_gemma":0.000052284533,"threshold_uncertainty_score":0.9999955},"labels":[],"label_agreement":null},{"id":"W3158098963","doi":"","title":"Carbon Dioxide Recycling for Fuels andChemical Products","year":2020,"lang":"en","type":"article","venue":"Progress in Petrochemical Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Carbon dioxide; Waste management; Environmental science; Business; Pulp and paper industry; Chemistry; Engineering; Organic chemistry","score_opus":0.024536273483844042,"score_gpt":0.28568840182979843,"score_spread":0.2611521283459544,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3158098963","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99603915,0.0008745226,0.00038806177,0.0013573762,0.00013809222,0.0003889552,0.000004523734,0.00022536096,0.00058394286],"genre_scores_gemma":[0.9900346,0.0000075782996,0.009295267,0.00007372508,0.00038595844,0.00014034031,0.0000099126255,0.000033143453,0.000019465453],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99716675,0.000008131959,0.0004543915,0.0008988435,0.00060216105,0.0008696975],"domain_scores_gemma":[0.9989647,0.00012817618,0.00009582079,0.0003054552,0.00013123955,0.00037456848],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005484621,0.00023524147,0.00035301186,0.000104023085,0.00006142457,0.000032318418,0.0008313809,0.00011741494,0.0000061058035],"category_scores_gemma":[0.0033787896,0.00021271853,0.00008352307,0.001553261,0.0005004144,0.00025971644,0.00034447762,0.00041705385,0.0000048844954],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006257911,0.00003943946,0.0031249886,0.00018909393,0.0000045492507,0.0000056822128,0.0002396803,0.000010192677,0.98893076,0.00016506133,0.000003381571,0.007224617],"study_design_scores_gemma":[0.000502334,0.00003467925,0.00006560463,0.000079945574,0.000010707796,0.000010618336,0.000037618942,0.019022504,0.9791668,0.00013590872,0.00064175,0.00029154585],"about_ca_topic_score_codex":0.000006246956,"about_ca_topic_score_gemma":5.093746e-7,"teacher_disagreement_score":0.019012311,"about_ca_system_score_codex":0.00029235307,"about_ca_system_score_gemma":0.00010104678,"threshold_uncertainty_score":0.86744094},"labels":[],"label_agreement":null},{"id":"W3162680207","doi":"10.1016/j.ijhydene.2021.04.124","title":"Simulation of methane steam reforming in a catalytic micro-reactor using a combined analytical approach and response surface methodology","year":2021,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":27,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Ministry of Science and ICT, South Korea; National Research Foundation of Korea; Ministry of Science and Innovation, New Zealand","keywords":"Steam reforming; Methane; Methane reformer; Catalysis; Process engineering; Response surface methodology; Nuclear engineering; Materials science; Hydrogen production; Thermodynamics; Environmental science; Chemistry; Engineering; Physics; Chromatography; Organic chemistry","score_opus":0.04818428857786462,"score_gpt":0.3235607405853281,"score_spread":0.27537645200746347,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3162680207","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98950976,0.00062483543,0.009558751,0.00006874247,0.00014225149,0.000027102049,0.000009113756,0.000007313937,0.000052113726],"genre_scores_gemma":[0.99189067,0.00002310596,0.007875714,0.000020185546,0.000080740916,5.500057e-7,0.000018966899,0.000026231379,0.00006383013],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979953,0.00024829758,0.0009097889,0.00019262807,0.0004542261,0.00019974062],"domain_scores_gemma":[0.9978106,0.0010507567,0.00046452373,0.00015468986,0.0004157331,0.00010372295],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0013635128,0.00015813994,0.000527768,0.00041626891,0.000009634608,0.000008173347,0.0002517476,0.00012871566,0.000011922024],"category_scores_gemma":[0.0017883092,0.00014619909,0.00017814332,0.00031419116,0.000055622393,0.000251004,0.00015346364,0.0002423629,2.8576525e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008351109,0.00009269964,0.00031205153,0.000016654927,0.00029690663,0.00017852287,0.0002703629,0.24282202,0.75403136,0.0002361163,1.2377369e-7,0.0009080387],"study_design_scores_gemma":[0.0011135145,0.000040194678,0.00004343491,0.00008799756,0.00006658825,0.00087361614,0.00022509768,0.29517898,0.7020368,0.00014740038,0.000078041,0.000108307184],"about_ca_topic_score_codex":0.00032148723,"about_ca_topic_score_gemma":0.000023076267,"teacher_disagreement_score":0.052356966,"about_ca_system_score_codex":0.00043958152,"about_ca_system_score_gemma":0.00020641825,"threshold_uncertainty_score":0.5961826},"labels":[],"label_agreement":null},{"id":"W3163400902","doi":"10.1039/d1cy00399b","title":"On the support dependency of the CO<sub>2</sub> methanation – decoupling size and support effects","year":2021,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":51,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Deutsche Forschungsgemeinschaft","keywords":"Methanation; Isostructural; Catalysis; Decoupling (probability); Dependency (UML); Rotation formalisms in three dimensions; Chemistry; Chemical engineering; Materials science; Computer science; Crystallography; Organic chemistry; Mathematics; Crystal structure; Artificial intelligence","score_opus":0.006642185293736994,"score_gpt":0.2394795154394788,"score_spread":0.2328373301457418,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3163400902","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9972952,0.00009024502,0.0007965604,0.0006619756,0.00014256882,0.00017803098,0.000004406016,0.000101782025,0.0007292329],"genre_scores_gemma":[0.99963224,0.000024440626,0.00012319189,0.000059458955,0.000013977557,0.00003663903,0.0000070737597,0.000017551103,0.00008544873],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981042,0.00002079045,0.00034693198,0.00051790976,0.00058039656,0.00042975083],"domain_scores_gemma":[0.9979603,0.0005850381,0.00019683535,0.0009977873,0.00019211526,0.00006789651],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011161031,0.00018191672,0.00031826587,0.00040014365,0.00026917443,0.000022675014,0.0008731402,0.0001773837,0.000027708871],"category_scores_gemma":[0.0057222573,0.00011634186,0.00013218187,0.0035290848,0.0009249247,0.00019351272,0.0004886676,0.00039354412,0.000019824442],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000020552054,0.000022968126,0.0005314636,0.000028869685,0.000027572903,0.000009113619,0.000105967796,0.0000792632,0.98625976,0.004746895,0.0000034047632,0.008182638],"study_design_scores_gemma":[0.0001458579,0.000028189037,0.00031686525,0.00003171534,0.000086446285,0.000106162595,0.00019663597,0.0009220304,0.99627227,0.0017085858,0.000052327778,0.00013293371],"about_ca_topic_score_codex":0.000007869047,"about_ca_topic_score_gemma":0.00002623882,"teacher_disagreement_score":0.010012462,"about_ca_system_score_codex":0.00017511248,"about_ca_system_score_gemma":0.00022947822,"threshold_uncertainty_score":0.685049},"labels":[],"label_agreement":null},{"id":"W3167231058","doi":"10.5539/ijc.v13n2p1","title":"A Chemical Reaction Can Save Mankind -A Review of Experiment Research on CO2+C=2CO and Application","year":2021,"lang":"en","type":"article","venue":"International Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Chemistry; Catalysis; Lime; Flue gas; Coal; Environmental pollution; Pollution; Waste management; Flue; Metallurgy; Organic chemistry; Environmental science; Engineering; Environmental protection","score_opus":0.02764179283042358,"score_gpt":0.36314805150617696,"score_spread":0.3355062586757534,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3167231058","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9895965,0.004846524,0.00014303195,0.0014503326,0.00011586224,0.000057912137,0.000011881336,0.000008069398,0.0037699211],"genre_scores_gemma":[0.99717134,0.0019418327,0.00022591268,0.000055767854,0.00036291135,0.0000071363334,0.000037181955,0.000013350784,0.00018457176],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984578,0.000015494825,0.00046202532,0.00013775314,0.0008184776,0.00010844822],"domain_scores_gemma":[0.9985664,0.00011898321,0.0002561686,0.00015343724,0.0008229727,0.00008206452],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004400749,0.00008505971,0.00020340507,0.000053762567,0.000012483417,0.000008868974,0.00021143057,0.00007206136,0.00007352499],"category_scores_gemma":[0.0004701786,0.0000795313,0.00009768678,0.00011263798,0.00004569845,0.000060236547,0.000084350024,0.00038267596,0.0000019470624],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000045453624,0.000071734496,0.000015081795,0.0005181748,0.000085688975,0.000033340533,0.000054265674,0.000005511648,0.9938904,0.00011499364,0.00008858617,0.0050767455],"study_design_scores_gemma":[0.0003373714,0.000009104555,0.000014727297,0.0027152863,0.00001649064,0.00062066404,0.00009638789,0.000058975416,0.9919454,0.00009438036,0.004026812,0.00006440816],"about_ca_topic_score_codex":0.0000113570395,"about_ca_topic_score_gemma":2.728256e-7,"teacher_disagreement_score":0.007574869,"about_ca_system_score_codex":0.0003560774,"about_ca_system_score_gemma":0.000092591785,"threshold_uncertainty_score":0.32431924},"labels":[],"label_agreement":null},{"id":"W3168255214","doi":"10.1515/revce-2020-0038","title":"State-of-the-art in methane-reforming reactor modeling: challenges and new insights","year":2021,"lang":"en","type":"article","venue":"Reviews in Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Methane; Process (computing); Methane reformer; Modeling and simulation; Process engineering; Work (physics); Steam reforming; Process simulation; Reactor design; Process modeling; Computer science; Work in process; Biochemical engineering; Engineering; Mechanical engineering; Chemistry; Catalysis; Simulation; Hydrogen production; Nuclear engineering; Operations management","score_opus":0.045997667808587946,"score_gpt":0.2633218760065419,"score_spread":0.21732420819795395,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3168255214","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.85518223,0.14266436,0.0010343775,0.00012506002,0.00018135353,0.00030654896,0.0000015918954,0.0000646513,0.00043981525],"genre_scores_gemma":[0.97039574,0.024655173,0.0044853403,0.000022611124,0.00013308144,0.000050255694,0.000011671419,0.000095108706,0.00015102574],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99809015,0.000026037898,0.00088167255,0.00038734268,0.00022685857,0.00038792638],"domain_scores_gemma":[0.9991347,0.00014248745,0.0000961726,0.00045313084,0.000027897042,0.00014557202],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00036882592,0.00028917706,0.0007922012,0.00014149348,0.000006202239,0.000005112917,0.00024563,0.00014235708,0.000006510155],"category_scores_gemma":[0.0012797975,0.00022974868,0.00016862071,0.0005232452,0.000016702734,0.00018827205,0.00026365323,0.0006017329,0.000004986423],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000049287155,0.000027934244,0.000012698684,0.0011206982,0.000016558146,0.000017934008,0.00078313594,0.005930656,0.9161007,0.00030037112,0.0000010397843,0.07568335],"study_design_scores_gemma":[0.0005772895,0.000004626824,0.000015023951,0.002800602,0.000021601687,0.00006369043,0.000030429981,0.10952743,0.87572473,0.00027914927,0.010579869,0.00037552454],"about_ca_topic_score_codex":0.000039312567,"about_ca_topic_score_gemma":0.00003235636,"teacher_disagreement_score":0.11800919,"about_ca_system_score_codex":0.00023073154,"about_ca_system_score_gemma":0.000052968473,"threshold_uncertainty_score":0.9368879},"labels":[],"label_agreement":null},{"id":"W3173003827","doi":"10.1016/j.jcou.2021.101608","title":"CO2 utilization for methanol production; Part I: Process design and life cycle GHG assessment of different pathways","year":2021,"lang":"en","type":"article","venue":"Journal of CO2 Utilization","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":109,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Natural Resources Canada","funders":"","keywords":"Life-cycle assessment; Waste management; Context (archaeology); Flue gas; Environmental science; Greenhouse gas; Kiln; Methanol; Electricity; Natural gas; Electricity generation; Pulp and paper industry; Process engineering; Engineering; Production (economics); Chemistry","score_opus":0.07665180469223634,"score_gpt":0.32570348525764076,"score_spread":0.24905168056540442,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3173003827","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.531018,0.00053398893,0.46762434,0.000103014405,0.00034026016,0.00029201235,0.0000073650444,0.000022610038,0.000058350823],"genre_scores_gemma":[0.9956349,0.0003139761,0.0036568644,0.000014145336,0.00021030432,0.00002050742,0.000046477206,0.00003330604,0.00006952285],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99841243,0.00007117611,0.00074186345,0.00018521561,0.00042187996,0.00016740774],"domain_scores_gemma":[0.9980106,0.00014742778,0.00061337225,0.00015628847,0.0009581234,0.00011422121],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00056161644,0.00015349631,0.00038898934,0.00014586942,0.000059775604,0.00002086242,0.000092515234,0.00009619388,0.000025948302],"category_scores_gemma":[0.0013334462,0.0001312228,0.0000956522,0.00034444418,0.00002747349,0.00034198014,0.000029017157,0.00013881348,1.833377e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023571496,0.00063111784,0.0017012043,0.001928751,0.0003918082,0.000007673117,0.0012160757,0.10113715,0.86614823,0.002680943,0.00012902947,0.023792276],"study_design_scores_gemma":[0.0007767423,0.00012311086,0.00060753745,0.00029050568,0.0001775972,0.000054914748,0.0003470328,0.14510007,0.85123074,0.0008062675,0.00034961075,0.00013585946],"about_ca_topic_score_codex":7.435417e-7,"about_ca_topic_score_gemma":0.0000015089623,"teacher_disagreement_score":0.46461684,"about_ca_system_score_codex":0.000107105116,"about_ca_system_score_gemma":0.00023393364,"threshold_uncertainty_score":0.535111},"labels":[],"label_agreement":null},{"id":"W3175264583","doi":"10.3390/catal11070771","title":"The ‘Green’ Ni-UGSO Catalyst for Hydrogen Production under Various Reforming Regimes","year":2021,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Fonds de recherche du Québec – Nature et technologies","keywords":"Methane; Space velocity; Catalysis; Carbon dioxide reforming; Hydrogen production; Steam reforming; Methane reformer; Sulfur; Atmospheric pressure; Molar ratio; Materials science; Hydrogen; Chemistry; Syngas; Inorganic chemistry; Chemical engineering; Nuclear chemistry; Metallurgy; Organic chemistry; Selectivity","score_opus":0.015316747328899186,"score_gpt":0.24904816255691792,"score_spread":0.23373141522801874,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3175264583","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9767524,0.0075289784,0.0021815689,0.004840905,0.0025181551,0.0012031781,0.00007179621,0.0008217776,0.0040812334],"genre_scores_gemma":[0.9442311,0.00007851459,0.0003034416,0.00008430762,0.001089303,0.00025563943,0.00076457293,0.000151601,0.053041514],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9975529,0.000029739946,0.0005766575,0.00069787324,0.0004104355,0.00073239347],"domain_scores_gemma":[0.9978296,0.00020128803,0.00020689267,0.001310194,0.00027727277,0.00017473099],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005933341,0.0003430039,0.00040066248,0.000104674626,0.0005256908,0.000048703943,0.0004628516,0.00019088297,0.0000080876225],"category_scores_gemma":[0.00084449264,0.00026150324,0.0003162446,0.00062652514,0.00010950842,0.00034442506,0.0002373419,0.000324996,0.000090618065],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007631675,0.00008424687,0.00007074257,0.00035501542,0.0005935142,0.000052979492,0.0011473128,0.0005546096,0.9604832,0.0029326074,0.0008329928,0.0328165],"study_design_scores_gemma":[0.00043165564,0.000016761933,0.000027699216,0.00007976294,0.0001799871,0.0003570723,0.00067281374,0.0007221005,0.95577806,0.00082566316,0.04050419,0.0004042427],"about_ca_topic_score_codex":0.00040181176,"about_ca_topic_score_gemma":0.0004290893,"teacher_disagreement_score":0.04896028,"about_ca_system_score_codex":0.00048496213,"about_ca_system_score_gemma":0.0001768103,"threshold_uncertainty_score":0.9999837},"labels":[],"label_agreement":null},{"id":"W3175962317","doi":"10.1016/j.jcat.2021.06.020","title":"New insights on CO and CO2 hydrogenation for methanol synthesis: The key role of adsorbate-adsorbate interactions on Cu and the highly active MgO-Cu interface","year":2021,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":70,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Horizon 2020; European Research Council; Horizon 2020 Framework Programme; Villum Fonden; University of Toronto; Danmarks Tekniske Universitet; European Commission; Stanford University","keywords":"Chemistry; Formate; Catalysis; Methanol; Density functional theory; Adsorption; Hydrogen; Photochemistry; Transition metal; Heterogeneous catalysis; Carbon monoxide; Inorganic chemistry; Transition state; Reaction intermediate; Computational chemistry; Physical chemistry; Organic chemistry","score_opus":0.010472942139207174,"score_gpt":0.25526763947631875,"score_spread":0.24479469733711157,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3175962317","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9950177,0.0015073657,0.0012526588,0.001326427,0.0001246239,0.0001625658,0.000021847178,0.00000923695,0.0005775481],"genre_scores_gemma":[0.99897254,0.00026722497,0.00022563976,0.000033584514,0.00013010745,0.000014599517,0.000007773506,0.000026026344,0.00032251026],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99869794,0.00009249214,0.0005414569,0.00017987115,0.00033653743,0.0001516847],"domain_scores_gemma":[0.9970153,0.0018084091,0.0005743531,0.0002770715,0.00023067549,0.0000942198],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004270984,0.00018434053,0.00050895836,0.00022216242,0.000096393276,0.000039021124,0.00018096266,0.00007197388,0.00002049564],"category_scores_gemma":[0.0010895318,0.00010361717,0.0002972382,0.00028707593,0.00007172564,0.00028941708,0.00006374792,0.0003713517,0.000003206744],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0011363588,0.00008954968,0.000010266266,0.00005553362,0.0017653614,0.000006855973,0.006254591,0.0019067107,0.95216566,0.0008997172,0.000052166237,0.035657246],"study_design_scores_gemma":[0.00097299676,0.00007051544,0.000043346412,0.00021178945,0.000717851,0.000116483614,0.0017720654,0.0041593798,0.9871197,0.0005462013,0.0041574803,0.00011221208],"about_ca_topic_score_codex":0.00007827605,"about_ca_topic_score_gemma":0.00007150671,"teacher_disagreement_score":0.035545032,"about_ca_system_score_codex":0.00013575586,"about_ca_system_score_gemma":0.00006171846,"threshold_uncertainty_score":0.42253855},"labels":[],"label_agreement":null},{"id":"W3176727482","doi":"10.1002/apj.2683","title":"Thermodynamic equilibrium analysis of oxy‐dry reforming of biogas with CO<sub>2</sub> sequestration using Aspen HYSYS","year":2021,"lang":"en","type":"article","venue":"Asia-Pacific Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Carbon dioxide reforming; Syngas; Biogas; Chemistry; Renewable energy; Methane; Waste management; Stoichiometry; Syngas to gasoline plus; Methane reformer; Catalysis; Pulp and paper industry; Hydrogen production; Steam reforming; Organic chemistry; Engineering","score_opus":0.010019035197072975,"score_gpt":0.2289120247622091,"score_spread":0.21889298956513611,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3176727482","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.980476,0.0003884371,0.018573888,0.000020029573,0.00010020835,0.000078286204,0.000022724873,0.000043206026,0.00029721888],"genre_scores_gemma":[0.99513113,0.00002362748,0.004575543,0.0000018143427,0.00012706257,0.0000017997759,0.000055526416,0.0000774439,0.0000060506736],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99714226,0.000026134514,0.0013611105,0.00028711162,0.00073121244,0.00045219844],"domain_scores_gemma":[0.9979125,0.00017863447,0.00080955157,0.0004471405,0.00044198253,0.00021014726],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00049553125,0.00035950402,0.0011644452,0.0007002522,0.000017799528,0.000019113053,0.00032490946,0.00022851989,0.000017277016],"category_scores_gemma":[0.00028070793,0.0003164635,0.00058132067,0.0017530096,0.00007749147,0.0005106472,0.000084970576,0.00058941677,8.3846913e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006730651,0.00005879344,0.00022392628,0.00020514388,0.0015256163,0.000072951865,0.0002307968,0.06323683,0.93349165,0.00013113537,4.4499524e-7,0.0007554148],"study_design_scores_gemma":[0.00045582093,0.000044060216,0.000051744504,0.00042802902,0.0009895668,0.0002458035,0.0002514618,0.16184387,0.835404,0.000013278746,0.000010441851,0.0002619397],"about_ca_topic_score_codex":0.000015438813,"about_ca_topic_score_gemma":0.0000010131771,"teacher_disagreement_score":0.09860703,"about_ca_system_score_codex":0.00040610234,"about_ca_system_score_gemma":0.00017329448,"threshold_uncertainty_score":0.9999288},"labels":[],"label_agreement":null},{"id":"W3177384514","doi":"10.53063/synsint.2021.1229","title":"Direct catalytic production of dimethyl ether from CO and CO2: A review","year":2021,"lang":"en","type":"review","venue":"Synthesis and Sintering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":26,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Bryden Centre, Queen's University Belfast; European Commission; Interreg; Department for the Economy","keywords":"Dimethyl ether; Cetane number; Syngas; Diesel fuel; Combustion; Waste management; NOx; Environmental science; Chemistry; Catalysis; Organic chemistry; Biodiesel; Engineering","score_opus":0.03514617852489527,"score_gpt":0.3046676729228126,"score_spread":0.26952149439791734,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3177384514","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0005078448,0.99830467,0.00001970432,0.000012849104,0.00015975496,0.0002752489,0.00005179551,0.000041075273,0.00062707823],"genre_scores_gemma":[0.00050858257,0.99873936,0.00018382883,0.000003855705,0.00011565541,0.00006176319,0.00004882438,0.00007665925,0.00026147207],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.998423,0.00008066795,0.00064566545,0.00050421385,0.0001549075,0.0001915573],"domain_scores_gemma":[0.9987066,0.00047160516,0.00028301607,0.00043181586,0.000030873485,0.00007613737],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004296293,0.00035692114,0.0022629383,0.000102191916,0.0000297588,0.000016791972,0.0001233506,0.0001624958,0.00006867495],"category_scores_gemma":[0.0011211048,0.00027927395,0.00033411157,0.00016328783,0.00005857846,0.000077430916,0.00015774556,0.00023342976,0.0000054557445],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000012438973,0.000010871295,7.4000747e-7,0.06661936,0.00032564244,0.0000067123087,0.000069779955,1.366625e-7,0.0026772206,0.00000584458,0.000015127528,0.93026733],"study_design_scores_gemma":[0.000039354985,0.0000074580553,7.336134e-7,0.32471755,0.002078485,0.00011063397,0.000032192856,0.000012502182,0.040828235,0.0000027391172,0.63173234,0.00043773334],"about_ca_topic_score_codex":0.00015298746,"about_ca_topic_score_gemma":0.000005785232,"teacher_disagreement_score":0.9298296,"about_ca_system_score_codex":0.00007450471,"about_ca_system_score_gemma":0.000029238847,"threshold_uncertainty_score":0.99996597},"labels":[],"label_agreement":null},{"id":"W3184800998","doi":"10.1016/j.rser.2021.111457","title":"Techno economic analysis of a micro Gas-to-Liquid unit for associated natural gas conversion","year":2021,"lang":"en","type":"article","venue":"Renewable and Sustainable Energy Reviews","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs; Canada Research Chairs; Canada Foundation for Innovation","keywords":"Syngas; Natural gas; Gas compressor; Operating cost; Capital cost; Methane; Process engineering; Partial oxidation; Greenhouse gas; Waste management; Fluidized bed; Liquefied natural gas; Methane reformer; Environmental science; Chemistry; Engineering; Mechanical engineering; Steam reforming","score_opus":0.01057218976140254,"score_gpt":0.24503666887366102,"score_spread":0.23446447911225848,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3184800998","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9214247,0.07034965,0.005282224,0.00036581617,0.00017362038,0.0006383809,0.00006499718,0.00014082184,0.0015598269],"genre_scores_gemma":[0.8510919,0.032061145,0.0028693627,0.0005657099,0.0002046434,0.00041150986,0.0018991923,0.00017835553,0.11071814],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982593,0.000046424382,0.0006098562,0.00040695854,0.00010331525,0.00057415845],"domain_scores_gemma":[0.9988416,0.00013770227,0.00022854614,0.0004221063,0.00022718031,0.00014286942],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006731893,0.00024219471,0.001067399,0.00042324353,0.00010779136,0.000022014026,0.00018190386,0.00015220647,0.00006976837],"category_scores_gemma":[0.0005254941,0.00022310605,0.00044145598,0.0013256804,0.000026983435,0.0001504362,0.00021313452,0.000093709095,0.0000021040757],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00020103164,0.00013088249,0.0002800775,0.0029565042,0.0025921052,0.000067508576,0.000246592,0.034321174,0.9434696,0.004711526,0.0012428019,0.009780219],"study_design_scores_gemma":[0.0004661725,0.00006933411,0.0000024197623,0.00016281226,0.0009305337,0.0000071259,0.00046042702,0.012922573,0.5632795,0.000091982016,0.42131937,0.00028773132],"about_ca_topic_score_codex":0.0036880074,"about_ca_topic_score_gemma":0.00051634945,"teacher_disagreement_score":0.42007658,"about_ca_system_score_codex":0.00037895792,"about_ca_system_score_gemma":0.00012812467,"threshold_uncertainty_score":0.90980005},"labels":[],"label_agreement":null},{"id":"W3184935145","doi":"10.3390/reactions2030015","title":"Fischer–Tropsch Synthesis for Light Olefins from Syngas: A Review of Catalyst Development","year":2021,"lang":"en","type":"review","venue":"Reactions","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":67,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Fischer–Tropsch process; Olefin fiber; Syngas; Catalysis; Selectivity; Chemical engineering; Transition metal; Cobalt; Chemistry; Materials science; Inorganic chemistry; Organic chemistry","score_opus":0.050637253019088,"score_gpt":0.32229120102137393,"score_spread":0.2716539480022859,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3184935145","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0000032742082,0.99635303,0.0008504172,0.000041066472,0.0002632783,0.0008135294,0.00051420473,0.00011274469,0.0010484282],"genre_scores_gemma":[0.0000017414192,0.9911169,0.0034502747,0.000009252655,0.0002470911,0.0015129673,0.002298908,0.00015181521,0.0012110438],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9970134,0.000062107145,0.0016040372,0.00059562625,0.00033990975,0.0003849316],"domain_scores_gemma":[0.9967431,0.001194921,0.000743883,0.0009723231,0.00018506407,0.00016075475],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00039313978,0.00054874795,0.0030085938,0.00022601892,0.00009416328,0.000013506451,0.0004170544,0.00039214594,0.00023308911],"category_scores_gemma":[0.002187966,0.0004677134,0.0014747145,0.0006549423,0.000020966583,0.00010908016,0.0001553623,0.0005072022,0.00010505846],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000012511641,0.00011622893,1.9054015e-7,0.25661907,0.001753748,0.000009291929,0.000037049907,6.623416e-7,0.0009777624,0.00012644414,0.0005959601,0.73976237],"study_design_scores_gemma":[0.000044898785,0.0000028253125,9.229745e-8,0.23696238,0.0025499042,0.000041852778,0.000010915209,0.0000029159576,0.007307851,0.0000012057122,0.7527273,0.00034786266],"about_ca_topic_score_codex":0.00015874207,"about_ca_topic_score_gemma":0.000045185283,"teacher_disagreement_score":0.75213134,"about_ca_system_score_codex":0.0006637408,"about_ca_system_score_gemma":0.00063628936,"threshold_uncertainty_score":0.99977744},"labels":[],"label_agreement":null},{"id":"W3185957938","doi":"10.1002/cjce.24266","title":"Experimental studies of catalyst deactivation due to carbon and sulphur during <scp>CO</scp> <sub>2</sub> reforming of <scp>CH</scp> <sub>4</sub> over Ni washcoated monolith in the presence of H <sub>2</sub> S","year":2021,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Monolith; Cordierite; Catalysis; Sulfur; Chemistry; Carbon fibers; Deposition (geology); Biogas; Fouling; CO poisoning; Chemical engineering; Nuclear chemistry; Waste management; Materials science; Organic chemistry; Composite material","score_opus":0.01174516007393719,"score_gpt":0.2267069248494603,"score_spread":0.21496176477552312,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3185957938","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99684674,0.0024703606,0.000042005187,0.000051999563,0.0001814649,0.00029855224,0.000034447185,0.00002586894,0.00004856737],"genre_scores_gemma":[0.99948686,0.00007487641,0.000079611425,0.000016826789,0.00019692416,0.000025909374,0.000016214326,0.00009889785,0.0000038946782],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9963746,0.00007253669,0.001483583,0.0003939546,0.0008013379,0.0008739794],"domain_scores_gemma":[0.9969454,0.0009578991,0.0006512667,0.00057418435,0.00037496802,0.0004963066],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0009610524,0.0005180813,0.0011274198,0.00062058575,0.00009125559,0.0000349524,0.0006507186,0.00026335559,4.867262e-7],"category_scores_gemma":[0.0032270865,0.0004211266,0.00027350057,0.0011673108,0.00019829738,0.00041843086,0.00019834413,0.0010011136,6.666348e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000016768427,0.00004316494,0.0003038368,0.00048947474,0.00029705634,0.00013933796,0.007130536,0.008135098,0.982984,0.000046987323,0.00000994797,0.00040378555],"study_design_scores_gemma":[0.00083939533,0.00005474419,0.00086667144,0.0011040067,0.000120457225,0.0005272813,0.0026232505,0.0023292764,0.9913434,0.000026289188,0.000010669455,0.00015455282],"about_ca_topic_score_codex":0.0010584183,"about_ca_topic_score_gemma":0.00044476773,"teacher_disagreement_score":0.0083594,"about_ca_system_score_codex":0.0009280693,"about_ca_system_score_gemma":0.0003512549,"threshold_uncertainty_score":0.99982405},"labels":[],"label_agreement":null},{"id":"W3186121807","doi":"10.21203/rs.3.rs-701447/v1","title":"The Role of Cu1-O3 Species in Single-Atom Cu Catalyst for Directional Methanol Synthesis from CO2 Hydrogenation","year":2021,"lang":"en","type":"preprint","venue":"Research Square","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China; Natural Science Foundation of Fujian Province; Canadian Light Source","keywords":"Catalysis; Methanol; Atom (system on chip); Chemistry; Materials science; Organic chemistry; Computer science; Parallel computing","score_opus":0.046863331117576415,"score_gpt":0.3242661336316922,"score_spread":0.2774028025141158,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3186121807","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9874845,0.006923721,0.0007219268,0.0002334014,0.00028741668,0.0011562753,0.0009047406,0.00009239841,0.0021956072],"genre_scores_gemma":[0.99612546,0.0003164203,0.0006838002,0.0000012785669,0.0003772001,0.0009302579,0.001030794,0.000091827445,0.00044297348],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9962096,0.0002695936,0.0007134881,0.0006856219,0.0014515601,0.0006700883],"domain_scores_gemma":[0.99275255,0.005298804,0.00020530347,0.0009029566,0.0007148153,0.00012555711],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0020333042,0.00030459045,0.00063106127,0.00053833204,0.00017727235,0.00010988145,0.0007410326,0.00043156612,0.00009516723],"category_scores_gemma":[0.0049908725,0.00025636665,0.00045882733,0.0006919391,0.00017115154,0.00013524291,0.00102675,0.0011978789,0.000009925777],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013404244,0.0002162159,0.0010723367,0.00086902763,0.00044505444,0.000011574032,0.0010279778,0.0015317211,0.96154225,0.000706274,0.000024198765,0.032419305],"study_design_scores_gemma":[0.00021376404,0.000015839178,0.0005905822,0.0010565683,0.00004621749,0.0000030434348,0.0021810783,0.008481807,0.9790762,0.0012649265,0.0068137953,0.000256159],"about_ca_topic_score_codex":0.0043369764,"about_ca_topic_score_gemma":0.0022185112,"teacher_disagreement_score":0.032163147,"about_ca_system_score_codex":0.0012237668,"about_ca_system_score_gemma":0.00032824924,"threshold_uncertainty_score":0.99998885},"labels":[],"label_agreement":null},{"id":"W3190402307","doi":"10.1039/d1se00514f","title":"A thermodynamic analysis of biogas-to-methanol conversion with CH<sub>4</sub> recycling and CO<sub>2</sub> utilization using Aspen HYSYS","year":2021,"lang":"en","type":"article","venue":"Sustainable Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Biogas; Methanol; Waste management; Materials science; Environmental science; Chemistry; Organic chemistry; Engineering","score_opus":0.011877561176272568,"score_gpt":0.23924306582973734,"score_spread":0.22736550465346478,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3190402307","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9670253,0.00058379385,0.031480744,0.000026575484,0.000053217478,0.00018892606,0.000018171011,0.00011513891,0.0005081261],"genre_scores_gemma":[0.9987654,0.00022869965,0.00036284717,0.000040995306,0.000054533644,0.000022729515,0.0002607928,0.0000996219,0.00016437277],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99737465,0.00009369711,0.00056066486,0.0007124877,0.0004987359,0.00075978076],"domain_scores_gemma":[0.9981392,0.00018033531,0.00029243572,0.000610228,0.0005361903,0.00024161731],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00044745192,0.00039732773,0.00081259775,0.0009977083,0.00017699231,0.000053611697,0.00020874671,0.00024305198,0.000022813638],"category_scores_gemma":[0.0002652133,0.00038658653,0.00023861881,0.0035130493,0.00008923066,0.000428495,0.00027551025,0.00021514129,0.0000021783303],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000099369856,0.000053263106,0.00036683292,0.00031053997,0.00090884004,0.0001485489,0.00033812525,0.021943135,0.9691762,0.001430858,0.0000012166117,0.0052230963],"study_design_scores_gemma":[0.0006215546,0.000056907775,0.00017981365,0.00015304457,0.0010624027,0.00002855899,0.0021237535,0.04834789,0.94669336,0.00013395424,0.00017312514,0.00042566177],"about_ca_topic_score_codex":0.00058154226,"about_ca_topic_score_gemma":0.00011878584,"teacher_disagreement_score":0.0317401,"about_ca_system_score_codex":0.00060376845,"about_ca_system_score_gemma":0.00022823056,"threshold_uncertainty_score":0.9998586},"labels":[],"label_agreement":null},{"id":"W3191975529","doi":"10.2139/ssrn.3892702","title":"Tunable Syngas Production from Biomass: Synergistic Effect of Steam, Ni-Cao Catalyst, and Biochar","year":2021,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institute of Particle Physics","funders":"","keywords":"Biochar; Syngas; Biomass (ecology); Steam reforming; Catalysis; Chemical engineering; Waste management; Pulp and paper industry; Materials science; Chemistry; Hydrogen production; Pyrolysis; Organic chemistry; Engineering; Agronomy","score_opus":0.004522313440746159,"score_gpt":0.2134696474636999,"score_spread":0.20894733402295373,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3191975529","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9812058,0.016933557,0.0011796436,0.00009528289,0.0003363867,0.0000974434,0.000010227426,0.000049093385,0.00009251964],"genre_scores_gemma":[0.9972153,0.0010544973,0.000048474118,0.0000028109357,0.00038935008,0.000006592089,0.000051324907,0.000047318856,0.0011843365],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976012,0.00008237347,0.00041450837,0.00034185473,0.0003110762,0.001248955],"domain_scores_gemma":[0.99915534,0.00012004324,0.00019847041,0.0003156147,0.000099986166,0.000110521156],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011108924,0.00023140266,0.00043832662,0.00014861017,0.00011348934,0.000021130698,0.00016579952,0.000099968755,0.000030113535],"category_scores_gemma":[0.00069200207,0.00019647118,0.00014256641,0.00036115537,0.000051675783,0.00021774368,0.00008605019,0.0010531408,0.000016647067],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000055533827,0.000030321187,0.00031458485,0.00011652438,0.0004149279,0.000022965838,0.000058681617,0.000048078986,0.99254316,0.0007232302,0.000008432238,0.005663584],"study_design_scores_gemma":[0.00066086714,0.00014774816,0.000026977788,0.00014908849,0.0002606901,0.0010576416,0.0002898667,0.00019245784,0.99445844,0.0024112058,0.0001371086,0.00020791258],"about_ca_topic_score_codex":0.0006288232,"about_ca_topic_score_gemma":0.00022206266,"teacher_disagreement_score":0.016009448,"about_ca_system_score_codex":0.0007348729,"about_ca_system_score_gemma":0.00045786382,"threshold_uncertainty_score":0.80118626},"labels":[],"label_agreement":null},{"id":"W3193844673","doi":"10.3390/app11062672","title":"Electrifying with High-Temperature Water Electrolysis to Produce Syngas from Wood via Oxy-Gasification, Leading to Superior Carbon Conversion Yield for Methanol Synthesis","year":2021,"lang":"en","type":"article","venue":"Applied Sciences","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Hydro-Québec; Université du Québec à Trois-Rivières","funders":"","keywords":"Syngas; Water-gas shift reaction; Waste management; Fossil fuel; Synthetic fuel; Carbon fibers; Greenhouse gas; Wood gas generator; Methanol; Biofuel; Integrated gasification combined cycle; Syngas to gasoline plus; Yield (engineering); Environmental science; Pulp and paper industry; Hydrogen production; Steam reforming; Chemistry; Coal; Materials science; Hydrogen; Catalysis; Organic chemistry; Engineering","score_opus":0.012534644944998239,"score_gpt":0.22191160766434584,"score_spread":0.2093769627193476,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3193844673","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99541605,0.000079890335,0.002339403,0.0011691968,0.000100756646,0.0005743842,0.000008980317,0.00014371914,0.00016764524],"genre_scores_gemma":[0.9909245,0.000003392238,0.007992207,0.00017748194,0.00018227205,0.0004527669,0.000028863864,0.000043067,0.0001954685],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974841,0.000019580302,0.00029933953,0.0009905068,0.000494199,0.00071226154],"domain_scores_gemma":[0.9988158,0.0003765391,0.000052821608,0.00042891715,0.0001359554,0.00018996421],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00055516144,0.00027911377,0.00044307695,0.0002330672,0.00030374454,0.000108306485,0.0004399473,0.00012864156,0.000037523205],"category_scores_gemma":[0.00035691378,0.00019981031,0.000078767014,0.001229576,0.000047747068,0.0001602391,0.00009081045,0.00021348393,0.000030424073],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006738313,0.000021072305,0.000042638807,0.00003903652,0.00006706793,0.0000027653568,0.00074200885,0.00053839927,0.9973088,0.00012086781,0.000010161839,0.0010397886],"study_design_scores_gemma":[0.0001521683,0.00006362497,0.000016833566,0.00007508703,0.00011410837,0.000008575941,0.000450162,0.00024752575,0.99820584,0.000045929486,0.00026148808,0.00035863224],"about_ca_topic_score_codex":0.00021324985,"about_ca_topic_score_gemma":0.00012431508,"teacher_disagreement_score":0.005652804,"about_ca_system_score_codex":0.00018245005,"about_ca_system_score_gemma":0.000090641304,"threshold_uncertainty_score":0.8148028},"labels":[],"label_agreement":null},{"id":"W3207355979","doi":"10.3390/catal10091056","title":"The Demonstration of the Superiority of the Dual Ni-Based Catalytic System for the Adjustment of the H2/CO Ratio in Syngas for Green Fuel Technologies","year":2020,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Syngas; Exothermic reaction; Endothermic process; Methane; Syngas to gasoline plus; Raw material; Water-gas shift reaction; Chemical engineering; Catalysis; Materials science; Fischer–Tropsch process; Chemistry; Process engineering; Steam reforming; Hydrogen production; Adsorption; Organic chemistry; Engineering","score_opus":0.019410732985200414,"score_gpt":0.23841163572036256,"score_spread":0.21900090273516215,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3207355979","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9840241,0.0021353492,0.0014664558,0.006279671,0.00062285893,0.004774896,0.00045694443,0.00011758001,0.00012212647],"genre_scores_gemma":[0.9995113,0.000006730818,0.00003503146,0.000016811864,0.000050680013,0.0002828681,0.000020873294,0.000026052172,0.000049639482],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99836135,0.00005313485,0.00068940676,0.00023169277,0.0003960691,0.00026834954],"domain_scores_gemma":[0.9975959,0.0007811123,0.00042257886,0.0010347596,0.00013772093,0.000027938353],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006033051,0.0002061845,0.00036544196,0.000031326934,0.00025757804,0.000014912367,0.0011389517,0.00014125522,4.0217992e-7],"category_scores_gemma":[0.0012614336,0.00008466905,0.00038518079,0.0005501471,0.00038115645,0.00007936318,0.00024110837,0.0002575725,4.8976887e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00020157783,0.00007526302,0.0030934457,0.0037024897,0.00031290497,5.5331054e-7,0.002046657,0.0032727253,0.9790138,0.0046593715,0.00009345547,0.0035277274],"study_design_scores_gemma":[0.0006660144,0.000035645102,0.0013086274,0.00022833778,0.00020467286,0.0000059426493,0.002654043,0.014161773,0.9803672,0.000058313824,0.00020466532,0.0001047904],"about_ca_topic_score_codex":0.0003956438,"about_ca_topic_score_gemma":0.0005348433,"teacher_disagreement_score":0.015487195,"about_ca_system_score_codex":0.00019991487,"about_ca_system_score_gemma":0.0002232728,"threshold_uncertainty_score":0.34527037},"labels":[],"label_agreement":null},{"id":"W3212582886","doi":"10.1007/978-3-030-88424-6_5","title":"Catalytic Upgrading of Heavy Oil Resources Under Methane","year":2021,"lang":"en","type":"book-chapter","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Methane; Petrochemical; Waste management; Environmental science; Hydrogen; Unconventional oil; Asphalt; Catalysis; Petroleum engineering; Oil reserves; Economic shortage; Fossil fuel; Process engineering; Engineering; Chemistry; Materials science; Petroleum; Organic chemistry","score_opus":0.02205364078520429,"score_gpt":0.23931271633310844,"score_spread":0.21725907554790413,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3212582886","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.002111454,0.003959205,0.00035142916,0.00008253339,0.00025875663,0.00006846667,0.000038962422,0.00021675466,0.9929124],"genre_scores_gemma":[0.018746182,0.00020433699,0.00061856426,0.000043404838,0.00030303941,0.0000055392884,0.00021723882,0.00021048666,0.9796512],"study_design_codex":"theoretical_or_conceptual","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977357,0.000008083491,0.00075580535,0.00053819804,0.0005691677,0.0003930417],"domain_scores_gemma":[0.9983393,0.0002562407,0.00028038298,0.0008307593,0.00011301814,0.00018028791],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00025298249,0.00050724926,0.0010452013,0.0003332206,0.000028592602,0.000013389542,0.0003708388,0.0005264111,0.0010375775],"category_scores_gemma":[0.00011745715,0.00046520177,0.00055382214,0.00010439817,0.00009618166,0.00008717493,0.00030535605,0.0006633976,0.00010075713],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000099910176,0.000081538885,0.000003760038,0.0047155167,0.0031758773,0.0003158469,0.0010584479,0.00078377256,0.3292094,0.59430003,0.0003952159,0.06586072],"study_design_scores_gemma":[0.0006351803,0.000036965397,7.040791e-7,0.0019642208,0.0006529879,0.00022552093,0.00022625679,0.0005128587,0.8529865,0.0026231597,0.1388567,0.0012789438],"about_ca_topic_score_codex":0.00029659303,"about_ca_topic_score_gemma":0.000058329362,"teacher_disagreement_score":0.5916769,"about_ca_system_score_codex":0.0003313902,"about_ca_system_score_gemma":0.00008890964,"threshold_uncertainty_score":0.9998756},"labels":[],"label_agreement":null},{"id":"W3214263638","doi":"","title":"Technoeconomic Assessment of Optimized Adsorption Processes for Post-Combustion CO 2 Capture in Hydrogen Plants","year":2020,"lang":"en","type":"article","venue":"2020 Virtual AIChE Annual Meeting","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Adsorption; Combustion; Hydrogen; Environmental science; Waste management; Chemistry; Engineering","score_opus":0.011531666120494657,"score_gpt":0.2623257516377139,"score_spread":0.2507940855172192,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3214263638","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9953146,0.00016340223,0.0026165154,0.0004752578,0.000058501155,0.00054788153,0.00036962095,0.00016185227,0.00029234544],"genre_scores_gemma":[0.9963731,0.000024280313,0.002800116,0.0001105481,0.00015977633,0.000086774075,0.00035547002,0.000053070853,0.000036859525],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984211,0.000025920262,0.0006443687,0.00039277997,0.0001869679,0.00032891406],"domain_scores_gemma":[0.9990886,0.00025270265,0.00027538036,0.00014456356,0.0001284376,0.00011032957],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00039716234,0.00023804292,0.0004939566,0.00010969472,0.000034999517,0.000011470666,0.0002575462,0.00019612545,0.00001791291],"category_scores_gemma":[0.0010963709,0.00023700658,0.00010457234,0.00028200672,0.000028537102,0.0003085789,0.000096525575,0.000308346,0.000008726583],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028901678,0.00006414969,0.000636179,0.0006388741,0.000073007286,0.0000044346643,0.0021508,0.048729196,0.94500387,0.00008825163,0.00005281907,0.0022693858],"study_design_scores_gemma":[0.002285647,0.00029061612,0.00010075373,0.00034852888,0.00006103505,0.000011408287,0.0045209914,0.09775428,0.89377236,0.000030265,0.0003791704,0.0004449675],"about_ca_topic_score_codex":0.0000869106,"about_ca_topic_score_gemma":0.000016795266,"teacher_disagreement_score":0.051231544,"about_ca_system_score_codex":0.00015171726,"about_ca_system_score_gemma":0.00010544346,"threshold_uncertainty_score":0.9664848},"labels":[],"label_agreement":null},{"id":"W32851517","doi":"","title":"Palladium-coated Vanadium-alloy membranes for Hydrogen Separation.","year":2024,"lang":"en","type":"article","venue":"OSTI OAI (U.S. Department of Energy Office of Scientific and Technical Information)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"St. Stephen's University","funders":"Los Alamos National Laboratory; Office of Fossil Energy; U.S. Department of Energy","keywords":"Hydrogen; Vanadium; Materials science; Membrane; Alloy; Palladium; Evaporation; Coating; Chemical engineering; Metallurgy; Analytical Chemistry (journal); Inorganic chemistry; Composite material; Catalysis; Chemistry; Chromatography; Thermodynamics","score_opus":0.012184251184525756,"score_gpt":0.24413192889663382,"score_spread":0.23194767771210806,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W32851517","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9314034,0.0022161854,0.02395386,0.00041690835,0.0011068739,0.00090342993,0.0008507326,0.0007259047,0.03842268],"genre_scores_gemma":[0.9950731,0.00004824253,0.0012180706,0.000024088788,0.000035391073,0.00006683347,0.0028605233,0.000016473014,0.00065729005],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99834424,0.000008496499,0.0007428004,0.00023779973,0.00039538668,0.00027125303],"domain_scores_gemma":[0.9990199,0.00020565568,0.00016265262,0.0002791579,0.00019889059,0.00013374559],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046671188,0.00018940706,0.00029802776,0.000347856,0.000113023365,0.00007646401,0.00022211875,0.00014178213,0.000059834718],"category_scores_gemma":[0.00016977175,0.00016417868,0.00016772797,0.000568922,0.0002158412,0.0009088021,0.000089102774,0.00008971329,0.000016971406],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002762894,0.00027178362,0.000101182624,0.003818511,0.00051090133,0.0000059999998,0.000064415544,0.0061276923,0.76691294,0.2093285,0.0042691305,0.008312685],"study_design_scores_gemma":[0.00060568866,0.0001293696,0.0002315594,0.0002204662,0.000158752,0.000040883915,0.000010122439,0.006914438,0.73464847,0.00041219816,0.2562655,0.0003625841],"about_ca_topic_score_codex":0.0000410847,"about_ca_topic_score_gemma":0.000025215728,"teacher_disagreement_score":0.25199637,"about_ca_system_score_codex":0.000071115486,"about_ca_system_score_gemma":0.00009407429,"threshold_uncertainty_score":0.66950125},"labels":[],"label_agreement":null},{"id":"W4200020553","doi":"10.1002/cjce.24333","title":"Dry reforming of methane: Effect of different calcination temperatures of <scp> Al <sub>2</sub> O <sub>3</sub> </scp> and <scp> Mg‐Al <sub>2</sub> O <sub>3</sub> </scp> supports on <scp>Ni</scp> catalysts","year":2021,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Calcination; Catalysis; Space velocity; Methane; Coke; Carbon dioxide reforming; Syngas; Chemistry; Nuclear chemistry; Chemical engineering; Materials science; Analytical Chemistry (journal); Mineralogy; Metallurgy; Selectivity; Organic chemistry","score_opus":0.005351603479934769,"score_gpt":0.2058454715437815,"score_spread":0.20049386806384673,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4200020553","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99487144,0.002562837,0.00024680895,0.0001283271,0.0009908163,0.0007021767,0.0002464034,0.00013050661,0.00012066569],"genre_scores_gemma":[0.9979811,0.0003201005,0.00011897658,0.000102512924,0.0007018842,0.000055809633,0.0002896067,0.00041032923,0.000019737945],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9910344,0.00027462383,0.003101898,0.0011453794,0.0021191284,0.0023245607],"domain_scores_gemma":[0.99036103,0.0035184708,0.0017428243,0.0013564546,0.00089904707,0.0021221386],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.00234778,0.0016864914,0.003062138,0.0016250601,0.00023853712,0.00013604636,0.0012609507,0.001046683,0.0000028647696],"category_scores_gemma":[0.008246598,0.001457047,0.0013115193,0.0017843682,0.00047485414,0.0007901349,0.0004126505,0.003289029,0.000008574825],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000039323288,0.00012677106,0.000376681,0.0015718556,0.0009780321,0.0004962003,0.0013446338,0.0042539854,0.9850122,0.000110770095,0.0004417578,0.005247824],"study_design_scores_gemma":[0.00247266,0.00036128555,0.00067286746,0.0022315616,0.00083409983,0.0010920601,0.0002826271,0.0035727134,0.9877939,0.00007377691,0.0002292521,0.00038315778],"about_ca_topic_score_codex":0.00039188648,"about_ca_topic_score_gemma":0.00052519597,"teacher_disagreement_score":0.0058988174,"about_ca_system_score_codex":0.0016464662,"about_ca_system_score_gemma":0.0009568678,"threshold_uncertainty_score":0.9995882},"labels":[],"label_agreement":null},{"id":"W4207062747","doi":"10.1002/advs.202104972","title":"Stable Cu Catalysts Supported by Two‐dimensional SiO<sub>2</sub> with Strong Metal–Support Interaction","year":2022,"lang":"en","type":"article","venue":"Advanced Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":57,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"National Key Research and Development Program of China; Natural Sciences and Engineering Research Council of Canada; Soochow University; National Natural Science Foundation of China; Foundation for Innovative Research Groups of the National Natural Science Foundation of China; Ministero dello Sviluppo Economico; Beijing Synchrotron Radiation Facility; Government of Canada","keywords":"Catalysis; Calcination; Exfoliation joint; Materials science; Metal; Chemical engineering; Nanoparticle; Nanotechnology; Chemistry; Graphene; Metallurgy; Organic chemistry","score_opus":0.008727916286736992,"score_gpt":0.2523323684896442,"score_spread":0.2436044522029072,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4207062747","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99694765,0.00005754669,0.001115283,0.000048173224,0.0003699161,0.00022566831,0.0000618131,0.00019134654,0.0009825872],"genre_scores_gemma":[0.9982759,0.000001973656,0.0008306148,0.00006278398,0.000026166328,0.00009033244,0.00022516509,0.000042306667,0.00044480566],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968764,0.000021452275,0.00036366793,0.0007320368,0.001257297,0.00074914086],"domain_scores_gemma":[0.99881566,0.000082748134,0.00020808363,0.0005128503,0.00012781579,0.00025283016],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006435381,0.00025581662,0.00028912447,0.0002544703,0.00052400294,0.000030039604,0.0005282493,0.000025017125,0.00017219105],"category_scores_gemma":[0.00012745005,0.00023233455,0.00007650294,0.0014994553,0.00021460977,0.0016529682,0.0004488817,0.00049437577,0.000041541127],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000054329048,0.000056242105,0.00005347416,0.000010032037,0.000019122977,0.0000262598,0.00010544997,0.05642638,0.9389794,0.00007966714,0.000052707794,0.004136948],"study_design_scores_gemma":[0.00064111745,0.000121431105,0.000031111966,0.000016654405,0.000031826305,0.00020804082,0.0002916247,0.0151240295,0.9812799,0.00002501759,0.0018972572,0.00033199677],"about_ca_topic_score_codex":0.00009556231,"about_ca_topic_score_gemma":0.000022842109,"teacher_disagreement_score":0.042300504,"about_ca_system_score_codex":0.00075465225,"about_ca_system_score_gemma":0.00025912534,"threshold_uncertainty_score":0.9474328},"labels":[],"label_agreement":null},{"id":"W4210611660","doi":"10.1139/cjc-2021-0185","title":"Preparation of highly dispersed CuO-ZnO-ZrO<sub>2</sub> catalysts and their improved catalytic performance for hydrogenation of CO<sub>2</sub>","year":2022,"lang":"en","type":"article","venue":"Canadian Journal of Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Calcination; Chemistry; Citric acid; Space velocity; Methanol; Stoichiometry; BET theory; Inorganic chemistry; Dispersion (optics); Specific surface area; Nuclear chemistry; X-ray photoelectron spectroscopy; Yield (engineering); Chemical engineering; Selectivity; Organic chemistry; Materials science; Metallurgy","score_opus":0.006629965136461757,"score_gpt":0.21028526418463456,"score_spread":0.2036552990481728,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4210611660","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985969,0.0005109554,0.00013074909,0.000052830022,0.0001080943,0.00020386597,0.00025381095,0.000010683621,0.00013207497],"genre_scores_gemma":[0.9995046,0.000021797681,0.000028134597,0.000010168593,0.000119525626,0.000023852654,0.0002178469,0.000044727312,0.000029308825],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983555,0.000014433974,0.00078752113,0.0002214716,0.00026195578,0.00035912858],"domain_scores_gemma":[0.99825174,0.000090031055,0.0007341356,0.0002908353,0.00024625091,0.00038700653],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00049486506,0.00023253176,0.000470555,0.00019857848,0.00013638438,0.000013882719,0.00031571163,0.000118379416,0.000007688985],"category_scores_gemma":[0.00022788414,0.00023272651,0.00021712635,0.00027793233,0.00011145061,0.00027351212,0.000038915878,0.0003350934,4.193228e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000093489216,0.000021273629,0.00015461307,0.00061303563,0.00011296354,0.0000051126494,0.0008506212,0.0010227887,0.9944142,0.0000038358253,0.0000508262,0.0026572489],"study_design_scores_gemma":[0.0009315827,0.00009751192,0.000054881813,0.00009097768,0.000083377636,0.00025298007,0.00038769413,0.010326396,0.9873299,0.000019021894,0.00020532712,0.00022036477],"about_ca_topic_score_codex":0.0002121256,"about_ca_topic_score_gemma":0.0002578468,"teacher_disagreement_score":0.009303607,"about_ca_system_score_codex":0.0006214437,"about_ca_system_score_gemma":0.0008169477,"threshold_uncertainty_score":0.9490311},"labels":[],"label_agreement":null},{"id":"W4210923808","doi":"10.3390/catal12020200","title":"Mechanistic Kinetic Modelling Framework for the Conversion of Waste Crude Glycerol to Value-Added Hydrogen-Rich Gas","year":2022,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation; University of Regina","keywords":"Glycerol; Chemistry; Thermodynamics; Catalysis; Adsorption; Steam reforming; Methanation; Methane reformer; Hydrogen; Reaction rate; Oxygen; Physical chemistry; Hydrogen production; Organic chemistry; Physics","score_opus":0.020833212723888432,"score_gpt":0.24763042996756823,"score_spread":0.2267972172436798,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4210923808","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.64386463,0.0005626115,0.35386744,0.00016514609,0.00043905622,0.0008091588,0.00009684257,0.00010555202,0.00008957668],"genre_scores_gemma":[0.99548525,0.000008110789,0.0035487665,0.00009056707,0.00015436359,0.0002954296,0.00010436964,0.00008371701,0.0002294421],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99809706,0.000030076499,0.00046068607,0.00040646864,0.0005363556,0.00046933882],"domain_scores_gemma":[0.9982146,0.00063476176,0.00017032144,0.0007520058,0.000077665296,0.0001506249],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045893193,0.0002460465,0.0003903795,0.00016641855,0.00025441975,0.000010895972,0.0006853116,0.000091288755,0.00007531588],"category_scores_gemma":[0.00031745838,0.0002100177,0.00024743294,0.0006185421,0.000031115538,0.000061000766,0.0004435293,0.00036342564,0.000025255702],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017046963,0.000048098642,0.0000038052567,0.00025901318,0.00015510566,0.0000069746925,0.0010575043,0.49881724,0.49222776,0.006552754,0.00006199782,0.00063926104],"study_design_scores_gemma":[0.00036219117,0.00007720854,2.889231e-7,0.000047312304,0.00018065631,0.000019795372,0.0004216275,0.33620587,0.66018456,0.0013302664,0.0009703065,0.00019992517],"about_ca_topic_score_codex":0.00014457332,"about_ca_topic_score_gemma":0.0000013091777,"teacher_disagreement_score":0.3516206,"about_ca_system_score_codex":0.00028507347,"about_ca_system_score_gemma":0.000043272288,"threshold_uncertainty_score":0.8564273},"labels":[],"label_agreement":null},{"id":"W4211216746","doi":"10.3389/fchem.2022.849505","title":"Highly Dispersed CoO Embedded on Graphitized Ordered Mesoporous Carbon as an Effective Catalyst for Selective Fischer–Tropsch Synthesis of C5+ Hydrocarbons","year":2022,"lang":"en","type":"article","venue":"Frontiers in Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"National Key Research and Development Program of China; Government of Jiangsu Province; Natural Science Foundation of Jiangsu Province; National Natural Science Foundation of China","keywords":"Fischer–Tropsch process; Catalysis; Mesoporous material; Materials science; Carbon fibers; Chemical engineering; Selectivity; Dispersion (optics); Nanotechnology; Chemistry; Organic chemistry; Composite number; Composite material","score_opus":0.004225008153006918,"score_gpt":0.22096709190990244,"score_spread":0.21674208375689552,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4211216746","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9938819,0.0002273993,0.00027490224,0.000035498797,0.00030363118,0.0008236103,0.00021932345,0.00014620545,0.004087549],"genre_scores_gemma":[0.9968355,0.000005437344,0.0008086913,0.000015009489,0.00009426053,0.0014800458,0.00031900866,0.00012511777,0.00031697997],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9975001,0.0000868049,0.0005495565,0.0007603293,0.00050395064,0.0005992311],"domain_scores_gemma":[0.99842304,0.0003923167,0.0002847771,0.00066246133,0.00006096748,0.00017644325],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00042728378,0.0004385659,0.0009051152,0.00022987706,0.00012744249,0.000009531602,0.0005283676,0.00023412863,0.000018729317],"category_scores_gemma":[0.000878438,0.00048186004,0.00032106446,0.0008178212,0.00011883776,0.0000873428,0.00013248142,0.0006882759,4.4825813e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0022408033,0.00047141835,0.00083395955,0.0004142208,0.0006105466,0.000040240528,0.0013343145,0.0014296236,0.9903672,0.000028396636,0.00019232747,0.002036971],"study_design_scores_gemma":[0.0021970456,0.00015699104,0.00005402576,0.00007537658,0.00020368684,0.00002198607,0.001979962,0.015860597,0.9784566,0.00035848154,0.000120750075,0.00051449344],"about_ca_topic_score_codex":0.0004903312,"about_ca_topic_score_gemma":0.000016446573,"teacher_disagreement_score":0.014430974,"about_ca_system_score_codex":0.0010585837,"about_ca_system_score_gemma":0.00011492252,"threshold_uncertainty_score":0.9997633},"labels":[],"label_agreement":null},{"id":"W4212968326","doi":"10.2139/ssrn.3959020","title":"Decarbonizing Methanol Production Via an Electrified Steam or Dry Methane Reformer","year":2021,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Methane; Waste management; Steam reforming; Production (economics); Methanol; Environmental science; Dry gas; Chemistry; Pulp and paper industry; Hydrogen production; Engineering; Economics; Catalysis; Chromatography; Organic chemistry","score_opus":0.015251028762154733,"score_gpt":0.26425140843070666,"score_spread":0.24900037966855193,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4212968326","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96645796,0.0065669585,0.02401287,0.0003907406,0.0008757477,0.00025466736,0.0000019043423,0.00032717027,0.0011119907],"genre_scores_gemma":[0.9846622,0.0023099175,0.0013405612,0.000058247475,0.0016031323,0.000024562636,0.00004569916,0.00016800757,0.009787672],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9945337,0.00017322389,0.0007156147,0.0006008046,0.0006512729,0.0033253604],"domain_scores_gemma":[0.9984662,0.0000748214,0.0002854537,0.0006041645,0.00029528385,0.00027410622],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0026659041,0.00039665183,0.0005405937,0.00031121247,0.00020968882,0.00004301076,0.00041604682,0.0002504288,0.00009909917],"category_scores_gemma":[0.0008029356,0.00031992188,0.00028236,0.0010453459,0.000036117646,0.0008561055,0.000078758356,0.003591671,0.000038934853],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019213086,0.000104716266,0.000034611232,0.000030634845,0.0004258552,0.000045142006,0.00017948764,0.00014026892,0.897412,0.0022345374,0.0000019996028,0.099198624],"study_design_scores_gemma":[0.0009105351,0.00027075852,0.000011918802,0.00006334763,0.00021000931,0.004733379,0.001265429,0.000981736,0.9798018,0.010075804,0.0011678647,0.00050746463],"about_ca_topic_score_codex":0.00014770882,"about_ca_topic_score_gemma":0.0012842107,"teacher_disagreement_score":0.09869116,"about_ca_system_score_codex":0.0029907094,"about_ca_system_score_gemma":0.0025075586,"threshold_uncertainty_score":0.99992526},"labels":[],"label_agreement":null},{"id":"W4213284230","doi":"10.1021/acs.jchemed.1c00957","title":"Methanation of Synthesis Gas to Produce Methane: A Hands-On Catalysis Experiment","year":2022,"lang":"en","type":"article","venue":"Journal of Chemical Education","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"National Natural Science Foundation of China","keywords":"Methanation; Syngas; Methane; Renewable energy; Process engineering; Catalysis; Chemical reaction engineering; Chemistry; Process (computing); Environmental science; Chemical engineering; Waste management; Biochemical engineering; Organic chemistry; Engineering; Computer science","score_opus":0.012746635075069231,"score_gpt":0.28548819255056196,"score_spread":0.2727415574754927,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4213284230","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99762505,0.0002228954,0.00015344424,0.0010091418,0.00034991812,0.00014556927,0.0000039540287,0.00001421023,0.0004758231],"genre_scores_gemma":[0.9977725,0.0000054738607,0.0015814336,0.000058698544,0.0002928008,0.00009446036,0.000014668481,0.000027139113,0.00015282875],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980768,0.000057001394,0.0007050266,0.00019740826,0.0007839848,0.0001798025],"domain_scores_gemma":[0.998528,0.00023061571,0.0005245782,0.0002917891,0.0002582189,0.00016681166],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008400283,0.00014793118,0.00039695157,0.00046555747,0.000031836145,0.000007096566,0.00033657433,0.00004851756,0.00019139789],"category_scores_gemma":[0.0018967288,0.00013595822,0.0002384263,0.0006707659,0.000016896007,0.00013656869,0.00009435256,0.0003142713,0.000005292618],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016318072,0.00048120169,0.000012153941,0.000050608916,0.00009983545,0.0000010658797,0.0012600436,0.00070160883,0.97516954,0.000096299416,0.00045435954,0.021510104],"study_design_scores_gemma":[0.00023361426,0.00014344287,0.000007000724,0.00007327265,0.0001325454,0.00006426005,0.0007589094,0.00013178919,0.9965793,0.00008910168,0.0016529682,0.00013383018],"about_ca_topic_score_codex":0.000043801745,"about_ca_topic_score_gemma":2.1842736e-7,"teacher_disagreement_score":0.021409728,"about_ca_system_score_codex":0.0007840988,"about_ca_system_score_gemma":0.0002461115,"threshold_uncertainty_score":0.55442154},"labels":[],"label_agreement":null},{"id":"W4214561195","doi":"10.1016/j.cattod.2022.02.006","title":"Tri-reforming of methane for syngas production using Ni catalysts: Current status and future outlook","year":2022,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":84,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Syngas; Carbon dioxide reforming; Catalysis; Steam reforming; Coke; Methane; Methane reformer; Partial oxidation; Raw material; Catalytic reforming; Chemical engineering; Process engineering; Waste management; Chemistry; Hydrogen production; Organic chemistry; Engineering","score_opus":0.019873225114102264,"score_gpt":0.27497904540832535,"score_spread":0.2551058202942231,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4214561195","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9889544,0.008051654,0.00069140655,0.00011116403,0.0012263089,0.00062341965,0.00018033442,0.00011417236,0.00004713303],"genre_scores_gemma":[0.99633116,0.00018751013,0.000890787,0.000009637748,0.00079547503,0.00024168719,0.0010064164,0.00010056729,0.00043674713],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9975189,0.000050027,0.0007185942,0.00062362116,0.00050792645,0.0005809107],"domain_scores_gemma":[0.9985631,0.00007223325,0.00040506737,0.00064164755,0.00014263092,0.00017530676],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00087619066,0.00032404147,0.0006931711,0.00047917917,0.00022527008,0.000012040771,0.000267118,0.000070349095,0.00003576728],"category_scores_gemma":[0.0003147206,0.00030659363,0.0003036788,0.000882441,0.00006903198,0.0003532696,0.00034365724,0.00040624125,0.0000021379665],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017254202,0.00020042036,0.00035998484,0.0009199315,0.0004947934,0.000004533589,0.0028624458,0.001883745,0.87954205,0.00024388051,0.00004947866,0.11326616],"study_design_scores_gemma":[0.0011842849,0.00008339986,0.000044862394,0.00006753177,0.00093159365,0.00010663279,0.003374437,0.0033846593,0.9523891,0.00010484576,0.03773439,0.0005942275],"about_ca_topic_score_codex":0.00038478858,"about_ca_topic_score_gemma":0.000020684669,"teacher_disagreement_score":0.112671934,"about_ca_system_score_codex":0.00067045004,"about_ca_system_score_gemma":0.00010968357,"threshold_uncertainty_score":0.9999386},"labels":[],"label_agreement":null},{"id":"W4220744211","doi":"10.1002/cssc.202200436","title":"Using Biomass Gasification Mineral Residue as Catalyst to Produce Light Olefins from CO, CO<sub>2</sub>, and H<sub>2</sub> Mixtures","year":2022,"lang":"en","type":"article","venue":"ChemSusChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Enerkem (Canada)","funders":"Nederlandse Organisatie voor Wetenschappelijk Onderzoek; Universiteit Utrecht","keywords":"Catalysis; Residue (chemistry); Biomass (ecology); Chemistry; Chemical engineering; Heterogeneous catalysis; Materials science; Organic chemistry","score_opus":0.018996955831770794,"score_gpt":0.25573792631873693,"score_spread":0.23674097048696613,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4220744211","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99644345,0.00086769037,0.00019644777,0.0005715519,0.00027682164,0.00053969695,0.00020921914,0.00032727138,0.0005678776],"genre_scores_gemma":[0.9972664,0.000014919164,0.000468728,0.00010649141,0.0005838533,0.00017203778,0.0011117146,0.00016364474,0.00011222225],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9966285,0.000056227636,0.00066551135,0.001153778,0.0007377772,0.00075817475],"domain_scores_gemma":[0.9980979,0.000115758856,0.00026143854,0.0009925838,0.00011306121,0.0004192495],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00045185143,0.00054811937,0.0006031578,0.00034558726,0.00038297696,0.00007829565,0.00050554815,0.00022119895,0.000031735974],"category_scores_gemma":[0.0004281217,0.000597378,0.00018850228,0.0008401253,0.00008509393,0.00028851564,0.0004462738,0.0006284447,0.00008707905],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001170636,0.0001009315,0.00032333896,0.00014063163,0.000108589666,0.000050397637,0.0010928138,0.000116428695,0.9954304,0.00003865924,0.00131021,0.0011705247],"study_design_scores_gemma":[0.0007144,0.00004452358,0.0002838794,0.000070881746,0.0001226855,0.00013360682,0.00030445066,0.00066194916,0.9912864,0.000052929438,0.0055898083,0.00073450885],"about_ca_topic_score_codex":0.0004961073,"about_ca_topic_score_gemma":0.00009087931,"teacher_disagreement_score":0.004279598,"about_ca_system_score_codex":0.0006787831,"about_ca_system_score_gemma":0.00013466045,"threshold_uncertainty_score":0.99964774},"labels":[],"label_agreement":null},{"id":"W4220973683","doi":"10.3390/catal12040363","title":"Prospects and Technical Challenges in Hydrogen Production through Dry Reforming of Methane","year":2022,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":56,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Syngas; Carbon dioxide reforming; Greenhouse gas; Hydrogen production; Environmental science; Methane; Enabling; Steam reforming; Raw material; Production (economics); Waste management; Process engineering; Hydrogen; Chemistry; Engineering","score_opus":0.02875700915151397,"score_gpt":0.25895024844933845,"score_spread":0.23019323929782448,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4220973683","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9903815,0.007151462,0.000008380663,0.00023493239,0.0001166136,0.00031934862,0.0000075583043,0.00011371066,0.0016665027],"genre_scores_gemma":[0.9990674,0.000215995,0.0002675856,0.000004885671,0.00007049975,0.00014087257,0.000041391642,0.00003774979,0.00015362122],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99853396,0.000029830546,0.00039658838,0.00042259772,0.00032843,0.00028857918],"domain_scores_gemma":[0.99931496,0.000040765513,0.00013172669,0.0004359112,0.000025064652,0.00005157023],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006035692,0.0001635764,0.00036040327,0.00018449439,0.000044352866,0.000001837881,0.000205841,0.000072579605,0.000010440549],"category_scores_gemma":[0.0002607905,0.00015980648,0.00007105022,0.00047486494,0.00006060224,0.00023518424,0.00039416066,0.00037476234,0.0000024807694],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004176749,0.0000898737,0.00039832512,0.00030931545,0.000034650206,0.000025808567,0.0016455454,0.00021890464,0.987044,0.001014031,0.000002815528,0.009175006],"study_design_scores_gemma":[0.000384923,0.00005412618,0.00029927286,0.00006431939,0.00003007255,0.0002575667,0.0007253028,0.00012498457,0.99641865,0.00054746476,0.00088052644,0.00021281333],"about_ca_topic_score_codex":0.00017091102,"about_ca_topic_score_gemma":0.00006933488,"teacher_disagreement_score":0.009374671,"about_ca_system_score_codex":0.00031570924,"about_ca_system_score_gemma":0.000030518793,"threshold_uncertainty_score":0.65167195},"labels":[],"label_agreement":null},{"id":"W4221105210","doi":"10.1002/ese3.1107","title":"The application of nonthermal plasma in methanol synthesis via CO<sub>2</sub> hydrogenation","year":2022,"lang":"en","type":"article","venue":"Energy Science & Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Natural Resources Canada; Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Methane; Renewable energy; Methanol; Combustion; Gasoline; Process engineering; Nonthermal plasma; Chemistry; Environmental science; Nanotechnology; Chemical engineering; Materials science; Plasma; Organic chemistry; Engineering; Physics","score_opus":0.004556461688578896,"score_gpt":0.2020764516916114,"score_spread":0.1975199900030325,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4221105210","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97215676,0.000113664544,0.02710659,0.00003435168,0.00015892809,0.00009087908,0.0000047126246,0.0000951918,0.00023894137],"genre_scores_gemma":[0.99939764,0.0000080449945,0.00023365788,0.0000041383396,0.00003953551,0.00027155795,0.000005054562,0.00002871893,0.000011661278],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99830174,0.000019909412,0.00034270447,0.00028832967,0.0006380008,0.00040929133],"domain_scores_gemma":[0.99917316,0.00026866075,0.000108322434,0.0003450303,0.000034181623,0.00007063186],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011554515,0.00014570792,0.00017362961,0.00036478628,0.00020082321,0.000013770424,0.00062094996,0.000037211823,0.000004945646],"category_scores_gemma":[0.0002619376,0.00013286625,0.00007181883,0.0013426411,0.00008457914,0.00025368397,0.00018401918,0.00020185437,0.0000026934893],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000040194554,0.0000098809,0.000014323839,0.000002244591,0.000005362863,0.0000010251545,0.00007066447,0.32503262,0.645883,0.014836237,1.5755428e-7,0.014140434],"study_design_scores_gemma":[0.00006533425,0.0000064394967,0.000077980985,0.0000057534876,0.0000045070233,0.000010949479,0.000035005418,0.34411743,0.653508,0.000013175991,0.0020550855,0.00010031774],"about_ca_topic_score_codex":0.00016729097,"about_ca_topic_score_gemma":0.000036743822,"teacher_disagreement_score":0.027240891,"about_ca_system_score_codex":0.00046826323,"about_ca_system_score_gemma":0.00005486549,"threshold_uncertainty_score":0.54181284},"labels":[],"label_agreement":null},{"id":"W4221120027","doi":"10.1016/j.cattod.2022.03.022","title":"Dual site contiguity study for CO2 catalytic activation and CO2 reforming of CH4 over Ni and NiM2 catalysts with MgO-spinel support","year":2022,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada); University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Spinel; Dual (grammatical number); Contiguity; Chemical engineering; Heterogeneous catalysis; Materials science; Chemistry; Inorganic chemistry; Metallurgy; Organic chemistry","score_opus":0.012072754002427216,"score_gpt":0.24794977147758035,"score_spread":0.23587701747515313,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4221120027","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99811536,0.00012647279,0.0002962128,0.000051211246,0.00007176215,0.0008699589,0.00022400111,0.00008405193,0.00016094779],"genre_scores_gemma":[0.99636257,0.0000052935015,0.00009926476,0.000024851182,0.0000707401,0.00026794054,0.0021687625,0.00007619342,0.00092439656],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976038,0.00003473136,0.00066085416,0.00067768275,0.00057870406,0.00044426313],"domain_scores_gemma":[0.99843526,0.00017777165,0.00040642938,0.00066668494,0.00013580077,0.00017806157],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00082077825,0.00036884018,0.00079694623,0.000338925,0.00029287147,0.000027069389,0.00021251364,0.000084890446,0.000027904654],"category_scores_gemma":[0.00023653288,0.00032699262,0.00012921932,0.0006149216,0.00012697908,0.00045925388,0.00045433125,0.00030988475,0.0000013312449],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010559994,0.0010029353,0.042796154,0.0011477987,0.002038623,0.00007411221,0.01594976,0.0007482359,0.92611957,0.00020218018,0.0002883847,0.008576224],"study_design_scores_gemma":[0.009891313,0.0014047578,0.0171358,0.00013501443,0.0021808632,0.00031761688,0.008813901,0.006198578,0.94818336,0.00004300074,0.0040846285,0.0016111874],"about_ca_topic_score_codex":0.0011373664,"about_ca_topic_score_gemma":0.00020155382,"teacher_disagreement_score":0.02566035,"about_ca_system_score_codex":0.00033248693,"about_ca_system_score_gemma":0.000082405175,"threshold_uncertainty_score":0.9999182},"labels":[],"label_agreement":null},{"id":"W4224000901","doi":"10.1016/j.cattod.2022.04.008","title":"Metallosilicates as an iron support to catalyze Fischer-Tropsch synthesis","year":2022,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; Polytechnique Montréal","funders":"Canada Research Chairs; Canada Foundation for Innovation","keywords":"Fischer–Tropsch process; Catalysis; Syngas; Selectivity; Cobalt; Molecular sieve; Chemistry; Inorganic chemistry; Chemical engineering; Nuclear chemistry; Materials science; Organic chemistry","score_opus":0.011756027495198362,"score_gpt":0.25437520141922665,"score_spread":0.2426191739240283,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4224000901","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.993088,0.00015755626,0.00019654003,0.00063053577,0.00020288552,0.00033758717,0.00014495739,0.00047592339,0.0047659823],"genre_scores_gemma":[0.98991704,0.0000054613456,0.00051677297,0.00024989227,0.0001647247,0.0007892291,0.0010497334,0.00014691356,0.0071602133],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99669135,0.00009390317,0.000630448,0.00095636724,0.0008501431,0.0007778121],"domain_scores_gemma":[0.9973966,0.00020887416,0.00015431209,0.0015948925,0.000071277136,0.0005740574],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00082227314,0.00044357055,0.0007023614,0.00046761805,0.0003523917,0.000048052156,0.0012033299,0.00011030266,0.0042370763],"category_scores_gemma":[0.00066112354,0.00044543904,0.00044354243,0.0012843632,0.000051978834,0.00042881514,0.00086332177,0.0005009173,0.0011918807],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007202552,0.000315618,0.0002955207,0.00006632167,0.00034166244,0.0000868529,0.0014945724,0.0026359204,0.9814574,0.00042988232,0.0005787193,0.012225466],"study_design_scores_gemma":[0.00025249613,0.0001299532,0.00011281106,0.0000094159495,0.0005251857,0.00013122604,0.0008592816,0.00091814785,0.93112624,0.000053712192,0.065117456,0.000764072],"about_ca_topic_score_codex":0.0009463687,"about_ca_topic_score_gemma":0.00004999884,"teacher_disagreement_score":0.06453873,"about_ca_system_score_codex":0.00058077346,"about_ca_system_score_gemma":0.000087128385,"threshold_uncertainty_score":0.9997997},"labels":[],"label_agreement":null},{"id":"W4225137944","doi":"10.11159/iceptp22.171","title":"Preparation of Cu/ZnO/SBA-15 Catalyst for Methanol Synthesis via CO2 Hydrogenation at Low Pressure: Effect of Calcination Temperature","year":2022,"lang":"en","type":"article","venue":"Proceedings of the World Congress on Civil, Structural, and Environmental Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"State Education Development Agency Republic of Latvia; European Regional Development Fund","keywords":"Calcination; Catalysis; Methanol; Materials science; Chemical engineering; Inorganic chemistry; Chemistry; Organic chemistry","score_opus":0.003284008115045571,"score_gpt":0.20617163161083218,"score_spread":0.20288762349578662,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4225137944","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9984647,0.00030955698,0.000015039346,0.00001979865,0.00024768675,0.00067209336,0.00018959165,0.00003429598,0.000047248046],"genre_scores_gemma":[0.99923426,0.000011689836,0.000112260735,0.000002532099,0.00003397235,0.00018963793,0.000054353284,0.000046323392,0.00031497527],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985994,0.000010601343,0.00042602656,0.0002978207,0.00045270417,0.00021342446],"domain_scores_gemma":[0.99917185,0.00021467757,0.00038136446,0.00015807677,0.000021742617,0.00005227906],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026937504,0.00026873266,0.00043446067,0.00019610682,0.00013227387,0.00000865324,0.00027437723,0.000070134316,0.000033538257],"category_scores_gemma":[0.00012776215,0.0002180083,0.0001804044,0.0002324818,0.00006624209,0.0002142365,0.0002489739,0.00019621736,1.6663027e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000211829,0.000015918047,0.0005506671,0.0011239185,0.00016638736,1.266887e-7,0.00016211404,0.043998737,0.9532095,0.00017739696,0.000017434173,0.0003659316],"study_design_scores_gemma":[0.0005015744,0.000109387176,0.0005990171,0.00014760715,0.00020895326,0.000015265767,0.000054258948,0.08310545,0.91496354,0.000014699293,0.000093065915,0.00018716267],"about_ca_topic_score_codex":0.000018288727,"about_ca_topic_score_gemma":0.0000053297435,"teacher_disagreement_score":0.03910672,"about_ca_system_score_codex":0.00022128566,"about_ca_system_score_gemma":0.000004002845,"threshold_uncertainty_score":0.889012},"labels":[],"label_agreement":null},{"id":"W4229024730","doi":"10.1016/j.fuel.2022.124246","title":"Verification of a 0D model for the heat and mass transfer inside a moving spherical catalyst for steam methane reforming","year":2022,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Steam reforming; Mass transfer; Methane; Particle (ecology); Thermal conduction; Diffusion; Heat transfer; Thermodynamics; Catalysis; Work (physics); Convection; Chemistry; Particle size; Mechanics; Materials science; Physical chemistry; Physics; Organic chemistry; Hydrogen production","score_opus":0.02469514454765875,"score_gpt":0.25129933617748634,"score_spread":0.2266041916298276,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4229024730","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.40561366,0.0016969626,0.59083223,0.00023735747,0.00012831183,0.00104667,0.00022575716,0.00008097972,0.00013803803],"genre_scores_gemma":[0.9939668,0.00002516307,0.0047317254,0.00003584779,0.00006244485,0.000714545,0.00008485085,0.000052365147,0.0003262608],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9989038,0.000013608948,0.00034907658,0.0002516267,0.00021588028,0.00026601925],"domain_scores_gemma":[0.9992319,0.0003074332,0.000043526885,0.0003104127,0.000048646274,0.000058115427],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00049838854,0.0001457234,0.0002782036,0.000056536526,0.00013286399,0.000006464392,0.00020772364,0.000054472235,0.0000085859765],"category_scores_gemma":[0.00015267747,0.00011476097,0.00016181312,0.00018193829,0.000034500707,0.0001239462,0.000073094205,0.00017525545,3.0017998e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021376355,0.00003130325,0.000011491633,0.00045157145,0.00008802401,4.994123e-7,0.0020181804,0.032932177,0.95742273,0.0006906344,0.000007066834,0.006132529],"study_design_scores_gemma":[0.0008401758,0.000058671863,0.000005639999,0.000016448445,0.00012006088,0.000014364941,0.001093972,0.7642618,0.23101193,0.0004098139,0.0020140256,0.00015311608],"about_ca_topic_score_codex":0.00015138843,"about_ca_topic_score_gemma":0.000019581596,"teacher_disagreement_score":0.7313296,"about_ca_system_score_codex":0.00017615002,"about_ca_system_score_gemma":0.000045040233,"threshold_uncertainty_score":0.46798164},"labels":[],"label_agreement":null},{"id":"W4229081365","doi":"10.1021/acsami.2c01959","title":"Reverse Microemulsion-Synthesized High-Surface-Area Cu/γ-Al<sub>2</sub>O<sub>3</sub> Catalyst for CO<sub>2</sub> Conversion via Reverse Water Gas Shift","year":2022,"lang":"en","type":"article","venue":"ACS Applied Materials & Interfaces","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":29,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Catalysis; Microemulsion; Calcination; Materials science; Selectivity; Water-gas shift reaction; Space velocity; Chemical engineering; Analytical Chemistry (journal); Chemistry; Chromatography; Organic chemistry","score_opus":0.00985259474511265,"score_gpt":0.21410687364664402,"score_spread":0.20425427890153136,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4229081365","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9916963,0.00013945193,0.00028018875,0.000605157,0.0021611808,0.0025029194,0.0017458862,0.00080081105,0.00006810278],"genre_scores_gemma":[0.9945696,0.00026518144,0.00029865667,0.00046723778,0.00032472835,0.0009838085,0.0025273145,0.0005018102,0.000061675186],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99246377,0.00022649333,0.0021025036,0.0020104768,0.0011586472,0.0020381263],"domain_scores_gemma":[0.9962325,0.00055734924,0.0008890091,0.0016901277,0.00019403624,0.00043695405],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0019160224,0.0015121124,0.002139555,0.00046973195,0.00076448655,0.00024369583,0.0015072218,0.0006014838,0.0005044005],"category_scores_gemma":[0.00017518735,0.0013856342,0.00035571566,0.000452517,0.000302927,0.00064891594,0.0018493093,0.0008592315,0.0011979125],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0023759273,0.00024256637,0.0000036100425,0.00093367393,0.0004816715,0.000059439735,0.001275393,0.00062498235,0.9891292,0.00006107438,0.003496932,0.0013155602],"study_design_scores_gemma":[0.0034534456,0.00017719502,0.0000052193222,0.00024893804,0.00054416084,0.00009368241,0.0006225026,0.00006576557,0.98795414,0.00027864738,0.004828116,0.0017281799],"about_ca_topic_score_codex":0.00027735575,"about_ca_topic_score_gemma":0.000035457582,"teacher_disagreement_score":0.003768771,"about_ca_system_score_codex":0.0011889911,"about_ca_system_score_gemma":0.00010131846,"threshold_uncertainty_score":0.9997628},"labels":[],"label_agreement":null},{"id":"W4235780819","doi":"10.1016/s1464-2859(16)30325-x","title":"Xebec compact PSA hydrogen purification for industry, fuel cells","year":2016,"lang":"en","type":"article","venue":"Fuel Cells Bulletin","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Fuel cells; Hydrogen; Engineering; Waste management; Process engineering; Environmental science; Mechanical engineering; Materials science; Chemistry; Chemical engineering; Organic chemistry","score_opus":0.017137621122821956,"score_gpt":0.23562141005383402,"score_spread":0.21848378893101206,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4235780819","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9275408,0.0022746492,0.013489421,0.01123102,0.0024742037,0.0033177931,0.00085885555,0.0016811081,0.037132178],"genre_scores_gemma":[0.9743785,0.00006657283,0.0010268867,0.00011649508,0.0006254905,0.00007284265,0.000066650384,0.00012809728,0.023518458],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980243,0.000029880897,0.0005001999,0.00049883756,0.00030787327,0.0006389255],"domain_scores_gemma":[0.99851066,0.0003063024,0.0001964656,0.00063821307,0.00008984031,0.00025852595],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.0003919943,0.0003288172,0.00037295438,0.00012781526,0.00006190311,0.000025344245,0.00044046692,0.00044331508,0.0013240763],"category_scores_gemma":[0.00013990758,0.00025186656,0.0002477317,0.00016391215,0.000065087406,0.00007794122,0.00007516422,0.00033256423,0.0022078417],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000447171,0.00007112243,0.000029717097,0.0002616518,0.00005171878,0.000004134863,0.00011173508,0.00011914215,0.98944134,0.00012956031,0.0072276606,0.0025074962],"study_design_scores_gemma":[0.0006566329,0.000026303807,0.000013272702,0.00006431129,0.000032395586,0.0000060128464,0.000024332445,0.00016959159,0.6046141,0.000088996385,0.3940471,0.00025694026],"about_ca_topic_score_codex":0.00016261154,"about_ca_topic_score_gemma":0.000006851573,"teacher_disagreement_score":0.38681945,"about_ca_system_score_codex":0.0002631493,"about_ca_system_score_gemma":0.000040549854,"threshold_uncertainty_score":0.9999934},"labels":[],"label_agreement":null},{"id":"W4237338049","doi":"10.22541/au.159130083.34579112","title":"0.5 wt% Ru/γ-Al 2 O 3 is a highly active and stable catalyst for direct conversion of biogas into renewable natural gas","year":2020,"lang":"en","type":"preprint","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Catalysis; Biogas; Renewable energy; Selectivity; Natural gas; Methane; Power to gas; Chemical engineering; Materials science; Renewable natural gas; Impurity; Electrolysis; Chemistry; Waste management; Organic chemistry; Fuel gas; Engineering; Physical chemistry","score_opus":0.013373998862203591,"score_gpt":0.24829833964487022,"score_spread":0.23492434078266664,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4237338049","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9637097,0.0030567187,0.007360001,0.0032466692,0.0022341711,0.0033018126,0.0018787275,0.0010069573,0.014205225],"genre_scores_gemma":[0.9916748,0.00018299372,0.0042586764,0.00011798022,0.00015754809,0.00007982896,0.001055035,0.00010212211,0.0023710537],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99785775,0.000016659244,0.0005268882,0.00082870305,0.00034916075,0.00042082314],"domain_scores_gemma":[0.99851537,0.00024213703,0.00030913923,0.00053754525,0.00018658729,0.00020925155],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001765567,0.00047384354,0.0009856019,0.00021905593,0.00006820194,0.000029172912,0.00037550865,0.00036576873,0.000063066036],"category_scores_gemma":[0.00028323315,0.0004206411,0.00035694387,0.00023166453,0.00008527725,0.00020561519,0.0012496717,0.0005352569,0.000008465839],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00046018115,0.00004561071,0.000028693135,0.0027448789,0.00070231705,0.0000073612155,0.0016729955,0.00024629442,0.9900414,0.00024944698,0.0025177335,0.001283121],"study_design_scores_gemma":[0.00080167,0.000052535575,0.0000045082934,0.00025573125,0.00021709202,0.0000056233876,0.00030616467,0.013053589,0.9660412,0.00041346237,0.018395897,0.00045252396],"about_ca_topic_score_codex":0.014310347,"about_ca_topic_score_gemma":0.00012940678,"teacher_disagreement_score":0.027965045,"about_ca_system_score_codex":0.0003982306,"about_ca_system_score_gemma":0.00012846707,"threshold_uncertainty_score":0.9998245},"labels":[],"label_agreement":null},{"id":"W4237562035","doi":"10.5383/ijtee.07.02.007","title":"Analysis of a modular high efficiency Polygeneration System in a Science and Technological Park","year":2014,"lang":"en","type":"article","venue":"International Journal of Thermal and Environmental Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"European Commission","keywords":"Chiller; Cogeneration; Modular design; Renewable energy; Process engineering; Electricity; Absorption refrigerator; Water cooling; Efficient energy use; Fossil fuel; Engineering; Environmental science; Electricity generation; Waste management; Mechanical engineering; Refrigeration; Computer science; Power (physics); Electrical engineering","score_opus":0.003055415010687901,"score_gpt":0.17770342340388506,"score_spread":0.17464800839319716,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4237562035","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9915465,0.00013898464,0.008176718,0.00001813846,0.00006892118,0.000021161823,0.0000037246969,0.000007798219,0.000018065428],"genre_scores_gemma":[0.9994651,0.000016334416,0.00047330413,0.0000031193686,0.000031875574,0.000001039835,0.0000019102115,0.0000051877264,0.000002142823],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99916863,0.000005634333,0.00027985248,0.00009462114,0.00035519875,0.000096060045],"domain_scores_gemma":[0.99975306,0.000031488282,0.00009933672,0.000055686833,0.000015349355,0.000045066536],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045829773,0.0000741245,0.0001797319,0.0004951327,0.000013102621,0.00001014108,0.00016530493,0.000036131754,0.000003897862],"category_scores_gemma":[0.00008391563,0.00006036966,0.000043755026,0.00019541364,0.000079347185,0.00015240334,0.00008414931,0.000102319005,1.862721e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000009803476,0.00001718895,0.0022282088,0.000008265241,0.000081378304,0.000005439301,0.000058760514,0.19292386,0.7986528,0.0005426772,1.11515766e-8,0.00547159],"study_design_scores_gemma":[0.00029452232,0.000029606836,0.026401721,0.00005435904,0.000061429215,0.00006564419,0.00008103264,0.820662,0.15225722,0.0000032877276,0.0000151086715,0.00007402444],"about_ca_topic_score_codex":0.000020884081,"about_ca_topic_score_gemma":4.5085082e-7,"teacher_disagreement_score":0.64639556,"about_ca_system_score_codex":0.00017087687,"about_ca_system_score_gemma":0.0000042104584,"threshold_uncertainty_score":0.24618033},"labels":[],"label_agreement":null},{"id":"W4239720415","doi":"10.1149/ma2013-01/8/451","title":"Comparison of Novel Anode Materials for the Production of Hydrogen Using CuCl/HCl Electrolyzers","year":2013,"lang":"en","type":"article","venue":"ECS Meeting Abstracts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Anode; Hydrogen production; Production (economics); Hydrogen; Materials science; Process engineering; Chemical engineering; Chemistry; Electrode; Engineering; Organic chemistry; Physical chemistry; Economics","score_opus":0.03446559703069429,"score_gpt":0.2916101447870585,"score_spread":0.2571445477563642,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4239720415","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99834955,0.00014502276,0.00014067594,0.00006164129,0.00028205407,0.00045751038,0.000008659488,0.0000494224,0.0005054838],"genre_scores_gemma":[0.9967009,0.0000022161073,0.0029674277,0.0000032667074,0.00020152297,0.000025150943,0.00001031882,0.00004147855,0.000047710077],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985386,0.000010667901,0.0006793898,0.00019386591,0.00027609165,0.00030139208],"domain_scores_gemma":[0.9986769,0.00027106423,0.0005427892,0.00028094937,0.00018710003,0.00004117817],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007778586,0.00015054872,0.0003553013,0.000070244096,0.00006621786,0.000011620215,0.00019072031,0.00008937426,0.0000116869805],"category_scores_gemma":[0.0014544282,0.000116270494,0.000094125455,0.00014020785,0.00004589205,0.00014113983,0.000041738356,0.00011756164,0.0000035419089],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017379863,0.000057820453,0.000085714986,0.00018724658,0.00005698594,5.335697e-8,0.00025706002,0.11275215,0.8863693,0.0000053394274,0.000016468597,0.00019446938],"study_design_scores_gemma":[0.0002067546,0.000019940953,0.00016491767,0.00017805504,0.00007432147,0.0000076096308,0.0001590769,0.02567349,0.9732995,0.000014316389,0.00008589035,0.000116099334],"about_ca_topic_score_codex":0.0010381378,"about_ca_topic_score_gemma":0.000005435552,"teacher_disagreement_score":0.08707866,"about_ca_system_score_codex":0.000090058864,"about_ca_system_score_gemma":0.000032221036,"threshold_uncertainty_score":0.4741373},"labels":[],"label_agreement":null},{"id":"W4241123771","doi":"10.1002/cjce.22987","title":"Issue Highlights","year":2018,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Biomass (ecology); USable; Citation; Download; Computer science; Process engineering; Operations research; Library science; World Wide Web; Engineering","score_opus":0.0075029864243753575,"score_gpt":0.20255513681956924,"score_spread":0.19505215039519389,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4241123771","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9924547,0.0005816554,0.0012156981,0.0018071362,0.0016194216,0.00008502495,0.0000054572843,0.00006362519,0.0021672817],"genre_scores_gemma":[0.99695045,9.4841e-7,0.000552097,0.00007056754,0.0021578202,0.0000012201745,0.0000013182296,0.000040295097,0.00022526104],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988571,0.0000060897437,0.00037778314,0.00009539181,0.00022735739,0.00043632556],"domain_scores_gemma":[0.99885654,0.00008458848,0.000097348326,0.0002409544,0.00016233788,0.0005582518],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00030598388,0.00016145944,0.00023971724,0.0001709395,0.00006778295,0.000030420833,0.0005326836,0.00010748352,0.00023109367],"category_scores_gemma":[0.00044803155,0.00011271851,0.00014206757,0.00028998757,0.000107338674,0.00013616121,0.000024863077,0.0004510317,0.00009849793],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000009870146,0.0000042034894,0.000016552101,0.000029739185,0.00009690673,0.000059219077,0.00060049706,0.00093319156,0.9935205,0.0027697927,0.0007299911,0.001229524],"study_design_scores_gemma":[0.0002081594,0.00002172101,0.000009406853,0.00009160353,0.000034895285,0.00040918312,0.0000082292845,0.0053627,0.93246603,0.00008063333,0.061142273,0.00016518008],"about_ca_topic_score_codex":0.0010686016,"about_ca_topic_score_gemma":0.00017172465,"teacher_disagreement_score":0.061054498,"about_ca_system_score_codex":0.0003369716,"about_ca_system_score_gemma":0.0001904544,"threshold_uncertainty_score":0.45965275},"labels":[],"label_agreement":null},{"id":"W4241380064","doi":"10.1016/b978-0-12-824372-5.00017-8","title":"Exergy analyses of hydrogen production systems","year":2020,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Exergy; Hydrogen production; Energy carrier; Process engineering; Hydrogen technologies; Hydrogen; Production (economics); Work (physics); Hydrogen economy; Hydrogen fuel; Exergy efficiency; Environmental science; Electricity; Process (computing); Biochemical engineering; Waste management; Computer science; Engineering; Chemistry; Mechanical engineering; Economics","score_opus":0.03355274752942337,"score_gpt":0.26396974375763355,"score_spread":0.23041699622821019,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4241380064","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00067210005,0.0038558745,0.0000118582475,0.000016770071,0.00049338624,0.00044017602,0.000036311216,0.0001941867,0.9942793],"genre_scores_gemma":[0.028892448,0.00006001579,0.00005782401,0.000009087156,0.0009120775,0.000031777512,0.00009383389,0.00017789949,0.969765],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9979735,0.000011959864,0.0007815274,0.0005167704,0.0004809821,0.00023525079],"domain_scores_gemma":[0.998592,0.000031454823,0.0004653006,0.0006600051,0.00011043704,0.0001408062],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00015486016,0.0004376708,0.0009730553,0.00021635022,0.00003103927,0.0000082190945,0.00029715884,0.0003322995,0.000048410137],"category_scores_gemma":[0.000082575745,0.0004005169,0.00043811297,0.00003588786,0.000070642134,0.00004977697,0.00014640737,0.00044741374,0.000105859726],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000031497548,0.000009110399,9.244402e-7,0.0021798755,0.0011601982,0.00004269229,0.00022534588,0.0005330298,0.46000078,0.0042456426,0.000024438108,0.5315465],"study_design_scores_gemma":[0.00015124123,0.00003261794,1.5136922e-7,0.0010989545,0.00059323123,0.00005933936,0.000013911437,0.0003326111,0.4168527,0.00043753834,0.57989234,0.00053537503],"about_ca_topic_score_codex":0.0000071830173,"about_ca_topic_score_gemma":0.0000027683966,"teacher_disagreement_score":0.5798679,"about_ca_system_score_codex":0.00017082294,"about_ca_system_score_gemma":0.0000583572,"threshold_uncertainty_score":0.9998447},"labels":[],"label_agreement":null},{"id":"W4245801234","doi":"10.2172/889655","title":"COST-EFFECTIVE METHOD FOR PRODUCING SELF SUPPORTED PALLADIUM ALLOY MEMBRANES FOR USE IN EFFICIENT PRODUCTION OF COAL DERIVED HYDROGEN","year":2006,"lang":"en","type":"report","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Investment (military); Production (economics); Work (physics); Coal; Return on investment; Production cost; Key (lock); Membrane; Business; Engineering; Operations management; Process engineering; Computer science; Waste management; Chemistry; Economics; Mechanical engineering; Political science; Microeconomics; Computer security","score_opus":0.03910315538319198,"score_gpt":0.3149435788946156,"score_spread":0.2758404235114236,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4245801234","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.77705395,0.0010308401,0.1583263,0.000094050956,0.0037071633,0.056918066,0.00073392084,0.0012072644,0.0009284445],"genre_scores_gemma":[0.60237604,0.00034153598,0.30717662,0.000034978857,0.0053983997,0.04304007,0.015857859,0.0020701105,0.023704397],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9954929,0.00007730237,0.0014948838,0.0013584126,0.00075638545,0.0008201512],"domain_scores_gemma":[0.9962975,0.000959674,0.00082443573,0.0007845992,0.0010127338,0.000121094425],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0030524035,0.00071036414,0.0016279311,0.0006810338,0.00006373692,0.00002077268,0.00026914245,0.00064728333,0.000010556995],"category_scores_gemma":[0.0033597122,0.0006414788,0.0006659865,0.00045062258,0.00004225446,0.0001567,0.00011126716,0.00043170893,0.000001233479],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003450716,0.00046104475,0.00020060984,0.013086714,0.00086348894,0.000009670135,0.0005764855,0.12756884,0.85185814,0.0000075243543,0.00032844304,0.004693957],"study_design_scores_gemma":[0.0012659574,0.00010059467,0.00009480428,0.00047785242,0.0006299722,0.00009766813,0.00005457502,0.056657713,0.92373365,0.0000070117067,0.0162054,0.0006748262],"about_ca_topic_score_codex":0.0034377405,"about_ca_topic_score_gemma":0.0008314576,"teacher_disagreement_score":0.17467792,"about_ca_system_score_codex":0.0015538475,"about_ca_system_score_gemma":0.00054279924,"threshold_uncertainty_score":0.9996036},"labels":[],"label_agreement":null},{"id":"W4246547797","doi":"10.2172/899680","title":"Cost-Effective Method for Producing Self Supported Palladium Alloy Membranes for Use in Efficient Production of Coal Derived Hydrogen","year":2006,"lang":"en","type":"report","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Task (project management); Palladium; Production (economics); Work (physics); Membrane; Process engineering; Coal; Alloy; Quarter (Canadian coin); Production cost; Hydrogen; Hydrogen production; Computer science; Industrial engineering; Engineering; Waste management; Materials science; Chemistry; Mechanical engineering; Metallurgy; Systems engineering; Catalysis; Economics; History","score_opus":0.03910315538319198,"score_gpt":0.3149435788946156,"score_spread":0.2758404235114236,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4246547797","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.77705395,0.0010308401,0.1583263,0.000094050956,0.0037071633,0.056918066,0.00073392084,0.0012072644,0.0009284445],"genre_scores_gemma":[0.60237604,0.00034153598,0.30717662,0.000034978857,0.0053983997,0.04304007,0.015857859,0.0020701105,0.023704397],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9954929,0.00007730237,0.0014948838,0.0013584126,0.00075638545,0.0008201512],"domain_scores_gemma":[0.9962975,0.000959674,0.00082443573,0.0007845992,0.0010127338,0.000121094425],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0030524035,0.00071036414,0.0016279311,0.0006810338,0.00006373692,0.00002077268,0.00026914245,0.00064728333,0.000010556995],"category_scores_gemma":[0.0033597122,0.0006414788,0.0006659865,0.00045062258,0.00004225446,0.0001567,0.00011126716,0.00043170893,0.000001233479],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003450716,0.00046104475,0.00020060984,0.013086714,0.00086348894,0.000009670135,0.0005764855,0.12756884,0.85185814,0.0000075243543,0.00032844304,0.004693957],"study_design_scores_gemma":[0.0012659574,0.00010059467,0.00009480428,0.00047785242,0.0006299722,0.00009766813,0.00005457502,0.056657713,0.92373365,0.0000070117067,0.0162054,0.0006748262],"about_ca_topic_score_codex":0.0034377405,"about_ca_topic_score_gemma":0.0008314576,"teacher_disagreement_score":0.17467792,"about_ca_system_score_codex":0.0015538475,"about_ca_system_score_gemma":0.00054279924,"threshold_uncertainty_score":0.9996036},"labels":[],"label_agreement":null},{"id":"W4246782212","doi":"10.32920/ryerson.14639241","title":"Optimal Fixed Bed Reactor Network Configuration for the Efficient Recycling of CO2 into Methanol","year":2021,"lang":"en","type":"preprint","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University; University of Waterloo","funders":"","keywords":"Methanol; Production (economics); Process engineering; Profit (economics); Environmental science; Mathematical optimization; Computer science; Mathematics; Engineering; Chemistry","score_opus":0.02308805620572214,"score_gpt":0.2780667128189267,"score_spread":0.25497865661320457,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4246782212","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.4411125,0.0014224163,0.55292785,0.00022278642,0.0016949051,0.0014415103,0.000026356365,0.00020644527,0.0009452637],"genre_scores_gemma":[0.9596328,0.00004818293,0.03806173,0.000026386977,0.0007396145,0.00032418297,0.00061294244,0.000097195145,0.00045692426],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99778867,0.00004495257,0.00087178603,0.0005254498,0.0003761742,0.00039297153],"domain_scores_gemma":[0.9969639,0.0013334452,0.00044997036,0.0008611453,0.00030837965,0.000083142],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00097474916,0.00035814385,0.0007161268,0.00007825598,0.00007397446,0.000044339537,0.0004698165,0.00044809325,0.00011876582],"category_scores_gemma":[0.001036892,0.00026056764,0.00054037967,0.0002184214,0.000052427127,0.000045005178,0.00054975506,0.0006780593,0.0000028945658],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000072272844,0.000034695764,0.0000044287376,0.00056514505,0.00041213114,0.0000015724745,0.00086117134,0.47369114,0.5200663,0.00043544493,0.000040591127,0.0038151029],"study_design_scores_gemma":[0.0002781094,0.000013797311,0.0000039666156,0.00031148468,0.00020988089,0.0000027827639,0.00032853262,0.3314324,0.66650856,0.000030230874,0.00064877624,0.00023149062],"about_ca_topic_score_codex":0.00048969965,"about_ca_topic_score_gemma":0.000030384635,"teacher_disagreement_score":0.51852036,"about_ca_system_score_codex":0.00023399564,"about_ca_system_score_gemma":0.00013778532,"threshold_uncertainty_score":0.9999847},"labels":[],"label_agreement":null},{"id":"W4246850886","doi":"10.1016/s1464-2859(09)70264-0","title":"Hydrogenics in reverse merger with Algonquin Power","year":2009,"lang":"en","type":"article","venue":"Fuel Cells Bulletin","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Power (physics); Engineering; Physics; Thermodynamics","score_opus":0.00486367908344175,"score_gpt":0.19598458952556388,"score_spread":0.19112091044212212,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4246850886","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9644673,0.00089865347,0.00024530204,0.0015891022,0.00022989548,0.00033287876,0.000010294565,0.00027367732,0.0319529],"genre_scores_gemma":[0.99259424,0.00003491988,0.0021038866,0.00040774787,0.00007268294,0.000008739361,0.000016575814,0.00004829317,0.0047128843],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998657,0.000017890467,0.00029873918,0.00031572758,0.00026196963,0.00044865964],"domain_scores_gemma":[0.9993594,0.00004169646,0.00006550094,0.00038388564,0.000027181712,0.00012232142],"candidate_categories":["insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00022193042,0.00022257087,0.0002729008,0.00011802447,0.000019968136,0.000009785971,0.00020987465,0.00012660387,0.0011956966],"category_scores_gemma":[0.00004260784,0.00018809117,0.000093267336,0.00028401145,0.000025639043,0.000044745164,0.000041057625,0.00033676022,0.00090270344],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019737422,0.0002525183,0.00008264805,0.00010780578,0.00005253524,0.00056443026,0.0010646059,0.0028903717,0.98731637,0.0002902251,0.0056743464,0.0015067543],"study_design_scores_gemma":[0.0013956156,0.00012736283,0.00010603455,0.00013073247,0.000032437256,0.000077077835,0.00014550559,0.00069829077,0.54934424,0.00005363959,0.44727823,0.00061082124],"about_ca_topic_score_codex":0.000087597145,"about_ca_topic_score_gemma":0.000009619611,"teacher_disagreement_score":0.44160387,"about_ca_system_score_codex":0.000119349876,"about_ca_system_score_gemma":0.000017433207,"threshold_uncertainty_score":0.9998752},"labels":[],"label_agreement":null},{"id":"W4250012799","doi":"10.2495/esu090141","title":"Iron catalysts supported on carbon nanotubes for Fischer–Tropsch synthesis: effect of pore size","year":2009,"lang":"en","type":"article","venue":"WIT transactions on ecology and the environment","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Carbon nanotube; Chemical engineering; Materials science; Carbon fibers; Chemistry; Nanotechnology; Organic chemistry; Composite material; Composite number; Selectivity","score_opus":0.003958277170368913,"score_gpt":0.1953705449259911,"score_spread":0.19141226775562217,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4250012799","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9971676,0.00008809094,0.00092670985,0.0006678133,0.00008781675,0.00058583915,0.000025253119,0.000037268317,0.00041359777],"genre_scores_gemma":[0.9992314,0.00005793325,0.00006918533,0.000044553894,0.000020945281,0.00020211279,0.000010149607,0.0000194465,0.00034425434],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99908906,0.00006700462,0.00024762613,0.00024216514,0.00012016174,0.00023400882],"domain_scores_gemma":[0.9983687,0.0012142194,0.00007170121,0.00028855665,0.0000034530556,0.000053398304],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035446647,0.00019704393,0.0003695365,0.00005616848,0.00010226724,0.000002479364,0.000108026645,0.00015473494,0.000051218627],"category_scores_gemma":[0.00006809999,0.00013026258,0.00015776238,0.000046644538,0.00013388848,0.000030183899,0.0000032675773,0.00020773843,0.0000054057145],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.009067218,0.0015015051,0.00048792415,0.00049532956,0.001504354,0.00003173465,0.0013965274,0.034565657,0.8268487,0.0013942936,0.000015001455,0.122691795],"study_design_scores_gemma":[0.0025533217,0.000997928,0.0016810795,0.0000385467,0.00048405363,0.000018436207,0.000039705308,0.0019887055,0.99172485,0.00010162427,0.0001930478,0.00017870203],"about_ca_topic_score_codex":0.00001700266,"about_ca_topic_score_gemma":0.0000070039528,"teacher_disagreement_score":0.1648762,"about_ca_system_score_codex":0.00009359442,"about_ca_system_score_gemma":0.00000611779,"threshold_uncertainty_score":0.5311954},"labels":[],"label_agreement":null},{"id":"W4250762619","doi":"10.1002/9783527656837.gloss","title":"Glossary","year":2013,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Glossary; Citation; Library science; Art history; Art; Computer science; Philosophy; Linguistics","score_opus":0.00853550505367374,"score_gpt":0.22250221826037228,"score_spread":0.21396671320669855,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4250762619","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00001251192,0.00050280156,0.00072718156,0.000012527569,0.00020978911,0.000099241,0.0000065075265,0.00091345207,0.997516],"genre_scores_gemma":[0.000046682093,0.000021148997,0.0010392185,0.000027719163,0.00047694668,0.000014620549,0.000047438887,0.0006385671,0.99768764],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9994235,0.0000020236969,0.000104271625,0.00016329877,0.00012227314,0.00018462236],"domain_scores_gemma":[0.9995593,0.000010189235,0.000040683197,0.00031901622,0.0000046854498,0.00006616302],"candidate_categories":["insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00002080384,0.00016910481,0.00020824771,0.00011211428,0.000004559025,0.0000048523384,0.00015964272,0.000251479,0.042312376],"category_scores_gemma":[0.000017362745,0.0001310213,0.00008458128,0.000065114386,0.000012862304,0.000021587328,0.000068683745,0.00015915741,0.008659663],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[3.278562e-7,0.0000075354233,0.0000025165887,0.00012668654,0.00007626137,0.000005580471,0.000004927877,6.9274245e-7,0.007959451,0.0027012525,0.9825034,0.006611344],"study_design_scores_gemma":[0.00007371117,0.000001830245,3.13295e-7,0.00007206084,0.0000133024105,0.000007143886,0.000003262155,0.00023783742,0.0100695975,0.0000135885,0.9893076,0.00019978607],"about_ca_topic_score_codex":0.0010196808,"about_ca_topic_score_gemma":0.000013773735,"teacher_disagreement_score":0.03365271,"about_ca_system_score_codex":0.000038759517,"about_ca_system_score_gemma":0.000006732832,"threshold_uncertainty_score":0.9921122},"labels":[],"label_agreement":null},{"id":"W4253156510","doi":"10.7763/ijcea.2015.v6.476","title":"Mathematical Modeling of Helium Recovery from a Multicomponent Fuel Gas with Polymeric Membrane","year":2015,"lang":"en","type":"article","venue":"International Journal of Chemical Engineering and Applications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"University of Waterloo","keywords":"Helium; Materials science; Membrane; Polymeric membrane; Chemical engineering; Helium gas; Nuclear engineering; Chemistry; Polymer; Engineering; Organic chemistry; Composite material","score_opus":0.012562949765636244,"score_gpt":0.22988449634226757,"score_spread":0.21732154657663133,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4253156510","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7183236,0.00055573444,0.28046843,0.00019770724,0.00006975671,0.00008191072,0.00002482513,0.000038689624,0.00023935235],"genre_scores_gemma":[0.9841172,0.000025311292,0.015471583,0.000008613571,0.0003036177,0.00001426404,0.000018793544,0.000025289375,0.000015324213],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9988389,0.0000038316684,0.0004939257,0.0001212724,0.00041873803,0.00012334027],"domain_scores_gemma":[0.99913526,0.00013422867,0.00016852184,0.00012811596,0.00024706678,0.00018679473],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001231658,0.00013316973,0.00027657172,0.00012451137,0.0000058224527,0.000013835625,0.00025766,0.00006170901,0.00001677106],"category_scores_gemma":[0.00012962882,0.000108660584,0.00008687191,0.00010330438,0.000028890196,0.00013240826,0.00006100683,0.0002168543,0.000004909935],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001343046,0.00011929579,0.000008354958,0.00005670744,0.0002808313,0.000007071727,0.00015386115,0.09850233,0.8970684,0.0008126767,0.0000022608222,0.0028539288],"study_design_scores_gemma":[0.0010664127,0.00003532475,0.0000015917803,0.00026419119,0.00008479893,0.00027627058,0.000065814726,0.5484036,0.44844195,0.00075177354,0.00043090316,0.00017734236],"about_ca_topic_score_codex":0.000028328153,"about_ca_topic_score_gemma":1.11280926e-7,"teacher_disagreement_score":0.44990128,"about_ca_system_score_codex":0.00009227314,"about_ca_system_score_gemma":0.00003438033,"threshold_uncertainty_score":0.44310498},"labels":[],"label_agreement":null},{"id":"W4256205737","doi":"10.32920/ryerson.14639241.v1","title":"Optimal Fixed Bed Reactor Network Configuration for the Efficient Recycling of CO2 into Methanol","year":2021,"lang":"en","type":"preprint","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University; University of Waterloo","funders":"","keywords":"Methanol; Production (economics); Profit (economics); Process engineering; Mathematical optimization; Environmental science; Mathematics; Computer science; Engineering; Chemistry","score_opus":0.02308805620572214,"score_gpt":0.2780667128189267,"score_spread":0.25497865661320457,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4256205737","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.4411125,0.0014224163,0.55292785,0.00022278642,0.0016949051,0.0014415103,0.000026356365,0.00020644527,0.0009452637],"genre_scores_gemma":[0.9596328,0.00004818293,0.03806173,0.000026386977,0.0007396145,0.00032418297,0.00061294244,0.000097195145,0.00045692426],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99778867,0.00004495257,0.00087178603,0.0005254498,0.0003761742,0.00039297153],"domain_scores_gemma":[0.9969639,0.0013334452,0.00044997036,0.0008611453,0.00030837965,0.000083142],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00097474916,0.00035814385,0.0007161268,0.00007825598,0.00007397446,0.000044339537,0.0004698165,0.00044809325,0.00011876582],"category_scores_gemma":[0.001036892,0.00026056764,0.00054037967,0.0002184214,0.000052427127,0.000045005178,0.00054975506,0.0006780593,0.0000028945658],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000072272844,0.000034695764,0.0000044287376,0.00056514505,0.00041213114,0.0000015724745,0.00086117134,0.47369114,0.5200663,0.00043544493,0.000040591127,0.0038151029],"study_design_scores_gemma":[0.0002781094,0.000013797311,0.0000039666156,0.00031148468,0.00020988089,0.0000027827639,0.00032853262,0.3314324,0.66650856,0.000030230874,0.00064877624,0.00023149062],"about_ca_topic_score_codex":0.00048969965,"about_ca_topic_score_gemma":0.000030384635,"teacher_disagreement_score":0.51852036,"about_ca_system_score_codex":0.00023399564,"about_ca_system_score_gemma":0.00013778532,"threshold_uncertainty_score":0.9999847},"labels":[],"label_agreement":null},{"id":"W4280527101","doi":"10.1016/j.cattod.2022.05.006","title":"Optimization of carbon nanotube growth via response surface methodology for Fischer-Tropsch synthesis over Fe/CNT catalyst","year":2022,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Carbon nanotube; Fischer–Tropsch process; Chemical engineering; Materials science; Acetylene; Chemical vapor deposition; Chemisorption; Hydrocarbon; Selectivity; Nanotechnology; Chemistry; Organic chemistry","score_opus":0.02337744880923646,"score_gpt":0.26494473515869454,"score_spread":0.2415672863494581,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4280527101","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96015203,0.00046702387,0.037807353,0.00024932303,0.00029073044,0.00048009568,0.00022335969,0.00016757421,0.00016251835],"genre_scores_gemma":[0.98226035,0.000012218273,0.01583962,0.000032631924,0.000074464966,0.0003306223,0.0005224721,0.00013448618,0.0007931497],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99682117,0.00051920896,0.00085257605,0.00069029833,0.0005510909,0.0005656734],"domain_scores_gemma":[0.9955883,0.0026829801,0.00043949654,0.000940177,0.0001971669,0.00015188476],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0029356633,0.00037841298,0.0009588504,0.00040617253,0.00019943304,0.000011869068,0.00063130603,0.00019333641,0.00021875711],"category_scores_gemma":[0.0034396986,0.00038812548,0.00054281857,0.0011875574,0.000090985435,0.0001709054,0.00043660984,0.00034118173,0.0000039221527],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008395249,0.00010231454,0.00017035154,0.00014717322,0.0004230567,0.000008034721,0.00064339524,0.12246513,0.8744828,0.00011301418,0.000034667704,0.00057052524],"study_design_scores_gemma":[0.00063787965,0.00008085944,0.00005017974,0.000019071134,0.0006158126,0.000031302465,0.00028791485,0.06940927,0.92742586,0.000039351075,0.00096958736,0.0004329319],"about_ca_topic_score_codex":0.0012367752,"about_ca_topic_score_gemma":0.0000188942,"teacher_disagreement_score":0.053055864,"about_ca_system_score_codex":0.00083052204,"about_ca_system_score_gemma":0.00010901501,"threshold_uncertainty_score":0.99985707},"labels":[],"label_agreement":null},{"id":"W4280578904","doi":"10.1002/cssc.202200851","title":"Using Biomass Gasification Mineral Residue as Catalyst to Produce Light Olefins from CO, CO<sub>2</sub>, and H<sub>2</sub> Mixtures","year":2022,"lang":"en","type":"article","venue":"ChemSusChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Enerkem (Canada)","funders":"Nederlandse Organisatie voor Wetenschappelijk Onderzoek; Universiteit Utrecht","keywords":"Residue (chemistry); Catalysis; Biomass (ecology); Chemistry; Nanoparticle; Chemical engineering; Materials science; Organic chemistry; Nanotechnology; Engineering; Geology","score_opus":0.018996955831770794,"score_gpt":0.25573792631873693,"score_spread":0.23674097048696613,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4280578904","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99644345,0.00086769037,0.00019644777,0.0005715519,0.00027682164,0.00053969695,0.00020921914,0.00032727138,0.0005678776],"genre_scores_gemma":[0.9972664,0.000014919164,0.000468728,0.00010649141,0.0005838533,0.00017203778,0.0011117146,0.00016364474,0.00011222225],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9966285,0.000056227636,0.00066551135,0.001153778,0.0007377772,0.00075817475],"domain_scores_gemma":[0.9980979,0.000115758856,0.00026143854,0.0009925838,0.00011306121,0.0004192495],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00045185143,0.00054811937,0.0006031578,0.00034558726,0.00038297696,0.00007829565,0.00050554815,0.00022119895,0.000031735974],"category_scores_gemma":[0.0004281217,0.000597378,0.00018850228,0.0008401253,0.00008509393,0.00028851564,0.0004462738,0.0006284447,0.00008707905],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001170636,0.0001009315,0.00032333896,0.00014063163,0.000108589666,0.000050397637,0.0010928138,0.000116428695,0.9954304,0.00003865924,0.00131021,0.0011705247],"study_design_scores_gemma":[0.0007144,0.00004452358,0.0002838794,0.000070881746,0.0001226855,0.00013360682,0.00030445066,0.00066194916,0.9912864,0.000052929438,0.0055898083,0.00073450885],"about_ca_topic_score_codex":0.0004961073,"about_ca_topic_score_gemma":0.00009087931,"teacher_disagreement_score":0.004279598,"about_ca_system_score_codex":0.0006787831,"about_ca_system_score_gemma":0.00013466045,"threshold_uncertainty_score":0.99964774},"labels":[],"label_agreement":null},{"id":"W4280603557","doi":"10.26434/chemrxiv-2022-rv7h5","title":"Coordination and homologation of CO at Al(I): mechanism and chain growth, branching, isomerization and reduction","year":2022,"lang":"en","type":"preprint","venue":"ChemRxiv","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Engineering and Physical Sciences Research Council; Natural Sciences and Engineering Research Council of Canada; EPSRC Centre for Doctoral Training in Medical Imaging; Leverhulme Trust","keywords":"Chemistry; Isomerization; Branching (polymer chemistry); Reagent; Adduct; Ethylene; Ligand (biochemistry); Bond cleavage; Molecule; Stereochemistry; Crystallography; Photochemistry; Organic chemistry; Catalysis","score_opus":0.009391976659365166,"score_gpt":0.23583225795157522,"score_spread":0.22644028129221005,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4280603557","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957666,0.00064456026,0.0024995217,0.00023026853,0.0002232769,0.00031670823,0.000012471041,0.00008646163,0.00022013256],"genre_scores_gemma":[0.9983075,0.00041281636,0.000314484,0.0000134792435,0.00006436613,0.000058741014,0.000512719,0.000041622017,0.0002742641],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99887484,0.00003230405,0.0003184171,0.0004384595,0.00019406028,0.0001419203],"domain_scores_gemma":[0.999324,0.000044739634,0.0003010103,0.00019753716,0.00006772205,0.000064968655],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003566548,0.00021368319,0.0003264977,0.00021503745,0.00010331197,0.000016259808,0.00007526818,0.00022326919,0.000035637175],"category_scores_gemma":[0.00018115623,0.00024107903,0.000044696713,0.000126628,0.000075818476,0.00013743181,0.00045398917,0.00034888549,4.485823e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000022610015,0.000014556157,0.00040969782,0.0008225221,0.00005385904,0.000001136223,0.0011097031,0.000069707094,0.99251634,0.0031079731,0.000013339777,0.0018585828],"study_design_scores_gemma":[0.00059553393,0.00003496256,0.00040683968,0.00011165323,0.00009131211,0.000085432985,0.00022054161,0.014581715,0.9774817,0.0059393696,0.00013062147,0.00032030177],"about_ca_topic_score_codex":0.00011185193,"about_ca_topic_score_gemma":0.000002440472,"teacher_disagreement_score":0.015034597,"about_ca_system_score_codex":0.000176528,"about_ca_system_score_gemma":0.000013691757,"threshold_uncertainty_score":0.9830918},"labels":[],"label_agreement":null},{"id":"W4280607161","doi":"10.1016/j.apcata.2022.118658","title":"Tandem catalysis: A sustainable alternative for direct hydrogenation of CO2 to light olefins","year":2022,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":68,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"King Fahd University of Petroleum and Minerals","keywords":"Tandem; Catalysis; Chemistry; Combinatorial chemistry; Nanotechnology; Organic chemistry; Materials science","score_opus":0.008075206888053712,"score_gpt":0.22995700326859,"score_spread":0.2218817963805363,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4280607161","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9858072,0.00023058626,0.0062750587,0.00017756704,0.00010793349,0.0010342057,0.00012554313,0.00015121223,0.00609073],"genre_scores_gemma":[0.9916267,0.0000026533824,0.00072358164,0.000071822265,0.00019002448,0.002002025,0.001083673,0.00008297852,0.004216577],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99748284,0.000024922061,0.0006182648,0.00062026916,0.00063376036,0.0006199495],"domain_scores_gemma":[0.9986881,0.0000903513,0.0002765888,0.00062165817,0.00015323095,0.0001700975],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00066497637,0.00030222457,0.0006670816,0.0005273867,0.00026764066,0.000019160161,0.00054609065,0.000068771675,0.00007875365],"category_scores_gemma":[0.000112585556,0.00031284103,0.00039964842,0.0014128808,0.000024325172,0.00011094756,0.00049976795,0.0001857294,0.0000132923615],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012111889,0.00019291083,0.00005389845,0.00009698188,0.00078983436,0.000009082763,0.0021237591,0.09250518,0.8890363,0.013034869,0.00039975994,0.0016362994],"study_design_scores_gemma":[0.00083199353,0.00007237269,0.0000092708715,0.0000050199387,0.00037375497,0.0000071123754,0.00093947456,0.010108147,0.96187884,0.00035357926,0.025022434,0.00039802233],"about_ca_topic_score_codex":0.0007574722,"about_ca_topic_score_gemma":0.00008242253,"teacher_disagreement_score":0.082397036,"about_ca_system_score_codex":0.00080092694,"about_ca_system_score_gemma":0.000079194375,"threshold_uncertainty_score":0.99993235},"labels":[],"label_agreement":null},{"id":"W4281387511","doi":"10.1016/j.energy.2022.124288","title":"Intensification of steam reforming process for off-gas upgrading and energy optimization using evolutionary algorithm","year":2022,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Science Foundation of Guangdong Province; National Natural Science Foundation of China","keywords":"Syngas; Exergy efficiency; Exergy; Pinch analysis; Process engineering; Natural gas; Coal; Environmental science; Process integration; Coal gasification; Chemistry; Waste management; Engineering; Hydrogen","score_opus":0.016684091882129926,"score_gpt":0.2471493699500045,"score_spread":0.23046527806787456,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4281387511","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.1686581,0.0032209414,0.82694167,0.000061583276,0.00038610492,0.000120252815,0.000064652435,0.00016630601,0.00038038296],"genre_scores_gemma":[0.9832064,0.00008458372,0.015483178,0.000028459945,0.0001703257,0.00012391031,0.000351884,0.00006855483,0.00048272166],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99895144,0.000019330026,0.00034045248,0.00024937175,0.00022667237,0.00021273109],"domain_scores_gemma":[0.9994005,0.000056501085,0.00019469285,0.00016774744,0.00012665307,0.00005388425],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001719224,0.00013261239,0.00021075697,0.00021817554,0.0001831367,0.000004095299,0.00012360731,0.0000549224,0.000018427218],"category_scores_gemma":[0.00008439216,0.0001420548,0.00006681616,0.00033575084,0.000029068426,0.00021457132,0.00011496147,0.000082004015,4.9165745e-8],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004359329,0.00004664482,0.000014773023,0.00008669235,0.00005982525,0.0000016728815,0.00034162722,0.70463043,0.15316725,0.0037911604,0.0000074626923,0.13780884],"study_design_scores_gemma":[0.00028098858,0.00003534891,0.0000014498987,0.000028798211,0.000031391726,0.000063318614,0.000655666,0.86676323,0.1289718,0.00023339331,0.0027852675,0.00014937115],"about_ca_topic_score_codex":0.00031031252,"about_ca_topic_score_gemma":0.000003133322,"teacher_disagreement_score":0.8145483,"about_ca_system_score_codex":0.00031464655,"about_ca_system_score_gemma":0.000046373814,"threshold_uncertainty_score":0.5792827},"labels":[],"label_agreement":null},{"id":"W4281693972","doi":"10.1002/cjce.24479","title":"Biomass‐gas‐and‐nuclear‐to‐liquids ( <scp>BGNTL</scp> ) polygeneration process part <scp>II</scp> : Techno‐economic analysis","year":2022,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":true,"ca_institutions":"ArcelorMittal (Canada); McMaster University","funders":"","keywords":"Biomass (ecology); Greenhouse gas; Raw material; Natural gas; Waste management; Environmental science; Carbon-neutral fuel; Dimethyl ether; Renewable natural gas; Syngas; Methane; Carbon dioxide; Environmental engineering; Fuel gas; Chemistry; Hydrogen; Methanol; Engineering; Ecology","score_opus":0.006607843934109202,"score_gpt":0.19623328881719648,"score_spread":0.18962544488308727,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4281693972","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978582,0.00044876843,0.00040341495,0.00040408166,0.00035054586,0.00015567736,0.000050175215,0.00008639511,0.00024270565],"genre_scores_gemma":[0.9988065,0.0000039834176,0.00028805833,0.0000855781,0.0004909331,0.0000271417,0.000023982644,0.000099097924,0.0001747221],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99771893,0.00002203435,0.0007619472,0.0003157088,0.00042269102,0.00075868727],"domain_scores_gemma":[0.9980945,0.00023321659,0.00025046422,0.0003902955,0.00008352099,0.00094800175],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007887336,0.00034674627,0.00058820867,0.00096849946,0.0003468429,0.00009005247,0.0008060146,0.00015472215,0.000039826504],"category_scores_gemma":[0.00095019356,0.00032091484,0.00033334928,0.0010484859,0.00006413927,0.00022956375,0.00018432256,0.00095101097,0.000008157365],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000046315695,0.00001574419,0.00013665945,0.00006334627,0.0007768857,0.00004923998,0.0021473584,0.25955194,0.7357227,0.0006299613,0.00035495244,0.00054656673],"study_design_scores_gemma":[0.0005591066,0.00011831943,0.000035004337,0.00006734235,0.00069532706,0.000570699,0.0005312591,0.16005725,0.80908686,0.00010541513,0.027963838,0.00020957504],"about_ca_topic_score_codex":0.0014506923,"about_ca_topic_score_gemma":0.00030763558,"teacher_disagreement_score":0.099494696,"about_ca_system_score_codex":0.0011932682,"about_ca_system_score_gemma":0.00031333268,"threshold_uncertainty_score":0.9999243},"labels":[],"label_agreement":null},{"id":"W4282597795","doi":"10.1016/j.compchemeng.2022.107892","title":"Robust simulation-optimization framework for synthesis and design of natural gas downstream Incorporating renewable hydrogen network under uncertainty","year":2022,"lang":"en","type":"article","venue":"Computers & Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Process engineering; Natural gas; Renewable energy; Syngas; Hydrogen production; Raw material; Renewable natural gas; Engineering; Environmental science; Waste management; Hydrogen; Chemistry; Fuel gas","score_opus":0.017319393534324993,"score_gpt":0.2152483046587362,"score_spread":0.19792891112441122,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4282597795","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"methods","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.07375865,0.0002504448,0.925288,0.00001953489,0.00020097654,0.0002986916,0.000012172374,0.00016850562,0.000003000611],"genre_scores_gemma":[0.65356874,0.0000017621943,0.34610674,0.00001200005,0.00015722704,0.000055803594,0.0000443336,0.000050578696,0.0000028216934],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99855727,0.000021235173,0.00044814957,0.0003515266,0.00024083545,0.00038095744],"domain_scores_gemma":[0.9977552,0.001663486,0.00017476258,0.00024418588,0.000055218636,0.00010709958],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00029406382,0.00025744346,0.00040586054,0.00010475769,0.000113668764,0.000016410128,0.00023831085,0.00011358221,0.000011551966],"category_scores_gemma":[0.0003761239,0.00028602217,0.00012038711,0.00044706283,0.000030920914,0.000121485915,0.00026822402,0.0003099732,1.4093273e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000036766392,0.000016374115,0.000008635838,0.00011199424,0.00008630751,0.0000013769504,0.00004510354,0.90591794,0.09301067,0.00028235844,0.0000046501086,0.00047781444],"study_design_scores_gemma":[0.0002541461,0.00001715329,3.1943782e-7,0.00012799348,0.00006148388,0.000013940749,0.000023264787,0.91835374,0.080509655,0.00034920743,0.00001268875,0.00027640729],"about_ca_topic_score_codex":0.000032799504,"about_ca_topic_score_gemma":1.1973786e-7,"teacher_disagreement_score":0.5798101,"about_ca_system_score_codex":0.00032051888,"about_ca_system_score_gemma":0.000030726016,"threshold_uncertainty_score":0.9999592},"labels":[],"label_agreement":null},{"id":"W4283644171","doi":"10.3390/reactions3030024","title":"Special Issue Editorial: Catalytic Conversion of Carbonaceous Materials to Fuels and Chemicals","year":2022,"lang":"en","type":"article","venue":"Reactions","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Syngas; Biogas; Greenhouse gas; Waste management; Coal; Environmental science; Carbon neutrality; Biomass (ecology); Substitute natural gas; Carbon fibers; Carbonization; Natural gas; Materials science; Catalysis; Engineering; Chemistry","score_opus":0.007837285488574644,"score_gpt":0.23549365669132347,"score_spread":0.22765637120274881,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4283644171","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96695447,0.000034868142,0.000014432769,0.00021523403,0.025591906,0.00029037168,0.00019243914,0.000106841544,0.0065994454],"genre_scores_gemma":[0.9497017,0.000011075714,0.000083009385,0.000017212109,0.047779545,0.000053075248,0.00008691587,0.00003794718,0.002229516],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991147,0.000013413909,0.00025805278,0.00018171054,0.0002639403,0.000168181],"domain_scores_gemma":[0.99949086,0.00009014014,0.00007673207,0.00020717786,0.000034391025,0.0001007283],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017912601,0.00009952789,0.00022832518,0.000107971966,0.0000770879,0.0000061918654,0.00010426409,0.00005434009,0.0005672291],"category_scores_gemma":[0.0001704838,0.00010701244,0.00004576558,0.00020659491,0.000021779773,0.000064781976,0.00020106796,0.00015267615,0.000029998575],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000027727276,0.00002495384,0.0000050050653,0.00006850125,0.000022516895,0.000002516885,0.00022910413,0.000056748817,0.99201745,0.000072429524,0.007181264,0.00029179943],"study_design_scores_gemma":[0.00014578915,0.000017896786,0.0000054426314,0.000009106466,0.000025382582,0.000026726799,0.00014593007,0.000012258334,0.61661243,0.000017020213,0.38290232,0.00007972304],"about_ca_topic_score_codex":0.00059882813,"about_ca_topic_score_gemma":0.0000021224037,"teacher_disagreement_score":0.37572104,"about_ca_system_score_codex":0.00023611827,"about_ca_system_score_gemma":0.00002622918,"threshold_uncertainty_score":0.6210761},"labels":[],"label_agreement":null},{"id":"W4288787934","doi":"10.1016/b978-0-323-85585-3.00003-1","title":"Dry reforming of methane and biogas to produce syngas: a review of catalysts and process conditions","year":2022,"lang":"en","type":"review","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Carbon dioxide reforming; Syngas; Syngas to gasoline plus; Methane; Methane reformer; Biogas; Coke; Catalysis; Greenhouse gas; Catalytic reforming; Natural gas; Waste management; Environmental science; Chemistry; Steam reforming; Hydrogen production; Engineering; Organic chemistry","score_opus":0.026621431334195853,"score_gpt":0.3277215803645956,"score_spread":0.3011001490303997,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4288787934","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00022818957,0.9901256,0.0000011278808,0.0000126775185,0.00008462425,0.0018992217,0.00026652837,0.000052187697,0.0073298733],"genre_scores_gemma":[0.000033816093,0.9956185,0.0002467656,0.000028831948,0.0000693026,0.0007373612,0.00024435297,0.00011284841,0.0029081872],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9969581,0.00010204283,0.001441998,0.0006632305,0.00046392056,0.0003707493],"domain_scores_gemma":[0.99779683,0.00025823686,0.00081761414,0.0007951528,0.00011282084,0.00021931583],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0011124116,0.000537893,0.003000316,0.0004737695,0.000050032988,0.0000058034257,0.00041557464,0.00016762444,0.000039874783],"category_scores_gemma":[0.00093058817,0.00043975856,0.00038943635,0.0004968793,0.00012030391,0.0000943107,0.00051720155,0.0005458613,0.0000034715688],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000021816147,0.000012862565,5.0300156e-7,0.25348976,0.00018603734,0.000006368673,0.00020674005,7.217838e-8,0.0003375581,0.000025142755,0.0000013375909,0.7457314],"study_design_scores_gemma":[0.000119962104,0.000049702827,1.4694545e-7,0.13464282,0.001621934,0.00016851387,0.000064653614,6.3727106e-7,0.004732383,0.000013925049,0.85817707,0.00040823905],"about_ca_topic_score_codex":0.000011345018,"about_ca_topic_score_gemma":0.00000649376,"teacher_disagreement_score":0.85817575,"about_ca_system_score_codex":0.0001588382,"about_ca_system_score_gemma":0.00024275445,"threshold_uncertainty_score":0.9998054},"labels":[],"label_agreement":null},{"id":"W4291340678","doi":"10.2139/ssrn.4189620","title":"Microwave-Assisted Hydrothermal Synthesis of Ru/Ceo2 Catalyst for Efficient and Stable Low-Temperature Dry Reforming of Methane","year":2022,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Carbon dioxide reforming; Methane; Catalysis; Hydrothermal circulation; Chemical engineering; Hydrothermal synthesis; Methane reformer; Chemistry; Syngas; Materials science; Inorganic chemistry; Nuclear chemistry; Steam reforming; Hydrogen production; Organic chemistry; Engineering","score_opus":0.005322020516582945,"score_gpt":0.21396361393363808,"score_spread":0.20864159341705513,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4291340678","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9942441,0.00427288,0.00088293164,0.000038816204,0.00010490474,0.00025212357,0.000069018,0.000026072066,0.00010913137],"genre_scores_gemma":[0.99886143,0.00013056921,0.00028989217,0.000006508243,0.0000796672,0.000046391273,0.000023776221,0.000070301045,0.00049148157],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971352,0.000063944,0.0006666266,0.00026209437,0.0004237616,0.0014483324],"domain_scores_gemma":[0.99887794,0.00021011636,0.00043828585,0.00027333005,0.0001019169,0.00009840576],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0022781126,0.00023678162,0.0005752216,0.00028908136,0.00018366807,0.000008900363,0.00035084513,0.000096959106,0.000026818827],"category_scores_gemma":[0.0002228828,0.00021139042,0.00028881675,0.00038502412,0.000057191548,0.000106287065,0.00016039533,0.0012961057,4.986859e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024391488,0.00010468562,0.000037582195,0.00022365905,0.0003739377,0.0000031574195,0.00034156756,0.0018080388,0.984897,0.0018162489,0.0000012144067,0.010148947],"study_design_scores_gemma":[0.0009977183,0.00017388845,0.000015471498,0.0001031029,0.000192096,0.0005874436,0.0025803042,0.0018105602,0.9927556,0.00038466233,0.00016074737,0.00023843783],"about_ca_topic_score_codex":0.00022570784,"about_ca_topic_score_gemma":0.00011784347,"teacher_disagreement_score":0.009910509,"about_ca_system_score_codex":0.0012190468,"about_ca_system_score_gemma":0.0006824975,"threshold_uncertainty_score":0.8620251},"labels":[],"label_agreement":null},{"id":"W4293152211","doi":"10.2139/ssrn.4185993","title":"Syngas Production Via Methane Dry Reforming Over Nickel Supported Mesoporous Uvm-7 Catalysts","year":2022,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Syngas; Carbon dioxide reforming; Syngas to gasoline plus; Methane; Nickel; Catalysis; Mesoporous material; Methane reformer; Production (economics); Materials science; Business; Waste management; Environmental science; Chemistry; Steam reforming; Metallurgy; Hydrogen production; Organic chemistry; Economics; Engineering","score_opus":0.0067388227956847145,"score_gpt":0.23205356939542962,"score_spread":0.2253147465997449,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4293152211","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9926742,0.0032279603,0.0015950294,0.0003706518,0.0011030479,0.00030029422,0.000009702086,0.00026658736,0.00045255065],"genre_scores_gemma":[0.99035704,0.00031597234,0.00007659649,0.000040803323,0.0007327442,0.00005399028,0.00013437796,0.00014315336,0.00814534],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99414027,0.00012672575,0.0008275707,0.0005575668,0.0010492617,0.0032986163],"domain_scores_gemma":[0.9985667,0.000048949794,0.00047775102,0.00058561517,0.00010349048,0.00021747945],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0038022355,0.00040366166,0.0005170988,0.00046797053,0.0005466519,0.000019511815,0.0006428195,0.000104904655,0.00021848755],"category_scores_gemma":[0.00027714204,0.00038472607,0.00037480428,0.00084215536,0.00004823869,0.00058988604,0.00032250263,0.004912256,0.00004372067],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022794341,0.000203352,0.00048249218,0.000055609908,0.00090097246,0.00012104639,0.00068395527,0.0013882704,0.9511971,0.0027523336,0.000055242763,0.041931666],"study_design_scores_gemma":[0.0032448622,0.0007577121,0.00012485386,0.000079879,0.0007589473,0.037297584,0.0068451082,0.0029731905,0.91284597,0.02242792,0.010785327,0.0018586591],"about_ca_topic_score_codex":0.00077937613,"about_ca_topic_score_gemma":0.0004317517,"teacher_disagreement_score":0.040073007,"about_ca_system_score_codex":0.0067385663,"about_ca_system_score_gemma":0.0012918127,"threshold_uncertainty_score":0.99986047},"labels":[],"label_agreement":null},{"id":"W4293205607","doi":"10.2139/ssrn.4059740","title":"Optimization of Olefins' Yield in Fischer-Tropsch Synthesis Using Carbon Nanotubes Supported Iron Catalyst with Molybdenum and Potassium Promoters","year":2022,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Molybdenum; Yield (engineering); Potassium; Chemistry; Carbon fibers; Inorganic chemistry; Materials science; Chemical engineering; Organic chemistry; Metallurgy; Selectivity; Composite number; Engineering","score_opus":0.007407478763249828,"score_gpt":0.20368636294594536,"score_spread":0.19627888418269554,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4293205607","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970797,0.00070033397,0.0018479022,0.00008578491,0.00004467341,0.00014180505,0.0000067414367,0.000025014748,0.000068066045],"genre_scores_gemma":[0.9993529,0.00012196215,0.00032315002,0.000004807949,0.00003866566,0.00001528156,0.000012504179,0.000055086148,0.00007568599],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99781543,0.000059414364,0.00040705383,0.00024027856,0.00037694696,0.0011009022],"domain_scores_gemma":[0.9994279,0.00005231244,0.00023273197,0.00018056342,0.000037298585,0.00006917337],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008636872,0.00019752215,0.00032819447,0.00031866398,0.00010801085,0.000013253158,0.00019321394,0.000069590475,0.000024600715],"category_scores_gemma":[0.00011729937,0.00017983075,0.00006511291,0.0004434533,0.00003843559,0.00016876329,0.000098090815,0.0013321996,1.23871e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002745655,0.00013961943,0.005110013,0.000107054046,0.00023110442,0.00004178795,0.00065245456,0.24917138,0.7417498,0.00023649343,4.1808067e-7,0.0022852984],"study_design_scores_gemma":[0.0025599792,0.0007944318,0.0003392778,0.0003892634,0.00056081405,0.0055867196,0.00849527,0.25458118,0.7252833,0.00032793047,0.0000280507,0.0010537422],"about_ca_topic_score_codex":0.0015447018,"about_ca_topic_score_gemma":0.00046443648,"teacher_disagreement_score":0.016466478,"about_ca_system_score_codex":0.001360133,"about_ca_system_score_gemma":0.00057860115,"threshold_uncertainty_score":0.7333285},"labels":[],"label_agreement":null},{"id":"W4294795491","doi":"10.1039/d2re00236a","title":"Autothermal CO<sub>2</sub> hydrogenation reactor for renewable natural gas generation: experimental proof-of-concept","year":2022,"lang":"en","type":"article","venue":"Reaction Chemistry & Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation","keywords":"Natural gas; Renewable energy; Proof of concept; Environmental science; Substitute natural gas; Process engineering; Chemistry; Computer science; Syngas; Organic chemistry; Engineering; Hydrogen","score_opus":0.011905981278512572,"score_gpt":0.2307197994405467,"score_spread":0.21881381816203413,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4294795491","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99375594,0.00047467006,0.0044042515,0.000034133715,0.00047950723,0.0003085105,0.00004993278,0.00027134767,0.00022168831],"genre_scores_gemma":[0.9976008,0.0000022401407,0.00031463985,0.000006946899,0.00065567286,0.00035112794,0.0007213649,0.00008638404,0.00026081587],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985277,0.000007650488,0.00041978856,0.0003484705,0.00036330122,0.00033307265],"domain_scores_gemma":[0.9993453,0.000054977892,0.00018233452,0.00027025118,0.000056866436,0.00009027696],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00017922783,0.0002504379,0.0002656452,0.00007670549,0.00011281569,0.000013983758,0.00016642301,0.00009923895,0.000052697593],"category_scores_gemma":[0.00009312739,0.00030057222,0.00019555054,0.0002239536,0.000016395568,0.0002564209,0.00006305663,0.00031351377,0.0000010453123],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000024273773,0.000056138102,9.4663454e-7,0.00009226012,0.000057842582,0.0000022123022,0.0001581851,0.083102375,0.9155041,0.000022409036,0.00008036649,0.0008989185],"study_design_scores_gemma":[0.00045631043,0.000020119069,6.5125863e-7,0.000017834254,0.000021501999,0.00008250765,0.000073162104,0.1933553,0.8005175,0.0000016396116,0.0052051945,0.00024824866],"about_ca_topic_score_codex":0.000020307452,"about_ca_topic_score_gemma":2.9734494e-7,"teacher_disagreement_score":0.114986554,"about_ca_system_score_codex":0.0008621357,"about_ca_system_score_gemma":0.00005855276,"threshold_uncertainty_score":0.9999446},"labels":[],"label_agreement":null},{"id":"W4295025151","doi":"10.1016/j.cej.2022.139079","title":"Tuning transport mechanisms in fuel-assisted solid oxide electrolysis cells for enhanced performance and product selectivity: Thermodynamic and kinetic modeling","year":2022,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Queen's University","funders":"","keywords":"Methane; Syngas; Electrolysis; Anode; Steam reforming; Solid oxide fuel cell; Hydrogen; Chemical engineering; Oxide; Carbon fibers; Water-gas shift reaction; Raw material; Hydrogen production; Carbon monoxide; Chemistry; Process engineering; Energy carrier; Materials science; Catalysis; Organic chemistry; Electrode; Engineering","score_opus":0.006395022585301448,"score_gpt":0.19861781244026092,"score_spread":0.19222278985495947,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4295025151","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7721341,0.00032823658,0.22716957,0.000022190843,0.00007263609,0.00017602566,0.000004376284,0.000081316895,0.000011542223],"genre_scores_gemma":[0.9909568,0.000063095635,0.008647523,0.000010224921,0.00008795489,0.00010371546,0.000013571118,0.00009162894,0.000025479007],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9981613,0.000013712352,0.00049040525,0.00041024626,0.00029211523,0.0006322084],"domain_scores_gemma":[0.99944246,0.00008414221,0.00009500262,0.00015962709,0.00004484531,0.00017394344],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00056819816,0.00030608487,0.00047884812,0.00028629796,0.00012052741,0.000023978058,0.00019504904,0.00007944672,0.000009324631],"category_scores_gemma":[0.00008763605,0.00032160044,0.00011223555,0.00038823174,0.00001649862,0.00019532662,0.00008291274,0.0010372708,1.92437e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000063932355,0.00002551918,0.000007831147,0.00020032878,0.000047054935,0.00000690398,0.00021346868,0.21582781,0.7815635,0.000021389842,1.6429921e-7,0.0020220834],"study_design_scores_gemma":[0.0006355782,0.000032427764,0.00002166507,0.000052968448,0.000039232116,0.00030241854,0.000024161147,0.53506994,0.463551,0.000049619168,0.000005955916,0.00021502138],"about_ca_topic_score_codex":0.000010575762,"about_ca_topic_score_gemma":9.84892e-7,"teacher_disagreement_score":0.31924212,"about_ca_system_score_codex":0.00039127242,"about_ca_system_score_gemma":0.000042303,"threshold_uncertainty_score":0.9999236},"labels":[],"label_agreement":null},{"id":"W4297782448","doi":"","title":"IEA Task 25: High Temperature Hydrogen Production Processes Quarter 2 FY2010.","year":2020,"lang":"en","type":"paratext","venue":"OSTI OAI (U.S. Department of Energy Office of Scientific and Technical Information)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Production (economics); Hydrogen production; Hydrogen; Task (project management); Computer science; Materials science; Engineering physics; Engineering; Chemistry; Systems engineering; Economics; History","score_opus":0.007503222634431488,"score_gpt":0.21334119633959522,"score_spread":0.20583797370516374,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4297782448","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.664556,0.00856894,0.0034632224,0.0033758504,0.012714159,0.004204983,0.008399127,0.0014235504,0.29329413],"genre_scores_gemma":[0.96843106,0.0002321333,0.0005323383,0.00005296398,0.0002457431,0.00010623032,0.023444686,0.000040460738,0.006914373],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99694073,0.000021138168,0.0012329044,0.0005299776,0.00088901527,0.0003862499],"domain_scores_gemma":[0.9977326,0.000086820306,0.00082952855,0.000569428,0.0005701329,0.00021150566],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003195167,0.00046996868,0.0007663496,0.0004205276,0.00017029494,0.00008832993,0.00047852646,0.0005264648,0.00024760453],"category_scores_gemma":[0.00039802387,0.00040353014,0.00018671532,0.0010623564,0.0004088027,0.0011447857,0.00024923144,0.0004391504,0.0002542194],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00056235073,0.00085663056,0.000028019125,0.013092417,0.0010370068,0.000008270091,0.000094037736,0.00403345,0.6516832,0.007303001,0.31778166,0.0035199518],"study_design_scores_gemma":[0.00047175426,0.00017459632,0.00006765283,0.0005712173,0.00021952992,0.00005027879,0.000012051136,0.00002617964,0.61472344,0.000039238956,0.3830507,0.0005933794],"about_ca_topic_score_codex":0.00004506815,"about_ca_topic_score_gemma":0.000010339048,"teacher_disagreement_score":0.30387506,"about_ca_system_score_codex":0.00011055427,"about_ca_system_score_gemma":0.00026909713,"threshold_uncertainty_score":0.99984163},"labels":[],"label_agreement":null},{"id":"W4301399264","doi":"10.1002/cjce.24696","title":"Comparative analysis of ethanol‐steam and ‐autothermal reforming for hydrogen production using Aspen Plus","year":2022,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs; Canada Foundation for Innovation; University of Regina","keywords":"Steam reforming; Methane reformer; Hydrogen production; Mole fraction; Hydrogen; Ethanol; Chemistry; Chemical engineering; Materials science; Waste management; Nuclear chemistry; Organic chemistry; Engineering; Physical chemistry","score_opus":0.02494025800901421,"score_gpt":0.24948566842217162,"score_spread":0.22454541041315743,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4301399264","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99835294,0.0006380845,0.00054764503,0.00008942114,0.00014516684,0.00015059958,0.000028767052,0.000011502079,0.00003586758],"genre_scores_gemma":[0.99926144,9.099964e-7,0.0005155832,0.000009335272,0.00014190677,0.00000895559,0.000009726086,0.000026014328,0.00002615428],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987742,0.000017037557,0.0005060855,0.00013731632,0.0002509268,0.00031446744],"domain_scores_gemma":[0.9991064,0.000110843444,0.00027634212,0.00017988119,0.00010284608,0.00022365776],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006564402,0.00015603848,0.0005403018,0.00049977505,0.00012355238,0.00000985995,0.00029538322,0.00005436147,0.000023938283],"category_scores_gemma":[0.0002041043,0.00013162705,0.00024009722,0.0007257652,0.000058629863,0.00013904371,0.000055938384,0.00043288487,1.1199601e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000021218035,0.00000320427,0.000017797116,0.000031774936,0.0005282039,0.0000032070645,0.0011354238,0.3973016,0.6007241,0.00006748293,0.0000016696721,0.00016428361],"study_design_scores_gemma":[0.00025192782,0.000023901777,0.000010159313,0.000036271522,0.0006307884,0.00018939312,0.00018619138,0.30111074,0.69713104,0.000018545366,0.00027239413,0.00013861914],"about_ca_topic_score_codex":0.0013584459,"about_ca_topic_score_gemma":0.000105883395,"teacher_disagreement_score":0.09640693,"about_ca_system_score_codex":0.00088111527,"about_ca_system_score_gemma":0.00028366648,"threshold_uncertainty_score":0.5367595},"labels":[],"label_agreement":null},{"id":"W4306407112","doi":"10.1016/j.ces.2022.118207","title":"Transport phenomena modeling of novel renewable natural gas reactors in various configurations","year":2022,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"","keywords":"Exothermic reaction; Methane; Carbon dioxide; Yield (engineering); Natural gas; Hydrogen; Nuclear engineering; Chemistry; Chemical reactor; Process engineering; Mechanics; Materials science; Chemical engineering; Engineering; Composite material; Organic chemistry","score_opus":0.012368445371232288,"score_gpt":0.21962132985211916,"score_spread":0.20725288448088686,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4306407112","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96914744,0.00009961034,0.029407976,0.000029693303,0.00025411823,0.00012777223,0.000016569735,0.0001404158,0.00077639945],"genre_scores_gemma":[0.996688,0.0000015737314,0.003130279,0.000007875189,0.000038525748,0.00003719825,0.000024334639,0.00002791693,0.00004426367],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9980947,0.0000025269212,0.0004497845,0.00038151426,0.00057926535,0.00049225864],"domain_scores_gemma":[0.9993886,0.0000611543,0.000059896734,0.0003128616,0.000052872983,0.00012461243],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045491432,0.0001754685,0.0002781296,0.00032310898,0.000070100206,0.000007656311,0.0005956052,0.000041164618,0.000029333703],"category_scores_gemma":[0.00026488828,0.00018922013,0.0000833031,0.0015611046,0.00008483421,0.0002731726,0.000136993,0.00049353833,6.8819264e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000039121264,0.000030930318,0.0000065947597,0.000021706635,0.000003009523,0.000001816748,0.00022649777,0.4594242,0.5396317,0.00059997727,1.9621618e-7,0.000049424656],"study_design_scores_gemma":[0.0002444597,0.0000057142734,0.0000049831674,0.00002251362,0.0000052070473,0.00001839179,0.00005005895,0.6151409,0.38430116,0.000018878969,0.00004346451,0.0001442623],"about_ca_topic_score_codex":0.00033475767,"about_ca_topic_score_gemma":0.0000019265392,"teacher_disagreement_score":0.15571669,"about_ca_system_score_codex":0.00056890585,"about_ca_system_score_gemma":0.00012165136,"threshold_uncertainty_score":0.7716173},"labels":[],"label_agreement":null},{"id":"W4307404703","doi":"10.1002/cjce.24736","title":"An overview of mono‐ethylene glycol synthesis via <scp>CO</scp> coupling reaction: Catalysts, kinetics, and reaction pathways","year":2022,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Construction Industry Institute, University of Texas at Austin","keywords":"Syngas; Ethylene glycol; Raw material; Catalysis; Yield (engineering); Chemistry; Organic chemistry; Chemical engineering; Materials science","score_opus":0.02136078757641685,"score_gpt":0.2273278642419796,"score_spread":0.20596707666556274,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4307404703","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9964911,0.0026984613,0.00023667578,0.00007030666,0.0002551989,0.00011377153,0.00003643295,0.000036071357,0.0000620188],"genre_scores_gemma":[0.99931526,0.000040902938,0.00023746208,0.000015198504,0.000277568,0.00001629893,0.0000168921,0.00006977783,0.000010616864],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99826515,0.000021386826,0.0006704979,0.00019451193,0.00042714374,0.00042130804],"domain_scores_gemma":[0.99825174,0.00038800124,0.000340843,0.00035767406,0.00011334615,0.0005483737],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007356571,0.00024428163,0.00047268817,0.00030999823,0.00012217948,0.00002440599,0.00044785562,0.00011614355,0.000012045468],"category_scores_gemma":[0.0006405131,0.00022552932,0.00017568239,0.00037564067,0.00006188202,0.00023526899,0.000051466108,0.0008616729,0.0000012337127],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00000775942,0.000017653429,0.000032243915,0.0001248851,0.00009591489,0.000034958914,0.0003759234,0.013555958,0.9843765,0.000115825555,0.000015206621,0.0012472027],"study_design_scores_gemma":[0.00024590569,0.000056375302,0.00008860911,0.00013465379,0.00014105502,0.00088435074,0.00016660047,0.028644778,0.9676705,0.00004684799,0.0017887607,0.00013157443],"about_ca_topic_score_codex":0.0023139883,"about_ca_topic_score_gemma":0.00007993752,"teacher_disagreement_score":0.01670598,"about_ca_system_score_codex":0.0008076866,"about_ca_system_score_gemma":0.00017079906,"threshold_uncertainty_score":0.91968185},"labels":[],"label_agreement":null},{"id":"W4311188347","doi":"10.1016/j.ijhydene.2022.11.137","title":"Comparative techno-economic study of typically combustion-less hydrogen production alternatives","year":2022,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":24,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut interdisciplinaire d'innovation technologique; Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Environmental science; Electricity generation; Renewable energy; Electric power; Electricity; Process engineering; Cost of electricity by source; Electric heating; Hydrogen production; Concentrated solar power; Nuclear engineering; Waste management; Engineering; Hydrogen; Power (physics); Mechanical engineering; Electrical engineering; Chemistry; Thermodynamics","score_opus":0.019959806322674748,"score_gpt":0.27577240903274514,"score_spread":0.2558126027100704,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4311188347","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99814045,0.00017661459,0.0003342508,0.00012833688,0.0008399884,0.00008239972,0.000020593465,0.00002429089,0.00025305452],"genre_scores_gemma":[0.99929994,0.0000152067005,0.00008457989,0.000013485486,0.00029954108,0.000019567344,0.000018146719,0.000023652017,0.00022586792],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99803436,0.00007295796,0.00080768403,0.00019541866,0.00074465945,0.00014493836],"domain_scores_gemma":[0.9986451,0.000065557695,0.00078962615,0.00017718578,0.00025676866,0.0000657424],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035509228,0.0001572374,0.0003882658,0.0004543881,0.00006438179,0.0000089350815,0.00079780986,0.000031937096,0.00013702619],"category_scores_gemma":[0.000053160275,0.00015198976,0.00017394405,0.00015606919,0.00004641881,0.00024827672,0.00027655778,0.00029158618,0.0000031151017],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00036260657,0.0008727961,0.0008265449,0.0000055479954,0.0014888657,0.000072775045,0.0015044673,0.6485316,0.3421087,0.0015257312,0.000028722292,0.0026716178],"study_design_scores_gemma":[0.001530349,0.0004689764,0.00010806921,0.00003514784,0.00009327267,0.00082794036,0.003826974,0.014688948,0.9757714,0.00056429947,0.0018577066,0.00022686197],"about_ca_topic_score_codex":0.00042349906,"about_ca_topic_score_gemma":0.000054946722,"teacher_disagreement_score":0.6338427,"about_ca_system_score_codex":0.00058342493,"about_ca_system_score_gemma":0.00007922188,"threshold_uncertainty_score":0.6197963},"labels":[],"label_agreement":null},{"id":"W4311214306","doi":"10.1016/j.enconman.2022.116549","title":"Energetic, GHG, and economic analyses of electrified steam methane reforming using conventional reformer tubes","year":2022,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut interdisciplinaire d'innovation technologique; Ministère de la Santé et des Services Sociaux (Québec); Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Steam reforming; Raw material; Electricity; Methane; Waste management; Process engineering; Environmental science; Hydrogen production; Hydrogen; Engineering; Chemistry","score_opus":0.021826140187019373,"score_gpt":0.2665815666723219,"score_spread":0.24475542648530255,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4311214306","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9950525,0.0011070885,0.0010061633,0.000046923255,0.00020848084,0.00009002779,0.000010018403,0.00004414721,0.0024346407],"genre_scores_gemma":[0.9966472,0.00067549804,0.00038363424,0.00005589597,0.00003068557,0.00001777322,0.000053899,0.000021600415,0.002113819],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989129,0.000035472818,0.00032370226,0.00028452784,0.00021903079,0.00022438852],"domain_scores_gemma":[0.9995932,0.000030430823,0.00010086544,0.00017681782,0.00001534011,0.000083372004],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002681113,0.00015758237,0.00027182582,0.00032261317,0.00013011887,0.000006471097,0.000120266166,0.000036297795,0.00029656437],"category_scores_gemma":[0.0000058066507,0.00015023573,0.00009298081,0.00014286676,0.00004554747,0.00013206158,0.00042063082,0.00009334095,0.0000010786484],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022857198,0.00008124894,0.00015415765,0.0004185994,0.0008953674,0.000030328469,0.00016051333,0.007829383,0.94088155,0.034426857,0.000102106715,0.014791287],"study_design_scores_gemma":[0.0016655783,0.000088648834,0.00005520206,0.000040210787,0.00027528053,0.000038357306,0.0013218381,0.05157568,0.9084968,0.0001269826,0.035980742,0.00033467807],"about_ca_topic_score_codex":0.0011698316,"about_ca_topic_score_gemma":0.000010009971,"teacher_disagreement_score":0.043746296,"about_ca_system_score_codex":0.0002599445,"about_ca_system_score_gemma":0.000016772266,"threshold_uncertainty_score":0.61264354},"labels":[],"label_agreement":null},{"id":"W4311420349","doi":"10.1039/d2cy01317g","title":"Synergetic effect of metal–support for enhanced performance of the Cu–ZnO–ZrO<sub>2</sub>/UGSO catalyst for CO<sub>2</sub>hydrogenation to methanol","year":2022,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada; Ministère de l'Europe et des Affaires Étrangères","keywords":"Catalysis; Methanol; Metal; Materials science; Residue (chemistry); Inorganic chemistry; Copper; Chemistry; Chemical engineering; Metallurgy; Organic chemistry","score_opus":0.006481253263329037,"score_gpt":0.24288709196662284,"score_spread":0.2364058387032938,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4311420349","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9904412,0.00013622158,0.0066758357,0.00015444992,0.00034211343,0.0018401811,0.00015211632,0.00020233591,0.000055523844],"genre_scores_gemma":[0.997074,0.000013466708,0.00036084032,0.00002542464,0.00003160509,0.002238298,0.00014111618,0.000070282345,0.000044966288],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99580103,0.00004871169,0.0010514652,0.0010393658,0.0010635346,0.0009958623],"domain_scores_gemma":[0.99674743,0.00036821683,0.00073428295,0.0015890046,0.00041046078,0.00015058124],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0029346514,0.00044314977,0.0010720238,0.0021172476,0.0005994349,0.000014646284,0.002454371,0.0002219288,0.000007517769],"category_scores_gemma":[0.0022810788,0.00036454637,0.00062209595,0.007332411,0.0009509763,0.00038154755,0.0009874036,0.00040768195,0.000011404494],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008950637,0.00006888016,0.00011650818,0.00028946993,0.00013448489,7.2497807e-7,0.00022472,0.004482587,0.97931635,0.00023197399,0.000010324143,0.015034445],"study_design_scores_gemma":[0.0006774169,0.00064496865,0.00001893058,0.000042293002,0.0004689719,0.00003974222,0.00015803009,0.010203981,0.987035,0.0000764804,0.00024977647,0.00038444778],"about_ca_topic_score_codex":0.000013467595,"about_ca_topic_score_gemma":0.000010120305,"teacher_disagreement_score":0.0146499965,"about_ca_system_score_codex":0.00075151504,"about_ca_system_score_gemma":0.00030915247,"threshold_uncertainty_score":0.9998807},"labels":[],"label_agreement":null},{"id":"W4311532608","doi":"10.1002/cjce.24807","title":"Comprehensive kinetic study for <scp>Fischer</scp> – <scp>Tropsch</scp> reaction over <scp>KMoFe</scp> / <scp>CNTs</scp> nano‐structured catalyst","year":2022,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Fischer–Tropsch process; Catalysis; X-ray photoelectron spectroscopy; Adsorption; Syngas; Chemistry; Activation energy; XANES; Space velocity; Carbon nanotube; Extended X-ray absorption fine structure; Chemical engineering; Carbon monoxide; Materials science; Physical chemistry; Absorption spectroscopy; Spectroscopy; Nanotechnology; Selectivity; Organic chemistry","score_opus":0.012030978693686929,"score_gpt":0.21909349378329898,"score_spread":0.20706251508961204,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4311532608","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9928235,0.0022047935,0.0006437495,0.000068990594,0.0020392009,0.0011979856,0.00026745972,0.00022589132,0.0005284556],"genre_scores_gemma":[0.99511325,0.00001678405,0.00067408034,0.0001729173,0.0016501106,0.00018614785,0.00021653771,0.0004568374,0.001513332],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9929965,0.00013978273,0.0019391808,0.0009253769,0.0016122726,0.0023868987],"domain_scores_gemma":[0.9911696,0.0040406645,0.0010357888,0.0012050739,0.000595522,0.0019534058],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0011980871,0.0012301315,0.0016979816,0.0010371269,0.0006361188,0.00023831737,0.002091502,0.0005171846,0.000022417851],"category_scores_gemma":[0.008109242,0.0011454276,0.0009929868,0.0016445525,0.00019651433,0.00062195706,0.0004131766,0.003445134,0.000022702805],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000008453925,0.00011303618,0.0003183362,0.00034338122,0.0011074023,0.0002765038,0.0048548416,0.0493927,0.9382602,0.00016552032,0.004905118,0.00025452022],"study_design_scores_gemma":[0.0054730237,0.0005328972,0.0011668353,0.00036054,0.0013196564,0.0028116151,0.0074963467,0.021703348,0.74034697,0.00025299995,0.2182116,0.00032419618],"about_ca_topic_score_codex":0.0026354634,"about_ca_topic_score_gemma":0.000354542,"teacher_disagreement_score":0.21330649,"about_ca_system_score_codex":0.002714903,"about_ca_system_score_gemma":0.000732929,"threshold_uncertainty_score":0.99909955},"labels":[],"label_agreement":null},{"id":"W4312084258","doi":"10.1016/j.ijhydene.2022.11.182","title":"Intensified bio-oil steam reforming for high-purity hydrogen production: Numerical simulation and sorption kinetics","year":2022,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Steam reforming; Hydrogen production; Isothermal process; Hydrogen; Chemical engineering; Sorption; Adsorption; Materials science; Catalysis; Chemistry; Thermodynamics; Organic chemistry","score_opus":0.016397187798283374,"score_gpt":0.26035192712625926,"score_spread":0.2439547393279759,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4312084258","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99189645,0.0004003415,0.005708514,0.0006430003,0.0011737199,0.00004856548,0.000024916597,0.000039175993,0.00006534459],"genre_scores_gemma":[0.9979073,0.00004127727,0.00036828214,0.00008189516,0.0010931452,0.000018992587,0.000081628226,0.000039755832,0.00036775388],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981776,0.000039096638,0.00067406887,0.00022121468,0.00068690575,0.00020111521],"domain_scores_gemma":[0.99873865,0.00009989204,0.00049033953,0.0001402215,0.00043008575,0.000100821184],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00039504634,0.00016605928,0.0002693879,0.0003146845,0.000099336394,0.000015159407,0.00032085105,0.00006244848,0.0000399762],"category_scores_gemma":[0.0003150496,0.00015911896,0.0001693095,0.00016638843,0.000032829423,0.0002957515,0.00019794605,0.00024396638,9.620534e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004078922,0.00015206399,0.0000596967,0.000018616774,0.00037461973,0.000034274584,0.00021014352,0.38990477,0.565059,0.0014342229,0.00001847193,0.04232623],"study_design_scores_gemma":[0.001386457,0.0002787529,0.000018418754,0.000051484516,0.00011643503,0.0014556068,0.00024365276,0.12225014,0.8385835,0.001403274,0.033899084,0.0003131757],"about_ca_topic_score_codex":0.000080652106,"about_ca_topic_score_gemma":0.000005390476,"teacher_disagreement_score":0.27352452,"about_ca_system_score_codex":0.0005663103,"about_ca_system_score_gemma":0.00004104036,"threshold_uncertainty_score":0.6488683},"labels":[],"label_agreement":null},{"id":"W4312948601","doi":"10.2139/ssrn.4289794","title":"Microwave-Assisted Hydrothermal Synthesis of Ru/Ceo2 Catalyst for Efficient and Stable Low-Temperature Dry Reforming of Methane","year":2022,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Carbon dioxide reforming; Methane; Catalysis; Hydrothermal circulation; Materials science; Hydrothermal synthesis; Methane reformer; Chemical engineering; Syngas; Chemistry; Inorganic chemistry; Steam reforming; Hydrogen production; Organic chemistry; Engineering","score_opus":0.005322020516582945,"score_gpt":0.21396361393363808,"score_spread":0.20864159341705513,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4312948601","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9942441,0.00427288,0.00088293164,0.000038816204,0.00010490474,0.00025212357,0.000069018,0.000026072066,0.00010913137],"genre_scores_gemma":[0.99886143,0.00013056921,0.00028989217,0.000006508243,0.0000796672,0.000046391273,0.000023776221,0.000070301045,0.00049148157],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971352,0.000063944,0.0006666266,0.00026209437,0.0004237616,0.0014483324],"domain_scores_gemma":[0.99887794,0.00021011636,0.00043828585,0.00027333005,0.0001019169,0.00009840576],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0022781126,0.00023678162,0.0005752216,0.00028908136,0.00018366807,0.000008900363,0.00035084513,0.000096959106,0.000026818827],"category_scores_gemma":[0.0002228828,0.00021139042,0.00028881675,0.00038502412,0.000057191548,0.000106287065,0.00016039533,0.0012961057,4.986859e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024391488,0.00010468562,0.000037582195,0.00022365905,0.0003739377,0.0000031574195,0.00034156756,0.0018080388,0.984897,0.0018162489,0.0000012144067,0.010148947],"study_design_scores_gemma":[0.0009977183,0.00017388845,0.000015471498,0.0001031029,0.000192096,0.0005874436,0.0025803042,0.0018105602,0.9927556,0.00038466233,0.00016074737,0.00023843783],"about_ca_topic_score_codex":0.00022570784,"about_ca_topic_score_gemma":0.00011784347,"teacher_disagreement_score":0.009910509,"about_ca_system_score_codex":0.0012190468,"about_ca_system_score_gemma":0.0006824975,"threshold_uncertainty_score":0.8620251},"labels":[],"label_agreement":null},{"id":"W4313390906","doi":"10.1039/d2re00281g","title":"Stochastic economic evaluation of different production pathways for renewable propylene glycol production <i>via</i> catalytic hydrogenolysis of glycerol","year":2022,"lang":"en","type":"article","venue":"Reaction Chemistry & Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"St. Peter's Hospital","funders":"","keywords":"Hydrogenolysis; Glycerol; Production (economics); Catalysis; Chemistry; Organic chemistry; Pulp and paper industry; Economics; Microeconomics; Engineering","score_opus":0.017370255948638835,"score_gpt":0.2252894741224044,"score_spread":0.20791921817376557,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4313390906","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99349654,0.00015818873,0.0045170174,0.000026642994,0.00061625784,0.0009221635,0.00004662858,0.00015374582,0.00006279459],"genre_scores_gemma":[0.99799055,0.000006182508,0.00012305974,5.147481e-7,0.0003526459,0.0009761867,0.00031477367,0.00007502523,0.00016108462],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979515,0.000015297512,0.000674786,0.0004970448,0.0005621084,0.00029926776],"domain_scores_gemma":[0.99877053,0.000050285376,0.00043402796,0.0005110358,0.00016087265,0.00007323049],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007049367,0.00026786118,0.00042844447,0.00015486975,0.00009127309,0.000004718918,0.0001735461,0.00008933283,0.000038129874],"category_scores_gemma":[0.00036106602,0.00030643938,0.00022183004,0.00028069908,0.000021165259,0.00019546902,0.00008255774,0.00023110455,0.0000010689719],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000050171428,0.000059825456,0.0000038025087,0.00035694416,0.000087184264,9.1069694e-8,0.00007481481,0.45686072,0.5414293,0.0000037256175,0.0000031652476,0.0010702618],"study_design_scores_gemma":[0.0004368075,0.00003034091,0.0000054797547,0.00005260739,0.00029586398,0.00005797489,0.00009411398,0.252056,0.74666834,0.000029633838,0.00007580931,0.00019706656],"about_ca_topic_score_codex":0.000105606334,"about_ca_topic_score_gemma":0.0000032126288,"teacher_disagreement_score":0.20523901,"about_ca_system_score_codex":0.0017897183,"about_ca_system_score_gemma":0.00010688926,"threshold_uncertainty_score":0.9999388},"labels":[],"label_agreement":null},{"id":"W4313537056","doi":"10.1016/j.enconman.2022.116548","title":"Process design and techno-economic analysis of CO2 reformation to synthetic crude oil using H2 produced by decomposition of CH4 in a molten media","year":2022,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada; Lakehead University","keywords":"Syngas; Syngas to gasoline plus; Natural gas; Fischer–Tropsch process; Tonne; Gasoline; Environmental science; Waste management; Catalytic reforming; Hydrogen; Steam reforming; Chemistry; Hydrogen production; Catalysis; Engineering; Organic chemistry","score_opus":0.007773592626554459,"score_gpt":0.22991229528950857,"score_spread":0.2221387026629541,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4313537056","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9960157,0.00009598214,0.003574388,0.00005586077,0.000028410686,0.000086693944,0.000007300581,0.000017908982,0.00011773728],"genre_scores_gemma":[0.9992671,0.00008808881,0.00048221718,0.000015021721,0.000002482312,0.000033002147,0.00007026641,0.0000078702515,0.000033941687],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99933356,0.000020286834,0.00024108696,0.00017466243,0.00013270797,0.00009770728],"domain_scores_gemma":[0.99970305,0.000020180638,0.00010563685,0.00012319906,0.000012453004,0.000035454785],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025350417,0.000079765836,0.00020387779,0.0005791355,0.000033146174,0.0000032459889,0.00007976863,0.000021843418,0.000014938862],"category_scores_gemma":[0.00000728531,0.00008161394,0.000029664616,0.00040991342,0.000014302584,0.00008244588,0.00015727512,0.000037867216,1.00953706e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001582884,0.00007415139,0.00008331145,0.00054363336,0.00036182735,0.0000035519906,0.0010129139,0.531607,0.4545741,0.0006750079,0.000009418649,0.010896803],"study_design_scores_gemma":[0.00037677982,0.000025402447,0.000026349178,0.00004411122,0.00022240319,0.0000015888592,0.00064405205,0.57401043,0.42427665,0.000012029527,0.00026015812,0.000100068246],"about_ca_topic_score_codex":0.00031767882,"about_ca_topic_score_gemma":0.0000059649956,"teacher_disagreement_score":0.042403445,"about_ca_system_score_codex":0.00019410522,"about_ca_system_score_gemma":0.000005873937,"threshold_uncertainty_score":0.332812},"labels":[],"label_agreement":null},{"id":"W4313585068","doi":"10.3390/methane2010002","title":"Fisher–Tropsch Synthesis for Conversion of Methane into Liquid Hydrocarbons through Gas-to-Liquids (GTL) Process: A Review","year":2023,"lang":"en","type":"review","venue":"Methane","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":62,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Memorial University of Newfoundland","funders":"","keywords":"Fischer–Tropsch process; Syngas; Gas to liquids; Syngas to gasoline plus; Methane; Partial oxidation; Natural gas; Steam reforming; Methane reformer; Catalytic reforming; Waste management; Hydrodeoxygenation; Chemistry; Catalysis; Organic chemistry; Hydrogen production; Engineering; Selectivity","score_opus":0.06018880645044815,"score_gpt":0.3630696822628119,"score_spread":0.3028808758123637,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4313585068","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00008066306,0.9912521,0.0023480053,0.00018188663,0.00052169466,0.004328298,0.00026342808,0.00052594766,0.0004979356],"genre_scores_gemma":[0.000032245618,0.99011976,0.0033427863,0.000110421825,0.00042010128,0.003952727,0.0005153488,0.0005859715,0.000920666],"study_design_codex":"systematic_review","study_design_gemma":"not_applicable","domain_scores_codex":[0.9933901,0.0003112729,0.0026671886,0.0014188603,0.0010457808,0.0011668197],"domain_scores_gemma":[0.9933957,0.0030244577,0.0011912487,0.0016781109,0.00027232172,0.00043818683],"candidate_categories":["metaresearch","metaepi_narrow"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.002696141,0.001353181,0.0070291236,0.0006817454,0.000061133906,0.00001457245,0.0015954146,0.0008970285,0.0001516216],"category_scores_gemma":[0.009679581,0.0011310163,0.0024682463,0.0029670126,0.00011489927,0.00026918392,0.00052885176,0.00090731494,0.0002905548],"study_design_candidate":"systematic_review","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00020447232,0.00012610227,9.637704e-8,0.8016563,0.0019214473,0.000039700026,0.00037187646,0.000010510675,0.0035479148,0.000090797796,0.00048700458,0.19154377],"study_design_scores_gemma":[0.00039801854,0.00031986585,5.8863607e-9,0.16550003,0.0059252526,0.00006612502,0.00004912904,0.00006058967,0.08930355,0.000080335456,0.7371149,0.0011822156],"about_ca_topic_score_codex":0.0002970662,"about_ca_topic_score_gemma":0.000012491431,"teacher_disagreement_score":0.7366279,"about_ca_system_score_codex":0.00061348255,"about_ca_system_score_gemma":0.0005070594,"threshold_uncertainty_score":0.9999219},"labels":[],"label_agreement":null},{"id":"W4318194845","doi":"10.1002/cjce.24859","title":"Recent advances in hydrogen production through catalytic steam reforming of ethanol: Advances in catalytic design","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":34,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs; Canada Foundation for Innovation; University of Regina","keywords":"Steam reforming; Catalysis; Bimetallic strip; Hydrogen production; Chemical engineering; Selectivity; Hydrogen; Materials science; Catalyst support; Chemistry; Inorganic chemistry; Organic chemistry","score_opus":0.018663978035075322,"score_gpt":0.2440682484860244,"score_spread":0.22540427045094907,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4318194845","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9725828,0.025668623,0.00022807527,0.0004553076,0.0005020964,0.00029599652,0.0000070002948,0.000052347285,0.00020771814],"genre_scores_gemma":[0.99810773,0.0014103187,0.00019921729,0.000007865456,0.00017275206,0.000013259987,0.0000094090055,0.000056069945,0.00002340417],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978875,0.000022403015,0.00089080783,0.00021080168,0.0003568422,0.0006316375],"domain_scores_gemma":[0.99894196,0.00019459048,0.00024840332,0.0002973939,0.00009551943,0.0002221408],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010212978,0.00024172424,0.0005029925,0.0005698779,0.000030776806,0.000008176808,0.00049829786,0.00013191804,0.0000058837386],"category_scores_gemma":[0.001500381,0.00019685968,0.00011657054,0.0016225951,0.00007972461,0.0008265156,0.000041906776,0.0007384611,0.0000058307214],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000044307362,0.000015404292,0.000114709976,0.0003277372,0.00003792422,0.00010600668,0.0016510091,0.5088183,0.46737307,0.00010350168,0.0000053625536,0.021402618],"study_design_scores_gemma":[0.00041171844,0.000024517336,0.000011893928,0.00077684276,0.000027838967,0.00020131914,0.00020756386,0.011631322,0.98353416,0.0002970649,0.0026358145,0.00023994861],"about_ca_topic_score_codex":0.0009408386,"about_ca_topic_score_gemma":0.0011499043,"teacher_disagreement_score":0.5161611,"about_ca_system_score_codex":0.0014160731,"about_ca_system_score_gemma":0.0003519146,"threshold_uncertainty_score":0.80277044},"labels":[],"label_agreement":null},{"id":"W4318706860","doi":"10.1038/s41467-023-36259-9","title":"COx hydrogenation to methanol and other hydrocarbons under mild conditions with Mo3S4@ZSM-5","year":2023,"lang":"en","type":"article","venue":"Nature Communications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":51,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"Ministry of Science and Technology of the People's Republic of China; National Natural Science Foundation of China","keywords":"Methanol; ZSM-5; Chemistry; Catalysis; Organic chemistry; Zeolite","score_opus":0.025021589801540116,"score_gpt":0.30706397756894505,"score_spread":0.2820423877674049,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4318706860","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9373627,0.004813287,0.0030714243,0.02101298,0.00025724777,0.0016153422,0.00042197667,0.0024315594,0.029013526],"genre_scores_gemma":[0.9957846,0.000059905447,0.0021300856,0.00082613877,0.00003501257,0.00018072735,0.0002759004,0.000060403752,0.00064725394],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990464,0.00004205713,0.00020372187,0.00023131994,0.00022342436,0.0002531077],"domain_scores_gemma":[0.9981048,0.00036549417,0.00005937398,0.0012718545,0.000057631954,0.00014086376],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002027396,0.00016819779,0.00018068499,0.00033021354,0.00023192794,0.00002243422,0.0005328937,0.00022724512,0.000021745242],"category_scores_gemma":[0.00015853708,0.00015008767,0.000054415555,0.00121286,0.00009350313,0.00012131041,0.00029127015,0.00068307406,0.00010990329],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003262726,0.00016881156,0.0008913054,0.000054511227,0.00056798506,0.000004737042,0.0027643384,0.0026134097,0.8758619,0.11358631,0.0022453319,0.0012087389],"study_design_scores_gemma":[0.0033857222,0.00019028157,0.009141845,0.00062531367,0.00075712893,0.00023206153,0.0024053075,0.09614285,0.6134025,0.008115579,0.263114,0.002487418],"about_ca_topic_score_codex":0.00009221911,"about_ca_topic_score_gemma":0.0004210169,"teacher_disagreement_score":0.2624594,"about_ca_system_score_codex":0.0001043294,"about_ca_system_score_gemma":0.00003128655,"threshold_uncertainty_score":0.61203974},"labels":[],"label_agreement":null},{"id":"W4319237613","doi":"10.1016/j.enconman.2023.116674","title":"Techno-economic analysis for hydrogen-burning power plant with onsite hydrogen production unit based on methane catalytic decomposition","year":2023,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":18,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Natural gas; Hydrogen production; Cost of electricity by source; Hydrogen; Waste management; Methane; Renewable natural gas; Environmental science; Combustion; Electricity generation; Chemistry; Fuel gas; Engineering; Power (physics); Organic chemistry; Thermodynamics","score_opus":0.009091840407116358,"score_gpt":0.22278359402534553,"score_spread":0.21369175361822917,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4319237613","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9876044,0.00003130719,0.010082028,0.00038263833,0.00012739477,0.00034961003,0.000025273492,0.00040538184,0.0009920155],"genre_scores_gemma":[0.9970088,0.00003589262,0.00024599966,0.00007115737,0.00002797957,0.000085176405,0.00089898607,0.00003215643,0.0015938445],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989264,0.000013318077,0.00019259106,0.00042875562,0.0001757949,0.00026315774],"domain_scores_gemma":[0.99944884,0.000047374444,0.00009016303,0.0003065654,0.00001767522,0.00008936959],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025821797,0.00019128431,0.00024120173,0.000888057,0.00010414234,0.000012968621,0.000101389036,0.000059850532,0.000026978872],"category_scores_gemma":[0.000007995057,0.00017119123,0.00011339499,0.00061521557,0.000023947618,0.000096160824,0.000075652744,0.000066890745,0.000022651413],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006133789,0.00009209529,0.00037042963,0.00036265812,0.0026481238,0.00008326963,0.00015619908,0.9125015,0.0730418,0.0034092118,0.00014962495,0.0065716947],"study_design_scores_gemma":[0.0009584859,0.00009661677,0.00008045296,0.000074817915,0.0007147788,0.0000060219872,0.0001772253,0.47872627,0.5093192,0.00002024672,0.009543555,0.00028235326],"about_ca_topic_score_codex":0.00017395987,"about_ca_topic_score_gemma":0.000038027814,"teacher_disagreement_score":0.4362774,"about_ca_system_score_codex":0.00017578324,"about_ca_system_score_gemma":0.000009899592,"threshold_uncertainty_score":0.6980976},"labels":[],"label_agreement":null},{"id":"W4319786167","doi":"10.1002/cjce.24876","title":"A review on catalyst development for conventional thermal dry reforming of methane at low temperature","year":2023,"lang":"en","type":"review","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Carbon dioxide reforming; Methane; Catalysis; Coke; Methane reformer; Chemical engineering; Materials science; Industrial catalysts; Process engineering; Waste management; Steam reforming; Hydrogen production; Chemistry; Catalyst support; Organic chemistry; Metallurgy; Engineering","score_opus":0.02986869747930319,"score_gpt":0.2711070844116961,"score_spread":0.24123838693239294,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4319786167","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0021606018,0.9965355,0.000017835117,0.000047329457,0.00044300128,0.0006230471,0.00011979201,0.000032253567,0.000020656298],"genre_scores_gemma":[0.0016564656,0.9926525,0.0009815939,0.00012848573,0.0017994987,0.00030132986,0.0008748209,0.0006927925,0.00091253256],"study_design_codex":"systematic_review","study_design_gemma":"not_applicable","domain_scores_codex":[0.9967937,0.000027861528,0.0017892113,0.00026665002,0.00047410218,0.00064850465],"domain_scores_gemma":[0.9973231,0.0005951557,0.000867327,0.0004355896,0.00022634988,0.0005525018],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013438297,0.00058237574,0.0021994922,0.00046774693,0.000069724236,0.000015270809,0.0009511444,0.00041081966,0.00003857975],"category_scores_gemma":[0.0012433311,0.00038667917,0.0012642671,0.00060077244,0.00006612448,0.00008533353,0.000089456546,0.0012044209,0.000021674477],"study_design_candidate":"systematic_review","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009123692,0.00007152461,9.787545e-7,0.60349876,0.006875618,0.00031350667,0.0006959617,0.0028518618,0.11297233,0.000557452,0.0011228624,0.2709479],"study_design_scores_gemma":[0.0005350554,0.00003731703,1.9836378e-7,0.2448169,0.0014610856,0.00052033784,0.0000069353177,0.00013356228,0.14960532,0.0000051652796,0.60206527,0.0008128309],"about_ca_topic_score_codex":0.00013808167,"about_ca_topic_score_gemma":0.000071317394,"teacher_disagreement_score":0.60094243,"about_ca_system_score_codex":0.0019605486,"about_ca_system_score_gemma":0.0015293377,"threshold_uncertainty_score":0.9998585},"labels":[],"label_agreement":null},{"id":"W4320014290","doi":"10.2139/ssrn.4335385","title":"Fischer-Tropsch to Light Olefins Over Bimetallic Promoted Fe/Cnts Nanocatalyst: Techno-Economic and Life-Cycle Assessment","year":2023,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Bimetallic strip; Fischer–Tropsch process; Life-cycle assessment; Materials science; Catalysis; Nanotechnology; Chemical engineering; Business; Metallurgy; Chemistry; Economics; Organic chemistry; Engineering; Macroeconomics","score_opus":0.006497899690599276,"score_gpt":0.2519178159256338,"score_spread":0.2454199162350345,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4320014290","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9956066,0.0007125825,0.0011858897,0.0011378456,0.00020349523,0.00029127617,0.00000974357,0.00034128476,0.00051129184],"genre_scores_gemma":[0.996517,0.00046227197,0.00019449915,0.000038298673,0.00033208646,0.00003892899,0.000028668725,0.000116740914,0.0022714976],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9959729,0.000033170014,0.00057284883,0.00048279684,0.00037487556,0.0025634228],"domain_scores_gemma":[0.99891895,0.00005167139,0.0001804062,0.00042130117,0.000041337084,0.0003863588],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001388585,0.00036376933,0.00047336865,0.00054200715,0.00020971833,0.000084470244,0.00046306144,0.00019389836,0.00006625941],"category_scores_gemma":[0.0001508509,0.00032931622,0.00019901028,0.0007101635,0.0000295207,0.00035260097,0.00027853434,0.0019036463,0.00032979602],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007136991,0.000110801906,0.0014633426,0.000089895235,0.0012199384,0.000041481257,0.00028739448,0.0021400605,0.94958097,0.016565964,0.00010688455,0.028321918],"study_design_scores_gemma":[0.014607093,0.002664512,0.016080374,0.0009924128,0.00149237,0.005534486,0.0040624603,0.13235988,0.68845356,0.07038671,0.056317996,0.007048137],"about_ca_topic_score_codex":0.00023503389,"about_ca_topic_score_gemma":0.0005269383,"teacher_disagreement_score":0.26112738,"about_ca_system_score_codex":0.002002409,"about_ca_system_score_gemma":0.0010107978,"threshold_uncertainty_score":0.9999159},"labels":[],"label_agreement":null},{"id":"W4320473012","doi":"10.1039/bk9781849734073-00327","title":"Methane for Transportation Fuel and Chemical Production","year":2012,"lang":"en","type":"book-chapter","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Natural gas; Methane; Petrochemical; Waste management; Energy carrier; Liquefied petroleum gas; Combustion; Liquefied natural gas; Environmental science; Syngas; Associated petroleum gas; Process engineering; Hydrogen; Chemistry; Engineering; Organic chemistry","score_opus":0.020510218033435227,"score_gpt":0.2361636900565665,"score_spread":0.2156534720231313,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4320473012","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.03647427,0.035697773,0.037446298,0.001743042,0.005852749,0.010491925,0.0012713433,0.004105004,0.8669176],"genre_scores_gemma":[0.054751024,0.0004248226,0.00746285,0.000032787324,0.0024453409,0.00013885954,0.0024839179,0.00033159778,0.9319288],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989844,0.0000010763036,0.00031471337,0.0003199096,0.0001623018,0.0002176016],"domain_scores_gemma":[0.9994895,0.00004903017,0.00009985068,0.0001957599,0.000058463225,0.00010741424],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001565565,0.00026269502,0.00034212923,0.000087406144,0.000013239461,0.000004099043,0.000062980755,0.00036174554,0.00016056436],"category_scores_gemma":[0.00004782285,0.00023758355,0.00014726639,0.00001638725,0.00003344927,0.00013164894,0.0000095738205,0.00022108703,0.00001817116],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009296691,0.000020369316,0.0000027656656,0.0020286818,0.00026387858,0.0000015593631,0.00032912323,0.0000056636404,0.8316933,0.11051849,0.00012867084,0.05491452],"study_design_scores_gemma":[0.00043800313,0.000020065992,0.0000027541507,0.00015317176,0.0004757341,0.000032039203,0.000011121695,0.000077782766,0.80501986,0.0055692596,0.1875948,0.0006053913],"about_ca_topic_score_codex":0.000010477224,"about_ca_topic_score_gemma":0.000013668206,"teacher_disagreement_score":0.18746613,"about_ca_system_score_codex":0.00007869333,"about_ca_system_score_gemma":0.000012428787,"threshold_uncertainty_score":0.96883756},"labels":[],"label_agreement":null},{"id":"W4322761373","doi":"10.1016/j.cej.2023.142230","title":"A low carbon methanol process using natural gas pyrolysis in a catalytic molten metal bubble reactor","year":2023,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":25,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Pyrolysis; Methane; Steam reforming; Natural gas; Methanol; Carbon fibers; Liquid metal; Chemical engineering; Waste management; Hydrogen; Catalysis; Hydrogen production; Syngas; Chemistry; Molten salt; Materials science; Inorganic chemistry; Organic chemistry; Composite material","score_opus":0.011798873018142798,"score_gpt":0.24585486880444443,"score_spread":0.23405599578630162,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4322761373","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99801683,0.00034481628,0.00045674003,0.0000522896,0.0004483649,0.00014233982,0.0000071775157,0.00042210324,0.0001093248],"genre_scores_gemma":[0.99807024,0.000015203659,0.0011265591,0.000008218661,0.0005143217,0.00002401208,0.000033866894,0.00015145056,0.00005610765],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99701905,0.000014879532,0.0007777774,0.0004444273,0.0006639662,0.0010798785],"domain_scores_gemma":[0.99885136,0.0001668063,0.00015995973,0.00034339033,0.0001026716,0.00037584105],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00057931856,0.00046413302,0.00071788736,0.000809377,0.000039136066,0.000054662938,0.0005258546,0.00025354137,0.000017108163],"category_scores_gemma":[0.0012037434,0.00043518108,0.00034123706,0.00201189,0.000037646543,0.00037278558,0.0001726883,0.0016501802,0.000038576076],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000026284031,0.000035416135,0.000082066756,0.00022790993,0.00014197739,0.0002681489,0.00035863568,0.05673805,0.94156295,0.0000053103995,0.000003660827,0.0005495887],"study_design_scores_gemma":[0.000505185,0.000006561606,0.000014437406,0.00024612242,0.0000679722,0.000530477,0.000058895926,0.43348286,0.5647197,0.000025363288,0.000020312862,0.00032215775],"about_ca_topic_score_codex":0.000047046244,"about_ca_topic_score_gemma":0.0000013533547,"teacher_disagreement_score":0.3768433,"about_ca_system_score_codex":0.00079166755,"about_ca_system_score_gemma":0.00010106548,"threshold_uncertainty_score":0.99981},"labels":[],"label_agreement":null},{"id":"W4323975086","doi":"10.1016/j.fuel.2023.127947","title":"Conversion of CO2 by reverse water gas shift (RWGS) reaction using a hydrogen oxyflame","year":2023,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":26,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Hydro-Québec","funders":"","keywords":"Syngas; Water-gas shift reaction; Process engineering; Residence time (fluid dynamics); Hydrogen; Operating temperature; Fossil fuel; Environmental science; Greenhouse gas; Materials science; Chemical engineering; Syngas to gasoline plus; Nuclear engineering; Steam reforming; Thermodynamics; Chemistry; Hydrogen production; Organic chemistry","score_opus":0.01585369933812495,"score_gpt":0.23687899322533593,"score_spread":0.22102529388721098,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4323975086","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99898964,0.000034071985,0.00007446344,0.00004881203,0.00015723908,0.000091054724,0.000016295538,0.00016939196,0.0004190092],"genre_scores_gemma":[0.99872124,0.000018845334,0.000049232724,0.000011128888,0.000064942484,0.0000036933816,0.00017164719,0.000034778695,0.000924466],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991047,0.000011931177,0.00022393462,0.00018032256,0.00021052062,0.00026863086],"domain_scores_gemma":[0.99958754,0.000029955612,0.000060484344,0.00022861692,0.000023901863,0.00006951979],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00020301665,0.00011653139,0.00018869445,0.000115559196,0.000024265562,0.0000037433783,0.00010247408,0.00011044108,0.0000860526],"category_scores_gemma":[0.000048337028,0.00009722726,0.000101088444,0.00021318893,0.000030851257,0.0001710034,0.00009516171,0.00013523719,0.00027086402],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001705364,0.0000104560095,0.00016079462,0.0001852868,0.000028990915,0.000009193781,0.00050647004,0.000148215,0.9986404,0.0000067550623,0.00018290969,0.000103452585],"study_design_scores_gemma":[0.00033942517,0.000010830629,0.000025980178,0.00006042946,0.000038529663,0.00000880321,0.000117641015,0.010478535,0.9810148,0.00004865586,0.0077246567,0.00013173498],"about_ca_topic_score_codex":0.00063067686,"about_ca_topic_score_gemma":0.0000033442402,"teacher_disagreement_score":0.017625643,"about_ca_system_score_codex":0.00012278897,"about_ca_system_score_gemma":0.000008656406,"threshold_uncertainty_score":0.39648128},"labels":[],"label_agreement":null},{"id":"W4362508016","doi":"10.1016/j.fuproc.2023.107750","title":"Direct flue gas hydrogenation to methane over hydroxyapatite-supported nickel catalyst","year":2023,"lang":"en","type":"article","venue":"Fuel Processing Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"National Research Council Canada; Université de Sherbrooke","funders":"","keywords":"Methanation; Flue gas; Methane; Substitute natural gas; Catalysis; Greenhouse gas; Carbon fibers; Chemistry; Power to gas; NOx; Chemical engineering; Environmental science; Materials science; Waste management; Syngas; Organic chemistry; Engineering; Composite material; Combustion","score_opus":0.012800433535570283,"score_gpt":0.26511609380980544,"score_spread":0.25231566027423513,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4362508016","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98764366,0.00046725475,0.0019270203,0.0011395692,0.00024519928,0.00037622088,0.000025808396,0.005279603,0.0028956584],"genre_scores_gemma":[0.99601066,0.000019468549,0.0013804557,0.00007853145,0.00011328832,0.00018649554,0.00025002833,0.00012810864,0.0018329695],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974942,0.000016583377,0.0005510646,0.000701591,0.00041439137,0.00082217273],"domain_scores_gemma":[0.99876547,0.00007117107,0.00018073777,0.0006885343,0.00012837643,0.00016568827],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00044410842,0.00035478926,0.0005138712,0.0016469293,0.0001113929,0.00002795273,0.0006119926,0.00047411444,0.000060915827],"category_scores_gemma":[0.0011169709,0.00035150748,0.00011918799,0.0046439394,0.00009562976,0.00028590014,0.00040657178,0.00043762074,0.00079841603],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001769354,0.000039983428,0.00029468205,0.00032003594,0.000066844776,0.00006044083,0.0003265342,0.00045876586,0.96085984,0.00018587521,0.00021956317,0.037149742],"study_design_scores_gemma":[0.00047533688,0.00004651519,0.000053848853,0.0001538868,0.000068024885,0.000066562876,0.00010734431,0.027890177,0.9573808,0.001253386,0.012013199,0.00049094955],"about_ca_topic_score_codex":0.0001085353,"about_ca_topic_score_gemma":0.000047819132,"teacher_disagreement_score":0.036658794,"about_ca_system_score_codex":0.00027895995,"about_ca_system_score_gemma":0.00008999887,"threshold_uncertainty_score":0.99997956},"labels":[],"label_agreement":null},{"id":"W4364380976","doi":"10.1002/cjce.24906","title":"Design framework for dimethyl ether ( <scp>DME)</scp> production from coal and biomass‐derived syngas via simulation approach","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Ministry of Education, India","keywords":"Syngas; Dimethyl ether; Methanol; Coal; Fischer–Tropsch process; Yield (engineering); Biomass (ecology); Chemistry; Gibbs free energy; Chemical engineering; Process engineering; Pulp and paper industry; Waste management; Materials science; Organic chemistry; Catalysis; Thermodynamics; Selectivity; Engineering","score_opus":0.025534314174456178,"score_gpt":0.2339615539291391,"score_spread":0.2084272397546829,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4364380976","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5960188,0.00033773095,0.40288505,0.00014349174,0.0003181836,0.00021101572,0.000009293061,0.00006835082,0.000008114632],"genre_scores_gemma":[0.97748977,0.0000024712995,0.021611812,0.000014278733,0.0007278302,0.000017059685,0.00002236174,0.000083306426,0.00003112702],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99864304,0.00002256731,0.00041522065,0.00021169108,0.00023532483,0.00047217833],"domain_scores_gemma":[0.99784464,0.0012741779,0.00015740946,0.00022297783,0.00010476325,0.00039601384],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00068793405,0.00022930563,0.00033603815,0.00030671916,0.000092894814,0.000047631176,0.00026741327,0.00024393777,0.0000039294478],"category_scores_gemma":[0.0027992583,0.00018670525,0.00013207659,0.00049312285,0.000062227446,0.00017184255,0.00002916935,0.000566021,0.000004162468],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000007036203,0.0000038445687,0.000014471818,0.00005485847,0.000112712274,0.0000052902537,0.0006992957,0.29231003,0.70611197,0.0000994925,0.000023445824,0.0005575947],"study_design_scores_gemma":[0.00022926638,0.000015383546,0.00003175681,0.00009968504,0.00007719409,0.00004034007,0.000044678618,0.38411462,0.613655,0.0013269203,0.0002669763,0.000098176744],"about_ca_topic_score_codex":0.00036433767,"about_ca_topic_score_gemma":0.0000079955125,"teacher_disagreement_score":0.38147098,"about_ca_system_score_codex":0.00026263902,"about_ca_system_score_gemma":0.00009935979,"threshold_uncertainty_score":0.7613619},"labels":[],"label_agreement":null},{"id":"W4365455991","doi":"10.1016/j.fuel.2023.128366","title":"Microwave-assisted hydrothermal synthesis of Ru/CeO2 catalyst for efficient and stable low-temperature dry reforming of methane","year":2023,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":25,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Mitacs; Canadian Natural Resources Limited","keywords":"Catalysis; Carbon dioxide reforming; Coke; Chemical engineering; Methane; Reactivity (psychology); Hydrothermal circulation; X-ray photoelectron spectroscopy; Materials science; Chemistry; Syngas; Inorganic chemistry; Metallurgy; Organic chemistry","score_opus":0.010862787333561675,"score_gpt":0.23403345407380918,"score_spread":0.22317066674024752,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4365455991","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99809885,0.00059793645,0.000107926004,0.000021605858,0.000112998896,0.00030719457,0.0002016675,0.000107068336,0.00044472495],"genre_scores_gemma":[0.9981465,0.000022591035,0.00083736447,0.0000050764047,0.000059928105,0.0000645179,0.00009300174,0.000067842026,0.0007032156],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985436,0.000017655302,0.0004986253,0.00029402063,0.00024682787,0.0003992684],"domain_scores_gemma":[0.9988873,0.00035332955,0.00018692657,0.00038235926,0.0000929279,0.000097134056],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005198954,0.00021377,0.00054890447,0.00025996155,0.000037461945,0.000006712599,0.00020018514,0.00017243277,0.000014635109],"category_scores_gemma":[0.00043064516,0.00018422924,0.0001904676,0.00055597327,0.000067863206,0.000082412735,0.00013140058,0.00014733082,0.0000068521867],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007292713,0.00004355149,0.000044877244,0.0020912548,0.000120317665,0.0000047519798,0.0005433147,0.00044329392,0.9928147,0.000090818714,0.000008844171,0.0037213569],"study_design_scores_gemma":[0.00053134747,0.00002455446,0.00017587573,0.00036106954,0.00010065962,0.000011051648,0.00039261486,0.0043103057,0.99363106,0.000015922642,0.0002456775,0.00019982691],"about_ca_topic_score_codex":0.00022461833,"about_ca_topic_score_gemma":0.00003216135,"teacher_disagreement_score":0.0038670118,"about_ca_system_score_codex":0.00008512203,"about_ca_system_score_gemma":0.000041283492,"threshold_uncertainty_score":0.75126505},"labels":[],"label_agreement":null},{"id":"W4366608418","doi":"10.1016/j.fuel.2023.128429","title":"Modeling of catalyst poisoning during hydrogen production via methane steam and dry reforming","year":2023,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":19,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation; University of Regina","keywords":"Steam reforming; Methane; Hydrogen production; Methane reformer; Hydrogen sulfide; Hydrogen; Biogas; Parametric statistics; Work (physics); Process engineering; Environmental science; Nuclear engineering; Chemistry; Chemical engineering; Waste management; Thermodynamics; Engineering; Mathematics; Physics; Organic chemistry; Statistics; Sulfur","score_opus":0.013570039439649156,"score_gpt":0.23569095299533574,"score_spread":0.22212091355568658,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4366608418","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.998094,0.000643964,0.00022668143,0.000034088174,0.00016669522,0.00014965977,0.000005350945,0.0003422427,0.00033727294],"genre_scores_gemma":[0.99871546,0.00007887564,0.0002051433,0.0000020435327,0.00020506188,0.000019858098,0.000051714396,0.00006266601,0.00065915036],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985104,0.000013942069,0.00043544357,0.00036090254,0.00028527674,0.00039400868],"domain_scores_gemma":[0.99936414,0.000027737136,0.00010088318,0.00035315912,0.000055420875,0.000098645796],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000459713,0.00019143039,0.0003310186,0.00032789094,0.000070988564,0.000004220351,0.0001423901,0.00010403622,0.000005891778],"category_scores_gemma":[0.00025931405,0.00018411149,0.0000938241,0.0006210402,0.0000289421,0.00034900854,0.00020960941,0.00022928021,0.000023684262],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019415156,0.000009307027,0.00019748625,0.00058700383,0.000063117135,0.000009376223,0.001064537,0.025518516,0.9692616,0.000014477927,1.8956663e-7,0.0032550069],"study_design_scores_gemma":[0.00027570935,0.000010450401,0.000047718193,0.00016920248,0.000047209247,0.000056621015,0.00056046975,0.16296716,0.83553994,0.0000999994,0.000022121947,0.00020338818],"about_ca_topic_score_codex":0.00047976148,"about_ca_topic_score_gemma":0.000030970972,"teacher_disagreement_score":0.13744864,"about_ca_system_score_codex":0.0001255137,"about_ca_system_score_gemma":0.00001666426,"threshold_uncertainty_score":0.7507849},"labels":[],"label_agreement":null},{"id":"W4367360111","doi":"10.5220/0012000200003491","title":"Optimal Control Strategy for Mixed Fuel Use in a Renewable Polygeneration System","year":2023,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Concordia University","funders":"","keywords":"Renewable energy; Control (management); Computer science; Waste management; Environmental science; Process engineering; Engineering; Electrical engineering","score_opus":0.030181643618614775,"score_gpt":0.25465682607476314,"score_spread":0.22447518245614836,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4367360111","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.94229835,0.00005279717,0.05515372,0.000051879975,0.00022824129,0.00056371477,0.00004479624,0.0006876242,0.00091887027],"genre_scores_gemma":[0.99388826,0.000001938168,0.0011232113,0.0000081310645,0.000109869616,0.00015990523,0.000114704555,0.000034474728,0.004559525],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99902266,0.000012230983,0.00029966448,0.00020835346,0.00012330455,0.0003337642],"domain_scores_gemma":[0.9995317,0.00014524476,0.000038902555,0.0001827201,0.000037241163,0.000064190666],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00028088826,0.00012213536,0.00021896014,0.00017025069,0.000025651163,0.00003194731,0.00008725362,0.00009821223,0.000009594323],"category_scores_gemma":[0.00012561894,0.00010895974,0.00008111497,0.00032693258,0.0000063712228,0.00023695304,0.000022085007,0.00006621205,0.000034426776],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005578736,0.000012438927,0.00006833275,0.00023085169,0.0000316251,0.000013255565,0.000048113954,0.43360132,0.5623256,0.0030783264,0.0001556237,0.00037874343],"study_design_scores_gemma":[0.001444456,0.000024869521,0.00005689534,0.000039414197,0.000015722473,0.00000939354,0.00029274958,0.8047057,0.19281718,0.000012722701,0.0004290189,0.0001518815],"about_ca_topic_score_codex":0.0014262288,"about_ca_topic_score_gemma":0.000624909,"teacher_disagreement_score":0.37110436,"about_ca_system_score_codex":0.00017464352,"about_ca_system_score_gemma":0.00002667983,"threshold_uncertainty_score":0.44432494},"labels":[],"label_agreement":null},{"id":"W4367400176","doi":"10.1016/j.enconman.2023.117079","title":"Green synthesis of Cu-Mo promoted Fe catalyst for production of the gaseous and liquid fuels through Fischer-Tropsch synthesis","year":2023,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs; Canadian Light Source","keywords":"Catalysis; Selectivity; Fischer–Tropsch process; Olefin fiber; Chemistry; Carbide; Chemical engineering; Inorganic chemistry; Materials science; Organic chemistry","score_opus":0.012364624250349303,"score_gpt":0.21698900307216107,"score_spread":0.20462437882181175,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4367400176","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99700993,0.00017085201,0.00052929437,0.00089157105,0.00021003811,0.0004340064,0.000019554918,0.00009890603,0.00063582964],"genre_scores_gemma":[0.99609697,0.00050791574,0.00024185433,0.000016409636,0.000035575165,0.00010239371,0.000012434537,0.00002389264,0.0029625478],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99912363,0.00002383101,0.00023522931,0.00025908757,0.00018758366,0.000170653],"domain_scores_gemma":[0.99943006,0.000108919434,0.000121467965,0.00026199757,0.000040902392,0.00003667536],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021946832,0.00013287964,0.00023552371,0.000106968684,0.00007079678,0.0000040648597,0.00013348616,0.000057202247,0.000007430197],"category_scores_gemma":[0.0001430368,0.000098817705,0.00009039855,0.00029491461,0.000079628626,0.000090378366,0.0002536462,0.000041363473,0.0000012295836],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00044095478,0.00012864724,0.000071093855,0.005877122,0.0008596965,0.000008663105,0.0010330104,0.0003158671,0.92315423,0.006033786,0.0008558935,0.061221033],"study_design_scores_gemma":[0.00024113343,0.00003527408,0.00008454306,0.00021636367,0.00022379232,0.000003993918,0.00054983253,0.0018833616,0.98582,0.000058238827,0.010760498,0.00012298452],"about_ca_topic_score_codex":0.00046797155,"about_ca_topic_score_gemma":0.000016212562,"teacher_disagreement_score":0.06266575,"about_ca_system_score_codex":0.000035597972,"about_ca_system_score_gemma":0.0000063850543,"threshold_uncertainty_score":0.40296692},"labels":[],"label_agreement":null},{"id":"W4368359182","doi":"10.1002/anie.202304470","title":"Solar Hydrocarbons: Single‐Step, Atmospheric‐Pressure Synthesis of C<sub>2</sub>−C<sub>4</sub> Alkanes and Alkenes from CO<sub>2</sub>","year":2023,"lang":"en","type":"article","venue":"Angewandte Chemie International Edition","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada; University of Toronto; Ministero dello Sviluppo Economico; National Key Research and Development Program of China; Lions Clubs International Foundation; Alexander von Humboldt-Stiftung","keywords":"Spinel; Hydrocarbon; Atmospheric pressure; Selectivity; Materials science; Cobalt; Alloy; Analytical Chemistry (journal); Chemical engineering; Chemistry; Inorganic chemistry; Organic chemistry; Metallurgy; Catalysis; Geology","score_opus":0.010747239243995592,"score_gpt":0.22238112038791705,"score_spread":0.21163388114392145,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4368359182","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99410343,0.00063173746,0.0014901961,0.00034794692,0.0012437905,0.0002683146,0.00075720233,0.0004785672,0.0006788017],"genre_scores_gemma":[0.99435323,0.0010708187,0.00018428128,0.000087867695,0.0019475758,0.0001712628,0.0020053252,0.00014907168,0.000030544208],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99654967,0.000044151082,0.0008823485,0.0008309326,0.0011018796,0.00059104693],"domain_scores_gemma":[0.99766296,0.00087113335,0.000491536,0.0004812541,0.00025205917,0.0002410422],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00039085312,0.00058022013,0.0007008419,0.00017085405,0.00013289136,0.00008435085,0.00047782244,0.0004672057,0.000034594996],"category_scores_gemma":[0.0010226233,0.0006145428,0.0003581933,0.00052246486,0.00020216957,0.0007813454,0.00027878096,0.0004525751,0.00009169483],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010704771,0.00012914241,0.00020944132,0.0002060746,0.0006270562,0.000049902894,0.00027645784,0.00023124348,0.98247635,0.00003221139,0.0015432255,0.014111868],"study_design_scores_gemma":[0.0007558576,0.00004295385,0.0004086956,0.0006165955,0.00031446107,0.00004925494,0.00022850324,0.005217456,0.98980695,0.0004959063,0.0014404028,0.0006229455],"about_ca_topic_score_codex":0.00013994907,"about_ca_topic_score_gemma":0.000054811157,"teacher_disagreement_score":0.013488922,"about_ca_system_score_codex":0.0002964188,"about_ca_system_score_gemma":0.00006005559,"threshold_uncertainty_score":0.9996306},"labels":[],"label_agreement":null},{"id":"W4368366468","doi":"10.1021/acssuschemeng.3c00600","title":"Highly Efficient CuPd<sub>0.1</sub>/γ-Al<sub>2</sub>O<sub>3</sub> Catalyst with Isolated Pd Species for CO<sub>2</sub> Hydrogenation to Methanol","year":2023,"lang":"en","type":"article","venue":"ACS Sustainable Chemistry & Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"Science and Technology Commission of Shanghai Municipality; National Natural Science Foundation of China","keywords":"Catalysis; Methanol; Selectivity; Space velocity; Hydrogen; Alloy; Materials science; Nanoparticle; Inorganic chemistry; Chemistry; Chemical engineering; Nanotechnology; Metallurgy; Organic chemistry","score_opus":0.0063538787149403095,"score_gpt":0.2090140465726387,"score_spread":0.2026601678576984,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4368366468","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.978317,0.00044212968,0.015283142,0.00030993126,0.00037807444,0.0020429995,0.00022390329,0.0027333752,0.00026942434],"genre_scores_gemma":[0.994344,0.00017931273,0.00025289872,0.00006699501,0.0007236301,0.0012214269,0.0020954274,0.00081771216,0.00029860387],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99048334,0.000042419022,0.0017547015,0.0022143666,0.0016313142,0.0038738663],"domain_scores_gemma":[0.9947072,0.0006413988,0.0005561537,0.0018872346,0.0010583624,0.0011496523],"candidate_categories":["metaepi_narrow"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0013165222,0.0019336875,0.0017491421,0.0010925757,0.000582435,0.00031718536,0.0012797216,0.0009260086,0.000008895449],"category_scores_gemma":[0.0016737843,0.0021059571,0.00072096207,0.004535974,0.0001625107,0.000844983,0.0008363672,0.0014873699,0.00016252758],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001979126,0.00013426384,0.000010508571,0.0027718467,0.0005438324,0.00037833734,0.0006975549,0.20430426,0.78937614,0.00012002577,0.0003491281,0.0011161878],"study_design_scores_gemma":[0.0020054919,0.00013329549,0.00002818577,0.00053992757,0.00040768427,0.00022253286,0.0013770274,0.05582504,0.9337686,0.000030305018,0.0033383085,0.0023236412],"about_ca_topic_score_codex":0.000038050297,"about_ca_topic_score_gemma":0.000007336607,"teacher_disagreement_score":0.14847922,"about_ca_system_score_codex":0.003513527,"about_ca_system_score_gemma":0.00044741554,"threshold_uncertainty_score":0.99934065},"labels":[],"label_agreement":null},{"id":"W4368368872","doi":"10.1002/ange.202304470","title":"Solar Hydrocarbons: Single‐Step, Atmospheric‐Pressure Synthesis of C<sub>2</sub>−C<sub>4</sub> Alkanes and Alkenes from CO<sub>2</sub>","year":2023,"lang":"en","type":"article","venue":"Angewandte Chemie","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada; University of Toronto; Ministero dello Sviluppo Economico; National Key Research and Development Program of China; Lions Clubs International Foundation; Alexander von Humboldt-Stiftung","keywords":"Spinel; Hydrocarbon; Cobalt; Atmospheric pressure; Selectivity; Materials science; Chemistry; Alloy; Analytical Chemistry (journal); Inorganic chemistry; Chemical engineering; Catalysis; Organic chemistry; Metallurgy","score_opus":0.011881931236475443,"score_gpt":0.21364728784744277,"score_spread":0.20176535661096734,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4368368872","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9927945,0.0042189565,0.00014727926,0.00015195768,0.0003401056,0.00043395162,0.00035517532,0.0008630922,0.0006949531],"genre_scores_gemma":[0.9960234,0.0020947855,0.000255678,0.00008447453,0.0005885734,0.00017339143,0.00040069886,0.00033198504,0.000047007274],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.995197,0.00007275294,0.0011515889,0.0012911353,0.0009776866,0.0013098599],"domain_scores_gemma":[0.996389,0.0012103163,0.00051799,0.0012311457,0.0001436284,0.0005079189],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005618053,0.0010147337,0.0015326093,0.00014921273,0.00021779968,0.00009177484,0.0006780685,0.0007741541,0.000019418794],"category_scores_gemma":[0.0009978092,0.0010231904,0.0005672424,0.0011482321,0.0003364456,0.0005513419,0.0005282172,0.00067954377,0.00012741779],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000104545405,0.00013188965,0.00041123776,0.00066326675,0.00076372945,0.00012114665,0.00057189807,0.00013791201,0.97777057,0.000008285745,0.00067467435,0.01864086],"study_design_scores_gemma":[0.00094416016,0.0000624805,0.00021089014,0.00068885804,0.00077255676,0.000056556004,0.00040789574,0.0015313908,0.99243486,0.00016395457,0.0015904435,0.001135953],"about_ca_topic_score_codex":0.00021288617,"about_ca_topic_score_gemma":0.0000927527,"teacher_disagreement_score":0.017504908,"about_ca_system_score_codex":0.00021909241,"about_ca_system_score_gemma":0.00009356295,"threshold_uncertainty_score":0.99922186},"labels":[],"label_agreement":null},{"id":"W4372329772","doi":"10.1016/j.rser.2023.113323","title":"A review of methane pyrolysis technologies for hydrogen production","year":2023,"lang":"en","type":"review","venue":"Renewable and Sustainable Energy Reviews","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":274,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Methane; Pyrolysis; Greenhouse gas; Waste management; Hydrogen production; Materials science; Steam reforming; Syngas; Hydrogen; Carbon fibers; Methane reformer; Environmental science; Process engineering; Chemical engineering; Chemistry; Engineering; Organic chemistry","score_opus":0.03797096401803817,"score_gpt":0.3082619429695013,"score_spread":0.27029097895146315,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4372329772","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[3.2478724e-7,0.9966352,0.00040079743,0.000046023553,0.0000902934,0.0021746221,0.000022010818,0.0003710579,0.00025969394],"genre_scores_gemma":[1.2308739e-7,0.9640852,0.0002730088,0.000018265395,0.00015590769,0.0034437776,0.000382136,0.00017565387,0.031465895],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9958305,0.00013354326,0.0020132288,0.0008816159,0.00023860352,0.00090251485],"domain_scores_gemma":[0.99699146,0.0002698236,0.0012026792,0.0011855679,0.00024901936,0.0001014445],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002846036,0.00075511617,0.0055170576,0.0006670204,0.0000908441,0.000012700491,0.0005430789,0.00051693054,0.000010869489],"category_scores_gemma":[0.004357246,0.00055365165,0.0014439388,0.0024306786,0.00008543301,0.00019773851,0.00045971858,0.00025892662,0.000007062424],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000016272102,0.000012295972,1.7169352e-8,0.49373344,0.00022093386,0.0000046669543,0.0000042318584,0.000008754816,0.000066539804,0.00043069423,0.00085792644,0.5046589],"study_design_scores_gemma":[0.00007678428,0.000038351744,3.011177e-10,0.16749144,0.0023548636,0.000049132763,0.00006650451,0.0000119400365,0.0026320643,0.000359996,0.82647204,0.00044687363],"about_ca_topic_score_codex":0.0005921295,"about_ca_topic_score_gemma":0.000019528241,"teacher_disagreement_score":0.8256141,"about_ca_system_score_codex":0.00031858194,"about_ca_system_score_gemma":0.0002545114,"threshold_uncertainty_score":0.9996915},"labels":[],"label_agreement":null},{"id":"W4376648948","doi":"10.1016/j.susmat.2023.e00630","title":"Direct CO2-to-renewable methanol: Outlook, performance and optimization approach","year":2023,"lang":"en","type":"article","venue":"Sustainable materials and technologies","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of New Brunswick; University of Toronto","funders":"Government of Ontario; Ford Motor Company","keywords":"Raw material; Renewable energy; Process engineering; Methanol; Waste management; Environmental science; Catalysis; Engineering; Chemistry; Organic chemistry","score_opus":0.010109386359699334,"score_gpt":0.21886928479619513,"score_spread":0.2087598984364958,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4376648948","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99245477,0.00028823505,0.002305751,0.00016267574,0.00006983219,0.00038047248,0.000011550288,0.002472478,0.0018542121],"genre_scores_gemma":[0.9891162,0.0005157903,0.005631556,0.0000064901687,0.000021991518,0.00016489004,0.00003750274,0.00004008325,0.0044655255],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988312,0.000010784439,0.00020858283,0.00032492567,0.00011558565,0.0005089253],"domain_scores_gemma":[0.9995554,0.00003609524,0.00005163664,0.00025930212,0.000055738234,0.000041842217],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004187153,0.00018917232,0.0003181176,0.000354942,0.00014725646,0.00008340568,0.00015739532,0.00017305872,0.000008813548],"category_scores_gemma":[0.0003806,0.00015822276,0.000018068102,0.0006217755,0.0000760656,0.00023592541,0.00058044866,0.00007109815,0.0000055804685],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000093051036,0.000036313206,0.00028409966,0.003699046,0.00010934126,0.000045465113,0.0006361067,0.12334499,0.8562647,0.0046704826,0.00022829081,0.0105881225],"study_design_scores_gemma":[0.00022987649,0.000050001752,0.000029387867,0.00004040513,0.000023315453,0.000014000534,0.004383477,0.011999396,0.9805603,0.0002537375,0.0021528306,0.0002632833],"about_ca_topic_score_codex":0.00022662496,"about_ca_topic_score_gemma":7.6749313e-7,"teacher_disagreement_score":0.12429559,"about_ca_system_score_codex":0.00006214417,"about_ca_system_score_gemma":0.0000134176735,"threshold_uncertainty_score":0.64521366},"labels":[],"label_agreement":null},{"id":"W4377195219","doi":"10.1016/j.jcat.2023.05.021","title":"Fischer-Tropsch synthesis: Osmium promoted Co@HCS catalysts","year":2023,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Canadian Light Source (Canada)","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation; Canadian Institutes of Health Research; National Research Council; University of the Witwatersrand, Johannesburg; National Research Foundation; University of Saskatchewan; Canadian Light Source","keywords":"Fischer–Tropsch process; Catalysis; Chemistry; Osmium; Nanoparticle; Chemical engineering; Nuclear chemistry; Selectivity; Nanotechnology; Ruthenium; Organic chemistry; Materials science","score_opus":0.017157034073561284,"score_gpt":0.2738502449470299,"score_spread":0.25669321087346864,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4377195219","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99612534,0.00044476418,0.0005889464,0.0007582523,0.00034765244,0.0001284556,0.000032092128,0.0002435788,0.0013309374],"genre_scores_gemma":[0.9971674,0.000073297444,0.0003855695,0.000028515202,0.000545933,0.000016559245,0.000082420076,0.00009111612,0.0016091784],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99699515,0.00005699291,0.0011247619,0.00027814758,0.0009707992,0.00057412987],"domain_scores_gemma":[0.99766296,0.00034472015,0.00066258496,0.00059891003,0.0004007447,0.0003300726],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012818191,0.00031843953,0.0008594076,0.0009331621,0.00012170511,0.00006111965,0.0005706862,0.00019819784,0.000117686184],"category_scores_gemma":[0.0022292251,0.00025886425,0.00073889835,0.001893642,0.00007681542,0.0005291221,0.00012950538,0.0006090243,0.0004953509],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000093188435,0.00012625987,0.00058050256,0.0002379911,0.0014241056,0.0005381606,0.00089925155,0.0007399474,0.9808558,0.00002482735,0.0025305937,0.011949346],"study_design_scores_gemma":[0.0005117457,0.00004823887,0.00040524322,0.00018677447,0.0007017837,0.00054325425,0.00038918975,0.0018129513,0.98565793,0.000046956564,0.009331338,0.00036460662],"about_ca_topic_score_codex":0.0000763197,"about_ca_topic_score_gemma":0.000010774963,"teacher_disagreement_score":0.01158474,"about_ca_system_score_codex":0.00028507935,"about_ca_system_score_gemma":0.00014937099,"threshold_uncertainty_score":0.99998635},"labels":[],"label_agreement":null},{"id":"W4377226903","doi":"10.1021/acs.jpcc.3c01381","title":"Theoretical Investigation of the Properties of Pd<sub>2</sub>Cu Intermetallics and CO<sub>2</sub> Hydrogenation to Ethanol Catalyzed on Pd<sub>2</sub>Cu (110)","year":2023,"lang":"en","type":"article","venue":"The Journal of Physical Chemistry C","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"National Natural Science Foundation of China","keywords":"Intermetallic; Homonuclear molecule; Catalysis; Crystal structure; Chemistry; Crystallography; Physical chemistry; Bond length; Materials science; Inorganic chemistry; Molecule; Organic chemistry; Alloy","score_opus":0.012905873582740441,"score_gpt":0.226677878017041,"score_spread":0.21377200443430056,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4377226903","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9986781,0.00006799727,0.000054516924,0.00060914556,0.0000865784,0.00029969975,0.000032678236,0.0000582859,0.000113002825],"genre_scores_gemma":[0.99934274,0.00006426757,0.000010678451,0.000050114635,0.00040266578,0.000016681111,0.00002370909,0.00008074918,0.0000083874265],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99697274,0.0001384369,0.000991218,0.0003131314,0.0011225627,0.0004618865],"domain_scores_gemma":[0.99755496,0.00048449863,0.00073863385,0.00061206345,0.00032812223,0.00028172194],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001019667,0.00043660155,0.00076199835,0.0001351216,0.000114751136,0.000028705479,0.0007437351,0.000223254,0.0000037174798],"category_scores_gemma":[0.001097278,0.00027290566,0.00044128817,0.00080981036,0.00072016416,0.00023100861,0.0003433124,0.0010023294,0.000019024614],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00029522993,0.000108214146,0.000015598267,0.00048997253,0.0002160872,0.0000050089625,0.0018202044,0.0012323428,0.9939023,0.00030432508,0.000032353535,0.0015783515],"study_design_scores_gemma":[0.0006757618,0.00011187093,0.00010148731,0.0008305354,0.00027711916,0.000079034384,0.0002444165,0.007218514,0.9884667,0.0016942988,0.00000500655,0.00029529052],"about_ca_topic_score_codex":0.000005690907,"about_ca_topic_score_gemma":0.0000016378923,"teacher_disagreement_score":0.0059861713,"about_ca_system_score_codex":0.00023156573,"about_ca_system_score_gemma":0.00013356663,"threshold_uncertainty_score":0.9999723},"labels":[],"label_agreement":null},{"id":"W4377965269","doi":"10.1002/cjce.24955","title":"Cerium‐promoted Ni/ <scp> SiO <sub>2</sub> </scp> catalyst for <scp>CO</scp> methanation","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Beijing Nova Program; National Natural Science Foundation of China","keywords":"Methanation; Catalysis; Arrhenius equation; Nickel; Cerium; Activation energy; Selectivity; Inorganic chemistry; Chemistry; Sintering; Dispersion (optics); Materials science; Nuclear chemistry; Physical chemistry; Organic chemistry","score_opus":0.01386799514922251,"score_gpt":0.22403253768742953,"score_spread":0.21016454253820702,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4377965269","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9953851,0.0003741656,0.002444655,0.00021989417,0.00071336795,0.00032952972,0.00008756968,0.00020609611,0.00023959656],"genre_scores_gemma":[0.99794674,0.000012600191,0.0004324999,0.000047920814,0.00096891145,0.00003988927,0.00015178342,0.00019231724,0.00020733941],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968411,0.000025475221,0.0009435721,0.00033491795,0.000603938,0.0012510015],"domain_scores_gemma":[0.9966462,0.0011152606,0.00035088524,0.00047006842,0.00032960463,0.0010879737],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013224278,0.00047285677,0.00068814453,0.0008151254,0.00016389623,0.00009849987,0.00089472893,0.0003648103,0.00000422999],"category_scores_gemma":[0.0065533174,0.00040972256,0.0004984949,0.0013153185,0.000091327085,0.00035777147,0.00006928574,0.0010591628,0.000054914774],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000024253727,0.000008654119,0.000016025097,0.00017790635,0.00022873265,0.000063911175,0.0007292331,0.013890388,0.98212314,0.00018581284,0.0010880214,0.0014857412],"study_design_scores_gemma":[0.0006521147,0.000034111898,0.00005433345,0.0001769004,0.00015418527,0.0002664265,0.000119996555,0.040717892,0.95158327,0.00017409094,0.005946989,0.00011971899],"about_ca_topic_score_codex":0.00047975482,"about_ca_topic_score_gemma":0.0001698809,"teacher_disagreement_score":0.030539908,"about_ca_system_score_codex":0.00096284534,"about_ca_system_score_gemma":0.00043641764,"threshold_uncertainty_score":0.9998355},"labels":[],"label_agreement":null},{"id":"W4378837336","doi":"10.1002/cjce.24973","title":"Synthesis and utilization of mesoporous alumina as a supporting material of Ce‐promoted Ni‐based catalysts in the methane reforming process","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Mesoporous material; Materials science; Coke; Chemical engineering; Raw material; Syngas; Methane; Nanocrystalline material; Steam reforming; Yield (engineering); Carbon dioxide reforming; Hydrogen production; Methane reformer; Metallurgy; Nanotechnology; Chemistry; Organic chemistry","score_opus":0.016449809559557705,"score_gpt":0.25408077292740205,"score_spread":0.23763096336784434,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4378837336","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9993389,0.00011817942,0.000051580108,0.00018264308,0.00008619577,0.00013626525,0.000015709475,0.000018752848,0.00005172217],"genre_scores_gemma":[0.9997536,0.0000027906237,0.00008953933,0.000008343952,0.00007722479,0.000009355354,0.000014229949,0.00003919935,0.000005740311],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982328,0.000029712559,0.0008311513,0.0001280505,0.000371236,0.00040703965],"domain_scores_gemma":[0.9987716,0.00031383047,0.0003825848,0.0002265277,0.00012404467,0.0001814287],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0015721201,0.00018573565,0.00045678153,0.00038206152,0.000046358335,0.00002287057,0.00045170664,0.00012274456,0.000013000831],"category_scores_gemma":[0.0023604773,0.00012709369,0.000105772946,0.00087671285,0.000085211635,0.00014594935,0.000028782164,0.0003427937,6.656858e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004303097,0.0000113418,0.00017301904,0.0006670995,0.000070819,0.00009604012,0.0029972151,0.0052238703,0.9884766,0.00007595033,0.000004014186,0.0021610486],"study_design_scores_gemma":[0.00026393885,0.000022341808,0.000074887714,0.0004618487,0.00008144849,0.00024323151,0.00042262123,0.021032967,0.9771773,0.0000747549,0.000014975345,0.00012965065],"about_ca_topic_score_codex":0.0040696464,"about_ca_topic_score_gemma":0.00026359034,"teacher_disagreement_score":0.015809096,"about_ca_system_score_codex":0.00016702642,"about_ca_system_score_gemma":0.00030561257,"threshold_uncertainty_score":0.61521155},"labels":[],"label_agreement":null},{"id":"W4379015535","doi":"10.1002/cjce.24975","title":"<scp>CO<sub>2</sub></scp> utilization for methanol production; Optimal pathways with minimum <scp>GHG</scp> reduction cost","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Natural Resources Canada; Concordia University","funders":"","keywords":"Greenhouse gas; Production (economics); Methanol; Tonne; Raw material; Life-cycle assessment; Environmental science; Business; Waste management; Pulp and paper industry; Chemistry; Economics; Engineering; Microeconomics","score_opus":0.02562366840444152,"score_gpt":0.22847736599931814,"score_spread":0.20285369759487662,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4379015535","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9921896,0.0002833348,0.005741445,0.00017511351,0.0007695951,0.000496817,0.000041365758,0.00018831439,0.00011442673],"genre_scores_gemma":[0.99705595,0.000019474212,0.0010175435,0.00001570414,0.001350305,0.00007902157,0.000094513474,0.00017301536,0.00019450195],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9975299,0.000021318852,0.0006826116,0.00033754148,0.00049049983,0.00093807734],"domain_scores_gemma":[0.99779505,0.0004471297,0.00030652914,0.00037166124,0.0003601651,0.0007194884],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0008973975,0.00038854431,0.0004823482,0.0005903531,0.00017237436,0.000077984994,0.00047580877,0.000247619,0.0000026838943],"category_scores_gemma":[0.0032705246,0.0003188077,0.00025822874,0.0011460036,0.00010812281,0.0004099715,0.00003334487,0.0007803884,0.000017100167],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000007344791,0.000010201804,0.00000946943,0.00013829385,0.00016019367,0.000025283198,0.0008631171,0.097598016,0.8985978,0.00013396869,0.001128033,0.0013282864],"study_design_scores_gemma":[0.00054292235,0.000057994646,0.000016303253,0.00022746802,0.00013806688,0.0007625879,0.00031910345,0.02976955,0.96213716,0.0000501733,0.0058710105,0.00010768768],"about_ca_topic_score_codex":0.000076325734,"about_ca_topic_score_gemma":0.00003427011,"teacher_disagreement_score":0.06782847,"about_ca_system_score_codex":0.00072787516,"about_ca_system_score_gemma":0.00044553858,"threshold_uncertainty_score":0.9999264},"labels":[],"label_agreement":null},{"id":"W4379162441","doi":"10.1016/j.matt.2023.05.022","title":"Bringing down the heat in methanol synthesis","year":2023,"lang":"en","type":"article","venue":"Matter","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"National Research Council Canada; Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Oxide; Methanol; Chemistry; Fossil fuel; Waste management; Chemical engineering; Catalysis; Materials science; Organic chemistry; Engineering","score_opus":0.012535582947192224,"score_gpt":0.23728648260767307,"score_spread":0.22475089966048084,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4379162441","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9895608,0.000041685587,0.00009358707,0.0020883929,0.00013065258,0.00009307988,0.0000029121625,0.00021249126,0.007776405],"genre_scores_gemma":[0.9970753,0.0000024610663,0.000042132684,0.00021719476,0.00008262832,0.00005823914,0.0000031923387,0.000035287023,0.002483544],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99921185,0.0000163474,0.00016324343,0.0001538852,0.00013950409,0.0003151872],"domain_scores_gemma":[0.9994137,0.000253507,0.000012652173,0.0002847214,0.0000058343194,0.000029555984],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00031607546,0.00010074591,0.0001395609,0.00014392572,0.000030091996,0.000014890515,0.00019412558,0.000044725526,0.00049205485],"category_scores_gemma":[0.00009727429,0.00006928912,0.00007210544,0.00043397804,0.000015813119,0.00007145793,0.00012748371,0.00016954489,0.0026768912],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000074417985,0.000012318788,0.005297318,0.00013365943,0.000048675658,0.000056178276,0.0010028189,0.0017812527,0.9818763,0.000077408185,0.0017572856,0.007949353],"study_design_scores_gemma":[0.00021782119,0.0000026857688,0.015280765,0.00019223969,0.000029149835,0.000037869522,0.00024954425,0.013407548,0.9569567,0.00013778116,0.013159884,0.0003280461],"about_ca_topic_score_codex":0.00034081592,"about_ca_topic_score_gemma":0.000024100975,"teacher_disagreement_score":0.024919624,"about_ca_system_score_codex":0.000069373804,"about_ca_system_score_gemma":0.000003849631,"threshold_uncertainty_score":0.9980996},"labels":[],"label_agreement":null},{"id":"W4380230955","doi":"10.1016/j.ijhydene.2023.05.281","title":"La–Ce binary oxide catalysts for low-temperature dry reforming","year":2023,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Mitacs; Canadian Natural Resources Limited","keywords":"Catalysis; Coke; Carbon dioxide reforming; Oxide; Methane; Chemical engineering; Hydrothermal circulation; Materials science; Mixed oxide; Inorganic chemistry; Chemistry; Syngas; Metallurgy; Organic chemistry","score_opus":0.00911563272560581,"score_gpt":0.25791085085351634,"score_spread":0.24879521812791053,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4380230955","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99780595,0.0003339089,0.00022396746,0.00029612074,0.0007193928,0.00003604184,0.000032443277,0.000082021725,0.00047013303],"genre_scores_gemma":[0.9967226,0.00010668233,0.00033129787,0.000079145175,0.0008753218,0.000012578152,0.00013431309,0.00006141315,0.0016766968],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983106,0.00002179032,0.0006124665,0.00017346881,0.0005990513,0.00028259857],"domain_scores_gemma":[0.99885863,0.00020161892,0.00031694837,0.00016542566,0.0003203882,0.00013700755],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004976408,0.00018704578,0.00028718318,0.00048838,0.00004448146,0.000026531452,0.0006646266,0.00015396562,0.000013316739],"category_scores_gemma":[0.00027720377,0.00015811331,0.0003863467,0.00028844422,0.000030444071,0.0003830866,0.00014710087,0.00026367,0.000016413525],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008798306,0.000039435865,0.000048821603,0.000024027366,0.00046812592,0.0005287366,0.00015029634,0.0073291766,0.98442876,0.0016831086,0.00045642894,0.0047550746],"study_design_scores_gemma":[0.00083166116,0.00003492659,0.000044926746,0.00021467137,0.000040506537,0.00067753013,0.00013386305,0.0040022223,0.9595515,0.00046983882,0.03379825,0.00020006993],"about_ca_topic_score_codex":0.00007975692,"about_ca_topic_score_gemma":0.000011704153,"teacher_disagreement_score":0.03334182,"about_ca_system_score_codex":0.00031424142,"about_ca_system_score_gemma":0.00009265549,"threshold_uncertainty_score":0.64476734},"labels":[],"label_agreement":null},{"id":"W4382404741","doi":"10.1016/j.ces.2023.119047","title":"Potential of microreactors for heat transfer efficient CO2 methanation","year":2023,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Fondo Nacional de Desarrollo Científico y Tecnológico; Agencia Nacional de Investigación y Desarrollo; Agenția Națională pentru Cercetare și Dezvoltare","keywords":"Microreactor; Isothermal process; Mechanics; Heat transfer; Methanation; Advection; Diffusion; Transient (computer programming); Steady state (chemistry); Thermal; Channel (broadcasting); Thermodynamics; Chemistry; Materials science; Physics; Computer science; Hydrogen","score_opus":0.009920262696279627,"score_gpt":0.23857556704583344,"score_spread":0.2286553043495538,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4382404741","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9361949,0.000028312337,0.06288603,0.00003605904,0.00031580523,0.00018146349,0.000020910595,0.00029096007,0.000045543344],"genre_scores_gemma":[0.9982883,0.0000018567747,0.0015093568,0.000003886447,0.000076297256,0.000031018542,0.00002951937,0.0000328574,0.000026962574],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983689,0.0000020018613,0.00031875406,0.00034753472,0.0004520843,0.0005106851],"domain_scores_gemma":[0.9993371,0.00013702133,0.000013877877,0.000242369,0.00011582008,0.00015383655],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005376477,0.00016704501,0.0002434988,0.00034147772,0.000040399893,0.000012286537,0.00040877686,0.00008790858,0.000007649405],"category_scores_gemma":[0.00062031415,0.00015809614,0.00015890256,0.0015092577,0.00013937365,0.00011711863,0.000072658564,0.00014141586,0.000009147716],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000007255249,0.00001384371,0.0000026877024,0.00011888129,0.000008852924,9.105417e-7,0.00010297217,0.111329876,0.88759637,0.00052216946,0.0000036998345,0.00029248424],"study_design_scores_gemma":[0.00020274085,0.0000074426785,0.000029834246,0.000031535747,0.000013156676,0.0000045496145,0.000013283199,0.3545434,0.6449651,0.000006988061,0.00006373466,0.00011822517],"about_ca_topic_score_codex":0.00001134039,"about_ca_topic_score_gemma":5.4998292e-8,"teacher_disagreement_score":0.24321352,"about_ca_system_score_codex":0.00016810159,"about_ca_system_score_gemma":0.00004624161,"threshold_uncertainty_score":0.6446973},"labels":[],"label_agreement":null},{"id":"W4383427679","doi":"10.1039/d3cy00835e","title":"Non-thermal plasma assisted non-oxidative methane liquefaction for fuel production at near ambient conditions","year":2023,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Methane; Catalysis; Nonthermal plasma; Liquefaction; Coke; Gasoline; Plasma; Thermal; Chemistry; Oxidative coupling of methane; Chemical engineering; Waste management; Materials science; Environmental science; Environmental chemistry; Organic chemistry; Thermodynamics; Engineering","score_opus":0.01664057612166447,"score_gpt":0.28100604081722563,"score_spread":0.26436546469556116,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4383427679","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99500567,0.000018334336,0.0018410146,0.0008904483,0.0005203071,0.00060204754,0.000036455473,0.0009004569,0.00018524741],"genre_scores_gemma":[0.9965759,0.000010328383,0.00070298143,0.000011294465,0.00007836139,0.00056072173,0.00037360072,0.00004014376,0.0016466675],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99743515,0.00000882449,0.00042812194,0.00090979435,0.0004359834,0.00078213715],"domain_scores_gemma":[0.99840736,0.0000753305,0.00023646565,0.0008150265,0.00032808093,0.00013772286],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007734606,0.00026161555,0.00040410034,0.0018269814,0.0005568984,0.0000326874,0.00063819584,0.0002747729,0.000030224319],"category_scores_gemma":[0.0010495931,0.00025069035,0.0001859498,0.0075086756,0.0011127358,0.00057633995,0.0003924134,0.00031269237,0.0003597565],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000021396243,0.000041788917,0.00012640542,0.00005436772,0.00005572046,0.0000049718137,0.00032475576,0.0018225166,0.9947853,0.000092269416,0.000047493668,0.0026230311],"study_design_scores_gemma":[0.00035517765,0.00006997728,0.00053610175,0.000029408733,0.00010912494,0.00006638431,0.00044905202,0.032136038,0.96459675,0.00012701427,0.00124721,0.00027774693],"about_ca_topic_score_codex":0.000060974377,"about_ca_topic_score_gemma":0.0000565902,"teacher_disagreement_score":0.030313522,"about_ca_system_score_codex":0.000976616,"about_ca_system_score_gemma":0.00015727694,"threshold_uncertainty_score":0.9999945},"labels":[],"label_agreement":null},{"id":"W4384571143","doi":"10.1039/d3cy00848g","title":"Unlocking the potential of catalysts in thermochemical energy conversion processes","year":2023,"lang":"en","type":"article","venue":"Catalysis Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Component (thermodynamics); Carbon fibers; Sustainable energy; Energy transformation; Nanotechnology; Energy (signal processing); Chemistry; Biochemical engineering; Materials science; Renewable energy; Thermodynamics; Physics; Engineering; Organic chemistry","score_opus":0.007612412118090321,"score_gpt":0.23296529072490238,"score_spread":0.22535287860681205,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4384571143","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979663,0.0002531775,0.0005334681,0.00047762127,0.000091753776,0.000077006756,0.0000026496366,0.00030357204,0.00029446784],"genre_scores_gemma":[0.99970347,0.000048299982,0.00003748008,0.000011241074,0.00002317854,0.00003157166,0.000028082173,0.000017480756,0.00009918388],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980575,0.000009240814,0.0003964909,0.00047971937,0.0004928605,0.00056419405],"domain_scores_gemma":[0.99884415,0.00009086259,0.000151667,0.0006910182,0.00016596472,0.000056357134],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00061651744,0.00016559263,0.00031758295,0.0017684206,0.00014527042,0.000011992663,0.0014314726,0.00017739032,0.0000103621505],"category_scores_gemma":[0.001018619,0.00012011986,0.00008579337,0.01428162,0.0013819381,0.0002341226,0.0006817253,0.00025366986,0.000026681128],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000005537703,0.000020220694,0.000574782,0.00004239343,0.000013406491,0.00001605981,0.00016745788,0.00065311213,0.99364686,0.00071148627,0.0000070416745,0.004141626],"study_design_scores_gemma":[0.0001676601,0.000010540011,0.000088962646,0.000043589465,0.000028725364,0.000037066253,0.0008576042,0.008208512,0.9897425,0.00048238045,0.00019336671,0.00013905989],"about_ca_topic_score_codex":0.00020757041,"about_ca_topic_score_gemma":0.000030808493,"teacher_disagreement_score":0.0125132,"about_ca_system_score_codex":0.00018821708,"about_ca_system_score_gemma":0.00018465999,"threshold_uncertainty_score":0.6861845},"labels":[],"label_agreement":null},{"id":"W4385445690","doi":"10.1002/cjce.25057","title":"A modelling approach to investigate the performance of slurry bubble column reactors implementing<scp>Fischer</scp>–<scp>Tropsch</scp>synthesis","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Fischer–Tropsch process; Syngas; Catalysis; Bubble column reactor; Slurry; Mass transfer; Bubble; Yield (engineering); Particle size; Chemistry; Mass transfer coefficient; Chemical engineering; Space velocity; Materials science; Chromatography; Mechanics; Composite material; Organic chemistry; Engineering; Physics","score_opus":0.020437460972474605,"score_gpt":0.2018901918493775,"score_spread":0.1814527308769029,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4385445690","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9972373,0.00029341472,0.0010357343,0.00013029018,0.00018318648,0.0002193322,0.000025441981,0.00008083119,0.0007944342],"genre_scores_gemma":[0.9974438,0.000014706858,0.0016906151,0.00004078543,0.00033838538,0.00003219358,0.000010559211,0.00012443517,0.0003045064],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99693793,0.00003065114,0.000956974,0.00026012398,0.00062117615,0.0011931635],"domain_scores_gemma":[0.99688166,0.0011370545,0.0003436943,0.00052397244,0.00019779996,0.00091580563],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001607511,0.0003809986,0.000616193,0.00043434225,0.00019697174,0.000074560725,0.0011761265,0.00018852657,0.000004637991],"category_scores_gemma":[0.0029091528,0.00027954622,0.0003106874,0.0014468675,0.00011726602,0.00025637107,0.0001549672,0.0011135169,0.00001493037],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000027540573,0.00000889662,0.0001850884,0.0002331594,0.00020048307,0.000012156132,0.0020350271,0.6011781,0.39517203,0.00030632538,0.0005139228,0.00015206568],"study_design_scores_gemma":[0.00018320173,0.000018921819,0.00002114596,0.00024905405,0.0001115616,0.00010474617,0.0003510541,0.42373106,0.5672272,0.000027319878,0.007880989,0.00009375628],"about_ca_topic_score_codex":0.0019303847,"about_ca_topic_score_gemma":0.000050546645,"teacher_disagreement_score":0.17744705,"about_ca_system_score_codex":0.00042530952,"about_ca_system_score_gemma":0.00039479148,"threshold_uncertainty_score":0.99996567},"labels":[],"label_agreement":null},{"id":"W4386392108","doi":"10.1016/j.ijhydene.2023.07.343","title":"Electrified steam methane reforming microreactor","year":2023,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut interdisciplinaire d'innovation technologique; Université de Sherbrooke","funders":"Ministère de l'Économie, de l’Innovation et des Exportations du Québec","keywords":"Microreactor; Methane; Syngas; Steam reforming; Space velocity; Methane reformer; Chemistry; Carbon fibers; Chemical engineering; Gas composition; Carbon dioxide reforming; Carbon capture and storage (timeline); Materials science; Nuclear engineering; Waste management; Environmental science; Process engineering; Catalysis; Hydrogen production; Thermodynamics; Organic chemistry; Engineering; Composite material","score_opus":0.013733927001579552,"score_gpt":0.26350400266319834,"score_spread":0.2497700756616188,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4386392108","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9962196,0.00041230218,0.00067395234,0.00027044097,0.00096046453,0.000021779604,0.000010334605,0.000096707336,0.001334419],"genre_scores_gemma":[0.9969216,0.00020384228,0.00014663344,0.00007688037,0.0009582387,0.0000031400893,0.00004380188,0.000046443805,0.0015994351],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981619,0.000022670978,0.00064594735,0.0001430085,0.0007249729,0.0003014801],"domain_scores_gemma":[0.99892545,0.000117885276,0.00037233756,0.00015273292,0.00029129427,0.0001402789],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045062,0.00016259452,0.0002813607,0.0006416864,0.00002163229,0.000014830557,0.0006860406,0.00009468266,0.00007630962],"category_scores_gemma":[0.0002720946,0.00013637726,0.00030587913,0.00037852942,0.000021252295,0.00030954942,0.00010582986,0.0002505602,0.000052032425],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007782791,0.000027958611,0.000032212956,0.000004776528,0.00045132652,0.00032494834,0.000100181656,0.0011184071,0.97356975,0.00080551015,0.0001147871,0.02337229],"study_design_scores_gemma":[0.00061577535,0.00003734185,0.000013356141,0.000056581823,0.00003110442,0.00087837555,0.00006463322,0.0019855858,0.9478463,0.0003908348,0.047932003,0.00014813183],"about_ca_topic_score_codex":0.00015736952,"about_ca_topic_score_gemma":0.000013736454,"teacher_disagreement_score":0.04781722,"about_ca_system_score_codex":0.00033851594,"about_ca_system_score_gemma":0.00008121115,"threshold_uncertainty_score":0.5561303},"labels":[],"label_agreement":null},{"id":"W4386827714","doi":"10.1016/j.ces.2023.119300","title":"Formulation of KMoFe/CNTs catalyst for production of light olefins and liquid hydrocarbons via Fischer-Tropsch synthesis: Fixed-bed reactor simulation","year":2023,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Selectivity; Chemical engineering; Calcination; Space velocity; Design of experiments; Chemistry; Materials science; Organic chemistry; Engineering","score_opus":0.012673457622546378,"score_gpt":0.24404656596893556,"score_spread":0.2313731083463892,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4386827714","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9914656,0.00004150986,0.0077560586,0.00004898863,0.00018125636,0.00026351315,0.000009759718,0.0002023491,0.000030959134],"genre_scores_gemma":[0.9984677,0.0000030503745,0.0012932247,0.0000010909641,0.000098039454,0.000053454085,0.000027534596,0.00003622723,0.000019718738],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983449,0.0000036276044,0.0004697252,0.00040938955,0.00039944504,0.00037292246],"domain_scores_gemma":[0.9989614,0.00030045456,0.00015051782,0.0003446158,0.00011958147,0.00012344743],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005049106,0.00019081803,0.0003271988,0.00034428862,0.0000431716,0.000008579025,0.0002465376,0.000121639554,0.0000014155139],"category_scores_gemma":[0.0034127864,0.00018520279,0.000094489,0.001254218,0.000110111716,0.00041481122,0.000107003194,0.00013246552,0.0000019442637],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003427932,0.000018726962,0.00004372634,0.00032556328,0.000014360833,2.5949404e-7,0.00023607224,0.023337543,0.97538775,0.00013494765,0.0000012301721,0.00046551786],"study_design_scores_gemma":[0.000118146556,0.000019896072,0.00010461109,0.00012942875,0.00002872986,0.0000028494976,0.0000132826635,0.3137838,0.6856216,0.000017226812,0.00002761762,0.00013279087],"about_ca_topic_score_codex":0.000015964291,"about_ca_topic_score_gemma":6.6164415e-7,"teacher_disagreement_score":0.29044625,"about_ca_system_score_codex":0.00013547199,"about_ca_system_score_gemma":0.000039502662,"threshold_uncertainty_score":0.7552351},"labels":[],"label_agreement":null},{"id":"W4386923990","doi":"10.1016/j.egyr.2023.09.058","title":"Hydrogen production by steam reforming of fusel oil over nickel deposited on pyrolyzed rice husk supports","year":2023,"lang":"en","type":"article","venue":"Energy Reports","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"School of Aerospace Science and Technology; Chulalongkorn University","keywords":"Husk; Pyrolysis; Fusel alcohol; Steam reforming; Materials science; Nickel; Catalysis; Hydrogen production; Pyrolysis oil; Hydrogen; Chemical engineering; Chemistry; Nuclear chemistry; Metallurgy; Organic chemistry; Alcohol","score_opus":0.007082186647005516,"score_gpt":0.2246030665099229,"score_spread":0.21752087986291738,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4386923990","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99481493,0.00022208181,0.000019212988,0.000047136004,0.00059289444,0.00006300553,0.0000073529445,0.0005603512,0.0036730487],"genre_scores_gemma":[0.9780003,0.00008282927,0.00002741951,0.000023939887,0.0002220139,0.000051744973,0.00044116066,0.00010841847,0.02104219],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972404,0.000024564408,0.0009164746,0.00063220353,0.0006689976,0.00051734946],"domain_scores_gemma":[0.99829555,0.00004951123,0.0005245102,0.00089111505,0.00007870916,0.00016059604],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00048405182,0.00030529295,0.00045288852,0.0003169236,0.00008234721,0.0000071249583,0.00014112148,0.00020509533,0.000031777985],"category_scores_gemma":[0.00034438714,0.00028032198,0.00021119736,0.00095418905,0.000037751575,0.0002544133,0.00012955359,0.000216866,0.000014103782],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000042745633,0.00008005156,0.00027895145,0.000106169864,0.00011984829,0.00036549944,0.00013943238,0.0014941115,0.98966587,0.000028603692,0.000571389,0.0071073542],"study_design_scores_gemma":[0.00022944645,0.00004061566,0.000081145125,0.000118083226,0.000057766836,0.00047148296,0.000044181706,0.0006779604,0.98764277,0.00003160672,0.010291694,0.00031325276],"about_ca_topic_score_codex":0.0010570347,"about_ca_topic_score_gemma":0.00003818529,"teacher_disagreement_score":0.017369142,"about_ca_system_score_codex":0.00023355002,"about_ca_system_score_gemma":0.00004943182,"threshold_uncertainty_score":0.9999649},"labels":[],"label_agreement":null},{"id":"W4386959181","doi":"10.1016/j.enconman.2023.117659","title":"Computational fluid dynamics simulation of Fischer-Tropsch synthesis coupled with a novel reaction kinetics using trimetallic catalyst over a biomass-based support","year":2023,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"","keywords":"Multiphysics; Computational fluid dynamics; Chemistry; Kinetics; Catalysis; Chemical kinetics; Reaction mechanism; Molecular dynamics; Chemical engineering; Thermodynamics; Materials science; Organic chemistry; Computational chemistry; Engineering; Physics","score_opus":0.014681192635725872,"score_gpt":0.24075912840953897,"score_spread":0.2260779357738131,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4386959181","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8062726,0.000010349494,0.19311842,0.00005162111,0.00007262752,0.00012929329,0.000022398452,0.00011678886,0.00020586772],"genre_scores_gemma":[0.9979696,0.000011897413,0.0012212279,0.000020985022,0.0000151894765,0.000009980658,0.00045733954,0.000028262657,0.00026550342],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9990192,0.000010319981,0.0002488022,0.00023184417,0.00032431417,0.00016552051],"domain_scores_gemma":[0.99948007,0.00011606732,0.00012618124,0.00016156195,0.000056581437,0.000059539547],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012595645,0.00015212625,0.00020372286,0.00034973954,0.000046846977,0.000010178854,0.00006890207,0.00006152757,0.00002378263],"category_scores_gemma":[0.000016968314,0.0001405437,0.00006413651,0.00050163514,0.000037038164,0.00009930671,0.00006175879,0.000041666965,0.0000024524718],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014287214,0.00008650434,0.00006537815,0.00033118407,0.00022896024,0.00001560507,0.000027817125,0.7162455,0.28042915,0.00088691124,0.000009842891,0.0015303233],"study_design_scores_gemma":[0.0010719857,0.00004304869,0.00030059955,0.00006172442,0.00017812997,0.0000027867618,0.00008273496,0.94262755,0.054392803,0.000005132131,0.0010773584,0.00015615176],"about_ca_topic_score_codex":0.00029133086,"about_ca_topic_score_gemma":0.0000118875405,"teacher_disagreement_score":0.22638208,"about_ca_system_score_codex":0.0001673254,"about_ca_system_score_gemma":0.000016284896,"threshold_uncertainty_score":0.5731206},"labels":[],"label_agreement":null},{"id":"W4387203697","doi":"10.1016/b978-0-443-15377-8.00010-2","title":"Conversion of syngas to olefins and green hydrocarbons through Fischer–Tropsch catalysis","year":2023,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dalhousie University; University of Saskatchewan","funders":"","keywords":"Syngas; Fischer–Tropsch process; Catalysis; Biochemical engineering; Chemistry; Materials science; Process engineering; Nanotechnology; Environmental science; Organic chemistry; Engineering; Selectivity","score_opus":0.017614266034833816,"score_gpt":0.2338521029703713,"score_spread":0.21623783693553747,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4387203697","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0073721553,0.00046660032,0.00003503452,0.00007739854,0.0002251851,0.00050718896,0.00012239942,0.00025376168,0.9909403],"genre_scores_gemma":[0.013666461,0.00011550907,0.0003588384,0.00007364077,0.00020518532,0.000030907297,0.0001436164,0.00025822376,0.9851476],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99779946,0.000011346391,0.0006523695,0.00062899315,0.0005006858,0.00040717734],"domain_scores_gemma":[0.998517,0.00014520987,0.0002540426,0.0008031375,0.000059505892,0.00022112731],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00020488506,0.00054267683,0.001024162,0.00030011102,0.000063029096,0.000011462501,0.00036341127,0.00047263832,0.000063215026],"category_scores_gemma":[0.00007253373,0.00052299915,0.0003861708,0.000069973496,0.00011929735,0.00006865979,0.00056081597,0.0005922037,0.00023009852],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010604404,0.000030202671,0.000039246886,0.0029448152,0.002395298,0.00024064661,0.0037012808,0.00003125638,0.12788276,0.008599658,0.00007327025,0.8539555],"study_design_scores_gemma":[0.001026706,0.0001882448,0.000013470455,0.0023568347,0.0017701692,0.00008235558,0.00009680788,0.00032265423,0.14247748,0.0043160864,0.84542024,0.0019289646],"about_ca_topic_score_codex":0.0000979978,"about_ca_topic_score_gemma":0.00008893648,"teacher_disagreement_score":0.8520266,"about_ca_system_score_codex":0.00015687846,"about_ca_system_score_gemma":0.000056156456,"threshold_uncertainty_score":0.9997222},"labels":[],"label_agreement":null},{"id":"W4387413552","doi":"10.2139/ssrn.4593973","title":"Co2-to-Methanol: Economic and Environmental Comparison of Emerging and Established Technologies","year":2023,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Methanol; Emerging technologies; Natural resource economics; Environmental science; Economics; Chemistry; Nanotechnology; Materials science; Organic chemistry","score_opus":0.012073739893094853,"score_gpt":0.25941540550251746,"score_spread":0.2473416656094226,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4387413552","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98907894,0.007650155,0.002271539,0.00026847,0.00026183517,0.00020440664,0.00003673155,0.00018929239,0.00003860701],"genre_scores_gemma":[0.99294686,0.006272768,0.00030632972,0.0000021686749,0.00009277678,0.000014815357,0.00003345619,0.00008090458,0.0002498917],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997294,0.000022730963,0.00063495175,0.00043440785,0.00020692246,0.0014069901],"domain_scores_gemma":[0.99910635,0.00009897283,0.00036827853,0.00032435716,0.000010105239,0.000091954156],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.00096546387,0.00033694317,0.0007031441,0.0004940256,0.000079666665,0.000039505252,0.00040135655,0.0003277288,0.000006459985],"category_scores_gemma":[0.00013341494,0.00033315705,0.00012832053,0.000087365064,0.00010098155,0.00011953301,0.0011722059,0.0033839352,0.000008605112],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028008115,0.00019576703,0.02921458,0.0011537069,0.0037949975,0.000032312215,0.004914931,0.029583521,0.5757674,0.014276405,0.000082322156,0.340704],"study_design_scores_gemma":[0.0038754402,0.00095465756,0.0011779813,0.001727264,0.0012064513,0.0021332721,0.0804412,0.07303603,0.661833,0.16742967,0.0024306336,0.0037544032],"about_ca_topic_score_codex":0.00018329592,"about_ca_topic_score_gemma":0.00023705303,"teacher_disagreement_score":0.3369496,"about_ca_system_score_codex":0.0013696117,"about_ca_system_score_gemma":0.00027536773,"threshold_uncertainty_score":0.999912},"labels":[],"label_agreement":null},{"id":"W4387501537","doi":"10.1063/5.0161954","title":"Investigating the effects of operating parameters on the performance of sorption-enhanced membrane reactor for ethanol steam reforming reaction using computational fluid dynamics method","year":2023,"lang":"en","type":"article","venue":"Physics of Fluids","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Computational fluid dynamics; Steam reforming; Space velocity; Membrane reactor; Hydrogen; Thermodynamics; Adsorption; Sorption; Membrane; Chemical engineering; Nuclear engineering; Chemistry; Physics; Hydrogen production; Catalysis; Organic chemistry; Engineering","score_opus":0.02594269585257149,"score_gpt":0.2870477382772825,"score_spread":0.26110504242471105,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4387501537","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9710344,0.000014120185,0.02812479,0.000042105217,0.00016737546,0.000492734,0.000023296048,0.0000536788,0.000047505415],"genre_scores_gemma":[0.9913634,0.000010746416,0.0083328225,0.000019472907,0.000083692736,0.000054612246,0.00007634483,0.000048724953,0.0000101978385],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984506,0.00006797836,0.0005895369,0.00021202497,0.00042975604,0.00025010342],"domain_scores_gemma":[0.9962515,0.0027599237,0.00039989298,0.00034116406,0.00021312953,0.00003435272],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00090746547,0.00019864165,0.00038971953,0.000090290785,0.00012459005,0.0000062180784,0.0002633918,0.000078741716,5.250056e-7],"category_scores_gemma":[0.0010052229,0.00013587883,0.00019573462,0.00061208056,0.000107246204,0.00024785462,0.00008383819,0.0002468015,9.1263837e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000016712736,0.000020861486,0.000014649144,0.0008783498,0.0000927373,5.6847497e-8,0.0011117485,0.14000653,0.85128343,0.0015117594,4.6108823e-7,0.005062728],"study_design_scores_gemma":[0.00018771991,0.000060549908,0.000013923758,0.0003793247,0.00004242877,8.557766e-7,0.0002151136,0.4761856,0.5226037,0.00023798927,4.2011246e-7,0.00007239481],"about_ca_topic_score_codex":0.00010739758,"about_ca_topic_score_gemma":0.0000011778237,"teacher_disagreement_score":0.33617908,"about_ca_system_score_codex":0.00016240036,"about_ca_system_score_gemma":0.00005865672,"threshold_uncertainty_score":0.5540978},"labels":[],"label_agreement":null},{"id":"W4387963822","doi":"","title":"Conversion of biogas to syngas via catalytic CO2 reforming reaction: An overview of thermodynamic aspects, catalytic design and reaction kinetics","year":2020,"lang":"en","type":"preprint","venue":"HAL (Le Centre pour la Communication Scientifique Directe)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Syngas; Catalysis; Kinetics; Syngas to gasoline plus; Biogas; Chemical kinetics; Chemical engineering; Catalytic reforming; Chemistry; Materials science; Waste management; Process engineering; Organic chemistry; Engineering; Steam reforming; Hydrogen production; Physics","score_opus":0.032535147087417775,"score_gpt":0.25604848910688766,"score_spread":0.22351334201946987,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4387963822","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8672661,0.001920692,0.1244225,0.0013303213,0.0002741877,0.0011812259,0.00010148827,0.0003104057,0.0031930672],"genre_scores_gemma":[0.9883066,0.0006820884,0.009970863,0.000015867323,0.00002330562,0.00002656415,0.000670635,0.00008241379,0.00022165803],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99687076,0.00077429233,0.0008303734,0.0007358408,0.00048691462,0.00030183536],"domain_scores_gemma":[0.9955912,0.0006599356,0.0008017223,0.0017365175,0.00092733285,0.0002832679],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00222777,0.00039270826,0.0007061593,0.00031675052,0.00008294085,0.000034305616,0.00074181514,0.0003267112,0.000010417893],"category_scores_gemma":[0.0010082858,0.0004133235,0.00019076825,0.0005453773,0.00015406238,0.00022185457,0.0010120912,0.0005985674,0.000010999478],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003317972,0.00017449827,0.000030345105,0.00094097835,0.00010413564,0.000004032313,0.0029925434,0.00017453835,0.9852103,0.0030624068,0.0000042368556,0.0072688083],"study_design_scores_gemma":[0.00036996353,0.0000041026174,0.00044148674,0.002448118,0.00019890073,0.000040740313,0.00019084883,0.048841625,0.9462678,0.00051804236,0.00030100168,0.00037737013],"about_ca_topic_score_codex":0.0034772207,"about_ca_topic_score_gemma":0.0002576631,"teacher_disagreement_score":0.12104049,"about_ca_system_score_codex":0.00043151798,"about_ca_system_score_gemma":0.00014381389,"threshold_uncertainty_score":0.99983186},"labels":[],"label_agreement":null},{"id":"W4388420310","doi":"10.1016/j.joei.2023.101453","title":"Enhancement of higher alcohols selectivity in Fischer-Tropsch synthesis using Walnut and Almond shell derived biochars as Copper/Cobalt catalyst support","year":2023,"lang":"en","type":"article","venue":"Journal of the Energy Institute","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Biochar; Catalysis; Bimetallic strip; Cobalt; Selectivity; Fischer–Tropsch process; Chemistry; Copper; Carbon monoxide; Pyrolysis; Nuclear chemistry; Inorganic chemistry; Organic chemistry","score_opus":0.02225194069493196,"score_gpt":0.2694508691348552,"score_spread":0.24719892843992325,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4388420310","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99829906,0.00024491065,0.00018756522,0.000179521,0.0005520185,0.00006167234,0.000008237922,0.000016901839,0.00045011213],"genre_scores_gemma":[0.9987263,0.00017582781,0.00031022303,0.000035009292,0.0001296968,0.000005383049,0.000003927322,0.00002907911,0.0005845645],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99833465,0.000050610746,0.00065137056,0.00019103038,0.00043802356,0.00033430225],"domain_scores_gemma":[0.9989874,0.00008635433,0.0004395748,0.0002784888,0.00009308494,0.00011512258],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005431653,0.00021502771,0.0005104952,0.00029121732,0.00006852647,0.000014635265,0.00035719303,0.00012503905,0.000028896657],"category_scores_gemma":[0.0002849388,0.00015709057,0.00020347277,0.0007049279,0.00010476656,0.00035772196,0.00022399052,0.0002855649,0.0000039746337],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000059153146,0.000052177656,0.0005066352,0.00006513031,0.00020206193,0.000069239264,0.0001392071,0.0059590447,0.9912794,0.00013193574,0.00006164246,0.0014743626],"study_design_scores_gemma":[0.00047999687,0.000035312885,0.000709727,0.0003073901,0.00011603892,0.00018563338,0.00003887067,0.0013594583,0.9940696,0.000058496145,0.0024666863,0.0001728332],"about_ca_topic_score_codex":0.0011451642,"about_ca_topic_score_gemma":0.00011283709,"teacher_disagreement_score":0.0045995866,"about_ca_system_score_codex":0.0003260106,"about_ca_system_score_gemma":0.00016003461,"threshold_uncertainty_score":0.64059675},"labels":[],"label_agreement":null},{"id":"W4388552083","doi":"10.18280/ijdne.180502","title":"Production of Biomethane by Hydrogenation of CO2 and CO","year":2023,"lang":"en","type":"article","venue":"International Journal of Design & Nature and Ecodynamics","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Production (economics); Biogas; Waste management; Environmental science; Pulp and paper industry; Process engineering; Engineering; Economics","score_opus":0.01005650901694087,"score_gpt":0.2625648758432276,"score_spread":0.2525083668262867,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4388552083","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9941694,0.00083620654,0.0041767736,0.00021882687,0.0004578503,0.000055657085,0.00002871874,0.000010732852,0.000045840534],"genre_scores_gemma":[0.997855,0.0008751985,0.0010141446,0.0000074549616,0.00009809551,6.7331194e-7,0.00004208655,0.000011677044,0.00009565033],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990956,0.00001592555,0.00037796865,0.00008617162,0.0003351179,0.00008917896],"domain_scores_gemma":[0.9991525,0.00011824967,0.00035537704,0.000053323754,0.00027482145,0.00004577019],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004860778,0.00007828111,0.00018429408,0.00043904543,0.000011098548,0.000006434701,0.00011652656,0.00012338524,0.000003887237],"category_scores_gemma":[0.00035480442,0.00006777736,0.000054443317,0.00023393799,0.00003977497,0.000192855,0.000028946582,0.00022280798,5.1765704e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001077418,0.000029125535,0.00054652226,0.000050448074,0.00021221265,0.0000065181093,0.00017238532,0.0011357793,0.9899744,0.00026060967,0.00013464366,0.007369609],"study_design_scores_gemma":[0.00074220414,0.00011371081,0.00057357753,0.00016785391,0.00006261515,0.00036628175,0.00012554628,0.038935877,0.95704746,0.0010357995,0.00070763053,0.00012143568],"about_ca_topic_score_codex":0.000007881016,"about_ca_topic_score_gemma":0.0000012778547,"teacher_disagreement_score":0.0378001,"about_ca_system_score_codex":0.000056126675,"about_ca_system_score_gemma":0.000022590577,"threshold_uncertainty_score":0.27638802},"labels":[],"label_agreement":null},{"id":"W4388722970","doi":"10.2495/esus230071","title":"SUSTAINABLE HYDROGEN PRODUCTION, STORAGE AND TRANSPORT PATHWAYS","year":2023,"lang":"en","type":"article","venue":"WIT transactions on ecology and the environment","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"Ontario Tech University","funders":"University of Ontario Institute of Technology","keywords":"Hydrogen production; Natural gas; Environmental science; Hydrogen economy; Hydrogen storage; Hydrogen; Fossil fuel; Waste management; Power to gas; Steam reforming; Renewable energy; Hydrogen technologies; Substitute natural gas; Syngas; Engineering; Chemistry; Electrolysis; Electrical engineering","score_opus":0.0062729829111552145,"score_gpt":0.1763532386664834,"score_spread":0.17008025575532817,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4388722970","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9956981,0.000099894125,0.002508053,0.0010110997,0.000077684395,0.0003064206,0.0000062519175,0.00010360171,0.00018892961],"genre_scores_gemma":[0.9915333,0.00034612074,0.000017240187,0.000028874618,0.00002225563,0.0001347248,0.000008194435,0.000018015811,0.007891317],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99928266,0.000025932688,0.00013937445,0.00022680256,0.0000844002,0.00024084256],"domain_scores_gemma":[0.9996656,0.00006870918,0.000024382587,0.00018407298,0.000003240311,0.000053963187],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034491505,0.000114507384,0.00015086279,0.00007396712,0.00027197183,0.000002584561,0.000055358327,0.00007753292,0.00008809477],"category_scores_gemma":[0.000008301269,0.00008437112,0.00004688215,0.00009940835,0.00020354151,0.0000701825,0.0000055809824,0.00019962253,0.000046935278],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0018134807,0.0013104534,0.0036233359,0.0009991297,0.0025118468,0.00051622506,0.02932046,0.6772174,0.19501887,0.03377481,0.00007649171,0.05381749],"study_design_scores_gemma":[0.021264324,0.0011711427,0.06527924,0.00012784796,0.0022742846,0.001026953,0.020264216,0.048519272,0.741138,0.022032643,0.07388435,0.0030177233],"about_ca_topic_score_codex":0.000026199277,"about_ca_topic_score_gemma":0.000011489017,"teacher_disagreement_score":0.6286981,"about_ca_system_score_codex":0.000069757094,"about_ca_system_score_gemma":0.000006704805,"threshold_uncertainty_score":0.34405544},"labels":[],"label_agreement":null},{"id":"W4389066357","doi":"10.1016/j.fuel.2023.130427","title":"Fuel reforming processes for hydrogen production","year":2023,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":46,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Department of Mechanical Engineering, University of Alberta; Saudi Aramco; King Fahd University of Petroleum and Minerals","keywords":"Naphtha; Steam reforming; Methane reformer; Catalytic reforming; Hydrogen production; Methane; Process engineering; Environmental science; Waste management; Hydrogen; Chemistry; Catalysis; Engineering; Organic chemistry","score_opus":0.025590225763482785,"score_gpt":0.2687695521899685,"score_spread":0.2431793264264857,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389066357","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9921123,0.0008313364,0.00040670135,0.00063958357,0.0007044763,0.00063965254,0.00003227693,0.0016199704,0.0030137168],"genre_scores_gemma":[0.9888337,0.00008289297,0.0003825411,0.000018313782,0.00085555407,0.00026001528,0.0001814859,0.000081265,0.009304218],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99898624,0.000003285443,0.00021544984,0.00028125616,0.00015203214,0.00036170782],"domain_scores_gemma":[0.99948037,0.000053804077,0.000059192804,0.00025174874,0.000089623405,0.00006526628],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024323432,0.00013575886,0.00016459999,0.00014129712,0.00005955099,0.000008195663,0.00015254495,0.00007731538,0.000009598707],"category_scores_gemma":[0.0010018301,0.00011969372,0.00007914194,0.0006809963,0.000016742546,0.0002459188,0.00006422149,0.00009780161,0.0001608509],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000048142858,0.000038663282,0.00023453176,0.0052118767,0.000088988105,0.000006050959,0.001518596,0.0009313712,0.97361,0.0003922692,0.0004252011,0.017494336],"study_design_scores_gemma":[0.0003538483,0.000029350711,0.00005641742,0.0001210394,0.000040836676,0.000033523793,0.00027010572,0.001934834,0.93237966,0.0022344866,0.06223178,0.0003141332],"about_ca_topic_score_codex":0.000019346458,"about_ca_topic_score_gemma":0.000017879334,"teacher_disagreement_score":0.06180658,"about_ca_system_score_codex":0.00009860584,"about_ca_system_score_gemma":0.00003805225,"threshold_uncertainty_score":0.48809683},"labels":[],"label_agreement":null},{"id":"W4389096837","doi":"10.1080/01614940.2023.2275093","title":"Thermochemical conversion of biomass to fuels and chemicals: a review of catalysts, catalyst stability, and reaction mechanisms","year":2023,"lang":"en","type":"review","venue":"Catalysis Reviews","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"FPInnovations; University of British Columbia","funders":"Mitacs","keywords":"Catalysis; Biomass gasification; Biomass (ecology); Waste management; Syngas; Chemistry; tar (computing); Natural gas; Chemical engineering; Environmental science; Engineering; Biofuel; Organic chemistry; Computer science","score_opus":0.06782634917843772,"score_gpt":0.3319708505358419,"score_spread":0.2641445013574042,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389096837","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00030337845,0.9966216,0.00008460491,0.000027368444,0.000092890106,0.0024883528,0.00018536161,0.00009465508,0.000101755315],"genre_scores_gemma":[0.000083317755,0.9967057,0.00033530864,0.000021825788,0.00006492085,0.00040209334,0.0021380787,0.00015963911,0.000089085974],"study_design_codex":"systematic_review","study_design_gemma":"not_applicable","domain_scores_codex":[0.99381286,0.00023052646,0.003552376,0.0012659046,0.0006314123,0.0005068952],"domain_scores_gemma":[0.9949719,0.00057758595,0.0019592398,0.001830487,0.0002162376,0.0004445746],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002921198,0.00097169133,0.007622832,0.0005969923,0.000050381386,0.000012775569,0.0007107225,0.0005684849,0.000040978008],"category_scores_gemma":[0.0028031992,0.00074772915,0.0014961942,0.0024318267,0.00021691783,0.00018823943,0.0009890898,0.00053439435,0.00009804],"study_design_candidate":"systematic_review","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000004850541,0.000044865865,4.861666e-7,0.59168655,0.00044507673,0.0000040338123,0.00007882199,3.6457584e-9,0.19963445,0.000028289955,0.00013036259,0.20794219],"study_design_scores_gemma":[0.00022282367,0.000055384884,2.8754928e-7,0.24899915,0.008111961,0.00013940649,0.000040490428,0.0000046991004,0.25901997,0.000026611831,0.4824045,0.0009747125],"about_ca_topic_score_codex":0.00019717998,"about_ca_topic_score_gemma":0.00000529331,"teacher_disagreement_score":0.48227414,"about_ca_system_score_codex":0.0003541693,"about_ca_system_score_gemma":0.00011753713,"threshold_uncertainty_score":0.99949735},"labels":[],"label_agreement":null},{"id":"W4389151088","doi":"10.1002/cjce.25143","title":"Analysis of the high‐pressure steam import behaviour of an integrated <scp>ethylene oxide/ethylene glycol</scp> petrochemical plant under different production scenarios","year":2023,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Petrochemical; Ethylene oxide; Selectivity; Ethylene; Catalysis; Ethylene glycol; Ordinary least squares; Chemistry; Environmental science; Chemical engineering; Materials science; Econometrics; Engineering; Organic chemistry; Mathematics; Polymer","score_opus":0.00908741105206067,"score_gpt":0.20355763319376727,"score_spread":0.1944702221417066,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389151088","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9987779,0.00023719748,0.00013962339,0.00015694567,0.00035836003,0.00015634371,0.00011828179,0.00004921186,0.0000060951543],"genre_scores_gemma":[0.9994531,0.00000778362,0.00009352462,0.000010263182,0.00018472699,0.0000077571685,0.00009148135,0.00006612004,0.00008521902],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9973832,0.00004068737,0.0010338044,0.00026722296,0.00068945676,0.0005856309],"domain_scores_gemma":[0.9978537,0.00025249468,0.0004945035,0.0006324235,0.00024645965,0.00052043155],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00066717516,0.00034897018,0.00085072225,0.0006918055,0.00006668987,0.000021955133,0.00090224255,0.00026180266,0.000017894075],"category_scores_gemma":[0.0011348089,0.00022599206,0.00053493,0.0019321766,0.00014180767,0.00015877,0.00009586892,0.0010928961,8.7406096e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000013468617,0.000029232593,0.0011778211,0.0000874144,0.00094857166,0.000014132864,0.00034736458,0.16166729,0.8355449,0.000049250237,0.000034280907,0.0000863029],"study_design_scores_gemma":[0.00032702181,0.000030415,0.0045844875,0.00022688364,0.0015064426,0.00011509757,0.00021207031,0.032914463,0.9598278,0.000022352453,0.00009579754,0.00013719128],"about_ca_topic_score_codex":0.0031398016,"about_ca_topic_score_gemma":0.0007179186,"teacher_disagreement_score":0.12875283,"about_ca_system_score_codex":0.00048538935,"about_ca_system_score_gemma":0.0003091777,"threshold_uncertainty_score":0.9215689},"labels":[],"label_agreement":null},{"id":"W4389351339","doi":"10.2139/ssrn.4653633","title":"Dry Reforming of Methane at High Temperature and Elevated Pressure Over Nickel Spinellized Catalyst Powder and Pellets Prepared from a Metallurgical Residue","year":2023,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Pellets; Nickel; Residue (chemistry); Methane; Catalysis; Metallurgy; Carbon dioxide reforming; Materials science; Chemistry; Syngas; Composite material; Organic chemistry","score_opus":0.009665684097014918,"score_gpt":0.24285217878947943,"score_spread":0.2331864946924645,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389351339","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.972592,0.025795065,0.0001749587,0.00017867632,0.00032835835,0.0005006992,0.00022348609,0.00017581887,0.000030964675],"genre_scores_gemma":[0.9805297,0.010223866,0.00026442108,0.000012633271,0.00048035273,0.000034538687,0.0007285149,0.00023389478,0.007492054],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9942747,0.00017277437,0.001308741,0.0010956577,0.0008686032,0.0022795438],"domain_scores_gemma":[0.9974386,0.00027309064,0.0008916065,0.00086662866,0.0001918475,0.00033821902],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0018851965,0.0008530172,0.0017117037,0.00044552554,0.00014283031,0.000065604225,0.0006350879,0.0011308137,0.00009016877],"category_scores_gemma":[0.00051081885,0.00070463214,0.000454611,0.00035104257,0.00015287934,0.00025128396,0.0016549026,0.006189627,0.000009290328],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0012647697,0.00009927387,0.00051837025,0.0009123141,0.007851622,0.00012021553,0.00103941,0.0019702106,0.9845152,0.00095537835,0.000031164403,0.0007221003],"study_design_scores_gemma":[0.013236305,0.00048937957,0.0023374024,0.0033972752,0.007154276,0.0019066075,0.0018134152,0.011715903,0.9072651,0.045171224,0.0017098103,0.003803292],"about_ca_topic_score_codex":0.005086826,"about_ca_topic_score_gemma":0.002103831,"teacher_disagreement_score":0.07725006,"about_ca_system_score_codex":0.0011402768,"about_ca_system_score_gemma":0.00093494746,"threshold_uncertainty_score":0.9995405},"labels":[],"label_agreement":null},{"id":"W4389429119","doi":"10.1007/s10311-023-01673-4","title":"Hydrogen generation by heterogeneous catalytic steam reforming of short-chain alcohols: a review","year":2023,"lang":"en","type":"review","venue":"Environmental Chemistry Letters","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":34,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Steam reforming; Catalysis; Hydrogen; Hydrogen production; Raw material; Methanol; Chemistry; Energy carrier; Hydrogen fuel; Carbon fibers; Chemical engineering; Methane reformer; Waste management; Inorganic chemistry; Materials science; Organic chemistry","score_opus":0.03392261191091703,"score_gpt":0.27303458151943044,"score_spread":0.2391119696085134,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389429119","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0065717986,0.991782,0.000013955478,0.000024007091,0.00007705156,0.0007524799,0.0005706405,0.00014339451,0.00006468349],"genre_scores_gemma":[0.00040706433,0.99022496,0.000019527106,0.000074276475,0.000306214,0.0002804706,0.007815657,0.0003032729,0.00056855445],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99627554,0.000042298776,0.0015246127,0.0008742665,0.000670062,0.0006132367],"domain_scores_gemma":[0.9981036,0.00007029094,0.0005512177,0.0010530727,0.0000037269763,0.00021806973],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003524236,0.0008678987,0.0020743604,0.00006098298,0.00006335347,0.0000086098335,0.00066827587,0.00039866832,0.00012585304],"category_scores_gemma":[0.000060554405,0.00082188344,0.0010504515,0.0002601862,0.00012443971,0.00011529344,0.000374502,0.00065370684,0.00016337249],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000012136209,0.00004772972,5.5921845e-7,0.067373164,0.0005463063,0.00006219937,0.000019510799,0.000057069024,0.7934524,6.555256e-8,0.00035792333,0.13808186],"study_design_scores_gemma":[0.00017815786,0.000009796365,1.5438594e-8,0.027334921,0.0017329726,0.00048215518,0.000011772113,0.00016697467,0.5706377,2.5912277e-7,0.39826494,0.001180364],"about_ca_topic_score_codex":0.00002166359,"about_ca_topic_score_gemma":5.286592e-7,"teacher_disagreement_score":0.39790702,"about_ca_system_score_codex":0.001426039,"about_ca_system_score_gemma":0.00003178653,"threshold_uncertainty_score":0.9994232},"labels":[],"label_agreement":null},{"id":"W4389432550","doi":"10.3390/catal13121499","title":"Novel Ionic Liquid Synthesis of Bimetallic Fe–Ru Catalysts for the Direct Hydrogenation of CO2 to Short Chain Hydrocarbons","year":2023,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"UK Catalysis Hub; Tezpur University; European Commission; Queen's University; Queen's University Belfast; Engineering and Physical Sciences Research Council; Leverhulme Trust","keywords":"Catalysis; Bimetallic strip; Ionic liquid; Selectivity; Hydrocarbon; Product distribution; Fischer–Tropsch process; Chemistry; Chemical engineering; Materials science; Organic chemistry","score_opus":0.02363816119873547,"score_gpt":0.26367634492063263,"score_spread":0.24003818372189717,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389432550","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9950544,0.00048483882,0.0016891441,0.00027555146,0.00027325065,0.0009920768,0.00027409766,0.0002688071,0.0006878004],"genre_scores_gemma":[0.99843127,0.00003698426,0.00015037478,0.0000146842585,0.00012412983,0.0004770285,0.00027594806,0.00010333558,0.00038623915],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976291,0.000021580936,0.0007936708,0.00048075482,0.0005357358,0.0005391497],"domain_scores_gemma":[0.99731076,0.0012078462,0.00021241847,0.0009813413,0.00011885548,0.00016878104],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010760331,0.0003234041,0.00070269755,0.0004531902,0.00009727417,0.000009683027,0.0006935542,0.00016823378,0.0000036593192],"category_scores_gemma":[0.001835786,0.00025908358,0.00048875186,0.0018214856,0.00009380118,0.00013550413,0.00024579364,0.00015185916,0.000039636056],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006889122,0.000060767285,0.000032326134,0.00024457005,0.0004297598,0.000002254636,0.00037987088,0.0020205674,0.9940386,0.0002582829,0.00009367965,0.0023704595],"study_design_scores_gemma":[0.00023581936,0.000052952226,0.00011484894,0.00015472829,0.0003452926,0.000014917742,0.00010019323,0.014789663,0.9832063,0.000015931919,0.00068816013,0.00028119978],"about_ca_topic_score_codex":0.00038968615,"about_ca_topic_score_gemma":0.00010382648,"teacher_disagreement_score":0.012769096,"about_ca_system_score_codex":0.00019419804,"about_ca_system_score_gemma":0.00008429786,"threshold_uncertainty_score":0.9999861},"labels":[],"label_agreement":null},{"id":"W4389496645","doi":"10.1016/j.fuel.2023.130512","title":"Insights to the reaction kinetics of Fischer-Tropsch synthesis using an integral system over Cu-Mo promoted Fe catalyst","year":2023,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs; Canadian Light Source","keywords":"Catalysis; Fischer–Tropsch process; Space velocity; Chemistry; Kinetics; Chemical kinetics; Activation energy; Reaction rate; Reaction mechanism; Chemical engineering; Work (physics); Syngas; Thermodynamics; Order of reaction; Physical chemistry; Reaction rate constant; Organic chemistry; Selectivity","score_opus":0.028194401205229355,"score_gpt":0.26253441119007764,"score_spread":0.23434000998484827,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389496645","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979932,0.00005112199,0.00068751216,0.00003706724,0.0002457058,0.0002572733,0.000024950794,0.00028397364,0.0004192371],"genre_scores_gemma":[0.9991,0.0000026346231,0.00035177777,0.000006014789,0.00022647754,0.000032007356,0.00004749736,0.000059717204,0.00017381886],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99871135,0.00004341784,0.00037176072,0.00026436645,0.00033624913,0.00027287903],"domain_scores_gemma":[0.9990867,0.0000909468,0.00012227037,0.0005028637,0.00008628008,0.00011093963],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018612765,0.00018938322,0.0002952058,0.00021536171,0.00004877772,0.0000184105,0.00028522403,0.00012813712,0.0000050158014],"category_scores_gemma":[0.00036363435,0.00013298455,0.00011173369,0.00090489583,0.00002382706,0.00017052618,0.00012597816,0.00021709254,0.00006331214],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019035644,0.000031676187,0.00002430204,0.000305085,0.000055361797,0.000007144401,0.0008304286,0.0005901765,0.9964983,0.00014623553,0.000014062394,0.0014782007],"study_design_scores_gemma":[0.00014786045,0.000036212747,0.0008680817,0.0003405229,0.000113985356,0.000026028578,0.0010017334,0.06489923,0.93119365,0.000013439146,0.0011404568,0.00021880562],"about_ca_topic_score_codex":0.0015271778,"about_ca_topic_score_gemma":0.00011596239,"teacher_disagreement_score":0.06530465,"about_ca_system_score_codex":0.0002866291,"about_ca_system_score_gemma":0.000017683207,"threshold_uncertainty_score":0.5422953},"labels":[],"label_agreement":null},{"id":"W4389541215","doi":"10.17118/11143/20836","title":"Hydrogen-burning power plant with hydrogen produced by catalyticdecomposition of methane : techno-economic perspectives","year":2023,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Hydrogen; Methane; Decomposition; Catalysis; Environmental science; Power to gas; Waste management; Chemistry; Engineering; Organic chemistry; Physical chemistry","score_opus":0.0063825412389329275,"score_gpt":0.22171549815313837,"score_spread":0.21533295691420545,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389541215","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99680734,0.00018076575,0.00023556642,0.0001345387,0.000032025928,0.0002631169,0.000074540796,0.0005897474,0.0016823784],"genre_scores_gemma":[0.99874985,0.000012987664,0.00019916102,0.000004253696,0.000035433255,0.00003688458,0.00021505245,0.000068527086,0.00067782745],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99855745,0.000010970915,0.0003529752,0.00045073105,0.00023063428,0.00039724572],"domain_scores_gemma":[0.9992229,0.000074000774,0.00013833032,0.00042646224,0.000036391462,0.00010194835],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029348116,0.00024356507,0.00038520808,0.00029147064,0.000036079993,0.000007877414,0.00023447796,0.00010135137,0.00011459866],"category_scores_gemma":[0.00005046304,0.0002009697,0.00010938283,0.00042519497,0.00006172772,0.00020728107,0.00010583297,0.00019776347,0.00012845692],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004642351,0.00003290499,0.000075801996,0.000046316487,0.0001925144,0.000010289024,0.0007142205,0.0017496931,0.99642706,0.00046845517,0.000037778118,0.00019853633],"study_design_scores_gemma":[0.00046685754,0.000075473145,0.000010774445,0.00005698341,0.000052687017,0.000064864376,0.0011420384,0.009255416,0.98835284,0.000025584503,0.00021284114,0.00028367116],"about_ca_topic_score_codex":0.0003910459,"about_ca_topic_score_gemma":0.000011971694,"teacher_disagreement_score":0.008074257,"about_ca_system_score_codex":0.0002737809,"about_ca_system_score_gemma":0.000042926116,"threshold_uncertainty_score":0.81953067},"labels":[],"label_agreement":null},{"id":"W4389692233","doi":"10.2139/ssrn.4663157","title":"An Environmental Impact Comparison of Thermochemical Cycles and Steam Methane Reforming for Hydrogen Production Processes","year":2023,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Steam reforming; Hydrogen production; Methane reformer; Methane; Environmental science; Waste management; Production (economics); Hydrogen; Economics; Chemistry; Engineering; Macroeconomics","score_opus":0.013767903928420347,"score_gpt":0.30194404594136404,"score_spread":0.28817614201294367,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389692233","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970316,0.0022393246,0.00036003656,0.00003643339,0.00004040998,0.00019680859,0.0000090778285,0.0000751491,0.00001112357],"genre_scores_gemma":[0.9987511,0.0007389281,0.000059167804,0.000001211438,0.00024072938,0.000016111466,0.00006180227,0.000050091327,0.00008088026],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99776924,0.000020217705,0.0003869539,0.00023374571,0.00024979218,0.0013400547],"domain_scores_gemma":[0.9994189,0.0000612019,0.00020811254,0.00016245076,0.000028667508,0.00012068018],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001164044,0.00018295555,0.00032153924,0.00015817412,0.00009513284,0.000007717855,0.00018318908,0.00009471605,0.0000053542403],"category_scores_gemma":[0.00021597125,0.00014450731,0.00011415282,0.00022667526,0.000054338598,0.0003286531,0.000038853806,0.0006444565,0.0000023464243],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011264617,0.00006870242,0.002006018,0.00008329533,0.00017504324,4.156959e-7,0.00053522724,0.00043441416,0.9648498,0.00006801744,7.826423e-7,0.031665605],"study_design_scores_gemma":[0.00048027464,0.00033689168,0.000159589,0.00004322051,0.00008457818,0.00032077866,0.0031131844,0.002488871,0.9894339,0.0033220837,0.000029331337,0.00018729293],"about_ca_topic_score_codex":0.000029008072,"about_ca_topic_score_gemma":0.000031502652,"teacher_disagreement_score":0.031478312,"about_ca_system_score_codex":0.00076982664,"about_ca_system_score_gemma":0.00029386382,"threshold_uncertainty_score":0.5892837},"labels":[],"label_agreement":null},{"id":"W4389992248","doi":"10.1016/j.energy.2023.130061","title":"A novel machine learning framework for designing high-performance catalysts for production of clean liquid fuels through Fischer-Tropsch synthesis","year":2023,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs; CRC Health Group","keywords":"Fischer–Tropsch process; Selectivity; Catalysis; Principal component analysis; Process engineering; Carbon fibers; Chemistry; Computer science; Biochemical engineering; Engineering; Artificial intelligence; Organic chemistry; Algorithm","score_opus":0.024020225215048145,"score_gpt":0.2546950387064357,"score_spread":0.23067481349138752,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389992248","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5984116,0.00014480886,0.3999702,0.00015773074,0.0005041032,0.0002701227,0.000032232434,0.00043729658,0.00007189859],"genre_scores_gemma":[0.94811046,0.000070601396,0.049498305,0.000012479009,0.00053451565,0.00046159915,0.00019426848,0.0001307218,0.000987074],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983614,0.000017117667,0.00045392703,0.0004291787,0.00023651258,0.000501849],"domain_scores_gemma":[0.9985592,0.0006936531,0.0002194639,0.0003540618,0.000112086775,0.00006154278],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046560762,0.00025167258,0.0004348543,0.00016888435,0.00016015887,0.00000983598,0.0002400305,0.00019485464,0.00000620408],"category_scores_gemma":[0.0021955848,0.00024071183,0.00018071303,0.0006208922,0.000045362132,0.00028138538,0.0000899318,0.00021976266,0.000005277347],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030465884,0.00004150609,0.000025958585,0.0005870477,0.00015731233,6.9428387e-7,0.0005106942,0.031614278,0.94752663,0.0047727693,0.000040070863,0.014418351],"study_design_scores_gemma":[0.0003038681,0.00014490937,0.000011302655,0.00029932536,0.00008418573,0.0000075289936,0.00014608246,0.023939803,0.97159874,0.00027082028,0.002917423,0.00027602407],"about_ca_topic_score_codex":0.00033586615,"about_ca_topic_score_gemma":0.000016120028,"teacher_disagreement_score":0.35047188,"about_ca_system_score_codex":0.00011052207,"about_ca_system_score_gemma":0.00003427093,"threshold_uncertainty_score":0.9815943},"labels":[],"label_agreement":null},{"id":"W4390202049","doi":"10.1016/j.apcatb.2023.123665","title":"Selective cellobiose photoreforming for simultaneous gluconic acid and syngas production in acidic conditions","year":2023,"lang":"en","type":"article","venue":"Applied Catalysis B: Environmental","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Gluconic acid; Cellobiose; Chemistry; Syngas; Chromatography; Biochemistry; Cellulose; Catalysis; Cellulase","score_opus":0.006139341462087238,"score_gpt":0.21517425246483185,"score_spread":0.2090349110027446,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4390202049","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99846405,0.00009815599,0.000093399,0.00003730864,0.00007372151,0.000764125,0.000097077915,0.0001932112,0.00017894],"genre_scores_gemma":[0.9971302,0.00006492198,0.00012120769,0.00001593463,0.00009041335,0.0006038481,0.0015412892,0.00007095494,0.00036122795],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99825555,0.000009429356,0.00037589695,0.0006229915,0.00022394974,0.00051219703],"domain_scores_gemma":[0.9993201,0.0001459308,0.00010569226,0.00031298542,0.000004946451,0.0001103357],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00024127711,0.00028209056,0.00035173405,0.00030115925,0.0001602194,0.000013945305,0.00013975841,0.00012059135,0.000026801908],"category_scores_gemma":[0.00007821145,0.00029047643,0.00011724409,0.0004952753,0.00016089567,0.00016971455,0.00013208449,0.0002356196,0.0001252595],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004222916,0.00006568766,0.00014079573,0.000055944016,0.000098310506,0.000010160803,0.0006863586,0.002091032,0.99328357,0.000046259058,0.000008869548,0.0034708076],"study_design_scores_gemma":[0.0007411151,0.000027954684,0.0002039486,0.000016435206,0.000112840484,0.000034490953,0.001652568,0.004854997,0.99159294,0.00014212933,0.0002798917,0.00034067052],"about_ca_topic_score_codex":0.000052572006,"about_ca_topic_score_gemma":0.0000443946,"teacher_disagreement_score":0.0031301372,"about_ca_system_score_codex":0.00063286,"about_ca_system_score_gemma":0.000013243913,"threshold_uncertainty_score":0.99995476},"labels":[],"label_agreement":null},{"id":"W4391058271","doi":"10.2172/2279036","title":"Engineering Study of Svante’s Solid Sorbent Post-Combustion CO&lt;sub&gt;2&lt;/sub&gt; Capture Technology at a Linde Steam Methane Reforming H&lt;sub&gt;2&lt;/sub&gt; Plant","year":2023,"lang":"en","type":"report","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Burnaby Hospital","funders":"National Energy Technology Laboratory; U.S. Department of Energy","keywords":"Sorbent; Methane; Steam reforming; Combustion; Waste management; Natural gas; Chemical engineering; Environmental science; Process engineering; Chemistry; Nuclear engineering; Materials science; Engineering; Hydrogen production; Hydrogen; Organic chemistry","score_opus":0.02314802525152112,"score_gpt":0.2762746819144425,"score_spread":0.2531266566629214,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4391058271","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9699098,0.0066173575,0.0013613944,0.00018931535,0.005523667,0.0056273825,0.0016326146,0.0056344336,0.0035040437],"genre_scores_gemma":[0.9750641,0.00605688,0.000660373,0.000051443305,0.0021793111,0.0014112135,0.005767662,0.0022917434,0.0065172743],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.97868574,0.00023204548,0.006537908,0.004230292,0.0058881883,0.004425829],"domain_scores_gemma":[0.98758286,0.0010531563,0.0034417927,0.004649589,0.0020226685,0.001249941],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.004130108,0.004238787,0.007013945,0.0061374092,0.000509517,0.00013891455,0.0030949847,0.0055673807,0.0001655414],"category_scores_gemma":[0.0038959768,0.0039475355,0.002129304,0.003907044,0.00035316494,0.0008243271,0.0034813767,0.005711239,0.0004593985],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00046772853,0.0010411718,0.00008262928,0.004550846,0.0036515729,0.0016351696,0.0015302347,0.0094006965,0.9687923,0.00016849097,0.0009815657,0.0076975836],"study_design_scores_gemma":[0.004703621,0.0010998377,0.0001283774,0.004247347,0.0027289917,0.003593749,0.0020452833,0.009722731,0.9486591,0.000041238618,0.018102938,0.0049267435],"about_ca_topic_score_codex":0.0008475422,"about_ca_topic_score_gemma":0.0039562644,"teacher_disagreement_score":0.02013317,"about_ca_system_score_codex":0.007834308,"about_ca_system_score_gemma":0.0014457058,"threshold_uncertainty_score":0.99703264},"labels":[],"label_agreement":null},{"id":"W4391067209","doi":"10.1016/j.enconman.2023.118026","title":"A new system for hydrogen and methane production with post-combustion amine-based carbon capturing option for better sustainability","year":2024,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Sustainability; Methane; Hydrogen production; Combustion; Amine gas treating; Production (economics); Hydrogen; Carbon fibers; Waste management; Environmental science; Process engineering; Co2 removal; Chemistry; Carbon dioxide; Materials science; Engineering; Environmental engineering; Organic chemistry; Economics; Ecology","score_opus":0.005086795938622878,"score_gpt":0.2013606115793294,"score_spread":0.19627381564070653,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4391067209","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.813223,0.00047771801,0.18306546,0.0014706143,0.0003481604,0.0010345984,0.0000050659437,0.00030029225,0.000075084215],"genre_scores_gemma":[0.99626046,0.000015527847,0.0017773104,0.00002645762,0.00012044778,0.00015882943,0.00008169318,0.00002806649,0.0015312124],"study_design_codex":"design_other","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991933,0.000010239097,0.00014063863,0.00036271985,0.000115122835,0.00017798714],"domain_scores_gemma":[0.99966663,0.000035497666,0.000034068835,0.0001353534,0.000056804845,0.000071669325],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000207377,0.00014255707,0.0001434845,0.00016734448,0.000046210334,0.000023417688,0.000037274516,0.00005199811,0.0000010849814],"category_scores_gemma":[0.000015452702,0.00011832562,0.00004807435,0.00010364782,0.000014760489,0.00010623659,0.000039568484,0.000041577856,1.558784e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0032991667,0.00013172174,0.00017760761,0.07312426,0.0016008124,0.00009452214,0.0014235174,0.033636786,0.3568779,0.043969907,0.0002980385,0.48536578],"study_design_scores_gemma":[0.0022981965,0.00023600274,0.00003425074,0.0006026083,0.0006017496,0.000021966485,0.0013076118,0.2358735,0.7389474,0.00015652871,0.019511957,0.0004082527],"about_ca_topic_score_codex":0.0003665455,"about_ca_topic_score_gemma":0.000017103846,"teacher_disagreement_score":0.48495752,"about_ca_system_score_codex":0.0003065216,"about_ca_system_score_gemma":0.000018319055,"threshold_uncertainty_score":0.48251787},"labels":[],"label_agreement":null},{"id":"W4391090516","doi":"10.1021/acs.iecr.3c03647","title":"CO<sub>2</sub> Hydrogenation to Methanol in a Slurry Reactor: Catalytic Performance of CuO-Enhanced In<sub>2</sub>O<sub>3</sub>/ZrO<sub>2</sub>","year":2024,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation","keywords":"Catalysis; Methanol; Slurry; Materials science; Chemical engineering; Inorganic chemistry; Chemistry; Organic chemistry","score_opus":0.0375773191540839,"score_gpt":0.3002126090973152,"score_spread":0.26263528994323126,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4391090516","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99559516,0.0007468768,0.00012744563,0.00014245823,0.00069316686,0.0014953437,0.00019478977,0.00065112516,0.00035361233],"genre_scores_gemma":[0.9963311,0.00047164154,0.000028232882,0.0000095307005,0.0014779859,0.00069854496,0.0004996744,0.00044362334,0.000039689825],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.98966265,0.00015344535,0.0024020541,0.002015457,0.0028357839,0.0029306307],"domain_scores_gemma":[0.9952494,0.0013327586,0.0002983454,0.0016521162,0.00047848394,0.0009888763],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.004181076,0.001290709,0.0016846376,0.0020324008,0.000162369,0.00021906306,0.0015168086,0.0017884452,0.000016644288],"category_scores_gemma":[0.0041274778,0.0014750068,0.0005405834,0.006020003,0.0002530535,0.0010404777,0.00073445466,0.0058440943,0.00024131373],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00035078463,0.00019982761,0.00008454853,0.0020805872,0.00024561712,0.00021325384,0.0006246981,0.014831132,0.95806676,0.000011389846,0.00016179372,0.02312958],"study_design_scores_gemma":[0.002105744,0.00015015664,0.000057619676,0.0031267041,0.00008245025,0.000103475875,0.00013816617,0.035132896,0.9573477,0.000014696686,0.0004099266,0.0013304579],"about_ca_topic_score_codex":0.00014252972,"about_ca_topic_score_gemma":0.000037086407,"teacher_disagreement_score":0.021799123,"about_ca_system_score_codex":0.0039306306,"about_ca_system_score_gemma":0.0010963111,"threshold_uncertainty_score":0.99998444},"labels":[],"label_agreement":null},{"id":"W4391138805","doi":"10.1007/s13369-023-08576-0","title":"Cost-Effective Single-Step Synthesis of Metal Oxide-Supported Ni Catalyst for H2-Production Through Dry Reforming of Methane","year":2024,"lang":"en","type":"article","venue":"Arabian Journal for Science and Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Queen's University; King Saud University; Queen's University Belfast","keywords":"Methane; Catalysis; Carbon dioxide reforming; Production (economics); Hydrogen production; Materials science; Metal; Oxide; Methane reformer; Chemical engineering; Hydrogen; Syngas; Steam reforming; Chemistry; Metallurgy; Engineering; Organic chemistry; Economics","score_opus":0.02955983418478966,"score_gpt":0.2840618166834007,"score_spread":0.25450198249861106,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4391138805","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9006495,0.001217236,0.09565529,0.000090738635,0.0013758582,0.00081954926,0.000040020077,0.00008895909,0.000062870786],"genre_scores_gemma":[0.9858044,0.00004625957,0.01370334,0.0000031648024,0.00019113392,0.0001309293,0.0000052967653,0.000048084767,0.00006743479],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981109,0.000007792811,0.0006005796,0.0003663762,0.0004208359,0.0004934955],"domain_scores_gemma":[0.99876755,0.0003691072,0.00017082618,0.0002178369,0.00032602903,0.00014867332],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0021271517,0.00022624098,0.0004782269,0.0005034447,0.00011618678,0.00004039913,0.00027352414,0.000080825805,0.0000024897788],"category_scores_gemma":[0.0027510663,0.00019022106,0.00023555494,0.00092726515,0.00016205148,0.001321127,0.00006074786,0.00023381945,6.068973e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000031311207,0.000017030132,0.000011387504,0.00078314915,0.0001398671,0.0000038703492,0.0006095703,0.0029972182,0.9379657,0.00039387614,0.000003896877,0.05704311],"study_design_scores_gemma":[0.00020833079,0.00010878954,0.000027189239,0.00068366446,0.0002110333,0.00024992847,0.0005063819,0.04742906,0.94908655,0.00010290819,0.001172337,0.0002138152],"about_ca_topic_score_codex":0.000045285764,"about_ca_topic_score_gemma":0.000004732842,"teacher_disagreement_score":0.08515488,"about_ca_system_score_codex":0.00029497273,"about_ca_system_score_gemma":0.00010011451,"threshold_uncertainty_score":0.77569896},"labels":[],"label_agreement":null},{"id":"W4391583034","doi":"10.1016/b978-0-443-15740-0.00039-2","title":"Process and Reactor Consideration for Syngas Production from Natural Gas Steam Reforming","year":2024,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Syngas; Syngas to gasoline plus; Natural gas; Process (computing); Steam reforming; Process engineering; Waste management; Production (economics); Environmental science; Chemistry; Hydrogen production; Engineering; Economics; Computer science; Catalysis; Organic chemistry","score_opus":0.012987777748299727,"score_gpt":0.2478865640584048,"score_spread":0.23489878631010508,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4391583034","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.06751982,0.014262083,0.000015371143,0.00033071934,0.0042428155,0.0034967407,0.00033328042,0.0010083449,0.9087908],"genre_scores_gemma":[0.048755173,0.00007597419,0.00024939593,0.00003211856,0.0019812877,0.000175046,0.00046633568,0.0002704325,0.94799423],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99804175,0.000004805439,0.00056749495,0.00076131953,0.00031309252,0.00031152178],"domain_scores_gemma":[0.999005,0.000103499246,0.00023269722,0.00039706,0.00015531751,0.00010642142],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00021854458,0.0005046044,0.0005929178,0.00018814682,0.00009217013,0.000047507434,0.00012489228,0.0003341135,0.000017411066],"category_scores_gemma":[0.00018564174,0.00043604497,0.00020290096,0.000017263623,0.00007354387,0.00018367094,0.00009427036,0.0007691049,0.000029222072],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000063378684,0.0000047528,4.8153106e-7,0.0015511458,0.0003515207,0.00002139055,0.00083973946,0.0000027261012,0.107418016,0.002350286,0.000016450636,0.8873801],"study_design_scores_gemma":[0.0005510598,0.00006782799,5.4078157e-7,0.0044893757,0.0009322728,0.00026682645,0.0001344419,0.0007189862,0.38117418,0.040681858,0.5696861,0.0012965249],"about_ca_topic_score_codex":0.0000041182207,"about_ca_topic_score_gemma":0.000049752725,"teacher_disagreement_score":0.8860836,"about_ca_system_score_codex":0.0003196852,"about_ca_system_score_gemma":0.000077360644,"threshold_uncertainty_score":0.99980915},"labels":[],"label_agreement":null},{"id":"W4391610689","doi":"10.1002/cjce.25187","title":"Valorization of refinery flue gas through tri‐reforming and direct hydrogenation routes","year":2024,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Refinery; Flue gas; Oil refinery; Greenhouse gas; Environmental science; Waste management; Syngas; Carbon dioxide; Environmental engineering; Pulp and paper industry; Hydrogen; Chemistry; Engineering","score_opus":0.009140977177039508,"score_gpt":0.20596359594233352,"score_spread":0.196822618765294,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4391610689","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99312085,0.0038878736,0.0018479978,0.00025750534,0.00037542422,0.000066890476,0.000010217594,0.00004564655,0.0003875982],"genre_scores_gemma":[0.9991174,0.000021092052,0.00043743788,0.0000103054945,0.0003249219,0.000002231454,0.000007348968,0.00004292456,0.000036382902],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989104,0.000008059519,0.00048202844,0.00011423583,0.00022350911,0.00026174556],"domain_scores_gemma":[0.9993075,0.00018396309,0.00009778106,0.00013206566,0.00008213454,0.0001965667],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00040137768,0.00015834165,0.00027985024,0.0002214006,0.000035094705,0.000034264416,0.00018894499,0.000105606676,0.000011898148],"category_scores_gemma":[0.00054106035,0.000115737006,0.00013300641,0.0004029189,0.000045322897,0.0003427764,0.000021644708,0.00038483765,0.0000015930075],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000067502388,0.0000028736542,0.000024372726,0.00024338109,0.00012321204,0.000030094005,0.00092870573,0.010779959,0.98241526,0.002160384,0.00001627778,0.0032687453],"study_design_scores_gemma":[0.00016487447,0.000015512427,0.0000068981262,0.00048555736,0.0000861792,0.00031846747,0.000022227532,0.07175218,0.92530435,0.00021464509,0.0014819225,0.00014720923],"about_ca_topic_score_codex":0.00103736,"about_ca_topic_score_gemma":0.000052689455,"teacher_disagreement_score":0.060972225,"about_ca_system_score_codex":0.00032337848,"about_ca_system_score_gemma":0.00016121565,"threshold_uncertainty_score":0.47196183},"labels":[],"label_agreement":null},{"id":"W4392107268","doi":"10.1016/j.ijhydene.2024.02.179","title":"Sustainable hydrogen production and CO2 mitigation from acetic acid dry reforming over Ni/Al2O3 catalyst","year":2024,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Trường Đại học Nguyễn Tất Thành; National Foundation for Science and Technology Development","keywords":"Catalysis; Non-blocking I/O; Acetic acid; Syngas; Hydrogen; Chemistry; Carbon fibers; Amorphous solid; Desorption; Carbon dioxide reforming; Decomposition; Hydrogen production; Amorphous carbon; Particle size; Activation energy; Chemical engineering; Inorganic chemistry; Materials science; Adsorption; Organic chemistry; Physical chemistry; Composite number; Composite material","score_opus":0.005487739180750592,"score_gpt":0.23176579011428042,"score_spread":0.22627805093352982,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392107268","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99247843,0.0049075913,0.0007337847,0.00043878256,0.0009945318,0.000046838006,0.000017524637,0.00006738263,0.0003151222],"genre_scores_gemma":[0.9959555,0.0002310744,0.00017750039,0.000039398565,0.0015092706,0.0000072421453,0.000092660455,0.00005313547,0.0019341982],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99807376,0.00002578834,0.0006259304,0.0002810843,0.0006961923,0.0002972666],"domain_scores_gemma":[0.99911493,0.000057186873,0.00024100298,0.00016914449,0.00027988543,0.00013782395],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00038836704,0.00020920236,0.0002634191,0.00045216607,0.000060303573,0.00007618688,0.00033330853,0.00011624142,0.00007529961],"category_scores_gemma":[0.00027657568,0.00018337292,0.0001789363,0.0002268212,0.00005374214,0.0010697084,0.00016945838,0.00028320155,0.000009669331],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000073708215,0.000038016442,0.00025464184,0.00005259927,0.00084609113,0.00057507504,0.0006687395,0.0020999715,0.9825037,0.002256609,0.00007108058,0.010559752],"study_design_scores_gemma":[0.00031182673,0.00003165534,0.00003090483,0.00034283497,0.0001239737,0.0007592323,0.00033638932,0.0098392125,0.97410834,0.0019646054,0.011936825,0.00021422407],"about_ca_topic_score_codex":0.0011182461,"about_ca_topic_score_gemma":0.000073802345,"teacher_disagreement_score":0.011865744,"about_ca_system_score_codex":0.00066901563,"about_ca_system_score_gemma":0.0001047376,"threshold_uncertainty_score":0.74777305},"labels":[],"label_agreement":null},{"id":"W4392203454","doi":"10.1016/j.cherd.2024.02.046","title":"Feedback control strategy of Fischer–Tropsch process in a micro-GtL plant","year":2024,"lang":"en","type":"article","venue":"Process Safety and Environmental Protection","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; Queen's University; Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs; Canada Foundation for Innovation","keywords":"Fischer–Tropsch process; Gas to liquids; Process (computing); Process engineering; Control (management); Business; Computer science; Chemistry; Engineering; Catalysis; Waste management; Operating system; Organic chemistry","score_opus":0.007438329902474652,"score_gpt":0.2096586151022733,"score_spread":0.20222028519979865,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392203454","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9894004,0.0015828516,0.007840493,0.000065784596,0.000054525113,0.00057715207,0.00009606781,0.00008606442,0.00029665572],"genre_scores_gemma":[0.99955803,0.0001246946,0.0000148939525,0.000005062218,0.000046184425,0.00009203318,0.00004587088,0.000028477603,0.00008475773],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989694,0.000014816908,0.00032965917,0.00029706507,0.00017310854,0.00021594683],"domain_scores_gemma":[0.9997792,0.000020234394,0.000059434908,0.00008449084,0.000003779454,0.000052857882],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017950883,0.00017131292,0.00022037081,0.00009629851,0.000041200998,0.000012767335,0.000071726405,0.00012643913,0.000049639846],"category_scores_gemma":[0.0000151811955,0.00015325667,0.000046535846,0.00016691544,0.000060639733,0.00030232858,0.00002369507,0.0003389644,0.00001044966],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0007605719,0.0001425204,0.0005177474,0.0033878984,0.0000888096,0.000022279384,0.0013421301,0.03174663,0.9339319,0.000045299912,4.197255e-7,0.028013792],"study_design_scores_gemma":[0.0020733878,0.00019382646,0.0015457652,0.0007940576,0.000074585005,0.00027917916,0.0017032132,0.26123407,0.7305529,0.00058400305,0.00044372748,0.00052126945],"about_ca_topic_score_codex":0.000072882256,"about_ca_topic_score_gemma":0.000008832412,"teacher_disagreement_score":0.22948743,"about_ca_system_score_codex":0.00013402752,"about_ca_system_score_gemma":0.000015293526,"threshold_uncertainty_score":0.62496257},"labels":[],"label_agreement":null},{"id":"W4392235042","doi":"10.1002/cjce.25224","title":"Performance of Ni/Si‐MCM‐41 catalysts in CO <sub>2</sub> methanation","year":2024,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"Fundação Araucária; Conselho Nacional de Desenvolvimento Científico e Tecnológico","keywords":"Methanation; Catalysis; Space velocity; Thermogravimetric analysis; Selectivity; Methane; Scanning electron microscope; Yield (engineering); Materials science; Chemistry; Nickel; Activation energy; Analytical Chemistry (journal); Inorganic chemistry; Physical chemistry; Metallurgy; Organic chemistry; Composite material","score_opus":0.008013170610867053,"score_gpt":0.20908198028962313,"score_spread":0.20106880967875607,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392235042","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978214,0.0012385728,0.00013409459,0.00015564435,0.00035098285,0.0000744966,0.000010020938,0.000028132949,0.00018669199],"genre_scores_gemma":[0.99955136,0.000014952431,0.00011355444,0.00000993228,0.00023031828,0.0000041669027,0.000009569937,0.000050892813,0.000015228373],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984451,0.000011268045,0.0006577153,0.00013850108,0.00033068206,0.0004167263],"domain_scores_gemma":[0.99909484,0.00019244502,0.00010875004,0.00020719321,0.0000880765,0.0003086736],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007378299,0.00020006855,0.00036529987,0.0005858147,0.000023116883,0.000026689217,0.00040270688,0.00014241057,0.000012366381],"category_scores_gemma":[0.00044348286,0.00016149595,0.0001704071,0.0006892773,0.000057925976,0.00028442295,0.000023097129,0.0007996051,0.000009304078],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000088176575,0.000004186177,0.000085215484,0.00027428727,0.00007435043,0.000057957408,0.00045273826,0.013863645,0.9815157,0.00019295006,0.000031915326,0.0034382252],"study_design_scores_gemma":[0.00018265925,0.00001593023,0.0000561431,0.00056883064,0.00004422078,0.00025507467,0.000014629249,0.08168294,0.916769,0.000018152998,0.00023219678,0.00016021947],"about_ca_topic_score_codex":0.0007752355,"about_ca_topic_score_gemma":0.0002472749,"teacher_disagreement_score":0.0678193,"about_ca_system_score_codex":0.0007329811,"about_ca_system_score_gemma":0.00035629197,"threshold_uncertainty_score":0.65856135},"labels":[],"label_agreement":null},{"id":"W4392285397","doi":"10.1021/acs.energyfuels.3c04762","title":"Enhanced Biomass-Derived Glycerol Conversion to Syngas in the CO<sub>2</sub> Reforming Process: Influence of the Nickel Loading Method on Physicochemical Properties and Catalytic Performance","year":2024,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Syngas; Nickel; Catalysis; Biomass (ecology); Glycerol; Process (computing); Chemical engineering; Chemistry; Catalytic reforming; Materials science; Organic chemistry; Computer science","score_opus":0.012280932525984577,"score_gpt":0.24255486085982417,"score_spread":0.23027392833383958,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392285397","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99877155,0.00030042723,0.0002480098,0.00015800209,0.000071766444,0.00020306032,0.000004448434,0.000073254014,0.00016946107],"genre_scores_gemma":[0.999555,0.000041552958,0.000037552018,0.0001214948,0.00006278392,0.00009203952,0.000006119639,0.00003957352,0.000043901924],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984231,0.000042330477,0.00037075253,0.00040023174,0.0004000501,0.00036355288],"domain_scores_gemma":[0.99922335,0.00018261901,0.00008451811,0.0003936457,0.000049125192,0.0000667132],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035005301,0.0002609803,0.00030736066,0.00014931362,0.00008887903,0.000029251769,0.00042726734,0.00010787445,0.0000012117547],"category_scores_gemma":[0.00017654964,0.00015070062,0.00009538074,0.000678283,0.000104346946,0.00039958797,0.00015071436,0.00032383643,0.0000084526355],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006917022,0.000021175016,0.000014203096,0.0006606394,0.000032479842,0.0000032330245,0.002788944,0.0011007248,0.9904061,0.000099940284,0.0000018270188,0.0048015853],"study_design_scores_gemma":[0.00022799447,0.00005732837,0.00006817354,0.0014113826,0.00003237888,0.000023820052,0.000387823,0.0033143596,0.994175,0.000029944998,0.00006469211,0.00020705746],"about_ca_topic_score_codex":0.00012296188,"about_ca_topic_score_gemma":0.000008457522,"teacher_disagreement_score":0.004594528,"about_ca_system_score_codex":0.00018672502,"about_ca_system_score_gemma":0.00006003153,"threshold_uncertainty_score":0.6145393},"labels":[],"label_agreement":null},{"id":"W4392303547","doi":"10.1016/j.cej.2024.150053","title":"Thermally coupled catalytic hydrogen combustion-reverse water gas shift reactor: Model-based feasibility study and parametric analysis","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Water-gas shift reaction; Combustion; Hydrogen; Transient (computer programming); Thermal; Chemistry; Nuclear engineering; Catalysis; Parametric statistics; Thermodynamics; Materials science; Mechanics; Physical chemistry; Physics; Organic chemistry","score_opus":0.01584322536199308,"score_gpt":0.24709148803720302,"score_spread":0.23124826267520993,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392303547","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9388528,0.00044975476,0.05990453,0.000073088806,0.00013609522,0.00022039596,0.000012517714,0.00033225806,0.000018584928],"genre_scores_gemma":[0.99845636,0.000008050894,0.0011650361,0.000013249948,0.00016313049,0.00001756131,0.000058719696,0.00008675576,0.00003113987],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9975711,0.000019566573,0.0006849495,0.0005317659,0.00056374754,0.00062886457],"domain_scores_gemma":[0.9986872,0.0002491752,0.000060130562,0.00046427333,0.00007077109,0.00046842848],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00086176983,0.0004290106,0.00064374733,0.0007148892,0.00005628932,0.00014794321,0.0003314041,0.00019339679,0.00006708171],"category_scores_gemma":[0.00033554167,0.0003243837,0.0004461344,0.0010860548,0.000049203903,0.00029133653,0.00012507611,0.0011288605,0.000022336319],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000041021372,0.00017939693,0.00047625692,0.0002051449,0.001117645,0.00014021048,0.0004683752,0.44644073,0.5505304,0.000015205196,0.000004376761,0.00038127572],"study_design_scores_gemma":[0.0005762992,0.00002904287,0.00006212447,0.00006183635,0.0010866228,0.000077227705,0.000018490138,0.7944649,0.20322691,0.000028576624,0.000023079907,0.00034492605],"about_ca_topic_score_codex":0.000031955256,"about_ca_topic_score_gemma":0.0000013628438,"teacher_disagreement_score":0.34802413,"about_ca_system_score_codex":0.00051516684,"about_ca_system_score_gemma":0.0000649955,"threshold_uncertainty_score":0.99992085},"labels":[],"label_agreement":null},{"id":"W4392437716","doi":"10.1016/j.fuel.2024.131290","title":"A review of Computational Fluid Dynamics modeling of dry reforming of methane for improved catalyst and reactor design","year":2024,"lang":"en","type":"review","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"SAIT Polytechnic","funders":"Lebanese American University","keywords":"Computational fluid dynamics; Process engineering; Syngas; Methane; Hydrogen production; Computer science; Chemical reaction engineering; Chemical reactor; Process (computing); Hydrogen; Fluid dynamics; Biochemical engineering; Catalysis; Environmental science; Chemistry; Chemical engineering; Thermodynamics; Engineering; Physics","score_opus":0.049945495939151395,"score_gpt":0.32327280398466124,"score_spread":0.27332730804550986,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392437716","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.000009088994,0.94766587,0.050296865,0.0000053502995,0.00011499691,0.0010889904,0.00073914736,0.0000348167,0.000044891003],"genre_scores_gemma":[0.0000637759,0.97841364,0.019832063,0.0000043306945,0.000063351945,0.00010643131,0.0013494898,0.0001199303,0.000046956637],"study_design_codex":"systematic_review","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99729073,0.00003792108,0.0018033648,0.0003908913,0.00023005735,0.00024702313],"domain_scores_gemma":[0.9979494,0.0004877326,0.0007982461,0.00041999435,0.00026357206,0.00008103027],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010371151,0.00042572833,0.0028096968,0.00032960676,0.000009260357,0.0000035493613,0.00029783355,0.00027700042,0.0000033524225],"category_scores_gemma":[0.0006643079,0.00033087892,0.0007879746,0.00044257197,0.000051395753,0.000100271616,0.00018647395,0.00030375549,0.0000011075554],"study_design_candidate":"systematic_review","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000011587221,0.000020679678,1.8521227e-8,0.73041403,0.00051107747,7.920101e-7,0.000054074582,0.00018662166,0.0011937518,0.00021227615,0.00000391388,0.26739115],"study_design_scores_gemma":[0.00039476404,0.000097264434,6.241364e-9,0.38202223,0.00656935,0.00005464876,0.00003648981,0.58571154,0.0013969304,0.00056596,0.022533745,0.00061707245],"about_ca_topic_score_codex":0.00010638771,"about_ca_topic_score_gemma":0.0000036556467,"teacher_disagreement_score":0.5855249,"about_ca_system_score_codex":0.00025520692,"about_ca_system_score_gemma":0.00028384288,"threshold_uncertainty_score":0.99991435},"labels":[],"label_agreement":null},{"id":"W4392590540","doi":"10.1016/j.ijhydene.2023.12.258","title":"Design of a novel tubular membrane reactor with a middle annular injector for enhancement of dry reforming towards high hydrogen purity: CFD analysis","year":2024,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":25,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Windsor; Memorial University of Newfoundland","funders":"","keywords":"Injector; Computational fluid dynamics; Hydrogen; Membrane reactor; Hydrogen production; Materials science; Nuclear engineering; Membrane; Chemical engineering; Chemistry; Process engineering; Mechanics; Thermodynamics; Engineering; Physics; Organic chemistry","score_opus":0.019882349127231594,"score_gpt":0.25334538761294473,"score_spread":0.23346303848571315,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392590540","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.75917363,0.0011893195,0.239117,0.000074517404,0.00020647468,0.000091853035,0.00007797607,0.000020856374,0.00004834001],"genre_scores_gemma":[0.9896267,0.00012518751,0.009652543,0.000016873084,0.0002898723,0.000021117039,0.000070013644,0.00005610473,0.0001415745],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972417,0.000022210372,0.0011254394,0.00026177595,0.0010845729,0.00026434852],"domain_scores_gemma":[0.9981931,0.00016363838,0.0006304007,0.0002435713,0.0006455518,0.00012377495],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005398147,0.0002591623,0.0007120104,0.0010208212,0.000017771501,0.000020347588,0.00060478237,0.0001153408,0.000063977444],"category_scores_gemma":[0.00013160305,0.00020016941,0.0005686149,0.00061540847,0.00005409176,0.00037876747,0.00009682185,0.00017806866,6.01027e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004433527,0.00020189553,0.00002626565,0.00013613976,0.008738003,0.00008773931,0.00036695987,0.034919072,0.9500714,0.0006779102,0.0000016593458,0.004329599],"study_design_scores_gemma":[0.0009475028,0.00026986975,0.000003179047,0.00045571456,0.0010089434,0.00013416298,0.000058198064,0.06301801,0.9328514,0.0001001711,0.00095716026,0.00019571734],"about_ca_topic_score_codex":0.00057763065,"about_ca_topic_score_gemma":0.000024728757,"teacher_disagreement_score":0.23045306,"about_ca_system_score_codex":0.00040612445,"about_ca_system_score_gemma":0.00022855168,"threshold_uncertainty_score":0.8162672},"labels":[],"label_agreement":null},{"id":"W4392659549","doi":"10.1016/j.cej.2024.150274","title":"CO2-to-methanol: Economic and environmental comparison of emerging and established technologies with dry reforming and methane pyrolysis","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":30,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Methane; Natural gas; Methane reformer; Steam reforming; Pyrolysis; Cost of electricity by source; Methanol; Waste management; Carbon dioxide reforming; Syngas; Environmental science; Hydrogen; Hydrogen production; Process engineering; Chemistry; Electricity generation; Engineering; Organic chemistry","score_opus":0.005629140830328122,"score_gpt":0.2212659139015915,"score_spread":0.2156367730712634,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4392659549","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9855498,0.0065446384,0.0074004848,0.00009382359,0.00008658661,0.00008322459,0.0000119641445,0.00020755005,0.000021916414],"genre_scores_gemma":[0.9897289,0.00021122424,0.009887943,0.000002668562,0.00007450811,0.000008374181,0.000006977463,0.000060718583,0.000018679455],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986884,0.0000050478993,0.00044332442,0.00032629818,0.00018226285,0.00035466478],"domain_scores_gemma":[0.9993904,0.00016091242,0.000075191165,0.00016215543,0.000008958981,0.00020234253],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002662347,0.00027908824,0.0005111186,0.00038313968,0.000038163464,0.000060233127,0.00014260788,0.0001502853,0.000009269575],"category_scores_gemma":[0.00012121904,0.00023011245,0.000060479593,0.00017903639,0.00010314523,0.000321023,0.00023084607,0.0006503347,0.0000011624564],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000024509767,0.000009545498,0.00059823954,0.0002693436,0.00017095628,0.000023182944,0.0006527317,0.0024142517,0.9689676,0.000064470085,0.0000025968347,0.02680258],"study_design_scores_gemma":[0.00035690315,0.000052995794,0.00004413539,0.0004210013,0.00011882032,0.0006153725,0.00092875416,0.11155067,0.8851779,0.00002079496,0.00040843725,0.0003042252],"about_ca_topic_score_codex":0.000012754285,"about_ca_topic_score_gemma":6.450072e-7,"teacher_disagreement_score":0.10913642,"about_ca_system_score_codex":0.00018607493,"about_ca_system_score_gemma":0.000015993355,"threshold_uncertainty_score":0.93837136},"labels":[],"label_agreement":null},{"id":"W4393067479","doi":"10.2139/ssrn.4769406","title":"Experimental Study and Statistical Analysis of Hydrogen Selectivity in Methane Steam Reforming Over a Hydroxyapatite- Supported Nickel Catalyst","year":2024,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Steam reforming; Methane; Catalysis; Nickel; Selectivity; Methane reformer; Hydrogen; Hydrogen production; Waste management; Chemical engineering; Chemistry; Environmental science; Materials science; Metallurgy; Organic chemistry; Engineering","score_opus":0.009887667628150305,"score_gpt":0.2877944068552021,"score_spread":0.2779067392270518,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4393067479","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9920593,0.006382857,0.00053544383,0.000013793762,0.00013798269,0.000558388,0.00012824491,0.00007570598,0.00010827359],"genre_scores_gemma":[0.998918,0.0002902674,0.000047336278,0.0000036097022,0.00011172759,0.000061086444,0.00021677776,0.000119032535,0.00023213642],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9941725,0.00020931182,0.0014846972,0.000943249,0.0009127828,0.0022774497],"domain_scores_gemma":[0.9983263,0.00019514587,0.0005520883,0.0006064962,0.00008360641,0.00023635529],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0036117227,0.00066999474,0.0018005355,0.002033061,0.00006323061,0.000037098267,0.00050171005,0.00039131878,0.000054630975],"category_scores_gemma":[0.00024148343,0.0006110847,0.0005190077,0.0015544371,0.00009181339,0.00017856392,0.0011558894,0.006590031,0.000004579298],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00090320455,0.0043812385,0.03326433,0.0010107551,0.05677197,0.00060510234,0.012785978,0.007767159,0.8619006,0.0039265347,0.0000035674207,0.016679555],"study_design_scores_gemma":[0.0071286997,0.0025881366,0.004024369,0.0009256311,0.025446398,0.0015277283,0.023093244,0.17062846,0.7359614,0.0247879,0.000033517517,0.0038545374],"about_ca_topic_score_codex":0.0067231674,"about_ca_topic_score_gemma":0.00818381,"teacher_disagreement_score":0.1628613,"about_ca_system_score_codex":0.0047887275,"about_ca_system_score_gemma":0.0016849188,"threshold_uncertainty_score":0.99989116},"labels":[],"label_agreement":null},{"id":"W4393176617","doi":"10.1016/j.biombioe.2024.107179","title":"Engineering biochar-supported nickel catalysts for efficient CO2 methanation","year":2024,"lang":"en","type":"article","venue":"Biomass and Bioenergy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":31,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Methanation; Biochar; Methane; Catalysis; Nickel; Materials science; Yield (engineering); Space velocity; Chemistry; Selectivity; Substitute natural gas; Incipient wetness impregnation; Inorganic chemistry; Chemical engineering; Pyrolysis; Syngas; Metallurgy; Organic chemistry","score_opus":0.012522793751536018,"score_gpt":0.24331164733713312,"score_spread":0.2307888535855971,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4393176617","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9673332,0.005324334,0.02487424,0.0002982487,0.0009895761,0.00025040298,0.0001313427,0.00059387,0.00020478368],"genre_scores_gemma":[0.99794465,0.000029011424,0.0007490447,0.00001003646,0.00022727223,0.000059083814,0.00027727883,0.000050846982,0.00065276405],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988933,0.0000047304216,0.00025944016,0.0003660695,0.0001603811,0.0003160619],"domain_scores_gemma":[0.99954575,0.000088769135,0.000033058594,0.00017124155,0.00004049267,0.00012069883],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002216646,0.00019970197,0.00020248718,0.00026465047,0.000043246728,0.0000458033,0.000099877485,0.00012904902,0.000013257711],"category_scores_gemma":[0.00007124023,0.00016503228,0.0001316552,0.00037636465,0.00002326646,0.00007270742,0.0000627839,0.00006722945,0.00001613993],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000086486725,0.000014360345,0.000004084338,0.00032417636,0.000105357445,0.0000098893515,0.00005356809,0.00018584804,0.9860209,0.0049676197,0.00010786113,0.008197676],"study_design_scores_gemma":[0.00021110375,0.000022397879,0.00001359383,0.00007300254,0.000056781602,0.000028456905,0.000020078869,0.1625533,0.8116863,0.000014384185,0.025107954,0.00021267745],"about_ca_topic_score_codex":0.00019793541,"about_ca_topic_score_gemma":0.000009967938,"teacher_disagreement_score":0.17433465,"about_ca_system_score_codex":0.00009866033,"about_ca_system_score_gemma":0.000024135321,"threshold_uncertainty_score":0.67298216},"labels":[],"label_agreement":null},{"id":"W4393238196","doi":"10.1016/j.memsci.2024.122714","title":"Development of Nb-based alloy membranes with improved resistance to corrosion by H2S","year":2024,"lang":"en","type":"article","venue":"Journal of Membrane Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut National de la Recherche Scientifique","funders":"National Natural Science Foundation of China","keywords":"Membrane; Corrosion; Alloy; Materials science; Chemical engineering; Chemistry; Metallurgy; Engineering; Biochemistry","score_opus":0.00864427674621004,"score_gpt":0.24435176246854726,"score_spread":0.2357074857223372,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4393238196","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9825455,0.0006512835,0.015488617,0.00036064495,0.00038913652,0.00013781409,0.0000056600506,0.00004427204,0.00037706556],"genre_scores_gemma":[0.975522,0.000009594337,0.023808744,0.000037320406,0.00004658566,0.0000032381088,0.0000011204764,0.000023079507,0.00054831756],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977605,0.0000096150925,0.00062480796,0.00024950336,0.0010326579,0.00032291492],"domain_scores_gemma":[0.9989448,0.00011265341,0.00021355278,0.00021434318,0.00026257182,0.00025205227],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0015217528,0.0001627453,0.0003192663,0.00037800134,0.00008130937,0.00004526422,0.00058573775,0.000043431337,0.00002369707],"category_scores_gemma":[0.0002735687,0.0001098339,0.0000817827,0.0012481086,0.00014065109,0.00043430392,0.00005923911,0.00024249373,0.0000059384774],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014258354,0.000026933523,0.000005321045,0.00037870425,0.000010785337,0.000017143333,0.00047829756,0.0011077557,0.99583465,0.00003428828,0.000025898884,0.0019376497],"study_design_scores_gemma":[0.0003767599,0.00006784773,0.000014084157,0.0009920492,0.000022956823,0.00004738078,0.00008013369,0.003785521,0.98600554,0.000003597928,0.0084491735,0.00015497312],"about_ca_topic_score_codex":0.0000059238414,"about_ca_topic_score_gemma":0.000013292421,"teacher_disagreement_score":0.009829117,"about_ca_system_score_codex":0.00026189027,"about_ca_system_score_gemma":0.0006959091,"threshold_uncertainty_score":0.44788966},"labels":[],"label_agreement":null},{"id":"W4393306178","doi":"10.1016/j.mcat.2024.114091","title":"Monoethanolamine assisted CO2 hydrogenation to methanol – A computational study","year":2024,"lang":"en","type":"article","venue":"Molecular Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"European Regional Development Fund","keywords":"Methanol; Catalysis; Chemistry; Environmental science; Organic chemistry; Waste management; Engineering","score_opus":0.012458164549149,"score_gpt":0.27406731627059105,"score_spread":0.26160915172144206,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4393306178","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.88503796,0.00044452233,0.11264807,0.00022389626,0.00012055252,0.0004400391,0.000022278384,0.00048248254,0.00058019],"genre_scores_gemma":[0.9966661,8.027753e-7,0.0019166557,0.000057599853,0.0000611738,0.0001620274,0.00043306488,0.00008492114,0.00061765226],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99792695,0.00004803115,0.00042976526,0.0006039703,0.0006651829,0.00032609908],"domain_scores_gemma":[0.99912405,0.0000914312,0.00004465557,0.00046094542,0.000100907855,0.00017801228],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00037607306,0.00027456525,0.000350407,0.00066002045,0.00005596475,0.00007604288,0.00027799845,0.000090633774,0.00007289354],"category_scores_gemma":[0.0002018909,0.0002683008,0.00028415344,0.0018748621,0.000017432727,0.00016289817,0.00017057403,0.00021491718,0.00041589706],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000013722038,0.00019872496,0.000069977534,0.000077396035,0.0010561784,0.00040344027,0.00095487986,0.04017784,0.9399888,0.00030522325,0.000029779674,0.016724043],"study_design_scores_gemma":[0.00045668473,0.00009281147,0.00021843682,0.00006484578,0.00063528673,0.000076259625,0.00027780395,0.18431364,0.81190693,0.00013958335,0.0012949741,0.0005227411],"about_ca_topic_score_codex":0.00022190285,"about_ca_topic_score_gemma":0.000025576339,"teacher_disagreement_score":0.1441358,"about_ca_system_score_codex":0.00031255855,"about_ca_system_score_gemma":0.000043976826,"threshold_uncertainty_score":0.99997693},"labels":[],"label_agreement":null},{"id":"W4393853623","doi":"10.1016/j.ijhydene.2024.03.174","title":"Performance assessment of a novel porous catalytic reactor with a hydrogen-selective membrane for enhanced methane dry reforming process – CFD investigation","year":2024,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":26,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Memorial University of Newfoundland","funders":"","keywords":"Carbon dioxide reforming; Methane; Membrane reactor; Hydrogen; Catalysis; Porosity; Methane reformer; Chemical engineering; Process (computing); Membrane; Computational fluid dynamics; Hydrogen production; Dry gas; Chemistry; Materials science; Steam reforming; Environmental science; Chromatography; Syngas; Computer science; Thermodynamics; Engineering; Organic chemistry; Physics","score_opus":0.013006668261871636,"score_gpt":0.2792809208384063,"score_spread":0.26627425257653464,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4393853623","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9840924,0.00025901574,0.014594169,0.00008583076,0.00029867818,0.00012346408,0.000034146753,0.000045686822,0.00046656694],"genre_scores_gemma":[0.99685764,0.00004935691,0.0023212417,0.000024189909,0.00039218325,0.000045035842,0.0000820664,0.00006825449,0.000160008],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99770564,0.000013572186,0.00084479986,0.00026519794,0.0009031263,0.00026769278],"domain_scores_gemma":[0.9982309,0.00017345783,0.00060229463,0.0001518989,0.00071142014,0.00013005643],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004834603,0.00025221947,0.00043412598,0.0005397825,0.000025684834,0.000022282124,0.0004675269,0.00010218709,0.000008549229],"category_scores_gemma":[0.00013927705,0.00019483428,0.00021061976,0.00039242595,0.000061298444,0.0006904934,0.000049684975,0.00026908956,6.200621e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021804371,0.0000865436,0.00005920688,0.00022794041,0.0011261262,0.000031453157,0.0005825901,0.020456865,0.97133553,0.0005931833,8.3777763e-7,0.0052816705],"study_design_scores_gemma":[0.0010565296,0.0002453785,0.000012364997,0.00077824085,0.00015835639,0.0005954252,0.00009106115,0.10772086,0.8888653,0.00009614896,0.00017907312,0.00020125786],"about_ca_topic_score_codex":0.00013412154,"about_ca_topic_score_gemma":0.000033037144,"teacher_disagreement_score":0.087263994,"about_ca_system_score_codex":0.0006783515,"about_ca_system_score_gemma":0.0005337982,"threshold_uncertainty_score":0.7945112},"labels":[],"label_agreement":null},{"id":"W4394803106","doi":"10.1016/j.ijhydene.2024.03.286","title":"Reformation of CO2 to dimethyl ether using hydrogen produced by methane pyrolysis in molten metals: Lifecycle and technoeconomic analyses","year":2024,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada; Lakehead University","keywords":"Dimethyl ether; Tonne; Diesel fuel; Gallon (US); Syngas; Natural gas; Waste management; Refining (metallurgy); Methane; Pyrolysis; Fischer–Tropsch process; Pulp and paper industry; Environmental science; Chemistry; Catalysis; Engineering; Organic chemistry","score_opus":0.020261283516416623,"score_gpt":0.30713209195806124,"score_spread":0.2868708084416446,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4394803106","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99395305,0.0034907642,0.0020440503,0.00016570833,0.00015319008,0.0000492893,0.000021814709,0.000023645838,0.00009850211],"genre_scores_gemma":[0.9987617,0.000098142445,0.00085410575,0.000027038472,0.0001329162,0.0000053605213,0.000012993604,0.000037459366,0.00007028631],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99827176,0.000039174556,0.00090004224,0.00020192249,0.00041329567,0.00017378095],"domain_scores_gemma":[0.99919957,0.0000919325,0.00031517658,0.00015033934,0.0001368809,0.00010608907],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006773315,0.00017316363,0.0004250924,0.0010687003,0.00001086151,0.000026110905,0.00035359478,0.00009462087,0.000035061297],"category_scores_gemma":[0.00019574421,0.00014613647,0.00020624623,0.00039360608,0.000034050474,0.0005385276,0.0001222691,0.00017992765,0.0000026990797],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004323724,0.00003092887,0.00011036826,0.000021746133,0.0008803877,0.000026524933,0.00019341212,0.05331708,0.94091254,0.00016120741,0.0000059052268,0.004296675],"study_design_scores_gemma":[0.00027407779,0.000030680418,0.000009319417,0.00018282076,0.00012749352,0.00013802953,0.000057892496,0.069543935,0.9284768,0.00028584452,0.00073501415,0.00013805603],"about_ca_topic_score_codex":0.00084103044,"about_ca_topic_score_gemma":0.000028915152,"teacher_disagreement_score":0.016226854,"about_ca_system_score_codex":0.00034895458,"about_ca_system_score_gemma":0.000051804305,"threshold_uncertainty_score":0.59592724},"labels":[],"label_agreement":null},{"id":"W4396552700","doi":"10.31031/pps.2024.06.000632","title":"Towards Sustainable Fuels from Fischer-Tropsch Synthesis","year":2024,"lang":"en","type":"article","venue":"Progress in Petrochemical Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"","keywords":"Fischer–Tropsch process; Chemistry; Environmental science; Organic chemistry; Catalysis","score_opus":0.0096138727044986,"score_gpt":0.2758539298986508,"score_spread":0.2662400571941522,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4396552700","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98458546,0.006731423,0.00079677143,0.00043074499,0.00025674686,0.00016990815,0.0000123954,0.00047926244,0.006537262],"genre_scores_gemma":[0.9953253,0.000025902562,0.0038861693,0.000013382411,0.00019737706,0.00014788462,0.000007240001,0.000034735873,0.00036196498],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9969705,0.000014165474,0.00036069736,0.00080313283,0.00081921404,0.0010323332],"domain_scores_gemma":[0.9989489,0.00024784583,0.000036545025,0.00041996315,0.00008366483,0.00026308268],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00073345227,0.00024248911,0.00029339932,0.00029537172,0.000084194195,0.00019842187,0.0009886675,0.00013596367,0.00023305115],"category_scores_gemma":[0.001337498,0.00020245215,0.000113545255,0.0021525915,0.00058277725,0.0007225796,0.0005750934,0.00052774575,0.00008567854],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000025513711,0.000089311296,0.0025485468,0.00037901223,0.000026543243,0.0002964265,0.00049309974,0.000012940683,0.8761985,0.0069321105,0.000029538463,0.11296848],"study_design_scores_gemma":[0.00010397785,0.0000105560575,0.0002799202,0.00026850853,0.000019999397,0.000015439362,0.00020573453,0.014038539,0.9794845,0.001636069,0.0036199042,0.0003168336],"about_ca_topic_score_codex":0.00019681631,"about_ca_topic_score_gemma":0.0000027770516,"teacher_disagreement_score":0.112651646,"about_ca_system_score_codex":0.0008363441,"about_ca_system_score_gemma":0.0002161582,"threshold_uncertainty_score":0.82557595},"labels":[],"label_agreement":null},{"id":"W4396574493","doi":"10.1126/science.adl1260","title":"An active, stable cubic molybdenum carbide catalyst for the high-temperature reverse water-gas shift reaction","year":2024,"lang":"en","type":"article","venue":"Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":218,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Water-gas shift reaction; Catalysis; Carbide; Carbon dioxide; Molybdenum; Active carbon; Chemistry; Water gas; Materials science; Inorganic chemistry; Metallurgy; Organic chemistry; Syngas; Environmental science","score_opus":0.009100158166746045,"score_gpt":0.2573556085782114,"score_spread":0.24825545041146535,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4396574493","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9974219,0.00018469788,0.00022307615,0.00049486046,0.0010470442,0.0002578325,0.00004249718,0.00021963746,0.00010842169],"genre_scores_gemma":[0.9984975,0.000013268175,0.00011597482,0.000029695555,0.00027036347,0.000055050234,0.000048206617,0.00002891806,0.00094104663],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99846905,0.000009122863,0.00016167252,0.0004742306,0.0004002018,0.00048570015],"domain_scores_gemma":[0.99916214,0.00009325028,0.000024264955,0.0005340356,0.00006524475,0.000121064855],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007427261,0.00015310141,0.0001371935,0.00014290273,0.00026803653,0.0001518744,0.00053122937,0.000074376454,0.000020663212],"category_scores_gemma":[0.00012406531,0.000089301066,0.00007833424,0.0006593767,0.00016298737,0.0012301926,0.0000903057,0.00030411463,0.00005423784],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000011507048,0.000008725892,0.0000017518938,0.000054162327,0.000012394181,0.000005641033,0.00086937926,0.0003328481,0.99652225,0.00045637795,0.000025139243,0.0016998536],"study_design_scores_gemma":[0.000091025155,0.00002031617,0.000043673717,0.000050825172,0.000038237242,0.00002149148,0.00028176742,0.0044025662,0.98696554,0.00021521977,0.007718388,0.00015097266],"about_ca_topic_score_codex":0.00071282306,"about_ca_topic_score_gemma":0.00008334417,"teacher_disagreement_score":0.009556702,"about_ca_system_score_codex":0.00035291567,"about_ca_system_score_gemma":0.00011073714,"threshold_uncertainty_score":0.36415917},"labels":[],"label_agreement":null},{"id":"W4396605409","doi":"10.1021/acs.iecr.3c04276","title":"Preparation and Evaluation of Resistance Coke Formation Catalysts in Combined Reforming of Methane Using Steam and Oxygen for the Production of Synthesis Gas","year":2024,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"University of Kashan","keywords":"Coke; Steam reforming; Methane; Catalysis; Syngas; Oxygen; Methane reformer; Chemistry; Ammonia production; Chemical engineering; Waste management; Hydrogen production; Environmental science; Organic chemistry; Engineering","score_opus":0.12051900296923788,"score_gpt":0.38177410206689355,"score_spread":0.26125509909765565,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4396605409","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9974552,0.0015722835,0.000083639265,0.0000514981,0.00008139973,0.0006849761,0.000020426987,0.000019755835,0.00003086149],"genre_scores_gemma":[0.99956983,0.000054933662,0.0000658838,6.411401e-8,0.00011439316,0.0001105345,0.000019044344,0.000022334902,0.000042958305],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983428,0.000044399723,0.0005580608,0.00022370498,0.00061954453,0.0002114754],"domain_scores_gemma":[0.9983736,0.0009002915,0.0001176074,0.00024309831,0.000327966,0.000037413767],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0048656636,0.00011889733,0.00027410022,0.0002086699,0.000028351804,0.000011438242,0.00011690721,0.00016567024,0.0000024395324],"category_scores_gemma":[0.0048278053,0.000101841586,0.00004696558,0.0006230757,0.00007357625,0.00026318894,0.000067303576,0.00029941666,5.155426e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017479021,0.000013632067,0.0000150390615,0.0020344777,0.00005895638,2.7625154e-7,0.00055773964,0.010423562,0.9821065,0.000024153704,0.000004005313,0.0045868834],"study_design_scores_gemma":[0.00031678617,0.0000158145,0.000015418052,0.001090519,0.00007656522,0.0000066155967,0.00027962792,0.218564,0.77952236,0.000021266347,0.000025283925,0.00006573809],"about_ca_topic_score_codex":0.00018077834,"about_ca_topic_score_gemma":0.000012364641,"teacher_disagreement_score":0.20814045,"about_ca_system_score_codex":0.00032551857,"about_ca_system_score_gemma":0.00013136241,"threshold_uncertainty_score":0.57796824},"labels":[],"label_agreement":null},{"id":"W4396724585","doi":"10.1016/j.enconman.2024.118227","title":"Enhanced syngas production from CO2 reforming of biomass-derived glycerol: Influence of CaO.Al2O3 support composition on the catalytic performance of Ni-based catalysts","year":2024,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"University of Kashan","keywords":"Syngas; Catalysis; Glycerol; Composition (language); Chemical engineering; Biomass (ecology); Syngas to gasoline plus; Chemistry; Materials science; Steam reforming; Hydrogen production; Organic chemistry; Engineering; Geology","score_opus":0.007141677561974926,"score_gpt":0.205507841006499,"score_spread":0.19836616344452407,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4396724585","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99854547,0.00009447236,0.00034080472,0.00011286863,0.00019026978,0.0001588802,0.000012755666,0.00004906024,0.0004954288],"genre_scores_gemma":[0.99925905,0.0001166377,0.00005373957,0.000023410063,0.000019475721,0.000018516204,0.00013618899,0.000017690692,0.00035529857],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99887276,0.00001758785,0.00037634332,0.00027409248,0.0003095478,0.00014964791],"domain_scores_gemma":[0.99933225,0.000059007925,0.00016696898,0.00034301617,0.00005862634,0.00004011796],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00019314744,0.00015724746,0.00024144497,0.00018946873,0.00007193249,0.000008633753,0.00015579515,0.000047817713,0.00001931241],"category_scores_gemma":[0.00001533999,0.000117749696,0.00007423887,0.00029283948,0.00010203173,0.00015715686,0.00010929815,0.00007992848,0.0000053277327],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015137596,0.000040373972,0.000023014332,0.0011755797,0.00014960078,0.000005418733,0.00021984025,0.0025183079,0.99246514,0.000501131,0.00003462262,0.0027156095],"study_design_scores_gemma":[0.0003284799,0.00009685319,0.0002118294,0.0007496274,0.00011522991,0.0000020696398,0.00015822881,0.009873671,0.9880181,0.0000074513605,0.00032131287,0.00011713599],"about_ca_topic_score_codex":0.0010810995,"about_ca_topic_score_gemma":0.000016350568,"teacher_disagreement_score":0.007355363,"about_ca_system_score_codex":0.00010480954,"about_ca_system_score_gemma":0.000019940766,"threshold_uncertainty_score":0.48016933},"labels":[],"label_agreement":null},{"id":"W4396767721","doi":"10.1016/j.cej.2024.152052","title":"Sorption-enhanced intensified CO2 hydrogenation via reverse water–gas shift reaction: Kinetics and modelling","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":27,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Water-gas shift reaction; Sorption; Kinetics; Chemistry; Chemical engineering; Chemical kinetics; Catalysis; Environmental science; Organic chemistry; Adsorption; Engineering; Physics","score_opus":0.011199856354995215,"score_gpt":0.21140227484244672,"score_spread":0.20020241848745152,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4396767721","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.53697515,0.00048489188,0.4613172,0.00020014231,0.0005734503,0.00006024922,0.0000019829702,0.00030311648,0.00008383009],"genre_scores_gemma":[0.99487156,0.00009917027,0.0039989697,0.000016818465,0.0007967437,0.000007897359,0.000032816708,0.000085211985,0.00009081074],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984634,0.0000065264135,0.00048537127,0.0003015575,0.0003075514,0.00043562576],"domain_scores_gemma":[0.9993578,0.00008282696,0.000043958687,0.00017081625,0.00008188849,0.00026267904],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025434137,0.0002757385,0.00028132732,0.00021719908,0.000042176034,0.00009166257,0.0001382691,0.00020611963,0.00003519187],"category_scores_gemma":[0.0001121477,0.00023123794,0.00015350856,0.00020230758,0.000031154537,0.00036582217,0.00007450274,0.0009579698,0.00003919751],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000139496715,0.000012223494,2.658659e-7,0.00016497461,0.00007342575,0.00003636581,0.00041757245,0.061463118,0.93529063,0.00012444734,0.000011432468,0.002391582],"study_design_scores_gemma":[0.00015795417,0.000008942832,2.7494232e-7,0.00019678129,0.000041286658,0.0005500531,0.000010859862,0.44329563,0.55435294,0.00022924435,0.0009776496,0.00017838925],"about_ca_topic_score_codex":0.000007123802,"about_ca_topic_score_gemma":1.1858754e-7,"teacher_disagreement_score":0.4578964,"about_ca_system_score_codex":0.0003308465,"about_ca_system_score_gemma":0.00001370969,"threshold_uncertainty_score":0.942961},"labels":[],"label_agreement":null},{"id":"W4397030606","doi":"10.1021/acscatal.4c00742","title":"Phosphorization-Induced “Fence Effect” on the Active Hydrogen Species Migration Enables Tunable CO<sub>2</sub> Hydrogenation Selectivity","year":2024,"lang":"en","type":"article","venue":"ACS Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"National Postdoctoral Program for Innovative Talents; Higher Education Discipline Innovation Project; Collaborative Innovation Center of Suzhou Nano Science and Technology; Soochow University; China Postdoctoral Science Foundation; National Natural Science Foundation of China","keywords":"Catalysis; Selectivity; Methanation; Chemistry; Fence (mathematics); Hydrogen; Adsorption; Chemical engineering; Photochemistry; Combinatorial chemistry; Organic chemistry","score_opus":0.010092310614976067,"score_gpt":0.22458254190599095,"score_spread":0.21449023129101488,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4397030606","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99691445,0.00018811594,0.00072573766,0.00032553042,0.00015075307,0.00040226348,0.00003581335,0.00038333435,0.000874014],"genre_scores_gemma":[0.99859506,0.00005521963,0.000007531152,0.0000359779,0.00021541718,0.00019090644,0.00047577432,0.000068792324,0.00035535046],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979784,0.000085925436,0.00032815576,0.0005809698,0.0006128608,0.00041367087],"domain_scores_gemma":[0.9982378,0.00093499845,0.00011218246,0.00053053966,0.000095712196,0.00008878539],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005990056,0.00034484066,0.00033967913,0.0002806581,0.00026353355,0.00011945891,0.00029869645,0.00017157024,0.000033735123],"category_scores_gemma":[0.00081466953,0.00025485366,0.00024488205,0.0017054738,0.000049861585,0.00061548635,0.00007372603,0.00039974786,0.00029962845],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002477554,0.000031332187,0.00006261847,0.00007366283,0.0003300087,0.000009132181,0.0007368146,0.000986546,0.9870619,0.000562802,0.00008045061,0.010039937],"study_design_scores_gemma":[0.000119858894,0.00006399524,0.000056625366,0.00008152041,0.00023378231,0.000011604983,0.00008773492,0.016400304,0.9816741,0.00013128346,0.00084841135,0.0002908191],"about_ca_topic_score_codex":0.00020634636,"about_ca_topic_score_gemma":0.00011602624,"teacher_disagreement_score":0.015413758,"about_ca_system_score_codex":0.0006576961,"about_ca_system_score_gemma":0.000070051006,"threshold_uncertainty_score":0.99999034},"labels":[],"label_agreement":null},{"id":"W4399058437","doi":"10.2139/ssrn.4843402","title":"The Thermodynamic Assessment and Numerical Optimization for Sustainable Production of Syngas from Pyrolytic Bio-Oil","year":2024,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Syngas; Pyrolytic carbon; Production (economics); Petroleum engineering; Process engineering; Biochemical engineering; Environmental science; Pyrolysis; Waste management; Chemistry; Economics; Engineering; Catalysis; Organic chemistry; Microeconomics","score_opus":0.005557433927908746,"score_gpt":0.2530144936549534,"score_spread":0.24745705972704463,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4399058437","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.65077734,0.02680886,0.31763467,0.0019075307,0.0014714332,0.0008196733,0.000021815144,0.0001681423,0.00039052742],"genre_scores_gemma":[0.9918174,0.004171323,0.00074651476,0.0000028025638,0.00057935173,0.00008026463,0.00006530113,0.00009350865,0.0024435057],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.997469,0.000045355315,0.00050782575,0.00037648878,0.00029753303,0.0013038068],"domain_scores_gemma":[0.9989285,0.00016332146,0.0003310088,0.00032101147,0.00019710918,0.00005908139],"candidate_categories":["research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0016590265,0.00026854762,0.00036657735,0.00013581863,0.00018235248,0.000094251714,0.0002958398,0.00020564087,0.0000043269642],"category_scores_gemma":[0.0002620032,0.00018940402,0.00022307411,0.000152903,0.00005365643,0.000093267365,0.00036026468,0.0029099875,7.4376044e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00050864066,0.00022010777,0.00006626074,0.0026929583,0.005315731,0.000014671717,0.0007811213,0.49766606,0.08733732,0.21406366,0.000039958417,0.19129351],"study_design_scores_gemma":[0.00041794527,0.00012179416,0.00000975174,0.00032857186,0.0006146884,0.00015441874,0.0018527553,0.7064822,0.0049471394,0.2845481,0.00017564882,0.00034704342],"about_ca_topic_score_codex":0.00022354178,"about_ca_topic_score_gemma":0.00002869032,"teacher_disagreement_score":0.34104007,"about_ca_system_score_codex":0.003184188,"about_ca_system_score_gemma":0.0018894653,"threshold_uncertainty_score":0.99939036},"labels":[],"label_agreement":null},{"id":"W4399564366","doi":"10.1016/j.cej.2024.153011","title":"Solar-driven gasification for syngas production at low temperatures using a rotary hybrid porous media reactor","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Fondo Nacional de Desarrollo Científico y Tecnológico; Natural Sciences and Engineering Research Council of Canada; Science and Engineering Research Council; Agencia Nacional de Investigación y Desarrollo; Agenția Națională pentru Cercetare și Dezvoltare","keywords":"Syngas; Porous medium; Chemical engineering; Process engineering; Materials science; Production (economics); Waste management; Porosity; Environmental science; Catalysis; Chemistry; Engineering; Organic chemistry; Composite material","score_opus":0.013869244513959062,"score_gpt":0.23345783101782627,"score_spread":0.2195885865038672,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4399564366","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.955851,0.0015987628,0.03947015,0.00014885048,0.0021221212,0.00026644007,0.0000339955,0.000499991,0.0000086522205],"genre_scores_gemma":[0.9816028,0.000046244557,0.014471825,0.000010393056,0.00342886,0.000037569236,0.000141407,0.00016769471,0.00009323334],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980594,0.000008974249,0.000551878,0.0004410426,0.00037796373,0.00056072575],"domain_scores_gemma":[0.99903965,0.00018811715,0.0000879382,0.0002778876,0.0001207294,0.00028568445],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003429034,0.00034468688,0.0003553221,0.00024820268,0.00009249589,0.000104217856,0.00024652432,0.000138069,0.000029469302],"category_scores_gemma":[0.0011388586,0.00031583966,0.00028657794,0.00027381716,0.000031114756,0.0004212814,0.00007815003,0.00091370207,0.0000141994105],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003690604,0.000024063349,0.0000075810194,0.00047201855,0.000115958916,0.00007611255,0.00019696474,0.01246381,0.985373,0.00003648095,0.00023746934,0.0009595998],"study_design_scores_gemma":[0.00021120766,0.000010965995,0.0000051202046,0.0006241394,0.0000913679,0.004167293,0.000013556031,0.19294967,0.800418,0.000025598458,0.0011691481,0.00031390207],"about_ca_topic_score_codex":0.0000041714825,"about_ca_topic_score_gemma":1.9127793e-7,"teacher_disagreement_score":0.18495502,"about_ca_system_score_codex":0.0010868986,"about_ca_system_score_gemma":0.000075469376,"threshold_uncertainty_score":0.99992937},"labels":[],"label_agreement":null},{"id":"W4399730521","doi":"10.1016/j.surfin.2024.104643","title":"MgO/Ni nanocomposite and its PVP-modified derivative for catalytic CO2 methanation and photocatalytic hydrogen production","year":2024,"lang":"en","type":"article","venue":"Surfaces and Interfaces","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":29,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Materials science; Catalysis; Methanation; Polyvinylpyrrolidone; Nanocomposite; Hydrogen production; Fourier transform infrared spectroscopy; Photocatalysis; Thermogravimetry; Nuclear chemistry; Hydrogen; Chemical engineering; Organic chemistry; Nanotechnology; Chemistry; Polymer chemistry","score_opus":0.02049814506621274,"score_gpt":0.2722728581377741,"score_spread":0.25177471307156135,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4399730521","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.986231,0.012098471,0.00021600258,0.00025552727,0.00024125385,0.00063658593,0.000039279967,0.00013454842,0.00014727608],"genre_scores_gemma":[0.9980158,0.00039437434,0.00014595556,0.000008502591,0.00006269238,0.000061215076,0.000046480916,0.000039001403,0.0012259436],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988604,0.000014345965,0.0002649726,0.0004913028,0.00012918613,0.00023979107],"domain_scores_gemma":[0.9995365,0.00014387167,0.000059668582,0.00011651516,0.00005841685,0.00008503841],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00028912007,0.00023218432,0.00027635178,0.00013463802,0.00009669711,0.00008712016,0.000076322474,0.000091697155,0.0000054596508],"category_scores_gemma":[0.00012378428,0.00019449253,0.0000376666,0.00017611339,0.00007423113,0.00052589085,0.000104285384,0.00013788213,0.0000053327162],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004903758,0.000010932695,0.000031437306,0.0008954262,0.00017022439,0.0000015551295,0.0015750587,0.00027639957,0.99239886,0.00034027235,0.000017999408,0.0042328164],"study_design_scores_gemma":[0.00022561701,0.00007762255,0.000043865028,0.00026734176,0.00010459541,0.000045850593,0.00026013696,0.11378337,0.8839589,0.00023889469,0.00076626014,0.00022756396],"about_ca_topic_score_codex":0.00012985652,"about_ca_topic_score_gemma":0.000033241482,"teacher_disagreement_score":0.113506965,"about_ca_system_score_codex":0.00006464786,"about_ca_system_score_gemma":0.000016120666,"threshold_uncertainty_score":0.7931175},"labels":[],"label_agreement":null},{"id":"W4400179057","doi":"10.1627/jpi.67.136","title":"Improvement of Liquid Hydrocarbon Yield in CO&lt;sub&gt;2&lt;/sub&gt; Fischer–Tropsch Synthesis over Potassium-added Iron Carbide Catalyst","year":2024,"lang":"en","type":"article","venue":"Journal of the Japan Petroleum Institute","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Hokkaido University; Canadian Institute for Theoretical Astrophysics","keywords":"Chemistry","score_opus":0.009635422828723511,"score_gpt":0.2269186116860765,"score_spread":0.21728318885735298,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400179057","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9934377,0.0015639794,0.00008316542,0.00045169817,0.0019743047,0.00018616319,0.000053363572,0.000062978484,0.0021866683],"genre_scores_gemma":[0.9984617,0.0001884429,0.00007647853,0.00005663935,0.0006271148,0.000023088878,0.00000857177,0.000098157805,0.0004597856],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9960876,0.00006131198,0.0016414616,0.00040919037,0.0011401881,0.0006602075],"domain_scores_gemma":[0.9978762,0.00028484286,0.00071569555,0.00078480795,0.00009284973,0.00024555894],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012372121,0.0005077667,0.0009821564,0.00068067736,0.000081345686,0.000060267434,0.0010063077,0.00026858694,0.000041682226],"category_scores_gemma":[0.0008094794,0.00036812705,0.00083909096,0.00065332616,0.00015926207,0.0006754254,0.00031087513,0.0012786265,0.00001891228],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002883643,0.00012014879,0.00015391536,0.0004985115,0.00037771146,0.000119745666,0.00031835033,0.0057076253,0.9905905,0.0001504707,0.0002265934,0.0014480549],"study_design_scores_gemma":[0.00073474087,0.00022105548,0.00032518277,0.0017774358,0.000455151,0.00026318812,0.000071240705,0.0062581417,0.98354965,0.000021325657,0.0059112892,0.00041158],"about_ca_topic_score_codex":0.0003221714,"about_ca_topic_score_gemma":0.00033273431,"teacher_disagreement_score":0.007040839,"about_ca_system_score_codex":0.001139816,"about_ca_system_score_gemma":0.00032248115,"threshold_uncertainty_score":0.9998771},"labels":[],"label_agreement":null},{"id":"W4400188877","doi":"10.1016/j.cej.2024.153636","title":"Rhodium-doped iron oxides promoted by sodium for highly selective hydrogenation of CO2 to ethanol and C2+ hydrocarbons","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Coprecipitation; Rhodium; Chemistry; Inorganic chemistry; Chemisorption; Physisorption; Selectivity; Bifunctional; Adsorption; Organic chemistry","score_opus":0.006778872676251444,"score_gpt":0.22780507332986016,"score_spread":0.22102620065360873,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400188877","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.83317024,0.0013428833,0.16416667,0.0002789785,0.00028157752,0.0003609672,0.000038088376,0.00028766753,0.00007289796],"genre_scores_gemma":[0.9919024,0.000020073156,0.0075292555,0.000011915368,0.00024547076,0.000049304454,0.000026969563,0.00009862602,0.000115947274],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99844486,0.000007734364,0.00049373694,0.0003202117,0.00028632098,0.00044712587],"domain_scores_gemma":[0.99916655,0.00023673703,0.00007141009,0.00014028237,0.00007453571,0.000310508],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003163571,0.00028399096,0.0003824096,0.0002568952,0.00003741804,0.000050286206,0.00019169012,0.00019618089,0.0000052256855],"category_scores_gemma":[0.000493327,0.00026651318,0.00016575742,0.00041529525,0.000028343764,0.00019866244,0.00005570485,0.00055897865,0.0000036404358],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003618606,0.000025346351,0.0000021829972,0.000375903,0.00011915563,0.0000063876687,0.00030406503,0.0013335141,0.9954976,0.00010041317,0.00014752898,0.0020517048],"study_design_scores_gemma":[0.00041430627,0.00006153856,0.0000013847815,0.00030304634,0.00007799866,0.00020383773,0.00001246099,0.13304938,0.8648332,0.00008622303,0.0006932687,0.00026339808],"about_ca_topic_score_codex":0.000008058399,"about_ca_topic_score_gemma":1.5738676e-7,"teacher_disagreement_score":0.15873218,"about_ca_system_score_codex":0.00031458985,"about_ca_system_score_gemma":0.000049782935,"threshold_uncertainty_score":0.9999787},"labels":[],"label_agreement":null},{"id":"W4400248251","doi":"10.1038/s44296-024-00016-w","title":"A short review on green H2 production by aqueous phase reforming of biomass derivatives","year":2024,"lang":"en","type":"review","venue":"npj Materials Sustainability","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada; China Scholarship Council","keywords":"Hydrogen production; Catalysis; Environmentally friendly; Steam reforming; Biomass (ecology); Fossil fuel; Hydrogen; Materials science; Environmental science; Waste management; Chemical engineering; Chemistry; Organic chemistry; Engineering","score_opus":0.03152996797555832,"score_gpt":0.36787127375912093,"score_spread":0.3363413057835626,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400248251","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0065445434,0.98814833,0.000019559871,0.00013354239,0.000629864,0.0035665964,0.0005461601,0.0003395803,0.00007181708],"genre_scores_gemma":[0.001956832,0.99483836,0.000030434552,0.000010072995,0.00038528652,0.0007944863,0.00096849335,0.00021596804,0.000800041],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99488556,0.00032533697,0.0023233104,0.0012240784,0.000556756,0.0006849274],"domain_scores_gemma":[0.9972343,0.00013140411,0.0006079647,0.0015092246,0.0003623963,0.00015471454],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002128589,0.0009835669,0.0038532997,0.00033283094,0.00006983446,0.000032291286,0.0005661354,0.00049960066,0.00009393143],"category_scores_gemma":[0.0021626458,0.0007014703,0.00076027453,0.00091449136,0.00018045102,0.00024356946,0.00039251492,0.0005107723,0.000031613836],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000025121706,0.00014694849,5.646647e-8,0.4745699,0.00019412115,0.000022956374,0.0000578256,8.13729e-8,0.013596896,0.000034184934,0.0001618279,0.5111901],"study_design_scores_gemma":[0.0001533992,0.0001587303,6.451035e-8,0.08326278,0.002359332,0.00012424396,0.000055722398,0.000002159384,0.19530137,0.00023557659,0.7174448,0.00090182835],"about_ca_topic_score_codex":0.0004163335,"about_ca_topic_score_gemma":0.0000026500074,"teacher_disagreement_score":0.71728295,"about_ca_system_score_codex":0.002579479,"about_ca_system_score_gemma":0.0003596294,"threshold_uncertainty_score":0.99954367},"labels":[],"label_agreement":null},{"id":"W4400296588","doi":"10.1002/bbb.2659","title":"Dry reforming of methane at high temperature and elevated pressure over nickel spinellized powder catalyst and pellets prepared from a metallurgical residue","year":2024,"lang":"en","type":"article","venue":"Biofuels Bioproducts and Biorefining","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Pellets; Nickel; Methane; Residue (chemistry); Metallurgy; Materials science; Catalysis; Carbon dioxide reforming; Pellet; High pressure; Waste management; Chemistry; Syngas; Composite material; Engineering; Organic chemistry","score_opus":0.00946051864805421,"score_gpt":0.23126759721878826,"score_spread":0.22180707857073403,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400296588","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9565433,0.042244356,0.0000034529405,0.00022657902,0.00021695768,0.00024838018,0.00027694294,0.00018652988,0.000053469168],"genre_scores_gemma":[0.9952842,0.001029654,0.0010242645,0.000022338476,0.00027451038,0.000012725247,0.00034101334,0.000077450066,0.0019338359],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99742043,0.000040697614,0.0006188205,0.0011104844,0.00034757014,0.00046197267],"domain_scores_gemma":[0.99893296,0.00012618602,0.00015282704,0.0004906064,0.000076348864,0.00022106506],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00044888625,0.00047842966,0.0007719921,0.00024930484,0.000098221026,0.00007838211,0.00015563409,0.00039389834,0.00007955704],"category_scores_gemma":[0.00023513375,0.00034092684,0.000101401645,0.0004913184,0.00023292143,0.00031417637,0.0004891397,0.00039223826,0.0000048840366],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018193093,0.000023782652,0.00039219143,0.0007703366,0.0004665854,0.000050432096,0.0007132183,0.0000029878754,0.9945765,0.00017936928,0.000012187787,0.0026304913],"study_design_scores_gemma":[0.0010526876,0.00007909636,0.0014583279,0.0006402123,0.00047676894,0.00007805299,0.00014275938,0.0009175418,0.98924375,0.00009367621,0.0052823476,0.00053476536],"about_ca_topic_score_codex":0.0017643783,"about_ca_topic_score_gemma":0.000051287105,"teacher_disagreement_score":0.041214705,"about_ca_system_score_codex":0.000050980325,"about_ca_system_score_gemma":0.0000402253,"threshold_uncertainty_score":0.9999043},"labels":[],"label_agreement":null},{"id":"W4400477882","doi":"10.1016/j.ceramint.2024.07.087","title":"Highly pure hydrogen production via the thermocatalytic decomposition of methane over Ni/SiO2.MgO catalysts: Impact of the catalyst's chemical composition","year":2024,"lang":"en","type":"article","venue":"Ceramics International","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"University of Kashan","keywords":"Catalysis; Methane; Decomposition; Materials science; Hydrogen; Hydrogen production; Chemical composition; Composition (language); Chemical engineering; Organic chemistry; Chemistry","score_opus":0.00792723220240647,"score_gpt":0.2766972426211463,"score_spread":0.2687700104187398,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400477882","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99652755,0.00033476806,0.00059742795,0.00041888366,0.0010263599,0.0002900245,0.00013837502,0.000081675695,0.0005849084],"genre_scores_gemma":[0.9985666,0.00001431109,0.000049144743,0.000012409067,0.0004014236,0.00002407208,0.0006689346,0.00004836132,0.00021469458],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981725,0.000039185437,0.00058626634,0.00034700907,0.00063704175,0.00021797366],"domain_scores_gemma":[0.99885803,0.00013332714,0.00023580945,0.0005356852,0.00018579424,0.000051337476],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003344369,0.00024360514,0.00027480835,0.00016992491,0.000047347447,0.000025412217,0.00068283884,0.0001414775,0.00004752348],"category_scores_gemma":[0.000095802294,0.00015060304,0.00048932905,0.00048497878,0.00018506647,0.0003063396,0.0002141243,0.00041948812,0.0000135469],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000058443835,0.00009462868,0.00019043965,0.00010107075,0.0006127153,0.0000028226766,0.0004333059,0.0019810686,0.9937173,0.001264945,0.000055067983,0.001488152],"study_design_scores_gemma":[0.000253151,0.000016208976,0.00051716046,0.00021659165,0.00017588015,0.0002446529,0.000025977894,0.04579951,0.95189816,0.0006413558,0.0000514062,0.00015993266],"about_ca_topic_score_codex":0.0005850415,"about_ca_topic_score_gemma":0.000011985431,"teacher_disagreement_score":0.04381844,"about_ca_system_score_codex":0.00079187687,"about_ca_system_score_gemma":0.000094469426,"threshold_uncertainty_score":0.61414135},"labels":[],"label_agreement":null},{"id":"W4400612552","doi":"10.1016/j.enconman.2024.118749","title":"CO2 reforming of biodiesel-waste glycerol on nanostructure Ni-SiO2.MgO catalysts for syngas production: Influence of the catalyst chemical composition","year":2024,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Syngas; Catalysis; Biodiesel production; Glycerol; Biodiesel; Chemical engineering; Transesterification; Materials science; Composition (language); Waste management; Catalytic reforming; Chemistry; Organic chemistry; Engineering","score_opus":0.005578610225409335,"score_gpt":0.20749141907477545,"score_spread":0.2019128088493661,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400612552","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99795717,0.00029507186,0.00011726678,0.0003551851,0.00052672887,0.00027712333,0.000024161045,0.000060565057,0.00038672923],"genre_scores_gemma":[0.99876416,0.000091965085,0.00009158896,0.000039214185,0.00006688537,0.000030141953,0.000072554896,0.000019628187,0.000823865],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989094,0.000011560904,0.0003078301,0.0003217645,0.00027356585,0.00017588325],"domain_scores_gemma":[0.99940735,0.00003701681,0.0001076937,0.00034135956,0.0000572071,0.00004935691],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012857442,0.00017274175,0.00022592185,0.0001468515,0.00007279922,0.000009163622,0.0001899663,0.0000693928,0.0000037813631],"category_scores_gemma":[0.000025022124,0.00012127698,0.00012121982,0.0002890672,0.00009772845,0.00012646218,0.00022353529,0.00010152684,0.0000014837766],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013249755,0.000028010763,0.000010757067,0.0019965163,0.0002091997,0.0000053732065,0.00025649572,0.0013739789,0.98508185,0.005933734,0.0004989601,0.0044726473],"study_design_scores_gemma":[0.00035763445,0.000030742805,0.000019516692,0.00066175254,0.00013155238,0.000017654384,0.0002037178,0.001377375,0.98972976,0.00004541494,0.00728999,0.00013486373],"about_ca_topic_score_codex":0.00012196414,"about_ca_topic_score_gemma":0.000005749687,"teacher_disagreement_score":0.0067910296,"about_ca_system_score_codex":0.0001195608,"about_ca_system_score_gemma":0.0000120567365,"threshold_uncertainty_score":0.49455318},"labels":[],"label_agreement":null},{"id":"W4400644652","doi":"10.1016/j.cep.2024.109899","title":"Syngas production via microwave-assisted Dry Reforming of Methane over NiFe/MgAl2O4 alloy catalyst","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering and Processing - Process Intensification","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Carbon dioxide reforming; Methane; Catalysis; Alloy; Methane reformer; Materials science; Syngas to gasoline plus; Microwave; Steam reforming; Chemical engineering; Metallurgy; Waste management; Chemistry; Hydrogen production; Organic chemistry; Engineering","score_opus":0.013420509393605088,"score_gpt":0.2548659142710003,"score_spread":0.24144540487739521,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400644652","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97577053,0.0051729674,0.017263353,0.00014799056,0.0003978444,0.0002463832,0.000008846903,0.0008615973,0.0001304976],"genre_scores_gemma":[0.99699587,0.00004797433,0.0021122757,0.000013157814,0.00028364497,0.000068971385,0.00016203213,0.00012268142,0.00019338762],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99760336,0.000010034072,0.0007786106,0.0007576191,0.00039661527,0.0004537789],"domain_scores_gemma":[0.99882895,0.00008856687,0.00018462894,0.00036068552,0.00036582554,0.0001713315],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00047972545,0.00041913538,0.0005159666,0.0003550548,0.000058795307,0.00005625894,0.00024520096,0.0002577771,0.000006825643],"category_scores_gemma":[0.00086223613,0.0003851812,0.00013175835,0.0009631478,0.00012047471,0.0006296544,0.00007851745,0.0006308309,0.000006726311],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003378913,0.000036085865,0.00002018135,0.005021908,0.00008027962,0.0000063284774,0.0011738363,0.00044670032,0.9383475,0.00006878887,0.0000046280156,0.054759942],"study_design_scores_gemma":[0.00016349049,0.000014419448,0.00002518516,0.0015758591,0.00013835033,0.00022849106,0.00019152144,0.13786599,0.8590651,0.00007346081,0.00026329412,0.0003948108],"about_ca_topic_score_codex":0.000049387923,"about_ca_topic_score_gemma":0.0000013596878,"teacher_disagreement_score":0.1374193,"about_ca_system_score_codex":0.00022825353,"about_ca_system_score_gemma":0.00008518795,"threshold_uncertainty_score":0.99986},"labels":[],"label_agreement":null},{"id":"W4401114703","doi":"10.1016/j.mtcomm.2024.109999","title":"Nickel nanocatalyst on lanthanum aluminate: Optimizing preparation and evaluating performance in glycerol dry reforming for syngas production","year":2024,"lang":"en","type":"article","venue":"Materials Today Communications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"University of Kashan","keywords":"Syngas; Materials science; Carbon dioxide reforming; Nickel; Lanthanum; Aluminate; Glycerol; Chemical engineering; Catalysis; Metallurgy; Inorganic chemistry; Organic chemistry","score_opus":0.039215537770488314,"score_gpt":0.3323010602118832,"score_spread":0.2930855224413949,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4401114703","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99657416,0.00068809214,0.0002363121,0.00049093453,0.0004391136,0.00080437295,0.000035394718,0.00024860326,0.00048302728],"genre_scores_gemma":[0.9925172,0.00031346912,0.005388896,0.000011148189,0.00013188043,0.00064789056,0.00042679405,0.000058815924,0.0005039586],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984832,0.000075217264,0.0005914182,0.00037660668,0.00017661287,0.00029696026],"domain_scores_gemma":[0.9985704,0.00023186317,0.000117658885,0.00096990063,0.00006489178,0.00004529001],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0014849207,0.0002081251,0.0002806349,0.00025433474,0.00024517227,0.000093204304,0.0003501061,0.00009928972,0.0000115560515],"category_scores_gemma":[0.00038804015,0.00019561966,0.000048876613,0.00027578895,0.000062529994,0.00056656124,0.0002458733,0.00020269646,0.00002414629],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000087833636,0.00003823839,0.000021818782,0.0005614504,0.000031405503,6.835079e-7,0.00146553,0.0010610429,0.9867096,0.00072163966,0.000007044194,0.009293746],"study_design_scores_gemma":[0.0002983612,0.00009830817,0.000060052127,0.0011377445,0.000055887558,0.000027703707,0.00027333538,0.07590095,0.9207978,0.00008826757,0.0010087963,0.00025277774],"about_ca_topic_score_codex":0.00011698798,"about_ca_topic_score_gemma":0.000056910867,"teacher_disagreement_score":0.07483991,"about_ca_system_score_codex":0.00032846496,"about_ca_system_score_gemma":0.000050220773,"threshold_uncertainty_score":0.7977138},"labels":[],"label_agreement":null},{"id":"W4401344672","doi":"10.1088/1742-6596/2798/1/012053","title":"The road to carbon neutrality in the metallurgical industry: Hydrogen metallurgy processes represented by hydrogen-rich coke oven gas, short-process metallurgy of scrap and low-carbon policy","year":2024,"lang":"en","type":"article","venue":"Journal of Physics Conference Series","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dalhousie University","funders":"Qingdao University; Qingdao University of Science and Technology; Dalhousie University","keywords":"Scrap; Metallurgy; Hydrogen; Carbon fibers; Materials science; Coke; Chemistry; Composite material","score_opus":0.021352662288398837,"score_gpt":0.2889643291931696,"score_spread":0.2676116669047708,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4401344672","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99483544,0.0021344954,0.000120203666,0.0018784999,0.000077351906,0.00025008345,0.00001838721,0.00003312532,0.0006524027],"genre_scores_gemma":[0.9991232,0.00035983612,0.000012718845,0.000030283074,0.00025746663,0.000029982873,0.000009245042,0.000043373395,0.00013387931],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9972013,0.00015571211,0.0009763894,0.0003510476,0.000834293,0.00048125527],"domain_scores_gemma":[0.9984106,0.00032439225,0.0003021466,0.00041798205,0.0003560783,0.0001888041],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010534019,0.00038004312,0.00078864157,0.00018577513,0.00007321145,0.00014229245,0.000780241,0.00020395417,0.000006371223],"category_scores_gemma":[0.0005972615,0.00022933613,0.00020146635,0.001538986,0.0002677411,0.00055032404,0.00018404864,0.0011014944,5.3320207e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00049757207,0.00037209774,0.00035837817,0.0016542667,0.0022574314,0.00019914417,0.011135322,0.005744792,0.94130844,0.012235014,0.000016471604,0.024221046],"study_design_scores_gemma":[0.00029152964,0.00017109401,0.00007399441,0.0004203429,0.00027372438,0.00022465874,0.0026024578,0.007360094,0.9834375,0.004115086,0.0007003426,0.00032920166],"about_ca_topic_score_codex":0.0005065533,"about_ca_topic_score_gemma":0.00009845025,"teacher_disagreement_score":0.04212901,"about_ca_system_score_codex":0.00009682557,"about_ca_system_score_gemma":0.00048113902,"threshold_uncertainty_score":0.9352056},"labels":[],"label_agreement":null},{"id":"W4401537550","doi":"10.1016/j.jece.2024.113829","title":"Eco-techno-economic assessment of methanol production: A comparative study of GHG mitigation strategies through CCS and electrified CCU pathways","year":2024,"lang":"en","type":"article","venue":"Journal of environmental chemical engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Concordia University","funders":"Natural Sciences and Engineering Research Council of Canada; Natural Resources Canada; Environment and Climate Change Canada","keywords":"Greenhouse gas; Production (economics); Environmental science; Waste management; Natural resource economics; Business; Engineering; Economics","score_opus":0.014395746762691772,"score_gpt":0.26228428141749144,"score_spread":0.24788853465479965,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4401537550","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9963421,0.0007576658,0.0023808621,0.000014506021,0.0001587059,0.000197082,0.00001236789,0.00003439315,0.00010229884],"genre_scores_gemma":[0.99715126,0.00006702895,0.0025903427,7.1342765e-7,0.00013666679,0.0000096950125,0.0000059489744,0.000030652387,0.0000077140785],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985074,0.00001230049,0.0007865544,0.0002143861,0.0003004683,0.00017891187],"domain_scores_gemma":[0.9994177,0.00010740413,0.00024587326,0.00015062833,0.000012388377,0.00006600273],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002442376,0.00021816797,0.00052672066,0.00015480115,0.000014762171,0.00001559572,0.00014268099,0.000094958734,0.000023743047],"category_scores_gemma":[0.000024744118,0.00019917959,0.00013234341,0.00013691817,0.000055584227,0.00049915013,0.00006595474,0.00046248798,8.3526044e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017809305,0.00016768595,0.000059578757,0.00022288715,0.00028969915,0.000008705598,0.0010645762,0.033424232,0.9641381,0.0002731484,0.0000016385809,0.0003319612],"study_design_scores_gemma":[0.0005031195,0.00024236557,0.00019899252,0.0002036002,0.00012241471,0.0001325021,0.0017811434,0.03519653,0.96132255,0.0000876273,0.000036613215,0.00017255786],"about_ca_topic_score_codex":0.000007910305,"about_ca_topic_score_gemma":3.315022e-7,"teacher_disagreement_score":0.0028155448,"about_ca_system_score_codex":0.00040454662,"about_ca_system_score_gemma":0.00003688962,"threshold_uncertainty_score":0.81223077},"labels":[],"label_agreement":null},{"id":"W4401979731","doi":"10.1016/j.ijhydene.2024.08.422","title":"Steam reforming of dodecane using Ni-red mud catalyst: A sustainable approach for hydrogen production","year":2024,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Hydrogen production; Steam reforming; Catalysis; Hydrogen; Production (economics); Environmental science; Red mud; Methane reformer; Waste management; Chemistry; Materials science; Chemical engineering; Metallurgy; Engineering; Organic chemistry; Economics","score_opus":0.014687408822361686,"score_gpt":0.26426264846959363,"score_spread":0.24957523964723194,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4401979731","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97485375,0.0027390309,0.020726306,0.000113704504,0.0008607136,0.00013548494,0.00002432065,0.00005517576,0.00049149536],"genre_scores_gemma":[0.9948676,0.000053831216,0.002065086,0.000009943316,0.0012489322,0.0000144235455,0.00007926132,0.0000712557,0.0015896573],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99773824,0.000021507753,0.0009271983,0.00026720855,0.00071029586,0.00033555765],"domain_scores_gemma":[0.9985305,0.000054659326,0.00043679427,0.00020403418,0.000665793,0.000108201464],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006849638,0.00021660779,0.0003973151,0.0007216413,0.00004569515,0.00002605293,0.0005254514,0.00011340333,0.000014717404],"category_scores_gemma":[0.0002703351,0.00018668854,0.00040062444,0.00035680644,0.00004375668,0.0007091251,0.00012909668,0.00020351143,7.093046e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017710651,0.00010240687,0.000018273036,0.00027244206,0.0011972308,0.00010743937,0.0003425793,0.0864899,0.9017068,0.0023896443,0.00003188679,0.007164304],"study_design_scores_gemma":[0.0004389029,0.00005935189,5.621135e-7,0.0002314979,0.00016320476,0.0017102474,0.00038739596,0.086880095,0.90180147,0.0005672012,0.00757394,0.00018614082],"about_ca_topic_score_codex":0.00050458394,"about_ca_topic_score_gemma":0.00000838691,"teacher_disagreement_score":0.02001384,"about_ca_system_score_codex":0.00084239594,"about_ca_system_score_gemma":0.00021670942,"threshold_uncertainty_score":0.7612938},"labels":[],"label_agreement":null},{"id":"W4402175439","doi":"10.1016/j.joei.2024.101821","title":"Ceria-boosted Ni/Al2O3 catalysts for enhanced H2 production via acetic acid dry reforming","year":2024,"lang":"en","type":"article","venue":"Journal of the Energy Institute","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"King Saud University","keywords":"Catalysis; Coke; Yield (engineering); Acetic acid; Chemistry; Stoichiometry; Adsorption; Dispersion (optics); Carbon dioxide reforming; Metal; Nuclear chemistry; Inorganic chemistry; Syngas; Chemical engineering; Materials science; Organic chemistry; Metallurgy","score_opus":0.011545243916773,"score_gpt":0.24500376634143203,"score_spread":0.23345852242465903,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402175439","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9232706,0.0029792527,0.049483,0.0014123188,0.021317475,0.00028090205,0.000014874842,0.00021024553,0.0010313626],"genre_scores_gemma":[0.9936395,0.000068896996,0.0009008105,0.00003697182,0.0021833724,0.00002155336,0.000015557887,0.000059860497,0.0030734567],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982749,0.000021111315,0.000706928,0.00024180497,0.00040696785,0.00034825256],"domain_scores_gemma":[0.99895006,0.000037021884,0.00031895,0.0004092259,0.00017222048,0.000112495116],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004998134,0.00024358103,0.0003715359,0.00024676666,0.00014605754,0.000037508347,0.0004974412,0.00014252526,0.000006188286],"category_scores_gemma":[0.00045666436,0.00015690451,0.00042796676,0.00050706416,0.00007203821,0.0008785791,0.0001294182,0.00040866382,0.000006727416],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007334132,0.000021039714,0.0000013705029,0.00017418388,0.00024250979,0.000018083536,0.0002780085,0.0030169864,0.969647,0.00064033316,0.00013268528,0.025754461],"study_design_scores_gemma":[0.00034286495,0.000041968575,0.000005056071,0.0006513816,0.00019232508,0.00049799815,0.000038103746,0.0019162273,0.96308136,0.00037222294,0.032662068,0.00019840532],"about_ca_topic_score_codex":0.000092968316,"about_ca_topic_score_gemma":0.00009068618,"teacher_disagreement_score":0.07036895,"about_ca_system_score_codex":0.00060457975,"about_ca_system_score_gemma":0.00016291821,"threshold_uncertainty_score":0.63983804},"labels":[],"label_agreement":null},{"id":"W4402326856","doi":"10.1016/j.apcata.2024.119945","title":"Reforming of methane over two-dimensional Mo2C-Ni/γ-Al2O3 catalyst","year":2024,"lang":"en","type":"article","venue":"Applied Catalysis A General","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Catalysis; Methane; Heterogeneous catalysis; Methane reformer; Chemical engineering; Steam reforming; Organic chemistry; Hydrogen production","score_opus":0.00984744384214547,"score_gpt":0.2621037014217436,"score_spread":0.25225625757959813,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402326856","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9904586,0.0021263817,0.00055618444,0.000052948824,0.00042184847,0.00024677173,0.00008016217,0.00039987767,0.0056572347],"genre_scores_gemma":[0.9937934,0.0000120018485,0.00162084,0.00007035561,0.0006022398,0.00009967998,0.0010643799,0.00014592572,0.0025911427],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9965721,0.000020055091,0.00096611085,0.00085014425,0.0008678705,0.00072375935],"domain_scores_gemma":[0.9984079,0.0001293864,0.00017490149,0.00096599315,0.00007468694,0.00024714266],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006639129,0.0005091711,0.00085829635,0.0005905587,0.00006605386,0.000033767697,0.0004961546,0.00021156874,0.00031348676],"category_scores_gemma":[0.00005545383,0.00043795304,0.0005521544,0.0013944583,0.000117640615,0.00028501885,0.00039090053,0.0004895208,0.00023112427],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003929651,0.00005187032,0.000019053814,0.00021490398,0.00067558425,0.000040110754,0.00035495087,0.0048875487,0.97372496,0.0060435436,0.0001756975,0.0137725],"study_design_scores_gemma":[0.00066731987,0.000017034943,0.000020078278,0.00008028476,0.0005158093,0.00007776309,0.000064654225,0.027020115,0.96758276,0.000342658,0.0030461517,0.0005653674],"about_ca_topic_score_codex":0.0017844747,"about_ca_topic_score_gemma":0.00008946798,"teacher_disagreement_score":0.022132566,"about_ca_system_score_codex":0.00037394202,"about_ca_system_score_gemma":0.00012034001,"threshold_uncertainty_score":0.99980724},"labels":[],"label_agreement":null},{"id":"W4402393723","doi":"10.1016/j.apcatb.2024.124591","title":"Rare earth oxide promoted Ru/Al2O3 dual function materials for CO2 capture and methanation: An operando DRIFTS and TGA study","year":2024,"lang":"en","type":"article","venue":"Applied Catalysis B: Environmental","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Mitacs; Consejo Nacional de Ciencia y Tecnología","keywords":"Methanation; Rare earth; Oxide; Dual function; Earth (classical element); Materials science; Dual (grammatical number); Chemical engineering; Inorganic chemistry; Chemistry; Catalysis; Metallurgy; Physics; Organic chemistry; Computer science","score_opus":0.007607914562307312,"score_gpt":0.2160283894948766,"score_spread":0.2084204749325693,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402393723","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9970587,0.0004598063,0.00076933054,0.000025750704,0.00009861202,0.0011585102,0.00019035193,0.0001633999,0.00007555546],"genre_scores_gemma":[0.99705714,0.000021786074,0.00030140206,0.000021745798,0.00014338427,0.0004057077,0.0016171884,0.00008617446,0.0003454708],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981743,0.00002795536,0.00038938786,0.00072373304,0.00038148477,0.00030311188],"domain_scores_gemma":[0.99937266,0.00007030105,0.000064700376,0.00032756125,0.000007084038,0.00015768618],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00049525,0.00034009732,0.0004388046,0.0001560602,0.00014319022,0.00010973227,0.0000977099,0.00015337973,0.00012417226],"category_scores_gemma":[0.000016514345,0.00030319227,0.00007299939,0.00015106975,0.000073340205,0.00035247998,0.00014509106,0.0001697751,0.000021352935],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013374288,0.00012552066,0.000093522016,0.00010228563,0.00036994807,0.000013497219,0.001376877,0.000051857915,0.99281037,0.00014125575,0.000007667487,0.004773428],"study_design_scores_gemma":[0.0023506435,0.00016235746,0.0014766149,0.000024707993,0.0010146182,0.000073899566,0.00320309,0.0013918339,0.9883381,0.000061940016,0.0013458179,0.00055634725],"about_ca_topic_score_codex":0.00009503683,"about_ca_topic_score_gemma":0.000033947927,"teacher_disagreement_score":0.004472268,"about_ca_system_score_codex":0.0001456369,"about_ca_system_score_gemma":0.000011805768,"threshold_uncertainty_score":0.999942},"labels":[],"label_agreement":null},{"id":"W4402439024","doi":"10.11159/htff24.275","title":"Impact of Static Liquid Height on Hydrodynamics of the Thermolysis Reactor in the Cu-Cl Cycle for Hydrogen Production","year":2024,"lang":"en","type":"article","venue":"Proceedings of the World Congress on Mechanical, Chemical, and Material Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Hydrogen production; Hydrogen; Thermal decomposition; Production (economics); Liquid hydrogen; Nuclear engineering; Thermal; Decomposition; Materials science; Environmental science; Chemical reactor; Waste management; Process engineering; Chemical engineering; Chemistry; Thermodynamics; Engineering; Physics; Organic chemistry","score_opus":0.0070360488067748896,"score_gpt":0.23625100016066009,"score_spread":0.2292149513538852,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402439024","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9985892,0.000025444457,0.0000021805733,0.00018626296,0.00049408065,0.00053634774,0.000058705442,0.000052164858,0.00005557784],"genre_scores_gemma":[0.99953663,0.000020430267,0.00010053312,0.0000066463876,0.00014838963,0.00008076702,0.0000046469713,0.0000583938,0.000043548847],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99853766,0.000007698356,0.0005400087,0.00031330227,0.0003205031,0.00028083145],"domain_scores_gemma":[0.9992149,0.00019045325,0.00020224613,0.00027866152,0.00006912479,0.000044620156],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00043021288,0.0002683958,0.00043372423,0.00014466215,0.000030137595,0.000026422353,0.00054602715,0.00010043976,0.000007186748],"category_scores_gemma":[0.00039094297,0.00014361968,0.00030320496,0.0005072968,0.00006809408,0.000118742144,0.0001510011,0.00028143733,2.9060567e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028835487,0.00006948352,0.0000030997378,0.0008741768,0.000121191435,2.3492446e-7,0.000069127185,0.0013310977,0.9938273,0.0032390635,0.000016452017,0.00016044301],"study_design_scores_gemma":[0.00023308516,0.000107513166,0.0000051707157,0.001067059,0.00010709112,0.000007973276,0.000030848627,0.041078284,0.9568518,0.0003100089,0.00005123712,0.00014994705],"about_ca_topic_score_codex":0.0000308716,"about_ca_topic_score_gemma":0.0000019327406,"teacher_disagreement_score":0.039747186,"about_ca_system_score_codex":0.0001250437,"about_ca_system_score_gemma":0.000020830166,"threshold_uncertainty_score":0.58566403},"labels":[],"label_agreement":null},{"id":"W4402469789","doi":"10.1016/j.cep.2024.109995","title":"Intensified processes for CO2 capture and valorization by catalytic conversion","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering and Processing - Process Intensification","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Catalysis; Environmental science; Process engineering; Waste management; Chemistry; Engineering; Organic chemistry","score_opus":0.011482121420087185,"score_gpt":0.24061486257471387,"score_spread":0.22913274115462667,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402469789","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6838478,0.026349628,0.28512806,0.0011469425,0.00047705983,0.0008198532,0.000095671465,0.0020101303,0.00012487732],"genre_scores_gemma":[0.99806476,0.000103510465,0.0008199344,0.000047778944,0.00013652477,0.00012039991,0.00045190883,0.00009073239,0.00016443811],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985429,0.0000032191601,0.00035537285,0.0006030331,0.00016923745,0.0003262577],"domain_scores_gemma":[0.99901515,0.0001858423,0.00007156808,0.00013755845,0.00043500913,0.00015489502],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001858905,0.0003127237,0.00030187416,0.00014742617,0.00008494929,0.00014233383,0.00012339278,0.00024121038,0.0000017420298],"category_scores_gemma":[0.0012654903,0.00028678987,0.00004199995,0.00047584905,0.0000859958,0.00046782393,0.00003926462,0.0003126813,0.0000023370606],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004489221,0.000020456806,0.0000261869,0.014187596,0.000045076333,0.0000015514463,0.0014095749,0.00022038214,0.96945846,0.00026988648,0.00017643959,0.014139491],"study_design_scores_gemma":[0.00025906297,0.00001768359,0.000004219697,0.0009456198,0.00010260937,0.00008069781,0.00025063774,0.38150322,0.6145272,0.00015753311,0.0017895473,0.00036192697],"about_ca_topic_score_codex":0.00001233438,"about_ca_topic_score_gemma":1.5857468e-7,"teacher_disagreement_score":0.38128287,"about_ca_system_score_codex":0.000106096144,"about_ca_system_score_gemma":0.000075740936,"threshold_uncertainty_score":0.9999584},"labels":[],"label_agreement":null},{"id":"W4402609328","doi":"10.59277/rrst-ee.2024.69.3.17","title":"SIMULATION OF BIOMASS CARBONIZATION AND HEAT RECOVERY FOR ELECTRICITY PRODUCTION USING SEEBECK MODULES","year":2024,"lang":"en","type":"article","venue":"REVUE ROUMAINE DES SCIENCES TECHNIQUES — SÉRIE ÉLECTROTECHNIQUE ET ÉNERGÉTIQUE","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Agence Universitaire de la Francophonie","keywords":"Carbonization; Biomass (ecology); Production (economics); Materials science; Electricity; Process engineering; Thermoelectric generator; Environmental science; Electricity generation; Thermoelectric effect; Waste management; Chemical engineering; Power (physics); Electrical engineering; Thermodynamics; Economics; Composite material; Engineering; Physics","score_opus":0.03751310922816648,"score_gpt":0.324096540976834,"score_spread":0.2865834317486675,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402609328","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.3254039,0.0007689635,0.6714475,0.00014939293,0.00006446205,0.0010090945,0.000013141734,0.0009991938,0.00014432457],"genre_scores_gemma":[0.8985892,0.0003281475,0.10050082,0.000013502759,0.000167988,0.00020236392,0.000032264605,0.00007510071,0.00009061012],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99774855,0.00010123115,0.00063054595,0.0007622412,0.00027212017,0.00048528667],"domain_scores_gemma":[0.99887323,0.0003444929,0.00016233737,0.00031118796,0.00023070358,0.00007801707],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0020697757,0.00034270328,0.00045005785,0.00078180566,0.00025191906,0.00008413014,0.00025060473,0.00032805602,0.0000030035292],"category_scores_gemma":[0.00094930007,0.00032722348,0.00017870983,0.0019081843,0.00035323857,0.0009565438,0.000099034274,0.00033988396,2.0682882e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000032042655,0.000028532575,0.000022315216,0.0010823687,0.000026123083,0.0000021875412,0.00015791674,0.035590503,0.9484461,0.006998539,0.0000059240865,0.0076074447],"study_design_scores_gemma":[0.000035644258,0.00022967419,0.0000037666823,0.00056757696,0.000032189542,0.00006462982,0.000008539568,0.39565715,0.5893537,0.013704862,0.0001207092,0.00022159154],"about_ca_topic_score_codex":0.0005357398,"about_ca_topic_score_gemma":0.000056480185,"teacher_disagreement_score":0.5731853,"about_ca_system_score_codex":0.00079386006,"about_ca_system_score_gemma":0.00017341806,"threshold_uncertainty_score":0.999918},"labels":[],"label_agreement":null},{"id":"W4403083899","doi":"10.3390/fuels5040033","title":"Catalytic Performance of Hydroxyapatite-Based Supports: Tailored vs. Commercial Formulations for Dry Reforming of Methane","year":2024,"lang":"en","type":"article","venue":"Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Carbon dioxide reforming; Methane; Catalysis; Pulp and paper industry; Chemical engineering; Chemistry; Environmental science; Business; Syngas; Organic chemistry; Engineering","score_opus":0.016634539806124806,"score_gpt":0.2680222954069284,"score_spread":0.2513877556008036,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403083899","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98691404,0.00031735658,0.010767477,0.0000666638,0.00031050842,0.00044803647,0.00021069293,0.00014890876,0.0008163406],"genre_scores_gemma":[0.99664026,0.000008226309,0.0022694916,0.000013752834,0.000119527154,0.00007040183,0.00039642246,0.000060656177,0.0004212829],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99845195,0.000008475055,0.0006912223,0.00023463562,0.000278837,0.00033486699],"domain_scores_gemma":[0.99895924,0.00030707492,0.00015578685,0.00038701712,0.000108601285,0.000082276354],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00040269722,0.00019925783,0.00045097875,0.00032117686,0.000034615685,0.000007249563,0.00022241354,0.00012659865,0.000052053016],"category_scores_gemma":[0.00019601546,0.00017761756,0.00027859106,0.0004557728,0.0000632511,0.00041133203,0.000058433096,0.00016993072,0.000009796209],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00035799097,0.00014944443,0.0019952343,0.01209391,0.00034565508,0.000009747492,0.0016516611,0.005209828,0.90524143,0.002545724,0.000058055415,0.07034131],"study_design_scores_gemma":[0.0005030167,0.0001281575,0.00014164804,0.0004090464,0.00012069783,0.0000050803424,0.000026782156,0.14477028,0.8514282,0.00014873192,0.0021255857,0.00019278986],"about_ca_topic_score_codex":0.0001622495,"about_ca_topic_score_gemma":0.00002288694,"teacher_disagreement_score":0.13956045,"about_ca_system_score_codex":0.00015167841,"about_ca_system_score_gemma":0.00012478356,"threshold_uncertainty_score":0.7243034},"labels":[],"label_agreement":null},{"id":"W4403218319","doi":"10.1002/anie.202416899","title":"Highly Dispersed ZnO Sites in a ZnO/ZrO <sub>2</sub> Catalyst Promote Carbon Dioxide‐to‐Methanol Conversion","year":2024,"lang":"en","type":"article","venue":"Angewandte Chemie International Edition","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Chinese Government Scholarship; Newfoundland and Labrador; Central European Research Infrastructure Consortium; China Scholarship Council; Nederlandse Organisatie voor Wetenschappelijk Onderzoek; Universiteit Utrecht; Ministerstvo Školství, Mládeže a Tělovýchovy","keywords":"Catalysis; Monoclinic crystal system; Methanol; Tetragonal crystal system; Selectivity; Materials science; Formate; Dispersion (optics); Chemical engineering; Inorganic chemistry; Phase (matter); Chemistry; Crystallography; Crystal structure; Organic chemistry","score_opus":0.010110384901136507,"score_gpt":0.23968720694212514,"score_spread":0.22957682204098864,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403218319","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9928804,0.0002181661,0.00080093293,0.0009924421,0.0019380627,0.00030138154,0.00014750772,0.00036415426,0.002356967],"genre_scores_gemma":[0.9961167,0.000054072676,0.000091042755,0.00008498994,0.0014886983,0.00011545865,0.0015935506,0.00007301199,0.00038247078],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99787223,0.0000143763455,0.0004700655,0.0005956703,0.0006549676,0.00039271123],"domain_scores_gemma":[0.9992205,0.00014171099,0.000081032405,0.00025812862,0.00012791746,0.00017071315],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00029734342,0.00031398836,0.00029346973,0.0005488767,0.00003451165,0.000055997225,0.00031178497,0.00020695587,0.00007299121],"category_scores_gemma":[0.00035197218,0.00031200523,0.00019284633,0.0005995234,0.00004461923,0.00051595765,0.00016541869,0.00042743457,0.00016235301],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005492122,0.000057222172,0.00011258784,0.00017102109,0.00010537887,0.000113616865,0.00057012064,0.00009450429,0.9969472,0.00011166608,0.00035220347,0.0013095271],"study_design_scores_gemma":[0.0005194328,0.000029839424,0.000099775534,0.0005862942,0.00004834376,0.000045218647,0.00008527041,0.0056032273,0.9887576,0.00013612202,0.0037312184,0.00035767577],"about_ca_topic_score_codex":0.00029106424,"about_ca_topic_score_gemma":0.00007400152,"teacher_disagreement_score":0.008189648,"about_ca_system_score_codex":0.0010676131,"about_ca_system_score_gemma":0.000055614502,"threshold_uncertainty_score":0.9999332},"labels":[],"label_agreement":null},{"id":"W4403267708","doi":"10.1016/j.apcatb.2024.124683","title":"Highly active ternary Ir/In2O3-ZrO2 catalyst for CO2 hydrogenation towards methanol: The role of zirconia","year":2024,"lang":"en","type":"article","venue":"Applied Catalysis B: Environmental","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":29,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"Fundamental Research Funds for the Central Universities; National Key Research and Development Program of China","keywords":"Cubic zirconia; Ternary operation; Catalysis; Methanol; Materials science; Chemical engineering; Business; Inorganic chemistry; Chemistry; Organic chemistry; Computer science; Metallurgy; Engineering; Ceramic","score_opus":0.005345259859753262,"score_gpt":0.2080584519286886,"score_spread":0.20271319206893534,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403267708","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98942196,0.0020443262,0.0028497048,0.00013556505,0.00019634025,0.00096421,0.0006451094,0.00023464255,0.0035081536],"genre_scores_gemma":[0.9964119,0.00005405917,0.0003633419,0.000026215212,0.00021443612,0.0004954948,0.0018811397,0.00012266058,0.0004307448],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976584,0.000019188108,0.0005945172,0.0006656277,0.00059593766,0.00046637864],"domain_scores_gemma":[0.9987653,0.00022682562,0.00018265477,0.00069527124,0.000009190352,0.000120752695],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00035875576,0.00040817264,0.0005016957,0.00022063607,0.00012395505,0.00003186177,0.0005496637,0.00019470892,0.00010699915],"category_scores_gemma":[0.00002344097,0.0003212358,0.00049832126,0.0003579178,0.00019624883,0.0002581792,0.00028210797,0.0003160896,0.0001542808],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000060078222,0.0000852154,0.000021922913,0.000076132514,0.00083422667,0.0000040508617,0.0011296234,0.00041806954,0.9330538,0.0011926156,0.000016681335,0.06310762],"study_design_scores_gemma":[0.000411242,0.000029937695,0.00008321779,0.000022920374,0.0006938614,0.000026110292,0.0011522388,0.0092424825,0.97537374,0.0005238917,0.012083158,0.00035718505],"about_ca_topic_score_codex":0.00023245523,"about_ca_topic_score_gemma":0.000012898822,"teacher_disagreement_score":0.06275043,"about_ca_system_score_codex":0.0005966014,"about_ca_system_score_gemma":0.000035964233,"threshold_uncertainty_score":0.99992394},"labels":[],"label_agreement":null},{"id":"W4403311780","doi":"10.1016/j.jechem.2024.08.069","title":"Exploring catalyst developments in heterogeneous CO2 hydrogenation to methanol and ethanol: A journey through reaction pathways","year":2024,"lang":"en","type":"article","venue":"Journal of Energy Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":32,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Natural Resources Canada; Western University","funders":"Natural Resources Canada; Natural Sciences and Engineering Research Council of Canada; Western University","keywords":"Catalysis; Methanol; Ethanol; Chemistry; Chemical engineering; Organic chemistry; Engineering","score_opus":0.05550855364390575,"score_gpt":0.26094811580746957,"score_spread":0.20543956216356382,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403311780","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99605006,0.0013662118,0.00092368404,0.00008038394,0.0002997551,0.000030108482,0.0000037140253,0.00004881066,0.0011972928],"genre_scores_gemma":[0.99817985,0.00047026342,0.00078382535,0.00002299634,0.0002928268,0.000016349832,0.000013707501,0.000049728693,0.00017046208],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984369,0.000014354934,0.0006560448,0.00023949632,0.00037495227,0.000278213],"domain_scores_gemma":[0.9993615,0.00008074894,0.00016071108,0.00014426559,0.00008043679,0.00017230953],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035008363,0.00021130046,0.0003201474,0.00020349745,0.000030387942,0.000039577473,0.00016534088,0.0001292421,0.000008970012],"category_scores_gemma":[0.0001977095,0.0001956584,0.000120983736,0.00043688194,0.00001444586,0.00061694824,0.00008724355,0.00039235863,0.0000032198736],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002825995,0.000024172334,0.000014384435,0.00015849051,0.00011722105,0.00030037973,0.00081993465,0.0013138527,0.99049354,0.000029848847,0.000006181576,0.0066937264],"study_design_scores_gemma":[0.00028216734,0.000016714372,0.000010816724,0.0006007065,0.000036989666,0.0015741956,0.00011580895,0.00060016365,0.9911079,0.000087471766,0.005361381,0.00020569192],"about_ca_topic_score_codex":0.00007352009,"about_ca_topic_score_gemma":0.000007937563,"teacher_disagreement_score":0.0064880345,"about_ca_system_score_codex":0.0005780927,"about_ca_system_score_gemma":0.000093636714,"threshold_uncertainty_score":0.7978718},"labels":[],"label_agreement":null},{"id":"W4403633175","doi":"10.1016/j.cej.2024.156796","title":"Kinetics, catalyst design, and hydrodynamic analysis in Fischer–Tropsch synthesis: Fixed Bed vs Fluidized Bed Reactors","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Canada Research Chairs; Canada Foundation for Innovation","keywords":"Fischer–Tropsch process; Fluidized bed; Catalysis; Kinetics; Chemical engineering; Chemistry; Materials science; Organic chemistry; Engineering; Physics","score_opus":0.008010857203363872,"score_gpt":0.21606178574580873,"score_spread":0.20805092854244486,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403633175","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9469435,0.0026989463,0.049277358,0.00018295617,0.00029767017,0.00016664523,0.000013771481,0.00039297988,0.000026125208],"genre_scores_gemma":[0.98861057,0.00012822509,0.010722253,0.000008719607,0.00029123505,0.000034492634,0.00003665625,0.0001314625,0.000036417445],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99729604,0.000038152015,0.000903454,0.0005564533,0.00045248648,0.0007534251],"domain_scores_gemma":[0.99827117,0.0007695745,0.00009225171,0.00037294356,0.000055048367,0.00043902625],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00065897556,0.0005031907,0.0008890806,0.0010425639,0.00003892757,0.00015197125,0.0003918622,0.0003291101,0.0000724417],"category_scores_gemma":[0.0013847926,0.0004612077,0.00042522597,0.0016281037,0.00005426109,0.00031831543,0.00013988758,0.0013356935,0.000016159418],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000048731403,0.00003411924,0.00008974103,0.00020950739,0.0008215363,0.00020783146,0.00017183548,0.01634381,0.9810064,0.000025224734,0.000022143788,0.0010191213],"study_design_scores_gemma":[0.00033857688,0.000014477123,0.00003675421,0.00031965258,0.00058152806,0.00024582064,0.000014792798,0.37073076,0.6271651,0.000013172702,0.00014971597,0.0003897016],"about_ca_topic_score_codex":0.000043109212,"about_ca_topic_score_gemma":0.0000022230715,"teacher_disagreement_score":0.35438693,"about_ca_system_score_codex":0.0006152782,"about_ca_system_score_gemma":0.000041200954,"threshold_uncertainty_score":0.999784},"labels":[],"label_agreement":null},{"id":"W4403760434","doi":"10.1021/acs.energyfuels.4c03428","title":"Hydrogen Production from Methane Thermal Pyrolysis in a Microwave Heating-Assisted Fluidized Bed Reactor","year":2024,"lang":"en","type":"article","venue":"Energy & Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada; OCP Group","keywords":"Fluidized bed; Pyrolysis; Hydrogen production; Methane; Hydrogen; Waste management; Environmental science; Nuclear engineering; Materials science; Chemistry; Organic chemistry; Engineering","score_opus":0.012827477674211385,"score_gpt":0.23284200259904023,"score_spread":0.22001452492482884,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403760434","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.994465,0.003525782,0.00014245033,0.00017802353,0.00045960752,0.00010169516,0.000018536562,0.00044804392,0.0006608809],"genre_scores_gemma":[0.9974503,0.00004793784,0.0005528625,0.000029400528,0.00066386035,0.00008575953,0.000267906,0.00010218644,0.000799784],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980323,0.00007091,0.0005226028,0.0006346541,0.00030598303,0.00043360487],"domain_scores_gemma":[0.99914634,0.00016304127,0.00006881003,0.00047339627,0.00003383076,0.00011455024],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003206982,0.00030169904,0.00045498202,0.0003088022,0.00002641585,0.00003143433,0.00021011672,0.00020138871,0.00016288321],"category_scores_gemma":[0.00022890302,0.0002721131,0.0002533517,0.0007858435,0.000031634434,0.00026760323,0.000099454446,0.00031491637,0.000049291946],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000055866414,0.000042538846,0.000036208432,0.0000432346,0.00024395739,0.00006535838,0.0005269238,0.000053846743,0.9676565,0.000110813744,0.00001036437,0.031154402],"study_design_scores_gemma":[0.00039228876,0.000015069268,0.000046743862,0.0001880181,0.0001069415,0.000021168024,0.00005110775,0.0006320442,0.9960982,0.00020700636,0.0019390557,0.00030236228],"about_ca_topic_score_codex":0.0038331356,"about_ca_topic_score_gemma":0.0003109968,"teacher_disagreement_score":0.03085204,"about_ca_system_score_codex":0.0003516569,"about_ca_system_score_gemma":0.0000573859,"threshold_uncertainty_score":0.9999731},"labels":[],"label_agreement":null},{"id":"W4403924431","doi":"10.3390/molecules29215126","title":"Effect of the Reactor Material on the Reforming of Primary Syngas","year":2024,"lang":"en","type":"article","venue":"Molecules","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Syngas; Syngas to gasoline plus; Primary (astronomy); Waste management; Chemical engineering; Process engineering; Chemistry; Environmental science; Nuclear engineering; Steam reforming; Catalysis; Engineering; Organic chemistry; Physics; Hydrogen production","score_opus":0.006127523390892766,"score_gpt":0.21916435872586126,"score_spread":0.2130368353349685,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403924431","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99574476,0.00017591707,0.000025192492,0.0000871606,0.000317611,0.00014373503,0.00002233353,0.000050154707,0.0034331253],"genre_scores_gemma":[0.9996812,0.0000045366173,0.00001602859,0.000012843042,0.000074276286,0.00001255151,0.0000065134022,0.000027676959,0.00016439872],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992904,0.000045036202,0.00019809435,0.00011558664,0.0002196167,0.00013126417],"domain_scores_gemma":[0.9992827,0.00029603043,0.000050737493,0.00034283282,0.000010934458,0.000016772441],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034932862,0.00011183096,0.00018133645,0.000039642167,0.000019082112,0.000007196922,0.00024227386,0.000053296382,0.000022615775],"category_scores_gemma":[0.0002015533,0.000049442326,0.00015789243,0.00014865935,0.000050379513,0.00003550179,0.00011825314,0.0001513488,0.000008170422],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000036345635,0.000005306744,0.0000058863843,0.00045868213,0.00003973646,0.0000036090942,0.00010809572,0.000015082734,0.992129,0.0011919271,0.000016164344,0.005990121],"study_design_scores_gemma":[0.00006536249,0.0000559141,0.000030973322,0.00041857988,0.000038889735,0.00000908737,0.000008550955,0.00024085717,0.9982416,0.000035434154,0.0008001624,0.000054595697],"about_ca_topic_score_codex":0.00006834774,"about_ca_topic_score_gemma":0.0000010722249,"teacher_disagreement_score":0.00611255,"about_ca_system_score_codex":0.000075163,"about_ca_system_score_gemma":0.00001577759,"threshold_uncertainty_score":0.20161995},"labels":[],"label_agreement":null},{"id":"W4404021499","doi":"10.1016/j.rser.2024.115011","title":"Sustainability assessment of catalyst design on CO2-derived fuel production","year":2024,"lang":"en","type":"article","venue":"Renewable and Sustainable Energy Reviews","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; Polytechnique Montréal; National Research Council Canada","funders":"National Research Council Canada","keywords":"Sustainability; Production (economics); Catalysis; Business; Environmental science; Waste management; Engineering; Chemistry; Economics; Organic chemistry","score_opus":0.01907307230484465,"score_gpt":0.2819171929456186,"score_spread":0.26284412064077395,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404021499","genre_codex":"review","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.12692674,0.44421723,0.3866118,0.002783181,0.0017661251,0.006376809,0.000024386722,0.0016154597,0.029678274],"genre_scores_gemma":[0.95137054,0.012378875,0.00094575,0.000028998018,0.00022508035,0.00034727858,0.000060724415,0.00007546871,0.034567267],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.9976868,0.0001493671,0.00067808555,0.0006122105,0.0002666029,0.0006069117],"domain_scores_gemma":[0.99873006,0.0001545344,0.00013395856,0.0006127082,0.0002282081,0.00014051724],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0019229843,0.00032292938,0.00071713043,0.00027200032,0.00010781342,0.000047513888,0.00017081255,0.00013109487,0.00003263073],"category_scores_gemma":[0.00069256284,0.00025369116,0.00019738666,0.0008042141,0.0000784707,0.0003540592,0.00014008503,0.0001947624,0.0000022685285],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018580968,0.0006612021,0.00019069154,0.07179822,0.0006619926,0.0004612811,0.0013468323,0.1473797,0.48211676,0.13632973,0.005349543,0.15351826],"study_design_scores_gemma":[0.00038543728,0.00033008447,0.00002112597,0.0010916805,0.00026482076,0.00007086204,0.001739711,0.015548272,0.3385088,0.0066143433,0.6347097,0.00071511534],"about_ca_topic_score_codex":0.0020521067,"about_ca_topic_score_gemma":0.000028450593,"teacher_disagreement_score":0.8244438,"about_ca_system_score_codex":0.0007734589,"about_ca_system_score_gemma":0.00032063073,"threshold_uncertainty_score":0.99999154},"labels":[],"label_agreement":null},{"id":"W4404115306","doi":"10.1002/cctc.202400698","title":"Toward Carbon‐Negative Methanol Production from Biogas: Intensified Membrane Reactor","year":2024,"lang":"en","type":"article","venue":"ChemCatChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"Research Corporation for Science Advancement","keywords":"Biogas; Membrane reactor; Methanol; Biogas production; Carbon fibers; Production (economics); Waste management; Chemistry; Environmental science; Pulp and paper industry; Chemical engineering; Methane; Materials science; Catalysis; Organic chemistry; Anaerobic digestion; Engineering","score_opus":0.030210007926364118,"score_gpt":0.25248588748901624,"score_spread":0.22227587956265213,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404115306","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9896348,0.0012501681,0.00015392278,0.0010446629,0.0017172867,0.0002806679,0.000037149155,0.0012461734,0.004635141],"genre_scores_gemma":[0.995446,0.00005702461,0.0010876013,0.000032308333,0.0011145184,0.000070372225,0.00014964204,0.000115868126,0.0019266458],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99807316,0.00001620666,0.00039750536,0.0007501722,0.00034256428,0.00042039706],"domain_scores_gemma":[0.99887663,0.00021187353,0.0000696678,0.00056423375,0.00011720182,0.00016037325],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00022826283,0.00035363968,0.0004311616,0.00017063174,0.000024514164,0.00004007448,0.0002191706,0.00023506986,0.00012346795],"category_scores_gemma":[0.00089611753,0.00031118843,0.00021460402,0.0006607557,0.00007706829,0.00025691118,0.00013709237,0.0005804463,0.00018990359],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000029109133,0.00002438257,0.0000068454697,0.00013735483,0.00026144582,0.00004572601,0.0035806233,0.0000034127434,0.99242485,0.00018221249,0.000148965,0.0031550527],"study_design_scores_gemma":[0.0002046333,0.000010867433,0.000008847321,0.00025704797,0.00014134146,0.000040940253,0.0008577223,0.0012840268,0.99133575,0.00045097456,0.0050374786,0.000370387],"about_ca_topic_score_codex":0.0010973453,"about_ca_topic_score_gemma":0.000014499898,"teacher_disagreement_score":0.005811191,"about_ca_system_score_codex":0.00043959537,"about_ca_system_score_gemma":0.00006847773,"threshold_uncertainty_score":0.999934},"labels":[],"label_agreement":null},{"id":"W4404323437","doi":"10.2139/ssrn.5019565","title":"Mono (Cobalt) and Bimetallic (Fe and Co) Mof Nanocatalysts for Fischer-Tropsch Synthesis","year":2024,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Fischer–Tropsch process; Bimetallic strip; Cobalt; Nanomaterial-based catalyst; Chemistry; Chemical engineering; Materials science; Catalysis; Inorganic chemistry; Organic chemistry; Engineering; Selectivity","score_opus":0.012272604284470433,"score_gpt":0.26295269880509614,"score_spread":0.25068009452062573,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404323437","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92264956,0.06992029,0.004915808,0.000577311,0.0004650611,0.0006628017,0.00011263147,0.00022222205,0.00047433234],"genre_scores_gemma":[0.98420244,0.011491767,0.0006503774,0.000018399576,0.0007781418,0.00016062001,0.000057877052,0.00023268838,0.002407669],"study_design_codex":"bench_or_experimental","study_design_gemma":"theoretical_or_conceptual","domain_scores_codex":[0.99559546,0.000048110425,0.0007251278,0.0007843154,0.0003863842,0.0024605838],"domain_scores_gemma":[0.9985638,0.0003015661,0.00030757664,0.00045521432,0.00009402018,0.0002777905],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0019439686,0.00064580294,0.00091494736,0.00041498026,0.00017213117,0.00018387727,0.0004654715,0.0005516265,0.000012893122],"category_scores_gemma":[0.0004630335,0.0005648788,0.00044885,0.0001820476,0.000093266935,0.0001448241,0.0006768377,0.0050064716,0.000020304517],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00064265466,0.00025110468,0.00035575227,0.008299711,0.01481518,0.000109709574,0.0012497401,0.0007960849,0.5328583,0.09049018,0.00026910202,0.3498625],"study_design_scores_gemma":[0.0030338843,0.0005454633,0.000079821744,0.0031342383,0.005777037,0.008440722,0.0017302645,0.036972467,0.3864078,0.5383234,0.011376605,0.0041783233],"about_ca_topic_score_codex":0.00019325754,"about_ca_topic_score_gemma":0.00014442249,"teacher_disagreement_score":0.4478332,"about_ca_system_score_codex":0.0014745585,"about_ca_system_score_gemma":0.001202171,"threshold_uncertainty_score":0.9996803},"labels":[],"label_agreement":null},{"id":"W4404324061","doi":"10.1016/j.powtec.2024.120444","title":"Methane dry reforming in a microwave heating-assisted dense fluidized bed","year":2024,"lang":"en","type":"article","venue":"Powder Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada; Polytechnique Montréal","keywords":"Fluidized bed; Methane; Carbon dioxide reforming; Microwave; Microwave heating; Waste management; Materials science; Environmental science; Chemical engineering; Process engineering; Chemistry; Syngas; Engineering; Catalysis; Telecommunications; Organic chemistry","score_opus":0.013183928177480557,"score_gpt":0.2631433004709891,"score_spread":0.24995937229350854,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404324061","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99085,0.0043795346,0.0005968789,0.0008532806,0.00031531387,0.00024798763,0.0000065887034,0.0018597415,0.0008907235],"genre_scores_gemma":[0.99606913,0.00004234789,0.0030903344,0.000043112264,0.000075343196,0.00010549514,0.000029081348,0.00009997496,0.00044518316],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99788547,0.00002463013,0.0006007415,0.0005742055,0.00019639249,0.00071857066],"domain_scores_gemma":[0.99912053,0.00014925239,0.000057490346,0.00055148185,0.000041675954,0.00007958221],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00040854045,0.00031245258,0.00052411074,0.0013457405,0.000036992264,0.000019095309,0.00036223608,0.0005442868,0.000059039154],"category_scores_gemma":[0.000518975,0.00028622692,0.00015914696,0.0018669503,0.00010370139,0.00016496162,0.00027647178,0.0008933329,0.00016306767],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000021178745,0.00002847214,0.00019885086,0.00016446007,0.0000777144,0.00030529575,0.00027374402,0.0000026427058,0.9411936,0.0021573782,0.000009275379,0.055567384],"study_design_scores_gemma":[0.0006556831,0.00003153594,0.00001755855,0.00035004105,0.000044697354,0.00034814587,0.00033543102,0.002284396,0.9917416,0.0017873019,0.0020651934,0.00033839355],"about_ca_topic_score_codex":0.00031637523,"about_ca_topic_score_gemma":0.00017371411,"teacher_disagreement_score":0.05522899,"about_ca_system_score_codex":0.00052709586,"about_ca_system_score_gemma":0.00006852477,"threshold_uncertainty_score":0.999959},"labels":[],"label_agreement":null},{"id":"W4404404265","doi":"10.2139/ssrn.5022664","title":"Pilot Scale Study of Elevated Pressure Autothermal Dry Reforming of Methane Over Ni-Ugso Pellets","year":2024,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Pellets; Methane; Methane reformer; Environmental science; Scale (ratio); Materials science; Chemistry; Geography; Steam reforming; Catalysis; Hydrogen production; Composite material; Cartography","score_opus":0.010747097168720656,"score_gpt":0.2619429792408717,"score_spread":0.25119588207215104,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404404265","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98525727,0.011945357,0.00032753483,0.00003067364,0.0009114994,0.00062770187,0.00004090404,0.00014881065,0.00071026094],"genre_scores_gemma":[0.99307203,0.0006187815,0.00008435653,0.0000035914281,0.0005071895,0.000025398858,0.000025309471,0.00022215147,0.005441211],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9940646,0.00014807977,0.0016318203,0.0006636061,0.0011146159,0.00237723],"domain_scores_gemma":[0.9975457,0.00010864538,0.0010476231,0.00089411763,0.00023911156,0.0001647923],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0029605872,0.00067648443,0.0013827359,0.0006752169,0.000055681736,0.000026097538,0.0010763721,0.00037403047,0.00010677956],"category_scores_gemma":[0.00018876279,0.00057417597,0.00054905104,0.000484931,0.00007359095,0.00014541039,0.0012650636,0.009258018,0.000013975459],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008094019,0.0014686186,0.0009184942,0.0028248578,0.009269492,0.00005207418,0.0041707093,0.009658997,0.9559163,0.0018364207,0.00001743585,0.0130572375],"study_design_scores_gemma":[0.0111243,0.00558906,0.0006897018,0.005921555,0.008452969,0.0013162127,0.010891534,0.024112845,0.872177,0.055425994,0.0007486602,0.003550154],"about_ca_topic_score_codex":0.0028889305,"about_ca_topic_score_gemma":0.0009817757,"teacher_disagreement_score":0.08373924,"about_ca_system_score_codex":0.0013908579,"about_ca_system_score_gemma":0.0023046592,"threshold_uncertainty_score":0.999671},"labels":[],"label_agreement":null},{"id":"W4404861927","doi":"10.3390/engproc2024076095","title":"Investigating Sustainable Hydrogen Production via Catalytic Steam Reforming of Ethanol over Stable Commercial Catalysts","year":2024,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Steam reforming; Catalysis; Hydrogen production; Ethanol; Hydrogen; Methane reformer; Waste management; Production (economics); Chemical engineering; Chemistry; Environmental science; Materials science; Process engineering; Organic chemistry; Economics; Engineering","score_opus":0.012640922081306056,"score_gpt":0.2541130762315681,"score_spread":0.24147215415026205,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404861927","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9913847,0.00090747944,0.00039869908,0.00015969871,0.00035628528,0.00043868268,0.000009658879,0.00058422063,0.0057605943],"genre_scores_gemma":[0.988495,0.000009462643,0.00019583492,0.00002004301,0.0003273452,0.000042155745,0.000121657315,0.000104674866,0.010683833],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9975048,0.000024563924,0.0007070221,0.000533716,0.0005104998,0.0007194239],"domain_scores_gemma":[0.9988818,0.00008955973,0.00012983907,0.00059153215,0.00013246006,0.00017476713],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007864467,0.00031792858,0.00045382418,0.0003871267,0.00011670765,0.000024408464,0.0002910449,0.00018080793,0.000060052866],"category_scores_gemma":[0.00044610052,0.00027996444,0.00018755763,0.0011311563,0.00010012217,0.0010392935,0.00029942006,0.0004696379,0.000052915027],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000008856796,0.000038843875,0.0001927339,0.0020852466,0.0001634414,0.000026560398,0.0015374303,0.0007625648,0.98508584,0.0011808146,0.00012239766,0.008795255],"study_design_scores_gemma":[0.00018537212,0.000027571421,0.00001902458,0.0002769325,0.00011290451,0.00008197943,0.00068219774,0.010473803,0.9854322,0.0004071686,0.0019569192,0.0003439322],"about_ca_topic_score_codex":0.005497404,"about_ca_topic_score_gemma":0.00010996372,"teacher_disagreement_score":0.009711238,"about_ca_system_score_codex":0.000727344,"about_ca_system_score_gemma":0.00018911916,"threshold_uncertainty_score":0.99996525},"labels":[],"label_agreement":null},{"id":"W4405894506","doi":"10.1016/j.fuel.2024.134134","title":"CO hydrogenation in a microreactor under non-differential regime: Kinetics, and impact of reactor design and operational variables","year":2024,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Fondo Nacional de Desarrollo Científico y Tecnológico; Universidad de Santiago de Chile","keywords":"Microreactor; Reactor design; Kinetics; Differential (mechanical device); Process engineering; Chemistry; Chemical engineering; Thermodynamics; Nuclear engineering; Catalysis; Organic chemistry; Physics; Engineering","score_opus":0.014842700301239273,"score_gpt":0.2637854815780705,"score_spread":0.24894278127683125,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4405894506","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9889094,0.00059032993,0.010096867,0.000032178887,0.000054575365,0.00012952076,0.000028679306,0.000025504774,0.00013289486],"genre_scores_gemma":[0.99879336,0.00004313076,0.00092324655,0.0000030601825,0.00006178755,0.000006734152,0.000072253606,0.000020960517,0.000075438824],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9994273,0.000012430896,0.0001821807,0.00016474737,0.000091549984,0.0001217578],"domain_scores_gemma":[0.999692,0.0001308371,0.000024852327,0.00008306832,0.000020624522,0.000048620375],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010905968,0.00010847692,0.00015114594,0.00013808407,0.0000072628263,0.00002523778,0.000041609746,0.000082492676,0.00004255891],"category_scores_gemma":[0.000053723594,0.00008856241,0.000036566747,0.000108737004,0.000028650904,0.00012736917,0.00002197274,0.000107822765,0.0000022275678],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002155021,0.000022625805,0.00018551329,0.00012503326,0.000053586442,0.000002752682,0.00026964792,0.00016915651,0.9983543,0.00037798344,0.000029738489,0.0003881039],"study_design_scores_gemma":[0.00066069886,0.000074483934,0.0040056547,0.00017892336,0.00004421211,0.000054561115,0.00002765104,0.102195516,0.8918642,0.0005639919,0.0001294905,0.00020065301],"about_ca_topic_score_codex":0.0001987541,"about_ca_topic_score_gemma":0.000005309136,"teacher_disagreement_score":0.10649015,"about_ca_system_score_codex":0.00010723299,"about_ca_system_score_gemma":0.000039897997,"threshold_uncertainty_score":0.36114702},"labels":[],"label_agreement":null},{"id":"W4406002498","doi":"10.2139/ssrn.5077051","title":"Tri-Methane Reforming Process for Conversion of Biogas and CO2 into Chemicals and Fuels","year":2025,"lang":"en","type":"article","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Methane; Biogas; Waste management; Environmental science; Process (computing); Methane reformer; Business; Steam reforming; Chemistry; Engineering; Computer science; Hydrogen; Hydrogen production; Organic chemistry","score_opus":0.006439160035950784,"score_gpt":0.2675081249797987,"score_spread":0.2610689649438479,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4406002498","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98864645,0.006400175,0.0043325494,0.00020232111,0.0000646645,0.0001865928,0.0000031655659,0.000026546191,0.00013752404],"genre_scores_gemma":[0.997581,0.0016888591,0.00016599464,0.00001733585,0.00006395501,0.00000927767,0.000006696896,0.000020008287,0.00044684942],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983552,0.000011529571,0.00038331727,0.0001995874,0.00014642859,0.0009039061],"domain_scores_gemma":[0.99939257,0.00013870813,0.0001662792,0.00011252285,0.000108297856,0.00008162425],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010956847,0.00015813501,0.00034596192,0.00020593258,0.00007920813,0.000009173473,0.00015094176,0.00012921345,0.0000032660428],"category_scores_gemma":[0.00035259518,0.00013192998,0.00008902094,0.00023095215,0.00006891308,0.00019041408,0.00006669966,0.0006903202,3.8508503e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023365657,0.000026163514,0.0003587936,0.0005249716,0.00023093127,7.865685e-7,0.00030025,0.0000062390054,0.9644719,0.011086527,0.0000023643906,0.022757458],"study_design_scores_gemma":[0.0018933656,0.00012640003,0.000008071552,0.00020585448,0.0001145582,0.00016254857,0.0014754178,0.00046265722,0.9669385,0.027883952,0.0005753394,0.00015336045],"about_ca_topic_score_codex":0.000050844574,"about_ca_topic_score_gemma":0.000015844178,"teacher_disagreement_score":0.022604097,"about_ca_system_score_codex":0.00042857448,"about_ca_system_score_gemma":0.00039913045,"threshold_uncertainty_score":0.5379948},"labels":[],"label_agreement":null},{"id":"W4406052057","doi":"10.1093/ce/zkae098","title":"Elucidating the reaction kinetics of hydrogen generation via ethanol steam reforming using a nickel-based catalyst","year":2025,"lang":"en","type":"article","venue":"Clean Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs; Canada Foundation for Innovation","keywords":"Steam reforming; Catalysis; Kinetics; Nickel; Ethanol; Hydrogen production; Hydrogen; Methane reformer; Chemistry; Chemical engineering; Materials science; Organic chemistry; Engineering","score_opus":0.018498314775651063,"score_gpt":0.253426685440912,"score_spread":0.23492837066526095,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4406052057","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8880647,0.00021280815,0.10996033,0.000055812943,0.00026294863,0.00010388217,0.00000508307,0.00011021411,0.0012242155],"genre_scores_gemma":[0.9987359,0.000008186407,0.00047972213,0.000070709466,0.00022033122,0.000014219764,0.000118502874,0.00004512241,0.00030730892],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985891,0.000043814667,0.0005487574,0.0002775935,0.0002493871,0.00029133583],"domain_scores_gemma":[0.9989251,0.00009168972,0.00025524196,0.0005775555,0.00009980876,0.000050604296],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026517795,0.00020248996,0.00026790707,0.00020816235,0.000109555134,0.000009834074,0.00026323993,0.00015165185,0.0000068811555],"category_scores_gemma":[0.00017096165,0.00016451172,0.00015424412,0.0005870471,0.000062590094,0.00014497117,0.00010885118,0.00019572732,0.000002249675],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012173553,0.00002789299,0.000007765388,0.000054512417,0.000053452026,0.0000014979568,0.00007706233,0.020900887,0.91861445,0.0002781619,0.0000035840415,0.05996854],"study_design_scores_gemma":[0.00023464333,0.00001522825,0.000004219962,0.000094991105,0.00007835446,0.000008706816,0.0001258128,0.22926955,0.769278,0.000029135615,0.00073323096,0.00012812429],"about_ca_topic_score_codex":0.0015593264,"about_ca_topic_score_gemma":0.00022408359,"teacher_disagreement_score":0.20836866,"about_ca_system_score_codex":0.0003838327,"about_ca_system_score_gemma":0.000052165477,"threshold_uncertainty_score":0.67085934},"labels":[],"label_agreement":null},{"id":"W4406186234","doi":"10.1016/j.energy.2025.134398","title":"Hydrogen production in integration with CCUS: A realistic strategy towards net zero","year":2025,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":38,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Science Foundation of Jiangsu Province; National Natural Science Foundation of China","keywords":"Zero (linguistics); Production (economics); Zero emission; Hydrogen production; Environmental science; Net (polyhedron); Hydrogen; Engineering; Waste management; Economics; Physics; Mathematics; Microeconomics","score_opus":0.010020204337384,"score_gpt":0.23841122343351387,"score_spread":0.22839101909612985,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4406186234","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95157707,0.00034452387,0.022934634,0.00032577608,0.00025628068,0.00014079733,0.0000050794165,0.00025956242,0.024156254],"genre_scores_gemma":[0.99642074,0.000015100675,0.00014171842,0.000020927857,0.00007263059,0.000041608455,0.000087491164,0.000016150196,0.003183614],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992813,0.000015208308,0.00019061724,0.00022141039,0.00011773558,0.000173768],"domain_scores_gemma":[0.99967676,0.000013796732,0.00003619337,0.00021210799,0.00003088491,0.000030244333],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000102890124,0.000118109245,0.00014923242,0.0001672626,0.00001915755,0.000009030715,0.00008800666,0.000069369824,0.000010660821],"category_scores_gemma":[0.00010495247,0.00009471346,0.000028023489,0.00048351745,0.000018061473,0.000118424185,0.000024547082,0.00012046435,0.0000023147825],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016378879,0.000116600364,0.00011720529,0.00012193846,0.00010208422,0.000035961148,0.00038930232,0.11440201,0.57796246,0.050851274,0.00016453241,0.25557286],"study_design_scores_gemma":[0.00033755504,0.000034466415,0.00011194825,0.00018331235,0.000024322142,0.000015391935,0.00008795764,0.0153814955,0.9787611,0.0022967001,0.0025978647,0.00016793575],"about_ca_topic_score_codex":0.0038774984,"about_ca_topic_score_gemma":0.0014491521,"teacher_disagreement_score":0.40079862,"about_ca_system_score_codex":0.00021143343,"about_ca_system_score_gemma":0.000059763854,"threshold_uncertainty_score":0.58616436},"labels":[],"label_agreement":null},{"id":"W4406570718","doi":"10.1016/b978-0-44-313219-3.00127-1","title":"Hydrogen production: Plasma methods","year":2025,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Centre in Green Chemistry and Catalysis","funders":"","keywords":"Plasma; Production (economics); Hydrogen production; Hydrogen; Chemistry; Economics; Physics; Nuclear physics; Macroeconomics","score_opus":0.017429859985730472,"score_gpt":0.2789570932756177,"score_spread":0.2615272332898872,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4406570718","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.000058310678,0.0013758164,0.000058245685,0.00006348657,0.0011314797,0.00049725577,0.000021714119,0.0004012122,0.9963925],"genre_scores_gemma":[0.000046162633,0.000047965746,0.0054929005,0.00004728055,0.00097423757,0.000066309716,0.00006139824,0.0001631364,0.9931006],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9977703,0.000024240646,0.00066502445,0.00076108123,0.0003613414,0.00041799512],"domain_scores_gemma":[0.9983258,0.000114144226,0.00022892054,0.0010776825,0.000100178964,0.000153221],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005090797,0.00061531964,0.000845846,0.0003182467,0.00008989661,0.000015369948,0.00044711333,0.0005895518,0.00028287634],"category_scores_gemma":[0.00019403994,0.0005916315,0.00051699433,0.000037558722,0.0000917092,0.000056282563,0.00032773995,0.0009898051,0.00026511218],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000010838329,0.000003769004,1.5567149e-7,0.00034234973,0.00033562386,0.000019763416,0.00007855515,0.000010902317,0.011654313,0.0048564947,0.000066531684,0.9826207],"study_design_scores_gemma":[0.00013298178,0.000009979272,4.6710298e-8,0.0005967546,0.00027168644,0.00006967926,0.0000028834984,0.00010123575,0.16771406,0.0026388508,0.8279694,0.0004924443],"about_ca_topic_score_codex":8.654612e-7,"about_ca_topic_score_gemma":0.0000048794327,"teacher_disagreement_score":0.98212826,"about_ca_system_score_codex":0.00035826123,"about_ca_system_score_gemma":0.00012783844,"threshold_uncertainty_score":0.9996535},"labels":[],"label_agreement":null},{"id":"W4406714998","doi":"10.1016/j.mtsust.2025.101082","title":"Promotional role of methanol and CO2 in carbon dioxide-rich syngas hydrogenation over slurry reactor utilizing combustion induced Cu-based catalysts","year":2025,"lang":"en","type":"article","venue":"Materials Today Sustainability","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Federation of Indian Chambers of Commerce and Industry; Science and Engineering Research Board; Department of Science and Technology, Ministry of Science and Technology, India","keywords":"Syngas; Slurry; Methanol; Combustion; Catalysis; Carbon dioxide; Chemical engineering; Syngas to gasoline plus; Materials science; Carbon fibers; Waste management; Chemistry; Organic chemistry; Steam reforming; Hydrogen production; Composite material","score_opus":0.007974103398197081,"score_gpt":0.2537048224053392,"score_spread":0.24573071900714213,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4406714998","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99850976,0.00007755707,0.000034532914,0.00011505286,0.0001538451,0.0008320029,0.000038063656,0.00009707785,0.00014209186],"genre_scores_gemma":[0.99960876,0.0000018609331,0.000056856108,0.0000072828034,0.000029134977,0.00012072326,0.0001266012,0.00002693958,0.000021846587],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99785215,0.00019250959,0.00079684274,0.00047528747,0.00031128988,0.00037192873],"domain_scores_gemma":[0.9987866,0.00022113197,0.00022174326,0.0004345917,0.0002677362,0.00006814412],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0014935323,0.00026374016,0.00056438666,0.00038403808,0.00003917569,0.000019353578,0.00015639127,0.00026297118,0.000018302504],"category_scores_gemma":[0.0019653556,0.00026317325,0.000067097186,0.00054858514,0.00007591082,0.0002137831,0.00015691793,0.00019227319,3.930802e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013173475,0.00015659668,0.0133349495,0.0012475217,0.000034224726,0.0000045023526,0.00030647157,0.00014653728,0.983279,0.00070732506,3.5122358e-7,0.0006508155],"study_design_scores_gemma":[0.0007637696,0.000031189622,0.025127854,0.00014827457,0.00005136954,0.0000022387414,0.00033751683,0.0020156722,0.96927613,0.002025585,0.000014493347,0.00020590072],"about_ca_topic_score_codex":0.0028668446,"about_ca_topic_score_gemma":0.00006843823,"teacher_disagreement_score":0.0140028335,"about_ca_system_score_codex":0.001128371,"about_ca_system_score_gemma":0.00025723182,"threshold_uncertainty_score":0.99998206},"labels":[],"label_agreement":null},{"id":"W4406905738","doi":"10.3390/su17030980","title":"An Investigation of the Catalytic Activity of Inconel and Stainless Steel Powders in Reforming Primary Syngas","year":2025,"lang":"en","type":"article","venue":"Sustainability","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Horizon 2020 Framework Programme; Université de Sherbrooke","keywords":"Syngas; Inconel; Syngas to gasoline plus; Materials science; Catalysis; Metallurgy; Waste management; Steam reforming; Chemistry; Engineering; Organic chemistry; Hydrogen production","score_opus":0.0059874437890704195,"score_gpt":0.24911990038144893,"score_spread":0.2431324565923785,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4406905738","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9990416,0.00004823638,0.00009246525,0.00020142921,0.000034361794,0.00042332866,0.0000067191027,0.000022966222,0.00012886428],"genre_scores_gemma":[0.9998618,0.0000017536214,0.000033588873,0.000010709037,0.0000043699497,0.000015812942,0.0000052592745,0.00000959391,0.00005716172],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988922,0.00009537215,0.00037299687,0.00024490888,0.00017580859,0.0002187236],"domain_scores_gemma":[0.9988316,0.00017716495,0.00014409362,0.0005828056,0.0002168305,0.000047497775],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0009770764,0.00012794169,0.00031217493,0.00015292494,0.00003958141,0.0000042329525,0.00021679695,0.00010527508,7.2671736e-7],"category_scores_gemma":[0.0009866592,0.0001002616,0.00006166972,0.00059816905,0.0003017794,0.00031545956,0.00022513315,0.00025132205,3.226465e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012948026,0.00012407912,0.28311983,0.006260579,0.00003689191,0.0000019270453,0.0038195145,0.0008304329,0.6873343,0.0031473385,4.176065e-7,0.015195173],"study_design_scores_gemma":[0.0004723391,0.000022637036,0.27059853,0.00014240773,0.000028924409,0.0000014021253,0.0029336289,0.002216287,0.71618587,0.0072772997,0.0000041398666,0.00011657839],"about_ca_topic_score_codex":0.0026418527,"about_ca_topic_score_gemma":0.00022979354,"teacher_disagreement_score":0.028851517,"about_ca_system_score_codex":0.0014970326,"about_ca_system_score_gemma":0.000535147,"threshold_uncertainty_score":0.40885493},"labels":[],"label_agreement":null},{"id":"W4407157119","doi":"10.1016/j.matt.2024.11.009","title":"Decarbonizing syngas—Which ways to go?","year":2025,"lang":"en","type":"article","venue":"Matter","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Syngas to gasoline plus; Business; Chemistry","score_opus":0.010439648720261251,"score_gpt":0.2413814445168055,"score_spread":0.23094179579654422,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407157119","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7533077,0.00010287874,0.03937109,0.0028987848,0.0006108515,0.00022270076,0.000005362409,0.00034092637,0.2031397],"genre_scores_gemma":[0.98827153,6.4435676e-7,0.0015834282,0.0016527153,0.00009792756,0.00003144521,0.000006686232,0.000032795706,0.008322814],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992046,0.0000038403687,0.00017975707,0.00020731121,0.000112236354,0.0002922714],"domain_scores_gemma":[0.9995102,0.000048992184,0.000015878735,0.0003255113,0.000030075495,0.00006931922],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0001051675,0.000121669815,0.0001618434,0.00013284944,0.00003264572,0.000018965651,0.00018649132,0.000064308544,0.00026303894],"category_scores_gemma":[0.00007849703,0.00011190977,0.00005661992,0.0003794253,0.0000061977476,0.000059487305,0.00016941443,0.0001583868,0.0023557453],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000011087011,0.000018525168,0.0019110112,0.00015569644,0.000059892962,0.000009280935,0.00022117089,0.0003075638,0.98510456,0.0022834365,0.0067244167,0.003193386],"study_design_scores_gemma":[0.0003292473,0.000007896313,0.0013922367,0.00026271114,0.000044956145,0.000013591477,0.000030104906,0.0015727186,0.8990156,0.00044047678,0.096546955,0.00034349432],"about_ca_topic_score_codex":0.0000563347,"about_ca_topic_score_gemma":0.000016779242,"teacher_disagreement_score":0.23496385,"about_ca_system_score_codex":0.000121473255,"about_ca_system_score_gemma":0.000011701605,"threshold_uncertainty_score":0.998421},"labels":[],"label_agreement":null},{"id":"W4407291257","doi":"10.1016/j.ijhydene.2025.02.013","title":"Impact of oxygen vacancies on the catalytic activity of Ni/Co3O4 for CO2 methanation","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Science and Engineering Research Board; Department of Science and Technology, Ministry of Science and Technology, India; Canadian Anesthesiologists' Society","keywords":"Methanation; Catalysis; Oxygen; Chemistry; Materials science","score_opus":0.015387607651030042,"score_gpt":0.2961123712764417,"score_spread":0.28072476362541166,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407291257","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9930761,0.00021651873,0.0053222235,0.0002932804,0.00029719158,0.000049387694,0.000047826277,0.0000058437195,0.000691645],"genre_scores_gemma":[0.99943334,0.0000428392,0.000077579156,0.000022733508,0.000118660304,0.000005319041,0.000009898044,0.000012667581,0.00027693718],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988757,0.00002339958,0.0004648128,0.000086435066,0.00043256007,0.00011711818],"domain_scores_gemma":[0.99832416,0.00044432376,0.0005352602,0.00014542112,0.00051637756,0.00003447702],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00039354418,0.000114426315,0.00027213755,0.00033677826,0.000017432109,0.0000063155785,0.00048628479,0.000057838162,0.000021963973],"category_scores_gemma":[0.00058938755,0.0000757536,0.0004263095,0.00017680167,0.00003814916,0.00013719738,0.000058777463,0.00011486133,4.0728742e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00044555453,0.0001498393,0.0002201301,0.00002897852,0.002139219,0.0000041180465,0.00011641411,0.020372692,0.9523189,0.013026552,0.0001646056,0.0110129975],"study_design_scores_gemma":[0.0005303028,0.00010474369,0.00042354775,0.00012384464,0.000075230295,0.00002390007,0.00002265188,0.0073340097,0.98931587,0.0012797075,0.00070212886,0.00006406811],"about_ca_topic_score_codex":0.0005124193,"about_ca_topic_score_gemma":0.000025417405,"teacher_disagreement_score":0.036996968,"about_ca_system_score_codex":0.00036289115,"about_ca_system_score_gemma":0.00015158785,"threshold_uncertainty_score":0.3089142},"labels":[],"label_agreement":null},{"id":"W4407559425","doi":"10.1039/d4ee06191h","title":"Methane pyrolysis for hydrogen production: navigating the path to a net zero future","year":2025,"lang":"en","type":"article","venue":"Energy & Environmental Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":108,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto; University of Calgary; University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Alberta Innovates","keywords":"Hydrogen production; Path (computing); Net (polyhedron); Production (economics); Pyrolysis; Methane; Zero (linguistics); Environmental science; Hydrogen; Waste management; Chemistry; Computer science; Economics; Engineering; Mathematics; Computer network; Microeconomics; Organic chemistry; Philosophy","score_opus":0.004485181591879346,"score_gpt":0.2238241474020045,"score_spread":0.21933896581012513,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407559425","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99136585,0.00044891314,0.0046794857,0.0020802356,0.00050681096,0.00024275095,0.000012436003,0.00007440709,0.0005891154],"genre_scores_gemma":[0.9959999,0.000016182383,0.0013443598,0.00030982934,0.00028331307,0.00016086834,0.000015391262,0.000016783652,0.0018533745],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99841404,0.000013280503,0.00021924426,0.0005196186,0.00040375843,0.00043005377],"domain_scores_gemma":[0.9993091,0.00004081909,0.00005775886,0.00046705847,0.0000071760996,0.00011805635],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005294757,0.0001672733,0.00015752087,0.00006173382,0.00033614016,0.000021750318,0.00057831174,0.000048275848,0.00002525279],"category_scores_gemma":[0.00010208235,0.00012059356,0.000106322324,0.0007841684,0.00020654484,0.00020866333,0.00031962374,0.00015597895,0.000010883899],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000008312251,0.000019517724,0.000040078008,0.0000065238123,0.000017000435,8.044981e-7,0.00028407422,0.0036152075,0.95096195,0.0007383762,0.000028365364,0.0442798],"study_design_scores_gemma":[0.00011502008,0.000019790274,0.000085343585,0.000033017455,0.000029070454,0.000009823924,0.00041008525,0.00192148,0.9703004,0.00015752055,0.026767408,0.00015103628],"about_ca_topic_score_codex":0.000068132824,"about_ca_topic_score_gemma":0.00000899671,"teacher_disagreement_score":0.04412876,"about_ca_system_score_codex":0.00036789145,"about_ca_system_score_gemma":0.000031277923,"threshold_uncertainty_score":0.49176627},"labels":[],"label_agreement":null},{"id":"W4407564501","doi":"10.1016/j.ijhydene.2025.02.098","title":"Investigation of Al2O3, ZrO2, SiO2, and CeO2 supported nickel catalysts for tri-reforming of methane","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada; Canadian Natural Resources Limited","keywords":"Methane; Nickel; Catalysis; Methane reformer; Carbon dioxide reforming; Steam reforming; Chemistry; Syngas; Materials science; Metallurgy; Hydrogen production; Organic chemistry","score_opus":0.013541511021194127,"score_gpt":0.26525025594871354,"score_spread":0.25170874492751943,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407564501","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99379176,0.00092581834,0.004367149,0.00022766869,0.0003448249,0.000057857935,0.000037439342,0.000010008913,0.000237463],"genre_scores_gemma":[0.998038,0.00006609908,0.0013057058,0.00003926476,0.00012211106,0.000005377249,0.00006620496,0.000019472232,0.0003377498],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982256,0.000020937803,0.0010286327,0.00013647455,0.0004339025,0.00015439637],"domain_scores_gemma":[0.99820536,0.00020563518,0.00077064306,0.00013525193,0.0005956965,0.000087426124],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00047575968,0.00014755124,0.00042909232,0.00060524326,0.000013881138,0.0000065241766,0.00036815804,0.00010179333,0.000009485015],"category_scores_gemma":[0.00035246072,0.00012841081,0.0002489786,0.0002202032,0.00007112335,0.00026399814,0.00009820074,0.00011629043,2.3680568e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017910042,0.000030045747,0.00051152287,0.0000863703,0.0007742161,0.000009633317,0.00020970618,0.00040720686,0.98651826,0.003316998,0.000032150867,0.007924801],"study_design_scores_gemma":[0.0014193755,0.00006178774,0.000051193285,0.0002653586,0.000116634226,0.00012226599,0.00011422863,0.0024967503,0.991173,0.0023876545,0.0016902727,0.0001014732],"about_ca_topic_score_codex":0.00028622444,"about_ca_topic_score_gemma":0.000027316408,"teacher_disagreement_score":0.007823328,"about_ca_system_score_codex":0.00014147442,"about_ca_system_score_gemma":0.0001545139,"threshold_uncertainty_score":0.5236441},"labels":[],"label_agreement":null},{"id":"W4407693216","doi":"10.1016/j.energy.2025.135125","title":"Experimental investigation on the feasibility of integrating heat pipe in fixed-bed reactor for dry reforming of methane","year":2025,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"National Natural Science Foundation of China","keywords":"Methane; Carbon dioxide reforming; Waste management; Methane reformer; Environmental science; Nuclear engineering; Process engineering; Steam reforming; Syngas; Engineering; Chemistry; Hydrogen production; Hydrogen","score_opus":0.034615307396072575,"score_gpt":0.2918297651277094,"score_spread":0.25721445773163687,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407693216","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9972108,0.00018388368,0.0011259498,0.00008359667,0.0001110672,0.00015337339,0.000008226149,0.000026129646,0.0010969446],"genre_scores_gemma":[0.99902517,0.000002275844,0.0006110453,0.000038709295,0.00003017765,0.0000647549,0.000028308392,0.000014868875,0.00018468041],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989902,0.000039668394,0.00046932537,0.00019000072,0.00014529495,0.00016550816],"domain_scores_gemma":[0.9990383,0.0004700101,0.00010268643,0.00031518226,0.00004503458,0.000028805347],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046864644,0.00013001681,0.00028159266,0.00014455355,0.000017125229,0.000002622279,0.00017150519,0.00008621778,0.000009799195],"category_scores_gemma":[0.0008630454,0.0000910249,0.00011647623,0.00035866362,0.000054027445,0.00010603511,0.00006445437,0.00012665881,1.7392264e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000069396476,0.00003866616,0.00025500797,0.000076631804,0.000019130017,2.068798e-7,0.0005479942,0.00011219655,0.980889,0.016143106,0.0000022578172,0.0018464002],"study_design_scores_gemma":[0.00041530075,0.00005344517,0.000041686657,0.00027501024,0.000008072854,3.2732066e-7,0.0009551642,0.004640494,0.99281186,0.000600637,0.00012104206,0.00007698849],"about_ca_topic_score_codex":0.0022109894,"about_ca_topic_score_gemma":0.00018587954,"teacher_disagreement_score":0.015542468,"about_ca_system_score_codex":0.00028416322,"about_ca_system_score_gemma":0.000047372392,"threshold_uncertainty_score":0.3711888},"labels":[],"label_agreement":null},{"id":"W4407755657","doi":"10.1016/j.energy.2025.135106","title":"Development of an integrated energy system with CO2 capture and utilization in an industrial setting for clean hydrogen and methanol","year":2025,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":18,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Clean energy; Waste management; Methanol; Process engineering; Hydrogen; Environmental science; Hydrogen fuel; Engineering; Chemistry; Environmental engineering; Organic chemistry","score_opus":0.019064892324145547,"score_gpt":0.2421593157190801,"score_spread":0.22309442339493454,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407755657","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9727667,0.00012363106,0.02682084,0.000006102234,0.00003654099,0.00007915323,0.000007761241,0.000055573717,0.00010372542],"genre_scores_gemma":[0.9961411,0.0000021187182,0.0034871637,0.000008803346,0.000027149214,0.000037099908,0.00018556732,0.000022306549,0.00008871405],"study_design_codex":"design_other","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99919164,0.00002954655,0.00029290438,0.00023115093,0.00009228308,0.00016245148],"domain_scores_gemma":[0.99964476,0.000045426204,0.000079946534,0.00012193232,0.00004602725,0.00006192133],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00020588827,0.00013882655,0.0002425872,0.00019099256,0.00003609126,0.000010272197,0.00007388985,0.00015367648,8.532532e-7],"category_scores_gemma":[0.000041602136,0.00011572922,0.000013845056,0.00028029052,0.000020138828,0.0001287971,0.000039430004,0.000074900716,1.3933994e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004362579,0.00008328258,0.0006850148,0.00044604,0.00020795615,0.000009629502,0.0027092572,0.0046998234,0.44956696,0.020260205,0.0000032609494,0.5208923],"study_design_scores_gemma":[0.0011359362,0.000038683746,0.000025925217,0.00031626527,0.00002731836,0.000008184281,0.0021761353,0.08890949,0.9054712,0.000016779884,0.0017220231,0.00015205842],"about_ca_topic_score_codex":0.0008318755,"about_ca_topic_score_gemma":0.0023735003,"teacher_disagreement_score":0.5207403,"about_ca_system_score_codex":0.00013006877,"about_ca_system_score_gemma":0.000091470305,"threshold_uncertainty_score":0.47193006},"labels":[],"label_agreement":null},{"id":"W4407776765","doi":"10.20944/preprints202502.1670.v1","title":"Energy of the Chain’s Service Area Size of Biomethane Recovery","year":2025,"lang":"en","type":"preprint","venue":"Preprints.org","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"École de Technologie Supérieure","funders":"","keywords":"Biogas; Service (business); Energy (signal processing); Business; Chain (unit); Environmental science; Waste management; Engineering; Marketing; Mathematics; Physics; Statistics","score_opus":0.05765544313608248,"score_gpt":0.2935742576384771,"score_spread":0.23591881450239463,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407776765","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9823044,0.00033576397,0.00043709177,0.00029856325,0.0011595676,0.00037327272,0.00023100388,0.00014417068,0.014716181],"genre_scores_gemma":[0.9928042,0.00015518721,0.0001739029,0.00008961024,0.00010140064,0.00009462442,0.000047886337,0.0000537192,0.006479431],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9970829,0.000098577664,0.0010826034,0.00077970134,0.0005607488,0.00039547784],"domain_scores_gemma":[0.99548894,0.00052212615,0.00082232675,0.0027362634,0.00033085415,0.000099487515],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007314918,0.00046445898,0.0009941923,0.00028180468,0.00003211987,0.0000033918002,0.0017773376,0.00060913374,0.0004144087],"category_scores_gemma":[0.0013034774,0.00038663048,0.00069360127,0.0008694677,0.00009091167,0.00006751441,0.0057493863,0.00084376766,0.00002478222],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010340471,0.00014771846,0.009674244,0.0031578138,0.00072227936,0.0000027224085,0.0005746257,0.0046877377,0.9783082,0.0005882387,0.0000065528834,0.0020264746],"study_design_scores_gemma":[0.00032075532,0.0000055660125,0.0033566856,0.0013510786,0.00018226079,0.000005525941,0.000053158205,0.0010280233,0.99060994,0.0013988256,0.0013567177,0.00033145183],"about_ca_topic_score_codex":0.0040701414,"about_ca_topic_score_gemma":0.000103762344,"teacher_disagreement_score":0.0123017635,"about_ca_system_score_codex":0.00029234088,"about_ca_system_score_gemma":0.00027267772,"threshold_uncertainty_score":0.99985856},"labels":[],"label_agreement":null},{"id":"W4407802085","doi":"10.1016/j.jgsce.2025.205581","title":"Comparison of conventional and simplified heterogeneous modeling frameworks for simulation of sulfur poisoning in methane reforming catalyst","year":2025,"lang":"en","type":"article","venue":"Gas Science and Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation","keywords":"Methane; Sulfur; Catalysis; Methane reformer; Environmental science; Chemistry; Steam reforming; Materials science; Metallurgy; Hydrogen production; Organic chemistry","score_opus":0.022025622539609525,"score_gpt":0.3136612079481286,"score_spread":0.291635585408519,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407802085","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8455567,0.00042562734,0.15378578,0.000012645325,0.00005740439,0.00011852281,0.000003213987,0.000019970623,0.00002016811],"genre_scores_gemma":[0.9971816,0.000007847582,0.0027651088,0.0000032802945,0.000012463759,0.000010180592,0.0000061243154,0.000009329635,0.000004079717],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99890256,0.00000294276,0.00043296837,0.00021762116,0.00019706534,0.00024683008],"domain_scores_gemma":[0.999461,0.00017875116,0.0000736517,0.00012222561,0.00011415069,0.00005020006],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00062059,0.00011226255,0.0003091746,0.00041436087,0.00004242887,0.000009986427,0.00011873272,0.000099992976,6.563561e-7],"category_scores_gemma":[0.0006059245,0.00011280112,0.000039906787,0.0005337277,0.000062769264,0.00022522394,0.00009011955,0.00016957821,4.5266976e-8],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000010592173,0.000006539707,0.000443069,0.00021582808,0.000007673962,1.7276562e-7,0.00023470618,0.6444455,0.35211736,0.0003712727,2.5504258e-8,0.0021472808],"study_design_scores_gemma":[0.00023013998,0.000011475176,0.000056076533,0.0002468727,0.000012689991,0.0000020652003,0.00014689584,0.72501314,0.274115,0.000088783694,0.0000047347708,0.00007212736],"about_ca_topic_score_codex":0.000085140986,"about_ca_topic_score_gemma":0.000008863909,"teacher_disagreement_score":0.15162492,"about_ca_system_score_codex":0.00008824827,"about_ca_system_score_gemma":0.000037487043,"threshold_uncertainty_score":0.4599896},"labels":[],"label_agreement":null},{"id":"W4407846847","doi":"10.1093/ijlct/ctae295","title":"Multi-objective optimization evaluation of renewable and clean methanol synthesis","year":2025,"lang":"en","type":"article","venue":"International Journal of Low-Carbon Technologies","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Impact","funders":"Northern Border University; Guizhou Science and Technology Department","keywords":"Renewable energy; Methanol; Clean energy; Biochemical engineering; Process engineering; Chemistry; Environmental science; Computer science; Engineering; Environmental engineering; Organic chemistry; Electrical engineering","score_opus":0.0170534692987728,"score_gpt":0.2912636303290649,"score_spread":0.27421016103029205,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407846847","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9660912,0.0014920315,0.02951218,0.000583414,0.0005798371,0.00018523804,0.000008314214,0.000155063,0.0013927241],"genre_scores_gemma":[0.98840153,0.00025773278,0.011244441,0.0000045095862,0.000024265915,0.00001133525,0.0000016040755,0.000011246599,0.00004331453],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986562,0.00003413208,0.0005134314,0.00013365192,0.0005547355,0.00010785694],"domain_scores_gemma":[0.9982161,0.00022625152,0.00042849037,0.0001479129,0.00096558157,0.000015674583],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00084378803,0.00011809477,0.00026343222,0.0008114132,0.000016023936,0.000014203627,0.00039332273,0.00014987726,0.000008178088],"category_scores_gemma":[0.00463723,0.00010272669,0.0000935389,0.00028115444,0.00008618724,0.00019374129,0.00015629454,0.0001963887,2.1533351e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013997058,0.00012709193,0.0010558686,0.00007694619,0.0008700191,0.0000091121265,0.00018496408,0.14541693,0.68072397,0.00032036804,0.000007918132,0.17106684],"study_design_scores_gemma":[0.00062103686,0.000019883053,0.0002196704,0.00043340118,0.00013357257,0.000020322992,0.0010213896,0.16698676,0.8296371,0.0008160741,0.000012791174,0.000077967714],"about_ca_topic_score_codex":0.00007132964,"about_ca_topic_score_gemma":0.000014712347,"teacher_disagreement_score":0.17098886,"about_ca_system_score_codex":0.00032288808,"about_ca_system_score_gemma":0.00008172776,"threshold_uncertainty_score":0.55515325},"labels":[],"label_agreement":null},{"id":"W4407849196","doi":"10.1016/j.micromeso.2025.113548","title":"Investigating the role of zeolite supports in Ni-based catalysts for CO2-methanation using in situ/operando XAS–GC-MS","year":2025,"lang":"en","type":"article","venue":"Microporous and Mesoporous Materials","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"Center of Excellence for Innovation in Chemistry; Synchrotron Light Research Institute; Khon Kaen University","keywords":"Methanation; X-ray absorption spectroscopy; Catalysis; In situ; Zeolite; Chemical engineering; Materials science; Inorganic chemistry; Chemistry; Absorption spectroscopy; Organic chemistry; Physics","score_opus":0.008497558454058913,"score_gpt":0.25218005869878957,"score_spread":0.24368250024473065,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407849196","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9974739,0.0010382201,0.00014314093,0.00008704382,0.00019826538,0.0007544824,0.00006453337,0.000036160425,0.00020425963],"genre_scores_gemma":[0.998172,0.000017143284,0.0012819888,0.00009317861,0.00005294963,0.00006807032,0.00017022272,0.000040444636,0.00010402312],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99805045,0.00008148174,0.00093738,0.00035573493,0.0001547751,0.00042016766],"domain_scores_gemma":[0.99910176,0.00017175521,0.00027516836,0.00030140707,0.00009671737,0.00005320437],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0013495332,0.00026161913,0.00064402237,0.00027974782,0.00011237219,0.00006301893,0.00018934673,0.00016785618,0.000009419807],"category_scores_gemma":[0.000348878,0.00021063529,0.000070112364,0.0003570244,0.00010704152,0.00013376462,0.000097952914,0.000124769,7.1108724e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005860258,0.000043979144,0.0018290703,0.00042517902,0.000027304326,0.000005520773,0.0009758262,0.0002689145,0.9941421,0.0002723773,0.000009699237,0.0019414169],"study_design_scores_gemma":[0.0015869115,0.000020082809,0.00044983657,0.00037872072,0.00005728478,0.000017063283,0.00054296147,0.00093420444,0.9948041,0.0007142009,0.00028396683,0.00021068787],"about_ca_topic_score_codex":0.009409483,"about_ca_topic_score_gemma":0.0012994235,"teacher_disagreement_score":0.0081100585,"about_ca_system_score_codex":0.00021742102,"about_ca_system_score_gemma":0.00015130527,"threshold_uncertainty_score":0.99718696},"labels":[],"label_agreement":null},{"id":"W4407929551","doi":"10.1016/j.cep.2025.110248","title":"Integration of indirect mechanism autothermal reforming process with chilled methanol scrubbing solution for syngas purification: Power generation exploiting blue hydrogen as fuel","year":2025,"lang":"en","type":"article","venue":"Chemical Engineering and Processing - Process Intensification","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Alberta Energy","funders":"","keywords":"Syngas to gasoline plus; Syngas; Methane reformer; Data scrubbing; Methanol; Waste management; Steam reforming; Hydrogen; Process engineering; Chemistry; Hydrogen production; Engineering; Organic chemistry","score_opus":0.017537735594918374,"score_gpt":0.2608813112467819,"score_spread":0.24334357565186351,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4407929551","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7228492,0.0005862686,0.27530944,0.00014890371,0.000080106016,0.00053735217,0.0000063600596,0.00035182683,0.00013054768],"genre_scores_gemma":[0.9911789,0.00001542715,0.0077410433,0.000039895545,0.00012268242,0.0005309277,0.00020170394,0.00008974566,0.00007968947],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99771756,0.000014971774,0.0007993331,0.00068838394,0.00034297898,0.00043675007],"domain_scores_gemma":[0.99820364,0.00009882476,0.00043128658,0.00029572766,0.00086231454,0.00010822898],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00055155467,0.0004234537,0.000530144,0.00041095927,0.00018279858,0.00006670155,0.00025300085,0.0003174437,0.0000034524041],"category_scores_gemma":[0.0011292166,0.00038177634,0.0000945112,0.00081461365,0.000077268356,0.00068756007,0.00003942476,0.00039346912,0.0000010613707],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010756573,0.000047348567,0.000007536977,0.0015829916,0.00008099277,5.196218e-7,0.0026629004,0.0025229708,0.97575355,0.0013120364,8.3291474e-7,0.015920779],"study_design_scores_gemma":[0.00045401105,0.000038133196,0.0000054331567,0.0010032825,0.00010623949,0.000031144667,0.000603132,0.3275684,0.6695937,0.00029184556,0.00001843897,0.00028620433],"about_ca_topic_score_codex":0.000014304213,"about_ca_topic_score_gemma":8.365164e-7,"teacher_disagreement_score":0.32504547,"about_ca_system_score_codex":0.0002215318,"about_ca_system_score_gemma":0.00017340433,"threshold_uncertainty_score":0.9998634},"labels":[],"label_agreement":null},{"id":"W4408010023","doi":"10.26599/nr.2025.94907331","title":"High-selective Fischer–Tropsch synthesis to jet fuel over confined iron catalysts inside carbon nanocages","year":2025,"lang":"en","type":"article","venue":"Nano Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"National Key Research and Development Program of China; Government of Jiangsu Province; Natural Science Foundation of Jiangsu Province; National Natural Science Foundation of China","keywords":"Nanocages; Fischer–Tropsch process; Catalysis; Jet fuel; Materials science; Chemical engineering; Carbon fibers; Nanotechnology; Chemistry; Selectivity; Organic chemistry; Composite number; Composite material","score_opus":0.02389249246478813,"score_gpt":0.3245078505334348,"score_spread":0.30061535806864664,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408010023","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97443813,0.00066278357,0.000047812995,0.0010935558,0.00026627365,0.0006586986,0.000034185832,0.00022881562,0.022569748],"genre_scores_gemma":[0.99013114,0.000050632716,0.000323754,0.00005185707,0.00016782929,0.00033873145,0.000023630242,0.00007754833,0.008834889],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9962647,0.0002068554,0.0004732983,0.0007845488,0.0011138106,0.0011567957],"domain_scores_gemma":[0.9967263,0.001590886,0.00005410922,0.0009183987,0.0004195815,0.00029072948],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0013978835,0.0003455997,0.0005870761,0.0010802218,0.00016403252,0.000065578985,0.00070803164,0.00033450674,0.00010785337],"category_scores_gemma":[0.0055636284,0.0003095628,0.00015764419,0.0024405576,0.000119100834,0.00014876437,0.00061912235,0.0009473396,0.000151562],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018539093,0.0000757324,0.0005781124,0.00030101402,0.00014817709,0.0000378513,0.0003901692,0.00005692464,0.9907455,0.0013276543,0.0015058665,0.0046476503],"study_design_scores_gemma":[0.0004512591,0.000063857115,0.001199124,0.00035437063,0.000041842268,0.0000052645587,0.00015965596,0.00031750792,0.9901557,0.00015917039,0.006773032,0.00031921704],"about_ca_topic_score_codex":0.009478719,"about_ca_topic_score_gemma":0.0009390309,"teacher_disagreement_score":0.015693001,"about_ca_system_score_codex":0.001063118,"about_ca_system_score_gemma":0.0003066626,"threshold_uncertainty_score":0.9999356},"labels":[],"label_agreement":null},{"id":"W4408027367","doi":"10.1016/j.ijhydene.2025.02.214","title":"Effect of additives on nickel/calcined dolomite catalyst performance for corn stalk gasification hydrogen production","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Six Talent Peaks Project in Jiangsu Province; Jiangsu Agricultural Science and Technology Innovation Fund","keywords":"Dolomite; Calcination; Nickel; Catalysis; Hydrogen production; Stalk; Chemistry; Hydrogen; Chemical engineering; Steam reforming; Materials science; Metallurgy; Nuclear chemistry; Organic chemistry","score_opus":0.007951041879791764,"score_gpt":0.2642527418318164,"score_spread":0.2563016999520246,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408027367","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9965132,0.00022371978,0.0016718499,0.00018239091,0.0007861548,0.00012356295,0.000042003237,0.000023455854,0.00043368066],"genre_scores_gemma":[0.9982184,0.00007513306,0.0000963219,0.000025079447,0.00043304882,0.00002932576,0.00014054097,0.00002551084,0.00095660496],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984544,0.000045276633,0.0007071845,0.00020567632,0.00041021267,0.00017726884],"domain_scores_gemma":[0.99843085,0.0002891925,0.00057014736,0.00020075141,0.0004505319,0.000058555648],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000573861,0.00018831619,0.00035702952,0.00050762505,0.000038483242,0.000009498791,0.0004347864,0.0000869923,0.000017001325],"category_scores_gemma":[0.000616724,0.00015522628,0.00029907495,0.00021305977,0.00005002303,0.0002730464,0.00005127914,0.00015084448,0.0000032454982],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0017393272,0.00011928141,0.00027045814,0.00012461061,0.00088745944,0.0000058355777,0.000073914714,0.014106952,0.93934786,0.0009852462,0.00010276903,0.04223626],"study_design_scores_gemma":[0.0011779203,0.00036357943,0.000052681116,0.000359441,0.00011456039,0.00008773964,0.000016184784,0.008127385,0.9855583,0.00007333033,0.003951606,0.00011728651],"about_ca_topic_score_codex":0.000027844528,"about_ca_topic_score_gemma":0.000004492639,"teacher_disagreement_score":0.046210404,"about_ca_system_score_codex":0.00032340916,"about_ca_system_score_gemma":0.000069291746,"threshold_uncertainty_score":0.6329944},"labels":[],"label_agreement":null},{"id":"W4408200422","doi":"10.1016/j.tsep.2025.103475","title":"Experimental investigation of integrated systems for biohydrogen and biomethane production: Effects of thermal parameters","year":2025,"lang":"en","type":"article","venue":"Thermal Science and Engineering Progress","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"","keywords":"Biohydrogen; Production (economics); Biogas production; Process engineering; Thermal; Biogas; Environmental science; Biochemical engineering; Engineering; Waste management; Chemistry; Hydrogen production; Physics; Methane; Hydrogen; Thermodynamics; Economics; Anaerobic digestion","score_opus":0.010247979400275841,"score_gpt":0.24386285792047147,"score_spread":0.23361487852019563,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408200422","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99569637,0.003240317,0.00033327908,0.000018135679,0.0002500886,0.0003997638,0.000002869758,0.000050999515,0.000008184191],"genre_scores_gemma":[0.9989882,0.0000069098637,0.00088517496,0.0000013769974,0.000017188348,0.00007653349,0.0000029079783,0.00000944557,0.00001223979],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9992386,0.000006927641,0.00019779337,0.00019809527,0.0001669351,0.00019164165],"domain_scores_gemma":[0.9996206,0.000055915996,0.00006228204,0.00012251579,0.000079864934,0.000058834077],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00042344446,0.00011464279,0.0001973248,0.0002451136,0.00003695371,0.000014025257,0.0001227891,0.000046786747,3.292536e-7],"category_scores_gemma":[0.00014820516,0.00009241428,0.000024549063,0.0006631144,0.00036127525,0.00018638337,0.000059040147,0.00005242865,6.773638e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000018445635,0.000010898406,0.0002996604,0.00082137465,0.000028953142,3.5497726e-7,0.0003840778,0.0013850871,0.9922641,0.0002455653,2.6084965e-7,0.00454125],"study_design_scores_gemma":[0.00023278219,0.00006155838,0.0007172931,0.0002778745,0.000022251272,0.000004791066,0.000078190504,0.033765115,0.9647363,0.000002640848,0.0000129549235,0.00008823951],"about_ca_topic_score_codex":0.000047494916,"about_ca_topic_score_gemma":6.145145e-8,"teacher_disagreement_score":0.032380026,"about_ca_system_score_codex":0.000050043993,"about_ca_system_score_gemma":0.000034516794,"threshold_uncertainty_score":0.37685448},"labels":[],"label_agreement":null},{"id":"W4408283418","doi":"10.1016/j.jece.2025.116129","title":"Low-temperature catalytic CO2 methanation over nickel supported on praseodymium oxide","year":2025,"lang":"en","type":"article","venue":"Journal of environmental chemical engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Concordia University","funders":"National Research Foundation of Korea","keywords":"Methanation; Praseodymium; Catalysis; Nickel; Nickel oxide; Oxide; Inorganic chemistry; Chemistry; Materials science; Chemical engineering; Environmental science; Metallurgy; Organic chemistry; Engineering","score_opus":0.003547066211393522,"score_gpt":0.20715663711930699,"score_spread":0.20360957090791346,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408283418","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99837005,0.0002626684,0.0005555776,0.00008396535,0.000327312,0.00011756253,0.00002230901,0.000054387016,0.00020618281],"genre_scores_gemma":[0.9984925,0.000025640364,0.0005896477,0.00008853031,0.00018328238,0.0000060130096,0.00004860647,0.000056683453,0.0005090963],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99806494,0.000010866298,0.0007515066,0.0002592519,0.000528692,0.0003847211],"domain_scores_gemma":[0.99908894,0.00018111759,0.00021749991,0.00028778927,0.000018161856,0.00020647538],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0002700503,0.00033799716,0.00047944568,0.00032667088,0.000029112844,0.00002043643,0.0003237115,0.00025054358,0.000090192065],"category_scores_gemma":[0.00031699674,0.00030994118,0.0003136431,0.0002859438,0.000038748232,0.00028733787,0.00010944042,0.0009316532,0.00002027288],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006228264,0.00014031628,0.000056203484,0.00010905581,0.00017780201,0.00005057961,0.00003979259,0.009193965,0.98957694,0.00009955281,0.00009596792,0.00039754293],"study_design_scores_gemma":[0.0010320031,0.000036142435,0.00053205807,0.00032523664,0.00011204588,0.00008994757,0.000039098362,0.005146768,0.99180037,0.000014078898,0.0005963138,0.00027595097],"about_ca_topic_score_codex":0.0000046968244,"about_ca_topic_score_gemma":1.7075962e-7,"teacher_disagreement_score":0.004047197,"about_ca_system_score_codex":0.0010299006,"about_ca_system_score_gemma":0.00003428999,"threshold_uncertainty_score":0.99993527},"labels":[],"label_agreement":null},{"id":"W4408542713","doi":"10.58837/chula.the.2006.1085","title":"Dry reforming of methane using dense palladium membrane supported on porous stainless steel","year":2006,"lang":"en","type":"dissertation","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Methane; Porosity; Materials science; Palladium; Membrane; Chemical engineering; Metallurgy; Composite material; Engineering; Chemistry; Catalysis; Organic chemistry","score_opus":0.01624032503438353,"score_gpt":0.27107525002918853,"score_spread":0.254834924994805,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408542713","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97457564,0.00030888425,0.00015199212,0.0000049185282,0.00064141344,0.0004865273,0.000077244156,0.0002783793,0.023475014],"genre_scores_gemma":[0.94477326,0.000035179044,0.0015146302,0.000019766001,0.00032931735,0.00003008355,0.005726405,0.00039569964,0.04717566],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99597096,0.00004359673,0.0014424515,0.0007171551,0.0010066337,0.0008191928],"domain_scores_gemma":[0.9975842,0.0001873115,0.00083926215,0.0008767158,0.00031590884,0.00019659432],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00051191857,0.000800223,0.0013739744,0.0008046321,0.000058393052,0.000017229577,0.0004651507,0.00087300764,0.00024863976],"category_scores_gemma":[0.00022609299,0.0007190547,0.0004650424,0.0005872135,0.00003799455,0.00019940856,0.00006495952,0.00082392234,0.000020678384],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028444477,0.00011317316,0.000038251615,0.001895045,0.00030155163,0.000116801,0.00039529233,0.001677252,0.9906078,0.00030741686,0.0000068862705,0.004256087],"study_design_scores_gemma":[0.0008527239,0.000061873165,0.00008249945,0.0007640546,0.00040254102,0.000023711356,0.0013966885,0.0030315886,0.99230707,0.000033638004,0.00023926714,0.00080436736],"about_ca_topic_score_codex":0.0061994754,"about_ca_topic_score_gemma":0.0014327487,"teacher_disagreement_score":0.029802367,"about_ca_system_score_codex":0.00071153295,"about_ca_system_score_gemma":0.0002580783,"threshold_uncertainty_score":0.9995261},"labels":[],"label_agreement":null},{"id":"W4408827942","doi":"10.1177/02636174251330376","title":"Role of stable Ni nano catalysts for dry reforming of methane","year":2025,"lang":"en","type":"article","venue":"Adsorption Science & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Chemistry; Catalysis; Methane; Carbon dioxide reforming; Nano-; Chemical engineering; Adsorption; Organic chemistry; Syngas","score_opus":0.008864471163475534,"score_gpt":0.2724301936346497,"score_spread":0.26356572247117416,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408827942","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9879211,0.00051571586,0.008794285,0.00013758535,0.0001720196,0.000293717,0.00001756578,0.00018802559,0.0019599425],"genre_scores_gemma":[0.99565685,0.00001553747,0.003320126,0.000007701339,0.000010005133,0.0000564874,0.0000073677024,0.000011952586,0.00091397704],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984084,0.0000055143755,0.00052365556,0.0003606635,0.00027946138,0.0004223024],"domain_scores_gemma":[0.9987077,0.00007066909,0.00024539317,0.00060851796,0.00032632184,0.000041403768],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008837761,0.00013488969,0.00038266464,0.001793293,0.000050479797,0.000003879004,0.00074256305,0.000197111,0.000008386356],"category_scores_gemma":[0.0010003177,0.00012322322,0.00009274683,0.0037247746,0.0005903933,0.00042309478,0.00028585194,0.00015015497,0.000004954584],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000015454321,0.000026460242,0.00035501068,0.0000944775,0.000016288717,1.2143116e-7,0.00007641892,0.00006510135,0.9550286,0.026256688,0.0000022398453,0.018063132],"study_design_scores_gemma":[0.00031500813,0.000039797564,0.000030590123,0.00009216361,0.00002710162,0.000004878068,0.0005761893,0.001957295,0.9895713,0.005470505,0.0018083607,0.0001068211],"about_ca_topic_score_codex":0.00023185275,"about_ca_topic_score_gemma":0.000029730072,"teacher_disagreement_score":0.034542684,"about_ca_system_score_codex":0.00022331312,"about_ca_system_score_gemma":0.00019835711,"threshold_uncertainty_score":0.5024897},"labels":[],"label_agreement":null},{"id":"W4408909384","doi":"10.1002/cjce.25683","title":"A catalytic sites contiguity study on atomically‐dispersed <scp>ZnO</scp>‐Cu/<scp>SiO<sub>2</sub></scp> catalysts to improve methanol formation from <scp>CO<sub>2</sub></scp> hydrogenation","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Western University; Université Laval; Canadian Light Source (Canada); University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; China Scholarship Council","keywords":"Catalysis; Contiguity; Methanol; Materials science; Chemical engineering; Chemistry; Organic chemistry; Computer science","score_opus":0.009531139085007951,"score_gpt":0.22300267690091954,"score_spread":0.2134715378159116,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4408909384","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99455124,0.00046663624,0.0022269024,0.00016617165,0.000698629,0.0010996246,0.00019229062,0.00020757329,0.00039094556],"genre_scores_gemma":[0.99845237,0.00001138596,0.00018709053,0.00020480192,0.0005797485,0.00009769303,0.00021799085,0.00019817377,0.00005075434],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9943171,0.00010749044,0.001919586,0.0008046758,0.0011974137,0.0016537011],"domain_scores_gemma":[0.9934172,0.0025493414,0.0006963883,0.0010969674,0.0005068449,0.0017332572],"candidate_categories":["metaresearch","metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0014648993,0.0010165866,0.0014016492,0.0014119087,0.00027436597,0.00027541848,0.0015353864,0.00060359336,0.0000023312614],"category_scores_gemma":[0.009738222,0.00092752924,0.0007183025,0.0016152553,0.00012610677,0.00079318305,0.00022474922,0.0020723196,0.00010565049],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000011803263,0.00010434339,0.00017793305,0.0001626638,0.0006985457,0.00010706493,0.0030657423,0.0062472373,0.9871042,0.00008089279,0.0007413167,0.0014982674],"study_design_scores_gemma":[0.0018340738,0.0001208134,0.00034793638,0.0004886484,0.00054380676,0.000099766236,0.00080381386,0.020301828,0.974527,0.0001509024,0.0005725113,0.00020887663],"about_ca_topic_score_codex":0.0010144586,"about_ca_topic_score_gemma":0.00094153604,"teacher_disagreement_score":0.014054592,"about_ca_system_score_codex":0.002968667,"about_ca_system_score_gemma":0.00069551065,"threshold_uncertainty_score":0.9993175},"labels":[],"label_agreement":null},{"id":"W4409317878","doi":"10.1016/j.fuel.2025.135290","title":"Power- and biomass-to-liquid processes with fuel-assisted solid oxide electrolysis cells and water gas shift-adjusted systems: A techno-economic analysis","year":2025,"lang":"en","type":"article","venue":"Fuel","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Biomass (ecology); Electrolysis; Power to gas; Water-gas shift reaction; Process engineering; Chemical engineering; Environmental science; Fuel cells; Materials science; Oxide; Chemistry; Waste management; Catalysis; Electrode; Metallurgy; Organic chemistry; Physical chemistry; Engineering","score_opus":0.004974781119287243,"score_gpt":0.2153401296789051,"score_spread":0.21036534855961786,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409317878","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9949006,0.001375303,0.0021451374,0.00020057056,0.000047789094,0.00033783502,0.000035707333,0.00028282954,0.0006742607],"genre_scores_gemma":[0.9988607,0.00006172739,0.00023318308,0.000029865278,0.000024944029,0.00011489235,0.00004563152,0.00004787982,0.0005811829],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981336,0.00001887727,0.00047128374,0.0006343499,0.00017107591,0.0005708103],"domain_scores_gemma":[0.99907213,0.00009809524,0.000098338685,0.00047409078,0.00007752279,0.0001798043],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00021191366,0.00036381796,0.00074054097,0.0009811103,0.00007493418,0.000097907265,0.0002248511,0.00018031355,0.000020890797],"category_scores_gemma":[0.00005523851,0.00026451366,0.000104404404,0.0012757233,0.00006276875,0.00018814758,0.00017531312,0.00018262741,0.00001996614],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023819187,0.000038393795,0.0008788163,0.0020916234,0.001950614,0.000020274263,0.00042699426,0.0008160429,0.9933601,0.0000658971,0.000008150444,0.00010491107],"study_design_scores_gemma":[0.0007405071,0.00013857587,0.0005136429,0.0002211143,0.0014514577,0.000034558325,0.00029657094,0.0027532117,0.9924471,0.00002571797,0.00088098773,0.0004965833],"about_ca_topic_score_codex":0.0008981574,"about_ca_topic_score_gemma":0.00060263375,"teacher_disagreement_score":0.0039601265,"about_ca_system_score_codex":0.00024768815,"about_ca_system_score_gemma":0.00007562202,"threshold_uncertainty_score":0.9999807},"labels":[],"label_agreement":null},{"id":"W4409323074","doi":"10.1016/j.cej.2025.162342","title":"Supported NiCo nanosheet catalysts for production of hydrogen-rich syngas via sequential steam gasification-catalytic reforming of wood-waste hydrochar pellets","year":2025,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Memorial University of Newfoundland; University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Canadian Light Source; University of Saskatchewan; Alberta Diabetes Foundation; Canada Research Chairs; Canada Foundation for Innovation","keywords":"Syngas; Pellets; Hydrogen production; Catalysis; Steam reforming; Syngas to gasoline plus; Nanosheet; Waste management; Chemical engineering; Methane reformer; Hydrogen; Chemistry; Materials science; Organic chemistry; Engineering","score_opus":0.010517848960114765,"score_gpt":0.2375791998700409,"score_spread":0.22706135090992613,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409323074","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9674212,0.00084773696,0.03013672,0.00009102586,0.00081062823,0.00042804502,0.00002372802,0.00012271952,0.0001182352],"genre_scores_gemma":[0.99668837,0.000038635422,0.0022987272,0.000005199464,0.00038022202,0.000041457813,0.00014011591,0.000084853455,0.00032244917],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99702656,0.000013103723,0.00142499,0.00044298262,0.00047977085,0.00061258906],"domain_scores_gemma":[0.9982105,0.00014437037,0.00050041033,0.00057539204,0.00035481868,0.00021453566],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006474788,0.00039913386,0.00077490316,0.0005493323,0.00007580677,0.000010358331,0.0005409842,0.00027600283,0.000011956926],"category_scores_gemma":[0.0011201135,0.0003925878,0.00042794837,0.0008004834,0.000092150636,0.00031296143,0.00013949981,0.0006160668,0.0000037911395],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006180983,0.00010919481,0.000019954507,0.0011042517,0.00035579977,0.000004520588,0.0002365715,0.009207139,0.9874021,0.00006163594,0.000087718414,0.0013493137],"study_design_scores_gemma":[0.00086928625,0.00003354855,0.0000046199293,0.00063756783,0.00027490663,0.00031367198,0.00010211025,0.028516442,0.96862215,0.000053890275,0.00025263257,0.0003191555],"about_ca_topic_score_codex":0.000016243202,"about_ca_topic_score_gemma":4.9906316e-7,"teacher_disagreement_score":0.029267177,"about_ca_system_score_codex":0.00048449292,"about_ca_system_score_gemma":0.00015852369,"threshold_uncertainty_score":0.9998526},"labels":[],"label_agreement":null},{"id":"W4409351524","doi":"10.1016/j.cattod.2025.115322","title":"Experimental study and statistical analysis of hydrogen yield in methane steam reforming over a hydroxyapatite-supported nickel catalyst","year":2025,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Fonds de Recherche du Québec-Société et Culture; Canada Research Chairs","keywords":"Catalysis; Steam reforming; Methane; Nickel; Methane reformer; Hydrogen; Yield (engineering); Chemistry; Hydrogen production; Chemical engineering; Nuclear chemistry; Materials science; Organic chemistry; Metallurgy; Engineering","score_opus":0.012875120488532354,"score_gpt":0.2877986744116109,"score_spread":0.27492355392307855,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409351524","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9973678,0.00077816506,0.00043151152,0.00001487101,0.000054399887,0.00042750878,0.000098186436,0.0000725523,0.0007549893],"genre_scores_gemma":[0.99858534,0.000010794842,0.00009620256,0.000022627997,0.000017320985,0.00010254762,0.00054445246,0.000038112557,0.0005825906],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99687,0.000074541436,0.0012401055,0.0007771404,0.000519994,0.0005182645],"domain_scores_gemma":[0.99813753,0.0004321478,0.00025082225,0.0009357854,0.00006215447,0.0001815679],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0008137163,0.0004071463,0.0014176217,0.001915646,0.000057760524,0.000014206622,0.00038424277,0.00018428525,0.00018724393],"category_scores_gemma":[0.000552841,0.0003787318,0.00032216424,0.003664793,0.00012491025,0.0002852458,0.0004161266,0.00034505132,0.000007006611],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012506286,0.0013313983,0.04839396,0.00013016084,0.0055347327,0.00008244037,0.0034912354,0.0007212876,0.9367414,0.00016238431,0.000008122288,0.0032777821],"study_design_scores_gemma":[0.0014365239,0.0001137066,0.0069117434,0.00008758526,0.0040179733,0.000004834637,0.0037150434,0.018845905,0.96431893,0.000016591237,0.00006586436,0.00046529784],"about_ca_topic_score_codex":0.0052701193,"about_ca_topic_score_gemma":0.0012133697,"teacher_disagreement_score":0.041482218,"about_ca_system_score_codex":0.00040062141,"about_ca_system_score_gemma":0.00007157789,"threshold_uncertainty_score":0.9998665},"labels":[],"label_agreement":null},{"id":"W4409433648","doi":"10.1016/j.ijhydene.2025.03.320","title":"Decarbonization pathways for Gas Turbines: A thermodynamic and lifecycle evaluation of hydrogen and biogas blends","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"General Electric (Canada)","funders":"King Saud University","keywords":"Biogas; Power to gas; Hydrogen; Gas turbines; Environmental science; Process engineering; Waste management; Chemistry; Engineering; Physical chemistry; Mechanical engineering; Organic chemistry","score_opus":0.012360645358682856,"score_gpt":0.2636615501031083,"score_spread":0.25130090474442546,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409433648","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.991719,0.0018962227,0.005528865,0.0001410397,0.00020762152,0.0000663493,0.000017519194,0.000011059406,0.00041230416],"genre_scores_gemma":[0.9992991,0.00018863536,0.00024768402,0.000028832674,0.00014252092,0.000009764033,0.000027732103,0.000017456103,0.000038247283],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988148,0.000028954357,0.00047642767,0.00012985503,0.00044022006,0.000109694025],"domain_scores_gemma":[0.9988598,0.00011675975,0.00030483174,0.00008952615,0.00057697773,0.000052073512],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00051942543,0.00011780987,0.00021387904,0.00036418813,0.000022603745,0.000013510136,0.00018579036,0.00007310245,0.0000088935485],"category_scores_gemma":[0.0002866163,0.000104318744,0.0001073432,0.00012977279,0.000034837918,0.00017483124,0.00006782494,0.00006462429,1.3231136e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012874222,0.000052937343,0.00044002844,0.000031523763,0.0006992907,0.000004886373,0.00020896627,0.011849037,0.9062014,0.015975228,0.000004413278,0.06440351],"study_design_scores_gemma":[0.0014692519,0.00004581306,0.000080820544,0.0001542371,0.00020502225,0.00011198842,0.000052372365,0.3473254,0.64055073,0.00952213,0.00038695475,0.000095256844],"about_ca_topic_score_codex":0.00006655497,"about_ca_topic_score_gemma":0.000022539127,"teacher_disagreement_score":0.33547637,"about_ca_system_score_codex":0.00015907302,"about_ca_system_score_gemma":0.00011722234,"threshold_uncertainty_score":0.42539948},"labels":[],"label_agreement":null},{"id":"W4409434058","doi":"10.3390/app15084248","title":"Non-Thermal Plasma-Catalytic Conversion of Biogas to Value-Added Liquid Chemicals via Ni-Fe/Al2O3 Catalyst","year":2025,"lang":"en","type":"article","venue":"Applied Sciences","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs","keywords":"Catalysis; Biogas; Chemical engineering; Materials science; Waste management; Value (mathematics); Pulp and paper industry; Chemistry; Organic chemistry; Engineering; Mathematics","score_opus":0.009323845618064078,"score_gpt":0.2451049019134996,"score_spread":0.23578105629543553,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409434058","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9782806,0.000052753123,0.00090621755,0.00015838438,0.0002430268,0.00033861524,0.000010675754,0.00010931984,0.019900417],"genre_scores_gemma":[0.99846977,0.0000026177256,0.0009037808,0.00011831122,0.00005596014,0.00003692754,0.000023406004,0.000017932005,0.00037129244],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.997835,0.0000070217175,0.00050489395,0.00058297126,0.00052930246,0.00054083066],"domain_scores_gemma":[0.99900866,0.00017158018,0.00013641991,0.00045474738,0.00005333948,0.00017523409],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006236011,0.000260648,0.0004572287,0.00037593895,0.00014973822,0.000022093902,0.00090104126,0.00014632616,0.000063360545],"category_scores_gemma":[0.0001110715,0.00022465811,0.00012674235,0.001637321,0.00036395912,0.00015831369,0.0004203017,0.0001892806,0.00017251642],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007029727,0.000036565914,0.000038636186,0.00009971168,0.000037149977,0.0000016157569,0.00028310687,0.0006449619,0.9967403,0.0013634544,0.00010172882,0.00058246],"study_design_scores_gemma":[0.00041815586,0.000049205053,0.00002674836,0.00008779248,0.000051401606,0.0000035979997,0.00030730298,0.004908439,0.9933567,0.00004809136,0.00049610157,0.0002464501],"about_ca_topic_score_codex":0.0002742057,"about_ca_topic_score_gemma":0.0000039469605,"teacher_disagreement_score":0.020189183,"about_ca_system_score_codex":0.00014599206,"about_ca_system_score_gemma":0.00011677578,"threshold_uncertainty_score":0.91612923},"labels":[],"label_agreement":null},{"id":"W4409525273","doi":"10.1016/j.ijhydene.2025.04.217","title":"Enhanced CO2 methanation over Ni-based catalysts: a comparative study on silica and alumino-silicate supports","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Ministero dell'Università e della Ricerca; Fondazione Cariplo; European Commission; Royal Society","keywords":"Methanation; Silicate; Catalysis; Aluminosilicate; Materials science; Chemical engineering; Chemistry; Organic chemistry","score_opus":0.013809962164430176,"score_gpt":0.2999489344975409,"score_spread":0.2861389723331107,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409525273","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9952824,0.00017446434,0.0021491451,0.00021400464,0.00038150023,0.00008905678,0.00001144371,0.000026477526,0.0016714911],"genre_scores_gemma":[0.99896675,0.000010314395,0.000072614224,0.00015943745,0.00013503918,0.000015504214,0.0000324076,0.00001701081,0.0005908922],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981894,0.000058026446,0.0006687733,0.00024317663,0.00066425506,0.00017635747],"domain_scores_gemma":[0.9987594,0.00021212338,0.00039214213,0.00018611658,0.00034983753,0.000100364436],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00033393523,0.00020723179,0.0003899608,0.0005170738,0.000058341124,0.000049034225,0.0003878103,0.00007102557,0.000030505054],"category_scores_gemma":[0.0001436728,0.00018049637,0.00015427443,0.00023285054,0.000046833688,0.00020684575,0.00008499674,0.0002146131,0.0000035453777],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006833237,0.000891294,0.0013067437,0.000018678904,0.002216168,0.00020127294,0.00094167294,0.010764907,0.9741354,0.0024947915,0.00022940211,0.006116373],"study_design_scores_gemma":[0.0019123039,0.00017002525,0.000566739,0.0001133959,0.00011291611,0.00004670817,0.00033472237,0.006363083,0.98849213,0.00022031702,0.0014949883,0.0001726957],"about_ca_topic_score_codex":0.00032319073,"about_ca_topic_score_gemma":0.000117481446,"teacher_disagreement_score":0.014356733,"about_ca_system_score_codex":0.00034246698,"about_ca_system_score_gemma":0.00009850474,"threshold_uncertainty_score":0.73604286},"labels":[],"label_agreement":null},{"id":"W4409589974","doi":"10.1016/j.joei.2025.102116","title":"Hydrogen production from methane dry reforming on coke-resistant Pr-doped Co/mesoporous alumina catalysts","year":2025,"lang":"en","type":"article","venue":"Journal of the Energy Institute","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Trường Đại học Nguyễn Tất Thành","keywords":"Coke; Catalysis; Hydrogen production; Carbon dioxide reforming; Methane; Mesoporous material; Hydrogen; Methane reformer; Steam reforming; Materials science; Chemical engineering; Syngas; Chemistry; Waste management; Metallurgy; Organic chemistry; Engineering","score_opus":0.01157851261214309,"score_gpt":0.25041170404700114,"score_spread":0.23883319143485804,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409589974","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99112964,0.0009547478,0.00040183842,0.0007664155,0.003147084,0.000113111615,0.000015099057,0.000059072292,0.003412979],"genre_scores_gemma":[0.9936716,0.00006683718,0.00026593907,0.0001346625,0.000848747,0.000008525054,0.000026533211,0.0000362286,0.0049409233],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99777585,0.00006573447,0.0008903593,0.00028558384,0.0006382511,0.00034419127],"domain_scores_gemma":[0.99830055,0.00007603343,0.0006500632,0.000705429,0.00014300772,0.00012491937],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000625768,0.00029750552,0.00054463436,0.00031818228,0.00016717873,0.000019980136,0.0007604517,0.00015724586,0.000009052641],"category_scores_gemma":[0.00071571016,0.00019618645,0.00039989676,0.0005601586,0.00011201061,0.00046821355,0.0001650551,0.0005677702,0.000008156083],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00039276722,0.000114610695,0.000083375795,0.00005384643,0.00069512543,0.00011619206,0.0002233416,0.010947906,0.974677,0.0016111553,0.000247923,0.010836746],"study_design_scores_gemma":[0.0006990633,0.00004401223,0.000069961476,0.0006160309,0.00025662684,0.00009685747,0.00008259285,0.00033383517,0.9627153,0.0003762324,0.034503542,0.00020592738],"about_ca_topic_score_codex":0.001366722,"about_ca_topic_score_gemma":0.00028796593,"teacher_disagreement_score":0.03425562,"about_ca_system_score_codex":0.0008525643,"about_ca_system_score_gemma":0.00025690175,"threshold_uncertainty_score":0.8000251},"labels":[],"label_agreement":null},{"id":"W4410055713","doi":"10.1016/j.jcou.2025.103096","title":"Integrated direct air CO2 capture and solid oxide electrolyzer for sustainable chemical production: Case studies of methanol and synthesis fuel","year":2025,"lang":"en","type":"article","venue":"Journal of CO2 Utilization","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada; Environment and Climate Change Canada","keywords":"Electrolysis; Sustainable production; Methanol; Production (economics); Environmental science; Oxide; Process engineering; Waste management; Materials science; Chemical engineering; Chemistry; Engineering; Metallurgy; Organic chemistry","score_opus":0.01843997111920681,"score_gpt":0.29593248469682737,"score_spread":0.27749251357762056,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410055713","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9882835,0.0066878805,0.0043005943,0.00023040194,0.00007739903,0.000237193,0.0000037974703,0.00002316733,0.00015606076],"genre_scores_gemma":[0.9981338,0.00040598627,0.00075410225,0.000011734483,0.000054266122,0.000014697568,0.0000030083793,0.00001610476,0.0006062918],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990664,0.000028130013,0.00046001183,0.00014224861,0.00012998695,0.00017321797],"domain_scores_gemma":[0.99843365,0.00030965076,0.00026008248,0.000098009186,0.0008510825,0.0000475259],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005220079,0.0001375399,0.00045047505,0.00023990787,0.000048513804,0.000009683182,0.00005527012,0.00009814967,0.000001741821],"category_scores_gemma":[0.004197005,0.000107452826,0.00007596563,0.00036056357,0.00006521763,0.0002416153,0.00003789663,0.00015638376,3.6947306e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00035279262,0.00007914488,0.00013037917,0.002140855,0.00065833837,0.000081006205,0.0006256057,0.00046877234,0.99103105,0.00066720217,0.00024218461,0.0035226578],"study_design_scores_gemma":[0.00045851184,0.000038257673,0.000011081929,0.00026889544,0.0003749909,0.0008816031,0.0021175912,0.0023638825,0.9922298,0.00042279603,0.0007376306,0.00009496822],"about_ca_topic_score_codex":0.00001675858,"about_ca_topic_score_gemma":0.0000053062395,"teacher_disagreement_score":0.009850303,"about_ca_system_score_codex":0.00017084114,"about_ca_system_score_gemma":0.00008029019,"threshold_uncertainty_score":0.50245106},"labels":[],"label_agreement":null},{"id":"W4410076866","doi":"10.1021/acs.iecr.5c00364","title":"Cu on Co Improves C<sub>5+</sub> Selectivity in the Fischer–Tropsch Synthesis","year":2025,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke; National Research Council Canada; Polytechnique Montréal","funders":"National Research Council Canada; Natural Sciences and Engineering Research Council of Canada","keywords":"Fischer–Tropsch process; Selectivity; Chemistry; Catalysis; Organic chemistry","score_opus":0.051493454419065506,"score_gpt":0.32871734499065614,"score_spread":0.27722389057159064,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410076866","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9941469,0.000075770266,0.00003012748,0.0005221677,0.00014617549,0.00040756993,0.00001964836,0.00018703834,0.0044646403],"genre_scores_gemma":[0.9984796,0.000017256047,0.0000075372222,0.000011772685,0.00065968354,0.00032176427,0.000018766532,0.00005774852,0.00042586855],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9968331,0.00011115616,0.00046510797,0.00058937154,0.0009287991,0.001072464],"domain_scores_gemma":[0.996303,0.0026046464,0.000048493705,0.00079610845,0.00010558246,0.00014213848],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0027634606,0.0003574755,0.00043182512,0.0003222279,0.00014079348,0.00009780031,0.0009309548,0.00058958214,0.00002323378],"category_scores_gemma":[0.007403528,0.00027450995,0.00016840964,0.0020006523,0.00009194171,0.0001333245,0.00019467427,0.0036019043,0.000031763237],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008859521,0.00009822935,0.00012528889,0.00018027866,0.00007035492,0.00003257644,0.000063595784,0.0020079159,0.9873166,0.00007030767,0.00041051462,0.009535739],"study_design_scores_gemma":[0.00061972364,0.000022121108,0.00012164861,0.00035593903,0.000017241024,0.000011111823,0.000094369134,0.0065091476,0.98862237,0.000017859402,0.0033386464,0.00026982898],"about_ca_topic_score_codex":0.00015563853,"about_ca_topic_score_gemma":0.000004194682,"teacher_disagreement_score":0.009265911,"about_ca_system_score_codex":0.0008366849,"about_ca_system_score_gemma":0.0002434004,"threshold_uncertainty_score":0.99997073},"labels":[],"label_agreement":null},{"id":"W4410081314","doi":"10.1002/cjce.25708","title":"Highly active and stable Ru‐promoted Ni/<scp>CeO<sub>2</sub></scp> catalysts for <scp>CO<sub>2</sub></scp> methanation reaction","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"New Energy and Industrial Technology Development Organization","keywords":"Methanation; Catalysis; Ruthenium; Chemistry; Materials science; Organic chemistry","score_opus":0.00813623470793126,"score_gpt":0.21496640881306545,"score_spread":0.20683017410513418,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410081314","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9943276,0.0007762448,0.0030639123,0.00021132539,0.0006254902,0.00043417976,0.00008145383,0.00010715593,0.00037265994],"genre_scores_gemma":[0.9986821,0.000040834806,0.0003864925,0.000057234753,0.0004655063,0.000047952213,0.00009964684,0.0001257956,0.0000944307],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971041,0.000037206897,0.00091485766,0.0004245041,0.00048109097,0.0010382031],"domain_scores_gemma":[0.9967381,0.0011757391,0.00041846433,0.00042765538,0.00041603515,0.0008240111],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00092230574,0.0005292534,0.00075861585,0.0008584449,0.00021014374,0.00011732032,0.0005449945,0.00044876832,9.844193e-7],"category_scores_gemma":[0.004132478,0.0004883401,0.00033129222,0.00093104783,0.000110834815,0.0006365057,0.00007042607,0.0012523236,0.0000063254547],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012524576,0.000018428529,0.00001427967,0.00025075546,0.00041941679,0.000024487019,0.00052979734,0.0017434687,0.99139667,0.0002858624,0.0006157791,0.0046885638],"study_design_scores_gemma":[0.0009957484,0.0000421555,0.00008147867,0.0003741059,0.0003227088,0.0002059656,0.00014960472,0.008530405,0.98602337,0.00031221707,0.0028112815,0.0001509527],"about_ca_topic_score_codex":0.000647994,"about_ca_topic_score_gemma":0.00037212184,"teacher_disagreement_score":0.0067869364,"about_ca_system_score_codex":0.0016818694,"about_ca_system_score_gemma":0.00057145406,"threshold_uncertainty_score":0.9997568},"labels":[],"label_agreement":null},{"id":"W4410333578","doi":"10.1002/cjce.25755","title":"Trade‐offs in stability and activity: A study of ordered mesoporous alumina and γ‐Al <sub>2</sub> O <sub>3</sub> supported Ni catalysts for CO <sub>2</sub> methanation","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Consejo Nacional de Ciencia y Tecnología, Paraguay; McGill University","keywords":"Methanation; Mesoporous material; Catalysis; Materials science; Chemical engineering; Stability (learning theory); Chemistry; Computer science; Organic chemistry","score_opus":0.012213794587832593,"score_gpt":0.23374795558961195,"score_spread":0.22153416100177936,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410333578","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99755526,0.00046252966,0.00051893503,0.00040783564,0.00018780663,0.0007520479,0.00006424381,0.00003904243,0.000012323626],"genre_scores_gemma":[0.9996316,0.00002273717,0.00007305702,0.000029083361,0.000089267225,0.000046660352,0.00002721749,0.00007940433,9.603078e-7],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99712926,0.00007094997,0.0011112557,0.00045214107,0.00046064073,0.00077576766],"domain_scores_gemma":[0.9977487,0.0006662899,0.0003742991,0.0004258483,0.00018213665,0.00060275785],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0015232543,0.00048676872,0.0010486239,0.00075237144,0.000098738135,0.000053635464,0.0003885206,0.00029154564,0.000001429259],"category_scores_gemma":[0.0014923268,0.0004557685,0.00020417888,0.0008397712,0.00015929833,0.00037433242,0.00008014255,0.0010094497,3.2321245e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015419578,0.0000981564,0.0004154773,0.00037968042,0.00031527548,0.000048347003,0.0013946281,0.0007566752,0.98627424,0.000028882907,0.000028435727,0.010106012],"study_design_scores_gemma":[0.0023467215,0.00011737408,0.0013579021,0.0002527826,0.00028749945,0.00014705883,0.00031921643,0.011774966,0.98291695,0.000069302296,0.000023789502,0.00038641965],"about_ca_topic_score_codex":0.00092652626,"about_ca_topic_score_gemma":0.0032982442,"teacher_disagreement_score":0.01101829,"about_ca_system_score_codex":0.0009208719,"about_ca_system_score_gemma":0.00053580693,"threshold_uncertainty_score":0.9997894},"labels":[],"label_agreement":null},{"id":"W4410345623","doi":"10.1016/j.renene.2025.123453","title":"A novel microwave heating-assisted reactor for industrial-scale syngas production","year":2025,"lang":"en","type":"article","venue":"Renewable Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Fonds de recherche du Québec – Nature et technologies; Natural Sciences and Engineering Research Council of Canada; OCP Group","keywords":"Syngas; Process engineering; Microwave; Production (economics); Microwave heating; Scale (ratio); Environmental science; Waste management; Chemistry; Engineering; Physics; Catalysis; Telecommunications","score_opus":0.024819960865969118,"score_gpt":0.24545769891142777,"score_spread":0.22063773804545866,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410345623","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.43559733,0.0010187464,0.5278722,0.0010595314,0.005065858,0.0010601918,0.00009160679,0.0013081874,0.026926322],"genre_scores_gemma":[0.908987,0.000024987678,0.007820856,0.0001110523,0.0012653285,0.00036558273,0.00032639113,0.00011030617,0.0809885],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99855715,0.000013783771,0.0004083675,0.00044834492,0.00015542643,0.00041695108],"domain_scores_gemma":[0.99913067,0.00012850633,0.00011521572,0.00043344646,0.00010598383,0.00008619979],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024009956,0.0002234391,0.00034702074,0.00020648325,0.000091865695,0.000023923212,0.00018293601,0.0002097302,0.000011616095],"category_scores_gemma":[0.0005961854,0.00021781039,0.00016873087,0.00058139354,0.000027029724,0.00013412861,0.000082852304,0.00014114036,0.0000019952454],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006118168,0.00007923026,0.00002575878,0.00007957809,0.00008784927,7.656116e-7,0.000025154648,0.010111669,0.97846705,0.0003970499,0.0009441063,0.009720628],"study_design_scores_gemma":[0.00078870554,0.000022839567,0.00000813639,0.00022256398,0.00006828982,0.000021446336,0.000051264265,0.0046742954,0.9355642,0.0001676952,0.05819713,0.0002133893],"about_ca_topic_score_codex":0.007962346,"about_ca_topic_score_gemma":0.0009881215,"teacher_disagreement_score":0.52005136,"about_ca_system_score_codex":0.0003888429,"about_ca_system_score_gemma":0.00012594288,"threshold_uncertainty_score":0.9986437},"labels":[],"label_agreement":null},{"id":"W4410619627","doi":"10.1016/j.jcou.2025.103121","title":"Pilot scale study of elevated pressure autothermal dry reforming of methane over Ni-UGSO pellets","year":2025,"lang":"en","type":"article","venue":"Journal of CO2 Utilization","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Kinova (Canada); Université de Sherbrooke","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Pellets; Methane; Methane reformer; Carbon dioxide reforming; Environmental science; Materials science; Chemistry; Catalysis; Steam reforming; Syngas; Hydrogen production; Composite material","score_opus":0.020944759856025466,"score_gpt":0.29251567625105973,"score_spread":0.2715709163950343,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410619627","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99482894,0.0006382406,0.0031876767,0.000014379247,0.00031734377,0.00020634837,0.000005033684,0.000022482549,0.00077956705],"genre_scores_gemma":[0.99858457,0.00003030685,0.00019672902,0.000007086553,0.000061672465,0.0000018150556,0.0000051552597,0.000024934461,0.0010877308],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99809563,0.000065054344,0.0010411654,0.00012525376,0.00049953413,0.00017338303],"domain_scores_gemma":[0.99838054,0.00010350477,0.00080088427,0.00025031128,0.00040948877,0.00005525954],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006399388,0.0001537265,0.00051744527,0.00040852505,0.000023431117,0.000005510419,0.0002492552,0.0000807606,0.000075376105],"category_scores_gemma":[0.0003596183,0.0001278982,0.00011996919,0.0006171538,0.000029973296,0.00028749497,0.000074966425,0.0002584778,7.279664e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004246894,0.0005990657,0.006801068,0.00041705268,0.0004138013,0.0000051329794,0.001109621,0.0071593598,0.9792059,0.000094465046,0.000028238741,0.003741608],"study_design_scores_gemma":[0.0030435394,0.00051325624,0.008286034,0.0006122925,0.0004627161,0.00001327632,0.0007077481,0.01644375,0.96912175,0.00006207554,0.0005879869,0.00014557275],"about_ca_topic_score_codex":0.00014940811,"about_ca_topic_score_gemma":0.000027549013,"teacher_disagreement_score":0.010084146,"about_ca_system_score_codex":0.00008667202,"about_ca_system_score_gemma":0.00010368171,"threshold_uncertainty_score":0.5215537},"labels":[],"label_agreement":null},{"id":"W4410844553","doi":"10.20944/preprints202505.2167.v1","title":"Process for Converting Carbon Dioxide to Graphite Using Active Metal Liquid and Its Application for Green Hydrogen Production via Methane-Steam-Reforming Reaction","year":2025,"lang":"en","type":"preprint","venue":"Preprints.org","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Steam reforming; Hydrogen production; Carbon dioxide reforming; Methane; Carbon dioxide; Hydrogen; Methane reformer; Materials science; Chemical engineering; Process (computing); Graphite; Production (economics); Waste management; Chemistry; Syngas; Metallurgy; Organic chemistry; Engineering; Computer science; Economics","score_opus":0.07108463593578943,"score_gpt":0.34675361149269435,"score_spread":0.27566897555690495,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410844553","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99245256,0.00016862682,0.00054618274,0.00014346767,0.00047656434,0.005640717,0.000085746,0.0003812982,0.0001048107],"genre_scores_gemma":[0.9951169,0.000020453908,0.00003711704,0.000018449255,0.00052165624,0.0035833553,0.00022865094,0.00012760462,0.00034583115],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9962962,0.00004933383,0.0009395218,0.0017107181,0.0003790841,0.0006251365],"domain_scores_gemma":[0.99759424,0.00009339005,0.00073071197,0.0008247984,0.0005486486,0.00020821556],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012161995,0.00062236295,0.00088565197,0.0006184169,0.00017104049,0.0000014114336,0.00043260175,0.0005454828,0.0000018524231],"category_scores_gemma":[0.0011374712,0.00068731664,0.00036306505,0.00048128242,0.00003550274,0.00035946333,0.00085690484,0.00068778533,0.0000040070922],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00068490586,0.000048039827,0.0003720373,0.0025435898,0.00048550608,5.2024916e-7,0.0013620183,0.003822587,0.98787135,0.000021511654,2.8161602e-9,0.0027879565],"study_design_scores_gemma":[0.00047438068,0.000036290578,0.000058202717,0.00057687575,0.00071174,0.000026141473,0.00023398027,0.008586558,0.98792124,0.00053828274,0.00016838135,0.00066792336],"about_ca_topic_score_codex":0.0011441853,"about_ca_topic_score_gemma":0.00006370287,"teacher_disagreement_score":0.0047639706,"about_ca_system_score_codex":0.00084072223,"about_ca_system_score_gemma":0.00015398534,"threshold_uncertainty_score":0.9995578},"labels":[{"model":"gemma","categories":[],"domain":null,"study_design":"bench_or_experimental","genre":"empirical","about_ca_system":false,"about_ca_topic":false,"confidence":"low"},{"model":"gpt","categories":[],"domain":null,"study_design":"bench_or_experimental","genre":"empirical","about_ca_system":false,"about_ca_topic":false,"confidence":"low"}],"label_agreement":"agree"},{"id":"W4410912081","doi":"10.18331/brj2025.12.2.3","title":"Biochar-supported highly dispersed ultrasmall Cu/ZnO nanoparticles as a highly efficient novel catalyst for CO2 hydrogenation to methanol","year":2025,"lang":"en","type":"article","venue":"Biofuel Research Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"European Regional Development Fund; Generalitat de Catalunya; European Commission; Ministerio de Ciencia e Innovación; Institut Català de Nanociència i Nanotecnologia","keywords":"Biochar; Catalysis; Methanol; Nanoparticle; Materials science; Chemical engineering; Nanotechnology; Chemistry; Organic chemistry; Pyrolysis","score_opus":0.04333837257890409,"score_gpt":0.34925701262498343,"score_spread":0.3059186400460793,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410912081","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9866564,0.00054068683,0.00840975,0.0021108105,0.00045149782,0.0010227012,0.000107465865,0.0001327017,0.0005679418],"genre_scores_gemma":[0.99477035,0.0000428896,0.001845347,0.0000904652,0.00031032326,0.00017986714,0.00007096924,0.000070717426,0.0026190951],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99570787,0.000103701335,0.0008373455,0.0005946357,0.0013690863,0.0013873803],"domain_scores_gemma":[0.9969641,0.0006542048,0.00015019783,0.00052308524,0.00096985255,0.0007385724],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0033636582,0.00033240835,0.00045691305,0.0011295788,0.00051006523,0.00020673519,0.000817142,0.00022801761,0.00007687335],"category_scores_gemma":[0.0042596124,0.0002827271,0.00033963964,0.001927634,0.00013950767,0.00020607834,0.00026147792,0.00082093675,0.0002271593],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033268137,0.00028823823,0.000058309863,0.00016775152,0.00023340216,0.000028286257,0.0004117156,0.000533413,0.9920978,0.0019266473,0.00025144118,0.003670321],"study_design_scores_gemma":[0.0019548477,0.00018818531,0.00007429201,0.00023280583,0.00007094979,0.00011240474,0.0005044936,0.008332855,0.976899,0.00024638968,0.011072406,0.0003113688],"about_ca_topic_score_codex":0.00026935153,"about_ca_topic_score_gemma":0.000033247557,"teacher_disagreement_score":0.0151987905,"about_ca_system_score_codex":0.0010196388,"about_ca_system_score_gemma":0.00055294787,"threshold_uncertainty_score":0.9999625},"labels":[],"label_agreement":null},{"id":"W4411189859","doi":"10.1016/j.cej.2025.164655","title":"Integrated CO2 capture and conversion to methanol: A performance comparison of alcohol-amine solvents","year":2025,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation","keywords":"Methanol; Amine gas treating; Alcohol; Chemistry; Ethanol; Process engineering; Organic chemistry; Environmental science; Chemical engineering; Engineering","score_opus":0.012314572749116173,"score_gpt":0.25690476174326543,"score_spread":0.24459018899414925,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4411189859","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9688255,0.00059526146,0.029770555,0.00008079421,0.0003575195,0.000098822384,0.0000057620864,0.00008149517,0.00018427885],"genre_scores_gemma":[0.9929149,0.000021224694,0.0067555136,0.00002431423,0.00006441905,0.0000051075917,0.000012702766,0.00002835604,0.0001734431],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99869376,0.000006527401,0.0005138363,0.00020272924,0.00024507797,0.00033804815],"domain_scores_gemma":[0.9992811,0.00009844237,0.000093279,0.00017691882,0.00011709959,0.00023316899],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021900458,0.00023663072,0.0004897714,0.00027970815,0.000035584093,0.000017255737,0.00025208778,0.00017223036,0.000022705404],"category_scores_gemma":[0.0004122895,0.00020980925,0.000108065746,0.00048627143,0.000032958924,0.00012392091,0.00015401446,0.0007398631,0.000004269274],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000058443933,0.000035084577,0.00073218223,0.00030227684,0.00010295984,0.0000040181058,0.00021341875,0.0053436025,0.9898727,0.000036109082,0.0001191276,0.0031800887],"study_design_scores_gemma":[0.0007174423,0.0000250089,0.00010178509,0.0006144597,0.000056537596,0.000049895643,0.000075170516,0.14003927,0.8563872,0.0000038793723,0.0017491585,0.0001801798],"about_ca_topic_score_codex":0.000012965271,"about_ca_topic_score_gemma":1.6012251e-7,"teacher_disagreement_score":0.13469566,"about_ca_system_score_codex":0.00021424012,"about_ca_system_score_gemma":0.00003755821,"threshold_uncertainty_score":0.8555773},"labels":[],"label_agreement":null},{"id":"W4411255358","doi":"10.1016/j.ijhydene.2025.06.038","title":"Non-thermal plasma-assisted dry reforming of methane: catalyst design, in situ characterization and hybrid system development","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Canada First Research Excellence Fund","keywords":"Methane; In situ; Carbon dioxide reforming; Characterization (materials science); Catalysis; Plasma; Thermal; Materials science; Chemical engineering; Chemistry; Environmental science; Nanotechnology; Thermodynamics; Syngas; Engineering; Physics; Organic chemistry","score_opus":0.009273703973523667,"score_gpt":0.23054807056480311,"score_spread":0.22127436659127944,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4411255358","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9738486,0.00013601281,0.025356287,0.000033834152,0.00032493987,0.00004518332,0.0000045613615,0.000013379228,0.00023719341],"genre_scores_gemma":[0.99857235,0.000020794543,0.0010424327,0.000014149213,0.000083040206,0.0000067010888,0.000047965994,0.00001884495,0.00019371204],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99828863,0.000031572523,0.00096170517,0.0001444316,0.00041090473,0.00016275086],"domain_scores_gemma":[0.999011,0.000079375364,0.000507126,0.00010456079,0.0002351639,0.000062777915],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004966766,0.00015771677,0.00036592496,0.00068534486,0.00001747214,0.000012395614,0.00034411874,0.000070127084,0.000004064059],"category_scores_gemma":[0.00007455287,0.00014068231,0.00009450579,0.00019810378,0.000023909153,0.0002811861,0.00012062733,0.00014393803,9.0051196e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014777375,0.000045220077,0.00039123706,0.00006527632,0.00038828238,0.0001269192,0.00020574823,0.0020501032,0.9601277,0.00017122984,4.5475437e-7,0.03628007],"study_design_scores_gemma":[0.00091459317,0.000016008535,0.00062558294,0.0006410272,0.00003831615,0.00027789164,0.00009242592,0.009897512,0.9869133,0.0000062680183,0.0004589544,0.00011809092],"about_ca_topic_score_codex":0.000100255565,"about_ca_topic_score_gemma":0.00003100926,"teacher_disagreement_score":0.036161978,"about_ca_system_score_codex":0.0005579228,"about_ca_system_score_gemma":0.00016292195,"threshold_uncertainty_score":0.5736858},"labels":[],"label_agreement":null},{"id":"W4411399431","doi":"10.1016/j.joei.2025.102183","title":"Investigating the effect of nickel active site position and synthesis method on performance of Ni-La-Al2O3 catalyst in the steam reforming of methane: optimization by Box Behnken Design (BBD)","year":2025,"lang":"en","type":"article","venue":"Journal of the Energy Institute","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Simon Fraser University","funders":"","keywords":"Box–Behnken design; Nickel; Catalysis; Methane; Steam reforming; Materials science; Chemistry; Chemical engineering; Response surface methodology; Nuclear chemistry; Hydrogen production; Metallurgy; Engineering; Organic chemistry; Chromatography","score_opus":0.007811019446246061,"score_gpt":0.2475471378555537,"score_spread":0.23973611840930764,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4411399431","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9650542,0.00034982516,0.033710953,0.00017007435,0.00014192608,0.00015923286,0.000010921021,0.0000053580707,0.00039747037],"genre_scores_gemma":[0.9957697,0.0001091561,0.0039914884,0.00002743022,0.00003533825,0.000012268686,0.00000425857,0.000014152434,0.000036255766],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981707,0.00047752558,0.00070242176,0.00011754231,0.00038518404,0.0001466272],"domain_scores_gemma":[0.9972383,0.0014170704,0.0009203803,0.00030213574,0.0000934483,0.000028665663],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0025992272,0.00017633628,0.00047177583,0.00019025625,0.00007421804,0.000007740627,0.00045818498,0.00011051249,8.185556e-7],"category_scores_gemma":[0.0012285903,0.00008799541,0.00015996282,0.0005722549,0.00016716374,0.00036951262,0.000105485364,0.00036904562,5.1691114e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022462157,0.000034928915,0.00013897438,0.00020762722,0.00022619138,0.0000013913104,0.0007089509,0.43057978,0.5522026,0.00030113457,0.000006317842,0.015367513],"study_design_scores_gemma":[0.00053022546,0.00014049654,0.00007884233,0.0012268791,0.0003087942,0.000058974118,0.00014003256,0.04476564,0.9526195,0.000032143074,0.000023097145,0.000075411066],"about_ca_topic_score_codex":0.0004197401,"about_ca_topic_score_gemma":0.00001141014,"teacher_disagreement_score":0.40041688,"about_ca_system_score_codex":0.00016006817,"about_ca_system_score_gemma":0.00007793606,"threshold_uncertainty_score":0.35883486},"labels":[],"label_agreement":null},{"id":"W4412027779","doi":"10.1016/j.ijhydene.2025.150185","title":"Comparative minimization of CO2 emissions of methanol synthesis via tri-reforming and gas-heated reforming of methane","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada; Lakehead University","keywords":"Methane; Steam reforming; Carbon dioxide reforming; Methanol; Methane reformer; Syngas; Environmental science; Natural gas; Chemistry; Chemical engineering; Waste management; Hydrogen; Hydrogen production; Organic chemistry; Engineering","score_opus":0.013361168594507032,"score_gpt":0.27788507655971967,"score_spread":0.26452390796521263,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4412027779","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9899581,0.000911079,0.00797811,0.00008704362,0.00019837116,0.0000494334,0.00002919725,0.000010168097,0.00077850325],"genre_scores_gemma":[0.9981143,0.00019040274,0.0014684583,0.000009132365,0.000052395066,0.000003797567,0.000014087507,0.000016539938,0.00013092191],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977837,0.000060476366,0.0013212499,0.00013916467,0.00054325303,0.00015211388],"domain_scores_gemma":[0.9974047,0.00046394998,0.001143292,0.0001527391,0.00075199467,0.000083356055],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00042486135,0.00017670111,0.00073711923,0.00082021725,0.0000179333,0.0000034059012,0.00040125524,0.000116487194,0.00003915507],"category_scores_gemma":[0.0005527678,0.0001436877,0.00025129874,0.00039378463,0.00009162116,0.0002571719,0.0001301245,0.00015212563,1.8776916e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024005372,0.000100215504,0.00016212686,0.00007329917,0.0011529669,0.00000910664,0.0004247866,0.0056169475,0.97508043,0.00066266424,0.0000033913957,0.016473984],"study_design_scores_gemma":[0.00072984037,0.000051215284,0.000040108665,0.0007564383,0.00020482557,0.00011977505,0.00035020008,0.010709019,0.9862809,0.00036249554,0.00028899548,0.00010616218],"about_ca_topic_score_codex":0.00034012087,"about_ca_topic_score_gemma":0.000019342811,"teacher_disagreement_score":0.016367821,"about_ca_system_score_codex":0.00016984745,"about_ca_system_score_gemma":0.00011614606,"threshold_uncertainty_score":0.5859415},"labels":[],"label_agreement":null},{"id":"W4412513825","doi":"10.3390/en18143846","title":"Biofuels Production Using Structured Catalyst in Fischer–Tropsch Synthesis","year":2025,"lang":"en","type":"article","venue":"Energies","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"European Commission; Université de Sherbrooke","keywords":"Fischer–Tropsch process; Catalysis; Production (economics); Biofuel; Business; Chemistry; Waste management; Engineering; Economics; Organic chemistry","score_opus":0.012290419342838928,"score_gpt":0.2558859005198894,"score_spread":0.2435954811770505,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4412513825","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9977277,0.00052251027,0.00016794291,0.00010970743,0.0004253553,0.000083320665,0.000004602752,0.00014538981,0.0008134693],"genre_scores_gemma":[0.99734896,0.000015802636,0.0014349342,0.000009385658,0.00012045736,0.000024314793,0.000012352254,0.000023906467,0.001009901],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990097,0.000021421176,0.0002738664,0.00029229478,0.00013809155,0.00026457987],"domain_scores_gemma":[0.9994848,0.00006705231,0.000051688723,0.0003366181,0.00003053273,0.000029324257],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014582415,0.00016607268,0.00025175555,0.0003302883,0.000050515584,0.000016920969,0.00016781734,0.00011055874,0.000023137085],"category_scores_gemma":[0.00059361407,0.0001524118,0.00007433907,0.0006691443,0.000038043734,0.00020553323,0.000093224284,0.00017584555,0.000004847533],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001334284,0.00001263773,0.0007544038,0.00011249731,0.00004294965,0.0000047517315,0.00015450442,0.036464676,0.95568687,0.000528021,0.000013500538,0.0062118764],"study_design_scores_gemma":[0.00011300884,0.0000017887658,0.00045379967,0.00014608391,0.00003570907,0.00000742958,0.00021946433,0.0030846633,0.9946382,0.00021743012,0.0009199886,0.00016242037],"about_ca_topic_score_codex":0.00075143063,"about_ca_topic_score_gemma":0.0001546491,"teacher_disagreement_score":0.038951375,"about_ca_system_score_codex":0.0002400276,"about_ca_system_score_gemma":0.0000402509,"threshold_uncertainty_score":0.62151724},"labels":[],"label_agreement":null},{"id":"W4412582168","doi":"10.2139/ssrn.5362718","title":"Toward Electrified Co2-Free Hydrogen Production: A Multiphysics Model Investigating Microwave-Driven Methane Pyrolysis in Fluidized Beds","year":2025,"lang":"en","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Multiphysics; Methane; Pyrolysis; Production (economics); Hydrogen; Hydrogen production; Microwave; Fluidized bed; Nuclear engineering; Environmental science; Process engineering; Waste management; Physics; Chemistry; Engineering; Thermodynamics; Organic chemistry; Economics; Telecommunications","score_opus":0.021778007747581467,"score_gpt":0.25751464395632484,"score_spread":0.23573663620874338,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4412582168","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96685565,0.006973841,0.02230317,0.0015052744,0.00052178785,0.0010033996,0.000043934764,0.00035621156,0.00043674497],"genre_scores_gemma":[0.9872585,0.0033650803,0.0059645157,0.00007847284,0.0011006455,0.0001899509,0.00019406542,0.00020196168,0.0016468146],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9919367,0.00021906618,0.0016652046,0.001222044,0.00092365843,0.0040333383],"domain_scores_gemma":[0.99697113,0.00014518641,0.00084194815,0.0013579492,0.00040278203,0.00028102394],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.0030435056,0.0009905023,0.0016099245,0.001013712,0.00016055224,0.00007130454,0.0019220014,0.0008503799,0.000007296159],"category_scores_gemma":[0.0022584712,0.0010240639,0.0009233559,0.0012457023,0.000105320556,0.0003248397,0.0011729787,0.012577646,0.000009793631],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":true,"study_design_scores_codex":[0.00012726597,0.00012223184,0.00006144055,0.00036967685,0.0013872258,0.000013944218,0.00109921,0.14032191,0.8458071,0.003936454,0.000018850891,0.0067347246],"study_design_scores_gemma":[0.0019707815,0.000046119923,9.405478e-7,0.0006373181,0.0005214438,0.00026927306,0.00032881735,0.14652027,0.7099981,0.1387873,0.000027525997,0.0008921372],"about_ca_topic_score_codex":0.00051629817,"about_ca_topic_score_gemma":0.0008659992,"teacher_disagreement_score":0.13580899,"about_ca_system_score_codex":0.00674288,"about_ca_system_score_gemma":0.007069692,"threshold_uncertainty_score":0.99922097},"labels":[],"label_agreement":null},{"id":"W4413011849","doi":"10.1016/s1872-2067(25)64743-7","title":"Interface engineering of oxygen-vacancy-rich MgO/Ni@NiAlO enables low-temperature coke-free methane dry reforming","year":2025,"lang":"en","type":"article","venue":"CHINESE JOURNAL OF CATALYSIS (CHINESE VERSION)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"National Key Research and Development Program of China; Jiangsu Provincial Key Research and Development Program; Natural Science Foundation of Jiangsu Province; National Natural Science Foundation of China","keywords":"Coke; Methane; Carbon dioxide reforming; Materials science; Interface (matter); Oxygen; Chemical engineering; Methane reformer; Metallurgy; Catalysis; Syngas; Chemistry; Composite material; Steam reforming; Engineering; Organic chemistry; Hydrogen production","score_opus":0.003002303098086717,"score_gpt":0.23056895806573038,"score_spread":0.22756665496764367,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413011849","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99117976,0.0050199353,0.0011444096,0.00029692776,0.0015291353,0.00019484936,0.0000537136,0.0001008075,0.00048043506],"genre_scores_gemma":[0.9959946,0.00022276839,0.001560275,0.0000406738,0.00052930304,0.000007357423,0.000080712496,0.00010305528,0.001461232],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9956576,0.00007160257,0.0020166067,0.00050539646,0.0010857878,0.0006629852],"domain_scores_gemma":[0.99598736,0.0005175154,0.0010212174,0.0013060343,0.0008182787,0.00034960313],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012978633,0.0008349545,0.001980711,0.0019284826,0.00013188961,0.00004841648,0.001838562,0.00041841078,0.00013230252],"category_scores_gemma":[0.00422874,0.00056978187,0.0010729044,0.0036505866,0.00008962334,0.0011964084,0.0008489384,0.0013660142,0.00002057372],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004148547,0.00018407757,0.0055521554,0.0010827426,0.0014070987,0.000116263334,0.00091505336,0.012016249,0.97724617,0.00003593447,0.00018835143,0.00084107864],"study_design_scores_gemma":[0.005290392,0.00016044856,0.0043909224,0.0025547536,0.0010917688,0.000364458,0.00055070576,0.007793861,0.9749074,0.00039307706,0.0014103425,0.0010918945],"about_ca_topic_score_codex":0.00017931499,"about_ca_topic_score_gemma":0.000044723158,"teacher_disagreement_score":0.0048755375,"about_ca_system_score_codex":0.00076944486,"about_ca_system_score_gemma":0.00035738826,"threshold_uncertainty_score":0.9996754},"labels":[],"label_agreement":null},{"id":"W4413387839","doi":"10.1016/j.cattod.2025.115504","title":"Kinetic modelling of tri-reforming of methane for the production of synthesis gas over 5 wt.% Ni/ZrO2 catalyst","year":2025,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Science and Engineering Research Board; Ministry of Education, India; Department of Science and Technology, Ministry of Science and Technology, India","keywords":"Catalysis; Methane; Methane reformer; Syngas; Kinetic energy; Chemistry; Production (economics); Catalytic reforming; Heterogeneous catalysis; Chemical engineering; Steam reforming; Hydrogen production; Organic chemistry; Physics; Engineering; Economics","score_opus":0.01956171649992897,"score_gpt":0.2524174443075511,"score_spread":0.23285572780762212,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413387839","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95256263,0.0024726947,0.04304295,0.0001705177,0.00044015585,0.0007318128,0.00007733319,0.00006126856,0.00044061968],"genre_scores_gemma":[0.9975198,0.00010476294,0.0009771732,0.00000456074,0.000088434856,0.00013166606,0.00005891843,0.000044458127,0.0010702276],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99767154,0.000031617594,0.0011332815,0.00041783464,0.00040109735,0.00034464055],"domain_scores_gemma":[0.9970621,0.0009876164,0.0005735803,0.0010767253,0.00024717706,0.00005280042],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010920188,0.00028086916,0.00092494086,0.0004979443,0.000055417222,0.000004575328,0.0005268106,0.0001568118,0.000021701977],"category_scores_gemma":[0.0019278973,0.00020420733,0.0005952534,0.0012607115,0.00015753589,0.00018972957,0.0001399021,0.00018387499,0.0000015592636],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014561476,0.00011495999,0.00008976815,0.0013464463,0.0009880561,4.2538915e-7,0.00065126515,0.04337344,0.9263446,0.000458131,0.000022058228,0.026465246],"study_design_scores_gemma":[0.0003021315,0.000019288378,0.000025843374,0.0004141817,0.0014553547,0.0000032690698,0.00031913517,0.041568507,0.95523375,0.00012764912,0.00035619843,0.00017466806],"about_ca_topic_score_codex":0.0011020142,"about_ca_topic_score_gemma":0.000041688207,"teacher_disagreement_score":0.04495715,"about_ca_system_score_codex":0.00015014921,"about_ca_system_score_gemma":0.00007886408,"threshold_uncertainty_score":0.83273333},"labels":[],"label_agreement":null},{"id":"W4413435275","doi":"10.3390/catal15080795","title":"High-Pressure Catalytic Ethanol Reforming for Enhanced Hydrogen Production Using Efficient and Stable Nickel-Based Catalysts","year":2025,"lang":"en","type":"article","venue":"Catalysts","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta; University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation","keywords":"Catalysis; Nickel; Hydrogen production; Steam reforming; Catalytic reforming; Ethanol; Chemistry; Materials science; Organic chemistry","score_opus":0.01201788639056137,"score_gpt":0.25782248653373524,"score_spread":0.24580460014317387,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413435275","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98492604,0.0018443791,0.010350278,0.00019069063,0.0007881377,0.0012718167,0.00009303639,0.00035133242,0.0001842945],"genre_scores_gemma":[0.9961285,0.000006845847,0.0010628413,0.000038054673,0.00020855913,0.00021167715,0.0005157439,0.00010125637,0.0017265094],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9969423,0.000029725998,0.00074643985,0.0010456862,0.00038274768,0.00085311884],"domain_scores_gemma":[0.99804026,0.0001608476,0.00027006443,0.0010822779,0.00024068204,0.00020585614],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00064540916,0.00051562575,0.00074024027,0.0005413614,0.00032973854,0.00004090058,0.0004113456,0.00030249017,0.0000043373466],"category_scores_gemma":[0.00080066524,0.0004982641,0.00022801566,0.0009492653,0.00013784211,0.000309763,0.00024494567,0.00034446537,0.0000138272935],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010708757,0.00007538848,0.000036780395,0.0013036095,0.00025593568,0.000004500022,0.00028585372,0.03067201,0.96427464,0.00013829576,0.000038134363,0.0028077809],"study_design_scores_gemma":[0.0011653199,0.000023599103,0.000014979443,0.00047553942,0.0005669808,0.00002089774,0.00012339465,0.046146553,0.9501959,0.000057906098,0.0007053075,0.00050361024],"about_ca_topic_score_codex":0.00064086553,"about_ca_topic_score_gemma":0.000052223295,"teacher_disagreement_score":0.015474543,"about_ca_system_score_codex":0.0005839878,"about_ca_system_score_gemma":0.00024031488,"threshold_uncertainty_score":0.9997469},"labels":[],"label_agreement":null},{"id":"W4413677430","doi":"10.1016/j.jechem.2025.08.032","title":"Advances in Cu-based catalysts for methanol steam reforming: Mechanistic insights and atomic-level design","year":2025,"lang":"en","type":"article","venue":"Journal of Energy Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Petro-Canada","funders":"Fundamental Research Funds for the Central Universities; National Natural Science Foundation of China","keywords":"Steam reforming; Methanol; Catalysis; Chemical engineering; Materials science; Process engineering; Nanotechnology; Chemistry; Engineering; Hydrogen production; Organic chemistry","score_opus":0.015108685535370725,"score_gpt":0.2597207426126571,"score_spread":0.24461205707728637,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413677430","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5687747,0.019778477,0.40528235,0.00017306852,0.00057358446,0.00026099765,0.000027798073,0.00008710894,0.00504191],"genre_scores_gemma":[0.9943122,0.00027416245,0.0045992886,0.00003604242,0.00011966088,0.000022469318,0.000013881731,0.000032165208,0.0005901033],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985756,0.000016397044,0.0006910411,0.00022159866,0.00021382632,0.00028150273],"domain_scores_gemma":[0.99879456,0.00037170795,0.00034696513,0.00021417691,0.00014926422,0.00012334419],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00036959178,0.00023276111,0.0005072657,0.00021329965,0.000043045744,0.000011776949,0.0002818662,0.00019134984,0.0000040481345],"category_scores_gemma":[0.00053239655,0.0001963684,0.0001566387,0.00029839587,0.000035999492,0.00024861356,0.000055958797,0.00026311603,1.9571632e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022425638,0.00005892899,0.0000149127145,0.0004884117,0.00006804412,0.00003210363,0.00003833062,0.0017170236,0.98853844,0.000523406,0.000015303132,0.008280851],"study_design_scores_gemma":[0.0016161283,0.000029182562,0.0000025584382,0.000524329,0.000082647945,0.000059809718,0.0000919315,0.0076017054,0.9838582,0.0026461892,0.0032859743,0.00020131179],"about_ca_topic_score_codex":0.000020699641,"about_ca_topic_score_gemma":0.000013657924,"teacher_disagreement_score":0.42553753,"about_ca_system_score_codex":0.00038644776,"about_ca_system_score_gemma":0.00022002125,"threshold_uncertainty_score":0.8007671},"labels":[],"label_agreement":null},{"id":"W4413743187","doi":"10.1016/j.ccr.2025.217096","title":"A century of evolution: Progress and milestones in fischer-tropsch synthesis","year":2025,"lang":"en","type":"article","venue":"Coordination Chemistry Reviews","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":22,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Canada First Research Excellence Fund","keywords":"Chemistry; Fischer–Tropsch process; Catalysis; Organic chemistry","score_opus":0.010779764273207858,"score_gpt":0.2702347453366192,"score_spread":0.2594549810634113,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413743187","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.77060694,0.21610953,0.0018276706,0.00096461404,0.00016621329,0.00086093694,0.000018693903,0.00012527434,0.009320158],"genre_scores_gemma":[0.99668825,0.0013457314,0.0007414724,0.0000066083835,0.000036273566,0.00018504095,0.000016038292,0.000012062185,0.0009685091],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990765,0.000022016056,0.00045681643,0.0002106202,0.00009541841,0.00013865961],"domain_scores_gemma":[0.9994602,0.00008168967,0.00013762158,0.00022757026,0.000056722794,0.00003618204],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00032004848,0.00013318725,0.0003720651,0.00006495465,0.000020325893,0.0000056602303,0.0001302737,0.00010023825,0.00004284606],"category_scores_gemma":[0.0008297065,0.00012213257,0.00007857598,0.00046520104,0.00005888332,0.00008625335,0.0000710136,0.00013037393,0.000002864321],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000013315052,0.000088461864,0.007983582,0.0060081338,0.000030898806,0.000002212773,0.000075341646,0.000008574358,0.86415863,0.0006419139,0.00018232924,0.1208066],"study_design_scores_gemma":[0.00043937098,0.000004688045,0.0011679708,0.0025006665,0.00007537396,0.000012045501,0.0000945232,0.0011318378,0.90746313,0.00008724069,0.08677868,0.00024445853],"about_ca_topic_score_codex":0.000011654723,"about_ca_topic_score_gemma":0.0000015564682,"teacher_disagreement_score":0.22608136,"about_ca_system_score_codex":0.00014914636,"about_ca_system_score_gemma":0.000026843783,"threshold_uncertainty_score":0.49804217},"labels":[],"label_agreement":null},{"id":"W4413815139","doi":"10.1021/acsanm.5c03165","title":"Cu–Al–Zn/Magnetite Nanoparticle Composite Catalysts for Steam Reforming of MeOH by Magnetic Induction","year":2025,"lang":"en","type":"article","venue":"ACS Applied Nano Materials","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut interdisciplinaire d'innovation technologique; Université de Sherbrooke","funders":"Fonds de recherche du Québec – Nature et technologies; Canada Research Chairs; Centre québécois sur les matériaux fonctionnels","keywords":"Magnetite; Composite number; Catalysis; Nanoparticle; Steam reforming; Materials science; Magnetite Nanoparticles; Chemical engineering; Magnetic nanoparticles; Metallurgy; Methanol; Nuclear chemistry; Chemistry; Composite material; Nanotechnology; Hydrogen production; Engineering; Organic chemistry","score_opus":0.007599345949488423,"score_gpt":0.23804758215115346,"score_spread":0.23044823620166505,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413815139","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99662435,0.00042645924,0.00010928911,0.000105990126,0.0004659275,0.00078701554,0.00015667194,0.00016550197,0.0011588207],"genre_scores_gemma":[0.9979657,0.00004051985,0.0004301184,0.0000850546,0.0000804485,0.00029483996,0.0002778908,0.000060942675,0.00076449325],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979366,0.0000204474,0.0008698511,0.0004304129,0.00024936174,0.0004933395],"domain_scores_gemma":[0.99894375,0.000095506555,0.0002587001,0.000534773,0.00008705365,0.000080236416],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005046291,0.00030139714,0.0006317565,0.00022313595,0.00010419783,0.000031151732,0.0003339301,0.00019345163,0.000056017154],"category_scores_gemma":[0.000072274175,0.00028352762,0.000082180595,0.0004575237,0.00007408563,0.00017235846,0.00019446794,0.00009390409,0.000027192098],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017966544,0.00006524668,0.000006847419,0.00044441974,0.00005906518,5.8391066e-7,0.00011308837,0.000015812362,0.9906252,0.0018167621,0.0003873126,0.006285988],"study_design_scores_gemma":[0.0011950706,0.000059785114,0.000017748564,0.00012077946,0.00012333183,0.0000052501723,0.0000890687,0.000027308293,0.9924494,0.00027916592,0.0053530326,0.00028003717],"about_ca_topic_score_codex":0.00030122692,"about_ca_topic_score_gemma":0.000007473968,"teacher_disagreement_score":0.0060059507,"about_ca_system_score_codex":0.00017056697,"about_ca_system_score_gemma":0.00003741115,"threshold_uncertainty_score":0.9999617},"labels":[],"label_agreement":null},{"id":"W4413840685","doi":"10.1016/j.ijhydene.2025.151120","title":"Methane pyrolysis over activated biochar and red mud-biochar composite catalysts for turquoise hydrogen production","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada; Western University","keywords":"Biochar; Pyrolysis; Catalysis; Hydrogen production; Methane; Red mud; Composite number; Hydrogen; Chemistry; Pulp and paper industry; Waste management; Materials science; Organic chemistry; Composite material","score_opus":0.008175309415776556,"score_gpt":0.2544479736316587,"score_spread":0.24627266421588218,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413840685","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99488246,0.0018817072,0.0012982864,0.00091254944,0.000721133,0.00009836829,0.000039006998,0.000044033375,0.00012242116],"genre_scores_gemma":[0.9977518,0.00015763585,0.00043268703,0.00009955134,0.00053146016,0.000016982844,0.000115326475,0.000039196173,0.0008553702],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982416,0.000031170737,0.00070239254,0.00029917207,0.00048001594,0.00024566526],"domain_scores_gemma":[0.9986531,0.0001100156,0.00044973247,0.00020942675,0.00045024318,0.00012745667],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035378762,0.00024277584,0.0004185202,0.0006993669,0.000050043156,0.00002666475,0.00043862464,0.00013314742,0.00002306342],"category_scores_gemma":[0.0003055235,0.00021954264,0.00031885985,0.00030802522,0.000049963463,0.00036601996,0.00013699208,0.00018809008,0.000002243321],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00042189064,0.000081836595,0.00009879682,0.000027885768,0.0017223255,0.000028435903,0.00007232743,0.0019437502,0.988664,0.00040069773,0.0001438349,0.0063942415],"study_design_scores_gemma":[0.0012345526,0.000037516387,0.000026701353,0.00016353354,0.00023294178,0.00029405806,0.000020534098,0.0015834214,0.98807955,0.000591382,0.007539264,0.00019655026],"about_ca_topic_score_codex":0.00018384856,"about_ca_topic_score_gemma":0.000017009139,"teacher_disagreement_score":0.007395429,"about_ca_system_score_codex":0.0003152467,"about_ca_system_score_gemma":0.00006961201,"threshold_uncertainty_score":0.89526886},"labels":[],"label_agreement":null},{"id":"W4413963157","doi":"10.1016/j.biombioe.2025.108324","title":"Process design, techno-economic, and life cycle assessment of methanol production routes","year":2025,"lang":"en","type":"article","venue":"Biomass and Bioenergy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Concordia University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Production (economics); Process (computing); Life-cycle assessment; Methanol; Process engineering; Manufacturing engineering; Computer science; Engineering; Economics; Chemistry; Organic chemistry; Microeconomics","score_opus":0.011830608685126255,"score_gpt":0.27037764572833434,"score_spread":0.2585470370432081,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4413963157","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99213713,0.00082646846,0.005936598,0.00037044377,0.00013470933,0.00013290085,0.000006036492,0.00008437884,0.0003713206],"genre_scores_gemma":[0.99797773,0.00008429772,0.0016665251,0.000008386944,0.00004620842,0.000030088177,0.000006684359,0.000010856714,0.00016923108],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99931395,0.000009539616,0.00022151163,0.00024844863,0.00006757058,0.00013897747],"domain_scores_gemma":[0.999671,0.000029618857,0.000074926196,0.00014612771,0.000029393215,0.000048950187],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017295234,0.00012016242,0.00021019811,0.0001589061,0.00003730637,0.0000109967,0.00007432711,0.000087650755,0.0000042583843],"category_scores_gemma":[0.000054073622,0.000098452874,0.000030507676,0.00016287339,0.00005869384,0.00009830097,0.0000722508,0.000047958085,2.6776502e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001247412,0.000028567574,0.00076523557,0.0002723505,0.00009492084,5.686553e-7,0.000024053299,0.00047792614,0.9785314,0.0021137325,0.0000070094734,0.017671766],"study_design_scores_gemma":[0.00021733284,0.000028939512,0.00050135894,0.000060578663,0.000037056558,0.0000044848935,0.000077537035,0.0214713,0.9767531,0.000334287,0.000395654,0.000118381075],"about_ca_topic_score_codex":0.00028860368,"about_ca_topic_score_gemma":0.000013252779,"teacher_disagreement_score":0.020993374,"about_ca_system_score_codex":0.00004968527,"about_ca_system_score_gemma":0.000050182818,"threshold_uncertainty_score":0.40147918},"labels":[],"label_agreement":null},{"id":"W4414102039","doi":"10.1002/cjce.70082","title":"Catalytic transfer hydrogenation of nitrobenzene through the dehydrogenation of 1,2‐butanediol over Cu/SiO <sub>2</sub> catalyst","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Nitrobenzene; Dehydrogenation; Catalysis; Aniline; Transfer hydrogenation; Fourier transform infrared spectroscopy; Hydrogen; Hydrogen production","score_opus":0.006513211172854308,"score_gpt":0.2005567618780838,"score_spread":0.1940435507052295,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414102039","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99397886,0.0009951078,0.004137291,0.0002790314,0.00022067841,0.00016109647,0.000025292597,0.000016498341,0.00018617004],"genre_scores_gemma":[0.9996877,0.00001140853,0.00007062226,0.000033375818,0.00012711607,0.000005697268,0.000016658254,0.000038368922,0.000009058104],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981721,0.000018698709,0.00088819274,0.00014171502,0.00040601208,0.00037329062],"domain_scores_gemma":[0.998769,0.00027506388,0.00019525652,0.0003570708,0.00022776582,0.00017584082],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00048601834,0.0002352244,0.00045983016,0.00028150156,0.000060857285,0.00001565989,0.0006115852,0.00016625352,0.000008237395],"category_scores_gemma":[0.0005434307,0.00016435591,0.00033053596,0.0007516523,0.00011840416,0.00022408388,0.000032499454,0.0005641083,0.0000014773516],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00001696544,0.000010515378,0.0000275844,0.00016210698,0.00023952418,0.0000074853647,0.0005448781,0.034352507,0.9621964,0.001614931,0.000017425005,0.00080969423],"study_design_scores_gemma":[0.00043238272,0.000013827371,0.000028423556,0.00029983927,0.00022177049,0.00010618453,0.000032369313,0.019265449,0.9790509,0.00021893512,0.00018506564,0.00014490662],"about_ca_topic_score_codex":0.001601676,"about_ca_topic_score_gemma":0.00035599997,"teacher_disagreement_score":0.016854463,"about_ca_system_score_codex":0.0005078022,"about_ca_system_score_gemma":0.00039161582,"threshold_uncertainty_score":0.67022395},"labels":[],"label_agreement":null},{"id":"W4414293285","doi":"10.52825/solarpaces.v3i.2449","title":"Modeling of an High-Concentration Solar Reactor for Dry Methane Reforming","year":2025,"lang":"en","type":"article","venue":"SolarPACES Conference Proceedings","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"Université de Sherbrooke","funders":"Fonds de recherche du Québec – Nature et technologies; HORIZON EUROPE Framework Programme; European Commission; Natural Sciences and Engineering Research Council of Canada; Mitacs; European Climate, Infrastructure and Environment Executive Agency","keywords":"Methane; Steam reforming; Solar energy; Heat flux; Concentrated solar power; Plug flow reactor model; Work (physics); Flux (metallurgy)","score_opus":0.019587606026037242,"score_gpt":0.26946485847121154,"score_spread":0.2498772524451743,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414293285","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.936344,0.00012993863,0.061492454,0.00011946349,0.0001992176,0.00047627522,0.00002339435,0.0002078426,0.0010073598],"genre_scores_gemma":[0.99152017,0.000026687205,0.007823691,0.00002600066,0.00010967453,0.00009136436,0.00005080094,0.00003873809,0.00031286824],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99814814,0.000006404942,0.0006075907,0.0004700949,0.000279018,0.0004887552],"domain_scores_gemma":[0.99878985,0.000058168393,0.00020382341,0.00021162986,0.0006164133,0.000120097786],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00061440986,0.00028281906,0.0005101753,0.00019300776,0.00008371586,0.000052509018,0.00040298587,0.00024247242,0.000015664087],"category_scores_gemma":[0.0005783586,0.00026367942,0.00014175467,0.00036627424,0.000054351833,0.0015194439,0.00009995081,0.00029569416,0.0000020173188],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000121976125,0.000042314445,0.00019092923,0.000716196,0.00008517293,3.5942452e-7,0.0014617912,0.00022754389,0.9682206,0.018830445,0.0000014068287,0.010101274],"study_design_scores_gemma":[0.0004891633,0.000054088592,0.000005054916,0.000228978,0.00007147653,0.0000014319187,0.0013549565,0.40468475,0.59005624,0.0027510638,0.000114623836,0.00018818481],"about_ca_topic_score_codex":0.00036136262,"about_ca_topic_score_gemma":0.000027367021,"teacher_disagreement_score":0.4044572,"about_ca_system_score_codex":0.00016519614,"about_ca_system_score_gemma":0.00015012063,"threshold_uncertainty_score":0.9999815},"labels":[],"label_agreement":null},{"id":"W4414421896","doi":"10.1002/cjce.70078","title":"A new green synthesis approach using sodium palmitate in the synthesis of a Ni/ <scp> Al <sub>2</sub> O <sub>3</sub> </scp> catalyst for <scp> CO <sub>2</sub> </scp> methanation","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Methanation; Catalysis; Nickel; Space velocity; Substitute natural gas; Selectivity; Dispersion (optics); Syngas","score_opus":0.01444868650818916,"score_gpt":0.22170856817217383,"score_spread":0.20725988166398468,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414421896","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97959775,0.0010176057,0.017470881,0.0003923667,0.0003474762,0.0007304174,0.0001270246,0.000077965145,0.00023848594],"genre_scores_gemma":[0.9974179,0.00004387682,0.0015334542,0.00012479248,0.0005000837,0.000118379125,0.000040276856,0.00020779243,0.000013421555],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9947077,0.00016117549,0.0018749988,0.0006347313,0.000984691,0.0016366869],"domain_scores_gemma":[0.9920008,0.005066464,0.00079540914,0.0008694941,0.00037794124,0.000889902],"candidate_categories":["metaresearch","metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0030856666,0.00088222796,0.0015033417,0.001485121,0.000221607,0.00014818985,0.0017230768,0.00056999543,0.0000013669894],"category_scores_gemma":[0.009698915,0.00073161325,0.0009067299,0.0019585043,0.00020515965,0.0005300331,0.0001395262,0.0016425664,0.0000053073336],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002069741,0.000047638892,0.000047160564,0.00060141017,0.0006016699,0.000050340106,0.0011597283,0.017642522,0.9701718,0.00022240025,0.00035339006,0.009081248],"study_design_scores_gemma":[0.0007784195,0.000027202272,0.0000599155,0.00092768687,0.00074216095,0.00033741049,0.00045368136,0.05052501,0.9453329,0.00019299662,0.00037307324,0.00024956328],"about_ca_topic_score_codex":0.0016997064,"about_ca_topic_score_gemma":0.0006785929,"teacher_disagreement_score":0.032882486,"about_ca_system_score_codex":0.0015852588,"about_ca_system_score_gemma":0.0012033657,"threshold_uncertainty_score":0.9995135},"labels":[],"label_agreement":null},{"id":"W4414553721","doi":"10.1002/cjce.70096","title":"A review using data‐driven approach in quantitative assessment of Fischer–Tropsch synthesis","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Process (computing); Variance (accounting); Production (economics); Work (physics); Supply chain; Product (mathematics); Regression; Quantitative analysis (chemistry)","score_opus":0.044099504113448686,"score_gpt":0.3079904114020491,"score_spread":0.2638909072886004,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414553721","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92654103,0.036571886,0.032724094,0.0010772827,0.0003702094,0.0006114,0.00009683063,0.000037684185,0.0019695694],"genre_scores_gemma":[0.9826813,0.00008851048,0.017095428,0.00004446161,0.000041213923,0.00000545142,0.000008061496,0.000027928549,0.000007640891],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99852175,0.000033545435,0.00074281194,0.0001578595,0.00021432995,0.00032971008],"domain_scores_gemma":[0.9986665,0.0003630232,0.00021047916,0.00046244636,0.000109058965,0.0001884713],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0009794337,0.00017912617,0.00059466413,0.00032133632,0.000024605566,0.000013344665,0.00089470256,0.00009211513,0.000014320329],"category_scores_gemma":[0.0015089521,0.00013965668,0.00013673745,0.0007206846,0.000060147897,0.00018558414,0.00009598421,0.0006794954,3.697644e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000018169287,0.00005161232,0.00053525844,0.0050603794,0.0006142299,0.000054012165,0.0002490566,0.22109419,0.7651792,0.0055947555,0.0001358799,0.0014132475],"study_design_scores_gemma":[0.00038361712,0.000011314215,0.00008837685,0.00990207,0.00034442,0.00012568393,0.000057291396,0.8741405,0.11396466,0.000039659,0.0006590565,0.0002833279],"about_ca_topic_score_codex":0.0018123118,"about_ca_topic_score_gemma":0.00010327943,"teacher_disagreement_score":0.6530463,"about_ca_system_score_codex":0.0005961795,"about_ca_system_score_gemma":0.0006397289,"threshold_uncertainty_score":0.5695034},"labels":[],"label_agreement":null},{"id":"W4414569635","doi":"10.1016/j.enconman.2025.120569","title":"Techno-economic optimization of e-methanol production integrated with oxy-fuel power plants: an adaptive power management case study in Australia","year":2025,"lang":"en","type":"article","venue":"Energy Conversion and Management","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Production (economics); Power (physics); Electricity generation; Production manager; Electric power system","score_opus":0.009177703947640859,"score_gpt":0.23610915414033323,"score_spread":0.22693145019269237,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414569635","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98371273,0.00003197688,0.012757288,0.00003612466,0.00024240812,0.00064053753,0.0000040246377,0.000093926916,0.002480963],"genre_scores_gemma":[0.9948351,0.00006615986,0.0013723129,0.0000140117545,0.0000044261424,0.000057547608,0.000024882185,0.000015210676,0.0036103933],"study_design_codex":"simulation_or_modeling","study_design_gemma":"qualitative","domain_scores_codex":[0.99900126,0.000027562306,0.0002781565,0.00039730855,0.00012373025,0.00017196502],"domain_scores_gemma":[0.9995389,0.00000851171,0.00008739899,0.00029575513,0.000026095655,0.000043336124],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018655075,0.00018506615,0.00021453788,0.0005940432,0.00003225109,0.00001112493,0.00010874551,0.000057498328,0.000054738015],"category_scores_gemma":[0.0000029422677,0.00016184447,0.00002572799,0.0003097913,0.000034370056,0.0002077875,0.00014870084,0.00008978626,0.0000016177577],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0031506412,0.0031986546,0.0022189026,0.0014866546,0.0037392867,0.005391858,0.004883114,0.9033594,0.006747121,0.034407984,0.00045427174,0.03096207],"study_design_scores_gemma":[0.029160004,0.0039319443,0.0022815848,0.0030333132,0.0017242715,0.0006064524,0.36016148,0.3407946,0.23843846,0.00031236795,0.016072702,0.0034828528],"about_ca_topic_score_codex":0.0018160077,"about_ca_topic_score_gemma":0.00028004713,"teacher_disagreement_score":0.56256485,"about_ca_system_score_codex":0.00024864663,"about_ca_system_score_gemma":0.0000073558426,"threshold_uncertainty_score":0.6599826},"labels":[],"label_agreement":null},{"id":"W4414837463","doi":"10.1016/j.jcat.2025.116465","title":"A melt-based reaction pathway for CO2 and CH4 conversion to syngas and carbon using liquid In–Sn","year":2025,"lang":"en","type":"article","venue":"Journal of Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Science and Engineering Research Board; Alliance de recherche numérique du Canada; Natural Sciences and Engineering Research Council of Canada; Ministry of Education, India; University of British Columbia; Indian Institute of Technology Kanpur; Department of Science and Technology, Ministry of Science and Technology, India; Canada Foundation for Innovation","keywords":"Syngas; Catalysis; Methane; Carbon fibers; Pyrolysis; Activation energy; Density functional theory; Molecular dynamics","score_opus":0.010273153020525717,"score_gpt":0.25776444234611595,"score_spread":0.24749128932559022,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414837463","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99728966,0.00041462362,0.0018294799,0.00018119431,0.00010772742,0.000105301275,0.0000037162058,0.000008485058,0.00005984033],"genre_scores_gemma":[0.99906635,0.000023727738,0.0007594231,0.00003616267,0.000053939675,0.000003305569,0.000009199613,0.000012907972,0.000034981786],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991487,0.000013256125,0.00038210346,0.0001335271,0.00015181821,0.00017058359],"domain_scores_gemma":[0.99935913,0.0001452108,0.00016747894,0.00011538969,0.00010512617,0.000107637665],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004291192,0.00011132442,0.00034799008,0.0005585475,0.000032930337,0.0000130689805,0.000054156244,0.00008246621,9.423086e-7],"category_scores_gemma":[0.00037273346,0.00009972917,0.00010155923,0.00036220514,0.000017026501,0.00013694543,0.000040881754,0.00015324805,9.266651e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00036034745,0.000022203301,0.00036397943,0.00017285891,0.00008295569,0.000011043728,0.0001751061,0.00066909543,0.99629927,0.000015330608,0.0000021131118,0.0018257014],"study_design_scores_gemma":[0.0011414211,0.00010721704,0.00013245553,0.0003388745,0.0002437399,0.000041876883,0.00019809576,0.022922873,0.9737312,0.000018381163,0.0010070082,0.00011686289],"about_ca_topic_score_codex":0.00020086319,"about_ca_topic_score_gemma":0.00002445538,"teacher_disagreement_score":0.022568071,"about_ca_system_score_codex":0.0002928087,"about_ca_system_score_gemma":0.000069647496,"threshold_uncertainty_score":0.40668374},"labels":[],"label_agreement":null},{"id":"W4414862749","doi":"10.3390/polym17192695","title":"Production of Hydrogen-Rich Syngas via Biomass-Methane Co-Pyrolysis: Thermodynamic Analysis","year":2025,"lang":"en","type":"article","venue":"Polymers","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"","keywords":"Syngas; Methanation; Methane; Syngas to gasoline plus; Gibbs free energy; Carbon dioxide reforming; Carbon fibers; Cellulose","score_opus":0.007062554949186758,"score_gpt":0.25032505093333074,"score_spread":0.24326249598414398,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4414862749","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99181926,0.0014490838,0.0031783811,0.00013573011,0.00021013238,0.00014383403,0.000011964467,0.0001554942,0.0028961033],"genre_scores_gemma":[0.99746877,0.000020368141,0.00008100206,0.000012599603,0.000045495282,0.000025700694,0.00008702655,0.000028239885,0.0022307823],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984476,0.000037961836,0.0004712808,0.00040007674,0.00029798632,0.00034508796],"domain_scores_gemma":[0.99903417,0.00006760768,0.00017166961,0.000601765,0.000050955543,0.000073810515],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029572076,0.0002233605,0.00051626476,0.0009817748,0.00004488985,0.0000054747575,0.00026409654,0.00012969344,0.00012764333],"category_scores_gemma":[0.0001277075,0.00020785947,0.00038879848,0.0030013581,0.00008128233,0.00011759775,0.000060103073,0.00015548468,0.000019509507],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000022275482,0.00005362791,0.001637128,0.000115988536,0.0024548073,0.0000022241147,0.00013035907,0.00056296337,0.9871303,0.00007104657,0.0000036604092,0.007815638],"study_design_scores_gemma":[0.0002164566,0.000011015079,0.0006144157,0.000025397057,0.0016601845,0.0000045729057,0.00009671109,0.0076858983,0.9894037,0.000038410177,0.00005600102,0.00018722976],"about_ca_topic_score_codex":0.0007935601,"about_ca_topic_score_gemma":0.000031963424,"teacher_disagreement_score":0.0076284083,"about_ca_system_score_codex":0.00016896921,"about_ca_system_score_gemma":0.000038486607,"threshold_uncertainty_score":0.8476263},"labels":[],"label_agreement":null},{"id":"W4415370885","doi":"10.1016/j.cej.2025.169812","title":"Molten metal methane pyrolysis for distributed hydrogen production: Reactor design, hydrodynamics, and technoeconomic insights","year":2025,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary; University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Alberta Innovates","keywords":"Hydrogen production; Methane; Pyrolysis; Hydrogen; Steam reforming; Natural gas; Carbon fibers","score_opus":0.008336842050773398,"score_gpt":0.21559037783849805,"score_spread":0.20725353578772465,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415370885","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6740907,0.0019527816,0.3221791,0.0003533789,0.0005401683,0.00041622733,0.000027282596,0.0003803459,0.000060043287],"genre_scores_gemma":[0.9808615,0.00006599204,0.018143257,0.000014163682,0.0004648563,0.000089659785,0.00007882072,0.000083694074,0.0001980709],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982548,0.0000105659055,0.00063113327,0.00044164644,0.0001689125,0.0004929401],"domain_scores_gemma":[0.99897593,0.00020817075,0.00013990853,0.00033253705,0.000101944184,0.00024153001],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00041413773,0.00036511678,0.0005856174,0.00035244785,0.000072164235,0.00003984176,0.00032432063,0.000253581,0.000009188579],"category_scores_gemma":[0.001267651,0.00034198133,0.00026239167,0.00041423822,0.000056170553,0.00028334468,0.00012775492,0.000657284,0.0000032189637],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000049080347,0.000030630934,0.0000056669005,0.00012899874,0.00042295887,0.0000073108204,0.00003857895,0.026616823,0.97098464,0.000297382,0.00003784453,0.0013800914],"study_design_scores_gemma":[0.00062437926,0.000016062922,0.00000391464,0.00010454871,0.0002171292,0.00023222758,0.000014500266,0.20694663,0.7893937,0.00036804957,0.0017794545,0.0002993864],"about_ca_topic_score_codex":0.0000036938904,"about_ca_topic_score_gemma":2.2930291e-7,"teacher_disagreement_score":0.3067708,"about_ca_system_score_codex":0.0004891461,"about_ca_system_score_gemma":0.00006129839,"threshold_uncertainty_score":0.9999032},"labels":[],"label_agreement":null},{"id":"W4415429091","doi":"10.1038/s41467-025-64417-8","title":"Dynamic activation catalysts for CO2 hydrogenation","year":2025,"lang":"en","type":"article","venue":"Nature Communications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"Ministry of Science and Technology of the People's Republic of China; National Natural Science Foundation of China","keywords":"Catalysis; Methanol; Selectivity; Activation energy; Reaction conditions; Solid-state; Steady state (chemistry)","score_opus":0.011606477315845739,"score_gpt":0.30813429805610354,"score_spread":0.2965278207402578,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415429091","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5584282,0.026818888,0.20571715,0.0631719,0.0028790631,0.0077336584,0.00055741717,0.004051681,0.13064198],"genre_scores_gemma":[0.99099314,0.000053992117,0.0061805793,0.0001512643,0.000016144973,0.00020792223,0.0011991423,0.000020661866,0.0011771304],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99931014,0.000019164783,0.00023638648,0.00016581948,0.00010977661,0.00015873996],"domain_scores_gemma":[0.9980172,0.00042754112,0.00008234938,0.0012694411,0.00017153505,0.00003196068],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00019922474,0.00011477942,0.0001403323,0.00021448077,0.00020616112,0.000014685982,0.0007226904,0.000278884,0.0000024616977],"category_scores_gemma":[0.00072023086,0.00011720982,0.00010605099,0.00054625596,0.000038242117,0.0001751114,0.00018766281,0.00053339935,0.000009271945],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002978713,0.00015201907,0.00016160346,0.00013590803,0.00021803433,1.290656e-7,0.00023657834,0.0003078069,0.82924837,0.14858928,0.00195407,0.018966412],"study_design_scores_gemma":[0.00089756685,0.000011638994,0.00064025546,0.00016531892,0.00013619554,0.0000038907265,0.000116657546,0.15599571,0.66909766,0.0027045435,0.16990098,0.00032956808],"about_ca_topic_score_codex":0.00002506104,"about_ca_topic_score_gemma":0.00016215804,"teacher_disagreement_score":0.4325649,"about_ca_system_score_codex":0.00032901237,"about_ca_system_score_gemma":0.000053399024,"threshold_uncertainty_score":0.47796777},"labels":[],"label_agreement":null},{"id":"W4415547016","doi":"10.1016/j.ijhydene.2025.152137","title":"Thermodynamic optimization of syngas production via auto-thermal oxidative steam reforming of bio-oil","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal; Optech (Canada)","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Syngas; Syngas to gasoline plus; Yield (engineering); Steam reforming; Thermodynamic equilibrium; Work (physics)","score_opus":0.005587543701964167,"score_gpt":0.2349466396394266,"score_spread":0.22935909593746245,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415547016","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9670181,0.00041662008,0.0304494,0.00012973788,0.00067663647,0.000024743385,0.000007865694,0.000017972008,0.0012589139],"genre_scores_gemma":[0.99835217,0.00010099775,0.0008306061,0.000012066683,0.00016943677,0.000002653518,0.000021477097,0.000021170548,0.0004894387],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983809,0.000034631743,0.0008321939,0.00013340788,0.00048747237,0.00013138178],"domain_scores_gemma":[0.99831676,0.000051089653,0.0008044755,0.00015620043,0.0006324422,0.000039041704],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00031041887,0.00013956802,0.0003048343,0.00052429753,0.000019901016,0.000004156766,0.00042477975,0.00007368241,0.000040786108],"category_scores_gemma":[0.00019558883,0.00011935389,0.00021132178,0.00026322095,0.000056531895,0.00034359063,0.00009097692,0.00015019465,5.838507e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010701687,0.00007615003,0.0000399126,0.000025165702,0.0004917821,0.0000073641527,0.000101839796,0.2622111,0.71149415,0.0006177151,0.000001178591,0.024826614],"study_design_scores_gemma":[0.00040311762,0.000038389444,0.000017576791,0.0003070109,0.00006477044,0.00011420481,0.00007330999,0.09809051,0.9004775,0.00014184597,0.00018507594,0.000086679094],"about_ca_topic_score_codex":0.00018178599,"about_ca_topic_score_gemma":0.000010827143,"teacher_disagreement_score":0.18898335,"about_ca_system_score_codex":0.00033197468,"about_ca_system_score_gemma":0.00008604785,"threshold_uncertainty_score":0.48671106},"labels":[],"label_agreement":null},{"id":"W4415681194","doi":"10.1016/j.applthermaleng.2025.128835","title":"Modeling industrial shaft furnaces and investigation of CH4-related side reactions","year":2025,"lang":"en","type":"article","venue":"Applied Thermal Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Key Research and Development Program of China; Rio Tinto; Australian Research Council; Monash University","keywords":"Work (physics)","score_opus":0.013173345129497376,"score_gpt":0.21039006566076496,"score_spread":0.19721672053126757,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415681194","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9915246,0.00016446246,0.0057174684,0.000037270675,0.00014804979,0.00015667478,0.0000027413137,0.00021499922,0.0020337326],"genre_scores_gemma":[0.9991821,0.000010032999,0.00056941464,0.000006473545,0.000063362066,0.000024823603,0.000023612867,0.00003118638,0.00008901475],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9990495,0.000004848079,0.0004146764,0.00019124387,0.0001249564,0.00021476536],"domain_scores_gemma":[0.99958575,0.00008626481,0.000057993526,0.0001803302,0.00002289364,0.00006675464],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00020154234,0.0001703652,0.000245265,0.000221133,0.00003884414,0.000009947784,0.000110785855,0.00017884298,0.000006361074],"category_scores_gemma":[0.00008901184,0.00017539934,0.00005164413,0.0003779383,0.00002522831,0.0001230962,0.00008129632,0.0003618601,0.0000018746822],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000007768426,0.0000030376088,0.000022592838,0.000063693355,0.000059700917,4.3790465e-7,0.00012171876,0.34506005,0.646872,0.0062933033,3.1790012e-7,0.0014953839],"study_design_scores_gemma":[0.0004579976,0.000003838355,0.000045533183,0.00014478034,0.000044997814,0.0000033328035,0.00006138103,0.52779996,0.47106782,0.00016042824,0.00007017713,0.00013973561],"about_ca_topic_score_codex":0.00009249819,"about_ca_topic_score_gemma":0.0000012349074,"teacher_disagreement_score":0.18273993,"about_ca_system_score_codex":0.000071762835,"about_ca_system_score_gemma":0.000024465202,"threshold_uncertainty_score":0.71525776},"labels":[],"label_agreement":null},{"id":"W4415896479","doi":"10.1002/cjce.70161","title":"A study of Ni‐Co/ <scp> CeO <sub>2</sub> </scp> catalyst derived from metal–organic framework for dry reforming of methane","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Carbon dioxide reforming; Cobalt; Methane; Coke; Crystallite; Nickel; Dispersion (optics)","score_opus":0.011182873913487061,"score_gpt":0.23086722176566324,"score_spread":0.21968434785217617,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415896479","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98929256,0.0012331314,0.008569585,0.0000492561,0.00037582483,0.00034377325,0.000061305516,0.00003080107,0.000043785032],"genre_scores_gemma":[0.9978057,0.000006819736,0.0017990019,0.000018879911,0.00022677696,0.000019356772,0.0000184956,0.000085398446,0.000019541798],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9973566,0.000028975728,0.0012979887,0.00026029727,0.0004221818,0.0006339384],"domain_scores_gemma":[0.99680525,0.0013166056,0.0005514714,0.0005864986,0.00029431304,0.0004458816],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00078006164,0.00038023884,0.0010794094,0.00056322,0.000058378522,0.000020149986,0.0009579231,0.0002923112,0.000006808985],"category_scores_gemma":[0.0041464996,0.00031313708,0.0004252665,0.00083806633,0.00009253157,0.00022806977,0.000089844354,0.00096679083,0.0000014332521],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000019199464,0.000045388864,0.00011155813,0.00021834695,0.00092132954,0.00002056805,0.0017653644,0.0022619467,0.9934637,0.00025528422,0.0000067304004,0.0009106122],"study_design_scores_gemma":[0.0009822249,0.000067908986,0.00006503665,0.0005614229,0.000525473,0.000028565844,0.00078910275,0.0015131916,0.9947452,0.00048204084,0.00009714627,0.000142671],"about_ca_topic_score_codex":0.0023246722,"about_ca_topic_score_gemma":0.00060392777,"teacher_disagreement_score":0.008513192,"about_ca_system_score_codex":0.0005603874,"about_ca_system_score_gemma":0.00048407,"threshold_uncertainty_score":0.99993205},"labels":[],"label_agreement":null},{"id":"W4415943958","doi":"10.1016/j.scca.2025.100155","title":"Evaluation of the economic and technological aspects of producing blue hydrogen via ethanol-steam reforming with carbon capture","year":2025,"lang":"en","type":"article","venue":"Sustainable Chemistry for Climate Action","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina; University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs; Canada Foundation for Innovation; University of Regina","keywords":"Hydrogen; Hydrogen production; Carbon fibers; Steam reforming; Packed bed; Carbon capture and storage (timeline); Volumetric flow rate; Natural gas","score_opus":0.009876021706844306,"score_gpt":0.25291103664798514,"score_spread":0.24303501494114083,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415943958","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957486,0.0003466751,0.00007469667,0.00006419532,0.000031590676,0.0005933574,0.000006968734,0.000057815498,0.0030761396],"genre_scores_gemma":[0.9995052,0.000018582112,0.00003656246,0.0000015101397,0.000025531808,0.00010815866,0.000017217008,0.000019599596,0.000267629],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988762,0.000014336348,0.00030359387,0.00029090146,0.00021449542,0.00030044946],"domain_scores_gemma":[0.9990214,0.00004660909,0.00026272572,0.00037317243,0.00027200012,0.00002408604],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010053177,0.00015764902,0.0002512455,0.00006457036,0.00008399556,0.0000050870512,0.00014320094,0.00020482988,0.0000043791865],"category_scores_gemma":[0.0004090725,0.00011448831,0.00007454959,0.0002317819,0.000096822514,0.00011886002,0.00012477956,0.00019746694,6.526406e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000074428724,0.000019525436,0.00011318704,0.0060569677,0.000091337526,4.9895544e-7,0.00014703388,0.0058324374,0.9859879,0.00012060578,3.6044054e-7,0.0015556974],"study_design_scores_gemma":[0.0005958264,0.000017169034,0.00001982989,0.00015577901,0.00029908874,0.000020323158,0.0035196927,0.022285271,0.97187614,0.0009786079,0.000117103824,0.00011513345],"about_ca_topic_score_codex":0.00022999856,"about_ca_topic_score_gemma":0.000004425755,"teacher_disagreement_score":0.016452834,"about_ca_system_score_codex":0.0012816531,"about_ca_system_score_gemma":0.0002100705,"threshold_uncertainty_score":0.4668698},"labels":[],"label_agreement":null},{"id":"W4415972957","doi":"10.1016/j.apcatb.2025.126163","title":"Tri-coordinated copper single atoms on SAPO-34 boosts acetic acid production from methane and carbon dioxide","year":2025,"lang":"en","type":"article","venue":"Applied Catalysis B: Environmental","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Structural Genomics Consortium; University of Toronto","funders":"State Key Laboratory of Materials- Oriented Chemical Engineering; University of Toronto; Natural Sciences and Engineering Research Council of Canada; National Natural Science Foundation of China","keywords":"Catalysis; Selectivity; Antibonding molecular orbital; Copper; Methane; Density functional theory; Valence (chemistry)","score_opus":0.005910962496315335,"score_gpt":0.19651871473666213,"score_spread":0.1906077522403468,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415972957","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99534196,0.00062524236,0.00011440752,0.0001346048,0.00015388463,0.00042792692,0.000057928304,0.00017904998,0.0029650244],"genre_scores_gemma":[0.9975237,0.000055325272,0.00021956081,0.000073666946,0.00011300724,0.0001289032,0.0009409327,0.00007265484,0.0008722395],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99771345,0.000029481407,0.0004697764,0.0009284226,0.0003968018,0.00046208774],"domain_scores_gemma":[0.9988775,0.00009206567,0.00013854788,0.0007374731,0.0000049206683,0.00014944075],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00020323989,0.00044793187,0.0005864593,0.00025323755,0.00007947277,0.000019273266,0.00023662193,0.00022872766,0.00004652136],"category_scores_gemma":[0.000056761815,0.00043816486,0.00015071443,0.00037479275,0.00016195806,0.00011272718,0.00026342552,0.00037642897,0.00007907298],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013636443,0.00020005828,0.00030974593,0.000026697116,0.00035490893,0.000006859632,0.0001788236,0.000060030485,0.98401624,0.00005347277,0.000021790314,0.014635025],"study_design_scores_gemma":[0.0010862082,0.000032674947,0.00048011687,0.000043415635,0.0004710141,0.000008100379,0.00046813962,0.00025443643,0.99565345,0.00008009361,0.0010025128,0.00041982654],"about_ca_topic_score_codex":0.000312373,"about_ca_topic_score_gemma":0.000024661847,"teacher_disagreement_score":0.014215197,"about_ca_system_score_codex":0.0009281686,"about_ca_system_score_gemma":0.000011646277,"threshold_uncertainty_score":0.999807},"labels":[],"label_agreement":null},{"id":"W4416072389","doi":"10.1021/acs.iecr.5c03080","title":"Experimental Analysis of a Sabatier Reactor for Renewable Natural Gas Generation from Biogas: Ignition, Parameter Sensitivity Analysis, and Stability","year":2025,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Foundation for Innovation","keywords":"Biogas; Methane; Renewable energy; Natural gas; Refinery; Methanation; Renewable natural gas","score_opus":0.07469875037966268,"score_gpt":0.33762605746229885,"score_spread":0.2629273070826362,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416072389","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9962464,0.0002547898,0.0026154984,0.000043972854,0.0000953283,0.00028268996,0.0003536964,0.000063933374,0.000043719814],"genre_scores_gemma":[0.99795747,0.0000053743374,0.00035452572,0.0000019878498,0.0002604011,0.000081667255,0.0012135267,0.00002044402,0.000104595696],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979867,0.000059612063,0.0005182935,0.00055673014,0.00044662703,0.00043208568],"domain_scores_gemma":[0.9977859,0.00122009,0.00008497998,0.0004984145,0.00028321377,0.00012738105],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011695585,0.0002299359,0.00064943073,0.0005228028,0.00007158196,0.00005038848,0.00014719417,0.00032618848,0.00006110199],"category_scores_gemma":[0.0023927295,0.00023630318,0.00033378013,0.0027209867,0.000089050554,0.00014896136,0.0001467475,0.0005288198,3.0560344e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009642899,0.000063781794,0.0008803058,0.000037395817,0.002977835,0.0000019563736,0.000092070746,0.004454015,0.99114454,0.000030955915,0.00003431776,0.00018641629],"study_design_scores_gemma":[0.00054467417,0.000011063315,0.00011410687,0.00003099628,0.0008836268,4.5157222e-7,0.0001004974,0.19779392,0.8002085,0.000009244466,0.0001490511,0.00015389822],"about_ca_topic_score_codex":0.002255383,"about_ca_topic_score_gemma":0.00004874701,"teacher_disagreement_score":0.1933399,"about_ca_system_score_codex":0.0004614897,"about_ca_system_score_gemma":0.00008652917,"threshold_uncertainty_score":0.9636164},"labels":[],"label_agreement":null},{"id":"W4416091504","doi":"10.1016/j.cattod.2025.115631","title":"Effect of alkali promotion on the catalytic performance of the synergetic K/Fe3O4-Fe5C2/Al2O3 catalyst for CO2 hydrogenation to light paraffins and olefines","year":2025,"lang":"en","type":"article","venue":"Catalysis Today","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada; Ontario Ministry of Research, Innovation and Science; Canada Foundation for Innovation","keywords":"Catalysis; Yield (engineering); Alkali metal; Selectivity; Space velocity; Potassium","score_opus":0.006248475517767311,"score_gpt":0.2346502050310215,"score_spread":0.2284017295132542,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416091504","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99706894,0.00021542989,0.00016731369,0.0010112227,0.00015907199,0.00096644764,0.00003214691,0.00003984061,0.00033959656],"genre_scores_gemma":[0.99871874,0.000013681221,0.000017790584,0.000028916911,0.00003877595,0.00025633318,0.00009942087,0.000029415987,0.0007969549],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984526,0.000058153575,0.000531864,0.00036004258,0.00031953075,0.00027779196],"domain_scores_gemma":[0.99816895,0.00058047025,0.00023481408,0.0008322464,0.00012479287,0.000058759124],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008796158,0.00027008352,0.0005084497,0.00025695332,0.00014451382,0.000013600775,0.00046479638,0.000115396404,0.000004071907],"category_scores_gemma":[0.00105657,0.00015477801,0.0002754625,0.0010538562,0.000091512215,0.00011415269,0.00017913301,0.00015360181,0.000006949238],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018151985,0.00012828066,0.0015864169,0.0019584487,0.00046047318,5.111478e-7,0.00070922525,0.0038278718,0.9779494,0.001327706,0.00014841442,0.01172174],"study_design_scores_gemma":[0.0004173602,0.00018049504,0.0003343874,0.00039982708,0.00047699714,0.0000036665915,0.000033662865,0.0135543365,0.98400617,0.000018686964,0.00042113027,0.00015330804],"about_ca_topic_score_codex":0.000060613038,"about_ca_topic_score_gemma":0.00002903939,"teacher_disagreement_score":0.011568432,"about_ca_system_score_codex":0.0001352738,"about_ca_system_score_gemma":0.00003925963,"threshold_uncertainty_score":0.63116646},"labels":[],"label_agreement":null},{"id":"W4416134092","doi":"10.1007/s44371-025-00350-5","title":"The state-of-the-art technologies and recent trends of sustainable pathways to transform captured carbon into eight key valuable products across industrial applications","year":2025,"lang":"en","type":"article","venue":"Discover Chemistry.","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Raw material; Renewable energy; Fossil fuel; Chemical industry; Greenhouse gas; Industrial production; Carbon fibers; Process (computing); Capital cost","score_opus":0.008705373084375741,"score_gpt":0.2382430268836675,"score_spread":0.22953765379929175,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416134092","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.990128,0.0012258675,0.00023112932,0.0019070582,0.000083347106,0.0007108982,0.00008880919,0.00008720239,0.0055377265],"genre_scores_gemma":[0.98897034,0.00007674717,0.000042775377,0.000004100432,0.000025850379,0.00026301958,0.00003377302,0.000018399487,0.010565009],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987778,0.000006100718,0.00035710738,0.0002831073,0.00022034577,0.00035556188],"domain_scores_gemma":[0.99904644,0.00005295561,0.00010678581,0.0006284951,0.00013034086,0.000034988952],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00023574148,0.0001742368,0.00024609378,0.00003746679,0.00011976529,0.000021944785,0.00042125882,0.00012957775,0.0000022964302],"category_scores_gemma":[0.00035464406,0.00011434059,0.00006837488,0.0010601765,0.00016442506,0.00007034781,0.00027603412,0.00026279263,1.9188408e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000072690644,0.000052357445,0.00008274341,0.00047276274,0.00008648314,7.510518e-7,0.0014485985,0.0002422764,0.95449674,0.00040312592,0.00012554621,0.04251594],"study_design_scores_gemma":[0.0003735487,0.0000075367743,0.000012979852,0.000056824574,0.00003396226,0.000001381606,0.0020863812,0.000059167098,0.93626267,0.0008861612,0.060104553,0.00011486242],"about_ca_topic_score_codex":0.00033245725,"about_ca_topic_score_gemma":0.000048404043,"teacher_disagreement_score":0.059979007,"about_ca_system_score_codex":0.00024856854,"about_ca_system_score_gemma":0.0001550396,"threshold_uncertainty_score":0.46626738},"labels":[],"label_agreement":null},{"id":"W4416386811","doi":"10.1016/j.biombioe.2025.108645","title":"Stability of biochar-supported Ni catalysts during carbon dioxide methanation: A characteristic analysis of deactivation mechanisms and catalyst longevity","year":2025,"lang":"en","type":"article","venue":"Biomass and Bioenergy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada; Western University","keywords":"Biochar; Methanation; Catalysis; Methane; Selectivity; Carbon fibers; Economies of agglomeration; Nickel; Renewable energy; Carbon dioxide","score_opus":0.009903495078738554,"score_gpt":0.23090632188847404,"score_spread":0.2210028268097355,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416386811","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9980345,0.00035068384,0.0012109461,0.000039795956,0.00006464748,0.00010722237,0.0000939222,0.000038116406,0.000060176655],"genre_scores_gemma":[0.99946517,0.00003865578,0.00014372765,0.0000030870406,0.000013429882,0.000014624928,0.00026970584,0.000011861967,0.000039713967],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99857944,0.00003501801,0.0005837097,0.0003837728,0.00022106955,0.00019698935],"domain_scores_gemma":[0.99905044,0.00008046038,0.0003102493,0.00034932795,0.00013133508,0.00007819115],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003391412,0.00020197534,0.00063664484,0.00065185927,0.000041370233,0.000007796274,0.00010663426,0.00014336011,0.000009002434],"category_scores_gemma":[0.00017133047,0.00018028742,0.00012980944,0.001432659,0.00009181269,0.00010836661,0.00014194565,0.00006804429,8.049406e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000053078336,0.000052321193,0.0074395174,0.00044252348,0.00095832895,0.000002424994,0.000096013464,0.0000033514987,0.9890227,0.0006433895,7.9097525e-8,0.0012862753],"study_design_scores_gemma":[0.00030801145,0.000018434195,0.061360225,0.00005273523,0.000907325,0.0000028192355,0.000092456634,0.002413105,0.9346457,0.0000416632,0.0000054095667,0.00015207574],"about_ca_topic_score_codex":0.0058518094,"about_ca_topic_score_gemma":0.0005348732,"teacher_disagreement_score":0.05437696,"about_ca_system_score_codex":0.0001032814,"about_ca_system_score_gemma":0.000031900356,"threshold_uncertainty_score":0.88462245},"labels":[],"label_agreement":null},{"id":"W4416399651","doi":"10.1002/adfm.202524136","title":"Stabilizing Perovskite Phase via A‐Site Charge Density Modulation During Metal In Situ Exsolution for Robust CO <sub>2</sub> Electrolysis","year":2025,"lang":"en","type":"article","venue":"Advanced Functional Materials","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Central South University","keywords":"Perovskite (structure); Phase (matter); Density functional theory; Electrolysis; Heterojunction; Metal; In situ; Transition metal","score_opus":0.010958503200310414,"score_gpt":0.24571684160072715,"score_spread":0.23475833840041674,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416399651","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9062699,0.00007886074,0.09231998,0.000031540225,0.00053131394,0.0005024648,0.00007006029,0.00016455234,0.000031315398],"genre_scores_gemma":[0.9978351,0.00001733549,0.0007113358,0.000022068542,0.00020642382,0.00017630044,0.0008927298,0.00004394096,0.00009476382],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981157,0.00004089659,0.0006238439,0.00050026074,0.00023736041,0.00048190381],"domain_scores_gemma":[0.9992494,0.00013038272,0.00017655158,0.00024659443,0.00013508582,0.00006200641],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00042782238,0.00027907698,0.00047859777,0.00035373698,0.00017307053,0.000027313517,0.000082855615,0.00014484151,0.000042028405],"category_scores_gemma":[0.00028442193,0.0003009391,0.00015523193,0.00038003305,0.000024707046,0.00064830633,0.00005569498,0.00014261041,0.000022629343],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00091893034,0.00009170661,0.00005602688,0.00021507913,0.000079655096,0.0000020867758,0.000036261434,0.019534005,0.97704476,0.00029858676,0.0000014324568,0.0017214739],"study_design_scores_gemma":[0.002746147,0.000033807595,0.0013336892,0.00008063278,0.00007668374,0.000010893032,0.000014552152,0.012962913,0.982178,0.00026972222,0.000024883839,0.0002681156],"about_ca_topic_score_codex":0.000018659297,"about_ca_topic_score_gemma":0.00003064938,"teacher_disagreement_score":0.09160864,"about_ca_system_score_codex":0.00068044424,"about_ca_system_score_gemma":0.000033104097,"threshold_uncertainty_score":0.99994427},"labels":[],"label_agreement":null},{"id":"W4416427640","doi":"10.1016/j.ceja.2025.100958","title":"Modelling Fischer–Tropsch synthesis: A review of applications using genetic algorithms and hybrid GA–based models","year":2025,"lang":"en","type":"article","venue":"Chemical Engineering Journal Advances","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Process (computing); Key (lock); Renewable energy; Genetic algorithm; Sensitivity (control systems); Process modeling; Product (mathematics)","score_opus":0.01459830761455954,"score_gpt":0.2509807645820819,"score_spread":0.23638245696752236,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416427640","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.015136943,0.11092435,0.8735016,0.00005063311,0.00006080963,0.00016517153,0.000009997743,0.000071557595,0.00007891148],"genre_scores_gemma":[0.33898365,0.023134155,0.63707685,0.00010875156,0.0003503194,0.0001738144,0.0000118841535,0.000121634585,0.000038931077],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9984504,0.000010474494,0.0006766226,0.0002694696,0.00025961455,0.00033342233],"domain_scores_gemma":[0.9990425,0.00024205839,0.00016899858,0.00025024885,0.00013622119,0.00015996827],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00022718648,0.00026040748,0.00053595804,0.00017394521,0.00005394119,0.000017455737,0.0002715034,0.00007184772,0.000008843706],"category_scores_gemma":[0.00022102431,0.00024187757,0.00017606847,0.0003751678,0.00004583317,0.00026542973,0.00007334931,0.00044165395,5.8795257e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000064610754,0.000022867272,0.0000021480305,0.004946816,0.000056248802,0.000004788994,0.0000061365813,0.8153502,0.16868106,0.00012408232,0.000002070578,0.010797169],"study_design_scores_gemma":[0.00014248624,0.0000035644753,1.274291e-7,0.005948635,0.00011534456,0.000087533925,0.0000047013164,0.705874,0.28666118,0.00025489673,0.00073741237,0.00017009536],"about_ca_topic_score_codex":0.00000494322,"about_ca_topic_score_gemma":1.5153013e-8,"teacher_disagreement_score":0.3238467,"about_ca_system_score_codex":0.00014711941,"about_ca_system_score_gemma":0.000059280283,"threshold_uncertainty_score":0.9863481},"labels":[],"label_agreement":null},{"id":"W4416470729","doi":"10.3390/fuels6040086","title":"Harnessing Mechanical Force for Greenhouse Gas Conversion: A Mini-Review on Mechanochemistry in the Dry Reforming of Methane","year":2025,"lang":"en","type":"article","venue":"Fuels","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Alberta Energy","funders":"","keywords":"Mechanochemistry; Syngas; Carbon dioxide reforming; Methane; Coke; Greenhouse gas; Bimetallic strip","score_opus":0.018861268825898628,"score_gpt":0.28362425361910837,"score_spread":0.26476298479320975,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416470729","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.93033415,0.024096213,0.024575088,0.0047974763,0.0011099338,0.003839499,0.0001159603,0.0004149765,0.010716722],"genre_scores_gemma":[0.99429226,0.0007205506,0.0017919556,0.00090387603,0.00013043598,0.00025460753,0.00007198586,0.000056483284,0.0017778494],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984254,0.000038559185,0.00057318783,0.00031705643,0.00029110385,0.00035468754],"domain_scores_gemma":[0.9985524,0.0005915852,0.00016593994,0.0005720988,0.000066559915,0.000051445353],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010428728,0.00022481351,0.00053439446,0.0001222512,0.00003964432,0.0000066104813,0.00049788144,0.00016265307,0.000030495994],"category_scores_gemma":[0.00085991406,0.00016031985,0.00027083437,0.0005036384,0.000031819895,0.00010211751,0.00011853391,0.0003063527,0.0000052314317],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012939142,0.00010940243,0.00000805212,0.009213434,0.000083663894,0.000016810976,0.00022806869,0.000014789518,0.957894,0.0035149409,0.000118614975,0.02866883],"study_design_scores_gemma":[0.0008569961,0.000046110075,0.0000015052099,0.004730923,0.00011836187,0.0000129976515,0.0002662506,0.0009975994,0.98787576,0.0010060377,0.0039108912,0.00017657538],"about_ca_topic_score_codex":0.000045067864,"about_ca_topic_score_gemma":0.00000737173,"teacher_disagreement_score":0.06395812,"about_ca_system_score_codex":0.0001534608,"about_ca_system_score_gemma":0.00006293033,"threshold_uncertainty_score":0.6537654},"labels":[],"label_agreement":null},{"id":"W4416583997","doi":"10.1021/acs.iecr.5c03888","title":"Graphene Produced in RF-ICP Thermal Plasma Reactor: A Ni-Catalyst Support for CO <sub>2</sub> Methanation","year":2025,"lang":"en","type":"article","venue":"Industrial & Engineering Chemistry Research","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Mitacs","keywords":"Graphene; Methanation; Atmospheric pressure; Methane; Catalysis; Pyrolysis; Dispersion (optics); Raman spectroscopy; Space velocity; Selectivity","score_opus":0.058726181913284166,"score_gpt":0.3323447466653686,"score_spread":0.27361856475208446,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416583997","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9967581,0.00006989405,0.00008413151,0.00017943713,0.000354016,0.00092482526,0.00008975525,0.00027104648,0.0012687682],"genre_scores_gemma":[0.9972056,0.000012385034,0.00004080273,0.0000037237287,0.0007914166,0.00059338845,0.0005661646,0.00010467012,0.0006818471],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9962538,0.000038027792,0.0008123804,0.0008127379,0.00084297574,0.0012400897],"domain_scores_gemma":[0.9978869,0.00075701426,0.000097941556,0.00074759964,0.00027352746,0.00023701297],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0027138605,0.00042284717,0.0005963759,0.0006794708,0.000093816976,0.00007177356,0.000705762,0.0007319717,0.000034001027],"category_scores_gemma":[0.0043568085,0.00045727668,0.0002213593,0.0019406988,0.00008217375,0.00026101037,0.00022217359,0.0019199196,0.000019471661],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002088094,0.00009042194,0.00023685723,0.00045384085,0.00014753336,0.000019557303,0.00008949572,0.0020944604,0.99072826,0.00005041512,0.0003071641,0.005573214],"study_design_scores_gemma":[0.0023923118,0.000031296324,0.000036228957,0.00029527032,0.00003382363,0.000011136672,0.00007074962,0.007065283,0.98646176,0.000015101659,0.0031942257,0.00039279222],"about_ca_topic_score_codex":0.0001094698,"about_ca_topic_score_gemma":0.000005977008,"teacher_disagreement_score":0.005180422,"about_ca_system_score_codex":0.0010334551,"about_ca_system_score_gemma":0.00044199143,"threshold_uncertainty_score":0.99978787},"labels":[],"label_agreement":null},{"id":"W4416702658","doi":"10.1021/acscatal.5c06417","title":"Designing the Future of Advancing Catalysis: Structural Trends in Metal-Free Systems for CO <sub>2</sub> Conversion","year":2025,"lang":"en","type":"article","venue":"ACS Catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"PRIMA Québec; Canada Foundation for Innovation; National Research Council; Natural Sciences and Engineering Research Council of Canada; McGill University","keywords":"Catalysis; Work (physics)","score_opus":0.006477104750682615,"score_gpt":0.23888584721637784,"score_spread":0.23240874246569523,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416702658","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9899425,0.0051658163,0.003520135,0.00020712215,0.00043481647,0.000354817,0.00007416361,0.00010078927,0.00019983105],"genre_scores_gemma":[0.9984864,0.000050292874,0.00025849816,0.000020916113,0.00012628867,0.0001115525,0.00066221686,0.000043013024,0.00024083917],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99779564,0.000055283333,0.0007835892,0.00046661566,0.0003793833,0.00051947654],"domain_scores_gemma":[0.99799246,0.00042629082,0.00030773654,0.0010673053,0.00012995554,0.00007624413],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00075431855,0.0003375498,0.00080408464,0.0008193954,0.00014604165,0.00002737565,0.0007836543,0.00019973781,0.000005776215],"category_scores_gemma":[0.00030129505,0.00025484452,0.0004549311,0.001993023,0.00007538806,0.00034997065,0.0001856775,0.00031388988,0.0000034087877],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000057069068,0.000021139454,0.0005087797,0.00044770207,0.00069176883,0.0000050142307,0.0006962049,0.00696387,0.9753972,0.00038788005,0.00017671692,0.014646619],"study_design_scores_gemma":[0.0009986437,0.000017711089,0.00013348414,0.0001395561,0.00082040747,0.000006988854,0.0025652617,0.012226469,0.9821958,0.00004794338,0.00058019906,0.00026753548],"about_ca_topic_score_codex":0.00041517135,"about_ca_topic_score_gemma":0.00018218016,"teacher_disagreement_score":0.014379083,"about_ca_system_score_codex":0.0003581642,"about_ca_system_score_gemma":0.000050711227,"threshold_uncertainty_score":0.9999904},"labels":[],"label_agreement":null},{"id":"W4416902026","doi":"10.31635/ccschem.025.202506666","title":"Zeolite Nanosheet-Confined Pt–FeO <sub> <i>x</i> </sub> Catalysts for Reversible Hydrogen Cycling via the Methylcyclohexane–Toluene System","year":2025,"lang":"en","type":"article","venue":"CCS Chemistry","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"","keywords":"Catalysis; Zeolite; Hydrogen; Hydrogen production; Thermal stability","score_opus":0.006385509568513623,"score_gpt":0.2181996870493863,"score_spread":0.21181417748087267,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416902026","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9786085,0.0022365728,0.0039963247,0.00028665346,0.00048655242,0.0007278198,0.00009767761,0.0006548791,0.0129050445],"genre_scores_gemma":[0.9956748,0.00002833562,0.00027842016,0.00010818987,0.00040622396,0.00026494576,0.00030002926,0.00010266667,0.0028363846],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99720746,0.000026507223,0.0008098017,0.00074519654,0.00037079197,0.0008402546],"domain_scores_gemma":[0.9976369,0.0004717921,0.00027003628,0.0012566936,0.00016201897,0.00020251615],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007006742,0.0005155393,0.0007037138,0.00008957378,0.0003101012,0.00004871761,0.0008864104,0.0004328848,0.000008025773],"category_scores_gemma":[0.00044717442,0.00044226286,0.0005386544,0.000715203,0.00010870632,0.00015220651,0.0003176163,0.0005188808,0.000032248296],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000042257856,0.000030564748,0.000027641443,0.0022278375,0.00030051146,0.000011772939,0.000104998166,0.0002723487,0.9939238,0.00008189478,0.0005302784,0.002446083],"study_design_scores_gemma":[0.0010621229,0.0000057104744,0.0000032552564,0.00048796725,0.00035758977,0.000073171104,0.00023847658,0.0053104563,0.9863269,0.00009758876,0.0055808965,0.0004559101],"about_ca_topic_score_codex":0.00007090447,"about_ca_topic_score_gemma":0.000004443989,"teacher_disagreement_score":0.017066328,"about_ca_system_score_codex":0.000586237,"about_ca_system_score_gemma":0.00014045055,"threshold_uncertainty_score":0.9998029},"labels":[],"label_agreement":null},{"id":"W4416957512","doi":"10.1016/j.renene.2025.124932","title":"Intensified steam reforming of a simulated bio-oil for renewable hydrogen production over CeO2-promoted Ni/CaO bifunctional material: Experimental kinetics and reactor modeling","year":2025,"lang":"en","type":"article","venue":"Renewable Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada; Université Laval","keywords":"Steam reforming; Hydrogen production; Bifunctional; Renewable energy; Production (economics); Kinetics","score_opus":0.01480290211388058,"score_gpt":0.24272740742088328,"score_spread":0.2279245053070027,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4416957512","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.993685,0.0005572055,0.0040490483,0.0000335702,0.0007422572,0.00015419816,0.00003390401,0.00020326076,0.00054152013],"genre_scores_gemma":[0.9925133,0.000068445865,0.00063768245,0.00002293985,0.00023700685,0.00005125518,0.00032234786,0.00008004252,0.006066965],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99802387,0.000023335971,0.0006926145,0.0005597374,0.00025592893,0.00044453237],"domain_scores_gemma":[0.9990085,0.000049929607,0.00018944242,0.00044193177,0.00020972511,0.00010052358],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00022277953,0.00032831094,0.000511864,0.00035212003,0.00009942428,0.000018700686,0.00015917535,0.0002558005,0.00002659476],"category_scores_gemma":[0.0002399311,0.00031228428,0.00013018271,0.0004569861,0.000050801358,0.00025274808,0.00017710558,0.000088998524,3.858852e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024769676,0.000073608724,0.0000045237775,0.00013302152,0.00011565234,9.1094114e-7,0.000057815127,0.32724413,0.6714239,0.00004677618,0.00002332039,0.0006286106],"study_design_scores_gemma":[0.0006507872,0.00005875607,5.225405e-7,0.00021831217,0.00006418882,0.000010129644,0.00020295693,0.31602994,0.6809307,0.00014294033,0.0014800824,0.0002107412],"about_ca_topic_score_codex":0.014371008,"about_ca_topic_score_gemma":0.00022668281,"teacher_disagreement_score":0.014144325,"about_ca_system_score_codex":0.00037033428,"about_ca_system_score_gemma":0.00006999294,"threshold_uncertainty_score":0.99993294},"labels":[],"label_agreement":null},{"id":"W4417059094","doi":"10.1016/b978-0-443-27564-7.00005-3","title":"Production of green hydrocarbon fuels and chemicals from catalytic Fischer-Tropsch synthesis","year":2025,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Hydrocarbon; Production (economics); Raw material; Renewable energy; Carbon monoxide","score_opus":0.010016442141650496,"score_gpt":0.21571947006707506,"score_spread":0.20570302792542458,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417059094","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.020191802,0.003440287,0.0000050287604,0.00008058342,0.0003339916,0.00060572894,0.00014576848,0.00017196924,0.9750248],"genre_scores_gemma":[0.035327204,0.00013267445,0.0003154031,0.00001849083,0.00047649807,0.00006196472,0.00011554574,0.0001397746,0.96341246],"study_design_codex":"design_other","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99777025,0.000013072335,0.0007625734,0.000746554,0.00039726237,0.00031029852],"domain_scores_gemma":[0.998293,0.0002465653,0.0003598083,0.00088329945,0.000084386294,0.00013298313],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00021342273,0.0005561549,0.0010919293,0.00024210638,0.00003877129,0.000011322249,0.00031784736,0.0005730409,0.000057780966],"category_scores_gemma":[0.00030602355,0.0005329369,0.00029722496,0.00003576309,0.00015300141,0.00006580769,0.00029741012,0.0006290721,0.00002073696],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000028204342,0.000008403488,0.00000689181,0.00095605827,0.00047070908,0.000008589215,0.00016659316,9.187859e-7,0.20628768,0.00029462168,0.000011958271,0.7917594],"study_design_scores_gemma":[0.0002505465,0.000017573255,0.0000066919574,0.003217339,0.0012131811,0.000020003516,0.00001266326,0.000090744325,0.8730525,0.0037723046,0.11756429,0.0007821576],"about_ca_topic_score_codex":0.000061593455,"about_ca_topic_score_gemma":0.00002210784,"teacher_disagreement_score":0.7909772,"about_ca_system_score_codex":0.00019708932,"about_ca_system_score_gemma":0.0000723585,"threshold_uncertainty_score":0.9997122},"labels":[],"label_agreement":null},{"id":"W4417309650","doi":"10.1002/cctc.202501480","title":"Synergistic Cu‐Zn/Fly Ash Catalysts for Intensified Sorption‐Enhanced CO <sub>2</sub> Hydrogenation to CO Through the RWGS Reaction","year":2025,"lang":"en","type":"article","venue":"ChemCatChem","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Catalysis; Syngas; Yield (engineering); Adsorption; Selectivity; Water-gas shift reaction","score_opus":0.017285161912861672,"score_gpt":0.2803469378994818,"score_spread":0.2630617759866201,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417309650","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9569113,0.000109764456,0.03511752,0.0011201126,0.0005217162,0.0009055301,0.000037722446,0.00039377584,0.0048825447],"genre_scores_gemma":[0.99628633,0.00001763094,0.00028659173,0.00037410905,0.00030462304,0.0005159659,0.0006061037,0.000073546755,0.0015351083],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979234,0.000017891769,0.0005848276,0.00059615535,0.00033945014,0.0005382865],"domain_scores_gemma":[0.99825764,0.00037029246,0.00019191083,0.00075462373,0.00031001322,0.000115493516],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00037428646,0.00036398467,0.00044104725,0.00015017479,0.00020694903,0.00004292635,0.00041396028,0.0002529104,0.0000050020617],"category_scores_gemma":[0.0010827485,0.0003128007,0.00026411284,0.00073323975,0.00007552704,0.0002622601,0.00010541263,0.00034653558,0.0001705501],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008832737,0.00004710129,0.0000034517298,0.00019079707,0.00014062678,0.0000011961381,0.0009104832,0.000108902124,0.9894205,0.000673451,0.002762947,0.005652248],"study_design_scores_gemma":[0.000678194,0.000019826231,0.000023678154,0.00015133704,0.00014765524,0.000007658723,0.0005216665,0.0012079484,0.9910201,0.0007487981,0.005130024,0.0003431279],"about_ca_topic_score_codex":0.00010235612,"about_ca_topic_score_gemma":0.000044486045,"teacher_disagreement_score":0.039375007,"about_ca_system_score_codex":0.00073528744,"about_ca_system_score_gemma":0.00009733226,"threshold_uncertainty_score":0.9999324},"labels":[],"label_agreement":null},{"id":"W4417312149","doi":"10.1007/s10751-025-02340-6","title":"Mössbauer characterization of low-temperature iron-based Fischer-Tropsch catalysts","year":2025,"lang":"en","type":"article","venue":"Interactions","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Manitoba; Saskatchewan Research Council (Canada)","funders":"","keywords":"Goethite; Calcination; Catalysis; Hyperfine structure; Magnetite; Paramagnetism; Mössbauer spectroscopy; Quadrupole","score_opus":0.005471253097656958,"score_gpt":0.25164951863854107,"score_spread":0.24617826554088412,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417312149","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99419874,0.00002274263,0.0016563954,0.0004516044,0.0006833557,0.00013592548,0.00008718153,0.00012549692,0.0026385398],"genre_scores_gemma":[0.99351525,0.0000026662542,0.00013909828,0.000077943274,0.00009080455,0.000038606962,0.00055178703,0.000022958338,0.005560878],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991343,0.000016874415,0.00034182827,0.00020216603,0.00013146481,0.00017335589],"domain_scores_gemma":[0.9992835,0.000096364405,0.00010229424,0.00034769205,0.00012238076,0.000047798807],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00006135516,0.00014837409,0.00021034379,0.0002565892,0.00005466564,0.000015737176,0.00015340843,0.000100177196,0.00016636982],"category_scores_gemma":[0.00015648977,0.00014170374,0.0001441787,0.0004673699,0.000026451695,0.00023608813,0.000042282787,0.00031479474,0.000046775924],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00002331558,0.00007691705,0.00022996662,0.00015496761,0.000047726877,0.000002017473,0.000082392515,0.00030905652,0.99799085,0.00019117181,0.00008695326,0.0008046664],"study_design_scores_gemma":[0.0002743731,0.000007220432,0.0011630732,0.0002945996,0.00004435053,0.000004197408,0.000033391087,0.0035471863,0.9880228,0.000005779723,0.0064796614,0.0001233408],"about_ca_topic_score_codex":0.00006955325,"about_ca_topic_score_gemma":0.000025847117,"teacher_disagreement_score":0.009968022,"about_ca_system_score_codex":0.00015304598,"about_ca_system_score_gemma":0.00006165062,"threshold_uncertainty_score":0.57785106},"labels":[],"label_agreement":null},{"id":"W4417348520","doi":"10.1002/cjce.70215","title":"Random forest regression for catalyst performance prediction and validation of tri‐reforming of methane ( <scp>TRM</scp> )","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada; Mitacs; Canadian Natural Resources Limited","keywords":"Methane; Catalysis; Hydrogen; Syngas; Steam reforming; Random forest; Hydrogen production; Regression","score_opus":0.00817067511355419,"score_gpt":0.21290821661676104,"score_spread":0.20473754150320686,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417348520","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9949312,0.00081876275,0.0036685567,0.000046586443,0.00022888572,0.00018721557,0.000023707456,0.000012615687,0.000082424536],"genre_scores_gemma":[0.99918145,0.000017496304,0.00055336294,0.0000042419188,0.00011590828,0.0000090771655,0.00001930732,0.000024361509,0.00007479357],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99865615,0.000010098669,0.0007308415,0.00011195037,0.00020863299,0.0002823013],"domain_scores_gemma":[0.99859035,0.00048548446,0.00032603866,0.00018824232,0.00021558904,0.00019430669],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00081087934,0.00017058918,0.00046553987,0.00038588347,0.000041108226,0.000010537001,0.00026107221,0.00013949978,0.0000017063802],"category_scores_gemma":[0.0015658649,0.00012354726,0.0001716803,0.0003569149,0.00006829365,0.00023396222,0.000029417595,0.00031682113,1.2409464e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000050856524,0.000007098663,0.0005461208,0.00072397327,0.00014832249,0.0000014650468,0.00045228165,0.021088248,0.97464705,0.00016921617,0.000017116505,0.0021482678],"study_design_scores_gemma":[0.0013660638,0.00003472793,0.00010953038,0.00081955444,0.00015855688,0.000057668167,0.00004879418,0.04190094,0.9550249,0.00004756566,0.00037995446,0.00005176903],"about_ca_topic_score_codex":0.0004357094,"about_ca_topic_score_gemma":0.000038546314,"teacher_disagreement_score":0.020812694,"about_ca_system_score_codex":0.00022817227,"about_ca_system_score_gemma":0.00021194867,"threshold_uncertainty_score":0.5038111},"labels":[],"label_agreement":null},{"id":"W4417419363","doi":"10.1016/j.energy.2025.139708","title":"Machine learning–guided CO2 methanation: From catalyst design optimization to techno-economic and life cycle assessment analyses","year":2025,"lang":"en","type":"article","venue":"Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dalhousie University; Cancer Care Nova Scotia","funders":"Universiti Malaysia Terengganu; University of Tehran; Iran National Science Foundation; Dalhousie University","keywords":"Methanation; Flue gas; Catalysis; Renewable energy; Generalizability theory; Hydrogen; Life-cycle assessment; Process optimization; Power to gas","score_opus":0.022499423929951645,"score_gpt":0.30136843377812533,"score_spread":0.2788690098481737,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417419363","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.038129132,0.00077152683,0.9579171,0.0003944616,0.00014034998,0.00010408924,0.000016646587,0.00025974732,0.0022669462],"genre_scores_gemma":[0.9620192,0.00007970757,0.036019735,0.00011770368,0.000085191365,0.000058515754,0.00032447887,0.000034624638,0.001260855],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99895996,0.00004222361,0.0003339425,0.00034568115,0.00012909662,0.00018912154],"domain_scores_gemma":[0.99931437,0.00017807708,0.00008660568,0.0002644515,0.000037511636,0.00011896256],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00020686044,0.00018189235,0.00030069743,0.00032116336,0.000085853644,0.00003668308,0.00016853327,0.000101927755,0.00012911421],"category_scores_gemma":[0.00023260857,0.00018054427,0.0000607725,0.00034714537,0.000018244229,0.00013615936,0.00014929527,0.00013605255,0.000006705865],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000009608351,0.00001180689,0.000071061775,0.000008542064,0.00015567399,0.0000018083501,0.00002971446,0.9555176,0.03973862,0.0014855827,0.00004991079,0.0029200756],"study_design_scores_gemma":[0.00032757354,0.000013858834,0.000047497877,0.000026214831,0.000086311076,0.000001365729,0.000040983952,0.8106126,0.18640392,0.00015716995,0.0021104328,0.00017202867],"about_ca_topic_score_codex":0.00682681,"about_ca_topic_score_gemma":0.00009792751,"teacher_disagreement_score":0.92389005,"about_ca_system_score_codex":0.0003108566,"about_ca_system_score_gemma":0.0000705933,"threshold_uncertainty_score":0.9997868},"labels":[],"label_agreement":null},{"id":"W4417435370","doi":"10.1007/s13369-025-10980-7","title":"Emerging Trends in Catalyst Design for the Conversion of CO2 to Dimethyl Ether","year":2025,"lang":"en","type":"article","venue":"Arabian Journal for Science and Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Innovation, Science and Economic Development Canada","funders":"King Fahd University of Petroleum and Minerals","keywords":"Dimethyl ether; Catalysis; Context (archaeology); Methanol; Bifunctional; Transformative learning","score_opus":0.017917234697780712,"score_gpt":0.2819447559228439,"score_spread":0.2640275212250632,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417435370","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.44654536,0.0006042947,0.5507856,0.000902599,0.0007633884,0.00030010098,0.000004674953,0.00002550597,0.00006845957],"genre_scores_gemma":[0.99273056,0.000014176948,0.006927938,0.000030114952,0.00004314325,0.000023401204,6.5120213e-7,0.0000127414005,0.00021727572],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990733,0.0000039712127,0.00026098418,0.00015698822,0.00017825964,0.00032645924],"domain_scores_gemma":[0.99932057,0.0003064873,0.000045629884,0.00013250098,0.00010232497,0.000092470575],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0018272824,0.00010420389,0.00017735214,0.0006244244,0.00015464018,0.000030616517,0.00030465474,0.000034229306,0.0000025741845],"category_scores_gemma":[0.0006290949,0.00007648503,0.00007236532,0.0011104908,0.00005063104,0.0002319894,0.000054656073,0.00014202253,2.8244983e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000050703537,0.000009762856,0.00012824466,0.00012047917,0.000035677447,0.0000012808184,0.0010653054,0.15218197,0.8040522,0.0011925203,0.000073849995,0.041088015],"study_design_scores_gemma":[0.0007149667,0.000068477784,0.0004849873,0.00026282985,0.000042609023,0.000023136035,0.00051193184,0.4113308,0.58106863,0.000099648496,0.005215479,0.00017652326],"about_ca_topic_score_codex":0.000021012245,"about_ca_topic_score_gemma":0.0000023506157,"teacher_disagreement_score":0.5461852,"about_ca_system_score_codex":0.00012112132,"about_ca_system_score_gemma":0.000047561018,"threshold_uncertainty_score":0.3118969},"labels":[],"label_agreement":null},{"id":"W4417474293","doi":"10.2139/ssrn.5748702","title":"Decarbonizing Steam Methane Reforming through Direct Joule-Heated Fluidized Bed Reactor","year":2025,"lang":"","type":"preprint","venue":"SSRN Electronic Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Steam reforming; Fluidized bed; Methane; Hydrogen production; Methane reformer; Renewable energy; Hydrogen","score_opus":0.015181963273909109,"score_gpt":0.2723370271465001,"score_spread":0.257155063872591,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417474293","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8292116,0.12658174,0.008308893,0.0009932918,0.008409188,0.0029580095,0.00021215824,0.0014163965,0.021908736],"genre_scores_gemma":[0.8663167,0.11865648,0.0015680174,0.00012215774,0.003822115,0.00018387406,0.0004306013,0.00073548034,0.008164576],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9741064,0.00085406756,0.0051528965,0.0027554024,0.0025326246,0.014598646],"domain_scores_gemma":[0.99130785,0.0010928516,0.0029099255,0.0027634064,0.0010229223,0.0009030691],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.011759686,0.003129692,0.0048716064,0.0016302476,0.00084489066,0.00032640414,0.0037163822,0.0028996046,0.00018622607],"category_scores_gemma":[0.0032298535,0.0029905315,0.003401883,0.0024940704,0.00026451616,0.0015239172,0.0026252593,0.033735007,0.000096984964],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":true,"study_design_scores_codex":[0.0017265113,0.0004949521,0.00007690957,0.0014051665,0.013200001,0.00016873406,0.0027413825,0.0006786707,0.8947654,0.008787985,0.000019683363,0.07593464],"study_design_scores_gemma":[0.006943572,0.00048556266,0.0000028775914,0.0059431964,0.0039024146,0.003291581,0.004445339,0.0016065534,0.931041,0.029737242,0.008719894,0.0038807397],"about_ca_topic_score_codex":0.0039455,"about_ca_topic_score_gemma":0.0009456019,"teacher_disagreement_score":0.072053894,"about_ca_system_score_codex":0.031867906,"about_ca_system_score_gemma":0.017285053,"threshold_uncertainty_score":0.99839485},"labels":[],"label_agreement":null},{"id":"W4417507037","doi":"10.1016/j.memsci.2025.125078","title":"Hydrogen dissociation and diffusion through molten metal alloy membranes","year":2025,"lang":"en","type":"article","venue":"Journal of Membrane Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Science and Engineering Research Board; Natural Sciences and Engineering Research Council of Canada; University of British Columbia; Alliance de recherche numérique du Canada; Mitacs; Indian Institute of Technology Kanpur; Department of Science and Technology, Ministry of Science and Technology, India; Canada Foundation for Innovation","keywords":"Hydrogen; Bismuth; Dissociation (chemistry); Copper; Membrane; Transition metal; Adsorption; Metal","score_opus":0.00893403240856162,"score_gpt":0.2637004337332886,"score_spread":0.254766401324727,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4417507037","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9952381,0.0007445233,0.00036660238,0.0005353858,0.0002692492,0.000064298685,0.0000014333903,0.000022228642,0.0027581698],"genre_scores_gemma":[0.99847096,0.00021718479,0.00059925864,0.000057584228,0.000082473016,0.0000010319627,7.257727e-7,0.000008313976,0.00056246406],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99848175,0.000018347204,0.00043068858,0.00017898182,0.0006351461,0.00025507543],"domain_scores_gemma":[0.9992242,0.000116550924,0.0002500211,0.00015513386,0.00015518133,0.00009891913],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0011415817,0.00012341511,0.0002940756,0.00024581945,0.00015041613,0.00003667333,0.0003938889,0.000058539048,0.00001623093],"category_scores_gemma":[0.0007925206,0.0000918423,0.000112063804,0.0007699544,0.00017424827,0.000954913,0.00014429724,0.00022413139,0.000002541701],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017589184,0.0000247395,0.00014637024,0.00006273047,0.000030344452,0.000008476594,0.0003729222,0.0007160461,0.99615663,0.0008234537,0.0000030055587,0.0016377004],"study_design_scores_gemma":[0.000575137,0.000027965518,0.0005592588,0.00013708256,0.00008428464,0.0001296173,0.00019048943,0.011873629,0.9847008,0.0005162014,0.0010863186,0.0001192095],"about_ca_topic_score_codex":0.000036634854,"about_ca_topic_score_gemma":0.0000031516263,"teacher_disagreement_score":0.011455815,"about_ca_system_score_codex":0.00015192965,"about_ca_system_score_gemma":0.00011216105,"threshold_uncertainty_score":0.37452206},"labels":[],"label_agreement":null},{"id":"W56123770","doi":"10.1016/s0009-2509(00)00345-6","title":"Eggshell catalyst in Fischer–Tropsch synthesis","year":2001,"lang":"en","type":"article","venue":"Chemical Engineering Science","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":34,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Fischer–Tropsch process; Catalysis; Eggshell; Adsorption; Chemistry; Chemical engineering; Organic chemistry; Engineering; Geology","score_opus":0.009739463496205381,"score_gpt":0.22739112384810173,"score_spread":0.21765166035189634,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W56123770","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9949128,0.00012790988,0.0019171046,0.00008761777,0.0001742387,0.000098699755,0.0000030966835,0.00031633227,0.0023621717],"genre_scores_gemma":[0.9974136,0.000009947418,0.0021788536,0.00001810816,0.00012170241,0.000042674706,0.0000045503352,0.000042767955,0.00016782078],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99762934,0.0000039531196,0.00038854455,0.0005712014,0.0005379342,0.00086900283],"domain_scores_gemma":[0.9988815,0.00019447797,0.000044211007,0.0005297138,0.000051892886,0.0002981747],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005277067,0.00026763938,0.0003270606,0.00036390292,0.000044059107,0.000036935955,0.0008608857,0.00012567574,0.00007173004],"category_scores_gemma":[0.002129674,0.00025983984,0.00010092238,0.002132036,0.00016803254,0.00046463538,0.00022517369,0.00044438947,0.000108540145],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000054777997,0.000028630013,0.00041543358,0.000039970255,0.0000049443993,0.000035915145,0.00008903041,0.004930222,0.99239933,0.0002684426,0.000005453042,0.001777154],"study_design_scores_gemma":[0.00017438573,0.0000038740905,0.00028315518,0.000106423395,0.000008619615,0.000086042404,0.000020722888,0.07797633,0.9199295,0.000012186541,0.0010598205,0.00033893978],"about_ca_topic_score_codex":0.000079704136,"about_ca_topic_score_gemma":0.0000015832084,"teacher_disagreement_score":0.07304611,"about_ca_system_score_codex":0.00049797737,"about_ca_system_score_gemma":0.0000608547,"threshold_uncertainty_score":0.9999854},"labels":[],"label_agreement":null},{"id":"W6921519812","doi":"10.71892/11143/900","title":"Development of nickel-based catalysts with biosurfactants for CO2 hydrogenation","year":2025,"lang":"en","type":"other","venue":"USherbrooke-PROD","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Methanation; Renewable energy; Greenhouse gas; Fossil fuel; Raw material; Substitute natural gas; Natural gas; Electricity","score_opus":0.013662795809397534,"score_gpt":0.2446634320839803,"score_spread":0.23100063627458278,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6921519812","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.065763496,0.006661995,0.13409898,0.00018018925,0.0021690545,0.010749428,0.0015383044,0.003369239,0.7754693],"genre_scores_gemma":[0.053468,0.00002305425,0.14237553,0.00006240922,0.00035875986,0.0007098419,0.0030966247,0.001928016,0.79797775],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979526,0.000010516646,0.0005861938,0.0005785641,0.0004452432,0.00042689382],"domain_scores_gemma":[0.9986772,0.0000700848,0.00039108735,0.0006466547,0.00011435027,0.00010064222],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00022088844,0.0004905444,0.0007261558,0.0004896504,0.000044985518,0.0000105649515,0.0003869141,0.00041996286,0.00015741453],"category_scores_gemma":[0.00012131589,0.00041991277,0.00017337936,0.0003729604,0.00005193954,0.00004835603,0.00006998101,0.0002048332,0.000044020195],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0007825631,0.00085269514,0.00042567338,0.028881688,0.0048062457,0.000034560508,0.0010278145,0.0013779314,0.8585241,0.0013657752,0.022172632,0.07974832],"study_design_scores_gemma":[0.0013099622,0.000031192845,0.0000062223357,0.0017698726,0.00016945574,0.0000020444825,0.000019743335,0.0011367048,0.80877674,0.000009098342,0.18626028,0.00050868705],"about_ca_topic_score_codex":0.00016274567,"about_ca_topic_score_gemma":0.00044997336,"teacher_disagreement_score":0.16408765,"about_ca_system_score_codex":0.00039265575,"about_ca_system_score_gemma":0.00053329166,"threshold_uncertainty_score":0.9998253},"labels":[],"label_agreement":null},{"id":"W6921729076","doi":"10.1021/acs.jpcc.5b07511.s001","title":"Pulsed Laser Deposition of PdCuAu Alloy Membranes\\nfor Hydrogen Absorption Study","year":2016,"lang":"en","type":"article","venue":"Figshare","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institut National de la Recherche Scientifique","funders":"","keywords":"Alloy; Pulsed laser deposition; Solubility; Deposition (geology); Hydrogen; Diffraction; Analytical Chemistry (journal); Solid solution","score_opus":0.019575444480460814,"score_gpt":0.2435354047771755,"score_spread":0.2239599602967147,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6921729076","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96804345,0.00006785305,0.000015295042,0.000029726989,0.00004835503,0.0005856855,0.029375156,0.00024444764,0.0015900171],"genre_scores_gemma":[0.9911075,9.407977e-7,0.00001696703,0.000008921745,0.00009304735,0.00012844201,0.008069863,0.000037855512,0.0005364393],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990135,0.000015308651,0.00028756735,0.00020676902,0.00025995896,0.00021689881],"domain_scores_gemma":[0.99933946,0.00009368699,0.00011217771,0.00030353578,0.0000748787,0.00007626168],"candidate_categories":["insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.000063244,0.00014629272,0.00020194003,0.00008646607,0.000025717447,0.000005789887,0.00017888244,0.000093457646,0.028034022],"category_scores_gemma":[0.00040037322,0.00010515608,0.000114182934,0.00014835199,0.0000037740433,0.0002393373,0.00008058225,0.00007344466,0.0010598473],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000033772765,0.00010484478,0.000052495983,0.00026351353,0.000072764764,0.000013580111,0.00014939808,0.00013406326,0.99270546,0.0000020933924,0.00045619797,0.006011807],"study_design_scores_gemma":[0.0008270029,0.000054689106,0.00033106003,0.0006710854,0.00002743661,0.000011555121,0.00003582242,0.000752534,0.99588966,0.0000061045575,0.0012212209,0.00017182749],"about_ca_topic_score_codex":0.000024489082,"about_ca_topic_score_gemma":0.000023136625,"teacher_disagreement_score":0.026974175,"about_ca_system_score_codex":0.000097150216,"about_ca_system_score_gemma":0.000017117074,"threshold_uncertainty_score":0.99971795},"labels":[],"label_agreement":null},{"id":"W6921984349","doi":"10.7939/r3hh46","title":"Experimental and Theoretical Investigation of Solar Molten Media Methane Cracking for Hydrogen Production","year":2014,"lang":"en","type":"dissertation","venue":"University of Alberta Library","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Blank; Methane; Cracking; Steam reforming; Hydrogen; Solar energy; Thermal; Kinetic energy","score_opus":0.00672544326370672,"score_gpt":0.19689230235196303,"score_spread":0.1901668590882563,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6921984349","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9973692,0.00025760615,0.000042992935,0.00008470429,0.00017836482,0.00025232442,0.000009625428,0.000033042004,0.0017720988],"genre_scores_gemma":[0.9943286,0.000028173063,0.0015327568,0.000004617982,0.00015659543,0.0000011384573,0.0021806294,0.000049609585,0.0017178467],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991683,0.000028281675,0.00021590132,0.00028277322,0.0001655364,0.00013922305],"domain_scores_gemma":[0.99920535,0.00022700817,0.00025103256,0.00019210062,0.000036628575,0.000087887514],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00009763263,0.00017689276,0.0003749715,0.00019224454,0.000038299695,0.0000033848592,0.00018215523,0.000254401,0.000092488444],"category_scores_gemma":[0.00013290989,0.00020021945,0.0001340277,0.000113270704,0.00013553438,0.00044409357,0.0000609102,0.00014221083,0.0000014665764],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006122807,0.000045817284,0.00034203805,0.0014467455,0.0002675875,0.0000017102843,0.020747563,0.000036959475,0.95223004,0.022860562,0.0000752785,0.0013334104],"study_design_scores_gemma":[0.00038168498,0.000045042638,0.00008911929,0.00023602531,0.00015692685,0.0000029637658,0.002872037,0.0011807199,0.99364394,0.00085799705,0.00034188264,0.00019168758],"about_ca_topic_score_codex":0.0001729901,"about_ca_topic_score_gemma":0.000020221274,"teacher_disagreement_score":0.041413866,"about_ca_system_score_codex":0.000024753137,"about_ca_system_score_gemma":0.00005070219,"threshold_uncertainty_score":0.8164712},"labels":[],"label_agreement":null},{"id":"W6940020017","doi":"10.6084/m9.figshare.c.5976096","title":"New neurons in old brains: implications of age in the analysis of neurogenesis in post-mortem tissue","year":2022,"lang":"en","type":"other","venue":"Figshare","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Neurogenesis; Hippocampus; Fixation (population genetics); Brain tissue; Ageing; Senescence; Adult male","score_opus":0.026456490252522787,"score_gpt":0.27677603626185604,"score_spread":0.25031954600933326,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6940020017","genre_codex":"dataset","genre_gemma":"dataset","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"dataset","genre_consensus":"dataset","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.03559915,0.005245398,0.0000062235445,0.00067750027,0.00011512237,0.0035089506,0.76836145,0.00032886784,0.18615732],"genre_scores_gemma":[0.2445343,0.00010431433,0.00024150802,0.000606493,0.00027160696,0.001951511,0.64306736,0.0016192236,0.10760369],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9987129,0.0000555106,0.00048089266,0.00030415322,0.00022996542,0.00021655633],"domain_scores_gemma":[0.99871975,0.00022516774,0.00024865541,0.0007530258,0.000014397042,0.000038990678],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00007475196,0.00020104971,0.0005665411,0.001446072,0.000007127426,0.0000045378956,0.0006925055,0.00014704847,0.082001045],"category_scores_gemma":[0.0006630662,0.00018372903,0.0001986742,0.0030754586,0.0000047082776,0.00003193708,0.00020062613,0.000350406,0.00002058559],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009015991,0.0018209607,0.010638589,0.008798632,0.0041643754,0.0016775274,0.012932324,0.034977112,0.23946734,0.00074418186,0.5850782,0.099610604],"study_design_scores_gemma":[0.0018233671,0.00010863304,0.20112415,0.00362823,0.0012070106,0.00003743422,0.00067736796,0.0013316202,0.015371212,0.000027462544,0.7730027,0.0016608321],"about_ca_topic_score_codex":0.0030112788,"about_ca_topic_score_gemma":0.015901554,"teacher_disagreement_score":0.22409613,"about_ca_system_score_codex":0.00009810606,"about_ca_system_score_gemma":0.00006500274,"threshold_uncertainty_score":0.91883814},"labels":[],"label_agreement":null},{"id":"W6959139135","doi":"10.1021/acs.iecr.5b02616.s001","title":"Modeling Vapor–Liquid–Liquid Phase Equilibria\\nin Fischer–Tropsch Syncrude","year":2016,"lang":"en","type":"article","venue":"Figshare","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Virial coefficient; Binary number; Non-random two-liquid model; Mixing (physics); Phase (matter); UNIQUAC; Equation of state; Cubic function","score_opus":0.04262077735076644,"score_gpt":0.2883932180488421,"score_spread":0.24577244069807566,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6959139135","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.88867164,0.0011909308,0.0019212882,0.00035185568,0.00028498753,0.00060756464,0.09857367,0.0016157716,0.006782287],"genre_scores_gemma":[0.9802539,0.0000063383327,0.00024206539,0.00006640854,0.00067831675,0.00022376598,0.016682457,0.00016844342,0.001678322],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976836,0.000026786383,0.00052716443,0.0005499267,0.00043229113,0.00078023906],"domain_scores_gemma":[0.99854815,0.00017840206,0.000108284345,0.0007144606,0.00012924697,0.00032147835],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00012725475,0.00038280748,0.00041080214,0.00014431632,0.00007436787,0.000027763397,0.00055797736,0.00026179312,0.07116722],"category_scores_gemma":[0.0021737204,0.0002863424,0.0002714466,0.00026696175,0.000009503965,0.0005545199,0.0003938012,0.0003068778,0.004028139],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021594386,0.000056241668,4.1080202e-7,0.0001904093,0.00006640584,0.00005922304,0.00008060958,0.00064919627,0.9911387,0.00003791611,0.004041654,0.003463286],"study_design_scores_gemma":[0.0021062577,0.00022048492,3.4492157e-7,0.0029269182,0.000036844835,0.000065038956,0.000023445516,0.08014527,0.8732356,0.000015209344,0.040493302,0.000731285],"about_ca_topic_score_codex":0.000021742639,"about_ca_topic_score_gemma":0.00000612411,"teacher_disagreement_score":0.117903106,"about_ca_system_score_codex":0.0002526875,"about_ca_system_score_gemma":0.00007625914,"threshold_uncertainty_score":0.9999589},"labels":[],"label_agreement":null},{"id":"W6959518891","doi":"10.1021/acscatal.6b01464.s001","title":"Zinc Hinders Deactivation of Copper-Mordenite: Dimethyl\\nEther Carbonylation","year":2016,"lang":"en","type":"article","venue":"Figshare","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Zinc; Carbonylation; Catalysis; Methanol; Selectivity; Dimethyl ether","score_opus":0.024993733171303916,"score_gpt":0.2467352451834493,"score_spread":0.2217415120121454,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6959518891","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.89392376,0.00077068014,0.00076953426,0.00050322345,0.00038799437,0.0011389347,0.063939445,0.0009892471,0.037577175],"genre_scores_gemma":[0.99308056,0.0000011048413,0.00007546892,0.000010764485,0.00009479834,0.000037158556,0.005943155,0.000035871526,0.0007211266],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99921745,0.000013092926,0.00021603139,0.00015932792,0.00022162695,0.00017249725],"domain_scores_gemma":[0.99930567,0.0002085684,0.00012439577,0.00022859618,0.00008090294,0.00005187545],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00005075029,0.00011562611,0.00015133074,0.000088265384,0.000018627834,0.0000040856758,0.00012321876,0.000113413575,0.0176692],"category_scores_gemma":[0.0012317728,0.000083767365,0.00007822094,0.00016462518,0.0000055374817,0.00021247313,0.000053295513,0.000085512496,0.00029184524],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000014656574,0.000014764987,0.00009760743,0.00013273377,0.00003442476,0.00000153641,0.00014634941,0.00007897238,0.97091836,0.000041349023,0.0024624493,0.026056776],"study_design_scores_gemma":[0.00040274885,0.000014435381,0.0006651182,0.00090470794,0.00001081901,0.0000036188856,0.000019243958,0.0007410054,0.982079,0.000054654378,0.014931559,0.0001730847],"about_ca_topic_score_codex":0.00003582245,"about_ca_topic_score_gemma":0.000008892753,"teacher_disagreement_score":0.09915679,"about_ca_system_score_codex":0.00013981012,"about_ca_system_score_gemma":0.000022137285,"threshold_uncertainty_score":0.9832288},"labels":[],"label_agreement":null},{"id":"W6977571372","doi":"10.71892/11143/907","title":"Développement de nouveaux catalyseurs partiellement biosourcés pour la synthèse Fischer-Tropsch à partir d'un biogaz","year":2025,"lang":"fr","type":"other","venue":"Open MIND","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Steam reforming; Hydrogen production; Pyrolysis; Catalysis; Methane reformer; Methane; Fluidized bed; Hydrogen; Biomass (ecology)","score_opus":0.023239780955301884,"score_gpt":0.29691522316270164,"score_spread":0.27367544220739976,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6977571372","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.17065284,0.005876157,0.008830003,0.010920679,0.0018535822,0.0037666042,0.0011547424,0.00007897351,0.7968664],"genre_scores_gemma":[0.042212512,0.00073173386,0.06843507,0.000141749,0.00075792096,0.00043997998,0.0007478777,0.00067893916,0.8858542],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9951083,0.00023076926,0.0012233786,0.0013698133,0.0005688563,0.0014988473],"domain_scores_gemma":[0.99696636,0.00038857953,0.0005240875,0.0014129217,0.00011269576,0.00059533364],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.0012071583,0.0011150476,0.0012804813,0.00038822764,0.00018265093,0.00029294268,0.0019458213,0.00092920347,0.06241968],"category_scores_gemma":[0.0005238772,0.0011136761,0.00050548546,0.0006588433,0.00016998852,0.00018593339,0.002007169,0.0009996032,0.005951674],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016368272,0.0011857942,0.0013667423,0.00079579133,0.0036921955,0.00060828956,0.0036315955,0.0006657053,0.1772853,0.00078524824,0.005853195,0.80396646],"study_design_scores_gemma":[0.0009571499,0.000029190745,0.000025714897,0.001064408,0.0006748681,0.000029600886,0.00053169014,0.000612682,0.4268319,0.000034590692,0.56844056,0.00076765363],"about_ca_topic_score_codex":0.00091281446,"about_ca_topic_score_gemma":0.00031879384,"teacher_disagreement_score":0.8031988,"about_ca_system_score_codex":0.0012143457,"about_ca_system_score_gemma":0.0008906751,"threshold_uncertainty_score":0.9991313},"labels":[],"label_agreement":null},{"id":"W6986356701","doi":"","title":"Performance of alumina supported Ni catalyst with core-shell and supported structures in dry reforming of methane","year":2023,"lang":"en","type":"dissertation","venue":"University Library (University of Saskatchewan)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Canadian Light Source","keywords":"Catalysis; Carbon dioxide reforming; Syngas; Methane; Sintering; X-ray photoelectron spectroscopy; Particle size; XANES; Industrial catalysts","score_opus":0.007595496231213977,"score_gpt":0.18373324546063285,"score_spread":0.17613774922941888,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6986356701","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978113,0.00006422934,0.00000567773,0.000011472145,0.00008446271,0.00028529746,0.0003238704,0.000109627734,0.0013040599],"genre_scores_gemma":[0.9756572,0.0001875154,0.0009800526,0.0000014547475,0.000012772411,8.54369e-8,0.003318797,0.000063108324,0.019779013],"study_design_codex":"bench_or_experimental","study_design_gemma":"qualitative","domain_scores_codex":[0.99831,0.00003079388,0.00037530548,0.0004894616,0.0004280704,0.00036636862],"domain_scores_gemma":[0.9984254,0.00010140797,0.0007404349,0.0004629265,0.00011374794,0.00015606672],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00013270212,0.00038930695,0.0010449433,0.0012627351,0.0000624509,0.0000030666083,0.000643703,0.0004596214,0.00017511855],"category_scores_gemma":[0.0000151720305,0.00045949224,0.00018523156,0.001288889,0.0002835733,0.0011584368,0.0002662834,0.0005059437,0.0000027004544],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.011687062,0.00043184884,0.20566304,0.02068821,0.0026041358,0.0016717553,0.20994596,0.0007413395,0.5312325,0.00019652018,0.000069719834,0.015067921],"study_design_scores_gemma":[0.0034224298,0.00037842817,0.054270428,0.001762096,0.00086194114,0.00001943507,0.47738326,0.0014357315,0.4593057,0.00004601609,0.00015453492,0.00095999666],"about_ca_topic_score_codex":0.011339552,"about_ca_topic_score_gemma":0.0071790065,"teacher_disagreement_score":0.26743728,"about_ca_system_score_codex":0.0001190132,"about_ca_system_score_gemma":0.0004394391,"threshold_uncertainty_score":0.99978566},"labels":[],"label_agreement":null},{"id":"W6990359982","doi":"","title":"Development of a catalyst dip-coating process for a catalytic plate reactor","year":2019,"lang":"en","type":"dissertation","venue":"eScholarship@McGill (McGill)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"McGill University","keywords":"Catalysis; Process (computing); Process control; Work (physics); Catalyst support","score_opus":0.022549705153076867,"score_gpt":0.266606353294744,"score_spread":0.24405664814166717,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6990359982","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9848463,0.00016881985,0.0000038785442,0.000001597653,0.00084217906,0.0016116664,0.0012957954,0.00031504553,0.010914724],"genre_scores_gemma":[0.9829493,0.00001057211,0.00226912,0.000013059176,0.000060666887,0.00058718456,0.008168332,0.0005051205,0.005436658],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9944344,0.00003481425,0.0020542128,0.0013106064,0.0010780201,0.001087918],"domain_scores_gemma":[0.9961129,0.00040296983,0.0015172826,0.0009923704,0.00063405366,0.00034041912],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0009983715,0.0010912868,0.001609341,0.0006411031,0.00040622626,0.0000321224,0.0010313704,0.0010069076,0.00003730225],"category_scores_gemma":[0.0019194598,0.0011202451,0.00061576895,0.000718001,0.00003409863,0.0007318701,0.00017108142,0.0013479127,0.00014534617],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00029659478,0.00014325773,0.0000052941127,0.007933874,0.00060835946,0.000011163685,0.00021714049,0.00007892608,0.9312962,0.0020235088,2.3263904e-7,0.05738544],"study_design_scores_gemma":[0.001248136,0.000051666168,0.000022824299,0.0021152392,0.00041818563,0.000023673001,0.0008614069,0.00035791323,0.98767614,0.00034350075,0.0055747833,0.001306506],"about_ca_topic_score_codex":0.00019679304,"about_ca_topic_score_gemma":0.0004911852,"teacher_disagreement_score":0.05637996,"about_ca_system_score_codex":0.0014303665,"about_ca_system_score_gemma":0.00026807762,"threshold_uncertainty_score":0.99912477},"labels":[],"label_agreement":null},{"id":"W6991028401","doi":"","title":"Experimental studies of catalyst deactivation due to carbon and sulphur during CO 2 reforming of CH 4 over Ni washcoated monolith in the presence of H 2 S","year":2021,"lang":"en","type":"article","venue":"Research Archive of Indian Institute of Technology Hyderabad (Indian Institute of Technology Hyderabad)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Monolith; Catalysis; Cordierite; Sulfur; Carbon fibers; Catalyst poisoning","score_opus":0.024107323703189874,"score_gpt":0.32077582947247346,"score_spread":0.2966685057692836,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6991028401","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9948423,0.0024640483,0.00003114597,0.00070574164,0.00016308676,0.0011039787,0.00016654754,0.00008031744,0.00044282625],"genre_scores_gemma":[0.99642277,0.000578227,0.00266633,0.0000042975043,0.000025805552,0.00016085872,0.00006220245,0.000053230255,0.000026299045],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99488366,0.00012459277,0.0020971578,0.0008548129,0.0010631055,0.0009766525],"domain_scores_gemma":[0.9961972,0.0002955404,0.0010559717,0.0016012605,0.00071842526,0.0001315711],"candidate_categories":["metaepi_narrow","sts"],"consensus_categories":[],"category_scores_codex":[0.0012279107,0.0005120756,0.0018875255,0.006319459,0.0001929303,0.0000070784117,0.0016255459,0.0007321615,0.000005721042],"category_scores_gemma":[0.0035161115,0.00046462665,0.00022119297,0.004397061,0.0055437875,0.0005434518,0.001246446,0.0013957103,9.10294e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028527057,0.0005468567,0.008830486,0.0023422039,0.0005981982,0.00040187212,0.0064941067,0.0002941702,0.97108126,0.0056566275,0.0000063588736,0.0034625954],"study_design_scores_gemma":[0.0017587192,0.00047756467,0.0020802661,0.002559772,0.000043035372,0.00044222074,0.011731254,0.00009152671,0.9788545,0.0015387272,0.000091947375,0.00033049678],"about_ca_topic_score_codex":0.0026133216,"about_ca_topic_score_gemma":0.0014964201,"teacher_disagreement_score":0.007773216,"about_ca_system_score_codex":0.00035185652,"about_ca_system_score_gemma":0.0006235163,"threshold_uncertainty_score":0.99978054},"labels":[],"label_agreement":null},{"id":"W6991119646","doi":"","title":"Étude théorique des composés métallo-organiques et des catalyseurs pour la réduction de l’oxygène dans les piles à combustible.","year":2020,"lang":"fr","type":"dissertation","venue":"EspaceINRS Institutional Digital Repository (Institut National de la Recherche Scientifique)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Sugar industry; Western europe; General interest","score_opus":0.0882650318704844,"score_gpt":0.339932942726801,"score_spread":0.2516679108563166,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6991119646","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6481864,0.0025629012,0.14069264,0.0009024865,0.0016544953,0.001050529,0.0007914786,0.0009097887,0.20324928],"genre_scores_gemma":[0.9286836,0.00086018833,0.043807656,0.00007747927,0.0007901096,0.00025601286,0.004966824,0.00022458698,0.020333573],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99209625,0.0017289312,0.0014057698,0.0016214284,0.0020414281,0.0011061928],"domain_scores_gemma":[0.9918444,0.003962305,0.00071096903,0.00048647393,0.002087326,0.0009085006],"candidate_categories":["metaresearch","metaepi_narrow","sts","scholarly_communication","research_integrity"],"consensus_categories":["sts","research_integrity"],"category_scores_codex":[0.004497894,0.0012605609,0.000932845,0.00081339694,0.0015986119,0.0014283361,0.0012063994,0.0023423,0.00003083201],"category_scores_gemma":[0.019425333,0.0013998115,0.00083728007,0.0018407214,0.0033552474,0.0030250377,0.00034775192,0.0037335989,0.00009316554],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":true,"study_design_scores_codex":[0.00028080834,0.0008822028,0.0036117393,0.002316974,0.0008418305,0.0004633541,0.013545512,0.052826192,0.76693004,0.15342501,0.0002558367,0.0046205297],"study_design_scores_gemma":[0.0013383317,0.000094095616,0.012684467,0.005388819,0.00047305538,0.0044493577,0.002450208,0.019042736,0.9046678,0.020736262,0.02653515,0.0021397118],"about_ca_topic_score_codex":0.0013535154,"about_ca_topic_score_gemma":0.0011183413,"teacher_disagreement_score":0.28049716,"about_ca_system_score_codex":0.01328626,"about_ca_system_score_gemma":0.009439526,"threshold_uncertainty_score":0.99970114},"labels":[],"label_agreement":null},{"id":"W6996775460","doi":"","title":"Synthesis of carbon nanotubes supported iron catalysts for light olefins via Fischer-Tropsch synthesis","year":2023,"lang":"en","type":"dissertation","venue":"University Library (University of Saskatchewan)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada; University of Saskatchewan","keywords":"Catalysis; Syngas; Selectivity; Carbon nanotube; Hydrocarbon; Acetylene; Yield (engineering); Olefin fiber","score_opus":0.006218243539394409,"score_gpt":0.17646590127950693,"score_spread":0.17024765774011252,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6996775460","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99211335,0.000093860355,0.00007477255,0.00016166909,0.00034523173,0.00055174547,0.0011314149,0.000488816,0.005039123],"genre_scores_gemma":[0.93461406,0.00009709137,0.0012196023,0.0000024815977,0.00007708685,0.0000011671195,0.0024801374,0.00017612411,0.06133224],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976602,0.000070479095,0.00041795126,0.00077294407,0.0005094656,0.00056895573],"domain_scores_gemma":[0.99744177,0.0006644529,0.00071027345,0.0007670616,0.00016188344,0.00025456081],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00015444146,0.0005826964,0.001329885,0.0011674061,0.00020054293,0.000009960594,0.0012590997,0.0009277057,0.00020382469],"category_scores_gemma":[0.00011462994,0.0007866818,0.0009260346,0.0010502937,0.00013733217,0.0008849324,0.00030720932,0.0004403073,0.00002587857],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0054345513,0.0008866389,0.004051844,0.018217571,0.005074132,0.0007738327,0.06954821,0.00025060234,0.8778568,0.0002205958,0.0022390252,0.015446216],"study_design_scores_gemma":[0.00078309927,0.000076984776,0.00081983773,0.0010198058,0.0019174512,0.0000044833732,0.11783534,0.00051434734,0.87389827,0.000039781833,0.0021684037,0.0009221886],"about_ca_topic_score_codex":0.006530706,"about_ca_topic_score_gemma":0.005222711,"teacher_disagreement_score":0.0574993,"about_ca_system_score_codex":0.00024623322,"about_ca_system_score_gemma":0.0004582122,"threshold_uncertainty_score":0.99945843},"labels":[],"label_agreement":null},{"id":"W6996818542","doi":"","title":"Syngas to liquid biofuels through Fisher-Tropsch synthesis using structured catalysts","year":2024,"lang":"en","type":"dissertation","venue":"Knowledge UdeS (Institutional Deposit of the University of Sherbrooke)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"European Commission","keywords":"Syngas; Biofuel; Raw material; Biomass (ecology); Fossil fuel; Renewable energy; Liquid fuel; Renewable fuels; Biomass to liquid; Lignocellulosic biomass","score_opus":0.013788062841015419,"score_gpt":0.23142728473640928,"score_spread":0.21763922189539386,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W6996818542","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9782797,0.005759233,0.0027410663,0.00002831771,0.001550931,0.00047046097,0.0001047266,0.00011327434,0.0109522985],"genre_scores_gemma":[0.9912705,0.00012718461,0.0037160157,0.000004865239,0.00016683285,0.0000019276627,0.00015892553,0.00007192197,0.0044818595],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979059,0.000047458147,0.00051676086,0.0005706175,0.0005939678,0.0003652934],"domain_scores_gemma":[0.998703,0.00007774148,0.00019956994,0.0006272799,0.0002524421,0.00013993769],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00013546563,0.0004905874,0.00077707204,0.00034469162,0.00031671286,0.000017900988,0.0011764412,0.0005148748,0.000059838134],"category_scores_gemma":[0.00021695382,0.00045364612,0.00074713735,0.00077744905,0.00021396462,0.0002872239,0.00039256908,0.00054748903,0.000064214866],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00039499658,0.00009609829,0.000025588322,0.012037434,0.00080078654,0.000028687304,0.008104841,0.01414473,0.961964,0.0010629114,0.00013265308,0.001207261],"study_design_scores_gemma":[0.00023308118,0.00003945229,0.00029008806,0.011612191,0.0011549342,0.00004387478,0.0005461105,0.0031311468,0.9783407,0.00009294975,0.004026826,0.00048867724],"about_ca_topic_score_codex":0.0043525626,"about_ca_topic_score_gemma":0.009285271,"teacher_disagreement_score":0.016376654,"about_ca_system_score_codex":0.002243719,"about_ca_system_score_gemma":0.00033196996,"threshold_uncertainty_score":0.9997915},"labels":[],"label_agreement":null},{"id":"W7011527522","doi":"","title":"$10.65 Million in Sales Expected for Hydrogenics Co. (HYGS) This Quarter","year":2018,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Payment; Revenue; Work (physics)","score_opus":0.013328953231712775,"score_gpt":0.2578791480320614,"score_spread":0.24455019480034865,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7011527522","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0014708776,0.0010330958,0.0016284477,0.000027025213,0.00031888532,0.0008344566,0.000102497856,0.0009211755,0.99366355],"genre_scores_gemma":[0.0008427288,0.00003925543,0.0016620074,0.00001911547,0.0006767695,0.00013048122,0.0007297632,0.0007211502,0.9951787],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.99847436,0.000012506571,0.00039024212,0.00044899783,0.00022874087,0.00044516902],"domain_scores_gemma":[0.99913657,0.00008329527,0.0001365381,0.00051805115,0.000031847667,0.00009372519],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00013067655,0.00039009782,0.00054117397,0.0004657025,0.000017267095,0.000011849088,0.0002922932,0.0006385962,0.022785788],"category_scores_gemma":[0.00009777853,0.00033639855,0.00024842066,0.0002150285,0.000041754654,0.000049892493,0.000050378025,0.00017787846,0.00387799],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006720023,0.000058183785,0.000010450452,0.0005235079,0.00024068909,0.000009570556,0.00021169751,0.0000044531107,0.03149551,0.00016463087,0.965291,0.0019230932],"study_design_scores_gemma":[0.000722998,0.000044400273,4.3528382e-7,0.00024898147,0.000039982264,0.000008336684,0.000039769813,0.0020003594,0.06594859,0.000019428653,0.9304323,0.00049438654],"about_ca_topic_score_codex":0.0002320192,"about_ca_topic_score_gemma":0.0003302378,"teacher_disagreement_score":0.034858685,"about_ca_system_score_codex":0.0002522491,"about_ca_system_score_gemma":0.000035390676,"threshold_uncertainty_score":0.9999088},"labels":[],"label_agreement":null},{"id":"W7011620960","doi":"","title":"$10.20 Million in Sales Expected for Hydrogenics Co. (HYGS) This Quarter","year":2018,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Payment; Revenue; Work (physics)","score_opus":0.013172217563134626,"score_gpt":0.25585037102960584,"score_spread":0.2426781534664712,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7011620960","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0011280241,0.00094004365,0.001513328,0.000030845804,0.00029945615,0.0007997446,0.00012326513,0.0008886835,0.9942766],"genre_scores_gemma":[0.0006268536,0.000031823645,0.0015833683,0.000018975947,0.0006846878,0.00012545225,0.0009143226,0.0007085072,0.995306],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9984878,0.000012322769,0.00038728293,0.00044613954,0.00022651721,0.0004399967],"domain_scores_gemma":[0.99914867,0.00008201637,0.00013574648,0.00050816033,0.00003120769,0.00009420612],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00012495587,0.00038815287,0.00053925934,0.0004563499,0.000016974313,0.0000117076925,0.00029102628,0.0006330753,0.021530077],"category_scores_gemma":[0.000088766436,0.0003349922,0.0002470985,0.00021448128,0.000041155337,0.000049670238,0.00004974479,0.00017691533,0.0037098082],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000619874,0.000051725907,0.000009919489,0.00047595147,0.0002163211,0.00000865104,0.00019067292,0.0000048849643,0.037380245,0.00012622587,0.9600991,0.0013743257],"study_design_scores_gemma":[0.000702129,0.00004326567,2.8139087e-7,0.0002363538,0.000037349855,0.000007879146,0.000038737056,0.0022014596,0.06563146,0.00001809334,0.93060696,0.0004760357],"about_ca_topic_score_codex":0.00018098942,"about_ca_topic_score_gemma":0.00043632748,"teacher_disagreement_score":0.029492132,"about_ca_system_score_codex":0.0002486548,"about_ca_system_score_gemma":0.000035536134,"threshold_uncertainty_score":0.99991024},"labels":[],"label_agreement":null},{"id":"W7020906811","doi":"","title":"$10.65 Million in Sales Expected for Hydrogenics Co. (HYGS) This Quarter","year":2018,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Payment; Revenue; Work (physics)","score_opus":0.013328953231712775,"score_gpt":0.2578791480320614,"score_spread":0.24455019480034865,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7020906811","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0014708776,0.0010330958,0.0016284477,0.000027025213,0.00031888532,0.0008344566,0.000102497856,0.0009211755,0.99366355],"genre_scores_gemma":[0.0008427288,0.00003925543,0.0016620074,0.00001911547,0.0006767695,0.00013048122,0.0007297632,0.0007211502,0.9951787],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.99847436,0.000012506571,0.00039024212,0.00044899783,0.00022874087,0.00044516902],"domain_scores_gemma":[0.99913657,0.00008329527,0.0001365381,0.00051805115,0.000031847667,0.00009372519],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00013067655,0.00039009782,0.00054117397,0.0004657025,0.000017267095,0.000011849088,0.0002922932,0.0006385962,0.022785788],"category_scores_gemma":[0.00009777853,0.00033639855,0.00024842066,0.0002150285,0.000041754654,0.000049892493,0.000050378025,0.00017787846,0.00387799],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006720023,0.000058183785,0.000010450452,0.0005235079,0.00024068909,0.000009570556,0.00021169751,0.0000044531107,0.03149551,0.00016463087,0.965291,0.0019230932],"study_design_scores_gemma":[0.000722998,0.000044400273,4.3528382e-7,0.00024898147,0.000039982264,0.000008336684,0.000039769813,0.0020003594,0.06594859,0.000019428653,0.9304323,0.00049438654],"about_ca_topic_score_codex":0.0002320192,"about_ca_topic_score_gemma":0.0003302378,"teacher_disagreement_score":0.034858685,"about_ca_system_score_codex":0.0002522491,"about_ca_system_score_gemma":0.000035390676,"threshold_uncertainty_score":0.9999088},"labels":[],"label_agreement":null},{"id":"W7024153399","doi":"","title":"PROCEEDINGS FROM SCIENTIFIC CONFERENCE ON GREEN ENERGY AND IT","year":2008,"lang":"en","type":"article","venue":"DiVA (Mälardalen University College)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Thermal energy; Sustainable energy; Cogeneration; Chinese academy of sciences; Electricity generation; Biofuel; Thermal power station","score_opus":0.021750072013438777,"score_gpt":0.1886327624754455,"score_spread":0.1668826904620067,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7024153399","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9861468,0.00003373778,0.00017351788,0.00053657155,0.00010762019,0.00009218179,0.00033095913,0.00014547262,0.012433161],"genre_scores_gemma":[0.95219594,0.000033044606,0.00018265007,0.000064299755,0.00006143936,5.8324343e-7,0.000042456675,0.000018087841,0.047401488],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.9987749,0.000009307892,0.00012566072,0.00046176254,0.00033357355,0.00029478295],"domain_scores_gemma":[0.99936116,0.000052563246,0.00006352764,0.0002041752,0.0001234711,0.00019508773],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00007750548,0.00018988982,0.00024812482,0.0002265759,0.00036798965,0.000015600108,0.00032677737,0.00012417269,0.00014687027],"category_scores_gemma":[0.00002672784,0.00020696527,0.00008145744,0.00040602277,0.00021439588,0.00031278725,0.00025149516,0.00015553362,0.00003697136],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0011129407,0.0005688484,0.008685504,0.0003018706,0.00079782517,0.002182764,0.0111332545,0.00007819812,0.67098516,0.26913682,0.02942656,0.0055902707],"study_design_scores_gemma":[0.0062655434,0.00024559392,0.004307584,0.00049219956,0.00028492123,0.00021859788,0.0038672609,0.04059359,0.3750731,0.001219381,0.5652539,0.002178281],"about_ca_topic_score_codex":0.0017326804,"about_ca_topic_score_gemma":0.000114634706,"teacher_disagreement_score":0.5358274,"about_ca_system_score_codex":0.0001882137,"about_ca_system_score_gemma":0.00006105507,"threshold_uncertainty_score":0.8439799},"labels":[],"label_agreement":null},{"id":"W7024245410","doi":"","title":"Reaching out: A look at initiatives – old and new – to increase diversity in Canadian law schools.","year":2020,"lang":"en","type":"article","venue":"eYLS (Yale Law School)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Diversity (politics); Legislation; Government (linguistics); Work (physics)","score_opus":0.025095665328962895,"score_gpt":0.24043999765792823,"score_spread":0.21534433232896533,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7024245410","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.973178,0.00026690788,0.00004503634,0.0015176855,0.000079539495,0.0002812089,0.00006644528,0.00014756354,0.024417581],"genre_scores_gemma":[0.9947312,0.000011666902,0.000587573,0.0036672219,0.00021745329,0.000008172155,0.00003811132,0.000042192154,0.0006963966],"study_design_codex":"observational","study_design_gemma":"not_applicable","domain_scores_codex":[0.9983004,0.000043667726,0.00028183885,0.00048848963,0.000251431,0.0006342072],"domain_scores_gemma":[0.99711454,0.00007468805,0.000051387982,0.00029284306,0.000026128324,0.0024403976],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00025248752,0.00026147737,0.0003636306,0.00010021751,0.0002480186,0.000052418338,0.0003156355,0.00013947084,0.00015152691],"category_scores_gemma":[0.0006803875,0.00028176926,0.00007780263,0.00028355065,0.000039176117,0.0006162283,0.00081940985,0.00062729756,0.0003702508],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":true,"about_ca_topic_consensus":true,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010525165,0.00016849131,0.34051856,0.0010861958,0.00063863734,0.002675226,0.04007743,0.0018788737,0.305936,0.29634264,0.0039081005,0.005717315],"study_design_scores_gemma":[0.016006557,0.00060572574,0.033855334,0.0023717845,0.00051162776,0.00023183666,0.0039290227,0.0059896684,0.3225613,0.0039626956,0.602727,0.0072474484],"about_ca_topic_score_codex":0.81877553,"about_ca_topic_score_gemma":0.7561884,"teacher_disagreement_score":0.5988189,"about_ca_system_score_codex":0.000855089,"about_ca_system_score_gemma":0.00012939863,"threshold_uncertainty_score":0.99996346},"labels":[],"label_agreement":null},{"id":"W7026674941","doi":"","title":"Approximation des fonctions harmoniques par des séries universelles surconvergentes","year":2012,"lang":"fr","type":"other","venue":"Library and Archives Canada (Government of Canada)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Term (time); Function (biology); Division (mathematics); Context (archaeology); Order (exchange)","score_opus":0.005384881156256358,"score_gpt":0.1449115274447301,"score_spread":0.13952664628847375,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7026674941","genre_codex":"other","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.07896471,0.009160558,0.0020240275,0.0006218656,0.00070905435,0.0005352345,0.00073981116,0.00008169739,0.907163],"genre_scores_gemma":[0.54182124,0.0034152553,0.008246359,0.00010110219,0.0003487334,0.000040502677,0.00011180016,0.00026590165,0.4456491],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99757755,0.00007056687,0.0004347701,0.00032122986,0.0010095217,0.0005863394],"domain_scores_gemma":[0.99868023,0.00030795363,0.000293963,0.00026985176,0.0000015812191,0.00044644164],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.000018024233,0.00046319596,0.0005038895,0.00006943773,0.0002959014,0.00002387392,0.0002645873,0.00011217942,0.0013281965],"category_scores_gemma":[0.000014596191,0.00046979674,0.00009631415,0.00013773012,0.00046157397,0.00073667034,0.00020831774,0.00027024111,4.1675463e-8],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":true,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004926251,0.00022103109,0.059335545,0.009556946,0.0020319724,0.00012215336,0.0019304497,0.00043578402,0.3817634,0.37568396,0.0010833796,0.16734277],"study_design_scores_gemma":[0.00031706505,0.00003534662,0.0048324903,0.000990424,0.00020226494,0.000022801929,0.0036974037,0.0018313689,0.72070414,0.0012573423,0.26548335,0.0006260222],"about_ca_topic_score_codex":0.017384823,"about_ca_topic_score_gemma":0.05006351,"teacher_disagreement_score":0.46285656,"about_ca_system_score_codex":0.00007183637,"about_ca_system_score_gemma":0.0008889709,"threshold_uncertainty_score":0.99977535},"labels":[],"label_agreement":null},{"id":"W7030254027","doi":"","title":"$13.75 Million in Sales Expected for Hydrogenics Co. (HYGS) This Quarter","year":2018,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Payment; Revenue; Work (physics)","score_opus":0.013105878802956526,"score_gpt":0.2607808143651274,"score_spread":0.24767493556217088,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7030254027","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.007177272,0.0017064543,0.0044665406,0.00004388617,0.0007691068,0.0013493113,0.0001547769,0.0014400186,0.98289263],"genre_scores_gemma":[0.004178938,0.00009436065,0.0025435307,0.000041983836,0.0010256572,0.00018551809,0.0009168688,0.0010541641,0.989959],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9984435,0.000012665246,0.00039856078,0.00045476554,0.00023230624,0.00045823588],"domain_scores_gemma":[0.99913305,0.00008424456,0.00013798443,0.00051934354,0.000029233839,0.000096131465],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00013201991,0.00039629426,0.0005542043,0.00047601294,0.000017793152,0.0000119972165,0.00029622525,0.0006496072,0.004481376],"category_scores_gemma":[0.000087059656,0.00034113135,0.00025243874,0.00022088856,0.000042693908,0.000051041723,0.000050647504,0.00020124731,0.0011723689],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000682075,0.00009331117,0.0000733302,0.0008634905,0.0003900258,0.000017013579,0.00051794853,0.000009520957,0.07372423,0.0003538536,0.9215072,0.0023818885],"study_design_scores_gemma":[0.0009947172,0.00004335597,0.0000016477433,0.00035997553,0.000054370066,0.000013199002,0.00007848581,0.0029560158,0.104083486,0.0000401351,0.89070594,0.0006686629],"about_ca_topic_score_codex":0.00043882054,"about_ca_topic_score_gemma":0.00063352025,"teacher_disagreement_score":0.03080123,"about_ca_system_score_codex":0.0002517243,"about_ca_system_score_gemma":0.000031127096,"threshold_uncertainty_score":0.9999041},"labels":[],"label_agreement":null},{"id":"W7034497240","doi":"","title":"U.S. Energy Initiatives Travels To Canada To Methes Plant - Spokane, North Idaho News &amp;amp; Weather KHQ.com","year":2013,"lang":"en","type":"other","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Energy (signal processing); Renewable energy; Climate change; Government (linguistics)","score_opus":0.016915381195551044,"score_gpt":0.22879994530466188,"score_spread":0.21188456410911083,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7034497240","genre_codex":"other","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":"other","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0040886267,0.0005358877,0.023796633,0.0005132933,0.00090249284,0.000886396,0.0012596365,0.0007460868,0.967271],"genre_scores_gemma":[0.0021534248,0.00006520985,0.004030544,0.0012083156,0.00077326724,0.00018218755,0.00068922836,0.0010168147,0.989881],"study_design_codex":"not_applicable","study_design_gemma":"not_applicable","domain_scores_codex":[0.9971567,0.000038401773,0.0005766828,0.000754728,0.00062159856,0.0008518969],"domain_scores_gemma":[0.99793357,0.00015792527,0.0001779976,0.00096459896,0.000045103898,0.0007208001],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.000083843544,0.0008323739,0.0010562397,0.0005309797,0.000040003586,0.000038258597,0.00071254425,0.00036160473,0.009209896],"category_scores_gemma":[0.00012544497,0.00066924706,0.00019645844,0.0004629119,0.000024779189,0.00007560954,0.00023627953,0.00036504757,0.00089080766],"study_design_candidate":"not_applicable","study_design_consensus":"not_applicable","about_ca_topic_candidate":true,"about_ca_topic_consensus":true,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000057971145,0.00012018723,0.00016317786,0.00044668835,0.0016844312,0.00008912332,0.0017086235,0.000592819,0.022786627,0.0027877402,0.93205124,0.037511367],"study_design_scores_gemma":[0.00018549092,0.00001213111,0.00002513837,0.00020780838,0.00005811186,0.000018389968,0.00006798369,0.00003306997,0.012446318,0.0000081216895,0.9859664,0.0009710801],"about_ca_topic_score_codex":0.91545093,"about_ca_topic_score_gemma":0.9780351,"teacher_disagreement_score":0.06258412,"about_ca_system_score_codex":0.00048267195,"about_ca_system_score_gemma":0.00026274065,"threshold_uncertainty_score":0.9998871},"labels":[],"label_agreement":null},{"id":"W7038843886","doi":"","title":"La prévention des blessures causées par les véhicules tout-terrains","year":2012,"lang":"fr","type":"article","venue":"Europe PMC (PubMed Central)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Poison control; Context (archaeology); Criminal liability; Child pornography","score_opus":0.024166209118318415,"score_gpt":0.23584288037838863,"score_spread":0.21167667126007023,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7038843886","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95171255,0.035835024,0.0008209869,0.00039841243,0.0031681976,0.0005128607,0.00009474114,0.0003876973,0.0070695556],"genre_scores_gemma":[0.9840675,0.0024399806,0.00069818995,0.000031517277,0.0021273878,0.000080206206,0.00010929135,0.0002265058,0.010219407],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99468184,0.00041364768,0.0007733975,0.0005715942,0.0005623687,0.0029971662],"domain_scores_gemma":[0.99765146,0.0002876767,0.00026425408,0.00062263524,0.00011782498,0.0010561678],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001221154,0.000670709,0.0005951998,0.0001884676,0.0002716759,0.00012946452,0.0005112622,0.00041241216,0.00040196136],"category_scores_gemma":[0.0013608854,0.000646153,0.0004032373,0.00060164504,0.00051789347,0.001016387,0.00033003595,0.000888945,0.000283666],"study_design_candidate":"design_other","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014213444,0.0016629356,0.13500923,0.0045173634,0.0015009078,0.000345118,0.04038736,0.0011181389,0.13176093,0.014311361,0.001616436,0.6676281],"study_design_scores_gemma":[0.0009910157,0.000034239467,0.11350349,0.00089507544,0.0006070556,0.00030991508,0.0006169434,0.00016388185,0.29793862,0.0000965345,0.5837405,0.001102761],"about_ca_topic_score_codex":0.0003080488,"about_ca_topic_score_gemma":0.00008639625,"teacher_disagreement_score":0.6665253,"about_ca_system_score_codex":0.00071056926,"about_ca_system_score_gemma":0.000073092204,"threshold_uncertainty_score":0.999599},"labels":[],"label_agreement":null},{"id":"W7039178750","doi":"","title":"[Letter from Geo. W. Manypenny on] Has received accounts for 3rd quarter of 1853, and from which you shall hear in due time","year":2013,"lang":"en","type":"article","venue":"ThinkTech (Texas Tech University)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Quarter (Canadian coin); Period (music); Ridiculous; Tone (literature); Window (computing)","score_opus":0.010785161281489536,"score_gpt":0.1873912564135338,"score_spread":0.17660609513204426,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7039178750","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.995514,0.00003740999,0.00055486476,0.0008579197,0.00007104203,0.0005754128,0.00016545363,0.00018780677,0.0020361252],"genre_scores_gemma":[0.9942173,0.000013248663,0.0029644317,0.00016349915,0.00010584666,0.000004997621,0.00016817571,0.000059065023,0.002303441],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985026,0.00003014397,0.00029793734,0.00051273336,0.00024829342,0.00040829688],"domain_scores_gemma":[0.9987962,0.00028472237,0.00013375063,0.0005493817,0.000114767165,0.00012114585],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001584894,0.00029052442,0.0005261319,0.0004624298,0.00006421124,0.00003384142,0.00049666886,0.0003611207,0.00048330493],"category_scores_gemma":[0.00009519023,0.00029350678,0.000114662296,0.0004501189,0.00008022906,0.0004908902,0.00020621915,0.00043475666,0.0002661902],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00047004636,0.00027131225,0.001808285,0.00013492076,0.00040117613,0.00008144355,0.0014896024,0.000101690304,0.988456,0.0005566284,0.0024227418,0.003806161],"study_design_scores_gemma":[0.011075918,0.0005219345,0.016545767,0.0011082757,0.0004303333,0.0000149217485,0.00078817655,0.022279045,0.8630878,0.007349516,0.07452783,0.0022704827],"about_ca_topic_score_codex":0.0036668761,"about_ca_topic_score_gemma":0.0002188613,"teacher_disagreement_score":0.1253682,"about_ca_system_score_codex":0.00025580515,"about_ca_system_score_gemma":0.000032938835,"threshold_uncertainty_score":0.9999517},"labels":[],"label_agreement":null},{"id":"W7043708426","doi":"","title":"Thermo-neutral methane reforming using a flow-through porous Rh-impregnated membrane catalyst reactor for carbon capture and utilisation.","year":2021,"lang":"en","type":"article","venue":"Open Access Institutional Repository at Robert Gordon University (Robert Gordon University)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Emissions Reduction Alberta","keywords":"Methane; Flue gas; Steam reforming; Syngas; Carbon dioxide reforming; Methane reformer; Catalytic reforming; Catalysis; Carbon dioxide","score_opus":0.03116561712853543,"score_gpt":0.2695165161977109,"score_spread":0.23835089906917545,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7043708426","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9395886,0.00047949693,0.0034663957,0.00022034327,0.0008157648,0.0010391464,0.00023132632,0.00025071215,0.053908207],"genre_scores_gemma":[0.96091104,0.00020182204,0.004901576,0.0000897938,0.00022218475,0.0000040662885,0.001124981,0.00010242237,0.032442104],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99663126,0.00018291798,0.00052465557,0.0013620632,0.0005228018,0.00077631854],"domain_scores_gemma":[0.99741775,0.00025801835,0.0004643416,0.00082791876,0.0006023379,0.00042962722],"candidate_categories":["metaepi_narrow","sts"],"consensus_categories":[],"category_scores_codex":[0.00029206727,0.00065725687,0.0008866985,0.00048884284,0.0013762948,0.00021971164,0.0017420724,0.000555103,0.000077302335],"category_scores_gemma":[0.00018919232,0.0007586709,0.000362719,0.0014452491,0.00039161238,0.0044119223,0.0029644254,0.00059783534,0.0000034975533],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_system_candidate":true,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0022793498,0.00045217076,0.0012264273,0.0006768369,0.0014260458,0.0057574976,0.0017366483,0.02450717,0.94122785,0.01949823,0.000047582562,0.0011641822],"study_design_scores_gemma":[0.0063886875,0.00008423947,0.00025706948,0.00073326996,0.0013528683,0.0026164344,0.0025689632,0.028808367,0.8431891,0.00008833275,0.111936845,0.001975813],"about_ca_topic_score_codex":0.026337583,"about_ca_topic_score_gemma":0.003566962,"teacher_disagreement_score":0.111889265,"about_ca_system_score_codex":0.004405549,"about_ca_system_score_gemma":0.0010820141,"threshold_uncertainty_score":0.99992377},"labels":[],"label_agreement":null},{"id":"W7071605395","doi":"","title":"Techno-Economic Analysis of a Biomass-Gas-and-Nuclear-to-Liquid Polygeneration Plant","year":2022,"lang":"en","type":"dissertation","venue":"MacSphere (McMaster University)","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Work (physics); Production (economics); Exclosure; Diafiltration; Limiting; Gloom","score_opus":0.007511434311790199,"score_gpt":0.20125864086563697,"score_spread":0.19374720655384678,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7071605395","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.913824,0.0001236512,0.00012072268,0.000029224864,0.00024093597,0.00026558162,0.0004688098,0.00016169291,0.08476535],"genre_scores_gemma":[0.6872244,0.000080273174,0.0005839434,0.000029466122,0.00011056072,0.000007877927,0.0056276135,0.00019891562,0.30613694],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.99865407,0.00002611289,0.00033252468,0.000501575,0.00022234736,0.0002633856],"domain_scores_gemma":[0.9992042,0.000035261997,0.00026041307,0.00034054677,0.00003059268,0.00012893825],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00009281802,0.0003060459,0.0006457774,0.0013740032,0.00010292404,0.000017097067,0.00038812173,0.00025251647,0.03531272],"category_scores_gemma":[0.000014299541,0.00036832446,0.00033146318,0.0012482399,0.000021779657,0.00014246137,0.00020921048,0.000278598,0.00002089399],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0016301862,0.00009697958,0.0002010657,0.00060021185,0.00639547,0.00010304575,0.0036704356,0.00811111,0.8746534,0.0064242557,0.000066078734,0.09804775],"study_design_scores_gemma":[0.0022307064,0.00064680184,0.00033745085,0.00032164124,0.013404135,0.00002713249,0.021284154,0.072932035,0.40732124,0.00002049082,0.47866407,0.0028101392],"about_ca_topic_score_codex":0.0022417468,"about_ca_topic_score_gemma":0.0021895203,"teacher_disagreement_score":0.478598,"about_ca_system_score_codex":0.00057756365,"about_ca_system_score_gemma":0.000052448497,"threshold_uncertainty_score":0.99987686},"labels":[],"label_agreement":null},{"id":"W7099094319","doi":"","title":"SIMULATION ET CONCEPTION D&amp;apos;HEURISTIQUES EFFICACES POUR UN","year":2015,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"Work (physics); Domain (mathematical analysis); Product (mathematics)","score_opus":0.12308815920750314,"score_gpt":0.3776993205121229,"score_spread":0.25461116130461975,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7099094319","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.87956965,0.00009186942,0.109853975,0.00020853832,0.00011445743,0.000109396104,0.0000034974166,0.0005154126,0.009533177],"genre_scores_gemma":[0.9929501,0.000003259483,0.004504264,0.00006342195,0.00015553708,0.000005783922,0.00007457732,0.000025255931,0.0022178476],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99923396,0.000025574567,0.00020420742,0.0001647214,0.00020629917,0.00016524678],"domain_scores_gemma":[0.9993751,0.00017384649,0.000054087202,0.00018270919,0.000098017415,0.00011622208],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00027844598,0.000120884535,0.00014297648,0.000055100565,0.00001899429,0.000015952784,0.00009081218,0.00008778114,0.00016141846],"category_scores_gemma":[0.00059562526,0.00010153059,0.000055437722,0.00011352819,0.000016700935,0.0002054611,0.00004607644,0.00012539732,0.0003329945],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008832376,0.00013104262,0.00081228255,0.000070006354,0.000092766015,0.0000069478883,0.003000413,0.52912796,0.4272701,0.0077160173,0.0005441857,0.03113995],"study_design_scores_gemma":[0.0016172326,0.000046414945,0.00017280474,0.0000591049,0.000051111554,0.000012533613,0.00038404134,0.4592802,0.49341616,0.0016898487,0.04271016,0.00056040677],"about_ca_topic_score_codex":0.00012373505,"about_ca_topic_score_gemma":0.000018153341,"teacher_disagreement_score":0.11338038,"about_ca_system_score_codex":0.00010958923,"about_ca_system_score_gemma":0.00002205858,"threshold_uncertainty_score":0.42800817},"labels":[],"label_agreement":null},{"id":"W7100870258","doi":"","title":"This is to certify that the thesis prepared","year":2009,"lang":"en","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"","keywords":"USable; Work (physics); Documentation; Context (archaeology)","score_opus":0.026485104203366888,"score_gpt":0.26394861323165253,"score_spread":0.23746350902828564,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7100870258","genre_codex":"other","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.47636524,0.00022418803,0.0015096948,0.016127566,0.00015867753,0.0005218611,0.000008744611,0.0008227281,0.5042613],"genre_scores_gemma":[0.97176874,0.000005461126,0.0005319346,0.0019833231,0.000070995964,0.000011961439,0.0000021950968,0.000017470238,0.025607942],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99914056,0.0000076249444,0.00014579868,0.00019715115,0.00023316505,0.00027568243],"domain_scores_gemma":[0.99926955,0.000076430886,0.00002412429,0.0005143897,0.000019444033,0.00009609038],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00014299028,0.00013139886,0.00014323449,0.00004511272,0.000053932647,0.000020019543,0.00031907292,0.000062326355,0.0015159955],"category_scores_gemma":[0.000099753976,0.000074669726,0.00012001648,0.00020552444,0.000009697669,0.00009233978,0.0000618393,0.00011459251,0.0006617967],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006333931,0.00007087449,0.00016996572,0.000026920196,0.000121811136,0.000009282002,0.006148443,0.00012771852,0.84566766,0.0035169125,0.02221099,0.12186609],"study_design_scores_gemma":[0.00009438207,0.0000180728,0.0001675471,0.000016125174,0.000020407777,0.000009938723,0.00009061098,0.0010493617,0.9191322,0.00015304564,0.07909303,0.00015529958],"about_ca_topic_score_codex":0.00013879243,"about_ca_topic_score_gemma":0.000007244399,"teacher_disagreement_score":0.49540347,"about_ca_system_score_codex":0.00007753547,"about_ca_system_score_gemma":0.000008165253,"threshold_uncertainty_score":0.99939674},"labels":[],"label_agreement":null},{"id":"W7104711351","doi":"10.1016/j.ijhydene.2025.152503","title":"Research progress on hydrogen production via methanol steam reforming: Catalysts, reactors, and mechanisms","year":2025,"lang":"en","type":"article","venue":"International Journal of Hydrogen Energy","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"Science and Technology Program of Guizhou Province; Shanghai Rising-Star Program; Department of Education of Guizhou Province; Natural Science Research of Jiangsu Higher Education Institutions of China; Guizhou University of Engineering Science; Peking University; Ministry of Scientific Research, Egypt; Donghua University; Friedrich-Alexander-Universität Erlangen-Nürnberg; Shanghai Lingjun Program; BASF","keywords":"Steam reforming; Hydrogen production; Catalysis; Hydrogen; Mass transfer; Methanol; Hydrogen fuel; Heat transfer; Production (economics)","score_opus":0.01799446025857065,"score_gpt":0.3105724803965249,"score_spread":0.29257802013795425,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7104711351","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9926674,0.0015872013,0.0012793449,0.001476158,0.0012562115,0.00012756349,0.000008142404,0.00006298434,0.0015350173],"genre_scores_gemma":[0.9977261,0.00015750076,0.00021478838,0.000050252296,0.0005297409,0.000018596864,0.000027503575,0.00004025174,0.0012352676],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99722713,0.00009373689,0.00072163047,0.0003338886,0.0012712603,0.00035235478],"domain_scores_gemma":[0.9983896,0.00011929331,0.0003319894,0.00030171176,0.00070584693,0.00015155044],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0013476966,0.00022329309,0.00034466258,0.0012329461,0.000086264154,0.000026875046,0.00068850466,0.00015824134,0.000013106583],"category_scores_gemma":[0.00035512407,0.0001847083,0.0001809472,0.00047018862,0.00010007579,0.0003913168,0.00025345237,0.0005373993,0.000006327808],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002830205,0.00018489071,0.00005156964,0.00003112469,0.00093586603,0.0001510124,0.00014763493,0.00055053754,0.9218823,0.014564015,0.00007894189,0.061139118],"study_design_scores_gemma":[0.0004949277,0.000113851966,0.000008818617,0.00029393646,0.000053729807,0.00062393746,0.00012852662,0.000755373,0.9787921,0.00579294,0.012781467,0.00016042394],"about_ca_topic_score_codex":0.0002133035,"about_ca_topic_score_gemma":0.00003172972,"teacher_disagreement_score":0.060978692,"about_ca_system_score_codex":0.0007026756,"about_ca_system_score_gemma":0.00012373351,"threshold_uncertainty_score":0.7532186},"labels":[],"label_agreement":null},{"id":"W7116841524","doi":"10.1038/s41467-025-67625-4","title":"Active bridging hydride species in ZnO nanorods originated from hydroxyl and oxygen vacancy","year":2025,"lang":"en","type":"article","venue":"Nature Communications","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Education and Child Care","funders":"Priority Academic Program Development of Jiangsu Higher Education Institutions; Nanjing University; National Natural Science Foundation of China","keywords":"Formate; Nanorod; Hydride; Methanol; Dissociation (chemistry); Hydrogen; Oxygen; Catalysis","score_opus":0.010335743161695896,"score_gpt":0.28014061290004716,"score_spread":0.26980486973835127,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7116841524","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9575591,0.013981749,0.0002485073,0.0030835092,0.00022052339,0.00027789312,0.000087403605,0.00023267794,0.024308614],"genre_scores_gemma":[0.99644804,0.0006467061,0.0015383222,0.00012024915,0.00004002971,0.0000376026,0.00021771822,0.000021489406,0.0009298625],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9990845,0.000047816535,0.00026954024,0.00024154613,0.00013162561,0.0002249817],"domain_scores_gemma":[0.99815166,0.00042996966,0.000068675465,0.0012315022,0.000066252745,0.000051943873],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014706775,0.00016720156,0.00025372827,0.00025850616,0.00013162,0.000022450104,0.00078102667,0.00029577388,0.000018666473],"category_scores_gemma":[0.0004267233,0.00017048365,0.0000575688,0.00074341695,0.00008113666,0.00020159465,0.00057817076,0.0014460053,0.0000072825933],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005882724,0.00020015101,0.010603823,0.00007853251,0.0003770047,0.00000970583,0.0020067592,0.00020800682,0.89993024,0.05132382,0.00063517963,0.03456793],"study_design_scores_gemma":[0.0021309864,0.000013618753,0.083891004,0.0008752819,0.00018204816,0.000011302725,0.00070022437,0.0389675,0.58897716,0.003454718,0.27993292,0.0008632651],"about_ca_topic_score_codex":0.0011782853,"about_ca_topic_score_gemma":0.0018311329,"teacher_disagreement_score":0.3109531,"about_ca_system_score_codex":0.0003219798,"about_ca_system_score_gemma":0.000052707124,"threshold_uncertainty_score":0.6952121},"labels":[],"label_agreement":null},{"id":"W7117147292","doi":"10.1016/j.cherd.2025.12.033","title":"Multiphasic simulation and thermal stress evaluation of an industrial methane reformer in the DRI hydrogen production process","year":2025,"lang":"en","type":"article","venue":"Process Safety and Environmental Protection","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Iron Ore Company (Canada)","funders":"","keywords":"Multiphysics; Endothermic process; Steam reforming; Hydrogen production; Hydrogen; Natural gas; Methane; Methane reformer; Carbon dioxide reforming","score_opus":0.029273091873726585,"score_gpt":0.2870300734997027,"score_spread":0.25775698162597616,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7117147292","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99754554,0.00016441515,0.0008949696,0.000064239815,0.000045872373,0.0011701016,0.000007813286,0.000021698059,0.00008535374],"genre_scores_gemma":[0.9996506,0.000015310352,0.000008133913,0.0000046759387,0.000066822126,0.00016543793,0.00006410029,0.000011146029,0.000013788415],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9988154,0.000102041624,0.00030574226,0.00028158832,0.00036009136,0.00013514279],"domain_scores_gemma":[0.99967355,0.000024065845,0.00012684637,0.0001328406,0.000018519551,0.000024194744],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010577329,0.00013631971,0.00014871437,0.000112636204,0.00009467102,0.0000073839224,0.00007278485,0.00013382504,0.000007968872],"category_scores_gemma":[0.00014200588,0.00010455102,0.000021265201,0.00023350942,0.00007007717,0.0005405044,0.000024761877,0.00024651812,3.4356884e-7],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005793858,0.0001822942,0.0012158306,0.00029384976,0.000033181383,2.4442053e-7,0.0024011869,0.6312957,0.16942175,0.0000056960953,9.8362e-9,0.19457087],"study_design_scores_gemma":[0.0012984071,0.00006275006,0.0022097502,0.000111087684,0.00009321106,0.0000062327567,0.002074879,0.583592,0.41017753,0.00024041177,0.000009410486,0.00012435092],"about_ca_topic_score_codex":0.00009766186,"about_ca_topic_score_gemma":0.000025996553,"teacher_disagreement_score":0.24075577,"about_ca_system_score_codex":0.00014583905,"about_ca_system_score_gemma":0.000018474992,"threshold_uncertainty_score":0.4263467},"labels":[],"label_agreement":null},{"id":"W7119061093","doi":"10.1002/cjce.70034","title":"Platinum‐containing catalysts for enhanced hydrogen production via methanol steam reforming","year":2025,"lang":"en","type":"article","venue":"The Canadian Journal of Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":true,"route_about_ca":false,"ca_institutions":"","funders":"","keywords":"Catalysis; Steam reforming; Hydrogen production; Methanol; Industrial catalysts; Hydrogen; Catalyst support","score_opus":0.008794089164599778,"score_gpt":0.22567687100750433,"score_spread":0.21688278184290455,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7119061093","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9880206,0.00090917514,0.008962013,0.00046820322,0.00083906355,0.00033708118,0.000007611169,0.00006707382,0.00038920436],"genre_scores_gemma":[0.9984229,0.0000016743877,0.0007202309,0.000035564495,0.0005128409,0.00002867341,0.000011502302,0.000055684548,0.00021093663],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99819976,0.000011352334,0.0007318188,0.0002153603,0.00023310732,0.00060860923],"domain_scores_gemma":[0.99867135,0.00020085949,0.00023213976,0.00033498328,0.00022257978,0.00033810682],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00081882835,0.00026756147,0.00046544964,0.00040685682,0.00012915356,0.000021846325,0.00053686806,0.000175654,0.000006255741],"category_scores_gemma":[0.0016278897,0.0002146035,0.00028400638,0.0005163886,0.00005204864,0.00026672948,0.000040085895,0.00063983095,0.000002712801],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000034501743,0.0000047535095,0.000006673621,0.00012230872,0.00020827517,0.0000066536836,0.00044625203,0.010603365,0.9817024,0.00022634753,0.000018745175,0.006619749],"study_design_scores_gemma":[0.0004469286,0.000023969895,0.0000021435005,0.00036600686,0.00013469724,0.00014439605,0.00006191838,0.007202647,0.9900568,0.0002023767,0.0011345379,0.00022354712],"about_ca_topic_score_codex":0.00084753305,"about_ca_topic_score_gemma":0.00028552877,"teacher_disagreement_score":0.010402318,"about_ca_system_score_codex":0.0010750861,"about_ca_system_score_gemma":0.00041221027,"threshold_uncertainty_score":0.8751277},"labels":[],"label_agreement":null},{"id":"W7133009605","doi":"","title":"Gas phase hydrogen permeation in palladium-25%Ag","year":2005,"lang":"","type":"dissertation","venue":"TSpace","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada; Division of Materials Research; University of Toronto","keywords":"Permeation; Hydrogen; Texture (cosmology); Membrane; Microstructure; Phase (matter)","score_opus":0.01574011155617985,"score_gpt":0.32513132260305305,"score_spread":0.3093912110468732,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7133009605","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97464114,0.0026118096,0.0001294419,0.00019445147,0.0005376734,0.00082144205,0.000020195439,0.00019756648,0.02084628],"genre_scores_gemma":[0.9696164,0.0007792266,0.00024722726,0.000027526703,0.0008948141,0.00013097667,0.0034316867,0.00028862242,0.024583511],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99562573,0.00006845221,0.0012412897,0.0010650618,0.00084638887,0.0011530746],"domain_scores_gemma":[0.99787563,0.00015236346,0.0005520224,0.0008759491,0.00015090729,0.00039315392],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00050923316,0.0010062809,0.0011317105,0.0008546246,0.00011829151,0.000058885853,0.0005575917,0.0011028702,0.0017079432],"category_scores_gemma":[0.0004829115,0.0011612353,0.00050013815,0.001000876,0.00004870847,0.00038303935,0.00008476067,0.0014394225,0.00067648233],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00029937577,0.0004656871,0.00006299964,0.0008708586,0.00018306922,0.00008596798,0.024572788,0.002693681,0.92968404,0.00020373188,0.000022459477,0.040855333],"study_design_scores_gemma":[0.0050935736,0.00013266112,0.000082324324,0.0013328032,0.0003634131,0.00005835223,0.008806833,0.06763429,0.90380937,0.000037401893,0.010995229,0.0016537491],"about_ca_topic_score_codex":0.0010566595,"about_ca_topic_score_gemma":0.0012609577,"teacher_disagreement_score":0.06494062,"about_ca_system_score_codex":0.0016915837,"about_ca_system_score_gemma":0.000242066,"threshold_uncertainty_score":0.99920464},"labels":[],"label_agreement":null},{"id":"W7133094611","doi":"","title":"Life Cycle Assessment of Gas Phase Heterogeneous Photocatalytic Processes: Solar Dry Methane Reforming","year":2023,"lang":"","type":"dissertation","venue":"TSpace","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"University of Toronto","keywords":"Methane; Syngas; Carbon dioxide reforming; Photocatalysis; Raw material; Steam reforming; Life-cycle assessment; Methane reformer; Carbon dioxide","score_opus":0.023116213126146024,"score_gpt":0.3611299857745698,"score_spread":0.33801377264842375,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7133094611","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9899098,0.0024369974,0.0017983039,0.000060919356,0.0013551574,0.0021843137,0.00012840626,0.0005985949,0.0015274814],"genre_scores_gemma":[0.9836862,0.0013586301,0.0009460102,0.000031513177,0.00049984705,0.0005790661,0.0041875904,0.0008453701,0.007865754],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9919329,0.000099548866,0.0025982938,0.0016990891,0.0019311311,0.0017390093],"domain_scores_gemma":[0.993424,0.0006764822,0.0021272558,0.0018216681,0.00078520685,0.0011653744],"candidate_categories":["metaepi_narrow"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0012965625,0.001634183,0.002731319,0.0011011976,0.00023210922,0.00007513331,0.0013376387,0.0011796172,0.0003517232],"category_scores_gemma":[0.0036725444,0.0016990235,0.0009704294,0.0025974736,0.00014885163,0.00047747704,0.00041604304,0.0018136061,0.00020652966],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00060490624,0.0011092244,0.00002186784,0.034119975,0.00247239,0.00031036788,0.021416714,0.015566049,0.90828377,0.000024935329,0.000009057395,0.016060716],"study_design_scores_gemma":[0.003101395,0.00045773177,0.0000044759586,0.0035534864,0.0014329216,0.000051018258,0.015665706,0.079861574,0.893828,0.00006483901,0.00040568173,0.0015732007],"about_ca_topic_score_codex":0.0026997302,"about_ca_topic_score_gemma":0.00033645288,"teacher_disagreement_score":0.06429552,"about_ca_system_score_codex":0.0011655266,"about_ca_system_score_gemma":0.002715057,"threshold_uncertainty_score":0.9996405},"labels":[],"label_agreement":null},{"id":"W7148809478","doi":"10.71465/ajcce265","title":"Production Chemical Engineering Approaches to Clean and Efficient Fuel","year":2021,"lang":"","type":"article","venue":"American Journal Of Chemistry And Chemical Engineering","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Production (economics); Renewable energy; Chemical industry; Clean energy; Chemical energy; Key (lock); Emerging technologies; Fuel cells; Synthetic fuel","score_opus":0.01127004156317451,"score_gpt":0.1909099835629226,"score_spread":0.1796399419997481,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7148809478","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9914823,0.00319658,0.004009483,0.0006945329,0.00032296707,0.00012413437,0.000012944013,0.000080903104,0.000076133656],"genre_scores_gemma":[0.98616904,0.00019826973,0.011967217,0.000027990272,0.0013945104,0.000010926427,0.000013509429,0.00014976614,0.00006875044],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99605775,0.000017579776,0.0013854202,0.0008774435,0.0006941559,0.00096766546],"domain_scores_gemma":[0.99721,0.00026823976,0.00046087374,0.00050317304,0.00022913875,0.0013285205],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005102557,0.0008153895,0.0014335293,0.00013040149,0.000051203446,0.00010602961,0.00037500486,0.00030223932,0.000030089408],"category_scores_gemma":[0.001860069,0.0008808816,0.000365953,0.0010205903,0.00023305863,0.0002138524,0.0004947478,0.001616071,0.000002441843],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011788538,0.00014413321,0.000022431612,0.0017198576,0.00036210672,0.00011825385,0.00074312085,0.029676488,0.9454255,0.00003473152,0.0000070737847,0.021628404],"study_design_scores_gemma":[0.00066720764,0.000061416904,0.000018336621,0.0011725436,0.00030399428,0.0043899356,0.0006565025,0.036060486,0.95510453,0.000006203558,0.00067185017,0.0008869673],"about_ca_topic_score_codex":0.000005037502,"about_ca_topic_score_gemma":3.965456e-8,"teacher_disagreement_score":0.020741437,"about_ca_system_score_codex":0.00040387988,"about_ca_system_score_gemma":0.00013167331,"threshold_uncertainty_score":0.9993642},"labels":[],"label_agreement":null},{"id":"W7163643894","doi":"10.13182/t130-46153","title":"Robustness of DRL Control for Long-Term Operating S-CO2 Microreactor","year":2024,"lang":"","type":"article","venue":"Transactions of the American Nuclear Society","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Kootenay Association for Science & Technology","funders":"","keywords":"Robustness (evolution); Microreactor; Control system; Process control; Control theory (sociology)","score_opus":0.009869217734419525,"score_gpt":0.2513432717445796,"score_spread":0.2414740540101601,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7163643894","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8079636,0.0007258625,0.18874647,0.0005041749,0.0007437392,0.0006780929,0.00048307618,0.00012378955,0.00003120425],"genre_scores_gemma":[0.99512476,0.00022895477,0.0038464586,0.000043220676,0.00020232736,0.000028947625,0.0000066174043,0.00019336435,0.00032533825],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.997734,0.00004947612,0.0008756064,0.00046569345,0.00035058832,0.0005246527],"domain_scores_gemma":[0.9980702,0.00049083534,0.00040480355,0.00073928153,0.00017576861,0.00011910771],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00037095867,0.00039938753,0.0009255025,0.00007187949,0.000243169,0.000048728583,0.0007076843,0.00016017334,0.0001443748],"category_scores_gemma":[0.000051866507,0.0003290721,0.002499368,0.0008880588,0.0009162995,0.0002672098,0.000038826918,0.0006942489,0.0000038115707],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009231821,0.00019112937,0.00006547388,0.0026074988,0.0020935726,6.33481e-7,0.003180027,0.0422423,0.9278826,0.00004936549,0.00006113762,0.021533914],"study_design_scores_gemma":[0.001613424,0.00031427044,0.00056448614,0.0016733614,0.0026464732,0.0000576656,0.0033559506,0.5578865,0.4303818,0.0000046928612,0.0007727697,0.00072861515],"about_ca_topic_score_codex":0.0002993293,"about_ca_topic_score_gemma":0.0000099186755,"teacher_disagreement_score":0.5156442,"about_ca_system_score_codex":0.00032401434,"about_ca_system_score_gemma":0.00014956672,"threshold_uncertainty_score":0.99991614},"labels":[],"label_agreement":null},{"id":"W7164386981","doi":"10.52843/cassyni.0msyrt","title":"Session 2A: Hydrogen from Natural Gas (Methane)","year":2025,"lang":"","type":"article","venue":"","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto; University of British Columbia","funders":"","keywords":"Steam reforming; Methane; Hydrogen production; Pyrolysis; Hydrogen; Carbon fibers; Natural gas; Catalysis","score_opus":0.007305548605964162,"score_gpt":0.24701652921643433,"score_spread":0.23971098061047016,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W7164386981","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95125186,0.010548973,0.0018089818,0.00078805105,0.0028595703,0.0003984648,0.000044482636,0.0004724622,0.031827156],"genre_scores_gemma":[0.9613174,0.00024660872,0.0011157896,0.00024929093,0.0004720503,0.00001980088,0.00019476528,0.00008041151,0.036303848],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99646854,0.00006441161,0.0009806665,0.0009841517,0.0005552215,0.0009469779],"domain_scores_gemma":[0.99777156,0.000573001,0.00016319379,0.0011152138,0.00010265635,0.00027439202],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.000336886,0.0006709373,0.0008811499,0.0003617739,0.00013535267,0.000057203462,0.00074956124,0.0005716315,0.0019025583],"category_scores_gemma":[0.0005771379,0.0005889721,0.00058587006,0.0010781077,0.00009191537,0.00042581843,0.0009021014,0.0012158693,0.0005585597],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008909909,0.00008966211,0.00018810671,0.00020512169,0.00055244175,0.000041156974,0.00021561413,0.00015316725,0.9306015,0.0007711647,0.00024474907,0.06684825],"study_design_scores_gemma":[0.0012906726,0.0000139370395,0.000043654538,0.00074544013,0.0003404454,0.000010623895,0.00023690527,0.03711358,0.9425088,0.0012037315,0.01587471,0.0006174788],"about_ca_topic_score_codex":0.0022499757,"about_ca_topic_score_gemma":0.00006448926,"teacher_disagreement_score":0.06623077,"about_ca_system_score_codex":0.00064871815,"about_ca_system_score_gemma":0.0001770208,"threshold_uncertainty_score":0.99965614},"labels":[],"label_agreement":null},{"id":"W879705706","doi":"10.1016/s0167-2991(01)80332-3","title":"Surface carbon coverage and selectivity in FT synthesis: a simple model for selectivity correlations","year":2001,"lang":"en","type":"book-chapter","venue":"Studies in surface science and catalysis","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Selectivity; Methane; Catalysis; Simple (philosophy); Chemistry; Cobalt; Carbon fibers; Inorganic chemistry; Chemical engineering; Materials science; Organic chemistry; Composite material","score_opus":0.03708452703644319,"score_gpt":0.29176535870035497,"score_spread":0.25468083166391176,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W879705706","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9750555,0.004910965,0.0006379583,0.00007593972,0.00009907157,0.0007164251,0.00011462674,0.00008051766,0.018308988],"genre_scores_gemma":[0.98775727,0.0021951448,0.00019772141,0.000009691192,0.000023259117,0.000041616262,0.00001350879,0.00004834278,0.009713438],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9973096,0.000016230462,0.00046909545,0.0010227654,0.000556169,0.00062610157],"domain_scores_gemma":[0.9982006,0.0008301412,0.00018711721,0.00040319242,0.00026419578,0.00011474983],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0017600567,0.0004611568,0.0010174656,0.00036032262,0.0002801875,0.000034308956,0.00024832826,0.0002329215,0.0000026352502],"category_scores_gemma":[0.0013273705,0.00044906596,0.00010798247,0.0007906171,0.00073428283,0.00038611938,0.000383839,0.00048599197,0.0000010244319],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00031806156,0.00033306747,0.021280413,0.0022761337,0.001519079,0.000081386796,0.020438598,0.8195273,0.10534998,0.00482332,0.00008181115,0.023970796],"study_design_scores_gemma":[0.00069863605,0.000049334696,0.00018776617,0.00046707565,0.00047513234,0.000027529539,0.00071734254,0.97488123,0.014912407,0.005894419,0.00040989628,0.0012792094],"about_ca_topic_score_codex":0.0008607735,"about_ca_topic_score_gemma":0.0037311774,"teacher_disagreement_score":0.1553539,"about_ca_system_score_codex":0.0010050945,"about_ca_system_score_gemma":0.000217008,"threshold_uncertainty_score":0.9997961},"labels":[],"label_agreement":null},{"id":"W95021955","doi":"10.1016/s1385-8947(00)00352-1","title":"Eggshell catalysts for Fischer–Tropsch synthesis","year":2001,"lang":"en","type":"article","venue":"Chemical Engineering Journal","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":41,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Eggshell; Catalysis; Metal; Fischer–Tropsch process; Chemical engineering; Materials science; Viscosity; Dispersion (optics); Chemistry; Metallurgy; Composite material; Organic chemistry; Selectivity","score_opus":0.012447871228999907,"score_gpt":0.230955135634586,"score_spread":0.2185072644055861,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W95021955","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.70009184,0.0015705882,0.29274526,0.0006194787,0.0014078603,0.00045609564,0.000041532297,0.00095202436,0.0021153362],"genre_scores_gemma":[0.96931964,0.00006460355,0.027174987,0.0000438312,0.0022085211,0.0001003363,0.000033580898,0.00020900054,0.0008455139],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979565,0.0000068408744,0.0005770155,0.00031727276,0.00034613785,0.0007962275],"domain_scores_gemma":[0.99856776,0.000403947,0.00011620001,0.00033817365,0.0001171845,0.00045674105],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000381176,0.00035791128,0.00047462204,0.00018971223,0.00008244799,0.000056083212,0.0004831359,0.00023933384,0.0000978294],"category_scores_gemma":[0.0018059562,0.0003311289,0.00042945382,0.00032830602,0.00002813254,0.0002708217,0.000086091924,0.0007236161,0.000053313994],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000046912937,0.000043993263,0.00005090847,0.00011974657,0.00013687565,0.00005436162,0.00007069921,0.0030503431,0.9896387,0.00014911163,0.00053354487,0.0061048153],"study_design_scores_gemma":[0.00064351206,0.0000167545,0.000015072378,0.00017370861,0.00010195087,0.0016206155,0.000021300992,0.04222487,0.93057406,0.00004748438,0.024074921,0.0004857766],"about_ca_topic_score_codex":0.0000065359195,"about_ca_topic_score_gemma":1.7932277e-7,"teacher_disagreement_score":0.2692278,"about_ca_system_score_codex":0.00034035544,"about_ca_system_score_gemma":0.000039498544,"threshold_uncertainty_score":0.99991405},"labels":[],"label_agreement":null},{"id":"W97492952","doi":"10.1016/b978-0-444-53882-6.00016-4","title":"Catalyst Development for CO2 Activation to Produce Syn-Gas through CO2 Reforming of CH4: Mitigation of Carbon Formation on Ni-Based Catalysts","year":2013,"lang":"en","type":"book-chapter","venue":"Elsevier eBooks","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Materials science; Chemical engineering; Carbon dioxide reforming; Syngas; Chemistry; Organic chemistry; Engineering","score_opus":0.018775856007851328,"score_gpt":0.24070344198934635,"score_spread":0.221927585981495,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W97492952","genre_codex":"other","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"other","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.29732302,0.00024309846,0.0010176837,0.00016501012,0.0006890955,0.008695164,0.00020466522,0.00031162074,0.69135064],"genre_scores_gemma":[0.6586504,0.000011648846,0.00725098,0.00011931914,0.0005221539,0.0014194293,0.0060308347,0.00051270553,0.32548255],"study_design_codex":"design_other","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99663633,0.000014641454,0.0015355219,0.0005998767,0.00078629184,0.00042735448],"domain_scores_gemma":[0.99706906,0.0001460438,0.0012548205,0.0008443953,0.00055788504,0.00012779383],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00046128948,0.000629359,0.0010147535,0.0004251513,0.00012929292,0.00002104054,0.0003603794,0.0004560355,0.0000081851485],"category_scores_gemma":[0.00024134907,0.00059228897,0.00027764565,0.000083750485,0.00006506966,0.00024059003,0.0001049313,0.00035266278,0.000017310438],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021106564,0.0000510489,0.0000027277165,0.0051260553,0.0003402104,0.0000014513937,0.002992044,0.00037488487,0.36359394,0.0010984677,0.000028602739,0.6261795],"study_design_scores_gemma":[0.0006003596,0.00012082081,0.0000036274153,0.0035624895,0.00015889581,0.000004560644,0.000042033604,0.00038226426,0.9349819,0.00025827927,0.05930892,0.00057586574],"about_ca_topic_score_codex":0.000041602743,"about_ca_topic_score_gemma":0.00005471671,"teacher_disagreement_score":0.6256037,"about_ca_system_score_codex":0.001090541,"about_ca_system_score_gemma":0.00024630936,"threshold_uncertainty_score":0.99965286},"labels":[],"label_agreement":null}]}