{"meta":{"page":1,"per_page":50,"max_per_page":100,"total":643,"total_is_capped":false,"direct_labels_cover":2,"predictions_cover":643,"direct_label_status":"direct model label, unvalidated","prediction_status":"machine_predicted_unvalidated (Codex and Gemma teacher distillation)","score_status":"score_only:v0-immature-baseline (scores rank; they never assert a category)","snapshot":{"source":"OpenAlex, pinned release, all 482 partitions","release":"2026-06-24","frame_built":"2026-07-12"},"query_hash":"9b02cbf431db","filters":{"topic":"Catalysts for Methane Reforming"}},"results":[{"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02263345107179989,"gpt":0.3137468421556037,"spread":0.2911133910838039,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000686058,0.0001484131,0.000318919,0.0003357723,0.00001860799,0.000005817232,0.0005569063,0.00007972548,0.0001991783],"category_scores_gemma":[0.0004488584,0.0001296675,0.0002801332,0.0001534997,0.00004067726,0.0002983679,0.0001140389,0.0001953627,0.000002570054],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.000215609,"about_ca_system_score_gemma":0.0001612571,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002820333,"about_ca_topic_score_gemma":0.000007546944,"domain_scores_codex":[0.9981788,0.00006532724,0.0008141747,0.0001539927,0.0006173725,0.0001703028],"domain_scores_gemma":[0.9984726,0.0000556337,0.0006752602,0.0001929656,0.0004263133,0.0001772042],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00009096626,0.0002935042,0.0003844401,0.00001656339,0.001458995,0.00007853648,0.0004177777,0.0230643,0.9405459,0.005311053,0.00002210183,0.02831583],"study_design_scores_gemma":[0.0003973961,0.00006861581,0.0001051705,0.00005603961,0.00008386237,0.0006046383,0.0000421554,0.01240776,0.9816898,0.001652724,0.002754714,0.0001371768],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9488753,0.0004341235,0.04445219,0.0001417352,0.001330081,0.00004036542,0.000005903015,0.0000334143,0.004686877],"genre_scores_gemma":[0.9791829,0.00006452649,0.01997587,0.00004686958,0.0005098077,0.000003735668,0.000006915929,0.00003218739,0.0001772174],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.04114383,"threshold_uncertainty_score":0.5287686,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01311037454554727,"gpt":0.2655171495261466,"spread":0.2524067749805993,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001387312,0.0007294372,0.002364609,0.0001815847,0.00004924557,0.00001329924,0.001100459,0.0004296994,0.0000128124],"category_scores_gemma":[0.0008357571,0.0005234942,0.0007857357,0.0005755256,0.00009663303,0.0001223081,0.0003225059,0.001272322,0.0000103188],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.001102971,"about_ca_system_score_gemma":0.00009287405,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00005227687,"about_ca_topic_score_gemma":7.651021e-7,"domain_scores_codex":[0.996518,0.0001315242,0.001366029,0.0007697524,0.000659047,0.0005556928],"domain_scores_gemma":[0.997754,0.0001632264,0.0007537804,0.001143776,0.00002993933,0.0001552711],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"design_other","study_design_gemma":"not_applicable","study_design_scores_codex":[0.00002824627,0.00007469741,0.000001966643,0.1146095,0.0002513805,0.00000641478,0.0001598761,0.00008484979,0.001775773,0.000004200876,0.0004114116,0.8825917],"study_design_scores_gemma":[0.0003677509,0.00001999347,5.659493e-7,0.1077415,0.001075285,0.0001210481,0.0004077976,0.0004728574,0.009784672,0.000008138055,0.8790032,0.0009971292],"study_design_candidate":"design_other","study_design_consensus":null,"genre_codex":"review","genre_gemma":"review","genre_scores_codex":[0.0002186808,0.9944231,0.001981266,0.00002712978,0.0003497333,0.0009700292,0.00003637492,0.0000573475,0.001936336],"genre_scores_gemma":[0.0001244413,0.9875335,0.01030408,0.00007787827,0.0002913915,0.0003385361,0.000749195,0.0001622796,0.0004186786],"genre_candidate":"review","genre_consensus":"review","teacher_disagreement_score":0.8815945,"threshold_uncertainty_score":0.9997216,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01384188665439101,"gpt":0.2211951017232185,"spread":0.2073532150688275,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006342847,0.0001538002,0.0005568229,0.0002027084,0.00005514203,0.000008337957,0.0001813166,0.0000944145,0.00002296592],"category_scores_gemma":[0.001025565,0.00009737891,0.000289587,0.0003353645,0.00008211782,0.0002218675,0.00005411393,0.0002521546,0.000004746697],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001099371,"about_ca_system_score_gemma":0.00001545866,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0006361866,"about_ca_topic_score_gemma":0.00003716013,"domain_scores_codex":[0.9986675,0.00009991101,0.0005810895,0.0001276308,0.0003825757,0.0001413256],"domain_scores_gemma":[0.9975193,0.001312759,0.0006983561,0.0002704291,0.0001187559,0.00008035608],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0005495908,0.00008533464,0.0001696648,0.0001123678,0.001397669,0.00002443627,0.003459644,0.0001690436,0.9714896,0.0003609755,0.00002840139,0.02215325],"study_design_scores_gemma":[0.0009489509,0.00006501329,0.001408482,0.0002432355,0.001198772,0.00004947733,0.00009638056,0.001794351,0.9927272,0.0009783404,0.0003613157,0.0001284976],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9970169,0.001009065,0.0009176652,0.00006699549,0.0001819126,0.0001007858,0.000002091373,0.00001437399,0.000690175],"genre_scores_gemma":[0.998552,0.0001980192,0.0009495165,0.000022178,0.0002222405,0.000006981221,0.000008696494,0.00002283715,0.00001756994],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02202476,"threshold_uncertainty_score":0.3970997,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.04358468711400098,"gpt":0.3106885341483419,"spread":0.2671038470343409,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001490544,0.001216029,0.004718652,0.0001060288,0.0001586106,0.00005439808,0.0008675791,0.00111172,0.00001581813],"category_scores_gemma":[0.001656726,0.001040909,0.007120067,0.0004631121,0.0001246933,0.000281368,0.0003078841,0.001436233,0.0001336219],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.001336786,"about_ca_system_score_gemma":0.0001040449,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002354191,"about_ca_topic_score_gemma":6.225862e-7,"domain_scores_codex":[0.9952591,0.0000906723,0.002201758,0.001063235,0.0005383488,0.0008468798],"domain_scores_gemma":[0.9960907,0.0004262408,0.001799467,0.001285109,0.00009052835,0.000308033],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.000001189551,0.00004258866,4.683072e-7,0.04185994,0.0006462063,0.000002230233,0.00005406379,0.00001042991,0.5100877,0.000001833858,0.0001309795,0.4471624],"study_design_scores_gemma":[0.0001750049,0.00002033079,1.166722e-8,0.009811405,0.00199319,0.0002248826,0.000002735087,0.0005647996,0.5450866,0.00000123898,0.4413602,0.0007596302],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"review","genre_gemma":"review","genre_scores_codex":[0.005715897,0.9918118,0.0003504889,0.000002006727,0.0002567155,0.001457139,0.0000865584,0.0002376934,0.00008168878],"genre_scores_gemma":[0.002058179,0.9953434,0.0002092812,0.000007231072,0.0004574876,0.0004195235,0.001179994,0.0002875824,0.00003727169],"genre_candidate":"review","genre_consensus":"review","teacher_disagreement_score":0.4464027,"threshold_uncertainty_score":0.9992041,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.06806138489142088,"gpt":0.3252968476475833,"spread":0.2572354627561624,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001082362,0.000369517,0.0004213333,0.000289176,0.00013874,0.00007145542,0.000416034,0.0005338637,0.0001308442],"category_scores_gemma":[0.0005156489,0.000369439,0.0001275002,0.000701911,0.0001162725,0.0008179924,0.000300462,0.001655094,0.00003010299],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.001176319,"about_ca_system_score_gemma":0.0001208352,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003305963,"about_ca_topic_score_gemma":0.00001048698,"domain_scores_codex":[0.997036,0.00003395982,0.0006240323,0.0004946931,0.0008609515,0.0009503447],"domain_scores_gemma":[0.9984623,0.0003616952,0.00009518085,0.0005829009,0.0001533772,0.0003445191],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00003223544,0.00003281508,0.000006499858,0.000170653,0.00007592656,0.000009124848,0.0001876982,0.04058044,0.9561598,0.0002764637,0.00002390341,0.002444424],"study_design_scores_gemma":[0.001115347,0.00001384116,0.000009087785,0.0002198527,0.00002965581,0.00006863623,0.0001839064,0.3811294,0.6161086,0.00009591137,0.0007059548,0.0003197678],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.996257,0.0005285,0.0006935202,0.0001508681,0.00008725275,0.0003684135,0.0000614939,0.0002843581,0.001568614],"genre_scores_gemma":[0.9973956,0.00005731295,0.00009161278,0.000008371199,0.000810663,0.0001254649,0.0002712493,0.0001019385,0.001137738],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.340549,"threshold_uncertainty_score":0.9998758,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.03797096401803817,"gpt":0.3082619429695013,"spread":0.2702909789514631,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002846036,0.0007551162,0.005517058,0.0006670204,0.0000908441,0.00001270049,0.0005430789,0.0005169305,0.00001086949],"category_scores_gemma":[0.004357246,0.0005536517,0.001443939,0.002430679,0.00008543301,0.0001977385,0.0004597186,0.0002589266,0.000007062424],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003185819,"about_ca_system_score_gemma":0.0002545114,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0005921295,"about_ca_topic_score_gemma":0.00001952824,"domain_scores_codex":[0.9958305,0.0001335433,0.002013229,0.0008816159,0.0002386035,0.0009025148],"domain_scores_gemma":[0.9969915,0.0002698236,0.001202679,0.001185568,0.0002490194,0.0001014445],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"design_other","study_design_gemma":"not_applicable","study_design_scores_codex":[0.00000162721,0.00001229597,1.716935e-8,0.4937334,0.0002209339,0.000004666954,0.000004231858,0.000008754816,0.0000665398,0.0004306942,0.0008579264,0.5046589],"study_design_scores_gemma":[0.00007678428,0.00003835174,3.011177e-10,0.1674914,0.002354864,0.00004913276,0.00006650451,0.00001194004,0.002632064,0.000359996,0.826472,0.0004468736],"study_design_candidate":"not_applicable","study_design_consensus":null,"genre_codex":"review","genre_gemma":"review","genre_scores_codex":[3.247872e-7,0.9966352,0.0004007974,0.00004602355,0.0000902934,0.002174622,0.00002201082,0.0003710579,0.0002596939],"genre_scores_gemma":[1.230874e-7,0.9640852,0.0002730088,0.00001826539,0.0001559077,0.003443778,0.000382136,0.0001756539,0.0314659],"genre_candidate":"review","genre_consensus":"review","teacher_disagreement_score":0.8256141,"threshold_uncertainty_score":0.9996915,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.006584584400491617,"gpt":0.2215010555146241,"spread":0.2149164711141325,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001654737,0.0001613542,0.0002790061,0.00002810912,0.00003454045,0.00000369371,0.0001557831,0.00008930889,0.00005944708],"category_scores_gemma":[0.0001150502,0.0001318539,0.00005617522,0.0005496718,0.00003933842,0.0000964443,0.0001039496,0.0001142612,0.00002967364],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002095983,"about_ca_system_score_gemma":0.0000288968,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001032917,"about_ca_topic_score_gemma":0.0002244827,"domain_scores_codex":[0.9989248,0.0000154346,0.0002069628,0.0002680436,0.0003152276,0.0002695198],"domain_scores_gemma":[0.9992617,0.00004845867,0.0001053643,0.0003699108,0.000107547,0.0001070246],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00008601425,0.00003433533,0.0007021464,0.00007763002,0.0001161783,0.000002266143,0.0002790536,0.0009996501,0.9971926,0.0000287875,0.00001130254,0.0004699873],"study_design_scores_gemma":[0.0003314828,0.0001317029,0.0004811781,0.00004563242,0.00009676139,0.00001638553,0.00001159905,0.0103364,0.987169,0.00001744621,0.001187897,0.0001745682],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9962138,0.00005943337,0.0008427256,0.00002590229,0.0000717777,0.0003071893,0.000006409333,0.0001077876,0.002364991],"genre_scores_gemma":[0.9963735,0.000001004849,0.001382719,0.00001413711,0.0001211766,0.00003888522,0.000008056428,0.00004595601,0.002014567],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.0100237,"threshold_uncertainty_score":0.5376844,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.009100158166746045,"gpt":0.2573556085782114,"spread":0.2482554504114654,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007427261,0.0001531014,0.0001371935,0.0001429027,0.0002680365,0.0001518744,0.0005312294,0.00007437645,0.00002066321],"category_scores_gemma":[0.0001240653,0.00008930107,0.00007833424,0.0006593767,0.0001629874,0.001230193,0.0000903057,0.0003041146,0.00005423784],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003529157,"about_ca_system_score_gemma":0.0001107371,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0007128231,"about_ca_topic_score_gemma":0.00008334417,"domain_scores_codex":[0.9984691,0.000009122863,0.0001616725,0.0004742306,0.0004002018,0.0004857001],"domain_scores_gemma":[0.9991621,0.00009325028,0.00002426495,0.0005340356,0.00006524475,0.0001210649],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00001150705,0.000008725892,0.000001751894,0.00005416233,0.00001239418,0.000005641033,0.0008693793,0.0003328481,0.9965222,0.000456378,0.00002513924,0.001699854],"study_design_scores_gemma":[0.00009102515,0.00002031617,0.00004367372,0.00005082517,0.00003823724,0.00002149148,0.0002817674,0.004402566,0.9869655,0.0002152198,0.007718388,0.0001509727],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9974219,0.0001846979,0.0002230761,0.0004948605,0.001047044,0.0002578325,0.00004249718,0.0002196375,0.0001084217],"genre_scores_gemma":[0.9984975,0.00001326818,0.0001159748,0.00002969555,0.0002703635,0.00005505023,0.00004820662,0.00002891806,0.0009410466],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.009556702,"threshold_uncertainty_score":0.3641592,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02209491384165214,"gpt":0.2909554397862813,"spread":0.2688605259446292,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002251657,0.0001503647,0.000293485,0.0001996338,0.00005221781,0.000009215681,0.001033291,0.0002256454,0.00001118631],"category_scores_gemma":[0.001158008,0.0001529695,0.00007085934,0.001261106,0.00004898032,0.0001788235,0.0004766968,0.0009584259,0.00004492901],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002532523,"about_ca_system_score_gemma":0.00006169287,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002349722,"about_ca_topic_score_gemma":0.0004348326,"domain_scores_codex":[0.9989337,0.00005714819,0.0003804142,0.0002209524,0.0001964565,0.0002113208],"domain_scores_gemma":[0.998459,0.0002976523,0.0001112723,0.0008631962,0.000156679,0.0001121728],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00002591604,0.00008146348,0.0004485479,0.00007778944,0.00008139397,9.065695e-7,0.004363992,0.001195709,0.989419,0.003023241,0.0002666475,0.001015398],"study_design_scores_gemma":[0.0003008644,0.00003488569,0.00009045795,0.00007855523,0.00003305757,0.000004050847,0.0002818707,0.01126047,0.98169,0.0001027925,0.005952199,0.0001708071],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9761532,0.004993037,0.0006172077,0.00858354,0.000120422,0.0009081002,0.00008864206,0.0002616375,0.008274201],"genre_scores_gemma":[0.9964304,0.00004469582,0.00307966,0.0001715186,0.00002153727,0.00005783406,0.0001054367,0.00003040144,0.00005852624],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02027718,"threshold_uncertainty_score":0.6237917,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.008393412339782393,"gpt":0.2473954353677053,"spread":0.2390020230279229,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0009110633,0.0003473516,0.0005748837,0.0002144218,0.0002255945,0.0000328649,0.0005794531,0.0001834288,0.000006399142],"category_scores_gemma":[0.001372015,0.0002535206,0.0004199946,0.000607107,0.0001157637,0.0003832498,0.0001793671,0.000201877,0.00005019387],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002058155,"about_ca_system_score_gemma":0.00005700807,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0007564409,"about_ca_topic_score_gemma":0.0005737139,"domain_scores_codex":[0.9977048,0.00003907915,0.000745764,0.0004962969,0.0005115245,0.0005025401],"domain_scores_gemma":[0.9973921,0.0007945574,0.0004149532,0.00107206,0.0002188693,0.0001074291],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001370204,0.00004699745,0.0001245328,0.0002357946,0.0003466854,9.957098e-7,0.001112883,0.0006985862,0.9826084,0.0005138175,0.00006439407,0.01410991],"study_design_scores_gemma":[0.0004711992,0.00009958069,0.00009552667,0.00009728854,0.0005613468,0.0000112254,0.000355399,0.006982609,0.9884276,0.0001074762,0.002468831,0.0003218988],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9949207,0.0005483452,0.002888792,0.0001341723,0.0001636359,0.0005315712,0.00006145406,0.0001492806,0.0006019995],"genre_scores_gemma":[0.9982858,0.00004068431,0.0002570793,0.00003575721,0.0002112081,0.0002074849,0.0005653435,0.00008153262,0.0003151493],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01378801,"threshold_uncertainty_score":0.9999917,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02138224398910478,"gpt":0.2422636578247676,"spread":0.2208814138356628,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001253757,0.0002668561,0.0003040624,0.0001162916,0.0005370158,0.0001011506,0.0004906819,0.0002255389,0.00003234345],"category_scores_gemma":[0.0004387923,0.0002451608,0.0001820772,0.00006854894,0.0000409602,0.0004635168,0.000176711,0.0001438556,0.00001425848],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003587676,"about_ca_system_score_gemma":0.00008092344,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001714516,"about_ca_topic_score_gemma":0.00006411893,"domain_scores_codex":[0.9984401,0.00001530891,0.0002799807,0.000456868,0.0002529903,0.0005546946],"domain_scores_gemma":[0.9984192,0.00009326464,0.0001831992,0.001001418,0.0001554754,0.0001474485],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00003859459,0.00003789748,0.000005391176,0.00004118225,0.00007679965,0.00004975007,0.0002032917,0.001277475,0.8442088,0.1483614,0.0001082379,0.005591201],"study_design_scores_gemma":[0.0006876924,0.00005971462,0.000009742324,0.0000235475,0.00003399469,0.000001346725,0.0001457096,0.005039125,0.9089201,0.01829657,0.06648342,0.0002989987],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9796425,0.0004760353,0.006300655,0.0001551683,0.0003317716,0.0002465422,0.00002802851,0.0001978613,0.01262148],"genre_scores_gemma":[0.9848197,0.00002155361,0.0002761757,0.00009152281,0.001126073,0.0002250492,0.00027061,0.00008231928,0.01308697],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1300649,"threshold_uncertainty_score":0.9997367,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.0200358454490967,"gpt":0.292801219396966,"spread":0.2727653739478693,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004808857,0.0001367366,0.0005363557,0.00001720837,0.00006329898,0.000009460358,0.000512848,0.00006874011,0.000006236475],"category_scores_gemma":[0.0006508199,0.00008977003,0.0003561334,0.000103372,0.00107846,0.0001466977,0.0001087488,0.0004153145,2.998048e-7],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001454155,"about_ca_system_score_gemma":0.00004620237,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003798965,"about_ca_topic_score_gemma":5.060827e-7,"domain_scores_codex":[0.9987993,0.00002558471,0.0004568578,0.0001183323,0.0004308724,0.0001690742],"domain_scores_gemma":[0.9973625,0.0002816497,0.001826917,0.0003352221,0.0001103276,0.00008337161],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001025006,0.00003782743,0.002156693,0.00005812944,0.0001616982,4.266812e-7,0.000308849,0.0001265323,0.9962761,0.00001718559,0.00007952925,0.0006745647],"study_design_scores_gemma":[0.000430409,0.0000630874,0.001191452,0.0001427854,0.00005452045,0.00002530806,0.0003762628,0.0002127678,0.9972412,0.0001204288,0.00004852457,0.00009327677],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9986637,0.00003131566,0.00005907144,0.0008410699,0.00005829699,0.00006022486,0.00001204072,0.000006077818,0.0002682133],"genre_scores_gemma":[0.9988672,0.00005943779,0.000854702,0.00007983347,0.00007530331,4.406814e-7,9.392204e-7,0.00001361434,0.00004855355],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.001436766,"threshold_uncertainty_score":0.3973632,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.09591798077029426,"gpt":0.4296508562828319,"spread":0.3337328755125377,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001623384,0.0001127595,0.0004145937,0.0004336967,0.00002635234,0.00001917731,0.001052153,0.00009268342,0.00001805582],"category_scores_gemma":[0.0003149407,0.00007054034,0.0001357317,0.0003647727,0.0001001484,0.000431657,0.0002031249,0.0004359916,0.000001133115],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002646556,"about_ca_system_score_gemma":0.0001783635,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0006827657,"about_ca_topic_score_gemma":0.00002728035,"domain_scores_codex":[0.9969642,0.0001107079,0.0008460385,0.000139834,0.001719237,0.0002200166],"domain_scores_gemma":[0.9973782,0.0001956764,0.0005961136,0.000291202,0.001441913,0.00009692956],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001776709,0.0001386484,0.007843014,0.0004878639,0.0004212585,0.000007759421,0.0008541665,0.002377533,0.9703354,0.009461857,0.00001126857,0.007883511],"study_design_scores_gemma":[0.0006104274,0.0001682034,0.0003153245,0.001228228,0.00002581163,0.0001813933,0.002111898,0.005319896,0.9882022,0.0003068282,0.001424987,0.0001047973],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9922715,0.005898604,0.00007121774,0.000101135,0.0003959548,0.00007443192,0.00001128647,0.000005188838,0.001170622],"genre_scores_gemma":[0.9992478,0.0003032805,0.000055724,0.000004266619,0.0001303992,0.000003242275,0.000006970088,0.00002100438,0.0002273246],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01786676,"threshold_uncertainty_score":0.2876552,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01105126682324821,"gpt":0.2467391692199206,"spread":0.2356879023966724,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001734248,0.0003362884,0.0004758596,0.0006188896,0.0001021388,0.00003322378,0.0002414662,0.000452281,0.000004882418],"category_scores_gemma":[0.0005240801,0.0002957126,0.00004483534,0.0005383294,0.000163092,0.0001157034,0.00007190798,0.0004920422,0.000009950619],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00009185467,"about_ca_system_score_gemma":0.00003233205,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002995224,"about_ca_topic_score_gemma":0.000004598771,"domain_scores_codex":[0.9984034,0.00001364747,0.0003195949,0.0005761011,0.0002120392,0.0004751899],"domain_scores_gemma":[0.9992263,0.00009118764,0.000123131,0.0004148776,0.0000423485,0.0001021555],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0000676495,0.000100259,0.0004073399,0.0002677353,0.00005619676,0.00005338467,0.0001477719,0.000008401488,0.8107408,0.0007200332,0.0000116981,0.1874187],"study_design_scores_gemma":[0.0004126106,0.0002293957,0.0003412323,0.000288258,0.0000822959,0.0001475179,0.00009435348,0.003279797,0.9925031,0.001326501,0.0008859214,0.0004089992],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9936071,0.001691753,0.00004115041,0.001129318,0.00003533222,0.0001559466,0.000005800992,0.0008139574,0.002519628],"genre_scores_gemma":[0.9988447,0.0000733628,0.0007244286,0.00007392656,0.00004683659,0.00003242895,0.00001303575,0.000049725,0.0001415799],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1870097,"threshold_uncertainty_score":0.9999495,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01988872682235859,"gpt":0.270637739835336,"spread":0.2507490130129774,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000755459,0.0002890947,0.000530493,0.000615348,0.00003589383,0.00001401006,0.0007607533,0.0001528493,0.00001355838],"category_scores_gemma":[0.0009381656,0.0002474253,0.0003667099,0.0003250451,0.00008200177,0.0007670989,0.0001657783,0.0002336613,0.000005933437],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0008700335,"about_ca_system_score_gemma":0.0002616955,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0004628807,"about_ca_topic_score_gemma":0.00005611452,"domain_scores_codex":[0.9970902,0.00003580758,0.001166166,0.000301752,0.001071292,0.0003347936],"domain_scores_gemma":[0.9969888,0.00007279425,0.001140252,0.0003136686,0.001250155,0.0002342843],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0004432166,0.0002260024,0.000127277,0.00005887665,0.001346139,0.00005137047,0.0008279759,0.006580205,0.9781652,0.0003610141,0.00008872683,0.01172396],"study_design_scores_gemma":[0.001457319,0.0001813671,0.000005433275,0.0002416152,0.0001515708,0.0008156292,0.0002311503,0.003771812,0.9872618,0.0005388639,0.005084389,0.0002590472],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9957438,0.0007419869,0.001494391,0.0002258245,0.001113691,0.0001707109,0.00006207783,0.0000438533,0.0004036311],"genre_scores_gemma":[0.997377,0.00004010081,0.0004520811,0.00002305513,0.001001947,0.00002080518,0.0001717856,0.00007213305,0.0008410927],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01146491,"threshold_uncertainty_score":0.9999978,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01555047531996219,"gpt":0.2008552615141143,"spread":0.1853047861941521,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00007478544,0.0002495706,0.0004444867,0.0003324039,0.000008685045,0.00000238586,0.0004526117,0.000545558,0.0002423728],"category_scores_gemma":[0.0009537838,0.0002530621,0.0001282692,0.0006203927,0.00007277307,0.0001032043,0.0001948233,0.0004664746,0.00001841395],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001100774,"about_ca_system_score_gemma":0.00001502012,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000106451,"about_ca_topic_score_gemma":3.520766e-7,"domain_scores_codex":[0.9986833,0.000002594023,0.0004486167,0.0003371889,0.0001559481,0.0003723883],"domain_scores_gemma":[0.9990631,0.0001135454,0.0001110482,0.000556697,0.00006231242,0.00009326727],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00001298451,0.00004259342,0.00004748351,0.00004798708,0.00008456157,0.000007925389,0.000103605,0.003903175,0.9936675,0.0008991541,0.000005018559,0.001177965],"study_design_scores_gemma":[0.0002300793,0.00001816344,0.000005119036,0.00009928438,0.00004679374,0.00001579183,0.00002041398,0.06381202,0.9351652,0.0001559124,0.0001917866,0.0002393907],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.7353251,0.0004050613,0.2608479,0.00005700977,0.0002606035,0.0001865441,0.00002531059,0.001662592,0.001229923],"genre_scores_gemma":[0.9482146,0.00001195641,0.05153877,0.000006183654,0.00006368385,0.0000365716,0.00002991243,0.0000707794,0.00002752727],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.2128895,"threshold_uncertainty_score":0.9999921,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.0411725654434792,"gpt":0.309957026014469,"spread":0.2687844605709898,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["research_integrity"],"category_scores_codex":[0.002743617,0.0009084348,0.0009764303,0.0005464756,0.000321346,0.0001764125,0.00143386,0.001608922,0.0001639946],"category_scores_gemma":[0.003695001,0.0009436652,0.0004680733,0.001858305,0.0002632723,0.0006121005,0.0007381135,0.008098206,0.0002803066],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.001101915,"about_ca_system_score_gemma":0.0004207906,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001313709,"about_ca_topic_score_gemma":0.000009952452,"domain_scores_codex":[0.9925892,0.00005760664,0.001197393,0.001277176,0.002319633,0.002559018],"domain_scores_gemma":[0.9959804,0.0006796439,0.0002099889,0.001699059,0.0003570227,0.001073928],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.000126175,0.0001026328,0.00006928477,0.0002707737,0.0002183698,0.0001156551,0.00007118095,0.0009020319,0.9852927,0.00003133983,0.0004355194,0.01236428],"study_design_scores_gemma":[0.002143617,0.00005278164,0.00002885257,0.0003026383,0.00005201855,0.0001788844,0.00006114721,0.005562406,0.9749163,0.00001311835,0.01571173,0.0009765122],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9959476,0.0001481568,0.00003058873,0.0001311368,0.0009705108,0.0006220168,0.00009070794,0.0008010021,0.001258279],"genre_scores_gemma":[0.9952649,0.00006899378,0.00003078441,0.00001563066,0.003538177,0.0002130634,0.0002243403,0.0003625952,0.0002815228],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01527621,"threshold_uncertainty_score":0.9996872,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01005900856648985,"gpt":0.2448120438058023,"spread":0.2347530352393125,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000668324,0.0002925811,0.000584936,0.000606409,0.00002662058,0.00001277832,0.0008207353,0.0001576992,0.00002098418],"category_scores_gemma":[0.0004081596,0.0002274246,0.0003284666,0.0004346573,0.00009543575,0.0004254311,0.000116461,0.0003711969,0.000001945071],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0005652938,"about_ca_system_score_gemma":0.0001140492,"about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00663393,"about_ca_topic_score_gemma":0.0002680446,"domain_scores_codex":[0.9964789,0.00006573954,0.00169089,0.000281742,0.001143872,0.0003388941],"domain_scores_gemma":[0.9978417,0.000102325,0.001057243,0.0003710088,0.0005429365,0.00008485618],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001835709,0.0001793448,0.0003523847,0.00003299304,0.0003988537,0.00004258855,0.0004221074,0.04288511,0.9546072,0.0001268173,0.00003266378,0.0007363388],"study_design_scores_gemma":[0.00102785,0.00005229961,0.00002139709,0.0003041635,0.0001040129,0.0004152175,0.0001192386,0.03989858,0.9571224,0.0004190126,0.0003025866,0.0002132781],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9976677,0.0011345,0.0003402912,0.0001421051,0.0003400661,0.0001100794,0.00004786276,0.00002099176,0.0001964013],"genre_scores_gemma":[0.9990249,0.00006986161,0.000084304,0.00001691322,0.0003984601,0.00001105923,0.0001911391,0.00006325907,0.0001401243],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.006365886,"threshold_uncertainty_score":0.999981,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.006224100918266994,"gpt":0.2126362847927963,"spread":0.2064121838745293,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006452012,0.000577281,0.001049792,0.0002784877,0.0001370783,0.00001832742,0.0008119366,0.0003134118,0.00002625986],"category_scores_gemma":[0.0009575051,0.0004004597,0.0005626184,0.00064072,0.000239379,0.00008846354,0.0001441421,0.0004785761,0.00001163154],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001049518,"about_ca_system_score_gemma":0.00008817582,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0004978058,"about_ca_topic_score_gemma":0.00009250248,"domain_scores_codex":[0.9969953,0.00002944522,0.0008878423,0.0006750184,0.0007467804,0.0006655762],"domain_scores_gemma":[0.9959069,0.002101697,0.0004650772,0.001251603,0.0001225115,0.0001521653],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002387667,0.0002169822,0.0000911359,0.0006264956,0.0004158772,0.000003450548,0.0004270674,0.0003793566,0.9905183,0.002008823,0.00005444737,0.005019245],"study_design_scores_gemma":[0.0007226804,0.0001264826,0.0002533289,0.0001003403,0.000715363,0.000007099121,0.0001072349,0.002866642,0.9943718,0.0000534063,0.0002350538,0.0004405621],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.996679,0.00009408989,0.00001813844,0.0001152014,0.000234626,0.0008741181,0.00007762494,0.00008887614,0.001818335],"genre_scores_gemma":[0.9978737,0.00001885112,0.000369984,0.00005001973,0.0002832831,0.0007020787,0.0002678686,0.0001174949,0.0003167723],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.004578683,"threshold_uncertainty_score":0.9998447,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02791763104760409,"gpt":0.2485478945940927,"spread":0.2206302635464886,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002036737,0.0001350685,0.0002958009,0.0001080557,0.00001327637,0.000001912413,0.0002374976,0.0001153312,0.00002026446],"category_scores_gemma":[0.000197795,0.0001052487,0.0001009955,0.0004378229,0.0001524757,0.00008334195,0.0001750301,0.0001778147,6.170463e-7],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00009018034,"about_ca_system_score_gemma":0.00002544247,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0008901426,"about_ca_topic_score_gemma":0.00007218812,"domain_scores_codex":[0.9989094,0.00002121571,0.000498182,0.0001869122,0.0002389235,0.0001454058],"domain_scores_gemma":[0.9991845,0.00006629867,0.0002507104,0.0003779426,0.00007408907,0.00004645878],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0000125941,0.00005746231,0.01854952,0.0002602065,0.0001081013,0.000001214596,0.003273703,0.0005073994,0.9748591,0.0001445991,6.661261e-7,0.002225417],"study_design_scores_gemma":[0.0004579963,0.000009026724,0.0145674,0.00008537282,0.00008841839,0.000006409536,0.0002637249,0.005450161,0.978719,0.0002290219,0.000007828494,0.0001156519],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9989529,0.0001831134,0.0003976861,0.00001735706,0.00003586167,0.00009921674,0.00001839049,0.00001472105,0.0002807998],"genre_scores_gemma":[0.9968534,0.000008294166,0.002846646,0.000007975353,0.00001843554,0.000007734517,0.00006100492,0.00001612237,0.0001804247],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.004942761,"threshold_uncertainty_score":0.4291916,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.009314113267608799,"gpt":0.2393985126335468,"spread":0.230084399365938,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008541143,0.0002787635,0.0007069635,0.0002339389,0.000009170823,0.00001102883,0.0007721813,0.0001905257,0.00000521102],"category_scores_gemma":[0.002012773,0.000206475,0.0001054467,0.0003354941,0.00008312107,0.0001553974,0.0003674559,0.001149102,2.815712e-7],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00007214143,"about_ca_system_score_gemma":0.00006363605,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001549297,"about_ca_topic_score_gemma":0.000004921391,"domain_scores_codex":[0.9981736,0.00002725023,0.0006627475,0.0002570892,0.0005628581,0.0003164671],"domain_scores_gemma":[0.9976935,0.001098316,0.0003475348,0.0006398499,0.00008694124,0.0001338629],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00008687491,0.0001671507,0.000403504,0.0004299952,0.0001486389,0.00001655394,0.00008797059,0.0001528054,0.997809,0.00006261621,0.00001426646,0.0006206486],"study_design_scores_gemma":[0.0008150475,0.00008337918,0.0005245908,0.0004354824,0.00009768196,0.00007307461,0.000005218545,0.01720499,0.9804386,0.000009467197,0.0001266643,0.0001858108],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9991209,0.0002231328,0.00004281233,0.0001382445,0.0001704729,0.0001702826,0.00002199521,0.00001774706,0.00009442178],"genre_scores_gemma":[0.9994351,0.00002503763,0.0002983447,0.000006012733,0.0001704442,0.000004855792,0.00001160652,0.00004208892,0.00000645972],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01737038,"threshold_uncertainty_score":0.8419807,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.00938002073757146,"gpt":0.2542005995488417,"spread":0.2448205788112702,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008431463,0.0002270959,0.0006419095,0.0004076662,0.00002606205,0.00000839771,0.0004488236,0.0001464741,0.0001947544],"category_scores_gemma":[0.0003295317,0.0001726586,0.0004262846,0.0003436749,0.000062564,0.0005521777,0.000103672,0.0004681903,0.00002017542],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002053706,"about_ca_system_score_gemma":0.00007853278,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00007371903,"about_ca_topic_score_gemma":0.00001540054,"domain_scores_codex":[0.9976037,0.00002709259,0.001165852,0.0001528957,0.0006870299,0.0003633897],"domain_scores_gemma":[0.9981323,0.0001172461,0.001003548,0.0003280173,0.000204961,0.0002138983],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001306963,0.0001518306,0.001094167,0.0001043336,0.0004951868,0.00004071664,0.003193819,0.0006700288,0.9795633,0.00005981903,0.000203012,0.01429309],"study_design_scores_gemma":[0.001152132,0.0001244578,0.0004050072,0.0002110607,0.000160018,0.0003702448,0.0009074048,0.0002105779,0.9686102,0.00002342441,0.02758629,0.000239212],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.996179,0.001593259,0.0002576525,0.000113481,0.0002766863,0.0000593843,0.000007935202,0.00003087584,0.001481696],"genre_scores_gemma":[0.9975017,0.00004339008,0.0007944086,0.00003363085,0.0004702405,9.165353e-7,0.000004551574,0.00004674972,0.001104394],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02738328,"threshold_uncertainty_score":0.7040815,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.07665180469223634,"gpt":0.3257034852576408,"spread":0.2490516805654044,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005616164,0.0001534963,0.0003889893,0.0001458694,0.0000597756,0.00002086242,0.00009251523,0.00009619388,0.0000259483],"category_scores_gemma":[0.001333446,0.0001312228,0.0000956522,0.0003444442,0.00002747349,0.0003419801,0.00002901716,0.0001388135,1.833377e-7],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001071051,"about_ca_system_score_gemma":0.0002339336,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":7.435417e-7,"about_ca_topic_score_gemma":0.000001508962,"domain_scores_codex":[0.9984124,0.00007117611,0.0007418634,0.0001852156,0.00042188,0.0001674077],"domain_scores_gemma":[0.9980106,0.0001474278,0.0006133722,0.0001562885,0.0009581234,0.0001142212],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.000235715,0.0006311178,0.001701204,0.001928751,0.0003918082,0.000007673117,0.001216076,0.1011371,0.8661482,0.002680943,0.0001290295,0.02379228],"study_design_scores_gemma":[0.0007767423,0.0001231109,0.0006075375,0.0002905057,0.0001775972,0.00005491475,0.0003470328,0.1451001,0.8512307,0.0008062675,0.0003496108,0.0001358595],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.531018,0.0005339889,0.4676243,0.0001030144,0.0003402602,0.0002920124,0.000007365044,0.00002261004,0.00005835082],"genre_scores_gemma":[0.9956349,0.0003139761,0.003656864,0.00001414534,0.0002103043,0.00002050742,0.00004647721,0.00003330604,0.00006952285],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.4646168,"threshold_uncertainty_score":0.535111,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.03878829924100211,"gpt":0.3254962498099407,"spread":0.2867079505689386,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005430193,0.0007207318,0.004384445,0.0003168056,0.0000379116,0.00001745814,0.0005241562,0.0003068981,0.0000182065],"category_scores_gemma":[0.003701838,0.000617706,0.0005674455,0.001603128,0.00003484787,0.0000800407,0.0005892928,0.0006104021,0.00002745087],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002944681,"about_ca_system_score_gemma":0.0001102549,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001429312,"about_ca_topic_score_gemma":0.00004393632,"domain_scores_codex":[0.9966763,0.0002081669,0.001241011,0.000905187,0.0005102663,0.0004590591],"domain_scores_gemma":[0.9969938,0.0007892599,0.0004687218,0.001355525,0.00009925087,0.0002934034],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"design_other","study_design_gemma":"not_applicable","study_design_scores_codex":[0.000002817692,0.0004169276,0.000004773049,0.1155332,0.001113293,0.00008386691,0.0001769682,0.000001406147,0.0006665208,0.000009044182,0.0001748225,0.8818164],"study_design_scores_gemma":[0.0002554172,0.0002095751,0.000003220815,0.2448891,0.01230301,0.0004501309,0.00008908959,0.00001772592,0.006990129,0.000001880655,0.7331902,0.001600545],"study_design_candidate":"design_other","study_design_consensus":null,"genre_codex":"review","genre_gemma":"review","genre_scores_codex":[0.0007120837,0.9970862,0.00002964995,0.00001259388,0.00009370987,0.001600722,0.00004925989,0.00008721082,0.0003285633],"genre_scores_gemma":[0.002594549,0.9961162,0.0001261214,0.00001492994,0.0001148001,0.0005787757,0.00009215631,0.0001596475,0.0002027832],"genre_candidate":"review","genre_consensus":"review","teacher_disagreement_score":0.8802159,"threshold_uncertainty_score":0.9996274,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.003925551398891057,"gpt":0.1879036477283172,"spread":0.1839780963294262,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004383166,0.0006614603,0.00108953,0.0002288711,0.0001299121,0.00001434231,0.0006026789,0.0002691793,0.0001174245],"category_scores_gemma":[0.000099807,0.0006424098,0.0005810458,0.0003645013,0.0001633272,0.0002247988,0.0003689041,0.0003020999,0.000372218],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0009231247,"about_ca_system_score_gemma":0.0000348742,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001154261,"about_ca_topic_score_gemma":0.00002224198,"domain_scores_codex":[0.9958961,0.00001714848,0.001085575,0.001307723,0.0009318009,0.0007616266],"domain_scores_gemma":[0.9977568,0.0001636393,0.0005827634,0.001244524,0.00001508621,0.0002371922],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002907206,0.0005668004,0.0000846172,0.00009442234,0.0008118519,0.00000164665,0.0003488237,0.002463752,0.988708,0.00002659591,0.00003076022,0.006572051],"study_design_scores_gemma":[0.001553276,0.00006526432,0.00005454643,0.00005579053,0.0008235477,0.00003303963,0.001205494,0.002403928,0.9915689,0.00001126643,0.001523337,0.0007015815],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9960696,0.0002900389,0.0006054593,0.00005871536,0.0002307711,0.001311814,0.0009558126,0.0001378856,0.0003399369],"genre_scores_gemma":[0.9950429,0.00002071445,0.0006330062,0.00003820384,0.000172962,0.0006023616,0.002846807,0.0001846602,0.0004583426],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.00587047,"threshold_uncertainty_score":0.9996027,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.004485181591879346,"gpt":0.2238241474020045,"spread":0.2193389658101251,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005294757,0.0001672733,0.0001575209,0.00006173382,0.0003361402,0.00002175032,0.0005783117,0.00004827585,0.00002525279],"category_scores_gemma":[0.0001020823,0.0001205936,0.0001063223,0.0007841684,0.0002065448,0.0002086633,0.0003196237,0.000155979,0.0000108839],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003678915,"about_ca_system_score_gemma":0.00003127792,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00006813282,"about_ca_topic_score_gemma":0.00000899671,"domain_scores_codex":[0.998414,0.0000132805,0.0002192443,0.0005196186,0.0004037584,0.0004300538],"domain_scores_gemma":[0.9993091,0.00004081909,0.00005775886,0.0004670585,0.0000071761,0.0001180563],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.000008312251,0.00001951772,0.00004007801,0.000006523812,0.00001700044,8.044981e-7,0.0002840742,0.003615208,0.9509619,0.0007383762,0.00002836536,0.0442798],"study_design_scores_gemma":[0.0001150201,0.00001979027,0.00008534358,0.00003301746,0.00002907045,0.000009823924,0.0004100853,0.00192148,0.9703004,0.0001575206,0.02676741,0.0001510363],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9913658,0.0004489131,0.004679486,0.002080236,0.000506811,0.0002427509,0.000012436,0.00007440709,0.0005891154],"genre_scores_gemma":[0.9959999,0.00001618238,0.00134436,0.0003098293,0.0002833131,0.0001608683,0.00001539126,0.00001678365,0.001853375],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.04412876,"threshold_uncertainty_score":0.4917663,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02274957827772589,"gpt":0.263363678581896,"spread":0.2406141003041701,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005266618,0.0003046076,0.0005612742,0.0002570655,0.00003759391,0.00004579421,0.0002536899,0.0001867056,0.00002267333],"category_scores_gemma":[0.001505078,0.0002607308,0.0001036606,0.0006517003,0.00008839104,0.0002594215,0.0001535254,0.0003435825,0.000123697],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003054556,"about_ca_system_score_gemma":0.00004655382,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0004291996,"about_ca_topic_score_gemma":0.0002884476,"domain_scores_codex":[0.9981593,0.00005056678,0.0004110191,0.000463748,0.0003655964,0.0005497693],"domain_scores_gemma":[0.998666,0.0003757853,0.00009074761,0.0004876664,0.00005282397,0.000326967],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001496695,0.0002082222,0.01366226,0.0001868502,0.0004481604,0.0001602926,0.004610382,0.001815456,0.9752882,0.0001046341,0.0001351142,0.003230834],"study_design_scores_gemma":[0.0004698278,0.00002577254,0.001098378,0.0001696614,0.0001441368,0.00001221537,0.0008667214,0.0006392669,0.9960881,0.00004845803,0.0000937283,0.0003437008],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9986564,0.0004799688,0.000001450558,0.0001349113,0.000139626,0.000128332,0.00002329994,0.0001083855,0.0003276371],"genre_scores_gemma":[0.9994122,0.0000508085,0.00006373905,0.00003682297,0.00008151449,0.0000341428,0.00005329469,0.00005709843,0.0002103141],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02080001,"threshold_uncertainty_score":0.9999845,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01491410690806463,"gpt":0.277833041208035,"spread":0.2629189342999704,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001369452,0.0004439894,0.001140086,0.0001523712,0.0000782826,0.0000415039,0.000226177,0.0002189486,0.00002528664],"category_scores_gemma":[0.0002822685,0.0003827923,0.0000949764,0.0001469132,0.0001058384,0.0004302361,0.0002814134,0.0001183721,0.000003342597],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002253222,"about_ca_system_score_gemma":0.0001022651,"about_ca_topic_candidate":true,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.008123684,"about_ca_topic_score_gemma":0.0001230721,"domain_scores_codex":[0.9974583,0.00008493131,0.0008809571,0.0006290826,0.0002911313,0.0006556401],"domain_scores_gemma":[0.998382,0.0001325635,0.0005098722,0.0004476419,0.0002075482,0.000320425],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0004952368,0.00007372717,0.00001935387,0.000516795,0.0002218934,0.000009460136,0.002122471,0.000004409665,0.9869837,0.0001238857,0.0003119504,0.009117182],"study_design_scores_gemma":[0.002751686,0.0001825594,0.00000411874,0.0001053983,0.0002208568,0.0001327662,0.00103636,0.00007946149,0.9870995,0.0004600433,0.007488622,0.0004386713],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9919623,0.002304793,0.003019065,0.0000497445,0.0003876363,0.0008597357,0.001055716,0.0001301475,0.0002308922],"genre_scores_gemma":[0.9710521,0.0001402941,0.02440071,0.0000510425,0.0002222443,0.0001818192,0.0007486385,0.0001702421,0.003032901],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02138164,"threshold_uncertainty_score":0.9998624,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01069615838801053,"gpt":0.254022281383787,"spread":0.2433261229957765,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006685742,0.0001689148,0.0003939288,0.0005155274,0.00001517819,0.000006397102,0.0005157941,0.0001231031,0.00003079764],"category_scores_gemma":[0.0008015534,0.000142297,0.0002714866,0.0001844977,0.0000405062,0.0004030923,0.00006747492,0.0002900804,0.000001210321],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002094113,"about_ca_system_score_gemma":0.0001087205,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002320146,"about_ca_topic_score_gemma":0.0001430555,"domain_scores_codex":[0.9979888,0.00001860654,0.0009901128,0.000183763,0.0005937128,0.0002249928],"domain_scores_gemma":[0.9984986,0.00008300838,0.0006407109,0.0001954446,0.0004886586,0.00009364392],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003860316,0.0001295365,0.00007313336,0.00002994267,0.0002323726,0.00002693278,0.0001741229,0.0004382333,0.9895456,0.0005124959,0.000003850485,0.008447718],"study_design_scores_gemma":[0.00139114,0.00006731597,0.000003719181,0.0001279747,0.0000391316,0.0006821656,0.00004862537,0.001313333,0.9918539,0.0003030937,0.00402687,0.000142713],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9982985,0.0001574258,0.0001043374,0.0002141605,0.000960037,0.0001051346,0.00001274984,0.00001955132,0.0001280936],"genre_scores_gemma":[0.9981222,0.00004847035,0.000734018,0.00001413223,0.0008737642,0.00001721742,0.00002874003,0.00004221437,0.0001192128],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.008305005,"threshold_uncertainty_score":0.5802705,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":false,"ca_venue":true,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01352122179207957,"gpt":0.2045671963142899,"spread":0.1910459745222103,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0006332434,0.0003542364,0.0005632106,0.0007686997,0.00004973893,0.00004166999,0.0004255413,0.0002125152,0.000002796575],"category_scores_gemma":[0.00122998,0.0003036113,0.0001515608,0.0007815895,0.00007926227,0.0003289482,0.00005617497,0.001220831,0.000003160291],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0009195753,"about_ca_system_score_gemma":0.0002263791,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0005061047,"about_ca_topic_score_gemma":0.001968686,"domain_scores_codex":[0.9976543,0.00002418373,0.0009238808,0.0002498769,0.0003853276,0.0007624759],"domain_scores_gemma":[0.9984279,0.0003388739,0.0001945434,0.0002785389,0.00009872479,0.0006614741],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00001952709,0.00002389191,0.00005676909,0.000040622,0.00003174164,0.0001411898,0.000534225,0.00886611,0.9784881,0.0001334202,0.000008196796,0.01165617],"study_design_scores_gemma":[0.0008492709,0.00004365214,0.0006707456,0.0004653212,0.00004237949,0.0006427641,0.00007825164,0.01304655,0.9834047,0.0002320432,0.0001597652,0.0003645463],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9973909,0.001272828,0.0001291415,0.0007997531,0.0001577257,0.000142142,0.00001250707,0.00002766435,0.00006734631],"genre_scores_gemma":[0.9992598,0.00007152027,0.0003027975,0.00009396777,0.0001842974,0.000007230229,0.00001952312,0.00005643199,0.000004372784],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01129162,"threshold_uncertainty_score":0.9999416,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"about_ca":false},"ca_institutions":"University of Toronto","funders":"","keywords":"Sparging; Supersaturation; Fermentative hydrogen production; Chemistry; Hydrogen; Hydrogen production; Environmental chemistry; Organic chemistry; Biohydrogen","retraction":null,"screen_n_in":null,"score":{"opus":0.00368027503531562,"gpt":0.1833259802461771,"spread":0.1796457052108615,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00005476232,0.000126392,0.0001658972,0.0001746189,0.00005098899,0.000003574808,0.00006824858,0.0001205342,0.000002361283],"category_scores_gemma":[0.0000251277,0.0001094216,0.00002532949,0.0002178969,0.0001684477,0.0001341786,0.00003983775,0.0001703177,0.000001436695],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00009719563,"about_ca_system_score_gemma":0.000003650075,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001393354,"about_ca_topic_score_gemma":0.0000229801,"domain_scores_codex":[0.9992788,0.000007450396,0.0001723029,0.0002453811,0.000100527,0.0001955237],"domain_scores_gemma":[0.9997048,0.00001101589,0.00008389877,0.0001700532,0.00001351239,0.00001671321],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00003287215,0.00001146176,0.001636754,0.00005088965,0.00003764064,0.000007348331,0.0001190346,0.000400983,0.9972932,0.0001681992,0.000002485835,0.0002391286],"study_design_scores_gemma":[0.000358233,0.00001802737,0.002151868,0.00004757084,0.00003067628,0.00007506934,0.0001602684,0.0002331638,0.9967602,0.00001307417,0.00002208459,0.0001297801],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9965706,0.00006391895,0.0005825614,0.002378697,0.00003719245,0.0001616148,0.000002748816,0.0001862604,0.00001643092],"genre_scores_gemma":[0.9989696,0.00000678938,0.0008785223,0.00001190824,0.00004720501,0.00001237553,0.00002232602,0.0000200774,0.00003117935],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.002399042,"threshold_uncertainty_score":0.4462085,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.04420868323808333,"gpt":0.2943625639690211,"spread":0.2501538807309378,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":[],"category_scores_codex":[0.001295845,0.0003256212,0.0004542998,0.0003719681,0.00005192428,0.00005065971,0.0003458118,0.0006956282,0.00002651854],"category_scores_gemma":[0.003386188,0.0003185109,0.00006123116,0.001055871,0.0001043414,0.0002317038,0.0001874415,0.003395841,0.000004840952],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003239839,"about_ca_system_score_gemma":0.0001725431,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001872059,"about_ca_topic_score_gemma":0.0001342166,"domain_scores_codex":[0.9974138,0.00003260652,0.0004713659,0.0005539908,0.0006791843,0.0008491011],"domain_scores_gemma":[0.9978352,0.001182816,0.0000519243,0.0005631537,0.00009279743,0.0002741342],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00009801707,0.00005071901,0.0001974765,0.0001104949,0.00002922739,0.00007006763,0.0001541312,0.05158874,0.9459369,0.00002656233,0.000002925468,0.001734706],"study_design_scores_gemma":[0.0009802399,0.000008069856,0.0000228659,0.000220927,0.00001098745,0.00004263935,0.00003711786,0.1515964,0.8466474,0.00001425484,0.0001165494,0.0003025446],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9987337,0.00004721173,0.00001945616,0.00009311845,0.00005509321,0.0002688908,0.00002180252,0.0001217608,0.0006389587],"genre_scores_gemma":[0.999159,0.00000946479,0.0002276949,0.000001466413,0.0003142242,0.0000700059,0.00002444902,0.0001043595,0.00008928621],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1000077,"threshold_uncertainty_score":0.9999267,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01747885539356251,"gpt":0.242011347109291,"spread":0.2245324917157284,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003632906,0.0003788886,0.0008024339,0.0005171199,0.0000840266,0.000008874115,0.0004136197,0.000258022,0.00006845169],"category_scores_gemma":[0.0001474085,0.0003696212,0.0002745597,0.001105411,0.0001094637,0.0002024973,0.0001126512,0.0003511709,0.00006154182],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003205513,"about_ca_system_score_gemma":0.00008163088,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001580206,"about_ca_topic_score_gemma":0.00009841387,"domain_scores_codex":[0.9973558,0.00003290338,0.0008958377,0.0005819548,0.0005908725,0.0005426222],"domain_scores_gemma":[0.9985542,0.000117117,0.0003182017,0.0007881057,0.00007685702,0.0001455752],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00005647837,0.0002667108,0.002672325,0.00005473966,0.0001320723,0.00002455774,0.0006458953,0.0003563485,0.9916274,0.0002084984,0.00003290402,0.003922045],"study_design_scores_gemma":[0.0006242598,0.00001281274,0.003966453,0.00002147902,0.0002011387,0.00004645242,0.00008484009,0.001316869,0.9931182,0.00001324517,0.0001906444,0.0004036664],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.996698,0.00006811562,0.0003683546,0.00002235369,0.0000446691,0.000419896,0.00003403574,0.0001253389,0.002219262],"genre_scores_gemma":[0.9969578,0.0000145996,0.001297922,0.00001249723,0.0001267029,0.0005455677,0.000598454,0.00008770084,0.0003587515],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.003518379,"threshold_uncertainty_score":0.9998755,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.0148174576829774,"gpt":0.2595131803485551,"spread":0.2446957226655777,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005926021,0.0006307976,0.0008033073,0.0003427248,0.0008082043,0.0001495126,0.001098755,0.000325058,0.0002373495],"category_scores_gemma":[0.000862805,0.0005169843,0.0002672235,0.0003380697,0.0002632385,0.001248915,0.0005255464,0.0005401355,0.0004317129],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0005631435,"about_ca_system_score_gemma":0.0001948459,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.004492509,"about_ca_topic_score_gemma":0.0009665276,"domain_scores_codex":[0.9964435,0.00002842945,0.0007055891,0.0009517765,0.0009067314,0.0009640009],"domain_scores_gemma":[0.9961889,0.0001127631,0.0006173281,0.002472583,0.0001856118,0.0004228224],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.002012882,0.00041773,0.02307055,0.001689959,0.002764271,0.001793048,0.005058832,0.0003025128,0.8440521,0.00187858,0.002379421,0.1145802],"study_design_scores_gemma":[0.007785161,0.0002305026,0.006029713,0.001736435,0.0008255166,0.001657322,0.001439081,0.0008876255,0.9282568,0.0001309676,0.04822522,0.002795679],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.963361,0.000683862,0.00006511957,0.0001797341,0.0006615013,0.0001937058,0.0000471865,0.0004152099,0.03439271],"genre_scores_gemma":[0.958594,0.0000309599,0.0003541131,0.00008053191,0.0006605634,0.0001104946,0.0004655357,0.0001936532,0.03951012],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1117845,"threshold_uncertainty_score":0.9997282,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.008976331475513374,"gpt":0.2350264864881537,"spread":0.2260501550126403,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006719686,0.0001640236,0.0003161418,0.0002543246,0.00003493167,0.000005310036,0.0004272555,0.0001509776,0.00001083069],"category_scores_gemma":[0.0001362021,0.00007679801,0.00005356255,0.0004701039,0.0002632288,0.0001096591,0.00006129935,0.0002059764,0.000002216908],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00009427354,"about_ca_system_score_gemma":0.00004392991,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0008407579,"about_ca_topic_score_gemma":0.0002039089,"domain_scores_codex":[0.9988467,0.0001987384,0.0003015447,0.0002374648,0.00006954573,0.000345985],"domain_scores_gemma":[0.999272,0.0001829188,0.0001441619,0.0003515268,0.0000244516,0.0000248633],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00009935276,0.00003505102,0.01057567,0.00003062244,0.00006688031,0.000005877825,0.0009244412,0.0002489003,0.9866221,0.0001337613,0.0002068186,0.001050513],"study_design_scores_gemma":[0.002092764,0.00007755357,0.003011785,0.0001771334,0.0001317939,0.00009295347,0.000715517,0.0008797367,0.9800622,0.0001099203,0.01229707,0.0003515234],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9887501,0.001101519,0.009198576,0.0003754627,0.0001711014,0.0002767072,0.00008094091,0.000017595,0.00002797573],"genre_scores_gemma":[0.9987558,0.00002118973,0.0009962061,0.00004492105,0.00005925545,0.00002203032,0.00004598762,0.00001954475,0.00003509904],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01209025,"threshold_uncertainty_score":0.3131732,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.1254149519263813,"gpt":0.3630331183411076,"spread":0.2376181664147263,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.001676729,0.0004513368,0.001133862,0.0004538028,0.00006008829,0.000006054497,0.0007603005,0.000469279,0.0000595197],"category_scores_gemma":[0.004245363,0.0004312504,0.0002938186,0.001644298,0.0003850387,0.0001606906,0.0004300259,0.001663446,0.000005619917],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0006226245,"about_ca_system_score_gemma":0.0002258577,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001272573,"about_ca_topic_score_gemma":0.000002659988,"domain_scores_codex":[0.995591,0.00004990251,0.001175424,0.000573929,0.001582909,0.001026832],"domain_scores_gemma":[0.9973692,0.0007062841,0.000244562,0.000975104,0.0004149294,0.0002899197],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0000786076,0.00006396881,0.0003431927,0.0006830344,0.0004412768,0.00006606869,0.0003318908,0.001981963,0.9954883,0.00001183233,0.0000340675,0.0004757739],"study_design_scores_gemma":[0.001307721,0.00005675774,0.00004109765,0.0005186438,0.00005930494,0.0001037078,0.0002202934,0.001467468,0.9944072,0.00000505723,0.001438797,0.0003739677],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9963112,0.001875219,0.000005194587,0.00003183732,0.0001907518,0.0002869624,0.00003530223,0.0001405717,0.001122929],"genre_scores_gemma":[0.997785,0.0002264394,0.0000538871,0.000001503359,0.000529143,0.00005710552,0.00005171188,0.0001177198,0.001177469],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.002568634,"threshold_uncertainty_score":0.9998139,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.08281913374498258,"gpt":0.2552247826605743,"spread":0.1724056489155917,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004226648,0.000244076,0.0004490949,0.000278698,0.0000621773,0.0000349955,0.0001069432,0.0001064318,0.000009992406],"category_scores_gemma":[0.00007523614,0.0002497097,0.0000643509,0.000284708,0.00002635187,0.00003479585,0.000225837,0.00008442478,0.00001164186],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002325322,"about_ca_system_score_gemma":0.00005228453,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00003311761,"about_ca_topic_score_gemma":0.00007492025,"domain_scores_codex":[0.9982945,0.00001347715,0.0004302777,0.0006391567,0.0002610595,0.0003615568],"domain_scores_gemma":[0.9993846,0.00006519876,0.00006077994,0.0002419459,0.00005157546,0.0001958371],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001363775,0.0001095647,0.00002951288,0.0002442336,0.0002292726,0.000005742379,0.002834826,0.005554508,0.9664081,0.00637742,0.00001185149,0.01805861],"study_design_scores_gemma":[0.000882843,0.00001657068,0.0004218296,0.00002834448,0.00007039291,0.00002869216,0.000416499,0.009369244,0.9870877,0.0000954991,0.001217881,0.0003644739],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.996261,0.0003211872,0.002165211,0.0003049413,0.00008809885,0.0005000659,0.00003853239,0.00004191688,0.0002790586],"genre_scores_gemma":[0.9916356,0.00001038982,0.006735706,0.00006714344,0.0001119516,0.0004720897,0.0007945251,0.00003928289,0.0001333634],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02067965,"threshold_uncertainty_score":0.9999955,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01987322511410226,"gpt":0.2749790454083254,"spread":0.2551058202942231,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0008761907,0.0003240415,0.0006931711,0.0004791792,0.0002252701,0.00001204077,0.000267118,0.0000703491,0.00003576728],"category_scores_gemma":[0.0003147206,0.0003065936,0.0003036788,0.000882441,0.00006903198,0.0003532696,0.0003436572,0.0004062412,0.000002137966],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00067045,"about_ca_system_score_gemma":0.0001096836,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003847886,"about_ca_topic_score_gemma":0.00002068467,"domain_scores_codex":[0.9975189,0.000050027,0.0007185942,0.0006236212,0.0005079265,0.0005809107],"domain_scores_gemma":[0.9985631,0.00007223325,0.0004050674,0.0006416476,0.0001426309,0.0001753068],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.000172542,0.0002004204,0.0003599848,0.0009199315,0.0004947934,0.000004533589,0.002862446,0.001883745,0.8795421,0.0002438805,0.00004947866,0.1132662],"study_design_scores_gemma":[0.001184285,0.00008339986,0.00004486239,0.00006753177,0.0009315936,0.0001066328,0.003374437,0.003384659,0.9523891,0.0001048458,0.03773439,0.0005942275],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9889544,0.008051654,0.0006914065,0.000111164,0.001226309,0.0006234196,0.0001803344,0.0001141724,0.00004713303],"genre_scores_gemma":[0.9963312,0.0001875101,0.000890787,0.000009637748,0.000795475,0.0002416872,0.001006416,0.0001005673,0.0004367471],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1126719,"threshold_uncertainty_score":0.9999386,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.005194956467865931,"gpt":0.2207758234873451,"spread":0.2155808670194791,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.002253285,0.0008730164,0.001483034,0.0001578,0.0002859944,0.00007103656,0.0006417672,0.0002798054,0.00002011732],"category_scores_gemma":[0.001077382,0.0006593901,0.0008297415,0.0005054836,0.0002641087,0.0006310682,0.0004613126,0.002033079,0.00008989922],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0007477064,"about_ca_system_score_gemma":0.0001095194,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001019647,"about_ca_topic_score_gemma":0.000003089198,"domain_scores_codex":[0.9952783,0.0003685662,0.001309868,0.0006199907,0.001576972,0.0008463007],"domain_scores_gemma":[0.9955814,0.001417588,0.001349365,0.0007458496,0.0004399303,0.0004658116],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.001207755,0.0007098097,0.000156252,0.0005190009,0.001111291,0.00002947238,0.0008457899,0.001072566,0.9888142,0.00001060453,0.00006623934,0.005457052],"study_design_scores_gemma":[0.002513518,0.0005841736,0.002713651,0.0003633596,0.001024509,0.0002735697,0.0003517751,0.0008954727,0.9903653,0.0002965969,0.00000375313,0.0006142817],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9985027,0.0001260735,0.0002001273,0.00009659408,0.0002310212,0.0005751536,0.00002457536,0.0001100966,0.0001337027],"genre_scores_gemma":[0.9986731,0.00005566876,0.000005041459,0.00003206353,0.001000198,0.00004075604,0.00002712505,0.0001443763,0.00002165333],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.004842771,"threshold_uncertainty_score":0.9995857,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01665747742766594,"gpt":0.2516752904941501,"spread":0.2350178130664842,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007873193,0.0005311383,0.0009393215,0.0004283786,0.0001245228,0.00001993244,0.0003770138,0.0002699511,0.000009378615],"category_scores_gemma":[0.0002739692,0.0004736043,0.0002402644,0.0009187338,0.0001802743,0.0004295328,0.0003119656,0.0002847776,0.00001675483],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0004749535,"about_ca_system_score_gemma":0.0001271537,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0008333807,"about_ca_topic_score_gemma":0.0001016797,"domain_scores_codex":[0.9969074,0.0000271195,0.0008654981,0.0009539636,0.0005895566,0.0006564719],"domain_scores_gemma":[0.9979399,0.00005612364,0.0005425616,0.0008622421,0.0002866202,0.0003124906],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001885996,0.000121417,0.00009941714,0.0001783402,0.0005974997,0.000002126422,0.00296736,0.0002668829,0.9890438,0.0001324929,0.00005068016,0.006351334],"study_design_scores_gemma":[0.001588787,0.00009831748,0.00003799776,0.00005021337,0.0004732075,0.00002252706,0.0009154359,0.002245697,0.9933659,0.0001998429,0.0004369392,0.0005651084],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9956791,0.0002607211,0.00176084,0.000056447,0.0001470066,0.001285811,0.0001026388,0.0001417692,0.0005656303],"genre_scores_gemma":[0.9945142,0.00001577259,0.002018569,0.0000190208,0.0004239831,0.0005207545,0.001418822,0.0001200905,0.0009488398],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.005786225,"threshold_uncertainty_score":0.9997715,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01228913714965806,"gpt":0.2395864186905733,"spread":0.2272972815409153,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000229468,0.0001321125,0.0002466361,0.000225618,0.00003883111,0.000006830721,0.0001351821,0.00006747186,0.000001646676],"category_scores_gemma":[0.0001409357,0.0001136367,0.0000731611,0.00005846,0.00008090141,0.0003292311,0.00008998949,0.00009836791,6.323872e-8],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00009431624,"about_ca_system_score_gemma":0.00003434893,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001912454,"about_ca_topic_score_gemma":0.000007737931,"domain_scores_codex":[0.9989145,0.0000115735,0.0004568634,0.0001552996,0.0003174776,0.0001443043],"domain_scores_gemma":[0.999248,0.00006078962,0.0003492959,0.00008349049,0.0001804615,0.0000779432],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001078623,0.0000271167,0.001602416,0.00003678896,0.0003204931,0.00003224015,0.0005357414,0.000800097,0.9840289,0.0001409904,6.658261e-7,0.01236672],"study_design_scores_gemma":[0.000674484,0.00006373814,0.0001379079,0.0001332279,0.00005717832,0.001353981,0.00006761603,0.006359279,0.9905875,0.0001234441,0.0003221357,0.0001195548],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9979316,0.001471714,0.00015214,0.00009935549,0.0001920545,0.00004931556,0.00000521409,0.000009746111,0.00008886716],"genre_scores_gemma":[0.9988683,0.0002897018,0.0003543388,0.00001746056,0.0003153692,0.000004237066,0.000007057521,0.00002567452,0.0001178351],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01224717,"threshold_uncertainty_score":0.4633968,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01540808081032042,"gpt":0.2777629901671438,"spread":0.2623549093568234,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007248138,0.0005630874,0.001096824,0.0004165766,0.0003783358,0.00006473131,0.001579702,0.0003484063,0.00014593],"category_scores_gemma":[0.0009144087,0.0005079905,0.0006539513,0.0004331274,0.0002793095,0.001103565,0.0008494499,0.0005736259,0.0001782898],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003887012,"about_ca_system_score_gemma":0.0000806428,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.002046039,"about_ca_topic_score_gemma":0.0001239593,"domain_scores_codex":[0.9964276,0.00003474618,0.00103497,0.0008177214,0.000830862,0.0008540962],"domain_scores_gemma":[0.9952066,0.00008790668,0.0009104919,0.003283379,0.0001829482,0.0003286934],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00003884047,0.0001014226,0.0008414052,0.0001900361,0.0004480276,0.00003598659,0.0006523762,0.00005251447,0.9844184,0.00007643719,0.0001151084,0.01302942],"study_design_scores_gemma":[0.001107894,0.00003925381,0.001031538,0.0002023693,0.0003199748,0.00005171031,0.00009585118,0.003040984,0.989741,0.00004165469,0.003676068,0.0006517518],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9900309,0.0003300663,0.000160962,0.000203509,0.000479936,0.0003175798,0.0000825491,0.0002409947,0.008153443],"genre_scores_gemma":[0.9951116,0.0000345728,0.0001754548,0.0000467418,0.0002383075,0.00005104519,0.000410881,0.0001374085,0.003793953],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01237767,"threshold_uncertainty_score":0.9997371,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.006088978396966335,"gpt":0.2492937594535817,"spread":0.2432047810566153,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001339461,0.0003443999,0.0007169431,0.00008314396,0.00009944135,0.0000504013,0.0004173111,0.0002068239,0.00002803254],"category_scores_gemma":[0.004474337,0.0002402773,0.0006537979,0.0003662161,0.0001076305,0.0001778907,0.0001361003,0.000427634,0.0000101029],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003122148,"about_ca_system_score_gemma":0.00007174319,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00003175014,"about_ca_topic_score_gemma":0.000002752115,"domain_scores_codex":[0.9974678,0.00003680725,0.0008865066,0.0003379807,0.0006412764,0.0006296088],"domain_scores_gemma":[0.9959938,0.002484809,0.000464724,0.0004521574,0.0001898318,0.0004146782],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002687042,0.0001415358,0.0002632005,0.0001279929,0.001054053,0.0002635198,0.0002077622,0.00004075038,0.9912414,0.0001256587,0.0000553115,0.006210125],"study_design_scores_gemma":[0.001228504,0.0001371277,0.00006028173,0.0001000618,0.001600916,0.0007730704,0.0001568482,0.0009322669,0.9937577,0.00008479637,0.0009069702,0.0002614324],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9896067,0.002579937,0.00678857,0.0003546113,0.0001198273,0.0003324428,0.000007593671,0.00004128207,0.0001690688],"genre_scores_gemma":[0.9974136,0.00005661565,0.001989709,0.0001405059,0.0002004018,0.00003706876,0.000008511419,0.0000680205,0.0000855994],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.007806901,"threshold_uncertainty_score":0.9798224,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01760833710495454,"gpt":0.2613462450751353,"spread":0.2437379079701807,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.002092885,0.0002727031,0.0007532325,0.001427734,0.00009021718,0.000006219582,0.001138368,0.0002179239,0.000008853866],"category_scores_gemma":[0.002715003,0.0001534634,0.0001442706,0.00391373,0.002641059,0.0003820054,0.0005533045,0.0002933773,0.000001405251],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0004606848,"about_ca_system_score_gemma":0.0001796776,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003450156,"about_ca_topic_score_gemma":0.0003406118,"domain_scores_codex":[0.9974498,0.0000391909,0.0007896845,0.0006282839,0.0004907952,0.0006022118],"domain_scores_gemma":[0.9974103,0.0005488588,0.0004816255,0.001282465,0.0001810044,0.00009577138],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00001399304,0.00005174133,0.2139971,0.00008705223,0.00002286762,0.000002557291,0.0003912521,0.00001051245,0.7731163,0.00008001885,3.290596e-8,0.01222661],"study_design_scores_gemma":[0.0005755288,0.0000727111,0.01239185,0.000150413,0.00006485097,0.000006690197,0.0009974091,0.0002003328,0.9852891,0.00006469341,0.000001138146,0.0001852915],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9983646,0.0003523695,0.0006392848,0.0001300444,0.00006677339,0.0002805835,0.0000110295,0.0001141711,0.0000411169],"genre_scores_gemma":[0.9998353,0.00001047355,0.00008326349,0.000002699064,0.000006262146,0.00001783371,0.000008318868,0.00002127251,0.00001462989],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.2121728,"threshold_uncertainty_score":0.9731094,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01224605748902072,"gpt":0.2717155436924628,"spread":0.259469486203442,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002752743,0.0001166529,0.0002812555,0.0002341445,0.00001609034,0.000002842637,0.0001354714,0.00008352668,0.000007145683],"category_scores_gemma":[0.000134617,0.0001187724,0.0001496943,0.0004241059,0.00002692566,0.0001202015,0.00003524621,0.00008621248,0.000005388201],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.000184,"about_ca_system_score_gemma":0.00001672426,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0009564194,"about_ca_topic_score_gemma":0.0002640026,"domain_scores_codex":[0.9989804,0.00000875621,0.0004133359,0.0002386992,0.0001574674,0.0002013635],"domain_scores_gemma":[0.9994246,0.00005239945,0.0001110142,0.0003282015,0.00005775553,0.00002601171],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0000364085,0.0001552271,0.001367323,0.000347476,0.0000861704,0.000002977511,0.0002017724,0.00944481,0.9731821,0.001667554,0.00002126529,0.01348688],"study_design_scores_gemma":[0.000284085,0.00001230884,0.0001821815,0.00002848046,0.00009819116,0.000008430052,0.00002103045,0.003427423,0.993961,0.001273471,0.0005739953,0.0001294554],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9962616,0.0002150868,0.002043177,0.0001433054,0.0001155496,0.0002432208,0.00001420326,0.00005089792,0.0009129652],"genre_scores_gemma":[0.9966827,0.000004555362,0.001460072,0.000003494695,0.0002537392,0.00005834078,0.0004449824,0.00002142919,0.001070657],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02077882,"threshold_uncertainty_score":0.4843397,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":false,"ca_venue":true,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.004880277637035635,"gpt":0.1876933771406775,"spread":0.1828130995036419,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003124638,0.0001574111,0.0002603919,0.0003056067,0.00006102374,0.00001412973,0.000598456,0.0001559226,0.00009527638],"category_scores_gemma":[0.0006831486,0.00009490646,0.0001498421,0.0004123325,0.00008144433,0.0001097625,0.00003575371,0.0003698044,0.00003736449],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0004430047,"about_ca_system_score_gemma":0.0001685786,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000100548,"about_ca_topic_score_gemma":0.00009909007,"domain_scores_codex":[0.9988277,0.00000549992,0.0003811794,0.0001175411,0.0001746538,0.0004934334],"domain_scores_gemma":[0.9988173,0.0002280895,0.0001093933,0.0003226426,0.0001081353,0.0004144195],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00000349296,0.000006146849,0.00008439268,0.00002244947,0.00006266899,0.00001604959,0.00007448877,0.0002792088,0.9886238,0.002445246,0.00004981693,0.008332217],"study_design_scores_gemma":[0.000208083,0.000005785799,0.000005092197,0.0001579389,0.00004812511,0.0004007707,0.00002049977,0.0008643615,0.9783279,0.0003833066,0.01941386,0.0001643235],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9503683,0.001097243,0.04036964,0.006776572,0.0003038316,0.0002206069,0.00004763627,0.0001618648,0.0006542615],"genre_scores_gemma":[0.9986739,0.000004431789,0.0008480513,0.00001983693,0.0003094116,0.00002521033,6.479913e-7,0.0000431284,0.00007545455],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.04830549,"threshold_uncertainty_score":0.3870173,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01136040399281639,"gpt":0.2334896315267623,"spread":0.2221292275339459,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0008384988,0.0004972065,0.001271215,0.0005280662,0.0001041169,0.00002220344,0.0004068372,0.0001608189,0.000006305963],"category_scores_gemma":[0.0002307807,0.0003711465,0.0002875345,0.0006955971,0.0002004679,0.0001985806,0.0002803191,0.0003826879,0.00003330835],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001882379,"about_ca_system_score_gemma":0.00002678043,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001884441,"about_ca_topic_score_gemma":0.00005115548,"domain_scores_codex":[0.9973295,0.00005957794,0.0009539252,0.0006330031,0.00052442,0.0004995149],"domain_scores_gemma":[0.99837,0.0001737332,0.0004603744,0.0007303647,0.00008029974,0.0001852389],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001229688,0.00005968387,0.000366433,0.0007660367,0.0005192905,8.629697e-7,0.0004729046,0.0002843066,0.9661171,0.0004477526,0.000003735645,0.03083888],"study_design_scores_gemma":[0.0008409361,0.0002062895,0.0001106965,0.0001697909,0.0008225339,0.0000203758,0.00006667541,0.003315699,0.9938769,0.00002053976,0.0001630302,0.0003864891],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9981257,0.0001684603,0.0002070214,0.00001773818,0.00005166838,0.0004934802,0.00002880232,0.0001064799,0.0008006293],"genre_scores_gemma":[0.9986093,0.000007958989,0.0001640327,0.00001026463,0.0002281668,0.000169292,0.0002923779,0.00009173058,0.0004268934],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.03045239,"threshold_uncertainty_score":0.9998741,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02895013240803851,"gpt":0.2663400529399203,"spread":0.2373899205318818,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003981314,0.0001325324,0.0003976776,0.0002587058,0.00004204434,0.00002468543,0.00009329163,0.00009216757,0.00002877913],"category_scores_gemma":[0.0002372649,0.00009417094,0.0001007217,0.0003574224,0.00002399902,0.0004550623,0.00002779364,0.0001845361,0.000001779162],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.000100319,"about_ca_system_score_gemma":0.00002664559,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001183856,"about_ca_topic_score_gemma":0.000003195416,"domain_scores_codex":[0.9989261,0.00003486844,0.0005074576,0.0001998562,0.0001816726,0.0001500204],"domain_scores_gemma":[0.9993759,0.00004758855,0.0002584271,0.00009367923,0.0001022317,0.0001221582],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001851245,0.00001547446,0.0005199484,0.0000424995,0.0005279727,0.000002885981,0.0006524995,0.0210492,0.9703555,0.000009522275,0.00000586126,0.006633564],"study_design_scores_gemma":[0.0003516046,0.00007459673,0.0001542178,0.00001735674,0.001090051,0.00004066019,0.00007986738,0.1001993,0.8975922,0.000162727,0.0001197009,0.0001176341],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8423674,0.0005092322,0.1564714,0.0004507549,0.00003822314,0.0001122738,0.000001671768,0.00003244282,0.00001666058],"genre_scores_gemma":[0.9983128,0.0001778827,0.001236327,0.00002271556,0.0001917874,0.0000038791,0.00001820733,0.00001971796,0.00001668237],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1559454,"threshold_uncertainty_score":0.384018,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.007393263242055275,"gpt":0.2282188903941321,"spread":0.2208256271520768,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001546677,0.0002567455,0.000772196,0.0002873753,0.00006509452,0.00002027708,0.0001467249,0.0001289937,0.00001379082],"category_scores_gemma":[0.001610155,0.0001711849,0.000252705,0.0006040023,0.00009354098,0.0003176357,0.00008013256,0.0006087057,0.000003693204],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001292229,"about_ca_system_score_gemma":0.00008073419,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001389267,"about_ca_topic_score_gemma":0.00003782826,"domain_scores_codex":[0.998313,0.000167828,0.0004829335,0.0002294357,0.0005129575,0.0002938425],"domain_scores_gemma":[0.9976707,0.001020718,0.0005785709,0.0003575667,0.0001760929,0.0001963731],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001632822,0.0001084188,0.002916557,0.0002349735,0.0007361444,0.00005013803,0.000475749,0.00003340748,0.9829695,0.0002083248,0.00004637531,0.0120571],"study_design_scores_gemma":[0.0007425564,0.000202856,0.003567288,0.00007075547,0.0005609989,0.0004766803,0.0000428909,0.00009425308,0.9935344,0.00005502802,0.0004751773,0.0001770997],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.998319,0.0005314895,0.0003020047,0.0001850929,0.00009142781,0.0001273289,0.000007876598,0.00001314341,0.0004226649],"genre_scores_gemma":[0.9994681,0.00009815129,0.0001754531,0.00003113927,0.00007934989,0.000004263467,0.000004325757,0.00002868313,0.0001105098],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01188,"threshold_uncertainty_score":0.6980716,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01176030660999451,"gpt":0.2619492685417887,"spread":0.2501889619317942,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.003094035,0.0002759222,0.000574736,0.0005970504,0.0001748637,0.00002432954,0.0007024132,0.00008176105,0.000003969386],"category_scores_gemma":[0.001627386,0.0001896754,0.0002104243,0.001403282,0.0002259651,0.001583753,0.00004895974,0.000433786,0.000003673382],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0005990818,"about_ca_system_score_gemma":0.0003338882,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002253395,"about_ca_topic_score_gemma":0.000006207484,"domain_scores_codex":[0.9971552,0.00001535434,0.000664358,0.0004232569,0.001118885,0.0006229117],"domain_scores_gemma":[0.9979276,0.0001479018,0.0006248892,0.0004086115,0.0005863455,0.0003046504],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003108775,0.0001033216,0.000004386389,0.0001078665,0.00005106823,0.00001214747,0.0004223794,0.004898407,0.98027,0.00008388854,0.000001170848,0.01373449],"study_design_scores_gemma":[0.001586456,0.0006314558,0.00004352173,0.0003479364,0.00014942,0.002216371,0.0002272361,0.002617092,0.9915895,0.0000478338,0.0002747047,0.0002684902],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9956352,0.0002018161,0.00228581,0.0004764425,0.0003657872,0.000586239,0.000006077699,0.00005181871,0.0003908572],"genre_scores_gemma":[0.9963458,0.000017344,0.002769985,0.00004481831,0.000417831,0.00001265269,0.000002772302,0.00003073779,0.0003580369],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01346599,"threshold_uncertainty_score":0.7734736,"prediction_status":"machine_predicted_unvalidated"},"labels":[],"label_agreement":null}]}