{"meta":{"query_hash":"c5a268753f51","filters":{"venue":"Fluid Phase Equilibria"},"cohort_total":125,"direct_labels_cover":0,"predictions_cover":125,"exported":125,"export_cap":100000,"truncated":false,"label_status":"direct model label, unvalidated","prediction_status":"machine_predicted_unvalidated (Codex and Gemma teacher distillation)","score_status":"score_only:v0-immature-baseline","snapshot":{"source":"OpenAlex, pinned release, all 482 partitions","release":"2026-06-24","frame_built":"2026-07-12"},"permalink":"https://metacan.xera.ac/q/c5a268753f51","api":"https://metacan.xera.ac/api/v1/cohort?venue=Fluid+Phase+Equilibria"},"results":[{"id":"W1618958288","doi":"10.1016/j.fluid.2015.09.032","title":"Non-random two-liquid modelling of switchable-hydrophilicity solvent systems: N,N -Dimethylcyclohexanamine, water, and toluene","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Queen's University","funders":"","keywords":"Chemistry; Toluene; Ternary operation; Ternary numeral system; Solvent; Liquid liquid; Thermodynamics; Phase (matter); Analytical Chemistry (journal); Chromatography; Organic chemistry","score_opus":0.029919850448328286,"score_gpt":0.25419254163580657,"score_spread":0.22427269118747828,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1618958288","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.91607684,0.004051797,0.077754,0.00005501058,0.00048395369,0.00044856916,0.00004984116,0.00018737103,0.00089264096],"genre_scores_gemma":[0.99837613,0.000032290794,0.0006647783,0.000029725534,0.00032023282,0.00004119662,0.000068097,0.00009360514,0.00037393434],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9976182,0.00006362881,0.00075578206,0.0004934078,0.0004487691,0.00062021025],"domain_scores_gemma":[0.9985769,0.000103683284,0.000116785566,0.00065798685,0.00015715662,0.00038751285],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00063575205,0.00040411906,0.00076495286,0.00013363938,0.000052043037,0.000041773674,0.00042334854,0.00017674999,0.000033254386],"category_scores_gemma":[0.00010864898,0.0003154863,0.00013137778,0.00012476266,0.00011537154,0.00030502237,0.0003221505,0.00024855064,0.0000177927],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0012713727,0.00014385353,0.000003377414,0.0002027588,0.00011889298,0.000014358676,0.0007326273,0.17119922,0.82590413,0.00013727267,0.00018678786,0.00008537013],"study_design_scores_gemma":[0.005007875,0.00026253847,1.7817372e-7,0.00016093516,0.00006044915,0.000019478048,0.000053166037,0.73126775,0.26229882,0.00013983273,0.00042727313,0.00030171705],"about_ca_topic_score_codex":0.001122728,"about_ca_topic_score_gemma":0.0000044038457,"teacher_disagreement_score":0.5636053,"about_ca_system_score_codex":0.00012541092,"about_ca_system_score_gemma":0.000055630902,"threshold_uncertainty_score":0.9999297},"labels":[],"label_agreement":null},{"id":"W1817172419","doi":"10.1016/j.fluid.2015.10.031","title":"Models for the thermodynamic properties of molten salt systems: Perspectives for ionic liquids","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Chemistry; Ionic liquid; Eutectic system; Thermodynamics; Molten salt; Ternary operation; Phase diagram; Ternary numeral system; Ionic bonding; Atmospheric temperature range; Physical chemistry; Phase (matter); Inorganic chemistry; Ion; Organic chemistry; Catalysis","score_opus":0.0708073031512437,"score_gpt":0.2910606757213199,"score_spread":0.22025337257007618,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1817172419","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.66627806,0.023027923,0.30204,0.0014199737,0.00053161255,0.004135528,0.00031756592,0.00032203455,0.0019273026],"genre_scores_gemma":[0.99559075,0.0000364942,0.00048378983,0.000022295984,0.00040674096,0.0016572303,0.000024142615,0.000065759385,0.0017127938],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99879026,0.000022234719,0.00039484305,0.00027981677,0.00018160911,0.00033121512],"domain_scores_gemma":[0.99883455,0.00013465573,0.00008661257,0.0004930515,0.00035780203,0.00009333956],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003349464,0.00019371662,0.00028517432,0.00003854125,0.00010703987,0.000041207244,0.0004179435,0.00009133662,0.000009022109],"category_scores_gemma":[0.00014769907,0.00012105251,0.0001721303,0.000114047594,0.00011242682,0.00020698263,0.00008230318,0.000083809624,0.000005503711],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00065949716,0.00019614193,1.7810444e-7,0.00024621832,0.00017415421,1.1032456e-7,0.0034037968,0.039566424,0.8113939,0.14223541,0.0019346856,0.00018946287],"study_design_scores_gemma":[0.0018191882,0.00029967874,8.960077e-8,0.000083609986,0.00007717962,0.0000032335747,0.0018894413,0.9627948,0.02912236,0.0014650495,0.0022697102,0.00017568159],"about_ca_topic_score_codex":0.000080896265,"about_ca_topic_score_gemma":0.0000010752849,"teacher_disagreement_score":0.9232284,"about_ca_system_score_codex":0.0001248743,"about_ca_system_score_gemma":0.00016229469,"threshold_uncertainty_score":0.4936378},"labels":[],"label_agreement":null},{"id":"W1965098557","doi":"10.1016/j.fluid.2007.02.008","title":"Gas–liquid partition coefficients and Henry's law constants of methyl mercaptan in aqueous solutions of Fe(II)–CDTA chelate complex","year":2007,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Industrial Gas Emission Control","field":"Engineering","cited_by":12,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Henry's law; Aqueous solution; Chelation; Partition (number theory); Partition coefficient; Inorganic chemistry; Thermodynamics; Polymer chemistry; Physical chemistry; Organic chemistry","score_opus":0.04080107709787626,"score_gpt":0.291670042964953,"score_spread":0.25086896586707674,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1965098557","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.989955,0.0007438544,0.0032749942,0.0000647754,0.0003500649,0.00045037747,0.00018887887,0.00010734738,0.004864719],"genre_scores_gemma":[0.9993863,0.000023640316,0.00036714945,0.000029835484,0.000074902695,0.0000075647295,0.000042454503,0.000035624285,0.00003250227],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9980668,0.00008084516,0.0008434448,0.00023352468,0.0002688041,0.00050657993],"domain_scores_gemma":[0.9991421,0.00017032327,0.000111477726,0.0002992853,0.000096015174,0.0001808169],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008634331,0.00022185856,0.00049283047,0.00020673506,0.00007399049,0.0000138476435,0.00015582079,0.00019737288,0.00023781811],"category_scores_gemma":[0.00012556963,0.00024042818,0.00007690065,0.00037460786,0.00023666654,0.00015487238,0.00008643458,0.00021153507,0.000005931003],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00048648875,0.00020998683,0.000027761691,0.00004766171,0.000055959124,0.000015600426,0.00036229333,0.0006337164,0.99062264,0.004519481,0.0006031782,0.0024152568],"study_design_scores_gemma":[0.014307931,0.0009919277,0.00016084565,0.00038865276,0.00013857587,0.000036129055,0.00019743977,0.22846444,0.74435127,0.00057531,0.009754825,0.0006326373],"about_ca_topic_score_codex":0.00014704747,"about_ca_topic_score_gemma":0.000059370763,"teacher_disagreement_score":0.24627133,"about_ca_system_score_codex":0.000089328976,"about_ca_system_score_gemma":0.000048365582,"threshold_uncertainty_score":0.98043764},"labels":[],"label_agreement":null},{"id":"W1965988733","doi":"10.1016/j.fluid.2014.01.040","title":"Corrigendum to “Performance comparison of adsorption isotherm models for supercritical hydrogen sorption on MOFs” [Fluid Phase Equilib. 363 (2014) 74–85]","year":2014,"lang":"en","type":"erratum","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université du Québec à Trois-Rivières","funders":"","keywords":"Chemistry; Supercritical fluid; Sorption; Adsorption; Thermodynamics; Phase (matter); Chromatography; Physical chemistry; Organic chemistry","score_opus":0.03987637455258663,"score_gpt":0.30859648483778934,"score_spread":0.2687201102852027,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1965988733","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8665198,0.0017368189,0.074215606,0.0001294217,0.03490103,0.003648066,0.0043508345,0.001298711,0.013199725],"genre_scores_gemma":[0.97374225,0.0003493909,0.0005038389,0.00022818829,0.005475593,0.00067187066,0.008391177,0.0009859974,0.009651725],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.992874,0.0002023614,0.0023215404,0.0015230859,0.0011975527,0.001881424],"domain_scores_gemma":[0.99627036,0.00020925944,0.00021355634,0.0020697394,0.00035237896,0.00088472734],"candidate_categories":["metaepi_narrow","research_integrity"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0007756758,0.0017230195,0.0025604405,0.00092313153,0.00016779888,0.00015658945,0.0014031437,0.0016641914,0.0005163737],"category_scores_gemma":[0.00013343786,0.0019031999,0.0008378546,0.0005016075,0.00028129682,0.00089705904,0.00023014277,0.0012531338,0.00048365642],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0017827722,0.0012344328,0.000002477231,0.0013191219,0.0003422761,0.0000055850046,0.00040349326,0.0127509115,0.58809376,0.0024990016,0.38788185,0.0036843237],"study_design_scores_gemma":[0.006573627,0.003335909,0.0000011984596,0.0008250351,0.00038284625,0.000015980162,0.000025231231,0.8435576,0.06595176,0.0013915565,0.076347165,0.0015921298],"about_ca_topic_score_codex":0.000023501401,"about_ca_topic_score_gemma":0.000016522423,"teacher_disagreement_score":0.8308067,"about_ca_system_score_codex":0.0006248687,"about_ca_system_score_gemma":0.0003071013,"threshold_uncertainty_score":0.9996319},"labels":[],"label_agreement":null},{"id":"W1969671023","doi":"10.1016/j.fluid.2014.07.037","title":"Phase behavior of Safaniya vacuum residue","year":2014,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Alberta Innovates; IFP Energies Nouvelles","keywords":"Asphaltene; Chemistry; Pentane; Differential scanning calorimetry; Phase diagram; Thermodynamics; Phase transition; Heat capacity; Glass transition; Analytical Chemistry (journal); Phase (matter); Organic chemistry; Polymer","score_opus":0.016930121881001636,"score_gpt":0.30546091574139206,"score_spread":0.28853079386039043,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1969671023","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96892834,0.00033123704,0.00051620783,0.00007435702,0.00008492854,0.000011919666,0.00011805316,0.00015576278,0.029779218],"genre_scores_gemma":[0.9846037,0.0000100866355,0.00040573848,0.00004702558,0.000413993,0.000022551869,0.00016519068,0.00004238587,0.014289345],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982877,0.0000377242,0.0005287435,0.00041965026,0.00034681335,0.0003793828],"domain_scores_gemma":[0.9987175,0.00008387058,0.00020220818,0.0007016224,0.000098165605,0.00019664432],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0002623745,0.00024879872,0.00046182974,0.0001129549,0.00009228961,0.000052216325,0.0004125306,0.00015109757,0.0032496452],"category_scores_gemma":[0.00013080484,0.00024039802,0.00019558336,0.00024992373,0.00010860764,0.00017751267,0.00008431508,0.00017868409,0.00007106998],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015001046,0.0013606066,0.00027171464,0.000099854195,0.000059548092,0.000013408809,0.000084734704,0.0000010654645,0.9756207,0.00011519285,0.0021215035,0.020101648],"study_design_scores_gemma":[0.008104227,0.00027719763,0.000014977955,0.00010676377,0.00041350946,0.000013860213,0.000036502297,0.008938418,0.95581186,0.00017631215,0.025755087,0.00035129263],"about_ca_topic_score_codex":0.000039876515,"about_ca_topic_score_gemma":0.0000032531677,"teacher_disagreement_score":0.023633583,"about_ca_system_score_codex":0.000031293086,"about_ca_system_score_gemma":0.000079223384,"threshold_uncertainty_score":0.99766153},"labels":[],"label_agreement":null},{"id":"W1973841173","doi":"10.1016/s0378-3812(03)00082-7","title":"SLLV phase behavior and phase diagram transitions in asymmetric hydrocarbon fluids","year":2003,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Phase diagram; Chemistry; Phase (matter); Thermodynamics; Ternary operation; Binary number; Component (thermodynamics); Statistical physics; Organic chemistry; Physics","score_opus":0.013173642319741333,"score_gpt":0.27137603167857993,"score_spread":0.2582023893588386,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1973841173","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9803406,0.002331401,0.0074171876,0.00003626653,0.00075339584,0.0008277962,0.000336283,0.0005682725,0.0073888097],"genre_scores_gemma":[0.99846864,0.00017455319,0.0004415528,0.00005056387,0.0001487713,0.00021652116,0.0002574701,0.00015657244,0.00008536402],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9972711,0.00014694639,0.0007630214,0.00059650256,0.00032612565,0.00089631043],"domain_scores_gemma":[0.9987262,0.00010428506,0.00004883465,0.0006042862,0.000035531102,0.00048090058],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00037113618,0.0005826004,0.0006276873,0.0007679586,0.00009856826,0.000118765456,0.0002532334,0.00027492674,0.0002415904],"category_scores_gemma":[0.000087367785,0.00065969175,0.00018140943,0.0013980838,0.00013309681,0.0006439489,0.000032738866,0.0004322363,0.000048335987],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017136952,0.003340312,0.00012152822,0.00008234366,0.00009673673,0.0003769018,0.00061840814,0.00016851208,0.9627081,0.0042928136,0.0003980407,0.02762489],"study_design_scores_gemma":[0.047940187,0.0014178058,0.00010278625,0.00010852188,0.0003601063,0.00026531468,0.000097890545,0.880432,0.059301686,0.0021613583,0.0062310733,0.0015812668],"about_ca_topic_score_codex":0.000014049706,"about_ca_topic_score_gemma":0.000016406411,"teacher_disagreement_score":0.90340644,"about_ca_system_score_codex":0.00016166625,"about_ca_system_score_gemma":0.00007716771,"threshold_uncertainty_score":0.99958545},"labels":[],"label_agreement":null},{"id":"W1979647647","doi":"10.1016/j.fluid.2006.05.030","title":"Measurement of gas solubility and diffusivity in polylactide","year":2006,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Polymer Foaming and Composites","field":"Materials Science","cited_by":124,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Solubility; Chemistry; Sorption; Dissolution; Swelling; Diffusion; Thermal diffusivity; Volume (thermodynamics); Thermodynamics; Gaseous diffusion; Carbon dioxide; Nitrogen; Nitrogen gas; Chemical engineering; Organic chemistry; Physical chemistry; Adsorption","score_opus":0.013843549561753078,"score_gpt":0.2503174805689916,"score_spread":0.23647393100723854,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1979647647","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99704826,0.0014760005,0.00018186521,0.000095269694,0.00017180805,0.000110423774,0.000022501084,0.000044005454,0.0008498853],"genre_scores_gemma":[0.9997079,0.0000031113013,0.00014324082,0.000016603019,0.00006354267,0.000007749671,0.0000030939343,0.000008350954,0.000046412173],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9987378,0.00011082252,0.00031740885,0.00027261346,0.00029836778,0.0002629531],"domain_scores_gemma":[0.9994984,0.000047811944,0.00007506717,0.00028210372,0.000036851645,0.000059710193],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000630131,0.00012281479,0.00023213134,0.000062918996,0.00003985066,0.00003209516,0.00013420857,0.000039836727,0.000092079295],"category_scores_gemma":[0.000053541888,0.00011511309,0.000037110676,0.00011047359,0.00011796145,0.00015186369,0.00008947032,0.000051045423,0.000011823531],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001073424,0.0004211558,0.006187366,0.00003100426,0.000002274002,0.000003823315,0.00006247029,0.000002114558,0.99195325,0.0001982873,0.00018609871,0.00084482774],"study_design_scores_gemma":[0.0011736655,0.00010470923,0.019897178,0.000041921237,0.0000103549255,0.000004881847,0.000007436551,0.0015473011,0.9759335,0.0010663084,0.00009251558,0.00012020934],"about_ca_topic_score_codex":0.0020066903,"about_ca_topic_score_gemma":0.0001696259,"teacher_disagreement_score":0.016019717,"about_ca_system_score_codex":0.00004551175,"about_ca_system_score_gemma":0.000052294537,"threshold_uncertainty_score":0.46941754},"labels":[],"label_agreement":null},{"id":"W1980850509","doi":"10.1016/j.fluid.2007.12.009","title":"Mutual interactions between crude oil and CO2 under different pressures","year":2008,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Enhanced Oil Recovery Techniques","field":"Engineering","cited_by":110,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Petroleum Technology Research Centre; University of Regina","funders":"","keywords":"Chemistry; Asphaltene; Crude oil; Saturation (graph theory); Enhanced oil recovery; Light crude oil; Surface tension; Thermodynamics; Pressure drop; Gas oil ratio; Bubble point; Petroleum engineering; Drop (telecommunication); Bubble; Chromatography; Mechanics; Organic chemistry; Geology","score_opus":0.027513174247878178,"score_gpt":0.28355184723861815,"score_spread":0.25603867299073996,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1980850509","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9834704,0.000631204,0.0058640083,0.000044857316,0.0003286782,0.000057997386,0.00008058208,0.00093173,0.008590571],"genre_scores_gemma":[0.99603456,0.00042066583,0.0006966435,0.000028124354,0.00029445853,0.000039010065,0.000049838825,0.0000573421,0.0023793562],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99907404,0.00003124483,0.00025182974,0.00021899793,0.00014960192,0.0002742706],"domain_scores_gemma":[0.9993718,0.00017647537,0.000025561276,0.0002699863,0.00002325031,0.00013288735],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000041188527,0.00022162324,0.00025987,0.000105715386,0.0000751711,0.00003515119,0.00013784361,0.000086045045,0.00021709829],"category_scores_gemma":[0.000026477825,0.00021841873,0.00006257041,0.00008916489,0.00007838365,0.00032423754,0.00007223838,0.00021360167,0.000035965902],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000043173644,0.000113156995,0.0011989371,0.00009779689,0.0002078056,0.000022448163,0.00050305907,0.0001787547,0.946069,0.00027350633,0.034146048,0.017146297],"study_design_scores_gemma":[0.0024623957,0.00034981998,0.010600306,0.00022643906,0.00013852828,0.0001091693,0.00003761294,0.021415398,0.8803022,0.0017757213,0.08154232,0.001040096],"about_ca_topic_score_codex":0.0000116003175,"about_ca_topic_score_gemma":0.000011188814,"teacher_disagreement_score":0.06576682,"about_ca_system_score_codex":0.000057085606,"about_ca_system_score_gemma":0.000012438473,"threshold_uncertainty_score":0.89068574},"labels":[],"label_agreement":null},{"id":"W1982000085","doi":"10.1016/s0378-3812(02)00030-4","title":"Prediction of interfacial tension between an organic solvent and aqueous solutions of mixed-electrolytes","year":2002,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Surface tension; Aqueous solution; Electrolyte; Organic solvent; Solvent; Thermodynamics; Organic chemistry; Chemical engineering; Inorganic chemistry; Physical chemistry","score_opus":0.05170462582373215,"score_gpt":0.2480389226060901,"score_spread":0.19633429678235795,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1982000085","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9906689,0.00074878114,0.0075669354,0.000085981184,0.00010642975,0.0001317793,0.00020074137,0.000114834416,0.00037562713],"genre_scores_gemma":[0.9992554,0.000033219545,0.00021152201,0.0000075872426,0.00028194088,0.000006656074,0.00007136756,0.000024921936,0.00010735865],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988158,0.00003301156,0.00044301455,0.00024285851,0.00017717248,0.00028814003],"domain_scores_gemma":[0.99933153,0.00009899635,0.000078409255,0.00026359846,0.00007991185,0.00014755722],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0000746469,0.00016220809,0.00031732628,0.00005227731,0.000066952394,0.000008072819,0.00015252449,0.000120406025,0.0003923876],"category_scores_gemma":[0.00014098552,0.00014788606,0.00009285528,0.0001825712,0.00018823113,0.00015777002,0.00013815128,0.00019759567,0.000012497532],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000041389347,0.00039959842,0.00006367678,0.000060351664,0.000051147046,5.668149e-7,0.00021369313,0.000020574313,0.99426526,0.0003234785,0.00071947713,0.0038407773],"study_design_scores_gemma":[0.00091276754,0.0005498019,0.000054313303,0.00007251047,0.00009386294,0.0000072707753,0.000012916753,0.28409782,0.71260464,0.0011329249,0.00031139443,0.00014980354],"about_ca_topic_score_codex":0.000030186933,"about_ca_topic_score_gemma":0.0000018348954,"teacher_disagreement_score":0.28407723,"about_ca_system_score_codex":0.000044781125,"about_ca_system_score_gemma":0.000011868023,"threshold_uncertainty_score":0.60306185},"labels":[],"label_agreement":null},{"id":"W1983750855","doi":"10.1016/j.fluid.2011.10.014","title":"Corrigendum to “The activity of individual ions. A conceptual discussion of the relation between the theory and the experimentally measured values” [Fluid Phase Equilibr. 312 (2011) 79–84]","year":2011,"lang":"en","type":"erratum","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Chemistry; Relation (database); Ion; Phase (matter); Thermodynamics; Organic chemistry; Physics; Data mining","score_opus":0.036716301490213314,"score_gpt":0.2761905316338971,"score_spread":0.2394742301436838,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1983750855","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92928517,0.018425496,0.006283662,0.0035094484,0.022779392,0.0070602046,0.004097906,0.00036248515,0.008196249],"genre_scores_gemma":[0.97545385,0.000056728888,0.000049742204,0.00016150966,0.0013838806,0.00020745197,0.00033364783,0.00019400004,0.022159178],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99408084,0.0018452948,0.0011405734,0.0007775671,0.0014581879,0.0006975238],"domain_scores_gemma":[0.99577194,0.00067667646,0.00083649764,0.0023245977,0.0001784503,0.00021181029],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0030433768,0.0008542077,0.0011475227,0.00012031318,0.0004128812,0.00008564679,0.0030892065,0.00071749755,0.0006109787],"category_scores_gemma":[0.0011217315,0.0003448241,0.0005809706,0.00030412126,0.0021507095,0.00034275666,0.0019449281,0.0016600647,0.000021117152],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0048900237,0.00043160608,0.000008409179,0.000120265766,0.0010875779,0.0000021043745,0.022609068,0.000019829937,0.7668735,0.003960598,0.19506079,0.0049362485],"study_design_scores_gemma":[0.046067987,0.003335784,0.0015574791,0.003919118,0.0070403176,0.00008425284,0.00762492,0.051137537,0.7499547,0.012366488,0.11224932,0.0046620965],"about_ca_topic_score_codex":0.0001146271,"about_ca_topic_score_gemma":0.00000986923,"teacher_disagreement_score":0.08281147,"about_ca_system_score_codex":0.00016508886,"about_ca_system_score_gemma":0.00036223046,"threshold_uncertainty_score":0.9999004},"labels":[],"label_agreement":null},{"id":"W1985430265","doi":"10.1016/j.fluid.2011.05.006","title":"A semi-empirical Henry's law expression for carbon dioxide dissolution in ionic liquids","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":28,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Chemistry; Fugacity; Thermodynamics; Ionic liquid; Solubility; Dissolution; Carbon dioxide; Henry's law; Activity coefficient; Ionic strength; Equation of state; Ionic bonding; Physical chemistry; Organic chemistry; Aqueous solution; Catalysis","score_opus":0.0470921864593373,"score_gpt":0.30068106244577447,"score_spread":0.2535888759864372,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1985430265","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9858443,0.00034988014,0.0062031155,0.00021241559,0.00020427874,0.0005679374,0.000030228319,0.00023687516,0.0063509406],"genre_scores_gemma":[0.99723655,0.000011197009,0.001083779,0.00010175872,0.00029593872,0.0004838936,0.000069587644,0.00005563203,0.0006616639],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984513,0.00003177204,0.00045543446,0.00040866053,0.00015612104,0.0004967012],"domain_scores_gemma":[0.9992386,0.00007217023,0.000053277443,0.0004387862,0.00004494803,0.00015221327],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018386131,0.00022014121,0.00026244813,0.00005938759,0.00007494996,0.000015439029,0.0002583854,0.00018228483,0.00014627581],"category_scores_gemma":[0.00007199368,0.00019540018,0.00012554141,0.00019008681,0.00006705878,0.00018836344,0.00012675064,0.00018718006,0.0000222337],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003624146,0.00032531208,0.000025761137,0.00004663223,0.000011652282,0.0000026060945,0.00063993374,0.000045639747,0.9867397,0.011091576,0.0005751206,0.00013363725],"study_design_scores_gemma":[0.002608775,0.00029032803,0.000020948508,0.00015024183,0.000025859556,0.0000059240756,0.000052615665,0.17477688,0.80997056,0.0016727027,0.010058924,0.00036624982],"about_ca_topic_score_codex":0.00019137282,"about_ca_topic_score_gemma":0.000010780167,"teacher_disagreement_score":0.17676917,"about_ca_system_score_codex":0.00015052577,"about_ca_system_score_gemma":0.000046987487,"threshold_uncertainty_score":0.7968188},"labels":[],"label_agreement":null},{"id":"W1986951230","doi":"10.1016/s0378-3812(02)00325-4","title":"Excess enthalpies of the ternary mixtures: diisopropyl ether + (2,2,4-trimethylpentane or n-heptane) + methylcyclohexane at 298.15 K","year":2003,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Diisopropyl ether; Methylcyclohexane; Chemistry; Ternary operation; Enthalpy; Heptane; UNIFAC; Ether; Physical chemistry; Thermodynamics; Organic chemistry; Activity coefficient; Toluene","score_opus":0.01999727971450287,"score_gpt":0.27145766256779624,"score_spread":0.25146038285329336,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1986951230","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9829252,0.008078416,0.0010525122,0.00022266535,0.0011407619,0.00060624303,0.00012793942,0.000251385,0.005594872],"genre_scores_gemma":[0.9778207,0.00006633006,0.0012048583,0.00020742476,0.0002616031,0.00005396638,0.000029838282,0.00016759356,0.020187674],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9967783,0.00031821307,0.0007988233,0.00063432776,0.00072775455,0.0007425633],"domain_scores_gemma":[0.9975723,0.00043304954,0.00026498677,0.0014167425,0.000097847274,0.00021507917],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00046821884,0.00057574216,0.0006985381,0.00010953408,0.00014139054,0.00003956636,0.0012610673,0.00031695465,0.00471538],"category_scores_gemma":[0.0008258816,0.00035871155,0.00038675833,0.0004238249,0.00034575126,0.00024755186,0.0005158297,0.00047981582,0.00008437544],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0007455567,0.00031862178,0.0001307072,0.00015940046,0.00026985133,0.000048480146,0.00087554,0.000080536265,0.99224293,0.0006787233,0.0031655936,0.0012840634],"study_design_scores_gemma":[0.0030834135,0.00018523283,0.000050846542,0.00018225588,0.00014375123,0.00014305527,0.000116590665,0.004865958,0.9667887,0.0007008305,0.023162508,0.0005768416],"about_ca_topic_score_codex":0.00011532444,"about_ca_topic_score_gemma":0.00001981362,"teacher_disagreement_score":0.02545421,"about_ca_system_score_codex":0.00022660794,"about_ca_system_score_gemma":0.0001118873,"threshold_uncertainty_score":0.9998865},"labels":[],"label_agreement":null},{"id":"W1987596929","doi":"10.1016/j.fluid.2009.09.023","title":"Thermodynamic modeling and experimental measurement of calcium sulfate in complex aqueous solutions","year":2009,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":45,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Solubility; Aqueous solution; Activity coefficient; Pitzer equations; Electrolyte; Gibbs free energy; Thermodynamics; Inorganic chemistry; Sodium sulfate; Osmotic coefficient; Physical chemistry; Sodium; Organic chemistry","score_opus":0.08098682265985165,"score_gpt":0.3007042611278833,"score_spread":0.21971743846803166,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1987596929","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.984489,0.001394387,0.011413037,0.00017498102,0.000046563353,0.00017826827,0.00002808838,0.0000890845,0.0021865543],"genre_scores_gemma":[0.99949104,0.0000074955624,0.00030040348,0.000041232135,0.00007531607,0.000012840924,0.000026976839,0.000017817534,0.000026873078],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9987022,0.000028144997,0.00039238468,0.00025950372,0.0002467072,0.00037103277],"domain_scores_gemma":[0.9995411,0.000024707613,0.000034300272,0.00022941794,0.000048835565,0.00012163175],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000109282424,0.00018537384,0.00028284703,0.000050767863,0.000057355137,0.000011935021,0.00015548788,0.0000751972,0.00010101798],"category_scores_gemma":[0.000047433306,0.00017377062,0.00008599407,0.00014425587,0.000086715496,0.00010027907,0.00009203375,0.0001779819,0.000006879657],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010126079,0.0005413911,0.0000014640443,0.000018759489,0.000015877979,0.0000024509588,0.00020911517,0.0034147007,0.9925483,0.002276439,0.00008551844,0.00078474684],"study_design_scores_gemma":[0.0011214055,0.00009406633,0.0000072774437,0.000047663045,0.00001100572,0.0000034540774,0.000019758167,0.7914494,0.20543471,0.0016136215,0.00003289019,0.00016475072],"about_ca_topic_score_codex":0.000116190255,"about_ca_topic_score_gemma":0.0000031277027,"teacher_disagreement_score":0.7880347,"about_ca_system_score_codex":0.0001642844,"about_ca_system_score_gemma":0.000024127703,"threshold_uncertainty_score":0.708616},"labels":[],"label_agreement":null},{"id":"W1992379499","doi":"10.1016/j.fluid.2003.11.009","title":"Excess enthalpies of the ternary mixtures: tetrahydrofuran + (diisopropyl ether or 2-methyltetrahydrofuran) + n-heptane at 298.15 K","year":2004,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Chemistry; Diisopropyl ether; Tetrahydrofuran; Ternary operation; Heptane; Enthalpy; Ether; Thermodynamics; Physical chemistry; Organic chemistry","score_opus":0.015873668712249704,"score_gpt":0.26241863042615116,"score_spread":0.24654496171390144,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1992379499","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98874843,0.00473768,0.0011101488,0.0007100696,0.0010435614,0.0006042606,0.00018797562,0.00037810227,0.0024797656],"genre_scores_gemma":[0.99213046,0.000049687013,0.0006465027,0.0002390702,0.00046401838,0.000050957216,0.000041445433,0.00018258044,0.0061952956],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9966821,0.00011965256,0.0008684928,0.00068303413,0.0008158113,0.0008309171],"domain_scores_gemma":[0.99774987,0.00023367698,0.00024601858,0.0014402195,0.00008981741,0.0002404214],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00028321857,0.0006413001,0.0007082304,0.0001355505,0.00017187504,0.00004470378,0.0016390387,0.00036922275,0.0017488368],"category_scores_gemma":[0.0003800969,0.00040172943,0.00046051852,0.0004693856,0.00048183557,0.00034467605,0.0006144329,0.0005877925,0.00011942805],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0009779548,0.00038669936,0.000051093164,0.00022607592,0.0002431646,0.00006836101,0.0016736592,0.0010600146,0.9923161,0.0004339941,0.0008571154,0.0017057653],"study_design_scores_gemma":[0.0056850836,0.0003000487,0.00008807322,0.0004463366,0.00012975783,0.00016206122,0.000105882405,0.013157937,0.97405195,0.001536548,0.0036089092,0.00072739634],"about_ca_topic_score_codex":0.00022936825,"about_ca_topic_score_gemma":0.000057544232,"teacher_disagreement_score":0.018264137,"about_ca_system_score_codex":0.00033582994,"about_ca_system_score_gemma":0.00013060945,"threshold_uncertainty_score":0.9998435},"labels":[],"label_agreement":null},{"id":"W1993659868","doi":"10.1016/j.fluid.2011.06.038","title":"Ionic liquids for CO2 capture using COSMO-RS: Effect of structure, properties and molecular interactions on solubility and selectivity","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":111,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Public Works and Government Services Canada; Government of Canada","keywords":"Chemistry; Ionic liquid; Solvation; Solubility; Thermodynamics; Henry's law; Selectivity; COSMO-RS; Dilution; Ionic bonding; Molar volume; Activity coefficient; Polarity (international relations); Physical chemistry; Ion; Organic chemistry; Aqueous solution","score_opus":0.04236408230057681,"score_gpt":0.2833351779089501,"score_spread":0.24097109560837326,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1993659868","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9951853,0.00043905192,0.003283201,0.000032966236,0.00008538634,0.0006644387,0.00009749966,0.0000633795,0.00014873497],"genre_scores_gemma":[0.9990217,0.000004046404,0.0007238087,0.000027657872,0.000055544657,0.000073268704,0.000017802797,0.000031999716,0.000044134144],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99907047,0.0000485741,0.00024545664,0.00031431438,0.00009283671,0.00022833225],"domain_scores_gemma":[0.99941736,0.00009775176,0.000060671966,0.00026583276,0.00007152541,0.00008686042],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001391124,0.00020114183,0.0002866968,0.000046961046,0.000099372635,0.000020167025,0.00009310649,0.000094050985,0.00004063939],"category_scores_gemma":[0.00013929645,0.00015499452,0.00006830885,0.000097377546,0.00012175452,0.00015121006,0.00007869511,0.00016143409,6.7089286e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006511011,0.00008866814,0.0000316475,0.00023978417,0.0000641206,5.0300616e-7,0.0003616175,0.000083696155,0.9969724,0.0011080249,0.000054991488,0.0003434482],"study_design_scores_gemma":[0.0011082888,0.0005938565,0.000014817259,0.00008421531,0.00008146475,0.000009846689,0.000017803319,0.1517311,0.84571624,0.0003350944,0.00014989826,0.00015737765],"about_ca_topic_score_codex":0.000133245,"about_ca_topic_score_gemma":0.0000042929805,"teacher_disagreement_score":0.1516474,"about_ca_system_score_codex":0.0000578449,"about_ca_system_score_gemma":0.000038686427,"threshold_uncertainty_score":0.6320493},"labels":[],"label_agreement":null},{"id":"W1994331925","doi":"10.1016/j.fluid.2004.12.016","title":"Liquid–liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor–liquid–liquid equilibrium with methane","year":2005,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":40,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Methylcyclohexane; Solubility; Methane; Aqueous solution; Heptane; Ether; Analytical Chemistry (journal); Chromatography; Organic chemistry; Toluene","score_opus":0.021176975570539755,"score_gpt":0.2674779367440171,"score_spread":0.24630096117347733,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1994331925","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98258907,0.003246769,0.0009286517,0.0020005775,0.0004305295,0.0017734716,0.00048649713,0.00038574668,0.008158668],"genre_scores_gemma":[0.9797286,0.00035143673,0.012678658,0.0008661173,0.00074718473,0.0001251373,0.0011464057,0.0004532209,0.0039032428],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9893711,0.00096203026,0.0020813805,0.0030618913,0.0019268021,0.002596754],"domain_scores_gemma":[0.99301076,0.00050872075,0.00075179734,0.004221275,0.00014764859,0.0013598143],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.0031139827,0.0017225785,0.00212585,0.00041215672,0.00023289242,0.000171245,0.0027350737,0.0007392836,0.008977516],"category_scores_gemma":[0.00013951687,0.0011415922,0.00027358875,0.0012929492,0.001936238,0.0028173476,0.0032692712,0.0011383517,0.00047304647],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.023446128,0.000948736,0.00006392108,0.00017182565,0.00071629084,0.00020826914,0.0017806714,0.0014729941,0.968386,0.000087055734,0.0017337523,0.000984338],"study_design_scores_gemma":[0.009796868,0.020484034,0.000028395354,0.000271065,0.0010145594,0.0005824021,0.00026650899,0.0071826386,0.88966334,0.0000731513,0.06829497,0.0023420914],"about_ca_topic_score_codex":0.00074913545,"about_ca_topic_score_gemma":0.00014833278,"teacher_disagreement_score":0.0787227,"about_ca_system_score_codex":0.00024837433,"about_ca_system_score_gemma":0.00021230547,"threshold_uncertainty_score":0.9995521},"labels":[],"label_agreement":null},{"id":"W1994653267","doi":"10.1016/s0378-3812(00)00407-6","title":"Reply to ‘Comment on “Vapor–Liquid Equilibria in Porous Media”’","year":2000,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Chemistry; Artificial neural network; Ionic liquid; Nonlinear system; Viscosity; Correlation coefficient; Work (physics); Mean squared error; Thermodynamics; Biological system; Artificial intelligence; Pattern recognition (psychology); Algorithm; Machine learning; Statistics; Computer science; Mathematics; Physics; Organic chemistry","score_opus":0.021392471400584766,"score_gpt":0.27558468760732074,"score_spread":0.254192216206736,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1994653267","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9603862,0.00015625369,0.00020721898,0.01969134,0.00027665313,0.00061046676,0.00006965851,0.00035634835,0.018245853],"genre_scores_gemma":[0.97570765,0.000029063885,0.00084386166,0.017425474,0.00081778504,0.0003344172,0.00015917608,0.00011968579,0.0045629134],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.99744606,0.000047133293,0.00072188163,0.00066353503,0.00037885443,0.0007425488],"domain_scores_gemma":[0.99843097,0.00014362785,0.000046474037,0.0009760551,0.000036946603,0.00036595238],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00029003873,0.00035335936,0.0003969455,0.00013897647,0.00007168466,0.00005154574,0.0005366435,0.00013116047,0.0066588195],"category_scores_gemma":[0.00013206236,0.00033160084,0.00011946521,0.00040331975,0.000044445427,0.00019158199,0.00014415346,0.0003023047,0.002021871],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0018440603,0.00092241965,0.000004291262,0.000035031826,0.000039713417,0.00005086605,0.0017087683,0.0010488385,0.8282741,0.008074793,0.14669716,0.011299964],"study_design_scores_gemma":[0.0034071272,0.0009004186,0.000009093003,0.00017477476,0.000020867818,0.000015354612,0.00005290763,0.033194065,0.14856496,0.00057403266,0.81240016,0.00068623666],"about_ca_topic_score_codex":0.00026327287,"about_ca_topic_score_gemma":0.0000042241213,"teacher_disagreement_score":0.67970914,"about_ca_system_score_codex":0.00023144367,"about_ca_system_score_gemma":0.000063645246,"threshold_uncertainty_score":0.99991363},"labels":[],"label_agreement":null},{"id":"W1996477731","doi":"10.1016/j.fluid.2013.07.006","title":"Temperature effects on the phase behaviour, mutual interactions and oil recovery of a light crude oil–CO2 system","year":2013,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Enhanced Oil Recovery Techniques","field":"Engineering","cited_by":58,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina; Petroleum Technology Research Centre","funders":"","keywords":"Chemistry; Asphaltene; Miscibility; Light crude oil; Surface tension; Saturation (graph theory); Crude oil; Swelling; Enhanced oil recovery; Petroleum engineering; Chromatography; Thermodynamics; Analytical Chemistry (journal); Composite material; Organic chemistry; Geology; Materials science","score_opus":0.006833215398056166,"score_gpt":0.2440023345451085,"score_spread":0.23716911914705233,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1996477731","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98896986,0.00058486033,0.00011188996,0.00013189173,0.00092739105,0.00023503782,0.00009365822,0.00067518203,0.008270209],"genre_scores_gemma":[0.99726516,0.00013318325,0.00042374118,0.00006454226,0.0002664382,0.00034159858,0.00003293118,0.00008381368,0.0013886092],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99864817,0.00010553895,0.00040836583,0.00029594215,0.00021369696,0.00032826664],"domain_scores_gemma":[0.99868333,0.0004694787,0.00007922372,0.0005621905,0.00007461044,0.00013116137],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00016216321,0.00033056305,0.00037721565,0.00017038353,0.00008055639,0.0001193885,0.00024302202,0.0001621478,0.00018077562],"category_scores_gemma":[0.00010700657,0.00025558422,0.00013297945,0.00023513193,0.00004594811,0.00052076904,0.00006471241,0.00040031032,0.00009678171],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007122242,0.0001418082,0.000008215546,0.00036036386,0.00007846385,0.00001513372,0.00020098322,0.000012459756,0.95549095,0.00025124793,0.02702858,0.01634056],"study_design_scores_gemma":[0.0013724843,0.0005746731,0.000027117398,0.0010815277,0.00006526123,0.000046419413,0.00007116879,0.00422806,0.98921084,0.00005652985,0.002959055,0.00030688194],"about_ca_topic_score_codex":0.000026199275,"about_ca_topic_score_gemma":0.0000064897868,"teacher_disagreement_score":0.03371986,"about_ca_system_score_codex":0.00013256619,"about_ca_system_score_gemma":0.00002339692,"threshold_uncertainty_score":0.9999896},"labels":[],"label_agreement":null},{"id":"W1998964147","doi":"10.1016/j.fluid.2004.06.052","title":"Vapor–liquid equilibrium of systems containing alcohols, water, carbon dioxide and hydrocarbons using SAFT","year":2004,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":64,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Chemistry; Methane; Propane; Methanol; Butane; Carbon dioxide; Hydrocarbon; Alkane; Ternary numeral system; Inorganic chemistry; Organic chemistry; Phase (matter); Catalysis","score_opus":0.017831907581868568,"score_gpt":0.24966914433175083,"score_spread":0.23183723674988227,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1998964147","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9890435,0.002990822,0.002335237,0.00002363885,0.001305561,0.00055435294,0.00009052307,0.00057009433,0.0030862887],"genre_scores_gemma":[0.999,0.000054165805,0.00023928337,0.00001631736,0.0003546106,0.000025415251,0.00008697464,0.00019421114,0.000029018616],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9970552,0.0000810773,0.0009645582,0.00053102523,0.0003992956,0.0009688552],"domain_scores_gemma":[0.9986792,0.00007579326,0.000115829105,0.00070503104,0.000052402575,0.00037174195],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00039241064,0.0005899947,0.0008912711,0.00030127133,0.00006494894,0.00007467922,0.0003545994,0.000272757,0.0000136964945],"category_scores_gemma":[0.000035836267,0.0005635057,0.00016766982,0.00029459377,0.00019283393,0.00048760403,0.00020370424,0.00029038632,0.0000069405864],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030983912,0.0001064694,0.000053597374,0.00021564878,0.00024087794,0.0000999468,0.00070693425,0.019257754,0.9776354,0.001312694,0.000004690698,0.000056192723],"study_design_scores_gemma":[0.00551902,0.0006066321,0.0000095996165,0.0003478924,0.00018407208,0.00022726324,0.00011315108,0.5850312,0.40614542,0.0009055915,0.00018011208,0.00073002005],"about_ca_topic_score_codex":0.0003851208,"about_ca_topic_score_gemma":0.000008532675,"teacher_disagreement_score":0.57148993,"about_ca_system_score_codex":0.00024133678,"about_ca_system_score_gemma":0.000105784355,"threshold_uncertainty_score":0.99968165},"labels":[],"label_agreement":null},{"id":"W1999627864","doi":"10.1016/j.fluid.2011.09.015","title":"A predictive correlation for the constant-pressure specific heat capacity of pure and ill-defined liquid hydrocarbons","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":42,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Chemistry; Heat capacity; Thermodynamics; Hydrocarbon; Group contribution method; Pentane; Vapor pressure; Analytical Chemistry (journal); Organic chemistry; Phase (matter)","score_opus":0.024486425599564356,"score_gpt":0.22304803816413668,"score_spread":0.19856161256457233,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1999627864","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9200037,0.002530051,0.06935652,0.000032551696,0.0008214457,0.0009088042,0.0007927535,0.00024319111,0.0053109666],"genre_scores_gemma":[0.9989681,0.00013869898,0.0004777777,0.000017844995,0.00015788981,0.00006983584,0.00005985251,0.00006170382,0.000048267273],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99879324,0.00004346663,0.00039112184,0.0002715559,0.00016776199,0.0003328238],"domain_scores_gemma":[0.99902815,0.00028127723,0.000057798137,0.00043946994,0.00007158331,0.000121719866],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001977205,0.0002754097,0.0003416224,0.00008251331,0.00008980381,0.000021044905,0.00021997967,0.00016538064,0.0000848795],"category_scores_gemma":[0.000064439344,0.00022748741,0.00012199326,0.00017847297,0.00024511802,0.00026591547,0.000053053802,0.00018127219,0.000004289014],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0017583055,0.00019764299,0.00011946213,0.00013940009,0.0006087534,0.0000045138418,0.004235236,0.0014881887,0.9705162,0.018954521,0.001491785,0.00048597835],"study_design_scores_gemma":[0.0029638328,0.0006541454,0.00012974534,0.00006625633,0.00024818713,0.000025287494,0.00012054087,0.9668608,0.022592623,0.003994292,0.0020524538,0.0002918825],"about_ca_topic_score_codex":0.000017601551,"about_ca_topic_score_gemma":0.000007161012,"teacher_disagreement_score":0.96537256,"about_ca_system_score_codex":0.000029018152,"about_ca_system_score_gemma":0.000031054053,"threshold_uncertainty_score":0.9276667},"labels":[],"label_agreement":null},{"id":"W2000237247","doi":"10.1016/j.fluid.2010.03.028","title":"Concerning “Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12K and pressures up to 34.5MPa” by Chapoy et al. [Fluid Phase Equilib. 214 (2003) 101–117]","year":2010,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Chemistry; Methane; Solubility; Binary number; Binary system; Thermodynamics; Phase (matter); Mineralogy; Physical chemistry; Organic chemistry","score_opus":0.028239520423767626,"score_gpt":0.2760615650773749,"score_spread":0.24782204465360727,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2000237247","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99224615,0.0022714166,0.0007824685,0.0005116093,0.0011502819,0.0017165872,0.00094105897,0.00014025836,0.00024018886],"genre_scores_gemma":[0.9988755,0.00003610368,0.0001598464,0.00034425306,0.000120897166,0.00013920493,0.00015924414,0.00011626499,0.000048703514],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9957654,0.00047581422,0.0011310696,0.0008377977,0.0008945749,0.00089535996],"domain_scores_gemma":[0.997844,0.00016059905,0.00010239676,0.0012780103,0.00026123936,0.00035378142],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0022788236,0.00067815254,0.0009384377,0.0002016077,0.00014280535,0.00012389212,0.000788859,0.0002290492,0.0001194854],"category_scores_gemma":[0.00018374289,0.0004138619,0.00014961853,0.00034962394,0.0001974579,0.00044064174,0.00057880726,0.00056867045,0.000008354728],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0012692153,0.0003403755,0.00007441575,0.00026854177,0.00021291485,0.000016477536,0.006427177,0.002523208,0.98650336,0.0001144529,0.0020308292,0.00021905777],"study_design_scores_gemma":[0.005995832,0.00037494896,0.000009257518,0.0002724962,0.00013711918,0.000027325063,0.0003366706,0.40673545,0.58284515,0.0000672676,0.0027560832,0.000442418],"about_ca_topic_score_codex":0.0003618427,"about_ca_topic_score_gemma":0.000104683146,"teacher_disagreement_score":0.40421224,"about_ca_system_score_codex":0.00013659881,"about_ca_system_score_gemma":0.00007599454,"threshold_uncertainty_score":0.9998313},"labels":[],"label_agreement":null},{"id":"W2006471397","doi":"10.1016/j.fluid.2007.09.004","title":"Modelling the fluid phase behaviour of polydisperse polyethylene blends in hydrocarbons using the modified Sanchez–Lacombe equation of state","year":2007,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":13,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Linear low-density polyethylene; Molar mass; Polyethylene; Branching (polymer chemistry); Thermodynamics; Molar mass distribution; Chemistry; High-density polyethylene; Equation of state; Hydrocarbon; Polymer chemistry; Analytical Chemistry (journal); Materials science; Organic chemistry; Polymer; Physics","score_opus":0.03608563815363906,"score_gpt":0.2922120723982,"score_spread":0.25612643424456094,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2006471397","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7924904,0.0009629778,0.20479688,0.00002693951,0.00040960906,0.00045736157,0.0001377208,0.00009743522,0.00062067766],"genre_scores_gemma":[0.9991166,0.00007780536,0.00042353108,0.000018256831,0.00014526788,0.000013465786,0.0000642957,0.00011043235,0.00003035408],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99709857,0.00013556749,0.0011971021,0.00033879257,0.0005031292,0.0007268472],"domain_scores_gemma":[0.99838424,0.00031270663,0.00022527095,0.0008719786,0.000061794664,0.00014399289],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0012738646,0.00042117297,0.0005422527,0.00033758004,0.00007826284,0.000033318203,0.00057544955,0.00016714605,0.00003574185],"category_scores_gemma":[0.000037451257,0.00033183664,0.00023118335,0.00090308266,0.00022432298,0.0003814902,0.000101787635,0.00038856117,0.0000026786552],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00031973814,0.00026832,0.00003154603,0.000034296183,0.0000766446,0.000012007894,0.0024571174,0.30967858,0.68510026,0.0011861979,0.000007406404,0.0008278495],"study_design_scores_gemma":[0.003012947,0.000115708724,0.000010462108,0.000075028816,0.00009561571,0.0000093142135,0.00021484053,0.74181086,0.25307107,0.001327031,0.000011429448,0.000245677],"about_ca_topic_score_codex":0.00054798264,"about_ca_topic_score_gemma":0.000048176855,"teacher_disagreement_score":0.43213227,"about_ca_system_score_codex":0.0001659784,"about_ca_system_score_gemma":0.00012757821,"threshold_uncertainty_score":0.9999134},"labels":[],"label_agreement":null},{"id":"W2008483717","doi":"10.1016/s0378-3812(01)00556-8","title":"Solubility of cesium chloride in water under high pressures","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Solubility; Chemistry; Aqueous solution; Caesium; Volume (thermodynamics); Chloride; Thermodynamics; Reproducibility; Analytical Chemistry (journal); Inorganic chemistry; Chromatography; Physical chemistry; Organic chemistry","score_opus":0.022112273916791787,"score_gpt":0.26912215135335354,"score_spread":0.24700987743656175,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2008483717","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9938283,0.00013897047,0.0011864539,0.0003299039,0.00021148856,0.00014069304,0.000022424778,0.00010597631,0.004035781],"genre_scores_gemma":[0.99809325,0.000009977082,0.00009346198,0.00005861118,0.0002713,0.000020902955,0.000049782368,0.000025062685,0.0013776612],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986143,0.000028127091,0.00042409406,0.00029439174,0.00019901755,0.0004400335],"domain_scores_gemma":[0.99930155,0.000108910026,0.00002849468,0.00040207306,0.000043154447,0.000115842915],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00011240362,0.00018047087,0.00031294257,0.0000401118,0.00002992279,0.000010839613,0.0002706009,0.00011368654,0.0012834516],"category_scores_gemma":[0.00007785001,0.0001338709,0.00011314318,0.00016158086,0.00014146323,0.00015034623,0.00018676456,0.00022923543,0.000073371426],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00031789413,0.0005076365,0.00009699036,0.00007082881,0.000025498268,0.0000053817116,0.00014484704,0.0015780663,0.99485624,0.0017399075,0.00047930027,0.00017738277],"study_design_scores_gemma":[0.0012269777,0.000052815085,0.00007518006,0.000036223784,0.00001909076,0.000003007608,0.000008019135,0.042886365,0.942646,0.009994301,0.0028457388,0.00020623744],"about_ca_topic_score_codex":0.00040626907,"about_ca_topic_score_gemma":0.0000093650115,"teacher_disagreement_score":0.052210223,"about_ca_system_score_codex":0.000060725397,"about_ca_system_score_gemma":0.000016514674,"threshold_uncertainty_score":0.9996295},"labels":[],"label_agreement":null},{"id":"W2011175851","doi":"10.1016/j.fluid.2004.03.001","title":"Development of a new equation of state for mixed salt and mixed solvent systems, and application to vapour–liquid and solid (hydrate)–vapour–liquid equilibrium calculations","year":2004,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":37,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Chemistry; Electrolyte; Equation of state; Thermodynamics; Activity coefficient; Clathrate hydrate; Aqueous solution; Hydrate; Solubility; van der Waals force; Salt (chemistry); Solvation; Solvent; Helmholtz free energy; Physical chemistry; Organic chemistry; Molecule","score_opus":0.02074630209828541,"score_gpt":0.27808066939867054,"score_spread":0.2573343673003851,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2011175851","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7289314,0.0006810202,0.26857367,0.00006825026,0.00022122487,0.0012026223,0.00017718501,0.00011132567,0.000033230983],"genre_scores_gemma":[0.99070054,0.00003660263,0.008599059,0.000013163056,0.00010374477,0.00016956551,0.0002571851,0.00008817733,0.000031972675],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99773693,0.000039574268,0.0010332271,0.00046055537,0.00027375697,0.00045594637],"domain_scores_gemma":[0.9987801,0.00011125287,0.00020662598,0.00036479047,0.00014308635,0.00039420085],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00041718164,0.00038119667,0.0006156414,0.00027439932,0.00008251888,0.00005165466,0.000154051,0.0001484764,0.0000043207824],"category_scores_gemma":[0.00006069148,0.00041611205,0.00006602611,0.00028838744,0.0000814176,0.00036082152,0.00013154653,0.000091602386,0.0000032108042],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006620999,0.00011699934,0.000010549326,0.0005377354,0.00016218689,0.0000012372993,0.0020110977,0.023330038,0.9696137,0.0015159583,0.000057279107,0.0019811632],"study_design_scores_gemma":[0.0062465426,0.00092343474,0.00021589553,0.00031994394,0.00014972861,0.000021531507,0.00014746228,0.44508013,0.5438543,0.0013486149,0.0010584466,0.00063397054],"about_ca_topic_score_codex":0.00006587777,"about_ca_topic_score_gemma":0.000056879526,"teacher_disagreement_score":0.42575935,"about_ca_system_score_codex":0.00013427984,"about_ca_system_score_gemma":0.00023948944,"threshold_uncertainty_score":0.99982905},"labels":[],"label_agreement":null},{"id":"W2012124422","doi":"10.1016/j.fluid.2004.01.030","title":"Solubility of hydrogen sulfide in aqueous solutions of Fe(II) complexes of trans-1,2-cyclohexanediaminetetraacetic acid","year":2004,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Industrial Gas Emission Control","field":"Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Hydrogen sulfide; Solubility; Inorganic chemistry; Aqueous solution; Sulfide; Kraft process; Sulfur; Pyrrhotite; Chelation; Solubility equilibrium; Kraft paper; Organic chemistry; Chemical engineering","score_opus":0.027433996466064838,"score_gpt":0.25834547594618035,"score_spread":0.2309114794801155,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2012124422","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99376017,0.0017949353,0.0024482687,0.00010723455,0.00026094337,0.00051887514,0.00027509264,0.00009702007,0.000737441],"genre_scores_gemma":[0.9990483,0.00002402517,0.0007173051,0.0000063731604,0.00008608145,0.000017228904,0.00003287275,0.000041003343,0.000026815398],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977941,0.000076397184,0.0011150248,0.00024210125,0.0003131985,0.00045915748],"domain_scores_gemma":[0.99899906,0.00014079415,0.0001191895,0.00051648705,0.00008647436,0.00013799034],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00041695414,0.0002530745,0.0007319484,0.00024664713,0.000033047803,0.000004595943,0.00033619272,0.00021031772,0.00022177034],"category_scores_gemma":[0.00021384179,0.00027412674,0.00020732229,0.00048508655,0.00020311409,0.00014248348,0.000053520132,0.00022339563,0.0000027128835],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017675728,0.00042326938,0.000072552175,0.00016101217,0.000065282344,0.000007224656,0.0005941082,0.014406898,0.98194945,0.00040215408,0.00016552953,0.001575739],"study_design_scores_gemma":[0.0074758925,0.00040840465,0.00013928326,0.00018071315,0.000065557164,0.000009808343,0.00004020185,0.026641289,0.9631035,0.0013317233,0.00035913027,0.00024450463],"about_ca_topic_score_codex":0.00023832405,"about_ca_topic_score_gemma":0.00006157155,"teacher_disagreement_score":0.01884598,"about_ca_system_score_codex":0.00011640894,"about_ca_system_score_gemma":0.00016735333,"threshold_uncertainty_score":0.9999711},"labels":[],"label_agreement":null},{"id":"W2012174797","doi":"10.1016/j.fluid.2012.03.006","title":"Viscosity prediction for natural gas processing applications","year":2012,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":19,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada; Virtual Materials Group","keywords":"Chemistry; Natural gas; Viscosity; Natural-gas processing; Thermodynamics; Organic chemistry","score_opus":0.013050593386208708,"score_gpt":0.2686431095567348,"score_spread":0.2555925161705261,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2012174797","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.78712064,0.0021398296,0.20496774,0.000030213054,0.0010604009,0.00085274293,0.00024876732,0.0009625254,0.002617139],"genre_scores_gemma":[0.995854,0.00001591772,0.0016902108,0.00002841829,0.001432941,0.0003633093,0.00041023476,0.00007519062,0.00012978418],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99884635,0.000015739073,0.0002774454,0.00019252188,0.00014203003,0.00052592135],"domain_scores_gemma":[0.99940276,0.000047321188,0.00003784832,0.00027691195,0.000047761183,0.00018740533],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017380816,0.00021718067,0.0001919847,0.00008462167,0.0001295917,0.000057403875,0.00017601921,0.000098739125,0.00003770995],"category_scores_gemma":[0.000015766453,0.00022684567,0.000102020094,0.00021550443,0.000040102048,0.00085356715,0.000032753833,0.00013897831,0.000042243482],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007712134,0.00024197836,0.00016629582,0.00020887326,0.00006672341,4.532718e-7,0.00030391553,0.00023370211,0.96531534,0.002435335,0.0025653515,0.028384922],"study_design_scores_gemma":[0.0016411429,0.00005339004,0.0001420968,0.000029954997,0.000077858276,0.000020017565,0.000017675413,0.936322,0.022698104,0.0012828569,0.037400328,0.0003145758],"about_ca_topic_score_codex":0.0000010636002,"about_ca_topic_score_gemma":7.776328e-7,"teacher_disagreement_score":0.94261724,"about_ca_system_score_codex":0.000103398546,"about_ca_system_score_gemma":0.000027195863,"threshold_uncertainty_score":0.92504984},"labels":[],"label_agreement":null},{"id":"W2013268522","doi":"10.1016/j.fluid.2007.09.015","title":"Tuning methane content in gas hydrates via thermodynamic modeling and molecular dynamics simulation","year":2007,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":78,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"National Research Council Canada; Steacie Institute for Molecular Sciences; University of British Columbia","funders":"","keywords":"Methane; Clathrate hydrate; Chemistry; Natural gas; Hydrate; Propane; van der Waals force; Molecular dynamics; Tetrahydrofuran; Thermodynamics; Chemical engineering; Organic chemistry; Molecule; Computational chemistry","score_opus":0.021134656833977153,"score_gpt":0.27155539725145106,"score_spread":0.2504207404174739,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2013268522","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.87044424,0.00034833627,0.12597078,0.00006424179,0.000096770586,0.00027529147,0.0000037961036,0.00004200037,0.0027545572],"genre_scores_gemma":[0.99854267,0.000021703625,0.0010857543,0.0001103828,0.00002206424,0.00000496569,0.0000476987,0.000034746558,0.00013004465],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9983793,0.0000895377,0.00043089731,0.00040588487,0.00024572742,0.00044868194],"domain_scores_gemma":[0.9994116,0.00010750688,0.0000794842,0.00022630577,0.00001031589,0.00016479325],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008079686,0.00021911938,0.00023478235,0.00009724553,0.0000574104,0.000030625175,0.00014425069,0.0001283796,0.0003441487],"category_scores_gemma":[0.000037356927,0.00019989155,0.0000508814,0.00028713918,0.00008609334,0.00021859395,0.0001502267,0.00020609896,0.000046015095],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011017544,0.00008095918,0.00069657405,0.000006746774,0.000015791802,0.000043093227,0.0004485063,0.25320414,0.73859346,0.00016320292,7.7582325e-7,0.006636544],"study_design_scores_gemma":[0.0013820202,0.00010100016,0.00014288662,0.000026586727,0.00002194044,0.000007154752,0.00008570773,0.99059,0.0037721891,0.0036071895,0.000019972074,0.0002433992],"about_ca_topic_score_codex":0.0005623208,"about_ca_topic_score_gemma":0.0001060722,"teacher_disagreement_score":0.7373858,"about_ca_system_score_codex":0.0002490758,"about_ca_system_score_gemma":0.000009911225,"threshold_uncertainty_score":0.8151341},"labels":[],"label_agreement":null},{"id":"W2013361285","doi":"10.1016/s0378-3812(03)00025-6","title":"Non-ideality of methanol solutions of artificial serum in the mole fraction range from 5 × 10−4 to 5 × 10−3 at 25 °C","year":2003,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Protein Interaction Studies and Fluorescence Analysis","field":"Biochemistry, Genetics and Molecular Biology","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Vancouver Hospital and Health Sciences Centre; University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada; Danmarks Tekniske Universitet","keywords":"Chemistry; Mole fraction; Enthalpy; Thermodynamics; Methanol; Mole; Freezing-point depression; Activity coefficient; Vapor pressure; Chromatography; Aqueous solution; Freezing point; Physical chemistry; Organic chemistry","score_opus":0.03191333328499121,"score_gpt":0.32291142634152775,"score_spread":0.29099809305653657,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2013361285","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9928614,0.00029948005,0.0049135922,0.00019212897,0.00012701502,0.0002490303,0.00021371429,0.0000038506964,0.0011397782],"genre_scores_gemma":[0.9989309,0.000032199645,0.00028629522,0.00009904627,0.00010834337,0.00004756601,0.0000816359,0.000008997505,0.00040503027],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99880403,0.00015269704,0.00039821788,0.00027048888,0.00017337519,0.00020120571],"domain_scores_gemma":[0.9992205,0.000041598974,0.00013438924,0.00043776183,0.000121644334,0.00004412826],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00040649754,0.00012317808,0.00023775524,0.00006518383,0.00007605854,0.000009085599,0.00016566468,0.00009450842,0.0008257642],"category_scores_gemma":[0.00015649515,0.00010252847,0.00016862199,0.00026110283,0.00006210701,0.000009949073,0.00009246197,0.0000625425,0.000045370354],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00029550705,0.00022099593,0.00038080369,0.0000072208672,0.00009967776,0.0000011396512,0.00014660657,0.00003023594,0.990886,0.00007220053,0.0074051223,0.00045449418],"study_design_scores_gemma":[0.00062540505,0.00025318857,0.000965647,0.000015803778,0.000059373047,0.0000010963464,0.00032293482,0.00071786466,0.9757754,0.00013124202,0.021009883,0.0001221116],"about_ca_topic_score_codex":0.0003597391,"about_ca_topic_score_gemma":0.0002338697,"teacher_disagreement_score":0.015110546,"about_ca_system_score_codex":0.000026002732,"about_ca_system_score_gemma":0.00003887563,"threshold_uncertainty_score":0.9041539},"labels":[],"label_agreement":null},{"id":"W2013597152","doi":"10.1016/s0378-3812(01)00768-3","title":"Densities and volumetric properties of the aqueous solutions of 2-amino-2-methyl-1-propanol, n-butyldiethanolamine and n-propylethanolamine at temperatures from 298.15 to 353.15 K","year":2002,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":67,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Aqueous solution; Alkanolamine; Propanol; Molar; Molar volume; Thermodynamics; Atmospheric temperature range; Physical chemistry; Analytical Chemistry (journal); Organic chemistry; Methanol","score_opus":0.023575049034746408,"score_gpt":0.21415134455001728,"score_spread":0.19057629551527086,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2013597152","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9533303,0.04471991,0.00010967491,0.00041131515,0.00027318182,0.0005623356,0.00030302914,0.00012742066,0.00016285798],"genre_scores_gemma":[0.99572134,0.0001849816,0.0005653625,0.0000969461,0.00017375397,0.00004580388,0.000019378158,0.000085493324,0.003106959],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99758995,0.00012338716,0.00068244693,0.0005683724,0.00047235304,0.00056351215],"domain_scores_gemma":[0.99845415,0.00017609954,0.0001805193,0.000827514,0.00017299676,0.00018873267],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00019517897,0.00046101515,0.00070945633,0.00024729117,0.00017024316,0.000044361168,0.0005220742,0.00022599833,0.00021211884],"category_scores_gemma":[0.0007765216,0.000327673,0.00014313092,0.0005028099,0.000505597,0.00021771358,0.0009951023,0.00032526124,0.000013624913],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024412147,0.00016577521,0.00010220048,0.00024029991,0.00017159995,0.000006420328,0.0017838799,0.00003173616,0.99370193,0.00009079384,0.0010632524,0.0023980022],"study_design_scores_gemma":[0.0017483865,0.0003554585,0.0005361903,0.00038546819,0.00014705681,0.000048084876,0.00015540395,0.08673985,0.90889144,0.000093228824,0.00043154543,0.000467912],"about_ca_topic_score_codex":0.00034883738,"about_ca_topic_score_gemma":0.000051400784,"teacher_disagreement_score":0.08670811,"about_ca_system_score_codex":0.00010633737,"about_ca_system_score_gemma":0.00002980769,"threshold_uncertainty_score":0.9999175},"labels":[],"label_agreement":null},{"id":"W2016127141","doi":"10.1016/j.fluid.2014.12.050","title":"Equation of state modeling for the vapor pressure of biodiesel fuels","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Biodiesel Production and Applications","field":"Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Virtual Materials Group (Canada); University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Acentric factor; Chemistry; Biodiesel; Vapor pressure; Equation of state; Thermodynamics; Heat capacity; Fatty acid methyl ester; Organic chemistry","score_opus":0.10574482368220058,"score_gpt":0.30506818387440426,"score_spread":0.1993233601922037,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2016127141","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.35286602,0.0050862636,0.6383132,0.00052463403,0.00063167757,0.0009999748,0.00056225975,0.00019924193,0.00081674574],"genre_scores_gemma":[0.99774104,0.000057620888,0.0017345869,0.000008802759,0.000113034366,0.00007847988,0.000039802097,0.000016743614,0.00020988399],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9993587,0.000014468782,0.00028111515,0.000106814456,0.00011972107,0.00011918862],"domain_scores_gemma":[0.9993768,0.000065494576,0.000047958103,0.00028439032,0.00018014,0.00004523535],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034247106,0.000084602325,0.00013129035,0.000041694308,0.000029353707,0.000010104544,0.0001323564,0.00003599286,0.00002072801],"category_scores_gemma":[0.00008351053,0.00006710891,0.000050507093,0.00013648423,0.00004313093,0.000110694855,0.000020476864,0.00004681687,0.000006700168],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016777976,0.00011692802,0.0000099329145,0.00028763834,0.00019138983,6.1145165e-8,0.0018331618,0.30435556,0.6624709,0.0022859077,0.021459963,0.0068207723],"study_design_scores_gemma":[0.00071458274,0.000045462493,0.0000021485926,0.000008473965,0.000043944274,4.8640055e-7,0.00008347252,0.90005046,0.0813164,0.0020846124,0.015582184,0.000067750785],"about_ca_topic_score_codex":0.000015567348,"about_ca_topic_score_gemma":0.000001220088,"teacher_disagreement_score":0.64487505,"about_ca_system_score_codex":0.000009197154,"about_ca_system_score_gemma":0.000027930955,"threshold_uncertainty_score":0.27366218},"labels":[],"label_agreement":null},{"id":"W2017298688","doi":"10.1016/j.fluid.2010.12.012","title":"Vapor–liquid and liquid–liquid equilibrium properties of ethane+methanol system at ambient temperature","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Chemistry; Vapor–liquid equilibrium; Methanol; Thermodynamics; Liquid liquid; Atmospheric temperature range; Binary system; Equation of state; Binary number; Analytical Chemistry (journal); Organic chemistry; Chromatography","score_opus":0.023182626127009213,"score_gpt":0.2171463081634576,"score_spread":0.19396368203644837,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2017298688","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9852988,0.0048621744,0.00010617143,0.000027169262,0.0016244192,0.00094278256,0.00025933306,0.0011876571,0.005691504],"genre_scores_gemma":[0.998436,0.00011784833,0.00018763497,0.000044375123,0.0003487791,0.00011592026,0.00008580676,0.0002615301,0.00040212585],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99618155,0.00019815571,0.0011797826,0.0008071312,0.0005692358,0.0010641639],"domain_scores_gemma":[0.99784774,0.000063233456,0.00020205442,0.001182217,0.00017798757,0.0005267658],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00051709346,0.0008564063,0.001088569,0.000355217,0.00010030156,0.000052885025,0.0006602045,0.0005293539,0.00024407925],"category_scores_gemma":[0.000060972696,0.0007923759,0.00029452896,0.00050027174,0.0003654535,0.0007241324,0.0005093467,0.0004340598,0.00008468515],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00530194,0.00023353037,0.000010829887,0.0012194895,0.00033242442,0.0000994931,0.0025202883,0.00007575446,0.9887599,0.0010825095,0.0003176121,0.000046230536],"study_design_scores_gemma":[0.0029919783,0.0025007487,0.0000104852525,0.00059360574,0.00018016141,0.00023896105,0.0002060249,0.021636467,0.969986,0.00002433732,0.0007478411,0.0008833443],"about_ca_topic_score_codex":0.00004842136,"about_ca_topic_score_gemma":0.000010118998,"teacher_disagreement_score":0.021560712,"about_ca_system_score_codex":0.0002665559,"about_ca_system_score_gemma":0.000112853304,"threshold_uncertainty_score":0.9994527},"labels":[],"label_agreement":null},{"id":"W2018439349","doi":"10.1016/j.fluid.2012.11.039","title":"Experimental results and thermodynamic investigation of carbon dioxide solubility in heavy liquid hydrocarbons and corresponding phase properties","year":2012,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":25,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Solubility; Chemistry; Octadecane; Decane; Thermodynamics; Carbon dioxide; Viscosity; Phase (matter); Hydrocarbon; Binary system; Dissolution; Volume (thermodynamics); Analytical Chemistry (journal); Organic chemistry; Binary number","score_opus":0.02291024168438794,"score_gpt":0.258529003119258,"score_spread":0.2356187614348701,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2018439349","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99404895,0.0040124375,0.00007384021,0.000023309449,0.0003608375,0.00046481297,0.000064621236,0.00017400157,0.00077721314],"genre_scores_gemma":[0.9995968,0.000040982006,0.00007647328,0.000011556817,0.00010540547,0.000041358508,0.000048058126,0.00006411104,0.000015264883],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99822104,0.00013812928,0.0006223639,0.0003192276,0.000193794,0.00050545216],"domain_scores_gemma":[0.9992024,0.00010053861,0.000081866565,0.00034796295,0.000013898837,0.0002533547],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00051862415,0.00032733942,0.0004247119,0.00023048485,0.000042163734,0.000024689294,0.00012717443,0.00014235784,0.0000052025334],"category_scores_gemma":[0.00007561529,0.00032639306,0.000049041824,0.00025051812,0.00025700952,0.0005953632,0.00011070729,0.000189283,0.0000010357569],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.001921094,0.00022599577,0.00055929483,0.00008344141,0.000037553702,0.000004764755,0.0044410587,0.00003266659,0.99225205,0.00018741067,0.000004720893,0.00024996515],"study_design_scores_gemma":[0.004404087,0.00038793258,0.0004782991,0.00012587807,0.000023445584,0.000018930443,0.00016392847,0.43737057,0.5566054,0.00013095817,0.000010525891,0.00028006008],"about_ca_topic_score_codex":0.00008315157,"about_ca_topic_score_gemma":0.000010293397,"teacher_disagreement_score":0.4373379,"about_ca_system_score_codex":0.00013108253,"about_ca_system_score_gemma":0.00003895967,"threshold_uncertainty_score":0.9999188},"labels":[],"label_agreement":null},{"id":"W2027025837","doi":"10.1016/j.fluid.2011.09.038","title":"Simulation of the phase behaviour of Athabasca vacuum residue+n-alkane mixtures","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Chemistry; Thermodynamics; Pentane; Alkane; Residue (chemistry); Dodecane; Hydrocarbon; Decane; Group contribution method; Activity coefficient; Phase (matter); Phase equilibrium; Organic chemistry; Aqueous solution","score_opus":0.03065000059159938,"score_gpt":0.3006013348312052,"score_spread":0.2699513342396058,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2027025837","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99204135,0.0005095304,0.00028805804,0.000025830133,0.00007406417,0.000018459652,0.00017641544,0.000052652664,0.006813664],"genre_scores_gemma":[0.99586815,0.0000052379983,0.00018664668,0.000016021464,0.00011848758,0.000005484516,0.000054732216,0.000027215088,0.0037180497],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985538,0.000043587283,0.0005398118,0.00027796958,0.00035048826,0.00023430181],"domain_scores_gemma":[0.99865216,0.000089753725,0.00036051558,0.00067320565,0.00014289867,0.00008146896],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00018127383,0.00019540128,0.00034793364,0.00007827754,0.000075012555,0.0000143169445,0.00045609448,0.0001348668,0.001830048],"category_scores_gemma":[0.0001486923,0.00014843134,0.00028669107,0.00028061224,0.00014140522,0.00015095113,0.00009997527,0.00014805194,0.0000066445427],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028158491,0.0008939613,0.0029593797,0.00012403297,0.00009496223,0.0000050816493,0.00067380903,0.000068732654,0.9928963,0.000031603657,0.00027894383,0.0016916081],"study_design_scores_gemma":[0.0026766728,0.00009173005,0.00026109928,0.0001423828,0.0003371494,0.0000026021903,0.00006486965,0.02515365,0.9705525,0.00021607056,0.0003316976,0.00016957117],"about_ca_topic_score_codex":0.00016318733,"about_ca_topic_score_gemma":0.000005923554,"teacher_disagreement_score":0.025084917,"about_ca_system_score_codex":0.000020832736,"about_ca_system_score_gemma":0.00008718983,"threshold_uncertainty_score":0.9990824},"labels":[],"label_agreement":null},{"id":"W2027096015","doi":"10.1016/j.fluid.2005.12.032","title":"Vapor–liquid equilibrium in the system ethane+ethylene glycol","year":2006,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Chemistry; Ethylene glycol; Equation of state; Thermodynamics; Solubility; Ethylene; Flory–Huggins solution theory; Vapor–liquid equilibrium; Physical chemistry; Organic chemistry; Chromatography; Polymer","score_opus":0.008268147093099755,"score_gpt":0.22873583931341349,"score_spread":0.22046769222031373,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2027096015","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.94972855,0.0011894896,0.0013196875,0.00013645063,0.0014657453,0.00086364243,0.00014558363,0.0010962449,0.04405463],"genre_scores_gemma":[0.99782306,0.000013804775,0.000142746,0.00008755116,0.0011184971,0.00017324544,0.00023598978,0.00016182303,0.00024325808],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99661106,0.00024165284,0.0009424321,0.000534238,0.0005862658,0.0010843716],"domain_scores_gemma":[0.9983343,0.00026106607,0.000091320624,0.0011068385,0.000050308576,0.00015617412],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00078783405,0.00059553573,0.0005965955,0.00028712058,0.00007428113,0.00016212199,0.0009758303,0.00029838012,0.00013954651],"category_scores_gemma":[0.000029556746,0.0005100756,0.00024579465,0.00087842613,0.00012043815,0.0005464363,0.000118205884,0.0004904553,0.00026912277],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003670633,0.0003123662,0.00005414279,0.00026226466,0.000063672596,0.0004432506,0.0004276407,0.0050459607,0.9763102,0.011461869,0.00494612,0.00030545646],"study_design_scores_gemma":[0.008407698,0.00061640964,0.0002518935,0.00027114683,0.00012757334,0.000426333,0.00030834303,0.91235113,0.057554092,0.0020104614,0.016226206,0.0014487297],"about_ca_topic_score_codex":0.00014708261,"about_ca_topic_score_gemma":0.000055553475,"teacher_disagreement_score":0.9187561,"about_ca_system_score_codex":0.00028247066,"about_ca_system_score_gemma":0.0000801016,"threshold_uncertainty_score":0.99973506},"labels":[],"label_agreement":null},{"id":"W2027540813","doi":"10.1016/s0378-3812(01)00636-7","title":"Experimental study of the stability of CO2-hydrate in a porous medium","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":47,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Solubility; Chemistry; Hydrate; Porosity; Clathrate hydrate; Porous medium; Phase (matter); Thermodynamics; Chemical stability; Chemical engineering; Organic chemistry","score_opus":0.0234199218433064,"score_gpt":0.27817752028989,"score_spread":0.25475759844658363,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2027540813","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99380356,0.00014659374,0.0000031502689,0.00004904279,0.0002342232,0.0006544983,0.000009161782,0.000011759205,0.0050880103],"genre_scores_gemma":[0.9997258,0.0000057518946,0.00002428644,0.00002206202,0.00001859277,0.000018230121,0.0000028147722,0.000013004658,0.00016943958],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982661,0.00025223923,0.00053121365,0.00029697825,0.00040048093,0.00025299293],"domain_scores_gemma":[0.9991759,0.000054575325,0.00015710283,0.00052840327,0.0000076129145,0.000076405915],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0004888048,0.00015059393,0.0002793975,0.000030555755,0.000039087096,0.0000060729003,0.00038184843,0.000059438644,0.0045623397],"category_scores_gemma":[0.000031016265,0.000101667436,0.00006097033,0.000509299,0.00023882839,0.0001344591,0.00033203114,0.00013335956,0.000028665547],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002257264,0.0044979197,0.065287516,0.0000058465325,0.000017240167,0.000010853515,0.0061141504,0.00029132454,0.9233279,0.000010838747,0.00011091862,0.00009973574],"study_design_scores_gemma":[0.010494526,0.0030825532,0.044536397,0.000044127577,0.000051909414,0.000016759699,0.0049678218,0.008177776,0.9272396,0.00041666464,0.0005757373,0.0003961334],"about_ca_topic_score_codex":0.001026768,"about_ca_topic_score_gemma":0.00011861396,"teacher_disagreement_score":0.020751119,"about_ca_system_score_codex":0.00008324369,"about_ca_system_score_gemma":0.00001990513,"threshold_uncertainty_score":0.9963476},"labels":[],"label_agreement":null},{"id":"W2030255185","doi":"10.1016/j.fluid.2015.03.035","title":"The UNIFAC model and the partition of alkyl and alkylphenol ethoxylate surfactants in the excess phases of middle phase microemulsions","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Surfactants and Colloidal Systems","field":"Chemistry","cited_by":22,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada; McLean Foundation","keywords":"Chemistry; Alkylphenol; UNIFAC; Microemulsion; Alkyl; Phase (matter); Thermodynamics; Activity coefficient; Organic chemistry; Chromatography; Pulmonary surfactant; Phase equilibrium; Aqueous solution","score_opus":0.06947267802274207,"score_gpt":0.3167720959125901,"score_spread":0.24729941788984802,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2030255185","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99155796,0.005148393,0.000046526606,0.00039231585,0.00009050955,0.00035093876,0.0003240613,0.000018393608,0.0020708784],"genre_scores_gemma":[0.99916923,0.00030274552,0.000029333001,0.0000405426,0.000053399177,0.000037447302,0.000022456967,0.000021029216,0.000323796],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981795,0.00021571168,0.0006485357,0.00026852408,0.0003752408,0.00031246606],"domain_scores_gemma":[0.99815905,0.00078547024,0.00027360333,0.00055562716,0.00011620284,0.000110063855],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012283277,0.00022483592,0.00040080666,0.00003399482,0.00016474855,0.00008391695,0.00039660896,0.00010352505,0.000041659754],"category_scores_gemma":[0.00023564679,0.00011542841,0.00007885099,0.0002135944,0.0005406503,0.00019781991,0.00011905403,0.00017759451,0.000001323304],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0020602895,0.0005561471,0.00042657717,0.00007579079,0.000086868065,0.00000735514,0.0064613367,0.00012933515,0.9847588,0.0010003782,0.00077638746,0.0036607229],"study_design_scores_gemma":[0.07065913,0.0006259825,0.0001256519,0.00080607506,0.00042773865,0.00011266402,0.016723491,0.42596585,0.4625517,0.013562664,0.00753419,0.0009048349],"about_ca_topic_score_codex":0.0003603507,"about_ca_topic_score_gemma":0.00008650038,"teacher_disagreement_score":0.5222071,"about_ca_system_score_codex":0.000020896588,"about_ca_system_score_gemma":0.000102321006,"threshold_uncertainty_score":0.47070342},"labels":[],"label_agreement":null},{"id":"W2033858830","doi":"10.1016/j.fluid.2011.10.006","title":"Erratum to “Modeling the phase behavior of heavy oil and solvent mixtures” [Fluid Phase Equilibria 304 (2011) 74–85]","year":2011,"lang":"en","type":"erratum","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Chemistry; Phase (matter); Solvent; Thermodynamics; Chromatography; Organic chemistry","score_opus":0.03228874241546302,"score_gpt":0.30669965811515437,"score_spread":0.27441091569969134,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2033858830","genre_codex":"empirical","genre_gemma":"other","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.82367295,0.06275446,0.0010122209,0.0012371162,0.012864759,0.00027721314,0.0055312994,0.0008803389,0.09176962],"genre_scores_gemma":[0.2661905,0.0034495424,0.0008189821,0.0007738929,0.010389585,0.00081593596,0.007892422,0.0010498007,0.70861936],"study_design_codex":"bench_or_experimental","study_design_gemma":"not_applicable","domain_scores_codex":[0.9912754,0.00022399372,0.0025526355,0.0024420447,0.0015771927,0.001928727],"domain_scores_gemma":[0.99380064,0.00014950607,0.001099492,0.0031654637,0.00056536694,0.0012195022],"candidate_categories":["metaepi_narrow","research_integrity","insufficient_payload"],"consensus_categories":["metaepi_narrow","research_integrity"],"category_scores_codex":[0.0010714487,0.0019525981,0.0026748956,0.0005306654,0.00060605165,0.00051067997,0.0023855234,0.001625614,0.004139136],"category_scores_gemma":[0.00032772683,0.0016433329,0.0012403415,0.00061766803,0.00066655566,0.00056222244,0.0010199056,0.0023517387,0.00016764329],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0013686591,0.0029000985,0.0000032307578,0.0009340851,0.0005972159,0.00014538904,0.00067075633,0.0000079353595,0.62545294,0.000023465453,0.34934753,0.018548712],"study_design_scores_gemma":[0.026585488,0.0020718698,7.1621724e-7,0.003979375,0.008640575,0.00029471432,0.000523042,0.13396634,0.15497069,0.00047791153,0.6636025,0.0048868037],"about_ca_topic_score_codex":0.00042396184,"about_ca_topic_score_gemma":0.000039882514,"teacher_disagreement_score":0.6168497,"about_ca_system_score_codex":0.00023707635,"about_ca_system_score_gemma":0.0012600652,"threshold_uncertainty_score":0.9999499},"labels":[],"label_agreement":null},{"id":"W2036565647","doi":"10.1016/j.fluid.2008.03.018","title":"A similarity variable for estimating the heat capacity of solid organic compounds","year":2008,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical Thermodynamics and Molecular Structure","field":"Chemistry","cited_by":30,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Shell Canada","keywords":"Chemistry; Heat capacity; Thermodynamics; Asphaltene; Enthalpy of fusion; Enthalpy; Hydrocarbon mixtures; Phase (matter); Similarity (geometry); Hydrocarbon; Organic chemistry; Melting point; Physics","score_opus":0.024161530695928267,"score_gpt":0.27421478830457485,"score_spread":0.2500532576086466,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2036565647","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9707523,0.00008082863,0.026119703,0.0000794538,0.00014268848,0.00014601191,0.00046890954,0.000059405917,0.002150698],"genre_scores_gemma":[0.98539793,0.0000028992993,0.013893536,0.00010209992,0.00026225465,0.000018084957,0.00013364063,0.000039993258,0.00014952719],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988741,0.000016651684,0.0003347851,0.0002746425,0.00019110704,0.00030867473],"domain_scores_gemma":[0.9990147,0.00016826013,0.000084569154,0.0005362489,0.00010459849,0.00009163195],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012817953,0.00019696898,0.0003180181,0.000015032523,0.00019094587,0.00001597548,0.00035797132,0.00014800779,0.00046623842],"category_scores_gemma":[0.00022050785,0.0001565652,0.00015775133,0.0001305017,0.00017483729,0.00005401511,0.00011887411,0.00020624354,0.0000015901678],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008173235,0.00011129723,0.00001811074,0.00013300999,0.00007295562,0.0000031021468,0.00020176715,0.00009092774,0.99755543,0.000573341,0.0010960079,0.00006228557],"study_design_scores_gemma":[0.0015243742,0.000035137462,0.0000035874823,0.0000347836,0.000048592432,0.000068484245,0.0000085601205,0.3544949,0.63653415,0.0057796747,0.0012971648,0.0001705631],"about_ca_topic_score_codex":0.00003334232,"about_ca_topic_score_gemma":0.0000017581858,"teacher_disagreement_score":0.36102128,"about_ca_system_score_codex":0.00005244975,"about_ca_system_score_gemma":0.000096883385,"threshold_uncertainty_score":0.6384544},"labels":[],"label_agreement":null},{"id":"W2038839325","doi":"10.1016/j.fluid.2013.08.035","title":"Characterization of reservoir fluids using an EOS based on perturbation from n-alkanes","year":2013,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":28,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"van der Waals force; Chemistry; Thermodynamics; Perturbation (astronomy); Combining rules; Complex fluid; Equation of state; Statistical physics; Molecule; Physics; Mathematics; Organic chemistry","score_opus":0.02190670265569243,"score_gpt":0.2518006419278381,"score_spread":0.22989393927214563,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2038839325","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9786231,0.000040393494,0.018973913,0.00003391699,0.0005917032,0.00043156787,0.00028439876,0.0003455163,0.00067547517],"genre_scores_gemma":[0.9970276,0.000006623026,0.000808398,0.00006531816,0.00037956444,0.000029137705,0.0015282524,0.00009923934,0.000055868808],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99851024,0.000093798386,0.0004707778,0.00030953716,0.00029750288,0.00031815158],"domain_scores_gemma":[0.9989479,0.00008578954,0.00007954962,0.00062019506,0.00009974018,0.00016681018],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.000114053255,0.0002934651,0.0003239712,0.0002000177,0.000053350137,0.000082268794,0.00026933645,0.00016807718,0.0010510766],"category_scores_gemma":[0.000038408703,0.00030208216,0.000092567105,0.0002724249,0.00004840663,0.0010176684,0.00002893362,0.00012799297,0.00008121879],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008444987,0.00022676458,0.00009026586,0.000039151022,0.000033795037,0.000003036237,0.00020918605,0.0065709925,0.99160093,0.0001643637,0.00005133778,0.00092575344],"study_design_scores_gemma":[0.0011663886,0.00017236188,0.0005258427,0.00006907911,0.000026253396,0.0000010324028,0.000009919538,0.7747236,0.22225232,0.00068913057,0.000121531695,0.00024252142],"about_ca_topic_score_codex":0.00009489643,"about_ca_topic_score_gemma":0.0000030708272,"teacher_disagreement_score":0.76934856,"about_ca_system_score_codex":0.00008822173,"about_ca_system_score_gemma":0.000046928337,"threshold_uncertainty_score":0.99994314},"labels":[],"label_agreement":null},{"id":"W2040705600","doi":"10.1016/s0378-3812(01)00647-1","title":"Solubility of propane in aqueous alkanolamine solutions","year":2002,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Analytical Chemistry and Chromatography","field":"Chemistry","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Alkanolamine; Diethanolamine; Chemistry; Solubility; Aqueous solution; Propane; Amine gas treating; Inorganic chemistry; Organic chemistry","score_opus":0.03784296220204031,"score_gpt":0.2605312158097029,"score_spread":0.2226882536076626,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2040705600","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95450145,0.0011374471,0.00006452239,0.00012623295,0.00003127861,0.000064331514,0.00007795263,0.00009208136,0.043904718],"genre_scores_gemma":[0.9978936,0.0000363748,0.00010516598,0.000017587705,0.00010970906,0.000016685884,0.000051513744,0.000018289624,0.0017511009],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.998455,0.00001876603,0.0005192976,0.00034896677,0.00022536714,0.00043258604],"domain_scores_gemma":[0.9990951,0.00007882423,0.00008746849,0.0005473822,0.00004911114,0.00014210938],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00011866702,0.0001947126,0.00033384038,0.000057286146,0.00004751,0.000013124851,0.0002640789,0.00016099917,0.009902858],"category_scores_gemma":[0.00013637308,0.00019557572,0.00017915189,0.00036032978,0.00024713477,0.00011582722,0.00009533002,0.00021032112,0.000051199986],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000055729524,0.001408912,0.0010502978,0.00025898818,0.000038893613,0.00003458874,0.00010685646,0.0000031688248,0.9936114,0.0002837953,0.0019215922,0.0012257836],"study_design_scores_gemma":[0.003395321,0.00009801931,0.00010918783,0.00013145142,0.000069230104,0.000041938554,0.00006770834,0.055296507,0.9351155,0.0012392979,0.0040264335,0.00040936744],"about_ca_topic_score_codex":0.000028434066,"about_ca_topic_score_gemma":0.0000055961523,"teacher_disagreement_score":0.058495853,"about_ca_system_score_codex":0.000042574,"about_ca_system_score_gemma":0.00002501762,"threshold_uncertainty_score":0.9910022},"labels":[],"label_agreement":null},{"id":"W2043510180","doi":"10.1016/j.fluid.2006.05.010","title":"Prediction of methane and carbon dioxide solubility in water in the presence of hydrate","year":2006,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":71,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University; University of Ottawa","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Solubility; Methane; Hydrate; Clathrate hydrate; Carbon dioxide; Thermodynamics; van der Waals force; Mass transfer; Hydrocarbon; Work (physics); Water vapor; Organic chemistry; Chromatography","score_opus":0.014792836708574241,"score_gpt":0.23287160282535913,"score_spread":0.2180787661167849,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2043510180","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99450237,0.00020533458,0.000012782222,0.00008268546,0.0000640125,0.00029699304,0.000011056004,0.0000063615234,0.0048184013],"genre_scores_gemma":[0.9997247,0.000022078919,0.00007109327,0.000009067538,0.000017868697,0.00001252868,0.000013183046,0.0000063171465,0.00012316337],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986568,0.00024718716,0.00042010317,0.0002321435,0.00022357654,0.00022017087],"domain_scores_gemma":[0.99955314,0.00009141481,0.00006383179,0.00025896152,0.0000045427655,0.000028078408],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0010041995,0.0001037214,0.00019572597,0.0000475175,0.000009543063,0.0000045228867,0.0001607283,0.00006757554,0.00017330964],"category_scores_gemma":[0.00002559331,0.00006245614,0.000028721232,0.00023807131,0.00022014987,0.00013193664,0.00010813644,0.00011779877,0.0000032012554],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009036271,0.00022651261,0.03870213,0.000020973659,0.000003694459,0.000004679332,0.001071072,0.0008310501,0.95880914,0.00003711712,0.000024317977,0.00017892527],"study_design_scores_gemma":[0.0026398594,0.0003403547,0.07489321,0.000053584896,0.000027053617,0.00000772615,0.0001340502,0.05177749,0.8625295,0.007187308,0.00025021526,0.00015963902],"about_ca_topic_score_codex":0.0032155812,"about_ca_topic_score_gemma":0.00015721965,"teacher_disagreement_score":0.09627965,"about_ca_system_score_codex":0.00002745674,"about_ca_system_score_gemma":0.0000057925517,"threshold_uncertainty_score":0.48610184},"labels":[],"label_agreement":null},{"id":"W2045725063","doi":"10.1016/j.fluid.2005.05.004","title":"Solubility of dimethyldisulfide (DMDS) in aqueous solutions of Fe(III) complexes of trans-1,2-cyclohexanediaminetetraacetic acid (CDTA) using the static headspace method","year":2005,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Catalysis and Hydrodesulfurization Studies","field":"Engineering","cited_by":23,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Aqueous solution; Solubility; Inorganic chemistry; Ferrous; Kraft process; Ferric; Sulfur; Chelation; Data scrubbing; Kraft paper; Organic chemistry; Chemical engineering","score_opus":0.04004587153872678,"score_gpt":0.3222535110808927,"score_spread":0.2822076395421659,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2045725063","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8160842,0.004329869,0.17859395,0.00014378142,0.00009115832,0.00031995066,0.00021394335,0.000046104105,0.00017703704],"genre_scores_gemma":[0.9888321,0.00012747523,0.010881931,0.000011211264,0.00004958426,0.0000134875645,0.00002922158,0.000033657438,0.000021334039],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99788636,0.00019773307,0.0010164597,0.00023641289,0.00031393932,0.0003490865],"domain_scores_gemma":[0.998625,0.0005364861,0.00016084031,0.00050530984,0.00011012182,0.00006228633],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008584767,0.00023692362,0.00076858554,0.0002271158,0.00005948662,0.000010979453,0.0002391294,0.000071199705,0.00010859051],"category_scores_gemma":[0.00012757805,0.00020819507,0.00020194311,0.00072788383,0.0002570085,0.00017350273,0.00006440741,0.00014052507,0.0000010823503],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005486221,0.00024222536,0.00008253885,0.00021227701,0.00014815816,7.7303827e-7,0.0028614115,0.06689468,0.92683846,0.00018047391,0.00015303874,0.0023310732],"study_design_scores_gemma":[0.0014886352,0.000067379755,0.00031546716,0.000071207214,0.00016718113,0.0000045442825,0.00030279983,0.607952,0.38895527,0.00021726039,0.00027615944,0.00018208582],"about_ca_topic_score_codex":0.00024751926,"about_ca_topic_score_gemma":0.00033142735,"teacher_disagreement_score":0.54105735,"about_ca_system_score_codex":0.00007077186,"about_ca_system_score_gemma":0.000052021827,"threshold_uncertainty_score":0.8489948},"labels":[],"label_agreement":null},{"id":"W2046927453","doi":"10.1016/j.fluid.2010.01.022","title":"Micelle formation of alkylimidazolium ionic liquids in water and in ethylammonium nitrate ionic liquid: A calorimetric study","year":2010,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":47,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Chemistry; Ionic liquid; Isothermal titration calorimetry; Aqueous solution; Enthalpy; Thermodynamics; C4mim; Micelle; Dilution; Calorimetry; Critical micelle concentration; Physical chemistry; Organic chemistry; Catalysis","score_opus":0.015750063557923553,"score_gpt":0.2648264665254207,"score_spread":0.24907640296749714,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2046927453","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99808574,0.00023624998,0.000121886915,0.000106654654,0.00021818298,0.00041410828,0.000011455523,0.0000629323,0.00074282003],"genre_scores_gemma":[0.9995069,0.000017133267,0.00007352472,0.000020851416,0.00013642138,0.000058947357,0.000046201167,0.000029782668,0.00011023295],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99829555,0.00005378744,0.0006555281,0.00031700102,0.00020400419,0.00047415573],"domain_scores_gemma":[0.99929297,0.0001365335,0.000049365924,0.00033778822,0.00005142455,0.00013191276],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002962839,0.00022858015,0.00037264382,0.00024438978,0.000041353436,0.000020946185,0.0002341455,0.00017396807,0.00013839138],"category_scores_gemma":[0.00012595618,0.00018302149,0.00007511793,0.0005324144,0.000105493935,0.00028874874,0.0002193635,0.0006521454,0.000032272415],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005588709,0.0010707179,0.00009370402,0.00008865394,0.000012054408,0.000006592723,0.0012602203,0.00027954322,0.99629104,0.00014164014,0.000040501036,0.00015646617],"study_design_scores_gemma":[0.0029551503,0.00039092143,0.00005701217,0.000044361648,0.000021083006,0.000005436897,0.00008312759,0.11685697,0.878767,0.00039227362,0.00016420793,0.0002624279],"about_ca_topic_score_codex":0.00035224526,"about_ca_topic_score_gemma":0.00012498928,"teacher_disagreement_score":0.117524005,"about_ca_system_score_codex":0.00007197011,"about_ca_system_score_gemma":0.000031130265,"threshold_uncertainty_score":0.74634},"labels":[],"label_agreement":null},{"id":"W2053190710","doi":"10.1016/j.fluid.2012.09.006","title":"Thermodynamics and fluid characterization using trajectory optimization","year":2012,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Process Optimization and Integration","field":"Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Virtual Materials Group (Canada); University of Calgary","funders":"National Institute of Standards and Technology; Virtual Materials Group; Shell","keywords":"Chemistry; Distillation; Non-random two-liquid model; Equation of state; Thermodynamics; Gasoline; Azeotrope; Boiling point; Boiling; Activity coefficient; Chromatography; Organic chemistry","score_opus":0.018148893842116664,"score_gpt":0.25325748751498856,"score_spread":0.2351085936728719,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2053190710","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.4958523,0.00025976467,0.50233805,0.000007805698,0.00035682024,0.000115811075,0.000021510405,0.00021956024,0.000828416],"genre_scores_gemma":[0.9914397,0.00020262953,0.0073604695,0.00006097148,0.0002843769,0.000011838511,0.0005198452,0.000058348927,0.00006181697],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99928635,0.000026581136,0.00022723706,0.00012230601,0.000106718835,0.0002308091],"domain_scores_gemma":[0.9996635,0.000012318902,0.00003656863,0.00012892525,0.000048898983,0.0001097934],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010789698,0.00016262992,0.00013256076,0.000111058325,0.00006568353,0.000064630265,0.00006115732,0.00010008977,0.00023946557],"category_scores_gemma":[0.00002285305,0.00016965618,0.000026387714,0.0001916876,0.000025026091,0.0012021543,0.0000150650385,0.00007033172,0.0000091658885],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000018330984,0.000054741813,0.0001099205,0.000039344766,0.000019018513,2.3693812e-7,0.00051948393,0.120789535,0.87564266,0.00041858296,0.00006306507,0.002325067],"study_design_scores_gemma":[0.0004896007,0.00002152995,0.00015548023,0.000018245406,0.000021533064,0.000008307624,0.000020078327,0.98853344,0.010076216,0.000009548485,0.0004573613,0.00018867101],"about_ca_topic_score_codex":0.000001608624,"about_ca_topic_score_gemma":3.0063993e-7,"teacher_disagreement_score":0.8677439,"about_ca_system_score_codex":0.000064428175,"about_ca_system_score_gemma":0.000016563801,"threshold_uncertainty_score":0.69183785},"labels":[],"label_agreement":null},{"id":"W2057622687","doi":"10.1016/j.fluid.2005.06.004","title":"Thermodynamic equilibrium of the O2–ZnSO4–H2SO4–H2O system from 25 to 250°C","year":2005,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":23,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Toronto","funders":"","keywords":"Chemistry; Solubility; Ternary operation; Thermodynamics; Activity coefficient; Ternary numeral system; Equilibrium constant; Electrolyte; Phase equilibrium; Solubility equilibrium; Phase (matter); Aqueous solution; Physical chemistry; Organic chemistry","score_opus":0.013780046071312254,"score_gpt":0.2465689132995874,"score_spread":0.23278886722827516,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2057622687","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9822192,0.00042184864,0.0029391916,0.0008632377,0.00055972143,0.0004145729,0.00042396592,0.000352014,0.011806202],"genre_scores_gemma":[0.9961382,0.0000020082794,0.0006732754,0.00022222525,0.0011478675,0.000048141854,0.000049532457,0.00007463048,0.0016441287],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9977784,0.00007037395,0.0006558086,0.0004842378,0.00043390394,0.0005772632],"domain_scores_gemma":[0.9982018,0.0002344281,0.00010461229,0.0010880176,0.000084756044,0.00028640844],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000108913846,0.00035149252,0.00048630973,0.000043245327,0.00007353175,0.000032574335,0.0009898279,0.00017483423,0.0006196553],"category_scores_gemma":[0.00016682026,0.0002522132,0.0003624601,0.00041489018,0.00015462555,0.00017308374,0.000587257,0.00036594074,0.0004876735],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012833138,0.00025271098,0.000009058761,0.00007231952,0.00007855857,0.0000014820278,0.00035555428,0.0010497441,0.9894013,0.0038027784,0.0032529952,0.0015951743],"study_design_scores_gemma":[0.001180815,0.00007393709,0.000022365724,0.00025360115,0.00007719338,0.000005310945,0.000034175555,0.46444255,0.51629096,0.00048657923,0.016744526,0.00038797955],"about_ca_topic_score_codex":0.00020503157,"about_ca_topic_score_gemma":0.0000066644275,"teacher_disagreement_score":0.47311032,"about_ca_system_score_codex":0.00027029036,"about_ca_system_score_gemma":0.00005564547,"threshold_uncertainty_score":0.999993},"labels":[],"label_agreement":null},{"id":"W2057966166","doi":"10.1016/s0378-3812(02)00054-7","title":"Liquid–liquid equilibria of copolymer mixtures based on an equation of state","year":2002,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China; Health Sciences Centre Foundation","keywords":"Chemistry; Thermodynamics; Copolymer; Equation of state; Liquid liquid; Liquid state; Chromatography; Organic chemistry; Physical chemistry; Polymer","score_opus":0.02182717964755076,"score_gpt":0.25424149522822814,"score_spread":0.23241431558067738,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2057966166","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9823385,0.00070332194,0.0074011306,0.000043628945,0.00077401113,0.00045052264,0.00049053744,0.00042802113,0.007370342],"genre_scores_gemma":[0.9987094,0.00004437283,0.0003943727,0.00007757461,0.00020806187,0.00002736807,0.00023307852,0.00016457877,0.00014120809],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.997058,0.00018082595,0.0010275933,0.00047052192,0.0006237547,0.0006393493],"domain_scores_gemma":[0.99803615,0.00023361345,0.00021910117,0.0010842107,0.000121816425,0.00030512697],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0003512161,0.00052052457,0.00071547006,0.00042284848,0.000047702917,0.000033618173,0.00054283725,0.00022300005,0.0015795606],"category_scores_gemma":[0.000085184976,0.0005429987,0.000256969,0.0005593761,0.0001944513,0.0006175836,0.00006147501,0.00024099268,0.00006627556],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0015196699,0.0007336171,0.000010630088,0.00018128265,0.000109903194,0.000015029095,0.00046870683,0.013767971,0.9802837,0.0009193837,0.0007421676,0.0012479498],"study_design_scores_gemma":[0.002218431,0.0020177802,0.0000066089187,0.00008580867,0.000043726122,0.0000023348287,0.000007578898,0.5671824,0.42766458,0.00017977171,0.00027627553,0.00031465833],"about_ca_topic_score_codex":0.000022105718,"about_ca_topic_score_gemma":0.000004092492,"teacher_disagreement_score":0.55341446,"about_ca_system_score_codex":0.00008367066,"about_ca_system_score_gemma":0.000056721594,"threshold_uncertainty_score":0.99970216},"labels":[],"label_agreement":null},{"id":"W2060074034","doi":"10.1016/j.fluid.2012.07.016","title":"Vapour–liquid and vapour–liquid–liquid equilibrium modeling for binary, ternary, and quaternary systems of solvents","year":2012,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Ternary operation; Liquid liquid; Binary number; Quaternary; Thermodynamics; Ternary numeral system; Chromatography; Organic chemistry","score_opus":0.025056807064722516,"score_gpt":0.2706490835050628,"score_spread":0.24559227644034026,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2060074034","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9662461,0.011764893,0.016956907,0.000053040407,0.0023751052,0.0011350036,0.00047769703,0.00046210678,0.00052909856],"genre_scores_gemma":[0.99737567,0.00026399703,0.00053033745,0.0000319806,0.001051154,0.00014899776,0.00019173988,0.0002797844,0.00012634245],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9962816,0.00011922713,0.0011760504,0.00063244475,0.0004354911,0.0013551483],"domain_scores_gemma":[0.9980224,0.00020944237,0.00019661794,0.00075648574,0.0001187713,0.0006962824],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007408509,0.0007781987,0.00103346,0.00036240343,0.00011732395,0.000094635536,0.00046929528,0.00037075244,0.000038261776],"category_scores_gemma":[0.000059612168,0.00081135065,0.00024017258,0.00023946178,0.00017044641,0.0013540824,0.0003726553,0.00028267977,0.000014493916],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0032448363,0.0003467128,0.00021267502,0.0010719321,0.0003845261,0.000021391998,0.0007899483,0.006127687,0.98643297,0.00086339,0.0003193383,0.00018460579],"study_design_scores_gemma":[0.004596711,0.0022617066,0.000018162375,0.000345455,0.0002236928,0.00017550681,0.00011492761,0.9538506,0.03668755,0.00015453972,0.00069229427,0.0008788241],"about_ca_topic_score_codex":0.000084837935,"about_ca_topic_score_gemma":0.000001716821,"teacher_disagreement_score":0.9497454,"about_ca_system_score_codex":0.00011684315,"about_ca_system_score_gemma":0.000065596956,"threshold_uncertainty_score":0.99943376},"labels":[],"label_agreement":null},{"id":"W2063599414","doi":"10.1016/s0378-3812(03)00026-8","title":"Effect of salt and volume ratio on the reverse micellar extraction of lysozyme using DODMAC","year":2003,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Surfactants and Colloidal Systems","field":"Chemistry","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Aqueous solution; Extraction (chemistry); Pulmonary surfactant; Chromatography; Aqueous two-phase system; Surface-area-to-volume ratio; Lysozyme; Phase (matter); Micellar liquid chromatography; Micelle; Micellar solutions; Volume (thermodynamics); Chemical engineering; Organic chemistry","score_opus":0.016887390231460162,"score_gpt":0.28663784811596615,"score_spread":0.26975045788450597,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2063599414","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9943515,0.00039360646,0.00003729112,0.000014630698,0.00019696231,0.00017088251,0.000034902052,0.000017249762,0.0047829747],"genre_scores_gemma":[0.9986594,0.000012724244,0.000029518094,0.000011682685,0.00007654739,0.000005294211,0.000005297119,0.000020164383,0.0011794086],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99891967,0.00016702573,0.00033715265,0.00019884875,0.00021751902,0.00015981667],"domain_scores_gemma":[0.9990297,0.00033979458,0.00020274735,0.00033233687,0.000040756906,0.000054650125],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0005231116,0.00015508384,0.00027956825,0.000029866693,0.000062268926,0.000021828888,0.00009160455,0.00009655474,0.0010525072],"category_scores_gemma":[0.00018956566,0.00011147661,0.000087517576,0.00012060479,0.000062386905,0.00009335817,0.000017223143,0.00009932247,0.00000895513],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030284267,0.00007224004,0.0008153461,0.00017368677,0.000046812216,0.0000038902717,0.00009092371,0.000014956244,0.9974579,0.00014632288,0.00059218606,0.00028289395],"study_design_scores_gemma":[0.0013562994,0.00020445124,0.000014264216,0.00012778252,0.00007182176,0.000018587243,0.000060765826,0.0067302845,0.9857613,0.000016218422,0.0055244872,0.00011373495],"about_ca_topic_score_codex":0.00009142941,"about_ca_topic_score_gemma":0.0000015587618,"teacher_disagreement_score":0.011696597,"about_ca_system_score_codex":0.000035650002,"about_ca_system_score_gemma":0.00004089485,"threshold_uncertainty_score":0.99986064},"labels":[],"label_agreement":null},{"id":"W2067830054","doi":"10.1016/s0378-3812(99)00319-2","title":"Application of the MSA to the modeling of the activity coefficients of individual ions","year":2000,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":14,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Ion; Electrolyte; Activity coefficient; Counterion; Aqueous solution; BATES; Thermodynamics; Physical chemistry; Organic chemistry","score_opus":0.02123402924068827,"score_gpt":0.2646091760390936,"score_spread":0.24337514679840536,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2067830054","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98471373,0.00004727565,0.012818414,0.00041121253,0.00007451191,0.000321793,0.00023135488,0.000019307601,0.0013623813],"genre_scores_gemma":[0.9995918,0.0000017061006,0.00006229381,0.000049774844,0.00007671051,0.000023075316,0.000006595639,0.00001196486,0.0001760305],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99905425,0.00004182792,0.00027785831,0.00014520994,0.000318305,0.0001625246],"domain_scores_gemma":[0.9991119,0.00010581746,0.00006411314,0.00061850494,0.000055266002,0.000044400957],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00011337073,0.00010221779,0.00016412839,0.00001094862,0.00008252187,0.0000048943357,0.0007311705,0.000055064767,0.0000980775],"category_scores_gemma":[0.00011104509,0.000052608077,0.00016389875,0.0003965376,0.00015010544,0.000037601974,0.0002533548,0.00017846297,0.000009033961],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004972338,0.0003023159,0.000008436279,0.000025055753,0.000024988552,1.00152455e-8,0.0004136817,0.10120096,0.89255077,0.000717841,0.0003418071,0.004364439],"study_design_scores_gemma":[0.0002214074,0.000016955662,0.000021741582,0.00003640639,0.000031898995,3.7784466e-7,0.000007948618,0.6239227,0.37449002,0.0003011158,0.00089759263,0.000051794974],"about_ca_topic_score_codex":0.00008424946,"about_ca_topic_score_gemma":0.0000020863704,"teacher_disagreement_score":0.52272177,"about_ca_system_score_codex":0.000023751018,"about_ca_system_score_gemma":0.000029346209,"threshold_uncertainty_score":0.2145295},"labels":[],"label_agreement":null},{"id":"W2069791171","doi":"10.1016/s0378-3812(00)00359-9","title":"Excess enthalpies of cyclohexane+n-hexane+(n-octane or n-dodecane) ternary mixture at 298.15 K","year":2000,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Cyclohexane; Ternary operation; Hexane; Octane; Enthalpy; Dodecane; Thermodynamics; Alkane; Physical chemistry; Organic chemistry; Hydrocarbon","score_opus":0.013647823083218467,"score_gpt":0.2589277773276937,"score_spread":0.2452799542444752,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2069791171","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98450184,0.0041248486,0.00015588835,0.00022112994,0.00040411268,0.00034527283,0.00029906724,0.0004499502,0.009497911],"genre_scores_gemma":[0.95822436,0.00015397737,0.00045719574,0.00015956217,0.0005169898,0.000037617956,0.00019903103,0.0001505006,0.040100776],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9970802,0.00007993809,0.00079583674,0.00066077657,0.0005957594,0.00078750914],"domain_scores_gemma":[0.99820745,0.0002070019,0.00014710282,0.0010587239,0.000073059644,0.00030665562],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00017442917,0.00057699444,0.00074483256,0.00012445048,0.000091057416,0.000039201805,0.0010393515,0.00032742476,0.023171717],"category_scores_gemma":[0.000117535266,0.00046201423,0.00025731095,0.0002780223,0.00022892901,0.00035868093,0.00030115593,0.00036342136,0.0002589877],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0024319636,0.0003349737,0.000044971926,0.00022727347,0.00019270353,0.00023980002,0.0007120199,0.00040050663,0.9772639,0.00005584268,0.008745824,0.009350198],"study_design_scores_gemma":[0.008474001,0.00083043566,0.00014548091,0.00064931426,0.00024470946,0.00069682696,0.00009321073,0.123549476,0.7607065,0.00038852703,0.10243586,0.0017856548],"about_ca_topic_score_codex":0.00012867087,"about_ca_topic_score_gemma":0.0000233053,"teacher_disagreement_score":0.21655741,"about_ca_system_score_codex":0.00018906697,"about_ca_system_score_gemma":0.00007199244,"threshold_uncertainty_score":0.99978316},"labels":[],"label_agreement":null},{"id":"W2070105039","doi":"10.1016/j.fluid.2014.12.045","title":"Phase equilibria, solubility and modeling study of CO 2 /CH 4 + tetra- n -butylammonium bromide aqueous semi-clathrate systems","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":34,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Natural Sciences and Engineering Research Council of Canada; McGill University","keywords":"Clathrate hydrate; Chemistry; Solubility; Methane; Fugacity; Thermodynamics; van der Waals force; Phase (matter); Hydrate; Bromide; Physical chemistry; Inorganic chemistry; Organic chemistry; Molecule","score_opus":0.05376296163383279,"score_gpt":0.31528694999960694,"score_spread":0.2615239883657742,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2070105039","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99132645,0.0015834477,0.0010168168,0.000032294418,0.0007110592,0.0014553991,0.00008631546,0.00013470642,0.0036534863],"genre_scores_gemma":[0.99863404,0.000037798323,0.00021792801,0.00002312572,0.00015431723,0.00004752312,0.000044447184,0.0000689571,0.0007718617],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9956931,0.0005090317,0.0011743936,0.0010086375,0.000835354,0.000779514],"domain_scores_gemma":[0.9978177,0.00013633519,0.0002977759,0.0009662868,0.000056426332,0.0007254925],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00175918,0.00050237396,0.00083583733,0.00010809955,0.00015811155,0.00012460748,0.000504201,0.00024055704,0.0003548475],"category_scores_gemma":[0.00012086083,0.00044069652,0.00010904021,0.00046375065,0.00028487548,0.00061634515,0.000490944,0.00038072857,0.00014695557],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0013795914,0.005941661,0.0026502847,0.00010971059,0.00021596844,0.00011157165,0.0054114563,0.027562082,0.95343566,0.000063263884,0.0016674747,0.0014513034],"study_design_scores_gemma":[0.013864843,0.0032609364,0.0000233394,0.00005450045,0.00015513987,0.000053284093,0.001163817,0.97146845,0.008098248,0.0006864152,0.0005976652,0.00057336234],"about_ca_topic_score_codex":0.0019658457,"about_ca_topic_score_gemma":0.00002984064,"teacher_disagreement_score":0.94533736,"about_ca_system_score_codex":0.00021061087,"about_ca_system_score_gemma":0.00007992371,"threshold_uncertainty_score":0.9998045},"labels":[],"label_agreement":null},{"id":"W2070496125","doi":"10.1016/j.fluid.2011.02.025","title":"Prediction of methane and carbon dioxide solubilities for the CH4+CO2+H2O system under hydrate–liquid–vapor equilibrium","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Chemistry; Methane; Carbon dioxide; Hydrate; Clathrate hydrate; Thermodynamics; Environmental chemistry; Organic chemistry","score_opus":0.0410461019644895,"score_gpt":0.24196147356705808,"score_spread":0.2009153716025686,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2070496125","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9840596,0.0012963548,0.00087639905,0.00009480684,0.0007779268,0.0010327516,0.00012547363,0.00011071228,0.0116260145],"genre_scores_gemma":[0.9976509,0.00005486976,0.00045210967,0.000042755142,0.00015756558,0.00012392754,0.00004708855,0.00005089173,0.0014198585],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99782753,0.0001671817,0.0006364018,0.00051693525,0.00034358032,0.00050837145],"domain_scores_gemma":[0.99867636,0.00027752478,0.00023614739,0.00059447455,0.000027643358,0.00018785388],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00096757687,0.00030419207,0.00041389297,0.000059259797,0.00008492941,0.000020813404,0.00034285692,0.00017654542,0.0005550473],"category_scores_gemma":[0.00005326841,0.00020965392,0.00014043873,0.00024494441,0.0004986772,0.00028277253,0.00028308743,0.00015818764,0.000014687297],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00094583235,0.00017885207,0.0003650208,0.00017504189,0.00018756752,0.0000036555562,0.0024473912,0.00022069483,0.9928537,0.0019369982,0.00038106967,0.00030418258],"study_design_scores_gemma":[0.007364972,0.0041753016,0.0010176826,0.00023204862,0.00092129584,0.00009826475,0.0046554995,0.15490028,0.81633276,0.0052195895,0.0041505327,0.0009317528],"about_ca_topic_score_codex":0.00054691744,"about_ca_topic_score_gemma":0.000012039874,"teacher_disagreement_score":0.17652091,"about_ca_system_score_codex":0.00008639458,"about_ca_system_score_gemma":0.00003209244,"threshold_uncertainty_score":0.8549439},"labels":[],"label_agreement":null},{"id":"W2072623962","doi":"10.1016/j.fluid.2011.02.003","title":"On the compatibility between vapor pressure data and the critical constants: Use of the van der Waals family of cubic equations of state to study the cases of 2-methoxyethanol and 2-ethoxyethanol","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Razi University","keywords":"Acentric factor; Chemistry; van der Waals force; Thermodynamics; Cubic function; Vapor pressure; Equation of state; Physical chemistry; Crystallography; Organic chemistry; Molecule; Physics; Mathematical analysis","score_opus":0.15913873739120943,"score_gpt":0.3408803154320085,"score_spread":0.18174157804079905,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2072623962","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9886814,0.0006807438,0.0044000847,0.00010445926,0.00014490285,0.0017981584,0.004010192,0.000025997622,0.00015407335],"genre_scores_gemma":[0.9995318,0.00002486943,0.00029741443,0.000036266643,0.000024444767,0.000028730225,0.0000137224915,0.00003548983,0.0000072404778],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99698424,0.0011111302,0.00089543575,0.0003290142,0.00041508445,0.00026511055],"domain_scores_gemma":[0.9892276,0.008257113,0.00020331702,0.002042357,0.0001825691,0.000087052096],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00190108,0.0002710326,0.0006537337,0.000067217836,0.00010085147,0.0000246121,0.0009067426,0.00007214835,0.00004744378],"category_scores_gemma":[0.0025267715,0.00013454803,0.00009118222,0.00034496587,0.0012647419,0.00023965427,0.00060246576,0.00024132611,6.04429e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0019943065,0.002170631,0.009137099,0.000642573,0.0035029019,0.000010528762,0.035268247,0.00068005937,0.9135235,0.02747868,0.00044484937,0.0051466525],"study_design_scores_gemma":[0.01312931,0.0026132895,0.04554849,0.0007417844,0.004859614,0.000023617564,0.003283583,0.5832795,0.31184736,0.03342801,0.00019802897,0.0010474065],"about_ca_topic_score_codex":0.00024760808,"about_ca_topic_score_gemma":0.000039274804,"teacher_disagreement_score":0.6016761,"about_ca_system_score_codex":0.000009115001,"about_ca_system_score_gemma":0.00006708876,"threshold_uncertainty_score":0.54867095},"labels":[],"label_agreement":null},{"id":"W2073687523","doi":"10.1016/s0378-3812(01)00396-x","title":"Vapor–liquid equilibrium in the system ethanethiol+tetraethylene glycol","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Chemistry; Ethanethiol; Thermodynamics; Vapor–liquid equilibrium; Phase equilibrium; Organic chemistry; Chromatography","score_opus":0.015319101536649088,"score_gpt":0.25388831288171254,"score_spread":0.23856921134506345,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073687523","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.954081,0.0013724603,0.0014568184,0.0002007036,0.00179996,0.00091078936,0.00008781221,0.0011566706,0.038933806],"genre_scores_gemma":[0.9980541,0.00009505885,0.000120711025,0.00018678964,0.0008663694,0.00016329736,0.0001433344,0.00016891462,0.00020146482],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9963368,0.00030994145,0.0009335169,0.00058381114,0.00062950636,0.0012064237],"domain_scores_gemma":[0.9979723,0.0003620774,0.00008804569,0.0012585168,0.000056035697,0.00026299787],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0010344654,0.0006349691,0.0006433581,0.00032219812,0.00009384714,0.00015710971,0.0011755704,0.0003625698,0.00024398566],"category_scores_gemma":[0.00006512909,0.00054153125,0.00025265836,0.001143782,0.00012799611,0.00062019785,0.00012752863,0.0006903557,0.0003496594],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00075227773,0.00033419824,0.00008147431,0.0002597804,0.0001297486,0.0010926988,0.0015049533,0.0030692387,0.98397136,0.0050208564,0.0024507286,0.0013327162],"study_design_scores_gemma":[0.008589673,0.0009098924,0.0001975899,0.00033679404,0.00013211265,0.0011211785,0.00067241583,0.9334087,0.023421055,0.00097162696,0.028713722,0.0015252453],"about_ca_topic_score_codex":0.000052050415,"about_ca_topic_score_gemma":0.000033866345,"teacher_disagreement_score":0.96055025,"about_ca_system_score_codex":0.0002831335,"about_ca_system_score_gemma":0.000089931724,"threshold_uncertainty_score":0.99970365},"labels":[],"label_agreement":null},{"id":"W2073771216","doi":"10.1016/j.fluid.2006.05.007","title":"Volumetric behavior of water–methanol mixtures in the vicinity of the critical region","year":2006,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":13,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"National Institute of Standards and Technology; University of Guelph","keywords":"Chemistry; Methanol; Thermodynamics; Organic chemistry","score_opus":0.013411721375102258,"score_gpt":0.25862123141308946,"score_spread":0.2452095100379872,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073771216","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9955106,0.0004675884,0.0007744704,0.00008773899,0.00050122425,0.00035088052,0.0000507721,0.00006130794,0.002195457],"genre_scores_gemma":[0.999642,0.000007917927,0.00006382628,0.00002073923,0.00013791569,0.000028431177,0.00002197766,0.00003510431,0.000042062566],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9984582,0.00017073145,0.00052792154,0.00017237484,0.00031617534,0.00035461635],"domain_scores_gemma":[0.9990202,0.00024221363,0.0000419791,0.0006090217,0.000049960447,0.000036635058],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00032241238,0.0001995646,0.00030481291,0.00017989798,0.000036583424,0.000018937186,0.00055397686,0.00012998424,0.00004844073],"category_scores_gemma":[0.000092939175,0.0001177716,0.00017209369,0.0006309486,0.00019831318,0.00015627354,0.000074853124,0.00023140412,0.000005496775],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047968162,0.00045049263,0.0015616262,0.000095550065,0.00001531606,0.00002221432,0.00033309456,0.00022880806,0.9938752,0.002218763,0.0005727943,0.0005781555],"study_design_scores_gemma":[0.0027606185,0.0002463947,0.011129036,0.000121416466,0.0002006535,0.000078645746,0.000062012616,0.10010397,0.876421,0.0077040847,0.0007622228,0.00040996593],"about_ca_topic_score_codex":0.00013415432,"about_ca_topic_score_gemma":0.000021566328,"teacher_disagreement_score":0.11745423,"about_ca_system_score_codex":0.00003804672,"about_ca_system_score_gemma":0.000022885792,"threshold_uncertainty_score":0.4802586},"labels":[],"label_agreement":null},{"id":"W2075444888","doi":"10.1016/j.fluid.2012.11.017","title":"Salt effects on the diffusion of caffeine in aqueous solutions","year":2012,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Diffusion Coefficients in Liquids","field":"Chemistry","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"St. Francis Xavier University","funders":"","keywords":"Chemistry; Caffeine; Diffusion; Salt (chemistry); Taylor dispersion; Aqueous solution; Salting out; Ternary operation; Inorganic chemistry; Analytical Chemistry (journal); Chromatography; Thermodynamics; Physical chemistry","score_opus":0.021655179329871987,"score_gpt":0.2840738092448432,"score_spread":0.2624186299149712,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2075444888","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98128134,0.0005858799,0.000103055114,0.0003246985,0.00064963027,0.00020297938,0.0000433171,0.000086966545,0.016722133],"genre_scores_gemma":[0.99785686,0.0000150331725,0.00006367647,0.00017470185,0.00045652277,0.000045496672,0.00003733161,0.000039290895,0.001311092],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9982468,0.00009968027,0.00039639082,0.00024680147,0.0004134632,0.0005968729],"domain_scores_gemma":[0.9981263,0.0008071918,0.00010724448,0.00077376957,0.000037296188,0.00014814717],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00043125518,0.00022622039,0.0002701536,0.000107402026,0.00010114648,0.000016977912,0.00041214313,0.00014067876,0.0020853414],"category_scores_gemma":[0.00061574345,0.00016546508,0.00011195529,0.00030934816,0.0001202132,0.000110892324,0.00029865067,0.00024685118,0.00015233271],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015881927,0.0017064086,0.0003882934,0.00008410287,0.000015520378,0.0000058851742,0.00055357255,0.000008802687,0.98091835,0.0040810346,0.007042375,0.0050368174],"study_design_scores_gemma":[0.0047075264,0.00031925284,0.00054505037,0.0004891887,0.00005472576,0.000014800449,0.000093933144,0.012189641,0.95722646,0.00042065466,0.023512607,0.00042616847],"about_ca_topic_score_codex":0.00003823015,"about_ca_topic_score_gemma":0.0000034235745,"teacher_disagreement_score":0.023691917,"about_ca_system_score_codex":0.00009510673,"about_ca_system_score_gemma":0.000051442817,"threshold_uncertainty_score":0.99882686},"labels":[],"label_agreement":null},{"id":"W2075560584","doi":"10.1016/j.fluid.2008.12.003","title":"Accurate thermodynamic and dielectric equations of state for high-temperature simulated water","year":2008,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":35,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Trent University","funders":"","keywords":"Chemistry; Dielectric; Thermodynamics; Critical point (mathematics); Range (aeronautics); Atmospheric temperature range; Water model; Thermodynamic state; Bar (unit); Material properties; Molecular dynamics; Computational chemistry; Materials science; Physics","score_opus":0.01248565757522797,"score_gpt":0.24007128883330894,"score_spread":0.22758563125808098,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2075560584","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9895961,0.0003767648,0.008239184,0.000034176992,0.00032854103,0.0005739338,0.00042887373,0.00026502745,0.00015735671],"genre_scores_gemma":[0.99873734,0.00012253711,0.00015984579,0.000020738142,0.000090411035,0.000029082708,0.0005021488,0.00009777248,0.00024012783],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99859923,0.000038281963,0.00044531818,0.00027741597,0.00015219027,0.00048758852],"domain_scores_gemma":[0.9992153,0.00018507818,0.000045623325,0.00033481902,0.00009233073,0.0001268527],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00012124891,0.00030513018,0.00039492964,0.00018068068,0.000109440974,0.000028985374,0.00018078297,0.00013812308,0.00006548752],"category_scores_gemma":[0.000036251222,0.00025323647,0.00009504239,0.0002546033,0.00008879692,0.00034346443,0.00004285285,0.00015196668,0.000011229368],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017748306,0.00008816278,0.000005938913,0.00008089372,0.00015569033,0.000011860347,0.00048461673,0.010969802,0.9867889,0.00078773475,0.00011514335,0.00033374946],"study_design_scores_gemma":[0.002916895,0.00020783917,0.00005271484,0.000019744917,0.0000462401,0.000013839068,0.0000041063777,0.78810406,0.20516284,0.003074513,0.000104653904,0.00029255764],"about_ca_topic_score_codex":0.000011159189,"about_ca_topic_score_gemma":0.0000037867906,"teacher_disagreement_score":0.7816261,"about_ca_system_score_codex":0.0000452776,"about_ca_system_score_gemma":0.000039772673,"threshold_uncertainty_score":0.999992},"labels":[],"label_agreement":null},{"id":"W2078912827","doi":"10.1016/s0378-3812(01)00600-8","title":"On the mean spherical approximation for the Lennard–Jones fluid","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":33,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa; Honeywell (Canada)","funders":"","keywords":"Chemistry; Work (physics); Lennard-Jones potential; Phase (matter); Statistical physics; Phase equilibrium; Thermodynamics; Physics; Computational chemistry; Molecular dynamics","score_opus":0.02452646739691206,"score_gpt":0.2600568196753957,"score_spread":0.23553035227848362,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2078912827","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.86978287,0.0005082647,0.11964252,0.0013156051,0.001229812,0.0010830197,0.00007757766,0.00056909793,0.005791255],"genre_scores_gemma":[0.99763113,0.000077473414,0.0003343981,0.00036069175,0.00071565097,0.00024046688,0.00008736545,0.00011249064,0.00044035923],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9984633,0.00006745832,0.00036684278,0.00028792684,0.00029368425,0.0005208245],"domain_scores_gemma":[0.99824685,0.0008275248,0.00004663024,0.0007393948,0.000047220405,0.00009239505],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004100479,0.00032821146,0.00025710787,0.000045980367,0.00022647368,0.00012528269,0.0005404421,0.00011571785,0.0003995936],"category_scores_gemma":[0.000087339664,0.0002032918,0.00021449826,0.0002752434,0.000105303596,0.0002438602,0.00005391801,0.00020629377,0.00015335019],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0007680647,0.00035229154,0.000012186078,0.00008065658,0.00037746472,0.000016214794,0.0012006982,0.009379158,0.8435713,0.09754312,0.032919828,0.013779035],"study_design_scores_gemma":[0.001499784,0.00018542023,0.000012767754,0.000023977567,0.00006132329,0.00002213969,0.000087036125,0.9401804,0.0077454504,0.00887091,0.041024983,0.0002858147],"about_ca_topic_score_codex":0.0000058403034,"about_ca_topic_score_gemma":0.00000648229,"teacher_disagreement_score":0.9308012,"about_ca_system_score_codex":0.00007977635,"about_ca_system_score_gemma":0.000027653825,"threshold_uncertainty_score":0.82899994},"labels":[],"label_agreement":null},{"id":"W2079713564","doi":"10.1016/j.fluid.2013.02.002","title":"Predictive correlations for liquid heat capacity – including the critical region","year":2013,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Alberta Innovates; ConocoPhillips","keywords":"Isobaric process; Chemistry; Heat capacity; Thermodynamics; Work (physics); Correlation; Physics; Mathematics","score_opus":0.03905405323936331,"score_gpt":0.2834522835644839,"score_spread":0.24439823032512056,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2079713564","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.80742925,0.00023957984,0.18458986,0.00069258315,0.0013618148,0.0009313468,0.00012800659,0.00054799434,0.004079557],"genre_scores_gemma":[0.9980032,0.000015310385,0.000498691,0.00011546994,0.0006962916,0.0004002021,0.00007642815,0.00008203686,0.00011240169],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9985603,0.00006510555,0.00037313037,0.0002800993,0.00018670011,0.0005346493],"domain_scores_gemma":[0.99847305,0.0007138106,0.00002220607,0.0004712374,0.00012396522,0.00019575024],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017407561,0.00027361672,0.00025650082,0.00008314047,0.00027415282,0.0001076539,0.0003037535,0.00015837149,0.00015245337],"category_scores_gemma":[0.00028939318,0.0002266657,0.00016345333,0.00022242231,0.0001935084,0.000734761,0.000079077065,0.00025721372,0.00009896282],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00037233686,0.00029365954,0.00006404691,0.0001564586,0.0002719638,0.000008978673,0.002073953,0.006122846,0.90656775,0.045345284,0.037805364,0.00091735576],"study_design_scores_gemma":[0.0011553474,0.0003360554,0.000043552936,0.000050623206,0.00007094235,0.000035004745,0.000056149544,0.9770876,0.005644905,0.010700647,0.0045386767,0.00028046814],"about_ca_topic_score_codex":0.00002604963,"about_ca_topic_score_gemma":0.0000039155802,"teacher_disagreement_score":0.9709648,"about_ca_system_score_codex":0.00013193257,"about_ca_system_score_gemma":0.00003649389,"threshold_uncertainty_score":0.92431587},"labels":[],"label_agreement":null},{"id":"W2079754015","doi":"10.1016/j.fluid.2005.07.022","title":"Heat capacity prediction for polynuclear aromatic solids using vibration spectra","year":2005,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":26,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Syncrude","keywords":"Chemistry; Heat capacity; Asphaltene; Spectral line; Raman spectroscopy; Thermodynamics; Density functional theory; Infrared spectroscopy; Infrared; Computational chemistry; Organic chemistry; Optics","score_opus":0.025030826614556818,"score_gpt":0.2573458540656983,"score_spread":0.2323150274511415,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2079754015","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.881099,0.0001224908,0.11498415,0.00007138398,0.0009267854,0.0005285442,0.00022131065,0.0007664097,0.0012799428],"genre_scores_gemma":[0.98900557,0.000011750035,0.009037483,0.000065854554,0.0015247266,0.000029796034,0.00015746901,0.00012241013,0.000044942506],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99849313,0.000034260203,0.00047160173,0.00029077902,0.00020618246,0.0005040203],"domain_scores_gemma":[0.9993375,0.000056501267,0.000026334073,0.0003778758,0.00002592026,0.00017588242],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00018286625,0.00029989658,0.00030353,0.00014917068,0.00012480927,0.00010055912,0.00017475671,0.00015922113,0.00016651717],"category_scores_gemma":[0.00002847429,0.0003355645,0.00015974799,0.00020352153,0.000050087972,0.0009331984,0.000024639703,0.00014739817,0.00005232202],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007341235,0.000113832844,0.000009055093,0.00006934501,0.00008165371,0.0000015759921,0.00030655865,0.015386545,0.9814833,0.0005547114,0.00086577056,0.0010542718],"study_design_scores_gemma":[0.0019319371,0.0001471753,0.000030341258,0.00004230247,0.00007490022,0.000032274373,0.00001295012,0.90604806,0.088094965,0.0012454817,0.0020549977,0.00028461986],"about_ca_topic_score_codex":0.000008564525,"about_ca_topic_score_gemma":0.000006215557,"teacher_disagreement_score":0.89338833,"about_ca_system_score_codex":0.0002691924,"about_ca_system_score_gemma":0.000037757865,"threshold_uncertainty_score":0.99990964},"labels":[],"label_agreement":null},{"id":"W2082153986","doi":"10.1016/s0378-3812(01)00559-3","title":"Excess enthalpies of the ternary mixtures: 2-methyltetrahydrofuran + n-hexane + (n-decane or n-dodecane) at 298.15 K","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermodynamic properties of mixtures","field":"Chemical Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Chemistry; Decane; Dodecane; Ternary operation; Hexane; Alkane; Thermodynamics; Hydrocarbon; Organic chemistry; Physical chemistry","score_opus":0.01963869787127748,"score_gpt":0.26886832164779645,"score_spread":0.24922962377651897,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2082153986","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9886911,0.0043318407,0.00043658927,0.0005525629,0.0009360108,0.0004147887,0.0001513007,0.00028645815,0.0041993787],"genre_scores_gemma":[0.9824355,0.00012330197,0.0001899744,0.00024929916,0.00047391249,0.000038124934,0.000055065328,0.0001288368,0.016305981],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971251,0.0001277705,0.00075099466,0.00057031953,0.00067899947,0.000746823],"domain_scores_gemma":[0.9977938,0.00032960836,0.00021418165,0.0013219506,0.00010504663,0.0002354127],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00025199263,0.00052044744,0.0006220689,0.0001191022,0.00013697114,0.000038027443,0.0015250822,0.00025473195,0.0028194627],"category_scores_gemma":[0.00042231873,0.00033617608,0.00032439225,0.0004337983,0.00032019496,0.0002704933,0.00066876184,0.00040335156,0.00008044838],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0013087055,0.000263762,0.00018044958,0.00014297465,0.00017784163,0.00010283209,0.000750333,0.000243105,0.9888891,0.000105951585,0.0051159197,0.0027190547],"study_design_scores_gemma":[0.0047012037,0.00029981372,0.00017962007,0.00037966648,0.00014512968,0.00039152385,0.00010029021,0.05918817,0.9059217,0.00038180046,0.027503036,0.0008080273],"about_ca_topic_score_codex":0.00019645174,"about_ca_topic_score_gemma":0.00006484293,"teacher_disagreement_score":0.08296735,"about_ca_system_score_codex":0.00022157273,"about_ca_system_score_gemma":0.000091653535,"threshold_uncertainty_score":0.99990904},"labels":[],"label_agreement":null},{"id":"W2084231145","doi":"10.1016/j.fluid.2008.02.012","title":"The effect of biological and polymeric inhibitors on methane gas hydrate growth kinetics","year":2008,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":76,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Saudi Aramco; Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Chemistry; Hydrate; Methane; Clathrate hydrate; Kinetics; Kinetic energy; Polymer; Chemical engineering; Thermodynamics; Organic chemistry","score_opus":0.01286746350392015,"score_gpt":0.2417468104612967,"score_spread":0.22887934695737655,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2084231145","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99345636,0.00087240705,0.000011751387,0.00017257968,0.00023533698,0.00025681406,0.0000072611415,0.000022528397,0.0049649295],"genre_scores_gemma":[0.99891067,0.0005317577,0.000053075357,0.000043637447,0.00007402844,0.0000100320785,0.000008567495,0.00001555587,0.00035270027],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99852675,0.00030219785,0.0003031855,0.0003014904,0.0002412408,0.0003251046],"domain_scores_gemma":[0.9990187,0.00046681278,0.00010650343,0.00025062164,0.0000044582957,0.00015287829],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00037418937,0.00020758953,0.00026006633,0.000030202726,0.00013432416,0.000011254288,0.00019640403,0.000100209225,0.00050102937],"category_scores_gemma":[0.000114718925,0.000110947556,0.00007741694,0.00029830335,0.0006811872,0.00006144735,0.00016754732,0.00015295412,0.00014788633],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003981928,0.00009304715,0.0037434609,0.0000056843305,0.000028045004,0.000021243672,0.00014354703,0.00003148774,0.9910806,0.000053041615,0.0008204384,0.0035812375],"study_design_scores_gemma":[0.0024870916,0.0064246715,0.0019087519,0.00002045181,0.000037841786,0.000059939473,0.000009693617,0.0025240995,0.9827793,0.0004946358,0.0029782825,0.00027521193],"about_ca_topic_score_codex":0.000039860173,"about_ca_topic_score_gemma":6.572541e-7,"teacher_disagreement_score":0.008301245,"about_ca_system_score_codex":0.000023625016,"about_ca_system_score_gemma":0.000004591092,"threshold_uncertainty_score":0.54859203},"labels":[],"label_agreement":null},{"id":"W2084432098","doi":"10.1016/s0378-3812(01)00531-3","title":"Predicting solubility in supercritical solvents using estimated virial coefficients and fluctuation theory","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":21,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Virial coefficient; Chemistry; Thermodynamics; Supercritical fluid; Solubility; Virial theorem; Virial expansion; Monte Carlo method; Statistical physics; Equation of state; Supercritical carbon dioxide; Naphthalene; Physical chemistry; Physics; Organic chemistry; Quantum mechanics; Statistics; Mathematics","score_opus":0.029137221454450368,"score_gpt":0.3008340506116949,"score_spread":0.2716968291572445,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2084432098","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9734193,0.0002406152,0.024140853,0.000009691006,0.0008129453,0.00035062668,0.000055302848,0.0003653459,0.0006052926],"genre_scores_gemma":[0.9992134,0.000020397936,0.0003709449,0.000017874434,0.0002073594,0.000010673567,0.00008829286,0.00006346471,0.0000075776734],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99820065,0.00013160391,0.0004977362,0.00036635294,0.0002435321,0.000560115],"domain_scores_gemma":[0.9992913,0.00018391802,0.0000142963445,0.0002885325,0.000038079284,0.00018389504],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00057954516,0.0002745287,0.00031499777,0.000169044,0.00008588426,0.000079387944,0.00015624595,0.0001666527,0.00013664029],"category_scores_gemma":[0.00024420378,0.00030585402,0.000057742585,0.00033310652,0.00012731379,0.0005174838,0.00009151896,0.00022227786,0.0000127678695],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003743989,0.0002805395,0.006998882,0.00006055195,0.000041210526,0.00005900269,0.00047756563,0.0067808256,0.98126805,0.000844122,0.000012786774,0.0028020677],"study_design_scores_gemma":[0.0033550088,0.0000729693,0.0014064317,0.00010426266,0.000039555518,0.00005427186,0.00003621116,0.98600763,0.0056195883,0.0030015877,0.000022977129,0.00027950868],"about_ca_topic_score_codex":0.000029046076,"about_ca_topic_score_gemma":0.00001278107,"teacher_disagreement_score":0.9792268,"about_ca_system_score_codex":0.00015961725,"about_ca_system_score_gemma":0.000042087275,"threshold_uncertainty_score":0.9999394},"labels":[],"label_agreement":null},{"id":"W2086759676","doi":"10.1016/j.fluid.2014.10.009","title":"On the use of departure function correlations for hydrocarbon isobaric liquid phase heat capacity calculation","year":2014,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Alberta Innovates; Shell Canada; ConocoPhillips","keywords":"Heat capacity; Isobaric process; Chemistry; Thermodynamics; Equation of state; Hydrocarbon mixtures; Hydrocarbon; Constant (computer programming); Ideal gas; Range (aeronautics); Physics; Organic chemistry","score_opus":0.03763820807980211,"score_gpt":0.2512642726255024,"score_spread":0.21362606454570027,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2086759676","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.77165323,0.00004529456,0.22563107,0.00009448421,0.0008390665,0.00060404977,0.00020646963,0.0002382376,0.0006880795],"genre_scores_gemma":[0.9986769,0.0000054875877,0.0002314958,0.00015657718,0.00031199845,0.00009003907,0.00038383502,0.00007601557,0.000067666326],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9985864,0.000101907666,0.00045643927,0.00027618586,0.0002365439,0.00034248445],"domain_scores_gemma":[0.99842536,0.00074213877,0.000069773465,0.0005627769,0.00007950623,0.000120423094],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0002553832,0.00029429793,0.00030574162,0.00013468768,0.00013062195,0.000050658873,0.00016642881,0.00018792752,0.00007036349],"category_scores_gemma":[0.00026613224,0.00024618182,0.00020077145,0.0003064551,0.00007215669,0.0004060699,0.000023829314,0.00020682489,0.000021514352],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0012226128,0.0003773574,0.000012755035,0.00006735884,0.00015532623,6.3903695e-7,0.00023163356,0.067057334,0.89047754,0.033452127,0.0060922056,0.0008530996],"study_design_scores_gemma":[0.0029044447,0.0010226221,0.000023899409,0.000045858535,0.00013137357,0.000003815699,0.0000027515664,0.9672776,0.014530605,0.0029169712,0.010890796,0.00024930472],"about_ca_topic_score_codex":0.000013089599,"about_ca_topic_score_gemma":0.000011566176,"teacher_disagreement_score":0.9002202,"about_ca_system_score_codex":0.00008488672,"about_ca_system_score_gemma":0.00002433799,"threshold_uncertainty_score":0.99999905},"labels":[],"label_agreement":null},{"id":"W2088551265","doi":"10.1016/j.fluid.2004.06.026","title":"Large scale data regression for process calculations—theory and description of the virtual database","year":2004,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"National Institute of Standards and Technology; Virtual Materials Group","keywords":"Database; Consistency (knowledge bases); Process (computing); Data mining; Documentation; Component (thermodynamics); Quality (philosophy); Computer science; Chemistry; Thermodynamics; Artificial intelligence","score_opus":0.02719661546210317,"score_gpt":0.2998715098407914,"score_spread":0.27267489437868825,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2088551265","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9249209,0.00039991643,0.07139098,0.00003128424,0.0004359285,0.0004665088,0.0020898962,0.00011793219,0.00014661162],"genre_scores_gemma":[0.99821746,0.000019315898,0.0005775504,0.00002363071,0.00013636917,0.000024903218,0.00088541635,0.000047989528,0.000067349785],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9989332,0.000050345883,0.00029903505,0.00028311895,0.00017499791,0.00025932095],"domain_scores_gemma":[0.9988704,0.000085057734,0.000058854806,0.0008528313,0.00004625118,0.00008662129],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00048023454,0.00018132656,0.00019790349,0.000062425876,0.00010847149,0.00003140401,0.00041888782,0.00008471992,0.000026637763],"category_scores_gemma":[0.00012227085,0.00013996434,0.000050274444,0.00020082704,0.000088913715,0.0007574804,0.00019638766,0.00010547851,0.0000026432488],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00031992822,0.00023338059,0.00008223211,0.00021867128,0.000057586927,0.0000017181095,0.0010501808,0.0012542211,0.98017764,0.015159547,0.00041259892,0.0010323096],"study_design_scores_gemma":[0.0067458935,0.00012468068,0.00017219495,0.0003747161,0.00014363982,0.00002187567,0.00026147216,0.91409796,0.060289726,0.016019806,0.0013994814,0.00034857524],"about_ca_topic_score_codex":0.0000030390681,"about_ca_topic_score_gemma":0.000016655948,"teacher_disagreement_score":0.9198879,"about_ca_system_score_codex":0.00003705401,"about_ca_system_score_gemma":0.0000638472,"threshold_uncertainty_score":0.570758},"labels":[],"label_agreement":null},{"id":"W2094716371","doi":"10.1016/j.fluid.2006.01.007","title":"Representation of carboxylic acid-containing systems by association model-incorporated equations of state","year":2006,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Equation of state; Carboxylic acid; Thermodynamics; Acetic acid; Monomer; Binary number; Hydrocarbon; Representation (politics); Dimer; Organic chemistry; Polymer; Mathematics","score_opus":0.01268371666192718,"score_gpt":0.2440879330204649,"score_spread":0.2314042163585377,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2094716371","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8749234,0.0004833766,0.11951362,0.000010718197,0.00033425904,0.00032139194,0.0006386614,0.00022431776,0.0035502221],"genre_scores_gemma":[0.99840325,0.000015212737,0.00025838832,0.000002942951,0.00007381725,0.000031682346,0.00084843143,0.00006089238,0.0003053559],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9981628,0.00009055291,0.0008498424,0.00021749202,0.00037212123,0.00030717018],"domain_scores_gemma":[0.99889076,0.00015456103,0.00036054596,0.00033589528,0.00019055913,0.00006769471],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00029525402,0.00021346757,0.0004595895,0.00017018357,0.00003315965,0.000033665077,0.0001656102,0.00013092147,0.000018410929],"category_scores_gemma":[0.00007296317,0.00024749746,0.00010729779,0.0005755872,0.0000313688,0.0004245901,0.000028116689,0.000110680776,0.000005897234],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047187812,0.00008258781,0.000228615,0.000057733225,0.00009449155,0.0000013345639,0.00013144754,0.25813156,0.7385493,0.0016063577,0.0009373552,0.00013204485],"study_design_scores_gemma":[0.0014323577,0.000070484086,0.00001988584,0.000038907685,0.000055537683,8.1893904e-7,0.000022112046,0.81123066,0.18526927,0.001657228,0.00003233858,0.0001704264],"about_ca_topic_score_codex":0.00029357732,"about_ca_topic_score_gemma":0.000020380554,"teacher_disagreement_score":0.55328,"about_ca_system_score_codex":0.00023314268,"about_ca_system_score_gemma":0.00006894321,"threshold_uncertainty_score":0.99999774},"labels":[],"label_agreement":null},{"id":"W2102848540","doi":"10.1016/s0378-3812(01)00787-7","title":"The impact of liquid–liquid–vapour phase behaviour on coke formation from model coke precursors","year":2002,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Thermochemical Biomass Conversion Processes","field":"Engineering","cited_by":23,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta; University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Coke; Anthracene; Alkane; Pyrene; Organic chemistry; Catalysis; Hexadecane; Chemical engineering","score_opus":0.02472284902676108,"score_gpt":0.2799381050907989,"score_spread":0.25521525606403783,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2102848540","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.995368,0.0008477342,0.00084828486,0.00007374429,0.00022010622,0.00034489075,0.00072391226,0.00036053263,0.0012127745],"genre_scores_gemma":[0.9991699,0.00013573778,0.00013320698,0.000023394668,0.00010372918,0.00003595375,0.0001570733,0.00006919566,0.00017185106],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983111,0.00004530599,0.0005659805,0.00026782768,0.0003583836,0.0004514115],"domain_scores_gemma":[0.99875444,0.00021654018,0.00012995033,0.0005798324,0.000101126054,0.00021810809],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00014139444,0.0003540733,0.00033029047,0.000105060906,0.00009559168,0.00005830732,0.0004943735,0.00018609263,0.00095942133],"category_scores_gemma":[0.000104999184,0.00027446783,0.0002465033,0.00025810348,0.00009030329,0.0005027354,0.00006807258,0.00021813087,0.00017854753],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010637303,0.00039252389,0.000003913362,0.000029671466,0.00009472271,0.000004638838,0.00066897937,0.0018821132,0.9789924,0.000048883318,0.015584996,0.0012333978],"study_design_scores_gemma":[0.00242834,0.0007905466,0.000002257381,0.000049990882,0.00004056809,0.0000027408942,0.000031807354,0.3591881,0.637016,0.00009018706,0.00013960696,0.00021987209],"about_ca_topic_score_codex":0.000024156234,"about_ca_topic_score_gemma":0.0000015295652,"teacher_disagreement_score":0.357306,"about_ca_system_score_codex":0.0001602467,"about_ca_system_score_gemma":0.000030926683,"threshold_uncertainty_score":0.99997073},"labels":[],"label_agreement":null},{"id":"W2102953387","doi":"10.1016/j.fluid.2007.06.020","title":"Molecular-level computer simulation of a vapor-compression refrigeration cycle","year":2007,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"National Research Council Canada; Grantová Agentura České Republiky; Ministerstvo Školství, Mládeže a Tělovýchovy","keywords":"Refrigerant; Equation of state; Chemistry; Refrigeration; Working fluid; Monte Carlo method; Vapor-compression refrigeration; Thermodynamics; Molecular dynamics; Statistical physics; Process (computing); Thermodynamic cycle; Compression (physics); Process engineering; Computer science; Computational chemistry; Gas compressor; Engineering; Statistics","score_opus":0.0179196675771666,"score_gpt":0.28779251904274256,"score_spread":0.26987285146557594,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2102953387","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.589369,0.00008427406,0.40824455,0.0000046866708,0.00042234026,0.00015261436,0.000045686324,0.00018768187,0.0014891424],"genre_scores_gemma":[0.9966866,0.0000037911893,0.0027090467,0.000027213026,0.0002527227,0.0000039374304,0.00023601195,0.000060576724,0.000020143154],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99859077,0.000034629982,0.000536976,0.00022712842,0.0002736668,0.0003368259],"domain_scores_gemma":[0.9992341,0.00010947655,0.00007721751,0.00037509127,0.000073944626,0.00013016122],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00027740016,0.00022566931,0.00026639085,0.00016895226,0.00003933695,0.000028851739,0.00017074769,0.0001438969,0.00007773131],"category_scores_gemma":[0.000016896869,0.00023800078,0.00010912347,0.00026035088,0.00003759916,0.00034071712,0.000048960013,0.00012671831,0.000021164515],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010006459,0.00009915183,0.000015592854,0.000039899605,0.000037453898,0.000018327979,0.00015549248,0.26454157,0.7240737,0.000702455,0.000092727445,0.010123542],"study_design_scores_gemma":[0.0014968156,0.00009191009,0.00021756791,0.000047761,0.0000197475,0.0000051536394,0.000003704923,0.8330031,0.1635815,0.0009524773,0.0003741697,0.00020606986],"about_ca_topic_score_codex":0.000007920417,"about_ca_topic_score_gemma":0.0000033407036,"teacher_disagreement_score":0.56846154,"about_ca_system_score_codex":0.00006571977,"about_ca_system_score_gemma":0.000020867135,"threshold_uncertainty_score":0.970539},"labels":[],"label_agreement":null},{"id":"W2104538585","doi":"10.1016/j.fluid.2014.02.031","title":"Thermodynamic analysis and correlation of solubility of disodium 5′-guanylate heptahydrate in aqueous ethanol mixtures","year":2014,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Crystallization and Solubility Studies","field":"Materials Science","cited_by":33,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"CNIB; Hebei University of Science and Technology","keywords":"Chemistry; Enthalpy; Solubility; Dissolution; Gibbs free energy; Solvent; Thermodynamics; Aqueous solution; Ethanol; Endothermic process; Physical chemistry; Organic chemistry","score_opus":0.01038084413420544,"score_gpt":0.27368615004383234,"score_spread":0.2633053059096269,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2104538585","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.980124,0.00026184783,0.018732453,0.00006905243,0.00013229175,0.0002162937,0.00005790354,0.000032007083,0.0003741319],"genre_scores_gemma":[0.9995773,0.00002602956,0.00024083068,0.000017122744,0.000016181903,0.000007743435,0.000032251108,0.000009274246,0.00007325639],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9983975,0.00028171018,0.0005873007,0.0003323186,0.00021169145,0.00018946924],"domain_scores_gemma":[0.99905056,0.00021956245,0.00021612374,0.0003657219,0.000096659096,0.00005139295],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00079219777,0.00014562042,0.0004927209,0.0001921442,0.00004395812,0.000020184301,0.00013574483,0.00008234773,0.00031373443],"category_scores_gemma":[0.0003058575,0.00012989414,0.00009941698,0.0004965022,0.00026681714,0.00015347602,0.00010352161,0.000059041096,0.0000034777695],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015426449,0.00019612143,0.016672216,0.000077874225,0.00004594358,5.2972547e-7,0.0015242291,0.00052936655,0.9796289,0.00031217653,0.000010900843,0.00084746897],"study_design_scores_gemma":[0.001900221,0.00025718153,0.059190176,0.000039119295,0.00024049613,0.0000010558928,0.00010001351,0.738306,0.19656183,0.003097221,0.00004842151,0.00025831145],"about_ca_topic_score_codex":0.00031038286,"about_ca_topic_score_gemma":0.00038915747,"teacher_disagreement_score":0.7830671,"about_ca_system_score_codex":0.000023949175,"about_ca_system_score_gemma":0.000025745014,"threshold_uncertainty_score":0.52969295},"labels":[],"label_agreement":null},{"id":"W2114751226","doi":"10.1016/s0378-3812(00)00469-6","title":"Mean activity coefficients in the NaCl–NH4HCO3–H2O system at 293.15–308.15 K","year":2001,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"Government of Jiangsu Province; National Natural Science Foundation of China; Alexander von Humboldt-Stiftung","keywords":"Chemistry; Molality; Activity coefficient; Thermodynamics; Ion; Physical chemistry; Aqueous solution","score_opus":0.026459797595464598,"score_gpt":0.27108323963492753,"score_spread":0.24462344203946293,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2114751226","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9767468,0.00039411391,0.0018409301,0.000399193,0.00037883193,0.00034774057,0.00007481634,0.00030770298,0.019509872],"genre_scores_gemma":[0.99759036,0.00000828117,0.000029870114,0.00018771745,0.00050677324,0.000045310768,0.000059680075,0.00003885236,0.0015331331],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9978645,0.00011614947,0.000399014,0.00047214507,0.00046389745,0.00068430713],"domain_scores_gemma":[0.9986976,0.00028490668,0.00006508524,0.0007089547,0.00004520659,0.0001982452],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024695217,0.00032682563,0.00038022114,0.000050925657,0.00017918946,0.000052446052,0.00064882264,0.00016232303,0.00037954215],"category_scores_gemma":[0.00012931213,0.00023680004,0.00020419298,0.00054374116,0.00012977581,0.00016525379,0.0002449793,0.00047542248,0.00048358095],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028478584,0.00079312804,0.000029123124,0.0000775314,0.00002748901,0.00004227514,0.00061422325,0.00033780612,0.98839694,0.0024860243,0.005700824,0.0012098654],"study_design_scores_gemma":[0.0044540036,0.00027760275,0.00005850624,0.0003432635,0.00008664633,0.00012838501,0.00016953124,0.64217055,0.3010055,0.0004330288,0.049879838,0.0009931192],"about_ca_topic_score_codex":0.00010658064,"about_ca_topic_score_gemma":0.000012725309,"teacher_disagreement_score":0.6873914,"about_ca_system_score_codex":0.000403463,"about_ca_system_score_gemma":0.000026601625,"threshold_uncertainty_score":0.9656426},"labels":[],"label_agreement":null},{"id":"W2123934148","doi":"10.1016/j.fluid.2010.01.009","title":"High pressure solubility of carbon dioxide (CO2) in aqueous piperazine solutions","year":2010,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":95,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Resources Canada; Natural Sciences and Engineering Research Council of Canada","keywords":"Piperazine; Solubility; Chemistry; Aqueous solution; Carbon dioxide; Absorption (acoustics); Molar solubility; Inorganic chemistry; Organic chemistry; Materials science","score_opus":0.010061064955380592,"score_gpt":0.23523455733173354,"score_spread":0.22517349237635295,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2123934148","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99313843,0.00062841154,0.00044445964,0.000052627176,0.0015917554,0.00037843935,0.00031309557,0.0003831616,0.003069644],"genre_scores_gemma":[0.9989596,0.000027866385,0.00040639428,0.0000100329125,0.00027641584,0.000037710386,0.00008102983,0.00007945189,0.00012150775],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9980671,0.000060805956,0.0006343252,0.0003614271,0.00024680147,0.0006295375],"domain_scores_gemma":[0.99872875,0.00011178227,0.00006190047,0.00085216167,0.000059513262,0.0001859051],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000346495,0.00032802596,0.0005122742,0.00019210263,0.000036825688,0.00002017884,0.0003898108,0.0002565394,0.00023143375],"category_scores_gemma":[0.00011476039,0.0003540957,0.00013288252,0.00038791454,0.00015294708,0.0002629097,0.000119839526,0.00053170155,0.000014490744],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008770702,0.00032311078,0.00035935626,0.000102632395,0.000076303695,0.00002080253,0.00017157971,0.0026870472,0.99251294,0.0024084882,0.00014550705,0.0011045358],"study_design_scores_gemma":[0.0035484557,0.00014701698,0.0015453681,0.000052726955,0.00008878205,0.000027136248,0.000010034599,0.8142951,0.17266297,0.004896666,0.0021878171,0.00053791795],"about_ca_topic_score_codex":0.00031642284,"about_ca_topic_score_gemma":0.00044763266,"teacher_disagreement_score":0.81984997,"about_ca_system_score_codex":0.000048485417,"about_ca_system_score_gemma":0.00007978811,"threshold_uncertainty_score":0.9998911},"labels":[],"label_agreement":null},{"id":"W2147288778","doi":"10.1016/j.fluid.2008.07.015","title":"Molecular-level simulations of chemical reaction equilibrium for nitric oxide dimerization reaction in disordered nanoporous carbons","year":2008,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Catalytic Processes in Materials Science","field":"Materials Science","cited_by":18,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ontario Institute of Technology","funders":"","keywords":"Nanoporous; Chemistry; Thermodynamics; Adsorption; Monte Carlo method; Physical chemistry; Langmuir; Langmuir adsorption model; Canonical ensemble; Organic chemistry; Physics","score_opus":0.03448897291398529,"score_gpt":0.3001068798097258,"score_spread":0.2656179068957405,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2147288778","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9899065,0.00007585687,0.00816117,0.00006564128,0.000500069,0.0007206993,0.00031650352,0.00012428744,0.00012928044],"genre_scores_gemma":[0.99653304,0.0000073930223,0.002827604,0.000027834016,0.00008917094,0.000086422,0.00033289538,0.000042955802,0.000052690313],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99756026,0.000074693984,0.0008329198,0.0006097694,0.00046252517,0.0004598244],"domain_scores_gemma":[0.99854183,0.00024678526,0.00035668883,0.00053446274,0.00021031237,0.00010992929],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00042512093,0.00024970705,0.00041004896,0.0002663945,0.00007929223,0.00003851519,0.00038761643,0.0001581078,0.00004667865],"category_scores_gemma":[0.001208206,0.0002717216,0.00008996877,0.00084781763,0.00027374204,0.00084161165,0.00013225684,0.000085219646,0.000018069826],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002976008,0.0003666501,0.00006279964,0.00007291765,0.000005117285,0.000005861777,0.000181724,0.000457143,0.9981934,0.0002088301,0.000057531033,0.00009046672],"study_design_scores_gemma":[0.0019020783,0.00008351367,0.0003411426,0.00004064056,0.000030105615,0.00004090877,0.000021602324,0.034312803,0.96149164,0.0014004734,0.00006342571,0.0002716387],"about_ca_topic_score_codex":0.00022382465,"about_ca_topic_score_gemma":0.000006482071,"teacher_disagreement_score":0.03670169,"about_ca_system_score_codex":0.00016434191,"about_ca_system_score_gemma":0.00029647423,"threshold_uncertainty_score":0.9999735},"labels":[],"label_agreement":null},{"id":"W2154733682","doi":"10.1016/j.fluid.2010.09.038","title":"On the phase behaviour of Athabasca vacuum residue + n-decane","year":2010,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Alberta Innovates; Virtual Materials Group","keywords":"Chemistry; Decane; Residue (chemistry); Phase (matter); Thermodynamics; Organic chemistry","score_opus":0.011086470058453342,"score_gpt":0.2607830122661453,"score_spread":0.24969654220769197,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2154733682","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9870704,0.00010467311,0.0006337485,0.00016413501,0.0016741938,0.0004301192,0.000425421,0.00038627366,0.009111078],"genre_scores_gemma":[0.9987717,0.000012939164,0.00016884938,0.00006762568,0.00037488542,0.000043107942,0.000100823774,0.00012320401,0.00033681293],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99813616,0.000063569874,0.0005400994,0.00033484583,0.0003842557,0.0005410452],"domain_scores_gemma":[0.99815077,0.00032693322,0.000086471824,0.0011498155,0.00006531201,0.0002207297],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00039888607,0.00039097754,0.000401791,0.00015577574,0.0000884171,0.00005455224,0.0006889314,0.00020116447,0.001542695],"category_scores_gemma":[0.00010407087,0.0003114936,0.00021997864,0.0003488549,0.00016132877,0.00024070987,0.00009186171,0.00059964345,0.0001558426],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019284544,0.0005095913,0.000046723,0.000029291554,0.00008461063,0.000036735742,0.00022304943,0.000042156575,0.9681983,0.0231655,0.006529748,0.00094143656],"study_design_scores_gemma":[0.008673635,0.0009265307,0.00027641637,0.00010087857,0.00016327221,0.000069581314,0.00004321766,0.2642174,0.7095199,0.01044896,0.0047130575,0.0008471566],"about_ca_topic_score_codex":0.000028904919,"about_ca_topic_score_gemma":0.00003343734,"teacher_disagreement_score":0.26417524,"about_ca_system_score_codex":0.0000371844,"about_ca_system_score_gemma":0.00007135539,"threshold_uncertainty_score":0.9999337},"labels":[],"label_agreement":null},{"id":"W2157550617","doi":"10.1016/j.fluid.2011.06.024","title":"Reversibility of asphaltene precipitation in porous and non-porous media","year":2011,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":25,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Asphaltene; Porous medium; Dissolution; Chemistry; Precipitation; Porosity; Enhanced oil recovery; Chemical engineering; Organic chemistry","score_opus":0.025590379582484505,"score_gpt":0.2688919306569379,"score_spread":0.2433015510744534,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2157550617","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9859463,0.00051851803,0.00006333075,0.000025150159,0.00005091965,0.000013591052,0.000040237657,0.000036701138,0.013305275],"genre_scores_gemma":[0.9983531,0.000028886378,0.00085753883,0.0000137986835,0.00005971143,0.000006861518,0.000060035414,0.000015025395,0.00060501386],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988207,0.000026829213,0.00041989898,0.0003364181,0.0001809173,0.00021523645],"domain_scores_gemma":[0.9992865,0.00007749769,0.00015296062,0.00031682875,0.00006795614,0.00009827814],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003054101,0.00014678999,0.00031146363,0.00009505438,0.000028146604,0.000011986,0.000155449,0.00011097698,0.0006056834],"category_scores_gemma":[0.0002158687,0.00014631069,0.00005337073,0.00020560995,0.00009659122,0.00022368309,0.000055605797,0.00011627973,0.000006054593],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00030770575,0.0004981969,0.013782623,0.0002567274,0.000048750902,0.00003195951,0.003308777,0.0000015205509,0.9675493,0.00003230302,0.00012672554,0.014055356],"study_design_scores_gemma":[0.0098753795,0.00028966778,0.015629921,0.00043138943,0.00036498884,0.000033871085,0.0011193792,0.013826455,0.95333076,0.0040083663,0.00028020085,0.0008096175],"about_ca_topic_score_codex":0.00025027216,"about_ca_topic_score_gemma":0.000043825992,"teacher_disagreement_score":0.014218589,"about_ca_system_score_codex":0.00003653516,"about_ca_system_score_gemma":0.00006734265,"threshold_uncertainty_score":0.6631809},"labels":[],"label_agreement":null},{"id":"W2161655326","doi":"10.1016/j.fluid.2008.04.003","title":"Solubility of carbon dioxide in aqueous solutions of 2-amino-2-hydroxymethyl-1,3-propanediol","year":2008,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Carbon Dioxide Capture Technologies","field":"Engineering","cited_by":46,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Solubility; Aqueous solution; Hydroxymethyl; Carbon dioxide; Amine gas treating; Inorganic chemistry; Organic chemistry","score_opus":0.027221787108897888,"score_gpt":0.24243251140945896,"score_spread":0.21521072430056107,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2161655326","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9914831,0.0043282374,0.00040127005,0.000035947516,0.00032830986,0.00039460548,0.000063262225,0.0006479545,0.0023173487],"genre_scores_gemma":[0.9988616,0.0001485504,0.0007828998,0.0000050699778,0.00005572664,0.000041763054,0.000013769759,0.000050908795,0.000039724746],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99799454,0.00005872529,0.0008185045,0.00031621286,0.00030092057,0.0005110746],"domain_scores_gemma":[0.9986954,0.00015836033,0.00009875356,0.0008927632,0.00007397695,0.00008079194],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00030992323,0.00028811608,0.00068782707,0.00039449515,0.00001414156,0.000003140479,0.0004083419,0.00026847702,0.000033998673],"category_scores_gemma":[0.0003903529,0.00031082256,0.00017588594,0.00069664617,0.0004145306,0.00013602333,0.00016880718,0.00031793505,0.0000042994384],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000047935326,0.00017225613,0.0011804157,0.00015813073,0.00004809166,0.000055429686,0.0003702122,0.001390274,0.9951838,0.00026314546,0.00024696492,0.00088329305],"study_design_scores_gemma":[0.0019431717,0.00021844721,0.002313622,0.00009738166,0.0000386809,0.00007518278,0.00008027913,0.07701747,0.9165196,0.0011401249,0.0001548996,0.0004011404],"about_ca_topic_score_codex":0.0002680373,"about_ca_topic_score_gemma":0.000059583483,"teacher_disagreement_score":0.07866425,"about_ca_system_score_codex":0.00015507372,"about_ca_system_score_gemma":0.0000786302,"threshold_uncertainty_score":0.9999344},"labels":[],"label_agreement":null},{"id":"W2161740710","doi":"10.1016/j.fluid.2004.11.004","title":"Asphaltene phase behavior: prediction at a crossroads","year":2004,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":29,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Basic Energy Sciences; Natural Sciences and Engineering Research Council of Canada; Office of Science; U.S. Department of Energy","keywords":"Asphaltene; Chemistry; Differential scanning calorimetry; Hydrocarbon; Phase (matter); Molar mass; Thermodynamics; Small-angle X-ray scattering; Organic chemistry; Chemical engineering; Polymer; Scattering","score_opus":0.01946892503692075,"score_gpt":0.3080251763614926,"score_spread":0.28855625132457186,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2161740710","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9844049,0.0009335991,0.0004991771,0.00011582892,0.00019493222,0.000021325835,0.000418444,0.0005019995,0.0129098],"genre_scores_gemma":[0.9798955,0.000033457556,0.00024807666,0.000078201956,0.000679129,0.00007717331,0.0007164443,0.000057538604,0.018214481],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9978899,0.000015920847,0.000506512,0.0006015833,0.00043783177,0.0005482497],"domain_scores_gemma":[0.9988299,0.000021429034,0.00015108005,0.0005980324,0.00008531033,0.00031425196],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00015476985,0.00032020343,0.00035366116,0.00010624627,0.0003293537,0.0001408091,0.00030835537,0.00020516309,0.003172042],"category_scores_gemma":[0.00006001831,0.00032225007,0.00026321318,0.00030443104,0.00013852934,0.00036542895,0.0001168207,0.000226424,0.000277285],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002549792,0.0015134746,0.0004818498,0.000056520938,0.00008054025,0.00010481351,0.00017257548,0.00004840846,0.98510414,0.00003172422,0.00094777544,0.011203192],"study_design_scores_gemma":[0.022541642,0.0003133753,0.000050904608,0.00015692758,0.00064248656,0.00016682259,0.00005308489,0.0071031814,0.9246755,0.00021057948,0.04347994,0.00060554646],"about_ca_topic_score_codex":0.00005825645,"about_ca_topic_score_gemma":0.000007638832,"teacher_disagreement_score":0.060428638,"about_ca_system_score_codex":0.00033381832,"about_ca_system_score_gemma":0.00015756936,"threshold_uncertainty_score":0.99992293},"labels":[],"label_agreement":null},{"id":"W2176557602","doi":"10.1016/j.fluid.2015.11.022","title":"Clathrate hydrate dissociation conditions for refrigerant + sucrose aqueous solution: Experimental measurement and thermodynamic modelling","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":23,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"National Research Foundation","keywords":"Clathrate hydrate; Chemistry; Hydrate; Isochoric process; Aqueous solution; Sucrose; Dissociation (chemistry); Thermodynamics; Chromatography; Organic chemistry","score_opus":0.061337140428648476,"score_gpt":0.2957677837707748,"score_spread":0.23443064334212632,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2176557602","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9801503,0.001057655,0.014858088,0.00023597118,0.00035708706,0.00068067777,0.00007028919,0.00007434793,0.0025155824],"genre_scores_gemma":[0.9981757,0.000026900827,0.0008662863,0.000071479495,0.00009942874,0.000106168016,0.00012748268,0.00003226231,0.00049429975],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99838746,0.00009795921,0.00033321846,0.0004057626,0.00039467387,0.0003809117],"domain_scores_gemma":[0.99934584,0.00003024697,0.00012095446,0.0002113959,0.000034073404,0.00025747652],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006867339,0.00021267748,0.00021001793,0.00003311634,0.0002698125,0.000072270945,0.00011763355,0.00010589434,0.00026584053],"category_scores_gemma":[0.00001997218,0.00018857507,0.00007071607,0.00012435761,0.0001331705,0.00035479543,0.000087278546,0.00010162439,0.000096760974],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021994463,0.0003067627,0.000034983586,0.0000073359324,0.00004572863,0.0000046812897,0.0019364051,0.009454009,0.9857342,0.00054369326,0.0012609123,0.00045131805],"study_design_scores_gemma":[0.0031260287,0.00037607693,0.00002020249,0.000020901414,0.00004743514,0.000009454332,0.000145259,0.97205925,0.014781661,0.0074380445,0.0016818005,0.00029390992],"about_ca_topic_score_codex":0.000115681476,"about_ca_topic_score_gemma":0.000011926508,"teacher_disagreement_score":0.9709526,"about_ca_system_score_codex":0.0004576948,"about_ca_system_score_gemma":0.000037812344,"threshold_uncertainty_score":0.7689868},"labels":[],"label_agreement":null},{"id":"W2209441792","doi":"10.1016/j.fluid.2015.12.033","title":"Modeling of the vaporization enthalpies of petroleum fractions","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Chemical Thermodynamics and Molecular Structure","field":"Chemistry","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"","keywords":"Vaporization; Chemistry; Boiling point; Enthalpy of vaporization; Enthalpy; Mean squared error; Artificial neural network; Thermodynamics; Outlier; Statistics; Computer science; Organic chemistry; Mathematics; Artificial intelligence","score_opus":0.02137125841996885,"score_gpt":0.27194088730110033,"score_spread":0.2505696288811315,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2209441792","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98633367,0.00016935042,0.004709143,0.00004701384,0.00015415286,0.00003237031,0.00007262182,0.000018354429,0.008463346],"genre_scores_gemma":[0.99945146,0.0000046637283,0.00017548134,0.000008881461,0.00008294207,0.0000028725829,0.000049835293,0.000015808397,0.0002080586],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9993203,0.000010857046,0.00023193151,0.0001217547,0.00021230188,0.00010284661],"domain_scores_gemma":[0.9993925,0.000014390232,0.00009099922,0.0003451557,0.000100969,0.0000559779],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000049855626,0.00008948035,0.00014043793,0.000018586032,0.000021089909,0.000006891589,0.00018681237,0.000079769656,0.00013764598],"category_scores_gemma":[0.00010213529,0.00006990644,0.00010650249,0.000091598136,0.0000459583,0.00004889973,0.00008368985,0.00009517726,9.1722114e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004166592,0.00006353997,0.000047601425,0.000031212723,0.000030170173,4.6403767e-7,0.0001449865,0.0041806195,0.99400705,0.0012447363,0.0000722929,0.00013566785],"study_design_scores_gemma":[0.0007260629,0.000011336137,0.0000019631918,0.000027660533,0.000031743984,0.0000037425946,0.00006075968,0.5430959,0.4523512,0.0032463071,0.00037921878,0.00006409718],"about_ca_topic_score_codex":0.00003240703,"about_ca_topic_score_gemma":0.0000014320141,"teacher_disagreement_score":0.54165584,"about_ca_system_score_codex":0.000028203736,"about_ca_system_score_gemma":0.00006646963,"threshold_uncertainty_score":0.28507018},"labels":[],"label_agreement":null},{"id":"W2287559199","doi":"10.1016/j.fluid.2016.02.018","title":"Vapor-liquid equilibria for n-heptane + (benzene, toluene, p-xylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture","year":2016,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":21,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Ministerio de Economía y Competitividad; FPInnovations; Comunidad de Madrid","keywords":"Chemistry; Ethylbenzene; Non-random two-liquid model; Toluene; Ionic liquid; Heptane; Dicyanamide; Benzene; Xylene; Organic chemistry; Chromatography; Analytical Chemistry (journal); Activity coefficient; Aqueous solution","score_opus":0.029821183393491133,"score_gpt":0.2945343826236702,"score_spread":0.26471319923017905,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2287559199","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96913666,0.0031763522,0.014523371,0.004414606,0.0016873108,0.0021718754,0.0010203545,0.001473344,0.0023961288],"genre_scores_gemma":[0.96333283,0.00051876105,0.0032232197,0.0010017676,0.0036068032,0.001552674,0.0004701576,0.00055219856,0.025741598],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99353784,0.00012953731,0.0017261107,0.0017666171,0.0007561645,0.002083716],"domain_scores_gemma":[0.99528176,0.0008471756,0.00038251493,0.002189267,0.00045867966,0.00084061077],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0006446447,0.0011652965,0.0012035047,0.0002932276,0.00044328326,0.00014443712,0.0016055298,0.00085004896,0.0036356477],"category_scores_gemma":[0.00074114685,0.0008110994,0.000754815,0.0008459132,0.00026284298,0.00097213173,0.00068535825,0.00050077867,0.0006568913],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0069620097,0.000555447,0.0000023485504,0.00023594189,0.00025323156,0.000037601,0.00021306376,0.000097779666,0.94457555,0.008274389,0.036637504,0.0021551212],"study_design_scores_gemma":[0.00886844,0.0038143636,0.0000038005846,0.0005488143,0.00024564035,0.00010528243,0.00007137063,0.021030799,0.7266568,0.0005289641,0.23643674,0.0016889742],"about_ca_topic_score_codex":0.000056186724,"about_ca_topic_score_gemma":0.000017446191,"teacher_disagreement_score":0.21791875,"about_ca_system_score_codex":0.00047801386,"about_ca_system_score_gemma":0.00061237835,"threshold_uncertainty_score":0.999434},"labels":[],"label_agreement":null},{"id":"W2398424577","doi":"10.1016/j.fluid.2016.05.021","title":"Modeling the solubility and volumetric properties of H2 and heavy hydrocarbons using the simplified PC-SAFT","year":2016,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"CMG Reservoir Simulation Foundation; Suncor Energy Incorporated; University of Calgary; Cenovus Energy; Natural Sciences and Engineering Research Council of Canada; Computer Modelling Group","keywords":"Solubility; Chemistry; Thermodynamics; Alkane; Asphalt; Hildebrand solubility parameter; Compressibility; Gibbs free energy; Hydrocarbon; Organic chemistry; Materials science","score_opus":0.03508912782120833,"score_gpt":0.24638326151189607,"score_spread":0.21129413369068775,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2398424577","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9676746,0.0035126721,0.0276935,0.00017308703,0.00022320251,0.00036890773,0.000034031596,0.00012811414,0.00019187953],"genre_scores_gemma":[0.9995084,0.00014228292,0.00010339537,0.000024375844,0.00012474124,0.000014180126,0.000001781207,0.000051430605,0.000029444009],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99864894,0.000092332106,0.00040599523,0.00027278072,0.00020138982,0.0003785772],"domain_scores_gemma":[0.9991017,0.00016575067,0.000043773147,0.00055048434,0.000034371373,0.00010394253],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00043877735,0.00025299063,0.00030395613,0.000094285555,0.00015012854,0.000060152794,0.00025470566,0.00009113995,0.000010056307],"category_scores_gemma":[0.000117757474,0.00012971125,0.00007400365,0.00028492327,0.00030370892,0.00030904962,0.00016998817,0.00013541042,0.0000017801203],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001314733,0.000040129064,0.00009380933,0.0000652602,0.00009435588,0.0000014182319,0.0004361552,0.0019059726,0.9933798,0.0004592983,0.00002072011,0.0033716082],"study_design_scores_gemma":[0.0010309035,0.000056851928,0.000020187557,0.00008366377,0.00007163028,0.000023225766,0.00005664042,0.9609692,0.035234954,0.0021902155,0.000065585715,0.00019691182],"about_ca_topic_score_codex":0.00007514705,"about_ca_topic_score_gemma":0.000013608894,"teacher_disagreement_score":0.95906323,"about_ca_system_score_codex":0.00004579072,"about_ca_system_score_gemma":0.000045002675,"threshold_uncertainty_score":0.5289471},"labels":[],"label_agreement":null},{"id":"W2520497164","doi":"10.1016/j.fluid.2016.09.017","title":"Criterion for determining crossover phenomenon in volume-translated equation of states","year":2016,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":26,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Isobaric process; Crossover; Thermodynamics; Volume (thermodynamics); Chemistry; Molar volume; Equation of state; Phenomenon; Statistical physics; Physics","score_opus":0.01939888067042767,"score_gpt":0.2713483187051519,"score_spread":0.25194943803472425,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2520497164","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8989306,0.00022303825,0.09928827,0.000032193624,0.00039737485,0.00036522976,0.00029676693,0.00016971408,0.00029678535],"genre_scores_gemma":[0.99878776,0.00003061568,0.00071303267,0.000011699856,0.000095465475,0.000048978563,0.000107714375,0.00007549779,0.0001292268],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99864113,0.000030149473,0.0005427582,0.00023855086,0.00013831489,0.00040909945],"domain_scores_gemma":[0.9993876,0.00015874594,0.00006249624,0.0002603712,0.000051346105,0.00007939822],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00022146828,0.00021824424,0.00031528572,0.00017913576,0.000023916687,0.000026036083,0.00016886195,0.00010977741,0.00015034039],"category_scores_gemma":[0.00004347063,0.00019338995,0.00009051241,0.00019328442,0.00005612582,0.0005490791,0.000020927662,0.000056163834,0.000015314827],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033262145,0.00007874408,0.00024409566,0.00011031073,0.00003551999,0.0000037404275,0.00071218394,0.00071850483,0.97998345,0.00022000347,0.00009855408,0.017462287],"study_design_scores_gemma":[0.0070757368,0.0002980978,0.00024386225,0.0002024136,0.000024851151,0.0000026141333,0.000013728562,0.8937007,0.09203388,0.0044305045,0.0016485987,0.0003250199],"about_ca_topic_score_codex":0.000007505331,"about_ca_topic_score_gemma":0.000007980453,"teacher_disagreement_score":0.8929822,"about_ca_system_score_codex":0.0000952775,"about_ca_system_score_gemma":0.000031532705,"threshold_uncertainty_score":0.7886213},"labels":[],"label_agreement":null},{"id":"W2562249225","doi":"10.1016/j.fluid.2016.12.012","title":"Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15–328.15) K","year":2016,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Crystallization and Solubility Studies","field":"Materials Science","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Government of Jiangsu Province; National Natural Science Foundation of China; CNIB; Jiangsu Agricultural Science and Technology Innovation Fund","keywords":"Chemistry; Solubility; Dissolution; Solvent; Enthalpy; Gibbs free energy; Dimethylformamide; Ethyl acetate; Crystallization; Thermodynamics; Physical chemistry; Organic chemistry","score_opus":0.026844668895670807,"score_gpt":0.2703197259432407,"score_spread":0.24347505704756991,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2562249225","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9972623,0.0009539819,0.00012636246,0.00030143207,0.00026728972,0.0006726766,0.00017586928,0.00006242513,0.00017768341],"genre_scores_gemma":[0.9981301,0.00008911716,0.000057858688,0.000039819446,0.00004380241,0.000017493025,0.000013005441,0.000026159276,0.0015826597],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99779695,0.00022093412,0.00055736885,0.0006605794,0.00036592234,0.00039823473],"domain_scores_gemma":[0.99895245,0.0001960405,0.00013896076,0.00045418198,0.000095783194,0.00016260236],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0005867273,0.00027432005,0.000511467,0.00015599754,0.00011390483,0.00005216348,0.0002531382,0.00007660467,0.0012947171],"category_scores_gemma":[0.00012012368,0.00020816817,0.00004885837,0.00025160905,0.00029152044,0.0006798564,0.0010235182,0.000058680005,0.000032114123],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00045910684,0.0006441671,0.0124060605,0.00007455345,0.000026697262,0.000021006284,0.0059193713,0.0000034851748,0.97876537,0.00008279369,0.001434747,0.00016266726],"study_design_scores_gemma":[0.09447336,0.005806343,0.056138393,0.0012399199,0.0006662567,0.00006738012,0.014143415,0.034225643,0.7730295,0.013196547,0.0027153727,0.0042978707],"about_ca_topic_score_codex":0.0000470575,"about_ca_topic_score_gemma":0.00022493748,"teacher_disagreement_score":0.20573585,"about_ca_system_score_codex":0.00008267077,"about_ca_system_score_gemma":0.000049918865,"threshold_uncertainty_score":0.99961823},"labels":[],"label_agreement":null},{"id":"W2572518038","doi":"10.1016/j.fluid.2017.01.018","title":"Fluid behavior of gas condensate system with water vapor","year":2017,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"National Natural Science Foundation of China","keywords":"Dew point; Chemistry; Equation of state; Thermodynamics; Water vapor; Wellbore; Volume (thermodynamics); Vapor pressure; Work (physics); Constant (computer programming); Petroleum engineering; Geology","score_opus":0.014282138371207157,"score_gpt":0.24804793562751085,"score_spread":0.2337657972563037,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2572518038","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98711205,0.00013833844,0.0010985951,0.000022529473,0.000985876,0.00047743804,0.00020415144,0.0004840757,0.009476977],"genre_scores_gemma":[0.99888414,0.000008854084,0.00020025858,0.000007017931,0.00023561933,0.000065963046,0.00009994942,0.00013563785,0.000362576],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9981818,0.000034098903,0.00050145324,0.00034443493,0.00032298267,0.0006152132],"domain_scores_gemma":[0.99812424,0.000026391375,0.000106904474,0.0014218794,0.00009217463,0.00022839196],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00020931958,0.00039575034,0.0005663851,0.000112811824,0.00016725248,0.00014087079,0.0006679933,0.00015406347,0.00021548489],"category_scores_gemma":[0.000012086731,0.00029977484,0.00014282462,0.00005497645,0.0002041085,0.0005513952,0.00013200619,0.00016667687,0.0001495454],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021087257,0.00011867899,0.00024283907,0.00023898497,0.00016283446,0.00024598485,0.0002183304,0.00018712673,0.99611545,0.0013800695,0.00024301566,0.0006357991],"study_design_scores_gemma":[0.0060069757,0.00043135518,0.00025330414,0.00024916817,0.00027315982,0.00020840472,0.000050279068,0.2760293,0.71454847,0.00010426773,0.0011556366,0.0006896923],"about_ca_topic_score_codex":0.00004495739,"about_ca_topic_score_gemma":0.0000102748245,"teacher_disagreement_score":0.28156698,"about_ca_system_score_codex":0.000086051485,"about_ca_system_score_gemma":0.00004010197,"threshold_uncertainty_score":0.99994546},"labels":[],"label_agreement":null},{"id":"W2736622548","doi":"10.1016/j.fluid.2017.07.011","title":"Ionic liquids for consumer products: Dissolution, characterization, and controlled release of fragrance compositions","year":2017,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Canada Excellence Research Chairs, Government of Canada","keywords":"Chemistry; Ionic liquid; Dissolution; Thermal stability; Ionic bonding; Ion; Characterization (materials science); Chemical engineering; Organic chemistry; Inorganic chemistry; Nanotechnology; Catalysis","score_opus":0.01864330773591538,"score_gpt":0.28247588704353854,"score_spread":0.26383257930762316,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2736622548","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.94024765,0.00054012757,0.054138,0.002955483,0.00020472512,0.0011886169,0.0004275524,0.00009294283,0.00020489274],"genre_scores_gemma":[0.9967629,0.00008772917,0.0006786135,0.000065259024,0.00024952478,0.00039843595,0.00030806984,0.000029908695,0.0014196127],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99891955,0.00001723465,0.00043909668,0.00028704404,0.00010357091,0.00023350045],"domain_scores_gemma":[0.9987234,0.00007349341,0.00020827212,0.0006261161,0.00027366763,0.00009504739],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014386544,0.00015837446,0.00035027717,0.000035146168,0.0004175742,0.00006531809,0.00023394731,0.0000748742,0.000055062825],"category_scores_gemma":[0.00042097497,0.00014091001,0.00008193045,0.000057339315,0.00020817318,0.0002714513,0.00007472302,0.00007654773,0.000008204409],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005878776,0.00018669752,0.000018035898,0.00011063133,0.00006502316,2.8666568e-7,0.00008716331,0.000010773387,0.9824662,0.015182235,0.00066169247,0.00062334276],"study_design_scores_gemma":[0.02432444,0.00041614895,0.00043335088,0.00029288649,0.00028485933,0.000013030716,0.000023037273,0.40754333,0.5197475,0.00066422956,0.04566435,0.000592839],"about_ca_topic_score_codex":0.000019647181,"about_ca_topic_score_gemma":6.668801e-7,"teacher_disagreement_score":0.46271873,"about_ca_system_score_codex":0.00002278422,"about_ca_system_score_gemma":0.00006175508,"threshold_uncertainty_score":0.57461435},"labels":[],"label_agreement":null},{"id":"W2739272774","doi":"10.1016/j.fluid.2017.07.010","title":"An augmented free-water three-phase Rachford-Rice algorithm for CO2/hydrocarbons/water mixtures","year":2017,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":21,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; University of Alberta","keywords":"Initialization; Chemistry; Phase (matter); Flash evaporation; Aqueous solution; Aqueous two-phase system; Thermodynamics; Three-phase; Chromatography; Computer science; Organic chemistry","score_opus":0.016314443797646974,"score_gpt":0.28816928135991143,"score_spread":0.2718548375622645,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2739272774","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8533695,0.0002609181,0.13917334,0.00015087368,0.0022102688,0.0010544079,0.0009227016,0.0009270398,0.0019309991],"genre_scores_gemma":[0.9916937,0.000017880135,0.0039262553,0.0001119085,0.0014500837,0.0002571461,0.0018186563,0.0003148707,0.00040954017],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.996662,0.000059697264,0.00069995824,0.0007574612,0.00040322985,0.0014176116],"domain_scores_gemma":[0.9965663,0.000069695314,0.00009530424,0.0026535422,0.00008319044,0.00053194625],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00046816497,0.00075405533,0.00070925435,0.00021322738,0.00059659407,0.0006001686,0.0017466864,0.0003506041,0.00031108462],"category_scores_gemma":[0.0000473996,0.0005880251,0.00033171786,0.00006963447,0.00021172849,0.001533635,0.00028950127,0.0003249413,0.00014041032],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00034589184,0.00059581967,0.000010068511,0.00008255224,0.00035305374,0.00008635426,0.0003278433,0.00012241516,0.9772425,0.0002117204,0.0026251015,0.017996665],"study_design_scores_gemma":[0.0106159905,0.0005048457,0.000009498926,0.00003255474,0.00014364264,0.000026057238,0.000007964732,0.6498789,0.32570496,0.0058177244,0.0065908823,0.0006669345],"about_ca_topic_score_codex":0.00007026916,"about_ca_topic_score_gemma":0.0000385612,"teacher_disagreement_score":0.65153754,"about_ca_system_score_codex":0.00012246688,"about_ca_system_score_gemma":0.00003712117,"threshold_uncertainty_score":0.9996571},"labels":[],"label_agreement":null},{"id":"W2744431527","doi":"10.1016/j.fluid.2017.08.008","title":"Comment on: Quasi-elastic neutron scattering investigation of the guest molecule dynamics in the bromomethane clathrate hydrate","year":2017,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"National Research Council Canada","funders":"","keywords":"Clathrate hydrate; Chemistry; Bromide; Molecule; Hydrate; Neutron scattering; Chemical physics; Hydrogen bond; Molecular dynamics; Scattering; Hydrogen bromide; Neutron diffraction; Crystallography; Computational chemistry; Crystal structure; Physics; Bromine; Organic chemistry; Optics","score_opus":0.02123226358754257,"score_gpt":0.266013310534851,"score_spread":0.24478104694730843,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2744431527","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9863299,0.000029749865,0.00004152048,0.0077808034,0.00054206274,0.00042394374,0.00001968334,0.000012605293,0.0048197033],"genre_scores_gemma":[0.9985625,0.000015393714,0.000058236,0.0010595024,0.00006958441,0.00002292981,0.000022087179,0.000020594225,0.00016916258],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99827695,0.0003459652,0.0003771301,0.00030964328,0.00037037648,0.0003199598],"domain_scores_gemma":[0.9984551,0.00011861154,0.00029700642,0.00104106,0.000006991069,0.0000812147],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008061121,0.00020353898,0.00020852014,0.00003730122,0.00028773528,0.00009279449,0.0009851173,0.00008517461,0.00017658295],"category_scores_gemma":[0.00006375291,0.00012363362,0.0000808823,0.00020391528,0.00046257713,0.0002208821,0.00036231955,0.0002992892,0.00011764384],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013397273,0.00042834887,0.0069957646,0.000037098504,0.000032130738,0.000018789378,0.0017687489,0.0022216053,0.98418856,0.0019593267,0.0016224682,0.00059317844],"study_design_scores_gemma":[0.009151558,0.002530424,0.09573219,0.000738976,0.00021528988,0.00003878885,0.00051522185,0.67506075,0.19932576,0.011309268,0.0040647313,0.0013170833],"about_ca_topic_score_codex":0.00036852813,"about_ca_topic_score_gemma":0.00008569438,"teacher_disagreement_score":0.7848628,"about_ca_system_score_codex":0.00015955449,"about_ca_system_score_gemma":0.000015344163,"threshold_uncertainty_score":0.5041633},"labels":[],"label_agreement":null},{"id":"W275407664","doi":"10.1016/s0378-3812(03)00348-0","title":"Erratum to “The activity of ions: analysis of the theory and data for aqueous solutions of MgBr2, CaBr2 and BaBr2 at 298.2 K”","year":2003,"lang":"en","type":"erratum","venue":"Fluid Phase Equilibria","topic":"Chemical and Physical Properties in Aqueous Solutions","field":"Chemical Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Chemistry; Ion; Aqueous solution; Physical chemistry; Organic chemistry","score_opus":0.042137033642865765,"score_gpt":0.30419204114659826,"score_spread":0.2620550075037325,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W275407664","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6470817,0.08521432,0.057289466,0.0056607174,0.022952659,0.009090359,0.12993824,0.00037872093,0.04239385],"genre_scores_gemma":[0.9303014,0.00046560942,0.00052150205,0.00017182302,0.0007234824,0.00015569589,0.0019124406,0.000131122,0.0656169],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9978238,0.00019018282,0.0006386753,0.0006080906,0.0003300057,0.00040926778],"domain_scores_gemma":[0.9964603,0.0009094119,0.00030683112,0.002005979,0.00015922403,0.00015822651],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005640925,0.00036512574,0.0009945572,0.000119926015,0.0001999326,0.000015285366,0.0009844434,0.00034489925,0.000101716374],"category_scores_gemma":[0.0018005535,0.00023787485,0.00038503035,0.0008120765,0.0006542313,0.00009338157,0.001593042,0.00052236405,0.0000012349539],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003027531,0.0003490395,0.000004612676,0.0005047939,0.001491889,3.1717977e-7,0.00025445505,0.00012288672,0.513983,0.0033194905,0.47891486,0.00075192226],"study_design_scores_gemma":[0.002520994,0.00047367465,0.00006231746,0.000997812,0.012882435,0.000017762064,0.00010921972,0.4586569,0.099132285,0.011477666,0.4122542,0.0014147194],"about_ca_topic_score_codex":0.00015043047,"about_ca_topic_score_gemma":0.00007241032,"teacher_disagreement_score":0.45853403,"about_ca_system_score_codex":0.00008169606,"about_ca_system_score_gemma":0.00013843882,"threshold_uncertainty_score":0.9700255},"labels":[],"label_agreement":null},{"id":"W2778573095","doi":"10.1016/j.fluid.2017.12.012","title":"Application of augmented free-water Rachford-Rice algorithm to water/hydrocarbons mixtures considering the dissolution of methane in the aqueous phase","year":2017,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Enhanced Oil Recovery Techniques","field":"Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"University of Alberta","keywords":"Chemistry; Methane; Phase (matter); Flash evaporation; Aqueous solution; Solubility; Hydrocarbon; Dissolution; Thermodynamics; Aqueous two-phase system; Organic chemistry; Chromatography","score_opus":0.014216574013766293,"score_gpt":0.2933071565321965,"score_spread":0.2790905825184302,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2778573095","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8781468,0.0002256076,0.11942477,0.0002640103,0.00016469137,0.00078296324,0.00007568766,0.0001417024,0.00077376404],"genre_scores_gemma":[0.9964144,0.00003169651,0.0030781315,0.00003848908,0.00007811717,0.00022736177,0.00006693065,0.0000386592,0.000026202963],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9986032,0.00008928339,0.00047887064,0.00022317925,0.00025242873,0.00035301025],"domain_scores_gemma":[0.99844074,0.0001311953,0.00008927316,0.0012475406,0.00003949051,0.000051755647],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006521987,0.00021489656,0.00030407638,0.00012296851,0.00008020419,0.000045663674,0.0008130535,0.00009739555,0.000016208474],"category_scores_gemma":[0.00011945687,0.00012481539,0.00009070628,0.000091666756,0.000109836015,0.0002558398,0.00017485456,0.00018036476,0.0000075059784],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000069567795,0.00012654731,0.000007268984,0.000052696134,0.00004370282,0.0000055053747,0.0012045526,0.00023879281,0.9791032,0.000071552015,0.00033325172,0.018743359],"study_design_scores_gemma":[0.0012192137,0.00015221586,0.000039713384,0.0000531078,0.00003825937,0.000011187512,0.000031613657,0.0831683,0.9118288,0.0023170444,0.0009894444,0.00015107106],"about_ca_topic_score_codex":0.00036807926,"about_ca_topic_score_gemma":0.000045008856,"teacher_disagreement_score":0.11826761,"about_ca_system_score_codex":0.00005607888,"about_ca_system_score_gemma":0.00001073822,"threshold_uncertainty_score":0.50898236},"labels":[],"label_agreement":null},{"id":"W2792545175","doi":"10.1016/j.fluid.2018.01.034","title":"An improved volume translation strategy for PR EOS without crossover issue","year":2018,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":32,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Volume (thermodynamics); Thermodynamics; Crossover; Polar; Work (physics); Nonlinear system; Diagram; Translation (biology); Equation of state; Range (aeronautics); Constraint (computer-aided design); Statistical physics; Statistics; Physics; Mathematics; Materials science","score_opus":0.024039711040643817,"score_gpt":0.3150910408284916,"score_spread":0.29105132978784776,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2792545175","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8907167,0.00018953047,0.1015349,0.000034079603,0.0012193948,0.0009310838,0.00042734097,0.00084288185,0.004104119],"genre_scores_gemma":[0.99412644,0.000006272286,0.0023057032,0.00005417217,0.0020638334,0.00009130171,0.00039744342,0.00017017158,0.00078465533],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9982511,0.000037114558,0.00045226768,0.00044090944,0.00017549456,0.0006431329],"domain_scores_gemma":[0.9989269,0.00003910315,0.00005497726,0.0006052386,0.000114216586,0.00025956435],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00020937856,0.0003771526,0.0003534981,0.00010544738,0.00012619374,0.00019187684,0.00033635867,0.00022569983,0.0007020832],"category_scores_gemma":[0.000017109704,0.0004023618,0.00013767765,0.0002048999,0.0001322092,0.0010470895,0.000016590144,0.0001397677,0.00015673113],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005497978,0.00015715287,0.00003151697,0.00007448207,0.00009200323,0.0000023400908,0.0004965613,0.0005045376,0.98106545,0.00031423362,0.001699714,0.0150121935],"study_design_scores_gemma":[0.0047148503,0.0009900244,0.000045982993,0.000019313995,0.00006240299,0.0000079105375,0.000018696366,0.9256771,0.042784173,0.0013814355,0.023818541,0.00047956852],"about_ca_topic_score_codex":0.000017257764,"about_ca_topic_score_gemma":0.00003208533,"teacher_disagreement_score":0.9382813,"about_ca_system_score_codex":0.00006897298,"about_ca_system_score_gemma":0.000072795636,"threshold_uncertainty_score":0.9998428},"labels":[],"label_agreement":null},{"id":"W2809631624","doi":"10.1016/j.fluid.2018.06.002","title":"Applying the Patel-Teja EoS with regular solution theory to predict the onset of asphaltene precipitation","year":2018,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":10,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Asphaltene; Chemistry; Molar volume; Thermodynamics; Alkane; Solubility; Mole fraction; Hildebrand solubility parameter; Hydrocarbon; Decane; Precipitation; Organic chemistry; Physical chemistry","score_opus":0.014506164893704454,"score_gpt":0.2689282964889465,"score_spread":0.2544221315952421,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2809631624","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98229223,0.000386971,0.010246761,0.0004393252,0.00007231543,0.000108825894,0.00006985651,0.00009984686,0.006283855],"genre_scores_gemma":[0.99555135,0.000007402807,0.00043388392,0.00014045011,0.0004551566,0.00026761062,0.000072590956,0.000029526196,0.0030420143],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9985168,0.000122162,0.0003259613,0.00031412463,0.00042274978,0.00029820562],"domain_scores_gemma":[0.99867374,0.00019949207,0.00018911337,0.00066489296,0.00018972886,0.000083023166],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00081521156,0.0001863266,0.00021155791,0.000055313867,0.00032671244,0.00006930065,0.00042848833,0.00007787676,0.0003050226],"category_scores_gemma":[0.00019553173,0.000103220555,0.00009222914,0.00037582984,0.000290919,0.00015347447,0.00008162612,0.00014222108,0.0000322025],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00078604935,0.00013560205,0.00020161388,0.000069000496,0.00020093008,0.0000032507546,0.001168698,0.000050336344,0.93433183,0.0001952896,0.0016127222,0.061244704],"study_design_scores_gemma":[0.002908517,0.0006712497,0.00020701929,0.0005823991,0.0007856246,0.000057511133,0.0013398068,0.06691237,0.8976506,0.002609255,0.025779637,0.00049598224],"about_ca_topic_score_codex":0.000036455145,"about_ca_topic_score_gemma":0.000013139793,"teacher_disagreement_score":0.06686203,"about_ca_system_score_codex":0.000037588135,"about_ca_system_score_gemma":0.000104811166,"threshold_uncertainty_score":0.4209212},"labels":[],"label_agreement":null},{"id":"W2899248951","doi":"10.1016/j.fluid.2018.10.018","title":"Nanoscale-extended alpha functions for pure and mixing confined fluids","year":2018,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Mitacs; Petroleum Technology Research Centre; University of Regina","keywords":"Acentric factor; Chemistry; Exponential function; RADIUS; Phase (matter); Thermodynamics; Exponential decay; Equation of state; Intermolecular force; Nanoscopic scale; Physics; Nanotechnology; Crystallography; Materials science; Molecule; Organic chemistry; Quantum mechanics","score_opus":0.013708184898899392,"score_gpt":0.25971585262595753,"score_spread":0.24600766772705815,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2899248951","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92506987,0.00066549744,0.06359105,0.00013746617,0.0020909442,0.00060377095,0.0003744077,0.00082102994,0.0066459677],"genre_scores_gemma":[0.9957869,0.000025861142,0.0011476241,0.00010212177,0.0012427407,0.00010321817,0.00022751822,0.00012845681,0.0012355648],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9983715,0.00003023576,0.00040115643,0.0004220613,0.00016550062,0.00060958957],"domain_scores_gemma":[0.99899685,0.0001316381,0.000037725553,0.00045749574,0.00010634126,0.00026994848],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00019163235,0.00036408115,0.00036873898,0.00015363886,0.00020434723,0.000109994915,0.00021617541,0.00019225365,0.00035660376],"category_scores_gemma":[0.0000684732,0.00038034562,0.00013411437,0.00025454594,0.00020455685,0.0003742566,0.00006863207,0.00013959712,0.00008154358],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021594134,0.000092374685,0.000021893396,0.00007815003,0.00015967846,0.0000063095094,0.00021896917,0.000010887812,0.9744153,0.004179752,0.014170223,0.006430535],"study_design_scores_gemma":[0.006265132,0.0007984837,0.00012118267,0.00007005034,0.00015882161,0.00006419379,0.00005555056,0.8546906,0.061348982,0.0049449992,0.07077506,0.0007069592],"about_ca_topic_score_codex":0.0000031557433,"about_ca_topic_score_gemma":0.000012222262,"teacher_disagreement_score":0.9130663,"about_ca_system_score_codex":0.000053575317,"about_ca_system_score_gemma":0.000047566344,"threshold_uncertainty_score":0.9998649},"labels":[],"label_agreement":null},{"id":"W2902186503","doi":"10.1016/j.fluid.2018.12.002","title":"A two-phase flash algorithm with the consideration of capillary pressure at specified mole numbers, volume and temperature","year":2018,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Enhanced Oil Recovery Techniques","field":"Engineering","cited_by":29,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; National Natural Science Foundation of China","keywords":"Chemistry; Thermodynamics; Mole fraction; Vapor pressure; Volume (thermodynamics); Flash evaporation; Algorithm; Mechanics; Mathematics; Physics","score_opus":0.006500670959081389,"score_gpt":0.24825292523214829,"score_spread":0.2417522542730669,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2902186503","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9894021,0.0016947201,0.0028413206,0.000081199076,0.00021564035,0.0005682936,0.00017928514,0.00040805328,0.0046093776],"genre_scores_gemma":[0.98545325,0.00011593992,0.011194682,0.00009350169,0.000472737,0.00007224132,0.00008743124,0.00008608344,0.0024241223],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9989633,0.000054609514,0.00024524794,0.0002663087,0.00021515004,0.0002553632],"domain_scores_gemma":[0.99923295,0.00007116563,0.0000591117,0.0004280458,0.00012139805,0.00008733136],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014598473,0.00024559756,0.0002711766,0.000056346387,0.00010047882,0.00006418672,0.00013620916,0.00012442358,0.0002786928],"category_scores_gemma":[0.000020741432,0.00018767542,0.000043258988,0.00017096313,0.0002367609,0.00029430093,0.000067573135,0.00017187785,0.000024120864],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021543128,0.0000520165,0.00002158489,0.00005743829,0.00011928353,0.000016616683,0.0005160681,0.00006218485,0.90696377,0.00012147165,0.08839089,0.0034632653],"study_design_scores_gemma":[0.0029452927,0.0007234229,0.000031780462,0.000091962575,0.000082928535,0.00009060696,0.00004355818,0.0762314,0.8728394,0.00020195356,0.046397585,0.000320144],"about_ca_topic_score_codex":0.000017687005,"about_ca_topic_score_gemma":0.000051494804,"teacher_disagreement_score":0.076169215,"about_ca_system_score_codex":0.000037978134,"about_ca_system_score_gemma":0.000034198372,"threshold_uncertainty_score":0.7653182},"labels":[],"label_agreement":null},{"id":"W2910750944","doi":"10.1016/j.fluid.2019.01.004","title":"Modeling the phase behaviour of bitumen/n-alkane systems with the cubic plus association (CPA) equation of state","year":2019,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":20,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada; Virtual Materials Group; Petrobras; Suncor Energy Incorporated; Schlumberger Foundation","keywords":"Acentric factor; Chemistry; Pentane; Asphalt; Propane; Alkane; Asphaltene; Phase (matter); Thermodynamics; Equation of state; Phase diagram; Distillation; Component (thermodynamics); Yield (engineering); Analytical Chemistry (journal); Hydrocarbon; Organic chemistry; Materials science; Crystallography; Composite material","score_opus":0.018533115774188483,"score_gpt":0.2706361108031421,"score_spread":0.2521029950289536,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2910750944","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99428165,0.00062710524,0.0035192887,0.00015106096,0.000074179836,0.000058853406,0.00012718933,0.00004462382,0.0011160207],"genre_scores_gemma":[0.9932559,0.000017342738,0.00002418338,0.000012511722,0.000094800635,0.000021318507,0.00012550082,0.000027900842,0.0064205336],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99824715,0.00008077891,0.00051105476,0.00025329518,0.00064618496,0.00026152676],"domain_scores_gemma":[0.99848205,0.00015045135,0.00055372505,0.00050773757,0.00025850532,0.00004753359],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007197432,0.00018340713,0.00038361788,0.00006530092,0.0000943947,0.000076042845,0.0003294669,0.000085368425,0.00012490155],"category_scores_gemma":[0.00005791737,0.000109475026,0.00012562427,0.00030250996,0.00004264776,0.00021224483,0.00004456204,0.00018514026,0.00001345286],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023182978,0.00021718955,0.0007008372,0.00018596454,0.00022956329,0.0000012893796,0.0008012935,0.036756184,0.96014875,0.000035701236,0.000117214186,0.00057419296],"study_design_scores_gemma":[0.0034468314,0.0001123994,0.000003173485,0.0001773998,0.0003477969,0.0000024464148,0.0005748038,0.9032565,0.09179954,0.000020899359,0.000118812284,0.00013939165],"about_ca_topic_score_codex":0.0003522768,"about_ca_topic_score_gemma":0.000009333295,"teacher_disagreement_score":0.8683492,"about_ca_system_score_codex":0.00014322807,"about_ca_system_score_gemma":0.0001756173,"threshold_uncertainty_score":0.4464262},"labels":[],"label_agreement":null},{"id":"W2915024708","doi":"10.1016/j.fluid.2019.02.005","title":"A robust multiphase isenthalpic flash model for water/solvent/hydrocarbon systems at high pressures and elevated temperatures","year":2019,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":14,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Chemistry; Enthalpy; Thermodynamics; Phase diagram; Phase (matter); Solubility; Mechanics; Physical chemistry; Organic chemistry; Physics","score_opus":0.014893399978782841,"score_gpt":0.2235605405875518,"score_spread":0.20866714060876895,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2915024708","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9888704,0.0018682266,0.0044249985,0.000024376988,0.0014558081,0.0017603649,0.0006304605,0.00072038453,0.00024498728],"genre_scores_gemma":[0.9954228,0.00007789805,0.00035981205,0.000027499585,0.0002850723,0.00019391575,0.00077749154,0.00021141044,0.0026441442],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9975235,0.000056281282,0.00058255874,0.00065875426,0.00030548684,0.0008734468],"domain_scores_gemma":[0.9987641,0.00011365651,0.000062914296,0.00068243843,0.0000715604,0.00030530503],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00022350403,0.00058796693,0.0006691739,0.00018767749,0.00011639612,0.0001863258,0.000325223,0.00027257283,0.00007240467],"category_scores_gemma":[0.000021348736,0.00050806755,0.00016424524,0.00012864554,0.00006418107,0.0004597701,0.00016198293,0.00020966517,0.00007552631],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003995954,0.00011172889,0.00003753929,0.00044823362,0.00021730912,0.000014108773,0.00034576963,0.2481534,0.74844486,0.00033879175,0.0014701703,0.000018479124],"study_design_scores_gemma":[0.0066499687,0.00018529265,0.000006570817,0.0001142172,0.00011921034,0.000031500927,0.000013680053,0.8835814,0.1073858,0.00026594655,0.0010586112,0.0005878208],"about_ca_topic_score_codex":0.000027109782,"about_ca_topic_score_gemma":0.00000853789,"teacher_disagreement_score":0.64105904,"about_ca_system_score_codex":0.0001387924,"about_ca_system_score_gemma":0.000031899533,"threshold_uncertainty_score":0.9997371},"labels":[],"label_agreement":null},{"id":"W2926644414","doi":"10.1016/j.fluid.2019.03.020","title":"Modelling density and excess volume of hydrocarbon + water mixtures near the critical region","year":2019,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Memorial University of Newfoundland; University of Alberta","funders":"","keywords":"Hydrocarbon; Chemistry; Supercritical fluid; Miscibility; Volume (thermodynamics); Thermodynamics; Hydrocarbon mixtures; Mixing (physics); Organic chemistry; Polymer","score_opus":0.011719639551477517,"score_gpt":0.23117056887174336,"score_spread":0.21945092932026586,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2926644414","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9822219,0.0005547767,0.015057255,0.0001227167,0.0005441839,0.00022334796,0.00000989875,0.00015406418,0.0011118664],"genre_scores_gemma":[0.99943125,0.000026913473,0.0001725985,0.000033463275,0.00013882101,0.0000057411976,0.000020154284,0.000055407443,0.00011562024],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99880916,0.000056396228,0.00030027638,0.00025498398,0.0001951813,0.0003840128],"domain_scores_gemma":[0.99926233,0.00010416833,0.000021187516,0.00046662276,0.000039708226,0.0001059679],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018109466,0.00022384405,0.000305818,0.000047702175,0.0000762076,0.00009166306,0.00021844503,0.00012914086,0.00006189553],"category_scores_gemma":[0.000015484746,0.0001575537,0.00008762259,0.00008754782,0.00020620698,0.00027889243,0.00009628021,0.00019817917,0.000039090068],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017290744,0.00007249696,0.00025502653,0.00022170886,0.0000825963,0.000024241022,0.0012550969,0.03230448,0.9629866,0.0020508033,0.00026667656,0.0003073727],"study_design_scores_gemma":[0.0007397284,0.00008133212,0.000013771488,0.00004398549,0.000043807246,0.000036225978,0.000013124227,0.9425903,0.051567707,0.003968188,0.00069825235,0.00020356517],"about_ca_topic_score_codex":0.000028288763,"about_ca_topic_score_gemma":0.0000010006889,"teacher_disagreement_score":0.9114189,"about_ca_system_score_codex":0.000022994773,"about_ca_system_score_gemma":0.000017972974,"threshold_uncertainty_score":0.6424854},"labels":[],"label_agreement":null},{"id":"W2967157067","doi":"10.1016/j.fluid.2019.112280","title":"Free-volume theory coupled with modified group-contribution PC-SAFT for predicting the viscosities. I. Non-associated compounds and their mixtures","year":2019,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":15,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Acentric factor; Chemistry; Thermodynamics; Viscosity; Group contribution method; Volume (thermodynamics); Phase (matter); Bar (unit); Relative viscosity; Absolute deviation; Atmospheric pressure; Phase equilibrium; Organic chemistry","score_opus":0.004919246464791754,"score_gpt":0.204803728970258,"score_spread":0.19988448250546625,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2967157067","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9219515,0.0006781756,0.07297417,0.000075974946,0.00062949804,0.0013834493,0.0008673285,0.00048763733,0.0009522935],"genre_scores_gemma":[0.99839205,0.000020835621,0.000063184896,0.00008301186,0.00027338928,0.00013976259,0.0006815518,0.00012657192,0.00021967104],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99819714,0.00010534174,0.00040848035,0.0003957272,0.00022613072,0.0006671584],"domain_scores_gemma":[0.99839234,0.000615973,0.000117564916,0.0006318095,0.00010167909,0.00014063493],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00073320314,0.00045961337,0.00052203034,0.000088366505,0.0002231079,0.00018830107,0.00043804658,0.00020681148,0.00004021784],"category_scores_gemma":[0.00008618348,0.00032188388,0.00013894537,0.00022080704,0.00014752877,0.0004444668,0.000111848734,0.00029100367,0.000006459266],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0016197161,0.0002258124,0.00042034278,0.0001645857,0.0009859742,0.00000567122,0.0016868301,0.006119724,0.9791819,0.007989274,0.0013007286,0.0002994281],"study_design_scores_gemma":[0.008301047,0.0004822858,0.000422195,0.00011988454,0.00011911797,0.000017026232,0.0001444048,0.98071426,0.00374614,0.0052330615,0.00027044164,0.00043015552],"about_ca_topic_score_codex":0.000025534378,"about_ca_topic_score_gemma":0.000021300553,"teacher_disagreement_score":0.9754358,"about_ca_system_score_codex":0.00013994973,"about_ca_system_score_gemma":0.000048882623,"threshold_uncertainty_score":0.99992335},"labels":[],"label_agreement":null},{"id":"W3021960256","doi":"10.1016/j.fluid.2020.112629","title":"The effects of sodium chloride on the diffusion of sulfonated resorcinarenes in aqueous solutions","year":2020,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"NMR spectroscopy and applications","field":"Physics and Astronomy","cited_by":2,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"St. Francis Xavier University","funders":"Natural Sciences and Engineering Research Council of Canada; Programa Operacional Temático Factores de Competitividade; Fundação para a Ciência e a Tecnologia; Universidad de los Andes","keywords":"Chemistry; Aqueous solution; Sodium; Diffusion; Chloride; Inorganic chemistry; Organic chemistry; Thermodynamics","score_opus":0.015885104787810602,"score_gpt":0.3045990201622402,"score_spread":0.28871391537442964,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3021960256","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9942137,0.00026715492,0.00041816133,0.0028764682,0.00008230271,0.00040962396,0.00004941618,0.00001611336,0.0016670444],"genre_scores_gemma":[0.9995663,0.000016935284,0.000013008719,0.000047241556,0.00015339335,0.00007217127,0.000022958098,0.000011365304,0.000096604635],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9991918,0.00006866819,0.0002601433,0.00015484588,0.00012773999,0.00019675706],"domain_scores_gemma":[0.99896437,0.0005515456,0.00010772849,0.00029854785,0.000031031035,0.000046781657],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010329007,0.00010929093,0.00015881743,0.000022089102,0.00015557099,0.000014918932,0.00026945508,0.000023284632,0.00006767087],"category_scores_gemma":[0.000049990787,0.000067896726,0.00008530295,0.00029667772,0.00010546293,0.000038556645,0.000085063984,0.00013232334,0.0000137834095],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002155557,0.00028959478,0.0003969004,0.000016981294,0.000023093924,6.005296e-7,0.00040131813,0.000008281015,0.87268156,0.12262315,0.0022750124,0.0010679506],"study_design_scores_gemma":[0.0015370129,0.00040707126,0.0007752147,0.000071025606,0.000028756438,1.3724768e-7,0.00016734874,0.007622094,0.97431046,0.009933577,0.005034621,0.00011271209],"about_ca_topic_score_codex":0.0001519708,"about_ca_topic_score_gemma":0.000004223384,"teacher_disagreement_score":0.11268958,"about_ca_system_score_codex":0.000009552731,"about_ca_system_score_gemma":0.00005712754,"threshold_uncertainty_score":0.2768748},"labels":[],"label_agreement":null},{"id":"W3043178214","doi":"10.1016/j.fluid.2020.112689","title":"Modelling of phase behavior of ammonia and its mixtures using the mg-SAFT","year":2020,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":11,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Refrigerant; Chemistry; Ammonia; Thermodynamics; Work (physics); Phase (matter); Computation; Hydrocarbon; Liquid phase; Organic chemistry; Heat exchanger","score_opus":0.05497978391349194,"score_gpt":0.2869185303031183,"score_spread":0.23193874638962636,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3043178214","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9705793,0.0026659465,0.025581086,0.000036897407,0.00020391963,0.00036783094,0.00026192385,0.00012492068,0.00017815238],"genre_scores_gemma":[0.99870205,0.00007758578,0.00091213046,0.000026029089,0.00016763536,0.000009930169,0.000025999267,0.00007084216,0.000007792603],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9986528,0.000048535374,0.00052336126,0.0002402943,0.00023181213,0.00030317364],"domain_scores_gemma":[0.99929583,0.00008460495,0.00009918793,0.0002894018,0.00006021389,0.00017074888],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013217081,0.00026652598,0.00042600874,0.000070387425,0.00004769632,0.000025026568,0.0002880363,0.000107353146,0.000057534075],"category_scores_gemma":[0.00002615829,0.00022900476,0.00012305232,0.0002789422,0.00009569634,0.00026031656,0.00009242829,0.00018210143,0.000002737118],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00016125882,0.00014754463,0.000014862257,0.00015851876,0.000089707006,0.000014189754,0.0008210803,0.03492385,0.96247715,0.00050921144,0.0000443629,0.0006382896],"study_design_scores_gemma":[0.0021925566,0.00014423279,0.0000017348959,0.000041350733,0.00014900934,0.000010595054,0.000026182714,0.7790027,0.21801737,0.00013053814,0.00011035567,0.00017334822],"about_ca_topic_score_codex":0.00001544809,"about_ca_topic_score_gemma":6.976563e-7,"teacher_disagreement_score":0.74445975,"about_ca_system_score_codex":0.000018297042,"about_ca_system_score_gemma":0.000039667724,"threshold_uncertainty_score":0.9338543},"labels":[],"label_agreement":null},{"id":"W3093709390","doi":"10.1016/j.fluid.2020.112865","title":"Water content of liquid H2S in equilibrium with the hydrate phase","year":2020,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Hydrate; Scrubber; Dehydration; Sulfur; Water content; Organic chemistry","score_opus":0.032398941536535865,"score_gpt":0.2523164832920316,"score_spread":0.21991754175549574,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3093709390","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98937976,0.00018233492,0.00015651748,0.004550188,0.00010416283,0.0005398415,0.000025475823,0.000044334804,0.0050173984],"genre_scores_gemma":[0.99798995,0.00001361859,0.000109694585,0.00097564864,0.00008591814,0.000027328746,0.000037913887,0.000038002687,0.00072189816],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9979538,0.0001699304,0.00048493466,0.0004624958,0.00039099544,0.00053786597],"domain_scores_gemma":[0.9991691,0.000058557365,0.000108997476,0.00040415753,0.000013432223,0.00024574948],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00038126393,0.00027183775,0.00036996912,0.000033673543,0.000050832517,0.000030254098,0.0004819908,0.000085426174,0.0049686492],"category_scores_gemma":[0.00002113389,0.00013916398,0.000092218615,0.00039536625,0.000355862,0.0002995446,0.00032314775,0.00025979907,0.000537461],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0020944846,0.0003489586,0.00015099783,0.000018830278,0.00003918327,0.000049653725,0.0030054483,0.0011672807,0.99120784,0.000050243038,0.001592259,0.00027479665],"study_design_scores_gemma":[0.012406147,0.0050587584,0.00008751061,0.000048878544,0.000083644496,0.000016849965,0.0003229117,0.051005073,0.90882355,0.00011805156,0.021506464,0.0005221628],"about_ca_topic_score_codex":0.0001239293,"about_ca_topic_score_gemma":0.000009511754,"teacher_disagreement_score":0.08238432,"about_ca_system_score_codex":0.000044013912,"about_ca_system_score_gemma":0.00001974924,"threshold_uncertainty_score":0.9959409},"labels":[],"label_agreement":null},{"id":"W3123264244","doi":"10.1016/j.fluid.2021.112964","title":"A comparative performance evaluation of cubic equations of state for predicting the compositional distribution of hydrate inhibitors in reservoir fluid systems","year":2021,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":9,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"University of Edinburgh","keywords":"Chemistry; Equation of state; Mixing (physics); Hydrate; Thermodynamics; Cubic function; Clathrate hydrate; Organic chemistry","score_opus":0.0454058247139777,"score_gpt":0.3142071124685774,"score_spread":0.2688012877545997,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3123264244","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9959168,0.00049420085,0.0015897811,0.000054727134,0.00017387622,0.0008044456,0.00044686385,0.0000059796303,0.0005133129],"genre_scores_gemma":[0.99907714,0.000016259615,0.00008736137,0.0000029102982,0.000026981186,0.00008019939,0.0006532737,0.0000070363553,0.000048861875],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9979587,0.00039165714,0.00071186136,0.00020091525,0.00056504254,0.00017178142],"domain_scores_gemma":[0.9988817,0.00033793686,0.0003471756,0.00021802107,0.00017618384,0.00003896865],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0016563301,0.00010898597,0.00027301756,0.00003657002,0.00008071559,0.000010309769,0.00013476523,0.000047863097,0.00013045844],"category_scores_gemma":[0.00011414128,0.00008574698,0.000066801236,0.00051493116,0.00018602637,0.00022968739,0.00008770316,0.00008916573,0.0000043310683],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001450706,0.00023423324,0.00163265,0.00006415675,0.00003705629,2.1442636e-7,0.0014823026,0.29444718,0.7014596,0.00022629942,0.00013455492,0.00013670663],"study_design_scores_gemma":[0.0014916911,0.0001976917,0.0025744475,0.00015972852,0.000056193185,0.0000013907235,0.00024662388,0.7745399,0.22029738,0.0003238483,0.00004344036,0.00006766665],"about_ca_topic_score_codex":0.0001216945,"about_ca_topic_score_gemma":0.000017653336,"teacher_disagreement_score":0.4811622,"about_ca_system_score_codex":0.00013298252,"about_ca_system_score_gemma":0.000104346895,"threshold_uncertainty_score":0.34966603},"labels":[],"label_agreement":null},{"id":"W3133495112","doi":"10.1016/j.fluid.2021.113004","title":"An improved vapor-liquid-asphaltene three-phase equilibrium computation algorithm","year":2021,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":8,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; National Natural Science Foundation of China","keywords":"Chemistry; Asphaltene; Computation; Phase equilibrium; Thermodynamics; Vapor–liquid equilibrium; Vapor phase; Phase (matter); Algorithm; Organic chemistry; Chromatography","score_opus":0.01883826732004785,"score_gpt":0.31722946498558274,"score_spread":0.2983911976655349,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3133495112","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.92862666,0.0019569262,0.06311633,0.0002703005,0.0003507662,0.00003052937,0.00036287453,0.00064988027,0.004635743],"genre_scores_gemma":[0.98007816,0.000024125913,0.009634823,0.0002837578,0.0015628783,0.000043449043,0.003719022,0.00014400008,0.0045098057],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9965255,0.000088743436,0.00085637165,0.0011395047,0.0005482344,0.00084159663],"domain_scores_gemma":[0.99765736,0.00009890824,0.00028706426,0.00096823164,0.00041522956,0.00057322544],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0003297612,0.00052877155,0.00069889694,0.00014253393,0.0002324311,0.0003800727,0.00050111633,0.00029319723,0.00237023],"category_scores_gemma":[0.00012130832,0.00056311575,0.000352645,0.0006617814,0.00013423058,0.00081855344,0.0001721244,0.0003738083,0.000098622164],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027293627,0.0014550603,0.00001539956,0.00011196713,0.00020821318,0.00024391394,0.00010867742,0.000084741194,0.8524351,0.000015731908,0.00042198278,0.14462624],"study_design_scores_gemma":[0.0055068154,0.00030845957,0.0000019944673,0.00006088362,0.00024127692,0.00006870673,0.00008037185,0.5781258,0.4121836,0.0002284702,0.002710276,0.00048334486],"about_ca_topic_score_codex":0.00006885172,"about_ca_topic_score_gemma":0.000013927709,"teacher_disagreement_score":0.578041,"about_ca_system_score_codex":0.00012732108,"about_ca_system_score_gemma":0.00050363253,"threshold_uncertainty_score":0.999682},"labels":[],"label_agreement":null},{"id":"W4206688089","doi":"10.1016/j.fluid.2022.113392","title":"A new vapor-liquid-asphaltene three-phase equilibrium computation algorithm based on the free-asphaltene assumption","year":2022,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; China Scholarship Council","keywords":"Asphaltene; Flow assurance; Chemistry; Precipitation; Phase (matter); Work (physics); Petroleum engineering; Thermodynamics; Bubble point; Wellbore; Mechanics; Organic chemistry; Geology; Bubble; Meteorology","score_opus":0.02474852889001144,"score_gpt":0.2917844790180464,"score_spread":0.26703595012803494,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4206688089","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8331533,0.0014400935,0.14533027,0.0061388295,0.00084659277,0.00017851451,0.0011002902,0.001000461,0.010811613],"genre_scores_gemma":[0.9817634,0.000008691503,0.004135092,0.0014961816,0.0015869694,0.0002495273,0.0022609746,0.00018890748,0.008310217],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9954757,0.00023461586,0.0008957549,0.001047078,0.0014751257,0.00087172666],"domain_scores_gemma":[0.99718666,0.00043366454,0.000480538,0.0013226839,0.00014425126,0.0004322138],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0009250854,0.00061063987,0.0006245495,0.00027950824,0.0007920146,0.00026546765,0.0012163344,0.00016393991,0.010434929],"category_scores_gemma":[0.00020460326,0.0005377285,0.00048430747,0.0009805587,0.0001110197,0.0003447305,0.00043107083,0.0007725538,0.00011484855],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00176078,0.0017802379,0.000019434043,0.00009705634,0.00026425064,0.00014816302,0.00015820179,0.009199127,0.81941295,0.0001554562,0.029712731,0.1372916],"study_design_scores_gemma":[0.010034661,0.0009398973,0.000003650927,0.00007761059,0.00031939844,0.000031957952,0.000081464445,0.9117181,0.05776703,0.0008627424,0.017541127,0.000622361],"about_ca_topic_score_codex":0.00019015926,"about_ca_topic_score_gemma":0.0000087628205,"teacher_disagreement_score":0.902519,"about_ca_system_score_codex":0.0003679867,"about_ca_system_score_gemma":0.0006058126,"threshold_uncertainty_score":0.9997074},"labels":[],"label_agreement":null},{"id":"W4245601693","doi":"10.1016/j.fluid.2005.03.011","title":"Asphaltene phase behavior: prediction at a crossroads","year":2005,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Basic Energy Sciences; Natural Sciences and Engineering Research Council of Canada; Office of Science; U.S. Department of Energy","keywords":"Asphaltene; Chemistry; Differential scanning calorimetry; Hydrocarbon; Molar mass; Phase (matter); Thermodynamics; Small-angle X-ray scattering; Drop (telecommunication); Mineralogy; Organic chemistry; Chemical engineering; Polymer; Scattering","score_opus":0.019453372633301092,"score_gpt":0.31243060793366184,"score_spread":0.29297723530036074,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4245601693","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9748428,0.0013238804,0.00021325483,0.00017337894,0.00013655047,0.000019331963,0.00041566204,0.00049429067,0.022380874],"genre_scores_gemma":[0.9402306,0.000038958515,0.0003069319,0.00010913241,0.0014033987,0.000074109,0.0006545261,0.00005551888,0.057126805],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99785477,0.000022639937,0.0005433813,0.0005907155,0.00043206563,0.00055642927],"domain_scores_gemma":[0.99880886,0.00003244126,0.00015627356,0.00060432067,0.00008413997,0.0003139484],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.00018246501,0.00031742477,0.0003512255,0.00010705713,0.00030898774,0.00014137024,0.00031513636,0.000201495,0.008380109],"category_scores_gemma":[0.000054991237,0.0003200178,0.00025752655,0.00025659884,0.00011756728,0.00045049953,0.00012003972,0.00022567651,0.00044331272],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00024010967,0.0013296857,0.00070023147,0.00003933951,0.00007340973,0.0000334367,0.00013958721,0.000020543217,0.928234,0.000010310173,0.0062118815,0.06296751],"study_design_scores_gemma":[0.011292034,0.00016635048,0.00003776203,0.00007527731,0.000522881,0.00010096628,0.000031137966,0.07114347,0.62970424,0.000018645964,0.2864095,0.0004977188],"about_ca_topic_score_codex":0.000019415194,"about_ca_topic_score_gemma":0.000008429779,"teacher_disagreement_score":0.2985297,"about_ca_system_score_codex":0.00025571662,"about_ca_system_score_gemma":0.00009178884,"threshold_uncertainty_score":0.9999252},"labels":[],"label_agreement":null},{"id":"W4302287618","doi":"10.1016/j.fluid.2022.113630","title":"Modeling solubility of oxygen in ionic liquids: Chemical structure-based Machine Learning Systems Compared to Equations of State","year":2022,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Solubility; Chemistry; Ionic liquid; Thermodynamics; Equation of state; Mean squared error; Organic chemistry; Statistics","score_opus":0.02693883003741305,"score_gpt":0.26894533130845233,"score_spread":0.2420065012710393,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4302287618","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95011365,0.00032240903,0.048396457,0.000110730805,0.00009049447,0.0004878083,0.0003596675,0.000074816264,0.000043973232],"genre_scores_gemma":[0.99878097,0.0000012505465,0.000616356,0.000020781157,0.000037451064,0.00015334245,0.00029255738,0.000035434554,0.000061836785],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9980842,0.00009858442,0.00083898375,0.00032297504,0.00034321664,0.00031206734],"domain_scores_gemma":[0.99915403,0.00012781091,0.00010581675,0.0004085188,0.00009779147,0.000106060346],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035574447,0.00017223772,0.00041006363,0.00013591882,0.00008201941,0.000012203665,0.0003560346,0.000046436966,0.00027246602],"category_scores_gemma":[0.00016984757,0.00017919278,0.00009586414,0.00049830216,0.000034412955,0.00006934139,0.00025648793,0.00032486906,0.0000028278494],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015907914,0.000117824005,0.000011868743,0.00006664508,0.000012630746,3.311817e-7,0.00028042114,0.4960431,0.50282794,0.00043536627,0.000010077351,0.000034738317],"study_design_scores_gemma":[0.0012777016,0.00011391101,0.0000010101032,0.00004138291,0.000013892812,9.138336e-7,0.00008879388,0.84443283,0.15365957,0.00009008284,0.00012986855,0.00015005871],"about_ca_topic_score_codex":0.0007539396,"about_ca_topic_score_gemma":0.000008874253,"teacher_disagreement_score":0.34916836,"about_ca_system_score_codex":0.00022231873,"about_ca_system_score_gemma":0.00014438773,"threshold_uncertainty_score":0.73072696},"labels":[],"label_agreement":null},{"id":"W4323929168","doi":"10.1016/j.fluid.2023.113797","title":"Measurements and modeling of dimethyl ether (DME) solubility in n-decane and DME-saturated liquid density at T = (293.15–393.15) K and P = (0.345–2.76) MPa","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Solubility; Chemistry; Decane; Dimethyl ether; Thermodynamics; Vapor–liquid equilibrium; Analytical Chemistry (journal); Ether; Phase (matter); Physical chemistry; Organic chemistry; Chromatography; Methanol","score_opus":0.04334690209208575,"score_gpt":0.2787967981505484,"score_spread":0.23544989605846267,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4323929168","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99554586,0.0021978423,0.00050524116,0.000047393645,0.00035299157,0.0004991291,0.00009730276,0.00034530097,0.0004089323],"genre_scores_gemma":[0.9990848,0.00029559847,0.00023481072,0.000025761134,0.00007619874,0.000019014247,0.000089607485,0.00009923953,0.00007497584],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9974712,0.00016632791,0.0006914092,0.00063606235,0.0003722346,0.0006627635],"domain_scores_gemma":[0.9988606,0.0001667201,0.00006967285,0.00050832296,0.000091429225,0.00030324838],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00095161033,0.00046401098,0.0007047239,0.0002921677,0.00009532156,0.00005643289,0.00018105961,0.00027118472,0.000055217413],"category_scores_gemma":[0.0001566798,0.0004839993,0.00007467957,0.0005579096,0.00018283639,0.00042411045,0.00035397767,0.0003017153,0.000012475635],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00074821303,0.00009424978,0.002072289,0.00028309107,0.00014466053,0.000031626234,0.0011672344,0.005158542,0.9893763,0.000044666795,0.0001015587,0.0007775653],"study_design_scores_gemma":[0.0035689925,0.00020515715,0.001047252,0.00014394747,0.00007280251,0.000023446308,0.00004950628,0.94856435,0.04476212,0.0010377027,0.000044768745,0.00047996306],"about_ca_topic_score_codex":0.00017601757,"about_ca_topic_score_gemma":0.00026992837,"teacher_disagreement_score":0.9446142,"about_ca_system_score_codex":0.00013247631,"about_ca_system_score_gemma":0.000049464146,"threshold_uncertainty_score":0.99976116},"labels":[],"label_agreement":null},{"id":"W4367845170","doi":"10.1016/j.fluid.2023.113837","title":"Vapor-liquid equilibria (VLE) of the binary mixture of normal hexane and water at P = 2.5 MPa and T=(456.85 – 487.85 K)","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":6,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Non-random two-liquid model; Chemistry; Activity coefficient; Mole fraction; Thermodynamics; Dilution; Hexane; Binary number; Binary system; Vapor–liquid equilibrium; Analytical Chemistry (journal); Chromatography; Physical chemistry; Aqueous solution","score_opus":0.008290230603119194,"score_gpt":0.2220626189359565,"score_spread":0.2137723883328373,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4367845170","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99377847,0.0012580391,0.00003359353,0.00027915015,0.0009868771,0.00048037243,0.00038602023,0.00034117204,0.0024562788],"genre_scores_gemma":[0.99811095,0.00021075911,0.000056320278,0.000037657384,0.00021247214,0.000021126678,0.00018345557,0.00013352594,0.0010337624],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9974761,0.000112981346,0.0007532989,0.00046725775,0.00041625422,0.0007741293],"domain_scores_gemma":[0.99860793,0.000137967,0.00011063305,0.0008299194,0.00006518365,0.000248336],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00039979708,0.0004966943,0.0006870017,0.0002357544,0.00011476191,0.00003640583,0.00046031093,0.0002774024,0.00029490757],"category_scores_gemma":[0.000044468474,0.00036673143,0.00020389761,0.000527323,0.000545088,0.00043037478,0.00084222824,0.00027133126,0.000036391153],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005305555,0.000101909274,0.000275394,0.00044275756,0.0001904073,0.000045614655,0.0010190388,0.0004826196,0.99365455,0.00047183983,0.0024653638,0.00031995436],"study_design_scores_gemma":[0.0054870197,0.0010408813,0.0016724195,0.00027829738,0.00024093667,0.00019053486,0.000085599444,0.33012915,0.6522531,0.001522376,0.0062169265,0.0008827586],"about_ca_topic_score_codex":0.000022157556,"about_ca_topic_score_gemma":0.000011825165,"teacher_disagreement_score":0.34140143,"about_ca_system_score_codex":0.000054864267,"about_ca_system_score_gemma":0.00004488668,"threshold_uncertainty_score":0.99987847},"labels":[],"label_agreement":null},{"id":"W4378219260","doi":"10.1016/j.fluid.2023.113852","title":"Measurements of the molecular diffusion coefficient of dimethyl ether (DME) in n-decane and DME-saturated liquid viscosity at T= (293.15 – 393.15) K and P= (0.345 – 2.76) MPa","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Diffusion Coefficients in Liquids","field":"Chemistry","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Decane; Chemistry; Diffusion; Activation energy; Viscosity; Thermodynamics; Arrhenius equation; Dimethyl ether; Analytical Chemistry (journal); Physical chemistry; Chromatography; Organic chemistry","score_opus":0.022502629683782433,"score_gpt":0.2869537477019807,"score_spread":0.26445111801819826,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4378219260","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9959828,0.0009556099,0.000051819126,0.00014505452,0.00040207803,0.00044364887,0.00014959271,0.00010094875,0.0017684414],"genre_scores_gemma":[0.9983644,0.00004992159,0.000079230624,0.0000822343,0.000042736305,0.000021745567,0.00007491296,0.000073814415,0.0012110447],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9964558,0.00024140609,0.000877443,0.0007452944,0.0010959825,0.00058409834],"domain_scores_gemma":[0.99805987,0.00022302274,0.0002968516,0.0010088385,0.00019499211,0.00021642247],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0008833494,0.0004366792,0.00063983543,0.00023216201,0.000135112,0.000037430826,0.000571872,0.00028681764,0.000631971],"category_scores_gemma":[0.00054387754,0.0003524077,0.00014816604,0.0010485696,0.0004943077,0.00010714012,0.0014942276,0.0002960646,0.000016004142],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010865693,0.00077255076,0.0020441625,0.00024691474,0.00006726017,0.00001784142,0.0010948122,0.0002587381,0.9931191,0.000055829267,0.0007747707,0.00046144432],"study_design_scores_gemma":[0.005065202,0.0002831212,0.0010754153,0.00044663285,0.000088024455,0.000009769604,0.000109824425,0.01570722,0.9759104,0.00004640342,0.0008883032,0.0003696766],"about_ca_topic_score_codex":0.00011231071,"about_ca_topic_score_gemma":0.000025642305,"teacher_disagreement_score":0.017208701,"about_ca_system_score_codex":0.00013326018,"about_ca_system_score_gemma":0.00010711506,"threshold_uncertainty_score":0.9998928},"labels":[],"label_agreement":null},{"id":"W4381952780","doi":"10.1016/j.fluid.2023.113878","title":"A comparison of the CPA equation of state and the Trebble-Bishnoi equation of state for use in correlating methane hydrate formation conditions in the presence of aqueous amino acids","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":1,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"University of Calgary","keywords":"Chemistry; Hydrate; Methane; Thermodynamics; Equation of state; Aqueous solution; Amino acid; Clathrate hydrate; Activity coefficient; Glycine; Physical chemistry; Organic chemistry","score_opus":0.05915664086382949,"score_gpt":0.32057723874339117,"score_spread":0.2614205978795617,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4381952780","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99485487,0.00009072193,0.0032295855,0.00012558953,0.00007721131,0.001309593,0.00014648655,0.0000061614724,0.00015980267],"genre_scores_gemma":[0.99946475,0.00004968541,0.00020785049,0.000011658906,0.000004670914,0.00006566694,0.0000838413,0.00000949356,0.00010239244],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9977835,0.0005628293,0.00092335284,0.00016485355,0.00036620212,0.00019927183],"domain_scores_gemma":[0.997279,0.0016708602,0.00069917896,0.00029370253,0.000033895718,0.000023346216],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0019393188,0.0001215668,0.00031736944,0.000102727274,0.000059189286,0.000014410771,0.00025114522,0.000053474734,0.00004125328],"category_scores_gemma":[0.0004118933,0.000070919115,0.00006938207,0.000885113,0.00039402553,0.0004446651,0.00011695097,0.00013753712,0.000002929777],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008297663,0.00030225934,0.013584425,0.00017556301,0.000037755202,6.513637e-7,0.039510198,0.20234309,0.73813134,0.0009788286,0.00012349639,0.003982592],"study_design_scores_gemma":[0.0031954772,0.0002170685,0.0068311715,0.000107069354,0.000042188527,9.526427e-7,0.0009275933,0.9001474,0.08122408,0.0072194207,0.000013396243,0.00007420777],"about_ca_topic_score_codex":0.00071027986,"about_ca_topic_score_gemma":0.00022332813,"teacher_disagreement_score":0.6978043,"about_ca_system_score_codex":0.000034100154,"about_ca_system_score_gemma":0.000022981663,"threshold_uncertainty_score":0.28919974},"labels":[],"label_agreement":null},{"id":"W4388871847","doi":"10.1016/j.fluid.2023.114005","title":"Phase equilibrium in canonical cubic structure I (sI) and II (sII) and hexagonal (sH) gas hydrate solid solutions","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":7,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Clathrate hydrate; Hydrate; Chemistry; Thermodynamics; Flow assurance; Methane; van der Waals force; Thermodynamic equilibrium; Natural gas; Organic chemistry; Molecule; Physics","score_opus":0.01996040174475496,"score_gpt":0.28762547415717377,"score_spread":0.2676650724124188,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4388871847","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.995205,0.00072697795,0.00001798751,0.0010203642,0.00038213213,0.00042107044,0.00019775255,0.00013504951,0.001893656],"genre_scores_gemma":[0.9973417,0.00020403758,0.00015862091,0.00019222319,0.00016268893,0.000022433092,0.0001892233,0.000049842976,0.0016792152],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9971158,0.0001703423,0.0005448937,0.0008063333,0.000372662,0.0009899574],"domain_scores_gemma":[0.9988905,0.00011925543,0.00009851738,0.00039903182,0.000009731955,0.00048293997],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0004984513,0.0003780708,0.00043357525,0.00016460737,0.0003055946,0.000090514615,0.0002683668,0.0002373381,0.0028224958],"category_scores_gemma":[0.00006483806,0.00033806346,0.000072611394,0.00086925674,0.00052617735,0.00046695673,0.0010008174,0.00044006578,0.00019343688],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019608224,0.0003741924,0.00059856125,0.000024206942,0.000039115115,0.00011057785,0.00095460896,0.0007481278,0.98824733,0.00034740122,0.0057082833,0.0026515226],"study_design_scores_gemma":[0.03031017,0.003513462,0.003959439,0.00019180498,0.00023307175,0.0003653481,0.00032184602,0.8592605,0.033366174,0.025027815,0.04117841,0.0022719752],"about_ca_topic_score_codex":0.00023261296,"about_ca_topic_score_gemma":0.00015193943,"teacher_disagreement_score":0.95488113,"about_ca_system_score_codex":0.0001075838,"about_ca_system_score_gemma":0.00006874153,"threshold_uncertainty_score":0.99990714},"labels":[],"label_agreement":null},{"id":"W4388914331","doi":"10.1016/j.fluid.2023.114006","title":"Vapor-liquid-liquid equilibrium (VLLE), density, and viscosity of the ternary mixtures of normal hexane, water and bitumen at T=185–210°C and at P= 2.5 MPa","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Ternary operation; Hexane; Asphalt; Thermodynamics; Viscosity; Chromatography; Vapor–liquid equilibrium; Organic chemistry; Composite material","score_opus":0.008840270160393337,"score_gpt":0.22498565604300078,"score_spread":0.21614538588260743,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4388914331","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9963122,0.0012853926,0.00003344061,0.00016841576,0.0005529113,0.00045611736,0.00025074586,0.00023979414,0.00070098316],"genre_scores_gemma":[0.9987698,0.00025731418,0.000038717433,0.000045969307,0.00014188336,0.000013832578,0.00012522087,0.00009693226,0.00051028695],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9976777,0.000114943155,0.00063963863,0.0005010228,0.00038325487,0.0006834368],"domain_scores_gemma":[0.998746,0.00015584832,0.00010789536,0.00066650525,0.00005513212,0.00026862792],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00038588105,0.00047475935,0.00066884037,0.00019920901,0.00014288869,0.000042891847,0.00034779095,0.00022697386,0.00008275899],"category_scores_gemma":[0.000032450935,0.00035766952,0.00014474374,0.0002784905,0.0004960625,0.0003949397,0.0017944411,0.00020809993,0.000011702316],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0010577736,0.000063180174,0.0016958015,0.00044241667,0.00018907762,0.000050390994,0.000919883,0.0001689703,0.9942511,0.000093017195,0.0009473319,0.000121062236],"study_design_scores_gemma":[0.0028979473,0.0006146653,0.0023427587,0.00012965864,0.00015194174,0.00023676164,0.000025322017,0.059970807,0.93204576,0.0003040184,0.0007798152,0.00050053466],"about_ca_topic_score_codex":0.000047431586,"about_ca_topic_score_gemma":0.000031998232,"teacher_disagreement_score":0.062205326,"about_ca_system_score_codex":0.00006960823,"about_ca_system_score_gemma":0.00002893136,"threshold_uncertainty_score":0.9998875},"labels":[],"label_agreement":null},{"id":"W4389003512","doi":"10.1016/j.fluid.2023.114010","title":"Solid-liquid-vapour equilibrium conditions of tetra-iso-amyl ammonium bromide (TiAAB) semiclathrates formed from H2","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Ministry of Education - Singapore; National University of Singapore","keywords":"Chemistry; Tetra; Ammonium bromide; Bromide; Ammonium; Inorganic chemistry; Hydrogen bromide; Organic chemistry; Bromine; Medicinal chemistry","score_opus":0.019672413344830542,"score_gpt":0.30803140999691175,"score_spread":0.2883589966520812,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4389003512","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98725015,0.00027621357,0.00014879282,0.0004415474,0.00089721277,0.0005660653,0.000845323,0.0003694427,0.009205233],"genre_scores_gemma":[0.99362326,0.00011254935,0.00038526804,0.00019023227,0.00025171338,0.00006159605,0.0010981706,0.00009750801,0.004179729],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9964008,0.00017517223,0.0009768035,0.00081565,0.0006249446,0.0010066426],"domain_scores_gemma":[0.9979256,0.00043977392,0.00030175195,0.0008506815,0.000032566782,0.0004496572],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00047604364,0.00047654138,0.00065553817,0.00018368679,0.00017772596,0.00006741435,0.0007174101,0.00031008915,0.014670612],"category_scores_gemma":[0.0001385478,0.00043562287,0.0003018556,0.0012153069,0.00049481564,0.0006699199,0.0005878084,0.00036330783,0.004420733],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003387047,0.0002608769,0.0006197289,0.000025913128,0.00013684892,0.00004160948,0.0007710165,0.0015384998,0.96609616,0.00016919835,0.029858338,0.00014311078],"study_design_scores_gemma":[0.004978057,0.0010073379,0.0015861465,0.00016641853,0.00022695724,0.000022196331,0.0003877856,0.0704192,0.8951763,0.013809651,0.011161773,0.0010581603],"about_ca_topic_score_codex":0.0006042149,"about_ca_topic_score_gemma":0.000033994125,"teacher_disagreement_score":0.07091984,"about_ca_system_score_codex":0.00014459684,"about_ca_system_score_gemma":0.000076351396,"threshold_uncertainty_score":0.99980956},"labels":[],"label_agreement":null},{"id":"W4390246015","doi":"10.1016/j.fluid.2023.114020","title":"Tetrabutylammonium lactate semiclathrate hydrate phase equilibria and polymorphs","year":2023,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":3,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Clathrate hydrate; Differential scanning calorimetry; Metastability; Dissociation (chemistry); Thermodynamics; Hydrate; Ionic bonding; Calorimetry; Phase transition; Recrystallization (geology); Physical chemistry; Ion; Organic chemistry","score_opus":0.017573946208731445,"score_gpt":0.28374392158985184,"score_spread":0.2661699753811204,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4390246015","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9831799,0.00054643286,0.00006264974,0.00070805906,0.0007999105,0.00054179644,0.0001408774,0.0005628081,0.013457521],"genre_scores_gemma":[0.9835412,0.00040560117,0.00024764123,0.00029809194,0.00024659812,0.0000443972,0.00023066021,0.00011989189,0.014865938],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9963154,0.00020942533,0.00069140387,0.0010291933,0.0005372699,0.0012172953],"domain_scores_gemma":[0.9982651,0.0001661317,0.00018805443,0.00070914096,0.0000144369105,0.0006571703],"candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["insufficient_payload"],"category_scores_codex":[0.00079965894,0.00054773106,0.00052502047,0.00018368865,0.00029613107,0.00018262568,0.00047879183,0.00024334912,0.0056524533],"category_scores_gemma":[0.00006293304,0.0004864807,0.00015415548,0.0013421291,0.00042897055,0.000758237,0.0006812634,0.000401772,0.005856703],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027806027,0.00025021797,0.00072749297,0.000024425377,0.00007061523,0.00021405834,0.0007342728,0.00010516515,0.97684443,0.0001703761,0.015997551,0.0045833527],"study_design_scores_gemma":[0.027696848,0.0025059197,0.002018068,0.000183747,0.00037021528,0.00028135756,0.00034552047,0.6108222,0.22155654,0.0111711575,0.119827785,0.0032206345],"about_ca_topic_score_codex":0.00019020155,"about_ca_topic_score_gemma":0.000010987439,"teacher_disagreement_score":0.7552879,"about_ca_system_score_codex":0.00010058878,"about_ca_system_score_gemma":0.000039967756,"threshold_uncertainty_score":0.99975866},"labels":[],"label_agreement":null},{"id":"W4400046745","doi":"10.1016/j.fluid.2024.114166","title":"Extensive data analysis and modelling of carbon dioxide solubility in ionic liquids using chemical structure-based ensemble learning approaches","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"","keywords":"Solubility; Chemistry; Gradient boosting; Carbon dioxide; Ionic liquid; Boosting (machine learning); Mean squared error; Artificial intelligence; Biological system; Random forest; Statistics; Organic chemistry; Computer science; Mathematics","score_opus":0.09048399818298053,"score_gpt":0.2919706034932169,"score_spread":0.20148660531023638,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400046745","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8556837,0.001521142,0.14236566,0.000047774633,0.000036516743,0.0001540659,0.00005282962,0.00008604714,0.00005226145],"genre_scores_gemma":[0.99372435,0.000012229244,0.0058415844,0.000007135203,0.00009968732,0.000010366546,0.00024965248,0.000037123948,0.000017873246],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99827975,0.00004894362,0.0004980486,0.00066351285,0.00019353458,0.00031619822],"domain_scores_gemma":[0.99899095,0.00016321674,0.000052756295,0.00066144805,0.00004189989,0.00008971922],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029747694,0.00021169358,0.0004227034,0.00018701403,0.00003789761,0.000040645697,0.0002692898,0.00013956182,0.000036677815],"category_scores_gemma":[0.00009849933,0.00019714558,0.00009584908,0.0007696196,0.000096936725,0.00017427611,0.00026909675,0.0003487025,5.327409e-7],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000061667946,0.000043406486,0.000045241308,0.00015673481,0.00012860697,0.000003107388,0.0001793248,0.2617642,0.73684776,0.00039509533,0.0000016227009,0.00037323177],"study_design_scores_gemma":[0.0003203143,0.000020422976,0.000002054072,0.00007590769,0.00023393906,0.000002351831,0.000033909404,0.71288896,0.28603476,0.00022207406,0.00001616804,0.00014910373],"about_ca_topic_score_codex":0.00032052895,"about_ca_topic_score_gemma":0.000006167076,"teacher_disagreement_score":0.4511248,"about_ca_system_score_codex":0.00009890462,"about_ca_system_score_gemma":0.00011295132,"threshold_uncertainty_score":0.80393636},"labels":[],"label_agreement":null},{"id":"W4400618479","doi":"10.1016/j.fluid.2024.114172","title":"Impact of hydrogen cage occupancy on the mechanical properties and elastic anisotropies of sII hydrates","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McGill University","funders":"Chemical Engineering Department, Worcester Polytechnic Institute; Alliance de recherche numérique du Canada; Natural Sciences and Engineering Research Council of Canada; McGill University","keywords":"Chemistry; Cage; Occupancy; Clathrate hydrate; Anisotropy; Thermodynamics; Organic chemistry; Hydrate; Structural engineering","score_opus":0.02743450186948042,"score_gpt":0.2716476259746828,"score_spread":0.24421312410520235,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4400618479","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99652493,0.001632521,0.000028568924,0.00011657664,0.00010542266,0.0002557624,0.00004666064,0.000033699536,0.0012558328],"genre_scores_gemma":[0.9994167,0.00011017483,0.0000422523,0.00001609631,0.000036155496,0.000009891391,0.00000515772,0.00002121157,0.0003423472],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988266,0.00010301451,0.0003127067,0.00027658496,0.0002445314,0.00023656408],"domain_scores_gemma":[0.99939615,0.00017740436,0.000060696344,0.0002714913,0.000006857507,0.00008740885],"candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0002325216,0.00018643115,0.00024462555,0.00004074329,0.000057358888,0.000030178393,0.00019379184,0.00007083213,0.0020782405],"category_scores_gemma":[0.00006204526,0.00009583247,0.00012361052,0.00025045226,0.00030087394,0.00014328837,0.0001687223,0.00014035091,0.0001127539],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0001484738,0.0001360886,0.00038475398,0.00004652028,0.00011663374,0.000008771168,0.0006986447,0.00046614907,0.99559194,0.0013186302,0.00051002414,0.0005733596],"study_design_scores_gemma":[0.0014343492,0.0046208776,0.0017600701,0.00048262248,0.00024641774,0.00004243016,0.00015520344,0.28734368,0.69565946,0.006734488,0.0009904427,0.00052995945],"about_ca_topic_score_codex":0.00017065837,"about_ca_topic_score_gemma":0.0000031796378,"teacher_disagreement_score":0.29993248,"about_ca_system_score_codex":0.00004127082,"about_ca_system_score_gemma":0.000028007287,"threshold_uncertainty_score":0.998834},"labels":[],"label_agreement":null},{"id":"W4401191897","doi":"10.1016/j.fluid.2024.114198","title":"A two-phase flash algorithm for confined fluids considering the effect of pore radius and cross-sectional shape at specified volume and temperature","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Enhanced Oil Recovery Techniques","field":"Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"National Natural Science Foundation of China","keywords":"Chemistry; Volume (thermodynamics); RADIUS; Flash (photography); Phase (matter); Thermodynamics; Mechanics; Algorithm; Optics; Physics; Organic chemistry","score_opus":0.011143343850427371,"score_gpt":0.29654559460962115,"score_spread":0.2854022507591938,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4401191897","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9871594,0.0057601663,0.0036644319,0.000027877326,0.00076639804,0.00081296184,0.00061763666,0.0006401118,0.0005510739],"genre_scores_gemma":[0.9925879,0.00016731503,0.005007682,0.000026399455,0.00053843315,0.00020956504,0.00019597803,0.00012244433,0.0011442777],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9986403,0.000045976194,0.00040402115,0.00040584875,0.00017995814,0.00032388663],"domain_scores_gemma":[0.998919,0.00062630174,0.00003186802,0.00026030152,0.000050364426,0.000112130016],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004183481,0.00033094911,0.00039111302,0.00012352254,0.0001124861,0.00023702078,0.00012647363,0.00017422266,0.00021178258],"category_scores_gemma":[0.00008623425,0.00026602767,0.00013063593,0.0001769215,0.00021903441,0.0002646176,0.000091086236,0.00023951176,0.000006179415],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00027833425,0.000015639838,0.00019369386,0.00044441936,0.00017062447,0.00004194889,0.00011700603,0.000040312043,0.96928096,0.0001937353,0.007162283,0.02206107],"study_design_scores_gemma":[0.0039486564,0.00079996133,0.0001998478,0.0001377728,0.000056892794,0.0002417644,0.0000043247237,0.498692,0.48303482,0.000244298,0.012350986,0.00028866148],"about_ca_topic_score_codex":0.000003922661,"about_ca_topic_score_gemma":0.0000031253678,"teacher_disagreement_score":0.4986517,"about_ca_system_score_codex":0.00008759394,"about_ca_system_score_gemma":0.00003137274,"threshold_uncertainty_score":0.9999792},"labels":[],"label_agreement":null},{"id":"W4402536964","doi":"10.1016/j.fluid.2024.114232","title":"An empirical model for predicting saturation pressure of pure hydrocarbons in nanopores","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Hydrocarbon exploration and reservoir analysis","field":"Engineering","cited_by":4,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Nanopore; Saturation (graph theory); Thermodynamics; Hydrocarbon; Chemical engineering; Organic chemistry","score_opus":0.02416681125448535,"score_gpt":0.31514675808745757,"score_spread":0.29097994683297224,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402536964","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9123691,0.0025826772,0.083253615,0.00015754327,0.00025896032,0.00033179185,0.0001010209,0.00044288157,0.00050242484],"genre_scores_gemma":[0.9986659,0.000031604923,0.00064720365,0.00001405464,0.00016915423,0.000066511915,0.00021115912,0.000045253702,0.00014911393],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9989339,0.000032214553,0.00039595796,0.00024135051,0.00018545856,0.00021108965],"domain_scores_gemma":[0.9995808,0.00005387706,0.00002086833,0.00023802267,0.00001754861,0.00008889263],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00016082998,0.00015455733,0.00023238859,0.0002510992,0.00002568562,0.000060491217,0.00014125572,0.00013767862,0.000018324507],"category_scores_gemma":[0.00004020547,0.00014278978,0.000114748924,0.00040205024,0.00002302978,0.00046425936,0.000014788954,0.00013825846,0.0000026818916],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00004620543,0.00008575396,0.00012937388,0.0002219811,0.00012079411,0.0000046089676,0.0035873367,0.50558704,0.4873632,0.0002350768,0.00201664,0.00060199486],"study_design_scores_gemma":[0.0004912409,0.00007381495,0.000008859461,0.00006385141,0.00007936279,0.0000012505209,0.00008333241,0.98550224,0.011920424,0.0010683133,0.00056570914,0.00014157275],"about_ca_topic_score_codex":0.0000056362696,"about_ca_topic_score_gemma":0.00005304349,"teacher_disagreement_score":0.47991523,"about_ca_system_score_codex":0.00002549432,"about_ca_system_score_gemma":0.000056373137,"threshold_uncertainty_score":0.5822798},"labels":[],"label_agreement":null},{"id":"W4403427017","doi":"10.1016/j.fluid.2024.114256","title":"Effect of Ion Specificity on Thermodynamic Inhibition of CH4 and CO2 Hydrates: An Experimental and Modeling Study","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; China Scholarship Council; University of Alberta","keywords":"Chemistry; Clathrate hydrate; Thermodynamics; Ion; Hydrate; Organic chemistry","score_opus":0.016562103250427587,"score_gpt":0.29427659281007634,"score_spread":0.2777144895596488,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403427017","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9977723,0.00065599754,0.000069844325,0.000006526738,0.0001312221,0.00048411574,0.000016890119,0.000030234958,0.0008328663],"genre_scores_gemma":[0.99983317,0.0000251317,0.00001976801,0.0000039374386,0.000036132868,0.0000102385375,0.000027827302,0.000019084628,0.000024728528],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9988687,0.000182399,0.0002562344,0.00035174913,0.00020355776,0.00013735796],"domain_scores_gemma":[0.99963784,0.00006745274,0.000041981726,0.00017024002,0.000003169539,0.00007933479],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046860139,0.00016093322,0.00022154851,0.000055658304,0.000044014985,0.000027005715,0.00005617907,0.000056720768,0.00027088443],"category_scores_gemma":[0.0000060375355,0.00012073999,0.000032802644,0.00013857419,0.0001153484,0.00022582541,0.00009148395,0.00010036961,0.0000069209323],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033945232,0.00042069907,0.0001945177,0.000044177777,0.000020996098,0.0000088701845,0.0019185052,0.0018263845,0.99400306,0.00006856645,0.000007123161,0.0011476738],"study_design_scores_gemma":[0.0011093633,0.00435445,0.000048514044,0.000082921244,0.000030660358,0.000003771207,0.00019102124,0.66727906,0.3266181,0.00017202,0.0000039807314,0.00010612444],"about_ca_topic_score_codex":0.00008193265,"about_ca_topic_score_gemma":0.0000015376118,"teacher_disagreement_score":0.6673849,"about_ca_system_score_codex":0.00003791404,"about_ca_system_score_gemma":0.000003986572,"threshold_uncertainty_score":0.4923634},"labels":[],"label_agreement":null},{"id":"W4404186471","doi":"10.1016/j.fluid.2024.114281","title":"The influence of pure compounds’ parameters on the phase behaviour of carbon dioxide + 1-hexanol binary system","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Ontario Ministry of Research and Innovation; Unitatea Executiva pentru Finantarea Invatamantului Superior, a Cercetarii, Dezvoltarii si Inovarii; Corporation for National and Community Service","keywords":"Chemistry; Carbon dioxide; Binary system; Binary number; Thermodynamics; Hexanol; Phase (matter); Organic chemistry; Alcohol","score_opus":0.013006503958923102,"score_gpt":0.2504156947965883,"score_spread":0.2374091908376652,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404186471","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99436873,0.0016131265,0.00007337499,0.000084506886,0.0010033908,0.0006129953,0.00024945615,0.0004380124,0.001556427],"genre_scores_gemma":[0.999563,0.000055733875,0.000022939983,0.000012699583,0.000096181844,0.00006865278,0.000028147444,0.000097985125,0.000054683172],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9978796,0.00014601527,0.00072388066,0.00031532443,0.0004446812,0.00049046305],"domain_scores_gemma":[0.9980321,0.00073011906,0.00009976797,0.0009521258,0.0000611615,0.0001247073],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005158832,0.0003722765,0.00043482182,0.00014993001,0.000086146065,0.00007713813,0.00070336513,0.0001352942,0.000009496945],"category_scores_gemma":[0.00005645273,0.00024383738,0.00024258508,0.0005330179,0.00026032623,0.00019083485,0.000099262084,0.00036162592,0.0000145707],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022532878,0.00016707546,0.000055208075,0.00036709054,0.00028469317,0.00007816221,0.0005100309,0.007114274,0.98201066,0.008365852,0.0003729352,0.00044866977],"study_design_scores_gemma":[0.0020361631,0.00076389563,0.0000992971,0.0011175956,0.00024042532,0.0000683191,0.00030966144,0.8318675,0.16199496,0.0005243054,0.0005441983,0.00043363732],"about_ca_topic_score_codex":0.00003601479,"about_ca_topic_score_gemma":0.0000037892119,"teacher_disagreement_score":0.8247533,"about_ca_system_score_codex":0.0001415582,"about_ca_system_score_gemma":0.00008951881,"threshold_uncertainty_score":0.99434},"labels":[],"label_agreement":null},{"id":"W4404356718","doi":"10.1016/j.fluid.2024.114285","title":"Vapor–liquid equilibria (VLE), density, and viscosity of the ternary mixtures of ethane, water, and bitumen at T = 190–210 °C and P = 2.5 MPa—Measurements and CPA-EoS modeling","year":2024,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Ternary operation; Thermodynamics; Viscosity; Vapor–liquid equilibrium; Asphalt; Ternary numeral system; Organic chemistry; Chromatography; Phase (matter)","score_opus":0.01916603685180142,"score_gpt":0.24634024224260082,"score_spread":0.2271742053907994,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4404356718","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98628175,0.011279553,0.00060088,0.00008915415,0.00054612325,0.00047139035,0.00013978223,0.00016235559,0.00042899948],"genre_scores_gemma":[0.99886113,0.0006108528,0.00014843998,0.000024692165,0.000120213364,0.000010122253,0.000036818186,0.00008937647,0.0000983651],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99790716,0.00010820834,0.0005822227,0.00054462516,0.00037847238,0.00047930327],"domain_scores_gemma":[0.9990913,0.000100568934,0.000060531274,0.00046414326,0.0000534209,0.00023003155],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00047820865,0.00045213438,0.0005901296,0.00017894042,0.00009629156,0.0001026005,0.00023215187,0.00020293395,0.000023388526],"category_scores_gemma":[0.000030093895,0.00034100455,0.00009976218,0.00016445892,0.00030010822,0.00046836704,0.0007758186,0.0002530223,0.0000015858674],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000342779,0.000058552825,0.00072179304,0.0008898103,0.0002852431,0.000025620946,0.0010970106,0.00035302495,0.9953742,0.00017798314,0.00008983401,0.00058417104],"study_design_scores_gemma":[0.0017275026,0.00023224897,0.00014410216,0.0003957967,0.00021360796,0.00017233995,0.000020593541,0.69731236,0.29714897,0.0021694894,0.000100627636,0.00036235392],"about_ca_topic_score_codex":0.000073097406,"about_ca_topic_score_gemma":0.00002390569,"teacher_disagreement_score":0.6982252,"about_ca_system_score_codex":0.000054028897,"about_ca_system_score_gemma":0.000036534377,"threshold_uncertainty_score":0.9999042},"labels":[],"label_agreement":null},{"id":"W4409593952","doi":"10.1016/j.fluid.2025.114442","title":"Solubility of water in bitumen","year":2025,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada; ConocoPhillips Canada; Alberta Innovates; Canada Excellence Research Chairs, Government of Canada; Suncor Energy Incorporated; Canadian Natural Resources Limited","keywords":"Chemistry; Asphalt; Solubility; Environmental chemistry; Organic chemistry; Chemical engineering; Composite material","score_opus":0.006712115222255826,"score_gpt":0.2541186311851946,"score_spread":0.2474065159629388,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4409593952","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97653645,0.00026674804,0.0017946169,0.000053003976,0.0006391875,0.00021932814,0.00003449685,0.00019122334,0.020264935],"genre_scores_gemma":[0.99941665,0.000014533063,0.00012047474,0.000023918294,0.000039716153,0.000018551664,0.00004460951,0.000025439347,0.00029613278],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9988079,0.000039642804,0.00045529025,0.00020958803,0.00011197361,0.00037559538],"domain_scores_gemma":[0.9994118,0.000050861505,0.000014613997,0.00044118505,0.000023931963,0.000057569632],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002484468,0.00018267446,0.0003252789,0.00022665261,0.00001567914,0.00001568504,0.00024645522,0.00010466251,0.00023673783],"category_scores_gemma":[0.000020730822,0.0001615554,0.00008847603,0.00029585263,0.000063843065,0.00020295095,0.000089940666,0.00013602471,0.0000332924],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007616551,0.00016807136,0.0005247614,0.0001494961,0.000051965206,0.000009177311,0.0002297639,0.00069183245,0.99380755,0.0020937575,0.00056686864,0.0016305575],"study_design_scores_gemma":[0.003016104,0.000057955607,0.00042675945,0.000086942484,0.000023263116,0.0000018948932,0.000016138534,0.47596925,0.50482965,0.012422087,0.0029074568,0.0002425033],"about_ca_topic_score_codex":0.000022197022,"about_ca_topic_score_gemma":0.000015359186,"teacher_disagreement_score":0.48897794,"about_ca_system_score_codex":0.00007923961,"about_ca_system_score_gemma":0.000034992456,"threshold_uncertainty_score":0.6588038},"labels":[],"label_agreement":null},{"id":"W4410266132","doi":"10.1016/j.fluid.2025.114466","title":"A hybrid strategy for solving cubic equations of state based on a novel root discriminant method","year":2025,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Advanced Control Systems Optimization","field":"Engineering","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Petro-Canada","funders":"National Natural Science Foundation of China","keywords":"Chemistry; Cubic function; Root (linguistics); Discriminant; Linear discriminant analysis; State (computer science); Applied mathematics; Artificial intelligence; Statistics; Algorithm; Mathematical analysis; Mathematics","score_opus":0.024741991250453423,"score_gpt":0.3236738739538522,"score_spread":0.2989318827033988,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4410266132","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"methods","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0152104385,0.00016820389,0.98179454,0.000053716773,0.00038438468,0.00090519607,0.00036969862,0.00020689622,0.00090694334],"genre_scores_gemma":[0.96052593,0.0000014674833,0.038687132,0.000023354809,0.00005308133,0.00025113492,0.00013027285,0.00005384915,0.0002737618],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9986992,0.000032712996,0.0005375098,0.00026626512,0.0001478388,0.00031651082],"domain_scores_gemma":[0.99878824,0.00056757574,0.000087267144,0.00038244875,0.000112306145,0.00006216501],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029197306,0.0002196684,0.00036085257,0.0002456103,0.000060327933,0.000037410722,0.00016374273,0.00004506985,0.000017305485],"category_scores_gemma":[0.0002559318,0.00022602348,0.00012115723,0.00024156211,0.000019190331,0.00021930605,0.000019939751,0.0000851345,0.0000028734116],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00009578501,0.00007666005,0.0000013183798,0.00014893577,0.00003936075,7.1138084e-7,0.00003500416,0.56952846,0.4231348,0.0033614384,0.00017093496,0.003406586],"study_design_scores_gemma":[0.0035538105,0.00016212973,0.000008597191,0.00018126189,0.00006407761,5.800294e-7,0.000013258708,0.9122863,0.081809945,0.0014064258,0.00033829862,0.00017531207],"about_ca_topic_score_codex":0.000017459244,"about_ca_topic_score_gemma":0.00001065033,"teacher_disagreement_score":0.9453155,"about_ca_system_score_codex":0.0001105865,"about_ca_system_score_gemma":0.000106569445,"threshold_uncertainty_score":0.921697},"labels":[],"label_agreement":null},{"id":"W4411225337","doi":"10.1016/j.fluid.2025.114498","title":"Experimental and theoretical quantification of phase behaviour for solvents/water/heavy oil systems with the PC-SAFT equation of state","year":2025,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"Natural Sciences and Engineering Research Council of Canada; National Natural Science Foundation of China","keywords":"Chemistry; Equation of state; Phase (matter); Thermodynamics; Organic chemistry","score_opus":0.015448771972885094,"score_gpt":0.2820206794035712,"score_spread":0.2665719074306861,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4411225337","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.908501,0.00058009045,0.08949959,0.000051916315,0.00030422164,0.00047274103,0.0002418289,0.000072461175,0.00027614977],"genre_scores_gemma":[0.99935913,0.000013472559,0.00012068895,0.000006157647,0.000036736288,0.00012845329,0.00019574123,0.000038645823,0.000100957004],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99881124,0.00006379981,0.00046628126,0.00021993167,0.00018269615,0.00025602957],"domain_scores_gemma":[0.99928683,0.00014022297,0.00007733775,0.00035391314,0.00008297306,0.000058737704],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034796147,0.00020480026,0.00031989347,0.00010631004,0.000057424593,0.00004242095,0.00017940879,0.00007097248,0.000019330448],"category_scores_gemma":[0.000014886615,0.00014086723,0.000070321825,0.00013563859,0.0002452728,0.00018388743,0.000039266895,0.00007599411,0.000001301186],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00096475444,0.00038680062,0.000018379256,0.00026118575,0.00012826461,0.0000011000504,0.0006451698,0.00074899703,0.95944744,0.036553115,0.00008602202,0.00075877097],"study_design_scores_gemma":[0.0034965933,0.000298689,0.0000052147548,0.00008539535,0.00008095947,0.0000025054376,0.00012991227,0.4555667,0.53971547,0.00044883837,0.000065497356,0.00010425409],"about_ca_topic_score_codex":0.000012291322,"about_ca_topic_score_gemma":0.0000010417785,"teacher_disagreement_score":0.45481768,"about_ca_system_score_codex":0.000041388786,"about_ca_system_score_gemma":0.000037074984,"threshold_uncertainty_score":0.5744399},"labels":[],"label_agreement":null},{"id":"W4411302145","doi":"10.1016/j.fluid.2025.114502","title":"Effects of temperature and flue gas composition on miscibility behavior between flue gas and gas condensate","year":2025,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"SINOPEC Petroleum Exploration and Production Research Institute; China Scholarship Council; China National Petroleum Corporation","keywords":"Chemistry; Flue gas; Miscibility; Gas composition; Thermodynamics; Organic chemistry; Polymer","score_opus":0.006104841385199587,"score_gpt":0.25147601941178316,"score_spread":0.24537117802658356,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4411302145","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99625915,0.001125981,0.00014135052,0.00008658711,0.00045645345,0.000819882,0.00026874332,0.00025115226,0.00059071433],"genre_scores_gemma":[0.99926865,0.00009269472,0.00012833664,0.00004803741,0.0001266859,0.000042325224,0.00017603686,0.00005271673,0.000064516615],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9983279,0.00012256905,0.00046242785,0.0004925572,0.00020176322,0.00039279836],"domain_scores_gemma":[0.9988675,0.0003547059,0.000057189412,0.000463068,0.000056842564,0.00020070704],"candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0002191377,0.00040537302,0.0006023005,0.00019905805,0.00009380475,0.00007984207,0.00017363472,0.0002646245,0.000025108124],"category_scores_gemma":[0.000043030373,0.00041025417,0.0001001475,0.00026279993,0.00018811336,0.00023449954,0.000101584854,0.0003251763,0.000007230872],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019009462,0.00019558964,0.00091060356,0.00063235994,0.00013950748,0.00003614412,0.0001750992,0.000037040005,0.9939061,0.00075532874,0.00036194653,0.0026601986],"study_design_scores_gemma":[0.0072711324,0.00057595177,0.009349822,0.0006475687,0.0005360216,0.000024777333,0.000016157774,0.04765047,0.92962515,0.0034426805,0.00024070464,0.00061957573],"about_ca_topic_score_codex":0.000014508231,"about_ca_topic_score_gemma":0.0000032301934,"teacher_disagreement_score":0.06428095,"about_ca_system_score_codex":0.00007664731,"about_ca_system_score_gemma":0.000039137274,"threshold_uncertainty_score":0.99983495},"labels":[],"label_agreement":null},{"id":"W4415951197","doi":"10.1016/j.fluid.2025.114618","title":"Modeling the solubility of iron oxides in wide temperature ranges: thermodynamic foundation for understanding flow-accelerated corrosion","year":2025,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Iron oxide chemistry and applications","field":"Energy","cited_by":0,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Suncor Energy (Canada)","funders":"Canada's Oil Sands Innovation Alliance","keywords":"Solubility; Dissolution; Corrosion; Electrolyte; Oxidizing agent; Hematite; Solubility equilibrium; Magnetite; Solvent","score_opus":0.047331370365627096,"score_gpt":0.3136650452844041,"score_spread":0.266333674918777,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4415951197","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9099672,0.00009898691,0.08756967,0.00046920977,0.00012485965,0.00051041454,0.000029665234,0.000058841724,0.0011711409],"genre_scores_gemma":[0.9987445,0.000015273738,0.00032715764,0.00007710078,0.000046881618,0.000142178,0.0003396774,0.000019109875,0.00028815074],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99888253,0.000062697116,0.000420147,0.00030505972,0.00010629727,0.0002232858],"domain_scores_gemma":[0.9991425,0.00028797254,0.00006759833,0.00040398448,0.00006953969,0.000028375463],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035240047,0.00016511788,0.00021465668,0.000060156115,0.00018037332,0.00004986825,0.00022775805,0.00014082789,0.00007253426],"category_scores_gemma":[0.00014115193,0.00013511076,0.00008894047,0.0003699303,0.000074701326,0.00015973752,0.000048761114,0.00014379693,0.0000020561192],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003422767,0.00011962543,0.000026931744,0.00011585075,0.00000955452,2.1783276e-7,0.00025767583,0.030176867,0.9529904,0.015437115,0.00011387937,0.00040958065],"study_design_scores_gemma":[0.0016145755,0.000022196677,0.000017316428,0.00010492635,0.00002776381,3.9897765e-7,0.00050473574,0.78900325,0.1896309,0.01886568,0.00009546815,0.00011279621],"about_ca_topic_score_codex":0.00010961679,"about_ca_topic_score_gemma":0.00017202493,"teacher_disagreement_score":0.76335955,"about_ca_system_score_codex":0.00023249253,"about_ca_system_score_gemma":0.00009284549,"threshold_uncertainty_score":0.55096567},"labels":[],"label_agreement":null},{"id":"W913323967","doi":"10.1016/j.fluid.2015.06.044","title":"Thermodynamic evaluation and optimization of the CH3COOLi–CH3COOK–CH3COOCs system using the Modified Quasichemical Model","year":2015,"lang":"en","type":"article","venue":"Fluid Phase Equilibria","topic":"Ionic liquids properties and applications","field":"Chemical Engineering","cited_by":5,"is_retracted":false,"has_abstract":false,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Liquidus; Chemistry; Thermodynamics; Ternary operation; Phase diagram; Ternary numeral system; Eutectic system; Molten salt; Ionic liquid; Interpolation (computer graphics); Phase (matter); Catalysis; Inorganic chemistry; Organic chemistry","score_opus":0.06610270003552664,"score_gpt":0.30593495884718774,"score_spread":0.2398322588116611,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W913323967","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"codex-gemma-dda1882f352a","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.76118666,0.00033520794,0.23654743,0.00020299536,0.00009887768,0.0005616644,0.000021192971,0.00006867914,0.0009773059],"genre_scores_gemma":[0.9979173,0.0000044832673,0.0017041764,0.000032154512,0.000121352234,0.000071568094,0.000021079428,0.000034677636,0.000093215116],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99866295,0.0000858869,0.0003875193,0.00024017059,0.00041113584,0.00021231176],"domain_scores_gemma":[0.99896806,0.000053092448,0.00012599163,0.00055302546,0.00021293241,0.00008689067],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005081472,0.00016611368,0.00019414832,0.000025722658,0.000112211404,0.000031952684,0.00031983884,0.000110771885,0.000011746643],"category_scores_gemma":[0.00013463972,0.000099506455,0.000073897645,0.00023949772,0.00012227937,0.0001398459,0.00016574135,0.00014560092,0.0000019387537],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000053300642,0.000041876607,0.000001538567,0.000028897175,0.00002046553,5.940881e-8,0.00030033907,0.5887523,0.40101674,0.009579704,0.000056068602,0.00014867507],"study_design_scores_gemma":[0.001212036,0.00002231939,0.0000010953665,0.0000625376,0.00011373401,0.000008862332,0.00015142822,0.9728513,0.025183557,0.0002547254,0.000015157238,0.00012329251],"about_ca_topic_score_codex":0.000036434903,"about_ca_topic_score_gemma":4.7859476e-7,"teacher_disagreement_score":0.38409895,"about_ca_system_score_codex":0.00018735495,"about_ca_system_score_gemma":0.00016126553,"threshold_uncertainty_score":0.40577552},"labels":[],"label_agreement":null}]}