{"meta":{"page":1,"per_page":50,"max_per_page":100,"total":125,"total_is_capped":false,"direct_labels_cover":0,"predictions_cover":125,"direct_label_status":"direct model label, unvalidated","prediction_status":"machine_predicted_unvalidated (Codex and Gemma teacher distillation)","score_status":"score_only:v0-immature-baseline (scores rank; they never assert a category)","snapshot":{"source":"OpenAlex, pinned release, all 482 partitions","release":"2026-06-24","frame_built":"2026-07-12"},"query_hash":"c5a268753f51","filters":{"venue":"Fluid Phase Equilibria"}},"results":[{"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01384354956175308,"gpt":0.2503174805689916,"spread":0.2364739310072385,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000630131,0.0001228148,0.0002321313,0.000062919,0.00003985066,0.00003209516,0.0001342086,0.00003983673,0.0000920793],"category_scores_gemma":[0.00005354189,0.0001151131,0.00003711068,0.0001104736,0.0001179614,0.0001518637,0.00008947032,0.00005104542,0.00001182353],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00004551175,"about_ca_system_score_gemma":0.00005229454,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00200669,"about_ca_topic_score_gemma":0.0001696259,"domain_scores_codex":[0.9987378,0.0001108225,0.0003174088,0.0002726135,0.0002983678,0.0002629531],"domain_scores_gemma":[0.9994984,0.00004781194,0.00007506717,0.0002821037,0.00003685164,0.00005971019],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001073424,0.0004211558,0.006187366,0.00003100426,0.000002274002,0.000003823315,0.00006247029,0.000002114558,0.9919533,0.0001982873,0.0001860987,0.0008448277],"study_design_scores_gemma":[0.001173666,0.0001047092,0.01989718,0.00004192124,0.00001035493,0.000004881847,0.000007436551,0.001547301,0.9759335,0.001066308,0.00009251558,0.0001202093],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9970483,0.001476001,0.0001818652,0.00009526969,0.000171808,0.0001104238,0.00002250108,0.00004400545,0.0008498853],"genre_scores_gemma":[0.9997079,0.000003111301,0.0001432408,0.00001660302,0.00006354267,0.000007749671,0.000003093934,0.000008350954,0.00004641217],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01601972,"threshold_uncertainty_score":0.4694175,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.04236408230057681,"gpt":0.2833351779089501,"spread":0.2409710956083733,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001391124,0.0002011418,0.0002866968,0.00004696105,0.00009937264,0.00002016702,0.00009310649,0.00009405099,0.00004063939],"category_scores_gemma":[0.0001392964,0.0001549945,0.00006830885,0.00009737755,0.0001217545,0.0001512101,0.00007869511,0.0001614341,6.708929e-7],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0000578449,"about_ca_system_score_gemma":0.00003868643,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000133245,"about_ca_topic_score_gemma":0.000004292981,"domain_scores_codex":[0.9990705,0.0000485741,0.0002454566,0.0003143144,0.00009283671,0.0002283323],"domain_scores_gemma":[0.9994174,0.00009775176,0.00006067197,0.0002658328,0.00007152541,0.00008686042],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0006511011,0.00008866814,0.0000316475,0.0002397842,0.0000641206,5.030062e-7,0.0003616175,0.00008369616,0.9969724,0.001108025,0.00005499149,0.0003434482],"study_design_scores_gemma":[0.001108289,0.0005938565,0.00001481726,0.00008421531,0.00008146475,0.000009846689,0.00001780332,0.1517311,0.8457162,0.0003350944,0.0001498983,0.0001573777],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9951853,0.0004390519,0.003283201,0.00003296624,0.00008538634,0.0006644387,0.00009749966,0.0000633795,0.000148735],"genre_scores_gemma":[0.9990217,0.000004046404,0.0007238087,0.00002765787,0.00005554466,0.0000732687,0.0000178028,0.00003199972,0.00004413414],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1516474,"threshold_uncertainty_score":0.6320493,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02751317424787818,"gpt":0.2835518472386181,"spread":0.25603867299074,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00004118853,0.0002216232,0.00025987,0.0001057154,0.0000751711,0.00003515119,0.0001378436,0.00008604505,0.0002170983],"category_scores_gemma":[0.00002647782,0.0002184187,0.00006257041,0.00008916489,0.00007838365,0.0003242375,0.00007223838,0.0002136017,0.0000359659],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00005708561,"about_ca_system_score_gemma":0.00001243847,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001160032,"about_ca_topic_score_gemma":0.00001118881,"domain_scores_codex":[0.999074,0.00003124483,0.0002518297,0.0002189979,0.0001496019,0.0002742706],"domain_scores_gemma":[0.9993718,0.0001764754,0.00002556128,0.0002699863,0.00002325031,0.0001328873],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00004317364,0.000113157,0.001198937,0.00009779689,0.0002078056,0.00002244816,0.0005030591,0.0001787547,0.946069,0.0002735063,0.03414605,0.0171463],"study_design_scores_gemma":[0.002462396,0.00034982,0.01060031,0.0002264391,0.0001385283,0.0001091693,0.00003761294,0.0214154,0.8803022,0.001775721,0.08154232,0.001040096],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9834704,0.000631204,0.005864008,0.00004485732,0.0003286782,0.00005799739,0.00008058208,0.00093173,0.008590571],"genre_scores_gemma":[0.9960346,0.0004206658,0.0006966435,0.00002812435,0.0002944585,0.00003901006,0.00004983883,0.0000573421,0.002379356],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.06576682,"threshold_uncertainty_score":0.8906857,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01006106495538059,"gpt":0.2352345573317335,"spread":0.225173492376353,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000346495,0.000328026,0.0005122742,0.0001921026,0.00003682569,0.00002017884,0.0003898108,0.0002565394,0.0002314337],"category_scores_gemma":[0.0001147604,0.0003540957,0.0001328825,0.0003879145,0.0001529471,0.0002629097,0.0001198395,0.0005317015,0.00001449074],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00004848542,"about_ca_system_score_gemma":0.00007978811,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003164228,"about_ca_topic_score_gemma":0.0004476327,"domain_scores_codex":[0.9980671,0.00006080596,0.0006343252,0.0003614271,0.0002468015,0.0006295375],"domain_scores_gemma":[0.9987288,0.0001117823,0.00006190047,0.0008521617,0.00005951326,0.0001859051],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.00008770702,0.0003231108,0.0003593563,0.0001026324,0.0000763037,0.00002080253,0.0001715797,0.002687047,0.9925129,0.002408488,0.000145507,0.001104536],"study_design_scores_gemma":[0.003548456,0.000147017,0.001545368,0.00005272695,0.00008878205,0.00002713625,0.0000100346,0.8142951,0.172663,0.004896666,0.002187817,0.0005379179],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9931384,0.0006284115,0.0004444596,0.00005262718,0.001591755,0.0003784393,0.0003130956,0.0003831616,0.003069644],"genre_scores_gemma":[0.9989596,0.00002786638,0.0004063943,0.00001003291,0.0002764158,0.00003771039,0.00008102983,0.00007945189,0.0001215078],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.81985,"threshold_uncertainty_score":0.9998911,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02113465683397715,"gpt":0.2715553972514511,"spread":0.2504207404174739,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008079686,0.0002191194,0.0002347823,0.00009724553,0.0000574104,0.00003062517,0.0001442507,0.0001283796,0.0003441487],"category_scores_gemma":[0.00003735693,0.0001998916,0.0000508814,0.0002871392,0.00008609334,0.000218594,0.0001502267,0.000206099,0.00004601509],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002490758,"about_ca_system_score_gemma":0.000009911225,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0005623208,"about_ca_topic_score_gemma":0.0001060722,"domain_scores_codex":[0.9983793,0.0000895377,0.0004308973,0.0004058849,0.0002457274,0.0004486819],"domain_scores_gemma":[0.9994116,0.0001075069,0.0000794842,0.0002263058,0.00001031589,0.0001647933],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0001101754,0.00008095918,0.000696574,0.000006746774,0.0000157918,0.00004309323,0.0004485063,0.2532041,0.7385935,0.0001632029,7.758233e-7,0.006636544],"study_design_scores_gemma":[0.00138202,0.0001010002,0.0001428866,0.00002658673,0.00002194044,0.000007154752,0.00008570773,0.99059,0.003772189,0.00360719,0.00001997207,0.0002433992],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8704442,0.0003483363,0.1259708,0.00006424179,0.00009677059,0.0002752915,0.000003796104,0.00004200037,0.002754557],"genre_scores_gemma":[0.9985427,0.00002170362,0.001085754,0.0001103828,0.00002206424,0.00000496569,0.0000476987,0.00003474656,0.0001300446],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.7373858,"threshold_uncertainty_score":0.8151341,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01286746350392015,"gpt":0.2417468104612967,"spread":0.2288793469573766,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003741894,0.0002075895,0.0002600663,0.00003020273,0.0001343242,0.00001125429,0.000196404,0.0001002092,0.0005010294],"category_scores_gemma":[0.0001147189,0.0001109476,0.00007741694,0.0002983033,0.0006811872,0.00006144735,0.0001675473,0.0001529541,0.0001478863],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00002362502,"about_ca_system_score_gemma":0.000004591092,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00003986017,"about_ca_topic_score_gemma":6.572541e-7,"domain_scores_codex":[0.9985268,0.0003021978,0.0003031855,0.0003014904,0.0002412408,0.0003251046],"domain_scores_gemma":[0.9990187,0.0004668128,0.0001065034,0.0002506216,0.000004458296,0.0001528783],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003981928,0.00009304715,0.003743461,0.000005684331,0.000028045,0.00002124367,0.000143547,0.00003148774,0.9910806,0.00005304161,0.0008204384,0.003581238],"study_design_scores_gemma":[0.002487092,0.006424672,0.001908752,0.00002045181,0.00003784179,0.00005993947,0.000009693617,0.0025241,0.9827793,0.0004946358,0.002978283,0.0002752119],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9934564,0.0008724071,0.00001175139,0.0001725797,0.000235337,0.0002568141,0.000007261141,0.0000225284,0.00496493],"genre_scores_gemma":[0.9989107,0.0005317577,0.00005307536,0.00004363745,0.00007402844,0.00001003208,0.000008567495,0.00001555587,0.0003527003],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.008301245,"threshold_uncertainty_score":0.548592,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01479283670857424,"gpt":0.2328716028253591,"spread":0.2180787661167849,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001004199,0.0001037214,0.000195726,0.0000475175,0.000009543063,0.000004522887,0.0001607283,0.00006757554,0.0001733096],"category_scores_gemma":[0.00002559331,0.00006245614,0.00002872123,0.0002380713,0.0002201499,0.0001319366,0.0001081364,0.0001177988,0.000003201255],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00002745674,"about_ca_system_score_gemma":0.000005792552,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.003215581,"about_ca_topic_score_gemma":0.0001572196,"domain_scores_codex":[0.9986568,0.0002471872,0.0004201032,0.0002321435,0.0002235765,0.0002201709],"domain_scores_gemma":[0.9995531,0.00009141481,0.00006383179,0.0002589615,0.000004542766,0.00002807841],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00009036271,0.0002265126,0.03870213,0.00002097366,0.000003694459,0.000004679332,0.001071072,0.0008310501,0.9588091,0.00003711712,0.00002431798,0.0001789253],"study_design_scores_gemma":[0.002639859,0.0003403547,0.07489321,0.0000535849,0.00002705362,0.00000772615,0.0001340502,0.05177749,0.8625295,0.007187308,0.0002502153,0.000159639],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9945024,0.0002053346,0.00001278222,0.00008268546,0.0000640125,0.000296993,0.000011056,0.000006361523,0.004818401],"genre_scores_gemma":[0.9997247,0.00002207892,0.00007109327,0.000009067538,0.0000178687,0.00001252868,0.00001318305,0.000006317146,0.0001231634],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.09627965,"threshold_uncertainty_score":0.4861018,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02357504903474641,"gpt":0.2141513445500173,"spread":0.1905762955152709,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000195179,0.0004610152,0.0007094563,0.0002472912,0.0001702432,0.00004436117,0.0005220742,0.0002259983,0.0002121188],"category_scores_gemma":[0.0007765216,0.000327673,0.0001431309,0.0005028099,0.000505597,0.0002177136,0.0009951023,0.0003252612,0.00001362491],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001063374,"about_ca_system_score_gemma":0.00002980769,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003488374,"about_ca_topic_score_gemma":0.00005140078,"domain_scores_codex":[0.9975899,0.0001233872,0.0006824469,0.0005683724,0.000472353,0.0005635121],"domain_scores_gemma":[0.9984542,0.0001760995,0.0001805193,0.000827514,0.0001729968,0.0001887327],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002441215,0.0001657752,0.0001022005,0.0002402999,0.0001716,0.000006420328,0.00178388,0.00003173616,0.9937019,0.00009079384,0.001063252,0.002398002],"study_design_scores_gemma":[0.001748387,0.0003554585,0.0005361903,0.0003854682,0.0001470568,0.00004808488,0.0001554039,0.08673985,0.9088914,0.00009322882,0.0004315454,0.000467912],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9533303,0.04471991,0.0001096749,0.0004113152,0.0002731818,0.0005623356,0.0003030291,0.0001274207,0.000162858],"genre_scores_gemma":[0.9957213,0.0001849816,0.0005653625,0.0000969461,0.000173754,0.00004580388,0.00001937816,0.00008549332,0.003106959],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.08670811,"threshold_uncertainty_score":0.9999175,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01783190758186857,"gpt":0.2496691443317508,"spread":0.2318372367498823,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003924106,0.0005899947,0.0008912711,0.0003012713,0.00006494894,0.00007467922,0.0003545994,0.000272757,0.00001369649],"category_scores_gemma":[0.00003583627,0.0005635057,0.0001676698,0.0002945938,0.0001928339,0.000487604,0.0002037042,0.0002903863,0.000006940586],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002413368,"about_ca_system_score_gemma":0.0001057844,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003851208,"about_ca_topic_score_gemma":0.000008532675,"domain_scores_codex":[0.9970552,0.0000810773,0.0009645582,0.0005310252,0.0003992956,0.0009688552],"domain_scores_gemma":[0.9986792,0.00007579326,0.0001158291,0.000705031,0.00005240257,0.0003717419],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0003098391,0.0001064694,0.00005359737,0.0002156488,0.0002408779,0.0000999468,0.0007069343,0.01925775,0.9776354,0.001312694,0.000004690698,0.00005619272],"study_design_scores_gemma":[0.00551902,0.0006066321,0.000009599617,0.0003478924,0.0001840721,0.0002272632,0.0001131511,0.5850312,0.4061454,0.0009055915,0.0001801121,0.0007300201],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9890435,0.002990822,0.002335237,0.00002363885,0.001305561,0.0005543529,0.00009052307,0.0005700943,0.003086289],"genre_scores_gemma":[0.999,0.0000541658,0.0002392834,0.00001631736,0.0003546106,0.00002541525,0.00008697464,0.0001942111,0.00002901862],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.5714899,"threshold_uncertainty_score":0.9996817,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.006833215398056166,"gpt":0.2440023345451085,"spread":0.2371691191470523,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001621632,0.0003305631,0.0003772156,0.0001703835,0.00008055639,0.0001193885,0.000243022,0.0001621478,0.0001807756],"category_scores_gemma":[0.0001070066,0.0002555842,0.0001329794,0.0002351319,0.00004594811,0.000520769,0.00006471241,0.0004003103,0.00009678171],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001325662,"about_ca_system_score_gemma":0.00002339692,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002619928,"about_ca_topic_score_gemma":0.000006489787,"domain_scores_codex":[0.9986482,0.000105539,0.0004083658,0.0002959422,0.000213697,0.0003282666],"domain_scores_gemma":[0.9986833,0.0004694787,0.00007922372,0.0005621905,0.00007461044,0.0001311614],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00007122242,0.0001418082,0.000008215546,0.0003603639,0.00007846385,0.00001513372,0.0002009832,0.00001245976,0.9554909,0.0002512479,0.02702858,0.01634056],"study_design_scores_gemma":[0.001372484,0.0005746731,0.0000271174,0.001081528,0.00006526123,0.00004641941,0.00007116879,0.00422806,0.9892108,0.00005652985,0.002959055,0.0003068819],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9889699,0.0005848603,0.00011189,0.0001318917,0.0009273911,0.0002350378,0.00009365822,0.000675182,0.008270209],"genre_scores_gemma":[0.9972652,0.0001331832,0.0004237412,0.00006454226,0.0002664382,0.0003415986,0.00003293118,0.00008381368,0.001388609],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.03371986,"threshold_uncertainty_score":0.9999896,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.0234199218433064,"gpt":0.27817752028989,"spread":0.2547575984465836,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0004888048,0.0001505939,0.0002793975,0.00003055576,0.0000390871,0.0000060729,0.0003818484,0.00005943864,0.00456234],"category_scores_gemma":[0.00003101626,0.0001016674,0.00006097033,0.000509299,0.0002388284,0.0001344591,0.0003320311,0.0001333596,0.00002866555],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00008324369,"about_ca_system_score_gemma":0.00001990513,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001026768,"about_ca_topic_score_gemma":0.000118614,"domain_scores_codex":[0.9982661,0.0002522392,0.0005312136,0.0002969783,0.0004004809,0.0002529929],"domain_scores_gemma":[0.9991759,0.00005457532,0.0001571028,0.0005284033,0.000007612914,0.00007640592],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002257264,0.00449792,0.06528752,0.000005846533,0.00001724017,0.00001085352,0.00611415,0.0002913245,0.9233279,0.00001083875,0.0001109186,0.00009973574],"study_design_scores_gemma":[0.01049453,0.003082553,0.0445364,0.00004412758,0.00005190941,0.0000167597,0.004967822,0.008177776,0.9272396,0.0004166646,0.0005757373,0.0003961334],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9938036,0.0001465937,0.000003150269,0.00004904279,0.0002342232,0.0006544983,0.000009161782,0.00001175921,0.00508801],"genre_scores_gemma":[0.9997258,0.000005751895,0.00002428644,0.00002206202,0.00001859277,0.00001823012,0.000002814772,0.00001300466,0.0001694396],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.02075112,"threshold_uncertainty_score":0.9963476,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01575006355792355,"gpt":0.2648264665254207,"spread":0.2490764029674971,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002962839,0.0002285801,0.0003726438,0.0002443898,0.00004135344,0.00002094619,0.0002341455,0.0001739681,0.0001383914],"category_scores_gemma":[0.0001259562,0.0001830215,0.00007511793,0.0005324144,0.0001054939,0.0002887487,0.0002193635,0.0006521454,0.00003227242],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00007197011,"about_ca_system_score_gemma":0.00003113026,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003522453,"about_ca_topic_score_gemma":0.0001249893,"domain_scores_codex":[0.9982955,0.00005378744,0.0006555281,0.000317001,0.0002040042,0.0004741557],"domain_scores_gemma":[0.999293,0.0001365335,0.00004936592,0.0003377882,0.00005142455,0.0001319128],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0005588709,0.001070718,0.00009370402,0.00008865394,0.00001205441,0.000006592723,0.00126022,0.0002795432,0.996291,0.0001416401,0.00004050104,0.0001564662],"study_design_scores_gemma":[0.00295515,0.0003909214,0.00005701217,0.00004436165,0.00002108301,0.000005436897,0.00008312759,0.116857,0.878767,0.0003922736,0.0001642079,0.0002624279],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9980857,0.00023625,0.0001218869,0.0001066547,0.000218183,0.0004141083,0.00001145552,0.0000629323,0.00074282],"genre_scores_gemma":[0.9995069,0.00001713327,0.00007352472,0.00002085142,0.0001364214,0.00005894736,0.00004620117,0.00002978267,0.0001102329],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.117524,"threshold_uncertainty_score":0.74634,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"about_ca":false},"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Solubility; Aqueous solution; Hydroxymethyl; Carbon dioxide; Amine gas treating; Inorganic chemistry; Organic chemistry","retraction":null,"screen_n_in":null,"score":{"opus":0.02722178710889789,"gpt":0.242432511409459,"spread":0.2152107243005611,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0003099232,0.0002881161,0.0006878271,0.0003944951,0.00001414156,0.000003140479,0.0004083419,0.000268477,0.00003399867],"category_scores_gemma":[0.0003903529,0.0003108226,0.0001758859,0.0006966462,0.0004145306,0.0001360233,0.0001688072,0.000317935,0.000004299438],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001550737,"about_ca_system_score_gemma":0.0000786302,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002680373,"about_ca_topic_score_gemma":0.00005958348,"domain_scores_codex":[0.9979945,0.00005872529,0.0008185045,0.0003162129,0.0003009206,0.0005110746],"domain_scores_gemma":[0.9986954,0.0001583603,0.00009875356,0.0008927632,0.00007397695,0.00008079194],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00004793533,0.0001722561,0.001180416,0.0001581307,0.00004809166,0.00005542969,0.0003702122,0.001390274,0.9951838,0.0002631455,0.0002469649,0.000883293],"study_design_scores_gemma":[0.001943172,0.0002184472,0.002313622,0.00009738166,0.0000386809,0.00007518278,0.00008027913,0.07701747,0.9165196,0.001140125,0.0001548996,0.0004011404],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9914831,0.004328237,0.0004012701,0.00003594752,0.0003283099,0.0003946055,0.00006326223,0.0006479545,0.002317349],"genre_scores_gemma":[0.9988616,0.0001485504,0.0007828998,0.000005069978,0.00005572664,0.00004176305,0.00001376976,0.00005090879,0.00003972475],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.07866425,"threshold_uncertainty_score":0.9999344,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"about_ca":false},"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada","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","retraction":null,"screen_n_in":null,"score":{"opus":0.08098682265985165,"gpt":0.3007042611278833,"spread":0.2197174384680317,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001092824,0.0001853738,0.000282847,0.00005076786,0.00005735514,0.00001193502,0.0001554879,0.0000751972,0.000101018],"category_scores_gemma":[0.00004743331,0.0001737706,0.00008599407,0.0001442559,0.0000867155,0.0001002791,0.00009203375,0.0001779819,0.000006879657],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001642844,"about_ca_system_score_gemma":0.0000241277,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001161903,"about_ca_topic_score_gemma":0.000003127703,"domain_scores_codex":[0.9987022,0.000028145,0.0003923847,0.0002595037,0.0002467072,0.0003710328],"domain_scores_gemma":[0.9995411,0.00002470761,0.00003430027,0.0002294179,0.00004883557,0.0001216317],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0001012608,0.0005413911,0.000001464044,0.00001875949,0.00001587798,0.000002450959,0.0002091152,0.003414701,0.9925483,0.002276439,0.00008551844,0.0007847468],"study_design_scores_gemma":[0.001121406,0.00009406633,0.000007277444,0.00004766304,0.00001100572,0.000003454077,0.00001975817,0.7914494,0.2054347,0.001613621,0.00003289019,0.0001647507],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.984489,0.001394387,0.01141304,0.000174981,0.00004656335,0.0001782683,0.00002808838,0.0000890845,0.002186554],"genre_scores_gemma":[0.999491,0.000007495562,0.0003004035,0.00004123214,0.00007531607,0.00001284092,0.00002697684,0.00001781753,0.00002687308],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.7880347,"threshold_uncertainty_score":0.708616,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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)","retraction":null,"screen_n_in":null,"score":{"opus":0.02448642559956436,"gpt":0.2230480381641367,"spread":0.1985616125645723,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001977205,0.0002754097,0.0003416224,0.00008251331,0.00008980381,0.00002104491,0.0002199797,0.0001653806,0.0000848795],"category_scores_gemma":[0.00006443934,0.0002274874,0.0001219933,0.000178473,0.000245118,0.0002659155,0.0000530538,0.0001812722,0.000004289014],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00002901815,"about_ca_system_score_gemma":0.00003105405,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001760155,"about_ca_topic_score_gemma":0.000007161012,"domain_scores_codex":[0.9987932,0.00004346663,0.0003911218,0.0002715559,0.000167762,0.0003328238],"domain_scores_gemma":[0.9990281,0.0002812772,0.00005779814,0.0004394699,0.00007158331,0.0001217199],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.001758305,0.000197643,0.0001194621,0.0001394001,0.0006087534,0.000004513842,0.004235236,0.001488189,0.9705162,0.01895452,0.001491785,0.0004859784],"study_design_scores_gemma":[0.002963833,0.0006541454,0.0001297453,0.00006625633,0.0002481871,0.00002528749,0.0001205409,0.9668608,0.02259262,0.003994292,0.002052454,0.0002918825],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9200037,0.002530051,0.06935652,0.0000325517,0.0008214457,0.0009088042,0.0007927535,0.0002431911,0.005310967],"genre_scores_gemma":[0.9989681,0.000138699,0.0004777777,0.000017845,0.0001578898,0.00006983584,0.00005985251,0.00006170382,0.00004826727],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9653726,"threshold_uncertainty_score":0.9276667,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02117697557053975,"gpt":0.2674779367440171,"spread":0.2463009611734773,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":["metaepi_narrow"],"category_scores_codex":[0.003113983,0.001722579,0.00212585,0.0004121567,0.0002328924,0.000171245,0.002735074,0.0007392836,0.008977516],"category_scores_gemma":[0.0001395169,0.001141592,0.0002735888,0.001292949,0.001936238,0.002817348,0.003269271,0.001138352,0.0004730465],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002483743,"about_ca_system_score_gemma":0.0002123055,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0007491354,"about_ca_topic_score_gemma":0.0001483328,"domain_scores_codex":[0.9893711,0.0009620303,0.00208138,0.003061891,0.001926802,0.002596754],"domain_scores_gemma":[0.9930108,0.0005087208,0.0007517973,0.004221275,0.0001476486,0.001359814],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.02344613,0.000948736,0.00006392108,0.0001718257,0.0007162908,0.0002082691,0.001780671,0.001472994,0.968386,0.00008705573,0.001733752,0.000984338],"study_design_scores_gemma":[0.009796868,0.02048403,0.00002839535,0.000271065,0.001014559,0.0005824021,0.000266509,0.007182639,0.8896633,0.0000731513,0.06829497,0.002342091],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9825891,0.003246769,0.0009286517,0.002000578,0.0004305295,0.001773472,0.0004864971,0.0003857467,0.008158668],"genre_scores_gemma":[0.9797286,0.0003514367,0.01267866,0.0008661173,0.0007471847,0.0001251373,0.001146406,0.0004532209,0.003903243],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.0787227,"threshold_uncertainty_score":0.9995521,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02074630209828541,"gpt":0.2780806693986705,"spread":0.2573343673003851,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004171816,0.0003811967,0.0006156414,0.0002743993,0.00008251888,0.00005165466,0.000154051,0.0001484764,0.000004320782],"category_scores_gemma":[0.00006069148,0.000416112,0.00006602611,0.0002883874,0.0000814176,0.0003608215,0.0001315465,0.00009160239,0.000003210804],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001342798,"about_ca_system_score_gemma":0.0002394894,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00006587777,"about_ca_topic_score_gemma":0.00005687953,"domain_scores_codex":[0.9977369,0.00003957427,0.001033227,0.0004605554,0.000273757,0.0004559464],"domain_scores_gemma":[0.9987801,0.0001112529,0.000206626,0.0003647905,0.0001430863,0.0003942008],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0006620999,0.0001169993,0.00001054933,0.0005377354,0.0001621869,0.000001237299,0.002011098,0.02333004,0.9696137,0.001515958,0.00005727911,0.001981163],"study_design_scores_gemma":[0.006246543,0.0009234347,0.0002158955,0.0003199439,0.0001497286,0.00002153151,0.0001474623,0.4450801,0.5438543,0.001348615,0.001058447,0.0006339705],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.7289314,0.0006810202,0.2685737,0.00006825026,0.0002212249,0.001202622,0.000177185,0.0001113257,0.00003323098],"genre_scores_gemma":[0.9907005,0.00003660263,0.008599059,0.00001316306,0.0001037448,0.0001695655,0.0002571851,0.00008817733,0.00003197268],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.4257593,"threshold_uncertainty_score":0.9998291,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01248565757522797,"gpt":0.2400712888333089,"spread":0.227585631258081,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001212489,0.0003051302,0.0003949296,0.0001806807,0.000109441,0.00002898537,0.000180783,0.0001381231,0.00006548752],"category_scores_gemma":[0.00003625122,0.0002532365,0.00009504239,0.0002546033,0.00008879692,0.0003434644,0.00004285285,0.0001519667,0.00001122937],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0000452776,"about_ca_system_score_gemma":0.00003977267,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001115919,"about_ca_topic_score_gemma":0.000003786791,"domain_scores_codex":[0.9985992,0.00003828196,0.0004453182,0.000277416,0.0001521903,0.0004875885],"domain_scores_gemma":[0.9992153,0.0001850782,0.00004562332,0.000334819,0.00009233073,0.0001268527],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0001774831,0.00008816278,0.000005938913,0.00008089372,0.0001556903,0.00001186035,0.0004846167,0.0109698,0.9867889,0.0007877348,0.0001151434,0.0003337495],"study_design_scores_gemma":[0.002916895,0.0002078392,0.00005271484,0.00001974492,0.0000462401,0.00001383907,0.000004106378,0.7881041,0.2051628,0.003074513,0.0001046539,0.0002925576],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9895961,0.0003767648,0.008239184,0.00003417699,0.000328541,0.0005739338,0.0004288737,0.0002650275,0.0001573567],"genre_scores_gemma":[0.9987373,0.0001225371,0.0001598458,0.00002073814,0.00009041103,0.00002908271,0.0005021488,0.00009777248,0.0002401278],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.7816261,"threshold_uncertainty_score":0.999992,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.05376296163383279,"gpt":0.3152869499996069,"spread":0.2615239883657742,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.00175918,0.000502374,0.0008358373,0.0001080995,0.0001581116,0.0001246075,0.000504201,0.000240557,0.0003548475],"category_scores_gemma":[0.0001208608,0.0004406965,0.0001090402,0.0004637506,0.0002848755,0.0006163451,0.000490944,0.0003807286,0.0001469556],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002106109,"about_ca_system_score_gemma":0.00007992371,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.001965846,"about_ca_topic_score_gemma":0.00002984064,"domain_scores_codex":[0.9956931,0.0005090317,0.001174394,0.001008637,0.000835354,0.000779514],"domain_scores_gemma":[0.9978177,0.0001363352,0.0002977759,0.0009662868,0.00005642633,0.0007254925],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.001379591,0.005941661,0.002650285,0.0001097106,0.0002159684,0.0001115717,0.005411456,0.02756208,0.9534357,0.00006326388,0.001667475,0.001451303],"study_design_scores_gemma":[0.01386484,0.003260936,0.0000233394,0.00005450045,0.0001551399,0.00005328409,0.001163817,0.9714684,0.008098248,0.0006864152,0.0005976652,0.0005733623],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9913265,0.001583448,0.001016817,0.00003229442,0.0007110592,0.001455399,0.00008631546,0.0001347064,0.003653486],"genre_scores_gemma":[0.998634,0.00003779832,0.000217928,0.00002312572,0.0001543172,0.00004752312,0.00004444718,0.0000689571,0.0007718617],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9453374,"threshold_uncertainty_score":0.9998045,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02452646739691206,"gpt":0.2600568196753957,"spread":0.2355303522784836,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004100479,0.0003282115,0.0002571079,0.00004598037,0.0002264737,0.0001252827,0.0005404421,0.0001157178,0.0003995936],"category_scores_gemma":[0.00008733966,0.0002032918,0.0002144983,0.0002752434,0.0001053036,0.0002438602,0.00005391801,0.0002062938,0.0001533502],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00007977635,"about_ca_system_score_gemma":0.00002765382,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000005840303,"about_ca_topic_score_gemma":0.00000648229,"domain_scores_codex":[0.9984633,0.00006745832,0.0003668428,0.0002879268,0.0002936843,0.0005208245],"domain_scores_gemma":[0.9982468,0.0008275248,0.00004663024,0.0007393948,0.0000472204,0.00009239505],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0007680647,0.0003522915,0.00001218608,0.00008065658,0.0003774647,0.00001621479,0.001200698,0.009379158,0.8435713,0.09754312,0.03291983,0.01377903],"study_design_scores_gemma":[0.001499784,0.0001854202,0.00001276775,0.00002397757,0.00006132329,0.00002213969,0.00008703613,0.9401804,0.00774545,0.00887091,0.04102498,0.0002858147],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8697829,0.0005082647,0.1196425,0.001315605,0.001229812,0.00108302,0.00007757766,0.0005690979,0.005791255],"genre_scores_gemma":[0.9976311,0.00007747341,0.0003343981,0.0003606917,0.000715651,0.0002404669,0.00008736545,0.0001124906,0.0004403592],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9308012,"threshold_uncertainty_score":0.8289999,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01038084413420544,"gpt":0.2736861500438323,"spread":0.2633053059096269,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007921978,0.0001456204,0.0004927209,0.0001921442,0.00004395812,0.0000201843,0.0001357448,0.00008234773,0.0003137344],"category_scores_gemma":[0.0003058575,0.0001298941,0.00009941698,0.0004965022,0.0002668171,0.000153476,0.0001035216,0.0000590411,0.000003477769],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00002394917,"about_ca_system_score_gemma":0.00002574501,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003103829,"about_ca_topic_score_gemma":0.0003891575,"domain_scores_codex":[0.9983975,0.0002817102,0.0005873007,0.0003323186,0.0002116915,0.0001894692],"domain_scores_gemma":[0.9990506,0.0002195625,0.0002161237,0.0003657219,0.0000966591,0.00005139295],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0001542645,0.0001961214,0.01667222,0.00007787423,0.00004594358,5.297255e-7,0.001524229,0.0005293665,0.9796289,0.0003121765,0.00001090084,0.000847469],"study_design_scores_gemma":[0.001900221,0.0002571815,0.05919018,0.0000391193,0.0002404961,0.000001055893,0.0001000135,0.738306,0.1965618,0.003097221,0.00004842151,0.0002583115],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.980124,0.0002618478,0.01873245,0.00006905243,0.0001322918,0.0002162937,0.00005790354,0.00003200708,0.0003741319],"genre_scores_gemma":[0.9995773,0.00002602956,0.0002408307,0.00001712274,0.0000161819,0.000007743435,0.00003225111,0.000009274246,0.00007325639],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.7830671,"threshold_uncertainty_score":0.5296929,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02403971104064382,"gpt":0.3150910408284916,"spread":0.2910513297878478,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0002093786,0.0003771526,0.0003534981,0.0001054474,0.0001261937,0.0001918768,0.0003363587,0.0002256998,0.0007020832],"category_scores_gemma":[0.0000171097,0.0004023618,0.0001376776,0.0002048999,0.0001322092,0.001047089,0.00001659014,0.0001397677,0.0001567311],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00006897298,"about_ca_system_score_gemma":0.00007279564,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001725776,"about_ca_topic_score_gemma":0.00003208533,"domain_scores_codex":[0.9982511,0.00003711456,0.0004522677,0.0004409094,0.0001754946,0.0006431329],"domain_scores_gemma":[0.9989269,0.00003910315,0.00005497726,0.0006052386,0.0001142166,0.0002595643],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0005497978,0.0001571529,0.00003151697,0.00007448207,0.00009200323,0.000002340091,0.0004965613,0.0005045376,0.9810655,0.0003142336,0.001699714,0.01501219],"study_design_scores_gemma":[0.00471485,0.0009900244,0.00004598299,0.00001931399,0.00006240299,0.000007910538,0.00001869637,0.9256771,0.04278417,0.001381436,0.02381854,0.0004795685],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8907167,0.0001895305,0.1015349,0.0000340796,0.001219395,0.0009310838,0.000427341,0.0008428819,0.004104119],"genre_scores_gemma":[0.9941264,0.000006272286,0.002305703,0.00005417217,0.002063833,0.00009130171,0.0003974434,0.0001701716,0.0007846553],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9382813,"threshold_uncertainty_score":0.9998428,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02416153069592827,"gpt":0.2742147883045749,"spread":0.2500532576086466,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001281795,0.000196969,0.0003180181,0.00001503252,0.0001909459,0.00001597548,0.0003579713,0.0001480078,0.0004662384],"category_scores_gemma":[0.0002205078,0.0001565652,0.0001577513,0.0001305017,0.0001748373,0.00005401511,0.0001188741,0.0002062435,0.000001590168],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00005244975,"about_ca_system_score_gemma":0.00009688338,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00003334232,"about_ca_topic_score_gemma":0.000001758186,"domain_scores_codex":[0.9988741,0.00001665168,0.0003347851,0.0002746425,0.000191107,0.0003086747],"domain_scores_gemma":[0.9990147,0.0001682601,0.00008456915,0.0005362489,0.0001045985,0.00009163195],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00008173235,0.0001112972,0.00001811074,0.00013301,0.00007295562,0.000003102147,0.0002017672,0.00009092774,0.9975554,0.000573341,0.001096008,0.00006228557],"study_design_scores_gemma":[0.001524374,0.00003513746,0.000003587482,0.0000347836,0.00004859243,0.00006848425,0.00000856012,0.3544949,0.6365342,0.005779675,0.001297165,0.0001705631],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9707523,0.00008082863,0.0261197,0.0000794538,0.0001426885,0.0001460119,0.0004689095,0.00005940592,0.002150698],"genre_scores_gemma":[0.9853979,0.000002899299,0.01389354,0.0001020999,0.0002622546,0.00001808496,0.0001336406,0.00003999326,0.0001495272],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.3610213,"threshold_uncertainty_score":0.6384544,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.006500670959081389,"gpt":0.2482529252321483,"spread":0.2417522542730669,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001459847,0.0002455976,0.0002711766,0.00005634639,0.0001004788,0.00006418672,0.0001362092,0.0001244236,0.0002786928],"category_scores_gemma":[0.00002074143,0.0001876754,0.00004325899,0.0001709631,0.0002367609,0.0002943009,0.00006757314,0.0001718779,0.00002412086],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00003797813,"about_ca_system_score_gemma":0.00003419837,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001768701,"about_ca_topic_score_gemma":0.0000514948,"domain_scores_codex":[0.9989633,0.00005460951,0.0002452479,0.0002663087,0.00021515,0.0002553632],"domain_scores_gemma":[0.9992329,0.00007116563,0.0000591117,0.0004280458,0.0001213981,0.00008733136],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002154313,0.0000520165,0.00002158489,0.00005743829,0.0001192835,0.00001661668,0.0005160681,0.00006218485,0.9069638,0.0001214716,0.08839089,0.003463265],"study_design_scores_gemma":[0.002945293,0.0007234229,0.00003178046,0.00009196257,0.00008292853,0.00009060696,0.00004355818,0.0762314,0.8728394,0.0002019536,0.04639759,0.000320144],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9894021,0.00169472,0.002841321,0.00008119908,0.0002156403,0.0005682936,0.0001792851,0.0004080533,0.004609378],"genre_scores_gemma":[0.9854532,0.0001159399,0.01119468,0.00009350169,0.000472737,0.00007224132,0.00008743124,0.00008608344,0.002424122],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.07616922,"threshold_uncertainty_score":0.7653182,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01946892503692075,"gpt":0.3080251763614926,"spread":0.2885562513245719,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0001547698,0.0003202034,0.0003536612,0.0001062463,0.0003293537,0.0001408091,0.0003083554,0.0002051631,0.003172042],"category_scores_gemma":[0.00006001831,0.0003222501,0.0002632132,0.000304431,0.0001385293,0.0003654289,0.0001168207,0.000226424,0.000277285],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0003338183,"about_ca_system_score_gemma":0.0001575694,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00005825645,"about_ca_topic_score_gemma":0.000007638832,"domain_scores_codex":[0.9978899,0.00001592085,0.000506512,0.0006015833,0.0004378318,0.0005482497],"domain_scores_gemma":[0.9988299,0.00002142903,0.0001510801,0.0005980324,0.00008531033,0.000314252],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002549792,0.001513475,0.0004818498,0.00005652094,0.00008054025,0.0001048135,0.0001725755,0.00004840846,0.9851041,0.00003172422,0.0009477754,0.01120319],"study_design_scores_gemma":[0.02254164,0.0003133753,0.00005090461,0.0001569276,0.0006424866,0.0001668226,0.00005308489,0.007103181,0.9246755,0.0002105795,0.04347994,0.0006055465],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9844049,0.0009335991,0.0004991771,0.0001158289,0.0001949322,0.00002132584,0.000418444,0.0005019995,0.0129098],"genre_scores_gemma":[0.9798955,0.00003345756,0.0002480767,0.00007820196,0.000679129,0.00007717331,0.0007164443,0.0000575386,0.01821448],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.06042864,"threshold_uncertainty_score":0.9999229,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.0470921864593373,"gpt":0.3006810624457745,"spread":0.2535888759864372,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001838613,0.0002201412,0.0002624481,0.00005938759,0.00007494996,0.00001543903,0.0002583854,0.0001822848,0.0001462758],"category_scores_gemma":[0.00007199368,0.0001954002,0.0001255414,0.0001900868,0.00006705878,0.0001883634,0.0001267506,0.0001871801,0.0000222337],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001505258,"about_ca_system_score_gemma":0.00004698749,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001913728,"about_ca_topic_score_gemma":0.00001078017,"domain_scores_codex":[0.9984513,0.00003177204,0.0004554345,0.0004086605,0.000156121,0.0004967012],"domain_scores_gemma":[0.9992386,0.00007217023,0.00005327744,0.0004387862,0.00004494803,0.0001522133],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003624146,0.0003253121,0.00002576114,0.00004663223,0.00001165228,0.000002606095,0.0006399337,0.00004563975,0.9867397,0.01109158,0.0005751206,0.0001336373],"study_design_scores_gemma":[0.002608775,0.000290328,0.00002094851,0.0001502418,0.00002585956,0.000005924076,0.00005261567,0.1747769,0.8099706,0.001672703,0.01005892,0.0003662498],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9858443,0.0003498801,0.006203115,0.0002124156,0.0002042787,0.0005679374,0.00003022832,0.0002368752,0.006350941],"genre_scores_gemma":[0.9972365,0.00001119701,0.001083779,0.0001017587,0.0002959387,0.0004838936,0.00006958764,0.00005563203,0.0006616639],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.1767692,"threshold_uncertainty_score":0.7968188,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02190670265569243,"gpt":0.2518006419278381,"spread":0.2298939392721456,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0001140533,0.0002934651,0.0003239712,0.0002000177,0.00005335014,0.00008226879,0.0002693365,0.0001680772,0.001051077],"category_scores_gemma":[0.0000384087,0.0003020822,0.0000925671,0.0002724249,0.00004840663,0.001017668,0.00002893362,0.000127993,0.00008121879],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00008822173,"about_ca_system_score_gemma":0.00004692834,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00009489643,"about_ca_topic_score_gemma":0.000003070827,"domain_scores_codex":[0.9985102,0.00009379839,0.0004707778,0.0003095372,0.0002975029,0.0003181516],"domain_scores_gemma":[0.9989479,0.00008578954,0.00007954962,0.0006201951,0.00009974018,0.0001668102],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.00008444987,0.0002267646,0.00009026586,0.00003915102,0.00003379504,0.000003036237,0.0002091861,0.006570993,0.9916009,0.0001643637,0.00005133778,0.0009257534],"study_design_scores_gemma":[0.001166389,0.0001723619,0.0005258427,0.00006907911,0.0000262534,0.000001032403,0.000009919538,0.7747236,0.2222523,0.0006891306,0.0001215317,0.0002425214],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9786231,0.00004039349,0.01897391,0.00003391699,0.0005917032,0.0004315679,0.0002843988,0.0003455163,0.0006754752],"genre_scores_gemma":[0.9970276,0.000006623026,0.000808398,0.00006531816,0.0003795644,0.00002913771,0.001528252,0.00009923934,0.00005586881],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.7693486,"threshold_uncertainty_score":0.9999431,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02503082661455682,"gpt":0.2573458540656983,"spread":0.2323150274511415,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001828662,0.0002998966,0.00030353,0.0001491707,0.0001248093,0.0001005591,0.0001747567,0.0001592211,0.0001665172],"category_scores_gemma":[0.00002847429,0.0003355645,0.000159748,0.0002035215,0.00005008797,0.0009331984,0.0000246397,0.0001473982,0.00005232202],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002691924,"about_ca_system_score_gemma":0.00003775787,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000008564525,"about_ca_topic_score_gemma":0.000006215557,"domain_scores_codex":[0.9984931,0.0000342602,0.0004716017,0.000290779,0.0002061825,0.0005040203],"domain_scores_gemma":[0.9993375,0.00005650127,0.00002633407,0.0003778758,0.00002592026,0.0001758824],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.00007341235,0.0001138328,0.000009055093,0.00006934501,0.00008165371,0.000001575992,0.0003065586,0.01538655,0.9814833,0.0005547114,0.0008657706,0.001054272],"study_design_scores_gemma":[0.001931937,0.0001471753,0.00003034126,0.00004230247,0.00007490022,0.00003227437,0.00001295012,0.9060481,0.08809496,0.001245482,0.002054998,0.0002846199],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.881099,0.0001224908,0.1149841,0.00007138398,0.0009267854,0.0005285442,0.0002213106,0.0007664097,0.001279943],"genre_scores_gemma":[0.9890056,0.00001175003,0.009037483,0.00006585455,0.001524727,0.00002979603,0.000157469,0.0001224101,0.00004494251],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.8933883,"threshold_uncertainty_score":0.9999096,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01939888067042767,"gpt":0.2713483187051519,"spread":0.2519494380347242,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002214683,0.0002182442,0.0003152857,0.0001791358,0.00002391669,0.00002603608,0.000168862,0.0001097774,0.0001503404],"category_scores_gemma":[0.00004347063,0.0001933899,0.00009051241,0.0001932844,0.00005612582,0.0005490791,0.00002092766,0.00005616383,0.00001531483],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0000952775,"about_ca_system_score_gemma":0.00003153271,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000007505331,"about_ca_topic_score_gemma":0.000007980453,"domain_scores_codex":[0.9986411,0.00003014947,0.0005427582,0.0002385509,0.0001383149,0.0004090994],"domain_scores_gemma":[0.9993876,0.0001587459,0.00006249624,0.0002603712,0.00005134611,0.00007939822],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0003326215,0.00007874408,0.0002440957,0.0001103107,0.00003551999,0.000003740427,0.0007121839,0.0007185048,0.9799834,0.0002200035,0.00009855408,0.01746229],"study_design_scores_gemma":[0.007075737,0.0002980978,0.0002438622,0.0002024136,0.00002485115,0.000002614133,0.00001372856,0.8937007,0.09203388,0.004430505,0.001648599,0.0003250199],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8989306,0.0002230383,0.09928827,0.00003219362,0.0003973749,0.0003652298,0.0002967669,0.0001697141,0.0002967854],"genre_scores_gemma":[0.9987878,0.00003061568,0.0007130327,0.00001169986,0.00009546548,0.00004897856,0.0001077144,0.00007549779,0.0001292268],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.8929822,"threshold_uncertainty_score":0.7886213,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02291024168438794,"gpt":0.258529003119258,"spread":0.2356187614348701,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005186241,0.0003273394,0.0004247119,0.0002304848,0.00004216373,0.00002468929,0.0001271744,0.0001423578,0.000005202533],"category_scores_gemma":[0.00007561529,0.0003263931,0.00004904182,0.0002505181,0.0002570095,0.0005953632,0.0001107073,0.000189283,0.000001035757],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001310825,"about_ca_system_score_gemma":0.00003895967,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00008315157,"about_ca_topic_score_gemma":0.0000102934,"domain_scores_codex":[0.998221,0.0001381293,0.0006223639,0.0003192276,0.000193794,0.0005054522],"domain_scores_gemma":[0.9992024,0.0001005386,0.00008186656,0.000347963,0.00001389884,0.0002533547],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.001921094,0.0002259958,0.0005592948,0.00008344141,0.0000375537,0.000004764755,0.004441059,0.00003266659,0.9922521,0.0001874107,0.000004720893,0.0002499651],"study_design_scores_gemma":[0.004404087,0.0003879326,0.0004782991,0.0001258781,0.00002344558,0.00001893044,0.0001639285,0.4373706,0.5566054,0.0001309582,0.00001052589,0.0002800601],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.994049,0.004012438,0.00007384021,0.00002330945,0.0003608375,0.000464813,0.00006462124,0.0001740016,0.0007772131],"genre_scores_gemma":[0.9995968,0.00004098201,0.00007647328,0.00001155682,0.0001054055,0.00004135851,0.00004805813,0.00006411104,0.00001526488],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.4373379,"threshold_uncertainty_score":0.9999188,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"about_ca":false},"ca_institutions":"University of Regina","funders":"","keywords":"Asphaltene; Porous medium; Dissolution; Chemistry; Precipitation; Porosity; Enhanced oil recovery; Chemical engineering; Organic chemistry","retraction":null,"screen_n_in":null,"score":{"opus":0.0255903795824845,"gpt":0.2688919306569379,"spread":0.2433015510744534,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003054101,0.00014679,0.0003114636,0.00009505438,0.0000281466,0.000011986,0.000155449,0.000110977,0.0006056834],"category_scores_gemma":[0.0002158687,0.0001463107,0.00005337073,0.0002056099,0.00009659122,0.0002236831,0.0000556058,0.0001162797,0.000006054593],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00003653516,"about_ca_system_score_gemma":0.00006734265,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002502722,"about_ca_topic_score_gemma":0.00004382599,"domain_scores_codex":[0.9988207,0.00002682921,0.000419899,0.0003364181,0.0001809173,0.0002152364],"domain_scores_gemma":[0.9992865,0.00007749769,0.0001529606,0.0003168288,0.00006795614,0.00009827814],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003077057,0.0004981969,0.01378262,0.0002567274,0.0000487509,0.00003195951,0.003308777,0.000001520551,0.9675493,0.00003230302,0.0001267255,0.01405536],"study_design_scores_gemma":[0.00987538,0.0002896678,0.01562992,0.0004313894,0.0003649888,0.00003387109,0.001119379,0.01382645,0.9533308,0.004008366,0.0002802009,0.0008096175],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9859463,0.000518518,0.00006333075,0.00002515016,0.00005091965,0.00001359105,0.00004023766,0.00003670114,0.01330527],"genre_scores_gemma":[0.9983531,0.00002888638,0.0008575388,0.00001379868,0.00005971143,0.000006861518,0.00006003541,0.0000150254,0.0006050139],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01421859,"threshold_uncertainty_score":0.6631809,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.06133714042864848,"gpt":0.2957677837707748,"spread":0.2344306433421263,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006867339,0.0002126775,0.0002100179,0.00003311634,0.0002698125,0.00007227094,0.0001176335,0.0001058943,0.0002658405],"category_scores_gemma":[0.00001997218,0.0001885751,0.00007071607,0.0001243576,0.0001331705,0.0003547954,0.00008727855,0.0001016244,0.00009676097],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0004576948,"about_ca_system_score_gemma":0.00003781234,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001156815,"about_ca_topic_score_gemma":0.00001192651,"domain_scores_codex":[0.9983875,0.00009795921,0.0003332185,0.0004057626,0.0003946739,0.0003809117],"domain_scores_gemma":[0.9993458,0.00003024697,0.0001209545,0.0002113959,0.0000340734,0.0002574765],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0002199446,0.0003067627,0.00003498359,0.000007335932,0.00004572863,0.00000468129,0.001936405,0.009454009,0.9857342,0.0005436933,0.001260912,0.000451318],"study_design_scores_gemma":[0.003126029,0.0003760769,0.00002020249,0.00002090141,0.00004743514,0.000009454332,0.000145259,0.9720592,0.01478166,0.007438045,0.0016818,0.0002939099],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9801503,0.001057655,0.01485809,0.0002359712,0.0003570871,0.0006806778,0.00007028919,0.00007434793,0.002515582],"genre_scores_gemma":[0.9981757,0.00002690083,0.0008662863,0.0000714795,0.00009942874,0.000106168,0.0001274827,0.00003226231,0.0004942997],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9709526,"threshold_uncertainty_score":0.7689868,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01378004607131225,"gpt":0.2465689132995874,"spread":0.2327888672282752,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0001089138,0.0003514925,0.0004863097,0.00004324533,0.00007353175,0.00003257433,0.0009898279,0.0001748342,0.0006196553],"category_scores_gemma":[0.0001668203,0.0002522132,0.0003624601,0.0004148902,0.0001546256,0.0001730837,0.000587257,0.0003659407,0.0004876735],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002702904,"about_ca_system_score_gemma":0.00005564547,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002050316,"about_ca_topic_score_gemma":0.000006664427,"domain_scores_codex":[0.9977784,0.00007037395,0.0006558086,0.0004842378,0.0004339039,0.0005772632],"domain_scores_gemma":[0.9982018,0.0002344281,0.0001046123,0.001088018,0.00008475604,0.0002864084],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001283314,0.000252711,0.000009058761,0.00007231952,0.00007855857,0.000001482028,0.0003555543,0.001049744,0.9894013,0.003802778,0.003252995,0.001595174],"study_design_scores_gemma":[0.001180815,0.00007393709,0.00002236572,0.0002536011,0.00007719338,0.000005310945,0.00003417555,0.4644426,0.516291,0.0004865792,0.01674453,0.0003879796],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9822192,0.0004218486,0.002939192,0.0008632377,0.0005597214,0.0004145729,0.0004239659,0.000352014,0.0118062],"genre_scores_gemma":[0.9961382,0.000002008279,0.0006732754,0.0002222253,0.001147868,0.00004814185,0.00004953246,0.00007463048,0.001644129],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.4731103,"threshold_uncertainty_score":0.999993,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"about_ca":false},"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Aqueous solution; Solubility; Inorganic chemistry; Ferrous; Kraft process; Ferric; Sulfur; Chelation; Data scrubbing; Kraft paper; Organic chemistry; Chemical engineering","retraction":null,"screen_n_in":null,"score":{"opus":0.04004587153872678,"gpt":0.3222535110808927,"spread":0.2822076395421659,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008584767,0.0002369236,0.0007685855,0.0002271158,0.00005948662,0.00001097945,0.0002391294,0.00007119971,0.0001085905],"category_scores_gemma":[0.0001275781,0.0002081951,0.0002019431,0.0007278838,0.0002570085,0.0001735027,0.00006440741,0.0001405251,0.00000108235],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00007077186,"about_ca_system_score_gemma":0.00005202183,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002475193,"about_ca_topic_score_gemma":0.0003314273,"domain_scores_codex":[0.9978864,0.0001977331,0.00101646,0.0002364129,0.0003139393,0.0003490865],"domain_scores_gemma":[0.998625,0.0005364861,0.0001608403,0.0005053098,0.0001101218,0.00006228633],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.00005486221,0.0002422254,0.00008253885,0.000212277,0.0001481582,7.730383e-7,0.002861412,0.06689468,0.9268385,0.0001804739,0.0001530387,0.002331073],"study_design_scores_gemma":[0.001488635,0.00006737975,0.0003154672,0.00007120721,0.0001671811,0.000004544283,0.0003027998,0.607952,0.3889553,0.0002172604,0.0002761594,0.0001820858],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8160842,0.004329869,0.1785939,0.0001437814,0.00009115832,0.0003199507,0.0002139433,0.00004610411,0.000177037],"genre_scores_gemma":[0.9888321,0.0001274752,0.01088193,0.00001121126,0.00004958426,0.00001348756,0.00002922158,0.00003365744,0.00002133404],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.5410573,"threshold_uncertainty_score":0.8489948,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02472284902676108,"gpt":0.2799381050907989,"spread":0.2552152560640378,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0001413944,0.0003540733,0.0003302905,0.0001050609,0.00009559168,0.00005830732,0.0004943735,0.0001860926,0.0009594213],"category_scores_gemma":[0.0001049992,0.0002744678,0.0002465033,0.0002581035,0.00009030329,0.0005027354,0.00006807258,0.0002181309,0.0001785475],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001602467,"about_ca_system_score_gemma":0.00003092668,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002415623,"about_ca_topic_score_gemma":0.000001529565,"domain_scores_codex":[0.9983111,0.00004530599,0.0005659805,0.0002678277,0.0003583836,0.0004514115],"domain_scores_gemma":[0.9987544,0.0002165402,0.0001299503,0.0005798324,0.0001011261,0.0002181081],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00106373,0.0003925239,0.000003913362,0.00002967147,0.00009472271,0.000004638838,0.0006689794,0.001882113,0.9789924,0.00004888332,0.015585,0.001233398],"study_design_scores_gemma":[0.00242834,0.0007905466,0.000002257381,0.00004999088,0.00004056809,0.000002740894,0.00003180735,0.3591881,0.637016,0.00009018706,0.000139607,0.0002198721],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.995368,0.0008477342,0.0008482849,0.00007374429,0.0002201062,0.0003448908,0.0007239123,0.0003605326,0.001212775],"genre_scores_gemma":[0.9991699,0.0001357378,0.000133207,0.00002339467,0.0001037292,0.00003595375,0.0001570733,0.00006919566,0.0001718511],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.357306,"threshold_uncertainty_score":0.9999707,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"about_ca":false},"ca_institutions":"University of Toronto","funders":"Natural Sciences and Engineering Research Council of Canada; McLean Foundation","keywords":"Chemistry; Alkylphenol; UNIFAC; Microemulsion; Alkyl; Phase (matter); Thermodynamics; Activity coefficient; Organic chemistry; Chromatography; Pulmonary surfactant; Phase equilibrium; Aqueous solution","retraction":null,"screen_n_in":null,"score":{"opus":0.06947267802274207,"gpt":0.3167720959125901,"spread":0.247299417889848,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001228328,0.0002248359,0.0004008067,0.00003399482,0.0001647485,0.00008391695,0.000396609,0.0001035251,0.00004165975],"category_scores_gemma":[0.0002356468,0.0001154284,0.00007885099,0.0002135944,0.0005406503,0.0001978199,0.000119054,0.0001775945,0.000001323304],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00002089659,"about_ca_system_score_gemma":0.000102321,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003603507,"about_ca_topic_score_gemma":0.00008650038,"domain_scores_codex":[0.9981795,0.0002157117,0.0006485357,0.0002685241,0.0003752408,0.0003124661],"domain_scores_gemma":[0.9981591,0.0007854702,0.0002736033,0.0005556272,0.0001162028,0.0001100639],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.002060289,0.0005561471,0.0004265772,0.00007579079,0.00008686807,0.00000735514,0.006461337,0.0001293352,0.9847588,0.001000378,0.0007763875,0.003660723],"study_design_scores_gemma":[0.07065913,0.0006259825,0.0001256519,0.0008060751,0.0004277386,0.000112664,0.01672349,0.4259658,0.4625517,0.01356266,0.00753419,0.0009048349],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.991558,0.005148393,0.00004652661,0.0003923159,0.00009050955,0.0003509388,0.0003240613,0.00001839361,0.002070878],"genre_scores_gemma":[0.9991692,0.0003027455,0.000029333,0.0000405426,0.00005339918,0.0000374473,0.00002245697,0.00002102922,0.000323796],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.5222071,"threshold_uncertainty_score":0.4707034,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02211227391679179,"gpt":0.2691221513533535,"spread":0.2470098774365617,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0001124036,0.0001804709,0.0003129426,0.0000401118,0.00002992279,0.00001083961,0.0002706009,0.0001136865,0.001283452],"category_scores_gemma":[0.00007785001,0.0001338709,0.0001131432,0.0001615809,0.0001414632,0.0001503462,0.0001867646,0.0002292354,0.00007337143],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0000607254,"about_ca_system_score_gemma":0.00001651467,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0004062691,"about_ca_topic_score_gemma":0.000009365011,"domain_scores_codex":[0.9986143,0.00002812709,0.0004240941,0.0002943917,0.0001990176,0.0004400335],"domain_scores_gemma":[0.9993016,0.00010891,0.00002849468,0.0004020731,0.00004315445,0.0001158429],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003178941,0.0005076365,0.00009699036,0.00007082881,0.00002549827,0.000005381712,0.000144847,0.001578066,0.9948562,0.001739908,0.0004793003,0.0001773828],"study_design_scores_gemma":[0.001226978,0.00005281508,0.00007518006,0.00003622378,0.00001909076,0.000003007608,0.000008019135,0.04288637,0.942646,0.009994301,0.002845739,0.0002062374],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9938283,0.0001389705,0.001186454,0.0003299039,0.0002114886,0.000140693,0.00002242478,0.0001059763,0.004035781],"genre_scores_gemma":[0.9980932,0.000009977082,0.00009346198,0.00005861118,0.0002713,0.00002090295,0.00004978237,0.00002506269,0.001377661],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.05221022,"threshold_uncertainty_score":0.9996295,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02913722145445037,"gpt":0.3008340506116949,"spread":0.2716968291572445,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0005795452,0.0002745287,0.0003149978,0.000169044,0.00008588426,0.00007938794,0.000156246,0.0001666527,0.0001366403],"category_scores_gemma":[0.0002442038,0.000305854,0.00005774259,0.0003331065,0.0001273138,0.0005174838,0.00009151896,0.0002222779,0.00001276787],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001596173,"about_ca_system_score_gemma":0.00004208727,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002904608,"about_ca_topic_score_gemma":0.00001278107,"domain_scores_codex":[0.9982007,0.0001316039,0.0004977362,0.0003663529,0.0002435321,0.000560115],"domain_scores_gemma":[0.9992913,0.000183918,0.00001429634,0.0002885325,0.00003807928,0.000183895],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0003743989,0.0002805395,0.006998882,0.00006055195,0.00004121053,0.00005900269,0.0004775656,0.006780826,0.981268,0.000844122,0.00001278677,0.002802068],"study_design_scores_gemma":[0.003355009,0.0000729693,0.001406432,0.0001042627,0.00003955552,0.00005427186,0.00003621116,0.9860076,0.005619588,0.003001588,0.00002297713,0.0002795087],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9734193,0.0002406152,0.02414085,0.000009691006,0.0008129453,0.0003506267,0.00005530285,0.0003653459,0.0006052926],"genre_scores_gemma":[0.9992134,0.00002039794,0.0003709449,0.00001787443,0.0002073594,0.00001067357,0.00008829286,0.00006346471,0.000007577673],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9792268,"threshold_uncertainty_score":0.9999394,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01631444379764697,"gpt":0.2881692813599114,"spread":0.2718548375622645,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.000468165,0.0007540553,0.0007092544,0.0002132274,0.0005965941,0.0006001686,0.001746686,0.0003506041,0.0003110846],"category_scores_gemma":[0.0000473996,0.0005880251,0.0003317179,0.00006963447,0.0002117285,0.001533635,0.0002895013,0.0003249413,0.0001404103],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001224669,"about_ca_system_score_gemma":0.00003712117,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00007026916,"about_ca_topic_score_gemma":0.0000385612,"domain_scores_codex":[0.996662,0.00005969726,0.0006999582,0.0007574612,0.0004032298,0.001417612],"domain_scores_gemma":[0.9965663,0.00006969531,0.00009530424,0.002653542,0.00008319044,0.0005319463],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0003458918,0.0005958197,0.00001006851,0.00008255224,0.0003530537,0.00008635426,0.0003278433,0.0001224152,0.9772425,0.0002117204,0.002625101,0.01799667],"study_design_scores_gemma":[0.01061599,0.0005048457,0.000009498926,0.00003255474,0.0001436426,0.00002605724,0.000007964732,0.6498789,0.325705,0.005817724,0.006590882,0.0006669345],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8533695,0.0002609181,0.1391733,0.0001508737,0.002210269,0.001054408,0.0009227016,0.0009270398,0.001930999],"genre_scores_gemma":[0.9916937,0.00001788013,0.003926255,0.0001119085,0.001450084,0.0002571461,0.001818656,0.0003148707,0.0004095402],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.6515375,"threshold_uncertainty_score":0.9996571,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":false,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.02982118339349113,"gpt":0.2945343826236702,"spread":0.2647131992301791,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0006446447,0.001165297,0.001203505,0.0002932276,0.0004432833,0.0001444371,0.00160553,0.000850049,0.003635648],"category_scores_gemma":[0.0007411469,0.0008110994,0.000754815,0.0008459132,0.000262843,0.0009721317,0.0006853582,0.0005007787,0.0006568913],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0004780139,"about_ca_system_score_gemma":0.0006123784,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00005618672,"about_ca_topic_score_gemma":0.00001744619,"domain_scores_codex":[0.9935378,0.0001295373,0.001726111,0.001766617,0.0007561645,0.002083716],"domain_scores_gemma":[0.9952818,0.0008471756,0.0003825149,0.002189267,0.0004586797,0.0008406108],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.00696201,0.000555447,0.00000234855,0.0002359419,0.0002532316,0.000037601,0.0002130638,0.00009777967,0.9445755,0.008274389,0.0366375,0.002155121],"study_design_scores_gemma":[0.00886844,0.003814364,0.000003800585,0.0005488143,0.0002456403,0.0001052824,0.00007137063,0.0210308,0.7266568,0.0005289641,0.2364367,0.001688974],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9691367,0.003176352,0.01452337,0.004414606,0.001687311,0.002171875,0.001020354,0.001473344,0.002396129],"genre_scores_gemma":[0.9633328,0.0005187611,0.00322322,0.001001768,0.003606803,0.001552674,0.0004701576,0.0005521986,0.0257416],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.2179188,"threshold_uncertainty_score":0.999434,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01853311577418848,"gpt":0.2706361108031421,"spread":0.2521029950289536,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007197432,0.0001834071,0.0003836179,0.00006530092,0.0000943947,0.00007604284,0.0003294669,0.00008536843,0.0001249015],"category_scores_gemma":[0.00005791737,0.000109475,0.0001256243,0.00030251,0.00004264776,0.0002122448,0.00004456204,0.0001851403,0.00001345286],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001432281,"about_ca_system_score_gemma":0.0001756173,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0003522768,"about_ca_topic_score_gemma":0.000009333295,"domain_scores_codex":[0.9982471,0.00008077891,0.0005110548,0.0002532952,0.000646185,0.0002615268],"domain_scores_gemma":[0.998482,0.0001504513,0.0005537251,0.0005077376,0.0002585053,0.00004753359],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0002318298,0.0002171895,0.0007008372,0.0001859645,0.0002295633,0.00000128938,0.0008012935,0.03675618,0.9601488,0.00003570124,0.0001172142,0.000574193],"study_design_scores_gemma":[0.003446831,0.0001123994,0.000003173485,0.0001773998,0.0003477969,0.000002446415,0.0005748038,0.9032565,0.09179954,0.00002089936,0.0001188123,0.0001393916],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9942816,0.0006271052,0.003519289,0.000151061,0.00007417984,0.00005885341,0.0001271893,0.00004462382,0.001116021],"genre_scores_gemma":[0.9932559,0.00001734274,0.00002418338,0.00001251172,0.00009480063,0.00002131851,0.0001255008,0.00002790084,0.006420534],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.8683492,"threshold_uncertainty_score":0.4464262,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01305059338620871,"gpt":0.2686431095567348,"spread":0.2555925161705261,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001738082,0.0002171807,0.0001919847,0.00008462167,0.0001295917,0.00005740387,0.0001760192,0.00009873912,0.00003770995],"category_scores_gemma":[0.00001576645,0.0002268457,0.0001020201,0.0002155044,0.00004010205,0.0008535672,0.00003275383,0.0001389783,0.00004224348],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001033985,"about_ca_system_score_gemma":0.00002719586,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0000010636,"about_ca_topic_score_gemma":7.776328e-7,"domain_scores_codex":[0.9988464,0.00001573907,0.0002774454,0.0001925219,0.00014203,0.0005259214],"domain_scores_gemma":[0.9994028,0.00004732119,0.00003784832,0.0002769119,0.00004776118,0.0001874053],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.00007712134,0.0002419784,0.0001662958,0.0002088733,0.00006672341,4.532718e-7,0.0003039155,0.0002337021,0.9653153,0.002435335,0.002565352,0.02838492],"study_design_scores_gemma":[0.001641143,0.00005339004,0.0001420968,0.000029955,0.00007785828,0.00002001757,0.00001767541,0.936322,0.0226981,0.001282857,0.03740033,0.0003145758],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.7871206,0.00213983,0.2049677,0.00003021305,0.001060401,0.0008527429,0.0002487673,0.0009625254,0.002617139],"genre_scores_gemma":[0.995854,0.00001591772,0.001690211,0.00002841829,0.001432941,0.0003633093,0.0004102348,0.00007519062,0.0001297842],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9426172,"threshold_uncertainty_score":0.9250498,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.03448897291398529,"gpt":0.3001068798097258,"spread":0.2656179068957405,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004251209,0.0002497071,0.000410049,0.0002663945,0.00007929223,0.00003851519,0.0003876164,0.0001581078,0.00004667865],"category_scores_gemma":[0.001208206,0.0002717216,0.00008996877,0.0008478176,0.000273742,0.0008416116,0.0001322568,0.00008521965,0.00001806983],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001643419,"about_ca_system_score_gemma":0.0002964742,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0002238247,"about_ca_topic_score_gemma":0.000006482071,"domain_scores_codex":[0.9975603,0.00007469398,0.0008329198,0.0006097694,0.0004625252,0.0004598244],"domain_scores_gemma":[0.9985418,0.0002467853,0.0003566888,0.0005344627,0.0002103124,0.0001099293],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002976008,0.0003666501,0.00006279964,0.00007291765,0.000005117285,0.000005861777,0.000181724,0.000457143,0.9981934,0.0002088301,0.00005753103,0.00009046672],"study_design_scores_gemma":[0.001902078,0.00008351367,0.0003411426,0.00004064056,0.00003010562,0.00004090877,0.00002160232,0.0343128,0.9614916,0.001400473,0.00006342571,0.0002716387],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9899065,0.00007585687,0.00816117,0.00006564128,0.000500069,0.0007206993,0.0003165035,0.0001242874,0.0001292804],"genre_scores_gemma":[0.996533,0.000007393022,0.002827604,0.00002783402,0.00008917094,0.000086422,0.0003328954,0.0000429558,0.00005269031],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.03670169,"threshold_uncertainty_score":0.9999735,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"about_ca":false},"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Chemistry; Hydrogen sulfide; Solubility; Inorganic chemistry; Aqueous solution; Sulfide; Kraft process; Sulfur; Pyrrhotite; Chelation; Solubility equilibrium; Kraft paper; Organic chemistry; Chemical engineering","retraction":null,"screen_n_in":null,"score":{"opus":0.02743399646606484,"gpt":0.2583454759461803,"spread":0.2309114794801155,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0004169541,0.0002530745,0.0007319484,0.0002466471,0.0000330478,0.000004595943,0.0003361927,0.0002103177,0.0002217703],"category_scores_gemma":[0.0002138418,0.0002741267,0.0002073223,0.0004850866,0.0002031141,0.0001424835,0.00005352013,0.0002233956,0.000002712884],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0001164089,"about_ca_system_score_gemma":0.0001673533,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000238324,"about_ca_topic_score_gemma":0.00006157155,"domain_scores_codex":[0.9977941,0.00007639718,0.001115025,0.0002421012,0.0003131985,0.0004591575],"domain_scores_gemma":[0.9989991,0.0001407941,0.0001191895,0.0005164871,0.00008647436,0.0001379903],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001767573,0.0004232694,0.00007255217,0.0001610122,0.00006528234,0.000007224656,0.0005941082,0.0144069,0.9819494,0.0004021541,0.0001655295,0.001575739],"study_design_scores_gemma":[0.007475893,0.0004084047,0.0001392833,0.0001807131,0.00006555716,0.000009808343,0.00004020185,0.02664129,0.9631035,0.001331723,0.0003591303,0.0002445046],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9937602,0.001794935,0.002448269,0.0001072345,0.0002609434,0.0005188751,0.0002750926,0.00009702007,0.000737441],"genre_scores_gemma":[0.9990483,0.00002402517,0.0007173051,0.00000637316,0.00008608145,0.0000172289,0.00003287275,0.00004100334,0.0000268154],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.01884598,"threshold_uncertainty_score":0.9999711,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01864330773591538,"gpt":0.2824758870435385,"spread":0.2638325793076232,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0001438654,0.0001583745,0.0003502772,0.00003514617,0.0004175742,0.00006531809,0.0002339473,0.0000748742,0.00005506282],"category_scores_gemma":[0.000420975,0.00014091,0.00008193045,0.00005733932,0.0002081732,0.0002714513,0.00007472302,0.00007654773,0.000008204409],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00002278422,"about_ca_system_score_gemma":0.00006175508,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00001964718,"about_ca_topic_score_gemma":6.668801e-7,"domain_scores_codex":[0.9989195,0.00001723465,0.0004390967,0.000287044,0.0001035709,0.0002335005],"domain_scores_gemma":[0.9987234,0.00007349341,0.0002082721,0.0006261161,0.0002736676,0.00009504739],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0005878776,0.0001866975,0.0000180359,0.0001106313,0.00006502316,2.866657e-7,0.00008716331,0.00001077339,0.9824662,0.01518224,0.0006616925,0.0006233428],"study_design_scores_gemma":[0.02432444,0.0004161489,0.0004333509,0.0002928865,0.0002848593,0.00001303072,0.00002303727,0.4075433,0.5197475,0.0006642296,0.04566435,0.000592839],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9402477,0.0005401276,0.054138,0.002955483,0.0002047251,0.001188617,0.0004275524,0.00009294283,0.0002048927],"genre_scores_gemma":[0.9967629,0.00008772917,0.0006786135,0.00006525902,0.0002495248,0.000398436,0.0003080698,0.0000299087,0.001419613],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.4627187,"threshold_uncertainty_score":0.5746143,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.09048399818298053,"gpt":0.2919706034932169,"spread":0.2014866053102364,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002974769,0.0002116936,0.0004227034,0.000187014,0.00003789761,0.0000406457,0.0002692898,0.0001395618,0.00003667781],"category_scores_gemma":[0.00009849933,0.0001971456,0.00009584908,0.0007696196,0.00009693672,0.0001742761,0.0002690968,0.0003487025,5.327409e-7],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00009890462,"about_ca_system_score_gemma":0.0001129513,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.000320529,"about_ca_topic_score_gemma":0.000006167076,"domain_scores_codex":[0.9982798,0.00004894362,0.0004980486,0.0006635129,0.0001935346,0.0003161982],"domain_scores_gemma":[0.998991,0.0001632167,0.0000527563,0.0006614481,0.00004189989,0.00008971922],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.00006166795,0.00004340649,0.00004524131,0.0001567348,0.000128607,0.000003107388,0.0001793248,0.2617642,0.7368478,0.0003950953,0.000001622701,0.0003732318],"study_design_scores_gemma":[0.0003203143,0.00002042298,0.000002054072,0.00007590769,0.0002339391,0.000002351831,0.0000339094,0.712889,0.2860348,0.0002220741,0.00001616804,0.0001491037],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.8556837,0.001521142,0.1423657,0.00004777463,0.00003651674,0.0001540659,0.00005282962,0.00008604714,0.00005226145],"genre_scores_gemma":[0.9937243,0.00001222924,0.005841584,0.000007135203,0.00009968732,0.00001036655,0.0002496525,0.00003712395,0.00001787325],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.4511248,"threshold_uncertainty_score":0.8039364,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.008268147093099755,"gpt":0.2287358393134135,"spread":0.2204676922203137,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0007878341,0.0005955357,0.0005965955,0.0002871206,0.00007428113,0.000162122,0.0009758303,0.0002983801,0.0001395465],"category_scores_gemma":[0.00002955675,0.0005100756,0.0002457947,0.0008784261,0.0001204381,0.0005464363,0.0001182059,0.0004904553,0.0002691228],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0002824707,"about_ca_system_score_gemma":0.0000801016,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.0001470826,"about_ca_topic_score_gemma":0.00005555348,"domain_scores_codex":[0.9966111,0.0002416528,0.0009424321,0.000534238,0.0005862658,0.001084372],"domain_scores_gemma":[0.9983343,0.0002610661,0.00009132062,0.001106838,0.00005030858,0.0001561741],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","study_design_scores_codex":[0.0003670633,0.0003123662,0.00005414279,0.0002622647,0.0000636726,0.0004432506,0.0004276407,0.005045961,0.9763102,0.01146187,0.00494612,0.0003054565],"study_design_scores_gemma":[0.008407698,0.0006164096,0.0002518935,0.0002711468,0.0001275733,0.000426333,0.000308343,0.9123511,0.05755409,0.002010461,0.01622621,0.00144873],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9497285,0.00118949,0.001319687,0.0001364506,0.001465745,0.0008636424,0.0001455836,0.001096245,0.04405463],"genre_scores_gemma":[0.9978231,0.00001380478,0.000142746,0.00008755116,0.001118497,0.0001732454,0.0002359898,0.000161823,0.0002432581],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.9187561,"threshold_uncertainty_score":0.9997351,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"about_ca":false},"ca_institutions":"University of Alberta","funders":"Alberta Innovates; Virtual Materials Group","keywords":"Chemistry; Decane; Residue (chemistry); Phase (matter); Thermodynamics; Organic chemistry","retraction":null,"screen_n_in":null,"score":{"opus":0.01108647005845334,"gpt":0.2607830122661453,"spread":0.249696542207692,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow","insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0003988861,0.0003909775,0.000401791,0.0001557757,0.0000884171,0.00005455224,0.0006889314,0.0002011645,0.001542695],"category_scores_gemma":[0.0001040709,0.0003114936,0.0002199786,0.0003488549,0.0001613288,0.0002407099,0.00009186171,0.0005996434,0.0001558426],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.0000371844,"about_ca_system_score_gemma":0.00007135539,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00002890492,"about_ca_topic_score_gemma":0.00003343734,"domain_scores_codex":[0.9981362,0.00006356987,0.0005400994,0.0003348458,0.0003842557,0.0005410452],"domain_scores_gemma":[0.9981508,0.0003269332,0.00008647182,0.001149816,0.00006531201,0.0002207297],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0001928454,0.0005095913,0.000046723,0.00002929155,0.00008461063,0.00003673574,0.0002230494,0.00004215657,0.9681983,0.0231655,0.006529748,0.0009414366],"study_design_scores_gemma":[0.008673635,0.0009265307,0.0002764164,0.0001008786,0.0001632722,0.00006958131,0.00004321766,0.2642174,0.7095199,0.01044896,0.004713058,0.0008471566],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9870704,0.0001046731,0.0006337485,0.000164135,0.001674194,0.0004301192,0.000425421,0.0003862737,0.009111078],"genre_scores_gemma":[0.9987717,0.00001293916,0.0001688494,0.00006762568,0.0003748854,0.00004310794,0.0001008238,0.000123204,0.0003368129],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.2641752,"threshold_uncertainty_score":0.9999337,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":true,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01688739023146016,"gpt":0.2866378481159662,"spread":0.269750457884506,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["insufficient_payload"],"consensus_categories":[],"category_scores_codex":[0.0005231116,0.0001550838,0.0002795683,0.00002986669,0.00006226893,0.00002182889,0.00009160455,0.00009655474,0.001052507],"category_scores_gemma":[0.0001895657,0.0001114766,0.00008751758,0.0001206048,0.00006238691,0.00009335817,0.00001722314,0.00009932247,0.00000895513],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00003565,"about_ca_system_score_gemma":0.00004089485,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00009142941,"about_ca_topic_score_gemma":0.000001558762,"domain_scores_codex":[0.9989197,0.0001670257,0.0003371527,0.0001988487,0.000217519,0.0001598167],"domain_scores_gemma":[0.9990297,0.0003397946,0.0002027474,0.0003323369,0.00004075691,0.00005465013],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0003028427,0.00007224004,0.0008153461,0.0001736868,0.00004681222,0.000003890272,0.00009092371,0.00001495624,0.9974579,0.0001463229,0.0005921861,0.0002828939],"study_design_scores_gemma":[0.001356299,0.0002044512,0.00001426422,0.0001277825,0.00007182176,0.00001858724,0.00006076583,0.006730285,0.9857613,0.00001621842,0.005524487,0.000113735],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.9943515,0.0003936065,0.00003729112,0.0000146307,0.0001969623,0.0001708825,0.00003490205,0.00001724976,0.004782975],"genre_scores_gemma":[0.9986594,0.00001272424,0.00002951809,0.00001168268,0.00007654739,0.000005294211,0.000005297119,0.00002016438,0.001179409],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.0116966,"threshold_uncertainty_score":0.9998606,"prediction_status":"machine_predicted_unvalidated"},"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,"routes":{"ca_aff":true,"ca_fund":false,"ca_venue":false,"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","retraction":null,"screen_n_in":null,"score":{"opus":0.01428213837120716,"gpt":0.2480479356275108,"spread":0.2337657972563037,"validation_status":"score_only:v0-immature-baseline"},"prediction":{"model_version":"codex-gemma-dda1882f352a","candidate_categories":["metaepi_narrow"],"consensus_categories":[],"category_scores_codex":[0.0002093196,0.0003957503,0.0005663851,0.0001128118,0.0001672525,0.0001408708,0.0006679933,0.0001540635,0.0002154849],"category_scores_gemma":[0.00001208673,0.0002997748,0.0001428246,0.00005497645,0.0002041085,0.0005513952,0.0001320062,0.0001666769,0.0001495454],"about_ca_system_candidate":false,"about_ca_system_consensus":false,"about_ca_system_score_codex":0.00008605148,"about_ca_system_score_gemma":0.00004010197,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_topic_score_codex":0.00004495739,"about_ca_topic_score_gemma":0.00001027482,"domain_scores_codex":[0.9981818,0.0000340989,0.0005014532,0.0003444349,0.0003229827,0.0006152132],"domain_scores_gemma":[0.9981242,0.00002639138,0.0001069045,0.001421879,0.00009217463,0.000228392],"domain_codex":null,"domain_gemma":null,"domain_candidate":null,"domain_consensus":null,"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","study_design_scores_codex":[0.0002108726,0.000118679,0.0002428391,0.000238985,0.0001628345,0.0002459848,0.0002183304,0.0001871267,0.9961154,0.00138007,0.0002430157,0.0006357991],"study_design_scores_gemma":[0.006006976,0.0004313552,0.0002533041,0.0002491682,0.0002731598,0.0002084047,0.00005027907,0.2760293,0.7145485,0.0001042677,0.001155637,0.0006896923],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","genre_codex":"empirical","genre_gemma":"empirical","genre_scores_codex":[0.987112,0.0001383384,0.001098595,0.00002252947,0.000985876,0.000477438,0.0002041514,0.0004840757,0.009476977],"genre_scores_gemma":[0.9988841,0.000008854084,0.0002002586,0.000007017931,0.0002356193,0.00006596305,0.00009994942,0.0001356378,0.000362576],"genre_candidate":"empirical","genre_consensus":"empirical","teacher_disagreement_score":0.281567,"threshold_uncertainty_score":0.9999455,"prediction_status":"machine_predicted_unvalidated"},"labels":[],"label_agreement":null}]}