{"meta":{"query_hash":"aa5ac6fa95dd","filters":{"venue":"Chemical Engineering & Technology"},"cohort_total":135,"direct_labels_cover":0,"predictions_cover":135,"exported":135,"export_cap":100000,"truncated":false,"label_status":"direct model label, unvalidated","prediction_status":"machine_predicted_unvalidated (Codex and Gemma teacher distillation)","score_status":"score_only:v0-immature-baseline","snapshot":{"source":"OpenAlex, pinned release, all 482 partitions","release":"2026-06-24","frame_built":"2026-07-12"},"permalink":"https://metacan.xera.ac/q/aa5ac6fa95dd","api":"https://metacan.xera.ac/api/v1/cohort?venue=Chemical+Engineering+%26+Technology"},"results":[{"id":"W1968307088","doi":"10.1002/ceat.200600311","title":"Evaluations and Modifications on Reynolds Stress Model in Cyclone Simulations","year":2006,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Cyclone Separators and Fluid Dynamics","field":"Engineering","cited_by":34,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of New Brunswick","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Reynolds stress; Turbulence; Cyclone (programming language); Mechanics; Flow (mathematics); Particle image velocimetry; Root mean square; Reynolds number; Mean flow; Turbulence kinetic energy; Computational fluid dynamics; Mathematics; Meteorology; Environmental science; Physics; Engineering","score_opus":0.005722884066254034,"score_gpt":0.21951794043641396,"score_spread":0.2137950563701599,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1968307088","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8983491,0.00043051594,0.09050288,0.00037311902,0.00020971108,0.00021959346,0.00037569538,0.0018807175,0.007658738],"genre_scores_gemma":[0.98215175,0.00011141596,0.016730413,0.00003094547,0.000020707304,0.00007605571,0.0001416682,0.00011454439,0.00062250905],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9994467,0.0002651766,0.000038405087,0.00005351529,0.00014107836,0.000055196466],"domain_scores_gemma":[0.9972445,0.0013576302,0.00016453808,0.00037751376,0.0007551276,0.00010073208],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001436677,0.0007110528,0.00072851504,0.00031588532,0.00029543386,0.0005743002,0.001072576,0.0006834486,0.0010779132],"category_scores_gemma":[0.006737362,0.00031094087,0.00048355214,0.000277828,0.00031184842,0.0007428118,0.0005051341,0.00068852835,0.00023498968],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00018276619,0.00014260873,0.006594289,0.00007380929,0.000042222284,0.00008621046,0.000042355372,0.9657427,0.0050372826,0.0011891241,0.00067462755,0.020191941],"study_design_scores_gemma":[0.000011184996,0.000046568788,0.00057764957,0.000004734079,0.0000062962304,0.0000053856206,0.0000056648487,0.99748343,0.0016095078,0.00006207925,0.00018190232,0.000005565542],"about_ca_topic_score_codex":0.010789696,"about_ca_topic_score_gemma":0.005281309,"teacher_disagreement_score":0.010789696,"about_ca_system_score_codex":0.0005621127,"about_ca_system_score_gemma":0.00069951883,"threshold_uncertainty_score":0.021453798},"labels":[],"label_agreement":null},{"id":"W1970776482","doi":"10.1002/ceat.200800290","title":"Simultaneous Aerodynamic and Thermal Analysis during Cooling of Stacked Spheres inside Ventilated Packages","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Heat Transfer Mechanisms","field":"Engineering","cited_by":43,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Agriculture and Agri-Food Canada; McGill University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Airflow; Aerodynamics; Mechanics; Heat transfer; Thermal; Convection; Aerodynamic heating; Materials science; Forced convection; Environmental science; Natural convection; Meteorology; Thermodynamics; Physics","score_opus":0.0035457524921279505,"score_gpt":0.1710274350898477,"score_spread":0.16748168259771973,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1970776482","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9976907,0.000027032129,0.002063166,0.0000033291,0.0000031549266,0.0000054268608,0.000044959226,0.000028944403,0.0001333744],"genre_scores_gemma":[0.999209,0.000011102722,0.0005877845,0.0000015666031,0.0000019927263,0.0000045260194,0.000046639783,0.000009141878,0.00012832922],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998807,0.000019772133,0.0000037983857,0.00002543952,0.000048901275,0.000021466481],"domain_scores_gemma":[0.9998561,0.000065569395,0.000016994203,0.000013875384,0.000035827994,0.000011502987],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018696557,0.00027131158,0.00042629422,0.00019175446,0.00026422777,0.00022226501,0.00019610689,0.0001727324,0.0006401852],"category_scores_gemma":[0.00036950508,0.00018270165,0.00026468717,0.000115984134,0.0003068729,0.0002000373,0.00014344769,0.00016697805,0.00009717135],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00032991925,0.000020690986,0.0037299905,0.000036467758,0.000016743452,0.00012472646,0.00016012385,0.0082239555,0.9831004,0.00007054906,0.00008860488,0.0040978338],"study_design_scores_gemma":[0.000025522917,0.000666765,0.08665913,0.000008735333,0.00004578899,0.00015042168,0.00010200516,0.10069341,0.81081676,0.00005666683,0.0007340041,0.00004070018],"about_ca_topic_score_codex":0.0014938854,"about_ca_topic_score_gemma":0.0013146289,"teacher_disagreement_score":0.0014938854,"about_ca_system_score_codex":0.0002677515,"about_ca_system_score_gemma":0.00017259427,"threshold_uncertainty_score":0.0029703379},"labels":[],"label_agreement":null},{"id":"W1972305234","doi":"10.1002/ceat.201300253","title":"Baker's Yeast Behavior during Vacuum Agitated Contact Drying","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Microbial Inactivation Methods","field":"Biochemistry, Genetics and Molecular Biology","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of New Brunswick","funders":"Fonds De La Recherche Scientifique - FNRS","keywords":"Impeller; Yeast; Mass transfer; Fluidized bed; Work (physics); Materials science; Fluidization; Chemistry; Vacuum drying; Phase (matter); Mechanics; Chromatography; Mechanical engineering; Engineering; Freeze-drying; Physics","score_opus":0.005083075289809797,"score_gpt":0.22160795660659405,"score_spread":0.21652488131678424,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1972305234","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99667835,0.0007962228,0.0010734698,0.000032879714,0.000022088443,0.000016780237,0.0003499088,0.000044989014,0.0009853315],"genre_scores_gemma":[0.99620074,0.0005246332,0.00096338504,0.00004281909,0.000009846108,0.000020649639,0.00054085755,0.000046408197,0.0016505499],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9996196,0.000049898452,0.000023426694,0.0000927717,0.00014656324,0.000067613706],"domain_scores_gemma":[0.99955684,0.00015136515,0.00007338265,0.000029955887,0.00015224988,0.000036149995],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002503075,0.0003479951,0.0005656214,0.00032905574,0.00027792735,0.0005852342,0.00027210973,0.00037919634,0.0012020986],"category_scores_gemma":[0.000604436,0.00015909414,0.00033225468,0.00066501176,0.00023407691,0.00037163,0.00019538442,0.0006812334,0.00036859844],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00046694765,0.00011163792,0.00131718,0.0000935436,0.000020552076,0.00019351396,0.00024681538,0.00036818936,0.99286216,0.00008096419,0.00012449907,0.004114025],"study_design_scores_gemma":[0.000010742128,0.00079910224,0.013820779,0.00002765475,0.000026739412,0.0001538948,0.00038646924,0.002456561,0.98099625,0.00005313823,0.0012440354,0.000024522702],"about_ca_topic_score_codex":0.0020105334,"about_ca_topic_score_gemma":0.0013199835,"teacher_disagreement_score":0.0020105334,"about_ca_system_score_codex":0.00022509955,"about_ca_system_score_gemma":0.00017652754,"threshold_uncertainty_score":0.004021466},"labels":[],"label_agreement":null},{"id":"W1974226525","doi":"10.1002/ceat.201000237","title":"A Sequential Iterative Scheme for Design of Experiments in Complex Polymerizations","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Polymer Synthesis and Characterization","field":"Chemistry","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Computer science; Bayesian probability; Set (abstract data type); Design of experiments; Iterative and incremental development; Process (computing); Sequential analysis; Bayesian optimization; Optimal design; Scheme (mathematics); Experimental data; Mathematical optimization; Algorithm; Mathematics; Artificial intelligence; Machine learning","score_opus":0.019288771256679074,"score_gpt":0.26153844792961983,"score_spread":0.24224967667294076,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1974226525","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.001236387,0.000036209858,0.99774903,0.000022105594,0.000013449649,0.00060441054,0.000012152205,0.00008007158,0.00024619835],"genre_scores_gemma":[0.03374812,0.00005524709,0.9625493,0.000038518065,0.000012332289,0.0032339902,0.00002631563,0.000018781142,0.00031734162],"study_design_codex":"simulation_or_modeling","study_design_gemma":"theoretical_or_conceptual","domain_scores_codex":[0.9389857,0.04795607,0.002300392,0.0034608704,0.006491265,0.0008056866],"domain_scores_gemma":[0.9426005,0.045103498,0.0040798346,0.0031073242,0.0043395315,0.0007694329],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0717209,0.0022445386,0.002661948,0.0017411577,0.0010281756,0.0015594757,0.0028020195,0.0017410443,0.005767384],"category_scores_gemma":[0.06277637,0.0017140337,0.0018147661,0.0013627758,0.0026932098,0.0016256921,0.0028073206,0.002591529,0.00090076035],"study_design_candidate":"theoretical_or_conceptual","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00252563,0.0006417275,0.0009633656,0.0012549058,0.00051931053,0.00014383622,0.00089000876,0.58595425,0.017535929,0.16358931,0.000835259,0.22514634],"study_design_scores_gemma":[0.00096835947,0.0023675424,0.0003849268,0.00011326317,0.00014739556,0.000059472826,0.000032232936,0.88155645,0.007947123,0.10040088,0.0059193354,0.00010313418],"about_ca_topic_score_codex":0.0011067985,"about_ca_topic_score_gemma":0.001801853,"teacher_disagreement_score":0.0717209,"about_ca_system_score_codex":0.0023850163,"about_ca_system_score_gemma":0.004777845,"threshold_uncertainty_score":0.3793009},"labels":[],"label_agreement":null},{"id":"W1978995184","doi":"10.1002/ceat.200301844","title":"Hydrodynamics and Mass Transfer in Gas‐Liquid‐Solid Circulating Fluidized Beds","year":2003,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of New Brunswick","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Mass transfer; Work (physics); Fluidized bed combustion; Mechanics; Chemistry; Particle (ecology); Thermodynamics; Mass transfer coefficient; Fluidized bed; Flow (mathematics); Chromatography; Physics; Geology","score_opus":0.003307718907997542,"score_gpt":0.1755982696757949,"score_spread":0.17229055076779734,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1978995184","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9725954,0.00028892414,0.02595646,0.00013048603,0.000028297845,0.00002128542,0.00002687444,0.00018141035,0.0007707598],"genre_scores_gemma":[0.9983247,0.000041712752,0.0013127102,0.000011207258,0.0000042204106,0.0000066676594,0.000019060408,0.00000386002,0.00027603],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99982375,0.000045797176,0.0000049536293,0.00002920021,0.00005698138,0.00003931357],"domain_scores_gemma":[0.9998264,0.00007357695,0.000033131582,0.000007843845,0.00003613251,0.000022995715],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002534196,0.000274028,0.00033207072,0.00030196295,0.00033963707,0.0005429397,0.00028848404,0.00034290666,0.00051545136],"category_scores_gemma":[0.00071039004,0.00018277222,0.00016095814,0.00018390098,0.00076080253,0.00042949006,0.00039110574,0.00024556584,0.00008989982],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00057440205,0.00018631048,0.005902525,0.00014486496,0.00002710658,0.0005553146,0.00024515405,0.26679397,0.70270324,0.0047772215,0.00059020997,0.017499689],"study_design_scores_gemma":[0.00010386764,0.0002969777,0.0069464063,0.000006498467,0.000010742543,0.00008867257,0.00008463213,0.85583395,0.13436309,0.0016164538,0.00062157895,0.000027148597],"about_ca_topic_score_codex":0.004250292,"about_ca_topic_score_gemma":0.00096352346,"teacher_disagreement_score":0.004250292,"about_ca_system_score_codex":0.0009657816,"about_ca_system_score_gemma":0.00043518876,"threshold_uncertainty_score":0.008451104},"labels":[],"label_agreement":null},{"id":"W1979514856","doi":"10.1002/ceat.200600281","title":"A Comparison of Flow Dynamics and Flow Structure in a Riser and a Downer","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Theoretical and Computational Physics","field":"Physics and Astronomy","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Mechanics; Flow (mathematics); Core (optical fiber); Correlation dimension; Chaotic; Physics; Mathematics; Fractal dimension; Fractal; Mathematical analysis","score_opus":0.001996270191621835,"score_gpt":0.20973118202613691,"score_spread":0.2077349118345151,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1979514856","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9992779,0.000008440444,0.00051363895,0.000003310556,0.000001449318,0.0000058219653,0.000016270746,0.000010070052,0.00016314712],"genre_scores_gemma":[0.99783605,0.000013154104,0.0014886588,0.000008360173,0.0000022756412,0.000008609084,0.00008393377,0.00000996715,0.00054904266],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99960226,0.000054875105,0.000021542462,0.00015129092,0.00009422363,0.00007573949],"domain_scores_gemma":[0.9994696,0.00012712773,0.00010415131,0.00008671723,0.000086715576,0.00012569314],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046209255,0.000283372,0.00082017976,0.00074046117,0.0004767285,0.0005591697,0.0003572888,0.00036376552,0.0014857668],"category_scores_gemma":[0.0007908876,0.00027811155,0.00048156182,0.00026378906,0.00055030285,0.0004721698,0.00075764017,0.0003075451,0.00022767743],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0026147414,0.00034506212,0.047917403,0.000053640673,0.00006402339,0.000812555,0.000597408,0.0048499685,0.9300544,0.00049125083,0.00008304243,0.012116609],"study_design_scores_gemma":[0.00022136042,0.00563856,0.63258225,0.000018998197,0.00025839914,0.0006576801,0.0010804638,0.059822906,0.2969763,0.0004920547,0.0021298614,0.000121174555],"about_ca_topic_score_codex":0.0016675593,"about_ca_topic_score_gemma":0.0012288304,"teacher_disagreement_score":0.0016675593,"about_ca_system_score_codex":0.00030383567,"about_ca_system_score_gemma":0.00022635903,"threshold_uncertainty_score":0.0049703717},"labels":[],"label_agreement":null},{"id":"W1980193653","doi":"10.1002/ceat.200600400","title":"Hydrodynamics and Flow Development in a 15.1 m Circulating Fluidized Bed Riser","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":23,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Fluidized bed combustion; Flow (mathematics); Mechanics; Materials science; Fluidized bed; Particle (ecology); Flow velocity; Engineering; Geology; Waste management; Physics","score_opus":0.0033022310763278517,"score_gpt":0.1755297363918547,"score_spread":0.17222750531552686,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1980193653","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9978703,0.00007035995,0.0016415204,0.00004225659,0.000009380198,0.000008912931,0.000029477158,0.000110445624,0.00021737283],"genre_scores_gemma":[0.9967871,0.000029928684,0.0025435209,0.000019437077,0.0000042993915,0.0000053491076,0.00007011345,0.000013994315,0.0005263782],"study_design_codex":"bench_or_experimental","study_design_gemma":"observational","domain_scores_codex":[0.9997694,0.00003665095,0.000009792699,0.00006718126,0.000063332714,0.000053683336],"domain_scores_gemma":[0.999728,0.00007940875,0.00003781887,0.00001545195,0.000047566227,0.00009177649],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00040106982,0.00031529498,0.0007442676,0.00026598165,0.0004967047,0.0007406934,0.00040928216,0.0005278433,0.00074781064],"category_scores_gemma":[0.0004063902,0.00020057456,0.00030586933,0.00018544913,0.000625784,0.0003645977,0.00023891454,0.0005391388,0.0002051385],"study_design_candidate":"observational","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00049186416,0.00018953848,0.00311646,0.00003487162,0.000011450085,0.0003719714,0.00025672305,0.006887906,0.98240745,0.00050265563,0.00017813272,0.0055509876],"study_design_scores_gemma":[0.00025841233,0.002900209,0.027623588,0.000015613385,0.000052168398,0.0003193408,0.00026970115,0.17734708,0.7889412,0.00029488924,0.001873752,0.00010405146],"about_ca_topic_score_codex":0.005204796,"about_ca_topic_score_gemma":0.0018533522,"teacher_disagreement_score":0.005204796,"about_ca_system_score_codex":0.0012568706,"about_ca_system_score_gemma":0.0007334837,"threshold_uncertainty_score":0.010348976},"labels":[],"label_agreement":null},{"id":"W1981286565","doi":"10.1002/ceat.201400026","title":"Application of the Electrodiffusion Method to Measure Wall Shear Stress: Integrating Theory and Practice","year":2014,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Membrane-based Ion Separation Techniques","field":"Engineering","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Mechanics; Shear stress; Flow (mathematics); Measure (data warehouse); Filtration (mathematics); Transient flow; Transient (computer programming); Shear flow; Computer science; Materials science; Mechanical engineering; Engineering; Mathematics; Physics; Electrical engineering; Data mining; Statistics","score_opus":0.0043596987374408085,"score_gpt":0.24025445992049133,"score_spread":0.23589476118305053,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1981286565","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.022145694,0.0131086605,0.9607777,0.0005010487,0.00028694322,0.00015528248,0.000051008312,0.0004591823,0.002514477],"genre_scores_gemma":[0.3470876,0.019641148,0.6301538,0.0002899796,0.00026155685,0.00034832847,0.00007503963,0.0001282704,0.0020143362],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99596345,0.0012246954,0.0002109492,0.00058395474,0.0019307693,0.000086187516],"domain_scores_gemma":[0.9981694,0.0009277203,0.00014548423,0.00020019349,0.0005072095,0.00004990977],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0043770364,0.0011737187,0.001362801,0.0032795942,0.00041312564,0.001803167,0.0018025537,0.0018544648,0.0007300169],"category_scores_gemma":[0.003897804,0.0008477693,0.0006944527,0.001596783,0.0017598197,0.0017896574,0.0018248578,0.0018155972,0.00058707385],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002000665,0.00052148156,0.0070919725,0.0021770794,0.00026546826,0.00043068433,0.0006855184,0.023890255,0.5678708,0.04004544,0.0016235622,0.35519764],"study_design_scores_gemma":[0.00006836889,0.0009851945,0.0063569793,0.0004877094,0.00015543684,0.0012614283,0.0004196925,0.4315131,0.49181858,0.035836242,0.030665256,0.00043207136],"about_ca_topic_score_codex":0.00063408044,"about_ca_topic_score_gemma":0.0004850058,"teacher_disagreement_score":0.0043770364,"about_ca_system_score_codex":0.0009948105,"about_ca_system_score_gemma":0.000845415,"threshold_uncertainty_score":0.023148239},"labels":[],"label_agreement":null},{"id":"W1993497069","doi":"10.1002/ceat.201200048","title":"Semicontinuous Thermal Separation Systems","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Process Optimization and Integration","field":"Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University","funders":"","keywords":"Extractive distillation; Distillation; Process engineering; Separation (statistics); Air separation; Batch distillation; Ternary operation; Process (computing); Separation process; Computer science; Fractional distillation; Engineering; Chemistry; Chromatography; Chemical engineering","score_opus":0.004045069835445797,"score_gpt":0.19617877275905837,"score_spread":0.19213370292361256,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1993497069","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.1566714,0.010311665,0.7332086,0.00057973445,0.00030060683,0.00020664722,0.0004482845,0.0012331428,0.09703986],"genre_scores_gemma":[0.9051266,0.0034031812,0.06377142,0.00020344574,0.000054367254,0.00015835276,0.00042423452,0.00007335587,0.026785076],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9995396,0.00008950846,0.000027816464,0.00011580869,0.00016577521,0.00006160104],"domain_scores_gemma":[0.99959105,0.00013749632,0.000057649093,0.000069726535,0.000116931005,0.000027160748],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003642956,0.00049168157,0.00068723946,0.00045695927,0.00057740835,0.0011520957,0.0009577163,0.0006534608,0.0067217797],"category_scores_gemma":[0.0006982357,0.00034689013,0.00039216198,0.000805588,0.00081075536,0.0012810694,0.0011487708,0.000847399,0.0009005244],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00032840337,0.00018931439,0.0010875491,0.00093780184,0.000094664465,0.00047913834,0.00027304623,0.5415142,0.071350925,0.22788426,0.0047676205,0.15109307],"study_design_scores_gemma":[0.000064146785,0.00023980912,0.00049899926,0.00006659563,0.000029504441,0.0002243904,0.00006134989,0.8919356,0.018331053,0.062414173,0.026097123,0.00003712775],"about_ca_topic_score_codex":0.001572677,"about_ca_topic_score_gemma":0.0014747039,"teacher_disagreement_score":0.0067217797,"about_ca_system_score_codex":0.0008285575,"about_ca_system_score_gemma":0.00091153616,"threshold_uncertainty_score":0.022486567},"labels":[],"label_agreement":null},{"id":"W1995321964","doi":"10.1002/ceat.200900075","title":"Particle Shape, Density, and Size Effects on the Distribution of Phase Holdups in an LSCFB Riser","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Mineral Processing and Grinding","field":"Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Materials science; Phase (matter); Fluidized bed combustion; Distributor; Mechanics; Three-phase; Particle (ecology); Particle size; Composite material; Fluidization; Fluidized bed; Chemistry; Geology; Thermodynamics; Physics","score_opus":0.005634463921156116,"score_gpt":0.21600846988733952,"score_spread":0.21037400596618339,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1995321964","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9975637,0.000060149738,0.0020885584,0.000011635697,0.0000022615027,0.0000046837577,0.000049274255,0.000085219275,0.00013451569],"genre_scores_gemma":[0.998412,0.000032288794,0.0011585972,0.000007463349,0.0000014312981,0.0000040171467,0.0000693397,0.000024502438,0.00029026734],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99977356,0.000027862063,0.000009127497,0.00005123298,0.00010156996,0.000036684116],"domain_scores_gemma":[0.9993524,0.0002864466,0.0001004809,0.00004149892,0.00015565637,0.00006349325],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00059106044,0.00018320755,0.0003349766,0.00039922868,0.000229723,0.00046199368,0.00033864725,0.0002784525,0.0006980893],"category_scores_gemma":[0.0009830667,0.0002979451,0.00018624938,0.00021969202,0.000319911,0.00027167553,0.00017681612,0.00031762838,0.00027996796],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00032065625,0.000019576859,0.0020692623,0.000012533036,0.000004593259,0.00007081825,0.00005521283,0.0006158993,0.99505264,0.000033976183,0.00002852842,0.0017162403],"study_design_scores_gemma":[0.000023115419,0.00028167115,0.030854773,0.0000032497383,0.000017793609,0.00010402738,0.00005406987,0.0154374,0.95298636,0.000024955098,0.00019352717,0.0000190879],"about_ca_topic_score_codex":0.0046444507,"about_ca_topic_score_gemma":0.0029388894,"teacher_disagreement_score":0.0046444507,"about_ca_system_score_codex":0.000433983,"about_ca_system_score_gemma":0.00017692083,"threshold_uncertainty_score":0.009234846},"labels":[],"label_agreement":null},{"id":"W1996786820","doi":"10.1002/ceat.200401912","title":"Liquid/Solid Mass Transfer in Fixed Beds","year":2004,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Heat and Mass Transfer in Porous Media","field":"Engineering","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"McMaster University; Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada; Lakehead University","keywords":"Raschig ring; Mass transfer; Cylinder; Dissolution; Chemistry; Diffusion; Copper; Packed bed; Analytical Chemistry (journal); Chromatography; Materials science; Thermodynamics; Geometry; Mathematics; Physics; Physical chemistry","score_opus":0.004297000989762597,"score_gpt":0.18959415386296735,"score_spread":0.18529715287320475,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W1996786820","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99552286,0.00067875447,0.0027422172,0.000025612137,0.000026562857,0.000016133972,0.000072498166,0.000083328305,0.0008319767],"genre_scores_gemma":[0.9970585,0.00023459547,0.0017767893,0.000012611302,0.000012852056,0.000011117193,0.000100732694,0.0000081944345,0.00078473566],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9995815,0.00006788701,0.000018310215,0.00008116857,0.00015062958,0.00010043744],"domain_scores_gemma":[0.9995453,0.00016255068,0.00007434082,0.000041785825,0.00011530901,0.00006067429],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005052562,0.00046254712,0.0006583347,0.0006585515,0.00055990194,0.0007657712,0.00082491076,0.00033675355,0.0019225926],"category_scores_gemma":[0.0007087438,0.00034191628,0.0004063418,0.0003016841,0.0005393213,0.00048549304,0.00043548734,0.0004340277,0.0005355107],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00077842816,0.00013105274,0.0017174471,0.00026258474,0.00003516583,0.00021476144,0.00007409764,0.007018586,0.97971445,0.000569734,0.00022516855,0.009258467],"study_design_scores_gemma":[0.000056964658,0.0009331029,0.0028666777,0.000011870818,0.00002855273,0.00009151183,0.000041211126,0.017909357,0.9767079,0.000113035334,0.0012194313,0.000020469],"about_ca_topic_score_codex":0.004776861,"about_ca_topic_score_gemma":0.0036462622,"teacher_disagreement_score":0.004776861,"about_ca_system_score_codex":0.0009766988,"about_ca_system_score_gemma":0.00045043085,"threshold_uncertainty_score":0.009498119},"labels":[],"label_agreement":null},{"id":"W2002008938","doi":"10.1002/ceat.201100626","title":"Microwave Synthesis of the CPM‐5 Metal Organic Framework","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Metal-Organic Frameworks: Synthesis and Applications","field":"Chemistry","cited_by":71,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Microwave; Materials science; Crystallization; Metal-organic framework; Porosity; Chemical engineering; Metal; Microwave irradiation; Specific surface area; Solvothermal synthesis; Nuclear chemistry; Nanotechnology; Chemistry; Catalysis; Organic chemistry; Metallurgy; Composite material; Adsorption; Computer science","score_opus":0.006261073316252216,"score_gpt":0.198191742163244,"score_spread":0.19193066884699178,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2002008938","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96459454,0.0029959667,0.017647527,0.00007115275,0.00009292386,0.0001221085,0.0009832146,0.00047097832,0.013021633],"genre_scores_gemma":[0.9922421,0.00045858577,0.0056382385,0.000011730639,0.000007149628,0.000023201628,0.00025587753,0.000011375019,0.001351837],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999926,0.0000051166685,0.0000025616118,0.000014259782,0.000018607398,0.00003360312],"domain_scores_gemma":[0.99997723,0.0000028129932,0.0000053476415,0.0000024320132,0.0000044923736,0.000007678984],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000070260634,0.0002651001,0.00017555531,0.00019582793,0.00014886999,0.00017142929,0.00028298164,0.00019897205,0.0021296688],"category_scores_gemma":[0.00011053441,0.000087355096,0.00012878908,0.00018043305,0.00008475954,0.00010757809,0.00015164529,0.00021556679,0.00035447924],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000042077572,0.000021881146,0.00008223381,0.0001808358,0.000011313281,0.00013202452,0.000014584342,0.0005833606,0.9899183,0.001366612,0.00018411218,0.0074625667],"study_design_scores_gemma":[0.000010300944,0.00025764594,0.0010074114,0.000009569367,0.000013766688,0.0001376252,0.000012918862,0.0012997198,0.98746455,0.00008965637,0.009687604,0.000009192351],"about_ca_topic_score_codex":0.00083179725,"about_ca_topic_score_gemma":0.0014171705,"teacher_disagreement_score":0.0021296688,"about_ca_system_score_codex":0.00028784032,"about_ca_system_score_gemma":0.0001771347,"threshold_uncertainty_score":0.0071244836},"labels":[],"label_agreement":null},{"id":"W2002438512","doi":"10.1002/ceat.201300092","title":"Kinetics of Bioethanol Production Employing Mono‐ and Co‐Cultures of <i>Saccharomyces cerevisiae</i> and <i>Pichia stipitis</i>","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Biofuel production and bioconversion","field":"Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Pichia stipitis; Xylose; Ethanol fuel; Chemistry; Fermentation; Biofuel; Sugar; Food science; Hydrolysate; Ethanol; Saccharomyces cerevisiae; Kinetics; Biochemistry; Yeast; Biotechnology; Biology; Hydrolysis; Physics","score_opus":0.00493358109366327,"score_gpt":0.19020990593624768,"score_spread":0.1852763248425844,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2002438512","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957318,0.00060589454,0.0024495008,0.000024637624,0.00001469214,0.000016440801,0.00027208822,0.000056718844,0.0008282852],"genre_scores_gemma":[0.99632436,0.00041316106,0.002115466,0.0000074989666,0.0000023258158,0.00002012702,0.00026525653,0.000014493645,0.0008372574],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99982494,0.000033912762,0.000024359355,0.0000401729,0.000043308457,0.000033455424],"domain_scores_gemma":[0.99984205,0.00006419825,0.000028084653,0.000013911665,0.000030874948,0.0000208628],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003067141,0.00046393942,0.00047242708,0.00020321837,0.0001066483,0.00043160416,0.00023981874,0.00021372955,0.0005164564],"category_scores_gemma":[0.00033611493,0.00017642372,0.00033229747,0.0003622463,0.00012715744,0.00026612723,0.00025411957,0.00028410132,0.00026630543],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00037171188,0.000061419734,0.0010706532,0.000111839836,0.000027995364,0.00007527794,0.000059696053,0.0020507884,0.99197704,0.000099108984,0.00004476916,0.0040497654],"study_design_scores_gemma":[0.0000070638102,0.00018424628,0.0019066071,0.000008154135,0.000022746528,0.000031587984,0.000041953135,0.008322493,0.98909295,0.000020605352,0.0003517557,0.0000098596365],"about_ca_topic_score_codex":0.0014008612,"about_ca_topic_score_gemma":0.0011596754,"teacher_disagreement_score":0.0014008612,"about_ca_system_score_codex":0.0002078595,"about_ca_system_score_gemma":0.00017709231,"threshold_uncertainty_score":0.0027854443},"labels":[],"label_agreement":null},{"id":"W2006358291","doi":"10.1002/ceat.201100423","title":"Synthesis of BZSM‐5 Membranes Using Nano‐Zeolitic Seeds: Characterization and Separation Performance","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Zeolite Catalysis and Synthesis","field":"Chemistry","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Membrane; Zeolite; Chemical engineering; Materials science; Morphology (biology); Nano-; Hydrothermal synthesis; Crystal (programming language); Hydrothermal circulation; Chromatography; Chemistry; Organic chemistry; Composite material; Catalysis","score_opus":0.0074810542862030725,"score_gpt":0.20477388055502918,"score_spread":0.1972928262688261,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2006358291","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9921399,0.0010139933,0.00595126,0.00006130575,0.000011448348,0.000019608773,0.00020588198,0.00006254017,0.0005340616],"genre_scores_gemma":[0.9940697,0.00039859215,0.0046056733,0.000016847775,0.0000028715456,0.000012669914,0.00021065556,0.000016579583,0.00066651625],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999188,0.0000101789865,0.000008517695,0.000016920052,0.000027419099,0.000018150298],"domain_scores_gemma":[0.99988115,0.000026708933,0.000034097775,0.000008086196,0.000028748522,0.000021261789],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00019595363,0.0002565337,0.0002792072,0.0002180351,0.00016103935,0.00022817423,0.00014136874,0.0003710961,0.00030366398],"category_scores_gemma":[0.00021067123,0.00014406054,0.0001833012,0.00013603491,0.00014006067,0.00029008396,0.00014769769,0.00023035008,0.00020121242],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012774825,0.0000015152933,0.000035855333,0.000014128069,0.000001332393,0.000006212655,0.000003001503,0.000014888554,0.99972063,0.000010739482,0.0000034313175,0.00017552334],"study_design_scores_gemma":[0.0000035234473,0.00001935569,0.0009689976,0.0000018250072,0.0000043943955,0.00002471302,0.000005987673,0.00030270725,0.99840075,0.000008468738,0.0002574544,0.0000017524562],"about_ca_topic_score_codex":0.0009936374,"about_ca_topic_score_gemma":0.0013771692,"teacher_disagreement_score":0.0009936374,"about_ca_system_score_codex":0.0003220534,"about_ca_system_score_gemma":0.00014931412,"threshold_uncertainty_score":0.0023367405},"labels":[],"label_agreement":null},{"id":"W2011685631","doi":"10.1002/ceat.201200211","title":"Estimation of Mixing Ratio for Saturated Air over Water","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Phase Equilibria and Thermodynamics","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Mixing ratio; Saturation (graph theory); Vapor pressure; Mixing (physics); Relative humidity; Thermodynamics; Water vapor; Humidity; Chemistry; Atmospheric pressure; Mechanics; Meteorology; Mathematics; Physics","score_opus":0.004158640790513775,"score_gpt":0.19817115356911752,"score_spread":0.19401251277860374,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2011685631","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8129596,0.0017952799,0.17889306,0.00005024774,0.000044516688,0.00011654283,0.0010045245,0.0012115677,0.0039246934],"genre_scores_gemma":[0.96787214,0.00044937976,0.030575695,0.00000961716,0.000006652781,0.00005523916,0.0003206734,0.000048815386,0.0006616738],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99954945,0.00008517874,0.000025740512,0.00008919303,0.0002173811,0.000033094053],"domain_scores_gemma":[0.9994572,0.00022001531,0.000101356316,0.000032301763,0.0001704886,0.000018667995],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0007116226,0.00041875875,0.00038098922,0.002023893,0.00017782854,0.00026842806,0.0005732217,0.00036416785,0.0009110915],"category_scores_gemma":[0.0015900817,0.00018644147,0.00032774924,0.0009137231,0.00013980581,0.0004528972,0.00019969237,0.00031373667,0.0005560269],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00043639058,0.000056365607,0.020724362,0.00038044192,0.00006789996,0.00015649873,0.0002004117,0.012413474,0.9060477,0.0008829349,0.00020055415,0.058432978],"study_design_scores_gemma":[0.00001027963,0.00026589527,0.025892178,0.000017593393,0.000052263546,0.00018017936,0.00008086989,0.14836442,0.8229554,0.00046926033,0.001670695,0.000040841624],"about_ca_topic_score_codex":0.00079874555,"about_ca_topic_score_gemma":0.00068776694,"teacher_disagreement_score":0.002023893,"about_ca_system_score_codex":0.00018539873,"about_ca_system_score_gemma":0.000146222,"threshold_uncertainty_score":0.0037634373},"labels":[],"label_agreement":null},{"id":"W2013570469","doi":"10.1002/ceat.200401996","title":"Coaxial Mixer Hydrodynamics with Newtonian and non‐Newtonian Fluids","year":2004,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":65,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Non-Newtonian fluid; Newtonian fluid; Mechanics; Coaxial; Mixing (physics); Power consumption; Rheology; Materials science; Power (physics); Physics; Mechanical engineering; Thermodynamics; Engineering","score_opus":0.0012316075191761832,"score_gpt":0.1447811621455941,"score_spread":0.14354955462641794,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2013570469","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98522204,0.0014630427,0.011759175,0.0000593524,0.000043820597,0.00005415065,0.00007091503,0.00009669623,0.0012307536],"genre_scores_gemma":[0.97603685,0.0012336737,0.020285783,0.0000252021,0.000060387774,0.0000494107,0.00023399058,0.000025776953,0.0020489623],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997224,0.00004984965,0.000025664463,0.000039107515,0.00012909414,0.000033889886],"domain_scores_gemma":[0.9994822,0.00018737321,0.00015523197,0.000024080626,0.00010428791,0.0000468145],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005850928,0.0004161861,0.0003861895,0.0004158286,0.00024304276,0.00043214942,0.00021188032,0.0002234611,0.0005662323],"category_scores_gemma":[0.00087873207,0.00013973437,0.00025607258,0.00044896096,0.00029976002,0.00033613687,0.0002545017,0.00037746265,0.000226067],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00039373265,0.000058810354,0.0010144095,0.00011421143,0.000011244294,0.000033333603,0.000041661922,0.0008097714,0.99115705,0.00020059569,0.000074799966,0.006090411],"study_design_scores_gemma":[0.000053213265,0.00077998097,0.0058182464,0.000005543844,0.000034526587,0.00008044401,0.000023668998,0.011297601,0.98010755,0.000041902385,0.0017451986,0.000012166457],"about_ca_topic_score_codex":0.0017540158,"about_ca_topic_score_gemma":0.0016415977,"teacher_disagreement_score":0.0017540158,"about_ca_system_score_codex":0.00037271762,"about_ca_system_score_gemma":0.0002539643,"threshold_uncertainty_score":0.0034876466},"labels":[],"label_agreement":null},{"id":"W2014242091","doi":"10.1002/ceat.201100655","title":"Dispersion Characteristics and Mass Transfer in a Pilot‐Scale Gas‐Liquid Oscillatory‐Plate Column","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dalhousie University; Western University","funders":"","keywords":"Mass transfer; Turbulence; Mechanics; Dispersion (optics); Dissipation; Turbulence kinetic energy; Mass transfer coefficient; Bubble; Superficial velocity; Chemistry; Amplitude; Flow (mathematics); Volumetric flow rate; Materials science; Analytical Chemistry (journal); Thermodynamics; Chromatography; Optics; Physics","score_opus":0.003446375523901161,"score_gpt":0.16412568919070405,"score_spread":0.16067931366680288,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2014242091","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9977913,0.00006181356,0.0018666008,0.000022064152,0.0000032019298,0.000014973755,0.000048768336,0.00004631596,0.00014498267],"genre_scores_gemma":[0.9969355,0.0000787753,0.0025061325,0.0000135747305,0.0000032998048,0.00002018228,0.00014614168,0.000011114995,0.0002853832],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999816,0.000037213562,0.00000974591,0.000035228622,0.00006393282,0.00003792857],"domain_scores_gemma":[0.9997843,0.00010685044,0.000020923482,0.000013653931,0.000041485273,0.000032708067],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025801355,0.00032052098,0.00034247345,0.00019439954,0.00024199623,0.0004862781,0.00033658135,0.00031629333,0.0004132702],"category_scores_gemma":[0.00046849932,0.00015455586,0.00017562915,0.0002028991,0.0003215481,0.00020666646,0.00014778307,0.0004446787,0.00019785417],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012886088,0.000085436805,0.00041146774,0.000022828439,0.000004089094,0.00003228519,0.00002502598,0.0004189329,0.9972728,0.000014043218,0.000017719578,0.0015665012],"study_design_scores_gemma":[0.000045163528,0.0016065977,0.0051122494,0.000004353986,0.000025639603,0.000057714977,0.000030828764,0.0073013,0.9853932,0.000023709816,0.00038591342,0.000013368085],"about_ca_topic_score_codex":0.0036530907,"about_ca_topic_score_gemma":0.002112799,"teacher_disagreement_score":0.0036530907,"about_ca_system_score_codex":0.00031789436,"about_ca_system_score_gemma":0.00034815507,"threshold_uncertainty_score":0.0072636604},"labels":[],"label_agreement":null},{"id":"W2017099970","doi":"10.1002/ceat.201400340","title":"Relationship between Pyrite in the Precursor and the Pore Structure of High‐Surface Area Activated Carbon Preparations","year":2014,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Supercapacitor Materials and Fabrication","field":"Materials Science","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan; Canadian Light Source (Canada)","funders":"","keywords":"Pyrite; Sulfur; Sulfide; Chemistry; Porosity; Activated carbon; Specific surface area; Chemical engineering; Inorganic chemistry; Volume (thermodynamics); Thioether; BET theory; Adsorption; Mineralogy; Catalysis; Organic chemistry","score_opus":0.009242233849384664,"score_gpt":0.20753909215491959,"score_spread":0.19829685830553492,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2017099970","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9966942,0.00032748384,0.0016438678,0.000020987896,0.000008643104,0.000013053448,0.00012766865,0.000058012698,0.0011060297],"genre_scores_gemma":[0.9987631,0.00008276514,0.00070151757,0.000005528265,0.000002077943,0.0000061841283,0.00009829606,0.0000068300324,0.0003337411],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998684,0.000011844069,0.000007340689,0.000033343644,0.000052804648,0.000026204716],"domain_scores_gemma":[0.99956805,0.0001475483,0.00008617421,0.000027995888,0.00010500445,0.00006531787],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013061365,0.00020490019,0.000082770595,0.00031631958,0.00012640332,0.00028324994,0.00020489337,0.00025779472,0.000792709],"category_scores_gemma":[0.00044576073,0.00016132352,0.00008514141,0.00016502863,0.00022143348,0.00020744432,0.00006822344,0.0003135441,0.000120431934],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000022422939,0.000007317025,0.00020498876,0.000017040034,0.0000027001136,0.000027461478,0.000010101627,0.000084707666,0.99912614,0.000053704545,0.000012361837,0.00043097106],"study_design_scores_gemma":[0.0000018754326,0.00005279499,0.0032547242,0.0000014337526,0.000003911855,0.000050178536,0.000011312064,0.0008068294,0.99560577,0.000015869822,0.00019289882,0.0000023644086],"about_ca_topic_score_codex":0.0009512927,"about_ca_topic_score_gemma":0.0015487005,"teacher_disagreement_score":0.0009512927,"about_ca_system_score_codex":0.00025141562,"about_ca_system_score_gemma":0.00014883763,"threshold_uncertainty_score":0.0026518703},"labels":[],"label_agreement":null},{"id":"W2018625503","doi":"10.1002/ceat.200800399","title":"An Engineering Model of a Disc Pump Stage for Heavy Oil","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Oil and Gas Production Techniques","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Schlumberger (Canada)","funders":"","keywords":"Laminar flow; Mechanics; Stage (stratigraphy); Flow (mathematics); Rotor (electric); Volumetric flow rate; Diffuser (optics); Materials science; Engineering; Mechanical engineering; Physics; Geology; Optics","score_opus":0.006989535727634902,"score_gpt":0.2130974632003911,"score_spread":0.2061079274727562,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2018625503","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.26035073,0.0005527634,0.6588302,0.00085570035,0.00015623827,0.00038494455,0.0008077057,0.0009176854,0.07714399],"genre_scores_gemma":[0.94927096,0.00028456608,0.018120889,0.000057573438,0.000021831249,0.00027186782,0.00016152245,0.000051655865,0.031759102],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9997639,0.00004505652,0.000009538224,0.000045773828,0.00010831529,0.000027434466],"domain_scores_gemma":[0.9998425,0.0000680338,0.000020369285,0.000013006439,0.0000399266,0.000016151924],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00023601156,0.00057010807,0.00063132256,0.00034821616,0.0009619201,0.0010851708,0.0012382788,0.0018526333,0.0050542285],"category_scores_gemma":[0.00054796296,0.00051537325,0.0005136825,0.0002697645,0.00088945136,0.0006939433,0.000584429,0.00050227926,0.00080609624],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000098166805,0.000045436496,0.00052669604,0.00009340701,0.000010543001,0.00029842905,0.00008488477,0.96767825,0.01737932,0.009780751,0.0004002817,0.0036038805],"study_design_scores_gemma":[0.000022598826,0.00006304781,0.00016168183,0.0000047495328,0.0000055755095,0.000033637938,0.000011481036,0.9963857,0.00156953,0.00074888475,0.000984228,0.000008887617],"about_ca_topic_score_codex":0.0070325662,"about_ca_topic_score_gemma":0.0032628276,"teacher_disagreement_score":0.0070325662,"about_ca_system_score_codex":0.0010759117,"about_ca_system_score_gemma":0.0012036775,"threshold_uncertainty_score":0.01690811},"labels":[],"label_agreement":null},{"id":"W2020458062","doi":"10.1002/ceat.200800132","title":"Continuous Multi‐Injection Reactor for Multipurpose Production – Part I","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Control Systems Optimization","field":"Engineering","cited_by":57,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Chemical reaction engineering; Reactor design; Modular design; Process engineering; Production (economics); Chemical reactor; Continuous stirred-tank reactor; Biochemical engineering; Nuclear engineering; Engineering; Waste management; Chemical engineering; Chemistry; Computer science; Catalysis; Organic chemistry","score_opus":0.008428850827318195,"score_gpt":0.19207892267852456,"score_spread":0.18365007185120635,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2020458062","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5842439,0.0022725463,0.37836847,0.00016132902,0.00010011092,0.0004331681,0.0008854382,0.0014860713,0.032049075],"genre_scores_gemma":[0.943953,0.00025631685,0.04979692,0.000024744633,0.000029573563,0.00017616719,0.0004643946,0.00017239293,0.0051266006],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99928457,0.00008191904,0.000021400776,0.00013269865,0.00039479817,0.00008461476],"domain_scores_gemma":[0.99932945,0.0002571989,0.00013462752,0.00010484002,0.00013346194,0.00004049926],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00096006104,0.0006193122,0.00056840415,0.00065162714,0.0004633452,0.001292602,0.0010870545,0.00045115105,0.0060857306],"category_scores_gemma":[0.0007385732,0.00046525386,0.0007697307,0.00045728366,0.00041955293,0.001041845,0.0006271528,0.00079425,0.0011659208],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008493168,0.00023383804,0.0014263942,0.00053638127,0.000026221669,0.00022152755,0.00006447925,0.030185955,0.89869773,0.011677038,0.0011289228,0.054952107],"study_design_scores_gemma":[0.00010062915,0.0014010422,0.0042207707,0.000032544278,0.00004505881,0.00033346002,0.000038426955,0.16371405,0.8142215,0.0034412937,0.012404877,0.000046438392],"about_ca_topic_score_codex":0.0006922939,"about_ca_topic_score_gemma":0.0006662462,"teacher_disagreement_score":0.0060857306,"about_ca_system_score_codex":0.0010307246,"about_ca_system_score_gemma":0.00081668084,"threshold_uncertainty_score":0.0203588},"labels":[],"label_agreement":null},{"id":"W2022032648","doi":"10.1002/ceat.201000400","title":"Thermogravimetry‐FTIR Analysis of Pyrolysis of Pyrolytic Lignin Extracted from Bio‐Oil","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Thermochemical Biomass Conversion Processes","field":"Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Pyrolytic carbon; Lignin; Pyrolysis; Fourier transform infrared spectroscopy; Thermogravimetry; Chemistry; Extraction (chemistry); Thermal stability; Nuclear chemistry; Materials science; Chemical engineering; Analytical Chemistry (journal); Organic chemistry; Inorganic chemistry","score_opus":0.004741834720989063,"score_gpt":0.18820587346121562,"score_spread":0.18346403874022654,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2022032648","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9897384,0.0004194802,0.0075469003,0.000026521535,0.0000133829535,0.0000150369615,0.00096099125,0.000031814554,0.0012476004],"genre_scores_gemma":[0.9929684,0.00027013975,0.0038575893,0.000015724107,0.0000025776299,0.000017065982,0.0010494948,0.000020976307,0.0017980742],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998784,0.000012450896,0.000008053344,0.000023334904,0.00006008032,0.00001761228],"domain_scores_gemma":[0.9998677,0.000035934827,0.000026458754,0.000008035935,0.000044920722,0.000016880731],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00015855364,0.00023861974,0.00012305018,0.0005639021,0.00018806603,0.00012596908,0.00018061051,0.00017729962,0.0013449353],"category_scores_gemma":[0.00029891304,0.00011308266,0.00017716055,0.00062893116,0.00015562269,0.00022736745,0.00008948031,0.00036782055,0.0002905722],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006559979,0.00001200607,0.000451976,0.000023968681,0.000003921308,0.000025237317,0.000030446052,0.00015470806,0.99808025,0.000050190924,0.000014930771,0.0010868739],"study_design_scores_gemma":[0.000003768546,0.00009013847,0.016325604,0.000009612954,0.000011814894,0.00008570908,0.00006680125,0.0029203044,0.97985786,0.000078673955,0.00054142793,0.000008393313],"about_ca_topic_score_codex":0.0010092633,"about_ca_topic_score_gemma":0.0011382614,"teacher_disagreement_score":0.0013449353,"about_ca_system_score_codex":0.00013649372,"about_ca_system_score_gemma":0.00017254753,"threshold_uncertainty_score":0.004499316},"labels":[],"label_agreement":null},{"id":"W2023958463","doi":"10.1002/ceat.200800564","title":"A Novel Liquid‐Solid Circulating Fluidized‐Bed Bioreactor for Biological Nutrient Removal from Municipal Wastewater","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Wastewater Treatment and Nitrogen Removal","field":"Environmental Science","cited_by":33,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Effluent; Chemistry; Bioreactor; Chemical oxygen demand; Phosphorus; Denitrification; Nitrification; Wastewater; Suspended solids; Fluidized bed; Biochemical oxygen demand; Nitrogen; Sewage treatment; Total suspended solids; Pulp and paper industry; Waste management; Environmental engineering; Environmental science; Organic chemistry","score_opus":0.014636912999673775,"score_gpt":0.2198573493146741,"score_spread":0.20522043631500034,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2023958463","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9681599,0.0009461527,0.029507583,0.00013378594,0.000060434348,0.000055804114,0.00013914761,0.00041389672,0.00058319134],"genre_scores_gemma":[0.9673858,0.00045894145,0.030384205,0.00005273235,0.000022989301,0.00006556129,0.00025721628,0.000021102287,0.001351463],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99976116,0.000036861806,0.000019540787,0.00005248932,0.0001066583,0.000023260516],"domain_scores_gemma":[0.9999225,0.0000151029335,0.00001923936,0.0000050927333,0.000021526032,0.000016551869],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00029648578,0.0005485394,0.0005973379,0.0002305841,0.00027686576,0.00050522,0.000768398,0.00058280164,0.00052962283],"category_scores_gemma":[0.00017852952,0.00020382303,0.00042832768,0.00021821917,0.00015306215,0.0004237987,0.00031225508,0.00041152255,0.00037627452],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000075237214,0.0000609404,0.0001527366,0.0000661922,0.0000045176957,0.000033235196,0.000009370429,0.00033079632,0.99525815,0.000029238268,0.000043710257,0.003935884],"study_design_scores_gemma":[0.000094323004,0.0010017906,0.0025700403,0.000013536071,0.000046845234,0.00024108721,0.000028347005,0.01638681,0.9771408,0.000031053212,0.0024181488,0.000027267497],"about_ca_topic_score_codex":0.0030989249,"about_ca_topic_score_gemma":0.0031176882,"teacher_disagreement_score":0.0030989249,"about_ca_system_score_codex":0.00059575896,"about_ca_system_score_gemma":0.0005902948,"threshold_uncertainty_score":0.006161809},"labels":[],"label_agreement":null},{"id":"W2032337683","doi":"10.1002/ceat.201100497","title":"Integration of H<sub>2</sub>‐Selective Membrane Reactors in the Integrated Gasification Combined Cycle for CO<sub>2</sub> Separation","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Carbon Dioxide Capture Technologies","field":"Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Helmholtz-Alberta Initiative","keywords":"Integrated gasification combined cycle; Flue gas; Water-gas shift reaction; Process engineering; Carbon capture and storage (timeline); Air separation; Waste management; Combined cycle; Syngas; Chemistry; Environmental science; Hydrogen; Gas turbines; Engineering; Mechanical engineering","score_opus":0.008164361271442551,"score_gpt":0.22324849588815496,"score_spread":0.2150841346167124,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2032337683","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99281365,0.0004016476,0.0057246787,0.000036454454,0.000024281331,0.00002028083,0.00004833997,0.00010282917,0.0008278627],"genre_scores_gemma":[0.99430215,0.00015353198,0.0048056594,0.000011340571,0.000004584208,0.000011686452,0.00004894151,0.000006166979,0.00065577263],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998179,0.000019954387,0.000007673317,0.00003540197,0.00007348909,0.00004553934],"domain_scores_gemma":[0.99992657,0.000013275739,0.000013459759,0.000008859587,0.000024280396,0.00001348453],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00016517297,0.00039680398,0.00034092806,0.00021238698,0.00018126992,0.00043296092,0.00039767098,0.0005245061,0.0005378538],"category_scores_gemma":[0.00020784246,0.00020107969,0.00030593344,0.00023478143,0.00025269287,0.000416247,0.00027143137,0.00038917008,0.00016612081],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00020720602,0.00006257399,0.00062827044,0.000053577627,0.000018586383,0.000086230306,0.000015419588,0.0012079404,0.9910664,0.00022087088,0.000059250928,0.0063737123],"study_design_scores_gemma":[0.000019688547,0.00024564573,0.0017058244,0.00000378019,0.00003347991,0.00007049752,0.000014483239,0.007892614,0.9892046,0.0000392031,0.00076391944,0.000006287247],"about_ca_topic_score_codex":0.0015744579,"about_ca_topic_score_gemma":0.0024084465,"teacher_disagreement_score":0.0015744579,"about_ca_system_score_codex":0.00043780365,"about_ca_system_score_gemma":0.00035743974,"threshold_uncertainty_score":0.00317657},"labels":[],"label_agreement":null},{"id":"W2033943225","doi":"10.1002/ceat.201000164","title":"Mass Transfer Behavior of Annular Ducts under Conditions with Superimposed Pulsating Flow","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University; SAIT Polytechnic","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Laminar flow; Laminar flow reactor; Mass transfer; Mechanics; Turbulence; Mass flow meter; Volumetric flow rate; Flow (mathematics); Flow coefficient; Open-channel flow; Isothermal flow; Annulus (botany); Residence time (fluid dynamics); Mass flow; Materials science; Chemistry; Thermodynamics; Physics; Geology","score_opus":0.006584949916901524,"score_gpt":0.16943733602354788,"score_spread":0.16285238610664635,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2033943225","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9979043,0.00013766914,0.0016688091,0.0000092846,0.000005690668,0.0000049581145,0.000031814638,0.000047335772,0.00019013693],"genre_scores_gemma":[0.99794394,0.00013371625,0.0014666019,0.000007449911,0.0000046057876,0.0000070929427,0.000057464975,0.000013191394,0.00036599158],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999752,0.000053689215,0.000019750007,0.00005013652,0.00007277971,0.0000515617],"domain_scores_gemma":[0.9994149,0.0002800312,0.00009179108,0.000052823398,0.000112739464,0.000047744044],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00044644473,0.00023782658,0.0004521053,0.00021370286,0.00016720765,0.00044475117,0.000266161,0.00024572885,0.0006539776],"category_scores_gemma":[0.0009855753,0.00015229492,0.00018653659,0.00025388927,0.00027949724,0.00040811568,0.00021132709,0.00037498734,0.00021380924],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023774242,0.000039136903,0.0005614993,0.000027959935,0.00000423584,0.000039117942,0.00008516405,0.00035359926,0.99569535,0.00005007157,0.000014905297,0.0028911019],"study_design_scores_gemma":[0.0000042862657,0.00029629705,0.0013521599,0.0000019310667,0.000006837346,0.000032043044,0.000021992766,0.0014403169,0.9966462,0.000015774132,0.00017837643,0.0000036956542],"about_ca_topic_score_codex":0.0003115376,"about_ca_topic_score_gemma":0.0001526638,"teacher_disagreement_score":0.0006539776,"about_ca_system_score_codex":0.000193071,"about_ca_system_score_gemma":0.00014988641,"threshold_uncertainty_score":0.0023609996},"labels":[],"label_agreement":null},{"id":"W2038757598","doi":"10.1002/ceat.200700263","title":"Numerical Investigation of Hydrocarbon Enrichment of Process Gas Mixtures by Permeation through Polymeric Membranes","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Membrane Separation and Gas Transport","field":"Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"National Research Council Canada","funders":"","keywords":"Permeance; Permeation; Membrane; Hydrocarbon mixtures; Polysulfone; Chemical engineering; Hydrocarbon; Chemistry; Thermodynamics; Materials science; Chromatography; Organic chemistry; Engineering","score_opus":0.0044639039875849894,"score_gpt":0.20978651922486172,"score_spread":0.20532261523727674,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2038757598","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97298235,0.0002231639,0.02139317,0.00023089522,0.00003082378,0.000046858953,0.0001414504,0.000114830786,0.004836385],"genre_scores_gemma":[0.9923545,0.00007066813,0.006696141,0.000017081427,0.0000045114625,0.000031892592,0.000038240207,0.000009141207,0.0007778393],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998895,0.000031772914,0.000006344416,0.000016143413,0.00003060891,0.00002559505],"domain_scores_gemma":[0.9993554,0.0004178342,0.0000776937,0.000031014195,0.00008503511,0.000033059867],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00036053505,0.0003561915,0.0005634073,0.0004151913,0.00049309054,0.00060311414,0.00047336158,0.0012347796,0.0010714919],"category_scores_gemma":[0.0011261024,0.00026457186,0.00042816353,0.00032260193,0.000780308,0.00041437557,0.0004074521,0.00041941757,0.00009995472],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017495136,0.0000701299,0.002235043,0.00007400013,0.000019575404,0.00019074703,0.00005534283,0.97617334,0.01705446,0.0017025638,0.00009344533,0.0021563084],"study_design_scores_gemma":[0.0000098808,0.000033099386,0.00022304546,0.0000025438505,0.0000026307453,0.0000092314085,0.000012672685,0.99775237,0.0017888268,0.00009558117,0.000066903296,0.0000032968694],"about_ca_topic_score_codex":0.007675326,"about_ca_topic_score_gemma":0.0025548853,"teacher_disagreement_score":0.007675326,"about_ca_system_score_codex":0.0007591875,"about_ca_system_score_gemma":0.0005462179,"threshold_uncertainty_score":0.015261292},"labels":[],"label_agreement":null},{"id":"W2039005885","doi":"10.1002/ceat.200401881","title":"Modeling Nonsteady‐State Regimes of Dilute Pneumatic Conveying","year":2004,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Mechanics; Pressure drop; Particle (ecology); Microscale chemistry; Materials science; Thermodynamics; Flow (mathematics); Steady state (chemistry); Pipeline transport; Chemistry; Physics; Geology","score_opus":0.004855355320165456,"score_gpt":0.17566321134584567,"score_spread":0.17080785602568022,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2039005885","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9791022,0.000051544197,0.019719137,0.000054812914,0.000006560394,0.000014830478,0.000037951108,0.00007719009,0.000935774],"genre_scores_gemma":[0.99917525,0.000021184866,0.000563032,0.0000033546187,0.0000017475147,0.0000065226077,0.000016178194,0.000002907098,0.00020970378],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9999298,0.000016484864,0.0000045391694,0.000011543167,0.00001759272,0.000019961091],"domain_scores_gemma":[0.99976176,0.00013438797,0.000042778258,0.000015881164,0.000022885675,0.000022346554],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00023866273,0.0003222343,0.00033597174,0.00031019945,0.00031846223,0.0005632843,0.00037570499,0.0005428005,0.0004116032],"category_scores_gemma":[0.00071775547,0.00022952378,0.00028423732,0.00015978146,0.00086760684,0.00049014203,0.00034266795,0.00035625874,0.000043985998],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010188831,0.000065892214,0.0030263586,0.000025589045,0.000011917171,0.00014056725,0.00006116439,0.9815948,0.010607547,0.002540753,0.000075163414,0.0017484146],"study_design_scores_gemma":[0.000004868246,0.000018415229,0.000515748,7.8378804e-7,0.000001711526,0.000004127877,0.0000049355285,0.9981761,0.0010090242,0.00022676957,0.000035305766,0.0000022044103],"about_ca_topic_score_codex":0.0067424215,"about_ca_topic_score_gemma":0.0022116536,"teacher_disagreement_score":0.0067424215,"about_ca_system_score_codex":0.0006900728,"about_ca_system_score_gemma":0.000355914,"threshold_uncertainty_score":0.013406336},"labels":[],"label_agreement":null},{"id":"W2040022949","doi":"10.1002/ceat.200800385","title":"New Turbine Impellers for Viscous Mixing","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":23,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Mixing (physics); Turbine; Power consumption; Mechanical engineering; Flow (mathematics); Mechanics; Materials science; Power (physics); Base (topology); Engineering; Physics; Mathematics; Thermodynamics; Mathematical analysis","score_opus":0.004567985302472233,"score_gpt":0.17596300980040389,"score_spread":0.17139502449793165,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2040022949","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.6661405,0.0033423242,0.32231838,0.00024322254,0.0007846025,0.00019538833,0.00024139918,0.0013365542,0.00539768],"genre_scores_gemma":[0.87561417,0.0007241266,0.11766567,0.000090436835,0.00015101142,0.00013474881,0.00034594926,0.00008866911,0.0051851207],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9995548,0.000050500803,0.00003087856,0.00006639839,0.00024288078,0.000054595745],"domain_scores_gemma":[0.9993162,0.00013883527,0.0001325081,0.00008236581,0.00022154076,0.00010853132],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006407883,0.0003629373,0.0004655163,0.0006753998,0.00026608285,0.0005227555,0.0006712871,0.00047245726,0.0014866061],"category_scores_gemma":[0.0010726792,0.0002894883,0.00029948924,0.0003290002,0.00051359384,0.00081196416,0.00046537496,0.00053324335,0.0005709311],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005377877,0.00013552286,0.0015467309,0.0003190653,0.000020474867,0.00030787417,0.0001291088,0.0032119737,0.9047749,0.0062871743,0.0018384368,0.08089087],"study_design_scores_gemma":[0.00030963024,0.003345072,0.01644879,0.00005505837,0.00013336934,0.0015444042,0.00005659063,0.056187313,0.84331715,0.0019343948,0.07649031,0.00017790424],"about_ca_topic_score_codex":0.0001347384,"about_ca_topic_score_gemma":0.00027946208,"teacher_disagreement_score":0.0014866061,"about_ca_system_score_codex":0.00021731223,"about_ca_system_score_gemma":0.0001884958,"threshold_uncertainty_score":0.004973173},"labels":[],"label_agreement":null},{"id":"W2043281939","doi":"10.1002/ceat.200900615","title":"Designing and Testing a Chemical Demulsifier Dosage Controller in a Crude Oil Desalting Plant: An Artificial Intelligence‐Based Network Approach","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fault Detection and Control Systems","field":"Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Demulsifier; Controller (irrigation); Artificial neural network; Process engineering; Engineering; Chemical plant; Crude oil; Petroleum engineering; Computer science; Environmental engineering; Artificial intelligence","score_opus":0.01569951039840478,"score_gpt":0.21038507357116729,"score_spread":0.1946855631727625,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2043281939","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.7868161,0.00020967076,0.20630954,0.00021104091,0.000069378875,0.00031741904,0.00009882143,0.0011563658,0.004811614],"genre_scores_gemma":[0.9798379,0.000043490152,0.018890534,0.000024639283,0.000004040272,0.000074291456,0.00003131158,0.000010019051,0.0010836825],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9997706,0.000047352263,0.000019624036,0.0000613255,0.000076167984,0.000024881125],"domain_scores_gemma":[0.99942386,0.00029480722,0.00006008417,0.000039878345,0.00015966388,0.000021797538],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000550005,0.00062001473,0.00039789415,0.00026795937,0.00031298533,0.00043314544,0.00069573516,0.00069376675,0.0010797457],"category_scores_gemma":[0.0009661176,0.00027253293,0.0002486643,0.00010622983,0.00029349676,0.0003883359,0.00022944763,0.0005181935,0.00013603334],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00047745818,0.0004987592,0.0061346004,0.000360932,0.00009480943,0.00025453608,0.00016380555,0.80696356,0.103808485,0.0006546878,0.00033938256,0.0802491],"study_design_scores_gemma":[0.000023756333,0.00024904555,0.001264229,0.000006955242,0.000019161964,0.000017640055,0.000013414702,0.9544177,0.04358533,0.00008466894,0.00030891795,0.000009164404],"about_ca_topic_score_codex":0.0075083137,"about_ca_topic_score_gemma":0.005278717,"teacher_disagreement_score":0.0075083137,"about_ca_system_score_codex":0.0007571364,"about_ca_system_score_gemma":0.0004466699,"threshold_uncertainty_score":0.014929235},"labels":[],"label_agreement":null},{"id":"W2044779468","doi":"10.1002/ceat.200800309","title":"Reactor Technologies for Propane Partial Oxidation to Acrylic Acid","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysis and Oxidation Reactions","field":"Chemical Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Propane; Acrylic acid; Fluidized bed; Selectivity; Raw material; Chemical engineering; Partial oxidation; Heat transfer; Materials science; Catalysis; Waste management; Process engineering; Chemistry; Organic chemistry; Thermodynamics; Polymer; Engineering; Copolymer","score_opus":0.009025221807072806,"score_gpt":0.23215432967821098,"score_spread":0.22312910787113818,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2044779468","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.39146203,0.037376236,0.50027186,0.0013270695,0.0012446622,0.0011400682,0.0014241844,0.0029341343,0.062819734],"genre_scores_gemma":[0.77484995,0.01567018,0.17496398,0.00027289646,0.00015827209,0.00062934164,0.0016608655,0.00015658188,0.03163791],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99960285,0.00004183492,0.000018982435,0.000065007924,0.00022128815,0.00005006512],"domain_scores_gemma":[0.99984586,0.000034934652,0.000022397959,0.00002636468,0.00005019893,0.000020190686],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00043934595,0.00041659336,0.00042884875,0.0008907044,0.00053206296,0.0005907051,0.0007121507,0.0005935831,0.0052562305],"category_scores_gemma":[0.00039003568,0.0003778257,0.00056079816,0.0005068557,0.00020204023,0.0006585851,0.0004422796,0.0013444051,0.0029082322],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006654098,0.000051503986,0.00018263196,0.0007247824,0.000018554118,0.000103469974,0.000039651706,0.0007387786,0.9632625,0.004081599,0.0010765186,0.029653436],"study_design_scores_gemma":[0.000043149343,0.00042352185,0.0011923491,0.000058134705,0.00003679667,0.0005262427,0.00003198289,0.004355856,0.9339559,0.0010327277,0.05831967,0.000023486127],"about_ca_topic_score_codex":0.0011506606,"about_ca_topic_score_gemma":0.0015856834,"teacher_disagreement_score":0.0052562305,"about_ca_system_score_codex":0.0006606851,"about_ca_system_score_gemma":0.00052664196,"threshold_uncertainty_score":0.017583847},"labels":[],"label_agreement":null},{"id":"W2048895654","doi":"10.1002/ceat.200401954","title":"The Effect of Solids Inventory and Other Factors on the Axial Solids Holdup Profiles in a Twin‐Riser System","year":2004,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Minerals Flotation and Separation Techniques","field":"Environmental Science","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Suspended solids; Total dissolved solids; Flux (metallurgy); Volatile suspended solids; Total suspended solids; Materials science; Chemistry; Mechanics; Environmental science; Environmental engineering; Metallurgy; Physics","score_opus":0.005997049358537965,"score_gpt":0.21167781660909088,"score_spread":0.20568076725055293,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2048895654","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9980332,0.000056812,0.0016546487,0.00000985336,0.0000022981317,0.0000040978316,0.000035108234,0.00006455976,0.00013942063],"genre_scores_gemma":[0.99895716,0.000030250945,0.00079301564,0.000003997226,9.082561e-7,0.000002632335,0.000043876815,0.000008682428,0.00015929402],"study_design_codex":"bench_or_experimental","study_design_gemma":"observational","domain_scores_codex":[0.99964976,0.000056398923,0.00003655738,0.000070820766,0.00010528178,0.00008121607],"domain_scores_gemma":[0.9991831,0.00027629585,0.00014448432,0.00007106977,0.00024827753,0.000076765784],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005104642,0.00032984914,0.00061351253,0.0004248344,0.0004489034,0.0006449417,0.00031729607,0.00030534662,0.0007249194],"category_scores_gemma":[0.0011400578,0.00031803714,0.00029186107,0.00043187616,0.00040359062,0.00059757853,0.00030268266,0.00033806096,0.00022592024],"study_design_candidate":"observational","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0023526787,0.00008594176,0.01009711,0.00011471962,0.00002972417,0.0003050226,0.00023615612,0.014868998,0.95823616,0.00016067002,0.00006246931,0.013450383],"study_design_scores_gemma":[0.00005026916,0.0016058654,0.032834277,0.0000091128995,0.00007736212,0.00022505021,0.00028459055,0.061991055,0.9023348,0.00010678264,0.00042505958,0.00005580449],"about_ca_topic_score_codex":0.0019482364,"about_ca_topic_score_gemma":0.002068903,"teacher_disagreement_score":0.0019482364,"about_ca_system_score_codex":0.0004843038,"about_ca_system_score_gemma":0.0003613573,"threshold_uncertainty_score":0.0038737655},"labels":[],"label_agreement":null},{"id":"W2054908466","doi":"10.1002/ceat.201100376","title":"Adsorption Characteristics of Atrazine on Granulated Activated Carbon and Carbon Nanotubes","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Adsorption and biosorption for pollutant removal","field":"Environmental Science","cited_by":45,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Adsorption; Freundlich equation; Activated carbon; Exothermic reaction; Aqueous solution; Chemistry; Langmuir; Carbon nanotube; Kinetics; Exothermic process; Chemical engineering; Endothermic process; Carbon fibers; Thermodynamics; Materials science; Organic chemistry; Composite material; Composite number","score_opus":0.005063179742770221,"score_gpt":0.1875181429476058,"score_spread":0.18245496320483556,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2054908466","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9991333,0.00019324658,0.00030975312,0.000010593671,0.000004823405,0.0000061191768,0.00011189119,0.000009217511,0.00022113782],"genre_scores_gemma":[0.9985368,0.00017483415,0.00052291364,0.000011055275,0.000003529962,0.000010311039,0.00020222807,0.000005510487,0.0005326478],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997609,0.000027938338,0.000016978976,0.000042449286,0.00011737525,0.000034319644],"domain_scores_gemma":[0.9998018,0.000049172057,0.000037627855,0.000013254033,0.00008103151,0.000017022263],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00015732116,0.0002495093,0.00028255404,0.00039472384,0.00017858112,0.00018795076,0.00022973,0.000491248,0.00071670825],"category_scores_gemma":[0.00044624516,0.0001483921,0.00027132969,0.0003238879,0.00017237192,0.0002002688,0.00011636976,0.00016350274,0.00020900322],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014930102,0.000015666941,0.0005595599,0.000046547066,0.0000077069535,0.00005693843,0.000019640405,0.00057024346,0.9977933,0.000019842642,0.000018361685,0.0007428927],"study_design_scores_gemma":[0.000020584326,0.000431799,0.020180786,0.000008432199,0.000023881174,0.00012332929,0.000044241482,0.006043075,0.97255796,0.000037364825,0.000511802,0.000016779317],"about_ca_topic_score_codex":0.0033932906,"about_ca_topic_score_gemma":0.0024345093,"teacher_disagreement_score":0.0033932906,"about_ca_system_score_codex":0.00034475492,"about_ca_system_score_gemma":0.00015224033,"threshold_uncertainty_score":0.006747067},"labels":[],"label_agreement":null},{"id":"W2055444611","doi":"10.1002/ceat.201200669","title":"Dual Effect of Low‐Dosage Poly(Ethylene Oxides) on Methane Hydrate Formation","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Hydrate; Methane; Nucleation; Clathrate hydrate; Chemistry; Isochoric process; Ethylene; Chemical engineering; Inorganic chemistry; Organic chemistry; Thermodynamics; Catalysis","score_opus":0.002395711124997053,"score_gpt":0.17487990812321985,"score_spread":0.1724841969982228,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2055444611","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99850285,0.0004847799,0.00042983313,0.000015858172,0.000009424534,0.000009723293,0.00006945562,0.000019615516,0.0004585549],"genre_scores_gemma":[0.99829763,0.00024308986,0.0008954426,0.000010626411,0.000006469316,0.000011397104,0.00005201115,0.0000075832213,0.00047589646],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998784,0.00003060878,0.000012130407,0.000026911664,0.0000321,0.000019842413],"domain_scores_gemma":[0.9997397,0.00011584724,0.000057039542,0.000018576435,0.000032520522,0.000036260863],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012894612,0.00030116254,0.00023336158,0.00016872899,0.000085116895,0.00023662669,0.00015285985,0.00018576272,0.000769006],"category_scores_gemma":[0.00043722772,0.00011880371,0.00014868996,0.000111156776,0.00018841421,0.00023105374,0.00016152284,0.0003145591,0.00011308719],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028298714,0.000029552433,0.00012314746,0.000058587135,0.0000055781024,0.000023828008,0.000011864358,0.00007706901,0.99813324,0.000018170438,0.000012025261,0.0012239217],"study_design_scores_gemma":[0.000005261835,0.00025442534,0.00076671236,0.000002380192,0.000008030751,0.00001372444,0.0000046165305,0.00031996868,0.9984378,0.0000026075886,0.00018237875,0.0000021712317],"about_ca_topic_score_codex":0.00031832958,"about_ca_topic_score_gemma":0.00057227025,"teacher_disagreement_score":0.000769006,"about_ca_system_score_codex":0.0001226022,"about_ca_system_score_gemma":0.00009632462,"threshold_uncertainty_score":0.002572596},"labels":[],"label_agreement":null},{"id":"W2058264227","doi":"10.1002/ceat.200800351","title":"A Practical Method to Estimate the Bed Height of a Fluidized Bed of Fine Particles","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"China Scholarship Council; University of British Columbia; National Natural Science Foundation of China","keywords":"Freeboard; Fluidized bed; Fluidization; Mechanics; Materials science; Engineering; Waste management; Physics","score_opus":0.012801111761589812,"score_gpt":0.27413124713950815,"score_spread":0.2613301353779183,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2058264227","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.069609165,0.00031450877,0.9277803,0.000057535464,0.000052591575,0.00009895409,0.00019026919,0.0009813485,0.00091536524],"genre_scores_gemma":[0.54560775,0.00019050916,0.45299402,0.000034632147,0.00001835273,0.00012320917,0.00021070235,0.000030166622,0.00079055026],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9994104,0.00012697576,0.000026408345,0.00009405115,0.0003188477,0.000023367997],"domain_scores_gemma":[0.999079,0.00038506222,0.00009482679,0.0001236053,0.00028599272,0.000031603853],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005297223,0.0005523433,0.00039228422,0.0011058057,0.00028706365,0.00038038916,0.0006457785,0.00061773177,0.00089274615],"category_scores_gemma":[0.0020261053,0.00025609383,0.00021317882,0.0005146632,0.0002763333,0.00044419424,0.0005170245,0.00036920086,0.00040691433],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00034893685,0.0001869141,0.016976552,0.0005952932,0.00007906497,0.00023959654,0.00023991891,0.093838565,0.44395238,0.004556973,0.001574223,0.43741164],"study_design_scores_gemma":[0.00003338285,0.00020367531,0.0092208125,0.000031848456,0.00002963553,0.00021884916,0.00007467252,0.809218,0.17720373,0.0014205738,0.0022753535,0.000069476635],"about_ca_topic_score_codex":0.0019105033,"about_ca_topic_score_gemma":0.002315971,"teacher_disagreement_score":0.0019105033,"about_ca_system_score_codex":0.00033741762,"about_ca_system_score_gemma":0.0004758972,"threshold_uncertainty_score":0.0037987828},"labels":[],"label_agreement":null},{"id":"W2060750406","doi":"10.1002/ceat.200700413","title":"Separation of Shikimic Acid from Pine Needles","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Protein purification and stability","field":"Biochemistry, Genetics and Molecular Biology","cited_by":35,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Shikimic acid; Chemistry; Adsorption; Desorption; Crystallization; Chromatography; Organic chemistry","score_opus":0.006828580443087106,"score_gpt":0.21476219410129352,"score_spread":0.20793361365820642,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2060750406","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.93959475,0.01965511,0.030762725,0.000209816,0.00017246917,0.00013064624,0.0022363923,0.00034135385,0.006896731],"genre_scores_gemma":[0.96969676,0.005276113,0.01348694,0.00014455535,0.00005519403,0.00004473237,0.0029034163,0.000076742755,0.008315579],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99992836,0.000007977868,0.00000405823,0.000020636258,0.000021724969,0.000017295664],"domain_scores_gemma":[0.99991417,0.00001592068,0.00001824281,0.000007047155,0.000022096656,0.000022581284],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000085596475,0.00049268815,0.00036091093,0.00041768514,0.00031849317,0.00032361323,0.00018282903,0.00021804924,0.0015545394],"category_scores_gemma":[0.00014176319,0.000109474764,0.00020044531,0.00026126305,0.00014325182,0.00032124232,0.00017676553,0.0006104055,0.0010852438],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003841112,0.0000086662185,0.0002275828,0.00005157736,0.0000044286057,0.000083729174,0.000016463182,0.000030336992,0.99692756,0.000040693256,0.000030836753,0.002539785],"study_design_scores_gemma":[0.0000112043535,0.000120685596,0.005754154,0.000026484622,0.000015511025,0.00037230545,0.00007190087,0.00041327722,0.98695,0.00015472858,0.006097735,0.000012040559],"about_ca_topic_score_codex":0.0014160473,"about_ca_topic_score_gemma":0.0021800087,"teacher_disagreement_score":0.0015545394,"about_ca_system_score_codex":0.00014373001,"about_ca_system_score_gemma":0.00030129869,"threshold_uncertainty_score":0.0052005053},"labels":[],"label_agreement":null},{"id":"W2068154599","doi":"10.1002/ceat.201000441","title":"Aging and Thermal Stability of the Mixed Product of the Ether‐Soluble Fraction of Bio‐Oil and Bio‐Diesel","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Thermochemical Biomass Conversion Processes","field":"Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada; National Key Research and Development Program of China; China Scholarship Council","keywords":"Diesel fuel; Thermogravimetric analysis; Fraction (chemistry); Gel permeation chromatography; Chemistry; Mass fraction; Thermal stability; Viscosity; Fourier transform infrared spectroscopy; Chemical engineering; Thermal decomposition; Ether; Pyrolysis oil; Decomposition; Analytical Chemistry (journal); Pyrolysis; Materials science; Chromatography; Organic chemistry; Composite material; Polymer","score_opus":0.008607473828117102,"score_gpt":0.17430671333144396,"score_spread":0.16569923950332685,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2068154599","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9984112,0.0005200573,0.0007008498,0.0000063952275,0.000010589659,0.000004049075,0.00013518913,0.00000925544,0.00020243184],"genre_scores_gemma":[0.9983746,0.00023256618,0.00049722515,0.000005743445,0.0000027908736,0.0000048289626,0.00020081736,0.000009634572,0.000671797],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998678,0.000012264234,0.000015469299,0.000032464475,0.00004595504,0.000025981763],"domain_scores_gemma":[0.99981016,0.00002971281,0.000055127723,0.000013601648,0.000059957856,0.000031396572],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000238574,0.0002794946,0.00026719048,0.00030104024,0.00014028802,0.00026117812,0.00014261056,0.00018671257,0.0010547563],"category_scores_gemma":[0.00035991313,0.00013013676,0.00020560024,0.00032052892,0.00015458668,0.00037828702,0.0001404781,0.00028977907,0.00022099688],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033207226,0.000024582347,0.0011237059,0.00002451829,0.000017672413,0.000041013132,0.000028208162,0.000144582,0.9968803,0.000028208726,0.000011076677,0.0013441566],"study_design_scores_gemma":[0.000003531712,0.00023268293,0.006695468,0.000004371968,0.000026246169,0.000056440233,0.00003512052,0.0009714465,0.9916224,0.000010696586,0.00033487522,0.00000672551],"about_ca_topic_score_codex":0.00087537727,"about_ca_topic_score_gemma":0.00085604825,"teacher_disagreement_score":0.0010547563,"about_ca_system_score_codex":0.00020048201,"about_ca_system_score_gemma":0.00011438124,"threshold_uncertainty_score":0.0035285354},"labels":[],"label_agreement":null},{"id":"W2070801510","doi":"10.1002/ceat.200390014","title":"Simulation of Pipeline Slurry Flow under Conditions of Granular Phase Ablation","year":2003,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Geotechnical and Geomechanical Engineering","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Slurry; Mechanics; Flow (mathematics); Suspension (topology); Two-phase flow; Materials science; Volumetric flow rate; Granular material; Mass transfer; Chemistry; Mathematics; Composite material; Physics","score_opus":0.0065986383797576875,"score_gpt":0.2192553292631243,"score_spread":0.2126566908833666,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2070801510","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97748315,0.00006321345,0.018129496,0.00015311163,0.000018223345,0.000041986124,0.00028440694,0.00019462571,0.0036318572],"genre_scores_gemma":[0.9981243,0.000026150303,0.0011391144,0.000006533013,0.0000021498827,0.00002038492,0.000089940935,0.000007697088,0.00058377156],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998721,0.000033798704,0.000005808973,0.000023048538,0.000025063227,0.000040127616],"domain_scores_gemma":[0.9996489,0.0001960636,0.000038884118,0.000021090504,0.00003911225,0.000055970173],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002532643,0.00044533663,0.00064628583,0.00035094444,0.00042953755,0.00071955187,0.0006267324,0.0014421565,0.0013925915],"category_scores_gemma":[0.00092662976,0.0003137618,0.000484461,0.0003815599,0.00078449136,0.00060760346,0.00044869076,0.0005061578,0.00014382982],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010761441,0.000046572095,0.0009411721,0.000016327684,0.000006685191,0.00012931006,0.00002504711,0.99485517,0.0026532554,0.0005669332,0.00007342662,0.0005785303],"study_design_scores_gemma":[0.000018893723,0.000040504707,0.00025434236,0.0000012190346,0.0000022418742,0.000006419345,0.000009031031,0.9989759,0.0005177388,0.00011335812,0.000056957168,0.000003453686],"about_ca_topic_score_codex":0.012702336,"about_ca_topic_score_gemma":0.0030660813,"teacher_disagreement_score":0.012702336,"about_ca_system_score_codex":0.0008181167,"about_ca_system_score_gemma":0.0007687166,"threshold_uncertainty_score":0.025256813},"labels":[],"label_agreement":null},{"id":"W2073284633","doi":"10.1002/1521-4125(200008)23:8<701::aid-ceat701>3.0.co;2-8","title":"A Comparison of Solids Fluxes in a Pair of Downer and Riser Reactors","year":2000,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Flux (metallurgy); Mechanics; Fluidized bed combustion; Materials science; Fluidization; Position (finance); Thermodynamics; Fluidized bed; Physics","score_opus":0.005388487372394304,"score_gpt":0.21076174165442232,"score_spread":0.20537325428202802,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073284633","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99578923,0.00019312344,0.0032411255,0.000032018426,0.000026594857,0.000016484297,0.00013797513,0.00008985366,0.00047365972],"genre_scores_gemma":[0.99030733,0.00018083582,0.0077785053,0.000038718677,0.000012413672,0.000037565136,0.00035016192,0.00006896146,0.0012255525],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99849844,0.0002148815,0.00009595615,0.00043494525,0.00053237827,0.00022335682],"domain_scores_gemma":[0.9987935,0.0004217535,0.0001828166,0.00015223128,0.00031640095,0.00013343476],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00094725617,0.00069129514,0.0020947442,0.0008512772,0.000664384,0.0014908591,0.0006601287,0.0015137647,0.0011615078],"category_scores_gemma":[0.0019251343,0.0004911155,0.00058251846,0.00076107663,0.0007639428,0.0011040979,0.0007295099,0.0013311964,0.00042440675],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.001151877,0.00008349404,0.0018278117,0.000056819732,0.000016926142,0.00013563539,0.0001305752,0.00050992536,0.99229395,0.00017891156,0.000032825985,0.0035811963],"study_design_scores_gemma":[0.000057683574,0.0013521716,0.011772742,0.000006726194,0.000044247823,0.00015487001,0.0001549743,0.004255712,0.9812402,0.00009980125,0.0008247258,0.00003616903],"about_ca_topic_score_codex":0.0014656055,"about_ca_topic_score_gemma":0.0010823249,"teacher_disagreement_score":0.0020947442,"about_ca_system_score_codex":0.0005368039,"about_ca_system_score_gemma":0.00036760533,"threshold_uncertainty_score":0.0050095916},"labels":[],"label_agreement":null},{"id":"W2073629333","doi":"10.1002/1521-4125(200101)24:1<85::aid-ceat85>3.0.co;2-p","title":"Heat Transfer in the Downer and the Riser of a Circulating Fluidized Bed - A Comparative Study","year":2001,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":28,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Heat transfer; Suspension (topology); Fluidized bed combustion; Heat transfer coefficient; Mechanics; Fluidized bed; Thermodynamics; Materials science; Fluidization; Flow (mathematics); Particle (ecology); Chemistry; Geology; Physics","score_opus":0.009429371122619344,"score_gpt":0.2101107183902503,"score_spread":0.20068134726763096,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2073629333","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9971077,0.0002601905,0.0019920357,0.00002135452,0.000011821622,0.000010772479,0.000028937286,0.000050667702,0.0005165693],"genre_scores_gemma":[0.99763393,0.00013159575,0.0012402959,0.000010832469,0.000009032949,0.000006671604,0.000058720056,0.000011923652,0.0008969961],"study_design_codex":"bench_or_experimental","study_design_gemma":"observational","domain_scores_codex":[0.9996761,0.000057431418,0.0000131681345,0.00006903953,0.00011910421,0.00006526976],"domain_scores_gemma":[0.99958664,0.00021842742,0.000035393477,0.00004164767,0.00007995128,0.000037980786],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00038081492,0.00028178035,0.00086608087,0.00038593664,0.0003526327,0.0007614372,0.00043988027,0.00040812365,0.0016994867],"category_scores_gemma":[0.0008321314,0.00021556555,0.00034336283,0.00025667806,0.00055050955,0.0008105278,0.00030682376,0.00052636646,0.00028664712],"study_design_candidate":"observational","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00076102256,0.00013461002,0.001783566,0.00014175734,0.000011771181,0.00019367137,0.00023034494,0.0031847563,0.97897273,0.00047928278,0.000082166334,0.014024279],"study_design_scores_gemma":[0.000046074212,0.0007841117,0.009240108,0.0000064392384,0.000024727004,0.00013405975,0.00011787372,0.019158933,0.96930534,0.00014087322,0.0010167666,0.00002456792],"about_ca_topic_score_codex":0.0018947943,"about_ca_topic_score_gemma":0.0010408384,"teacher_disagreement_score":0.0018947943,"about_ca_system_score_codex":0.0004321167,"about_ca_system_score_gemma":0.00022804958,"threshold_uncertainty_score":0.0056853294},"labels":[],"label_agreement":null},{"id":"W2074086104","doi":"10.1002/ceat.201200108","title":"Oxidation Kinetics of Carbon Deposited on Cerium‐Doped FePO<sub>4</sub> during Dehydration of Glycerol to Acrolein","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalytic Processes in Materials Science","field":"Materials Science","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Acrolein; Glycerol; Chemistry; Catalysis; Oxygen; Cerium; Carbon fibers; Inorganic chemistry; Adsorption; Yield (engineering); Kinetics; Dehydration; Organic chemistry; Materials science; Biochemistry","score_opus":0.004782843708082806,"score_gpt":0.20425998898423528,"score_spread":0.19947714527615248,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2074086104","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99881727,0.00011415935,0.00032882864,0.000013988971,0.000007972743,0.0000039317297,0.00007195321,0.000022195562,0.0006196635],"genre_scores_gemma":[0.9990895,0.00006636387,0.00024344957,0.0000052201713,0.0000012182227,0.0000024135581,0.00007338255,0.000008765283,0.00050970714],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998946,0.0000062347317,0.0000040538225,0.000021919483,0.00003410656,0.0000391194],"domain_scores_gemma":[0.99986446,0.000051026494,0.000023643977,0.000009761721,0.00003243735,0.000018682123],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010160716,0.0002651021,0.00025052906,0.0002603023,0.00020767389,0.000277372,0.000253035,0.0004006357,0.0014310648],"category_scores_gemma":[0.0003351814,0.00016682179,0.00019068766,0.00019269728,0.0002632825,0.00025133602,0.00011033791,0.00029300412,0.00022355553],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00032130157,0.00002171156,0.0005066385,0.00004663726,0.000008936268,0.000115373296,0.00003936404,0.00066454225,0.99691725,0.000068049216,0.00003944401,0.0012507773],"study_design_scores_gemma":[0.000009917182,0.00010637093,0.0042909207,0.0000048277757,0.0000088376,0.000035395704,0.000029014982,0.004354738,0.99079436,0.000021371427,0.0003370649,0.0000071084],"about_ca_topic_score_codex":0.003514231,"about_ca_topic_score_gemma":0.0033853354,"teacher_disagreement_score":0.003514231,"about_ca_system_score_codex":0.0005280511,"about_ca_system_score_gemma":0.00015828658,"threshold_uncertainty_score":0.0069875717},"labels":[],"label_agreement":null},{"id":"W2076432505","doi":"10.1002/ceat.200301652","title":"Performance of a New Mixed Down Pumping Impeller","year":2003,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Cavitation Phenomena in Pumps","field":"Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Mixing (physics); Power consumption; Turbine; Mechanics; Dispersion (optics); Non-Newtonian fluid; Newtonian fluid; Flow (mathematics); Materials science; Power (physics); Mechanical engineering; Thermodynamics; Optics; Engineering; Physics","score_opus":0.00501935682459567,"score_gpt":0.17800735344933982,"score_spread":0.17298799662474415,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2076432505","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.964891,0.00034276373,0.031598065,0.00010089852,0.00012859685,0.00005999302,0.00017749597,0.00051975047,0.0021814394],"genre_scores_gemma":[0.98625714,0.00012648606,0.0105190715,0.00003077694,0.000026388407,0.000028016231,0.00022095542,0.000047458016,0.0027437024],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99965453,0.000029469744,0.000026422882,0.00007075009,0.00017804661,0.000040753857],"domain_scores_gemma":[0.9996517,0.00007257266,0.00006661255,0.000051318908,0.0001053945,0.000052450643],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046837475,0.0005531465,0.0004864513,0.00030901493,0.00025392047,0.0006831211,0.00067983125,0.00052311807,0.0018552912],"category_scores_gemma":[0.00068615505,0.00026975936,0.0002650632,0.00015977217,0.00025322783,0.0007246814,0.00032140347,0.0003589044,0.00070222997],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0006338014,0.000053557935,0.00066438125,0.0001418172,0.000013959463,0.00019790065,0.00005180297,0.0015577839,0.9787643,0.0001778152,0.00023942397,0.017503424],"study_design_scores_gemma":[0.00012691515,0.0032128757,0.0073412177,0.0000114454915,0.000062441264,0.000804266,0.000030469455,0.022052152,0.958911,0.00004539217,0.0073427507,0.00005911088],"about_ca_topic_score_codex":0.0003167967,"about_ca_topic_score_gemma":0.00015783955,"teacher_disagreement_score":0.0018552912,"about_ca_system_score_codex":0.00019821594,"about_ca_system_score_gemma":0.00018260654,"threshold_uncertainty_score":0.006206572},"labels":[],"label_agreement":null},{"id":"W2078896921","doi":"10.1002/ceat.201100563","title":"Improvement of the Uniformity of Radial Solids Concentration Profiles in Circulating Fluidized‐Bed Risers","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Fluidized bed combustion; Mechanics; Computational fluid dynamics; Jet (fluid); Fluidized bed; Materials science; Fluid catalytic cracking; Flow (mathematics); Eulerian path; Kinetic energy; Fluid dynamics; Cracking; Thermodynamics; Composite material; Physics; Classical mechanics","score_opus":0.0045119695887402035,"score_gpt":0.18301655353720678,"score_spread":0.17850458394846658,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2078896921","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9580769,0.0002025824,0.040669356,0.000033718945,0.000016424354,0.000011159037,0.000018875457,0.00032754833,0.0006433606],"genre_scores_gemma":[0.99452186,0.000031201336,0.0052935486,0.0000043221767,0.0000020852817,0.0000024194053,0.000013879908,0.000010799018,0.00011981929],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99965644,0.00007631779,0.00001977577,0.00007495874,0.00012834677,0.000044108896],"domain_scores_gemma":[0.9995245,0.00013593581,0.00008239162,0.00006716981,0.00015475634,0.000035361016],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005824782,0.0003002566,0.00037828993,0.00028643568,0.00023067251,0.00064643886,0.00037687458,0.0002943885,0.0002663458],"category_scores_gemma":[0.0012254915,0.00019649904,0.00018268563,0.00027620583,0.0003670783,0.00038486236,0.0002469902,0.00028407451,0.00008896055],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00064477045,0.000085976935,0.001972164,0.0000686046,0.000011534762,0.00011270522,0.00009137345,0.045760352,0.92045426,0.0008857101,0.00010207813,0.029810559],"study_design_scores_gemma":[0.000059983926,0.00045930193,0.0030699105,0.0000055883415,0.000017606724,0.000064189764,0.000034232748,0.23823275,0.757369,0.00016107399,0.0005046726,0.000021783824],"about_ca_topic_score_codex":0.0015451491,"about_ca_topic_score_gemma":0.0008616466,"teacher_disagreement_score":0.0015451491,"about_ca_system_score_codex":0.00054737466,"about_ca_system_score_gemma":0.00032192786,"threshold_uncertainty_score":0.003971517},"labels":[],"label_agreement":null},{"id":"W2080457216","doi":"10.1002/ceat.200407063","title":"An Analysis of the Reaction Rate for Mercury Vapor and Chlorine","year":2005,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Mercury impact and mitigation studies","field":"Environmental Science","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Natural Resources Canada","funders":"","keywords":"Mercury (programming language); Chlorine; Chemistry; Environmental chemistry; Organic chemistry; Computer science","score_opus":0.006617896642526282,"score_gpt":0.22955949258101527,"score_spread":0.22294159593848897,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2080457216","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96406245,0.0034991226,0.02513428,0.000120736935,0.000055025826,0.00007215027,0.0018598619,0.00037463408,0.0048217718],"genre_scores_gemma":[0.99070823,0.001133222,0.0032910388,0.000021538797,0.000010127884,0.00003577296,0.001416161,0.000047628757,0.003336279],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99968946,0.000050176917,0.000014987625,0.00008372622,0.0001017104,0.000059998492],"domain_scores_gemma":[0.9991517,0.00046763528,0.00009472776,0.000048420472,0.0002075394,0.000030009696],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005749322,0.0003966183,0.00031714697,0.00091071095,0.00012102401,0.00022439325,0.00046992744,0.0005637769,0.0029945523],"category_scores_gemma":[0.0013734486,0.0002001932,0.00058887363,0.00046177837,0.00014862037,0.000323971,0.00012818653,0.00050002837,0.0012544888],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0009029572,0.000086154985,0.014792019,0.00029034025,0.00013462,0.00016341175,0.00010415472,0.0060835183,0.9520224,0.00096345786,0.00046584627,0.023991184],"study_design_scores_gemma":[0.00002019068,0.0006471282,0.027847229,0.000014543717,0.00009951706,0.00032368864,0.000051524647,0.038763713,0.92759067,0.00021026615,0.0043774024,0.000054066055],"about_ca_topic_score_codex":0.0042428216,"about_ca_topic_score_gemma":0.0018751535,"teacher_disagreement_score":0.0042428216,"about_ca_system_score_codex":0.0004292952,"about_ca_system_score_gemma":0.0002547685,"threshold_uncertainty_score":0.010017812},"labels":[],"label_agreement":null},{"id":"W2087374094","doi":"10.1002/ceat.200900376","title":"Solid‐state Materials and Methods for Hydrogen Storage: A Critical Review","year":2010,"lang":"en","type":"review","venue":"Chemical Engineering & Technology","topic":"Hydrogen Storage and Materials","field":"Materials Science","cited_by":425,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Hydrogen storage; Hydrogen; Desorption; Liquefaction; Materials science; Cryo-adsorption; Energy storage; Process engineering; Physisorption; Chemical engineering; Adsorption; Nanotechnology; Chemistry; Organic chemistry; Thermodynamics; Engineering","score_opus":0.025250397824435448,"score_gpt":0.38237483586823195,"score_spread":0.3571244380437965,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2087374094","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00016323975,0.9982151,0.00025020033,0.00024142281,0.0003514135,0.000008008159,0.000026058993,0.00000911539,0.0007356267],"genre_scores_gemma":[0.000872399,0.9978397,0.00032192227,0.00024365708,0.0002254025,0.0000130597655,0.000044116834,0.0000032252549,0.00043649203],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9995271,0.00006573275,0.000068839516,0.00007157699,0.00022206985,0.000044638047],"domain_scores_gemma":[0.9989089,0.00059147074,0.00012033406,0.000035310397,0.0002954911,0.00004850043],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012106905,0.0011709355,0.0013991111,0.002721872,0.0004491174,0.0011839551,0.0010530716,0.0014350674,0.00575586],"category_scores_gemma":[0.00146897,0.00060951844,0.0008925501,0.0033434203,0.00059526233,0.0022668499,0.0007568146,0.0020031235,0.0030558666],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008831413,0.00017872862,0.00027285653,0.061764725,0.00012734396,0.00035024915,0.00013381087,0.0009183107,0.0062068054,0.009869127,0.07206598,0.8480236],"study_design_scores_gemma":[0.000008773052,0.00012754013,0.0003383797,0.00355382,0.00008277963,0.00064312166,0.000046893092,0.00014337317,0.0015118478,0.0017368118,0.9917807,0.000025941912],"about_ca_topic_score_codex":0.0010070138,"about_ca_topic_score_gemma":0.0011353635,"teacher_disagreement_score":0.00575586,"about_ca_system_score_codex":0.0006187332,"about_ca_system_score_gemma":0.0015476015,"threshold_uncertainty_score":0.01925528},"labels":[],"label_agreement":null},{"id":"W2090585158","doi":"10.1002/ceat.201400503","title":"Techno‐Economic Comparison of a 7‐MW<sub>th</sub> Biomass Chemical Looping Gasification Unit with Conventional Systems","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Chemical Looping and Thermochemical Processes","field":"Engineering","cited_by":34,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Chemical looping combustion; Fluidized bed; Syngas; Pressure swing adsorption; Wood gas generator; Waste management; Oxygen; Integrated gasification combined cycle; Air separation; Biomass (ecology); Process engineering; Chemistry; Chemical engineering; Environmental science; Adsorption; Hydrogen; Engineering; Coal","score_opus":0.015863210924176856,"score_gpt":0.21850654939221334,"score_spread":0.20264333846803648,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2090585158","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99320364,0.00019949641,0.003124236,0.000036090096,0.000022107242,0.000065661574,0.0001439452,0.00008777704,0.003116986],"genre_scores_gemma":[0.9977197,0.000051699488,0.0016032428,0.0000035454768,0.0000024891954,0.0000192997,0.00011683338,0.0000050946155,0.00047805617],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9996673,0.00006290383,0.000014713344,0.000053617638,0.00014211089,0.000059335394],"domain_scores_gemma":[0.9996939,0.00010823687,0.000026048292,0.00003688341,0.00008531821,0.00004955521],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00038372338,0.00040412863,0.00028310844,0.00076846976,0.00035858652,0.0005475654,0.0008159734,0.00047226727,0.0032452724],"category_scores_gemma":[0.0006458329,0.00016107345,0.00035730415,0.0007875173,0.00028121032,0.00077271415,0.000345243,0.0003396766,0.00034899812],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.009406796,0.002125488,0.03385857,0.00090092723,0.00018319285,0.00088601996,0.00011840076,0.38343218,0.3370634,0.0046445625,0.0018279541,0.22555257],"study_design_scores_gemma":[0.0007325371,0.012834524,0.062210027,0.00003516535,0.00027686913,0.0003650691,0.00033059297,0.51619285,0.39775887,0.0009510205,0.008211173,0.000101317695],"about_ca_topic_score_codex":0.0039318968,"about_ca_topic_score_gemma":0.0034968692,"teacher_disagreement_score":0.0039318968,"about_ca_system_score_codex":0.001770416,"about_ca_system_score_gemma":0.0005997245,"threshold_uncertainty_score":0.012845397},"labels":[],"label_agreement":null},{"id":"W2091765201","doi":"10.1002/ceat.200800362","title":"Measuring Mixing Time in the Agitation of Non‐Newtonian Fluids through Electrical Resistance Tomography","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Electrical and Bioimpedance Tomography","field":"Engineering","cited_by":61,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University","funders":"","keywords":"Impeller; Shear thinning; Mixing (physics); Electrical resistance and conductance; Non-Newtonian fluid; Materials science; Mechanics; TRACER; Rheology; Newtonian fluid; Reynolds number; Tomography; Xanthan gum; Mechanical engineering; Composite material; Turbulence; Optics; Engineering; Physics","score_opus":0.006768977577147157,"score_gpt":0.17709866546123199,"score_spread":0.17032968788408484,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2091765201","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.943986,0.000373187,0.05470802,0.000063470565,0.000015022507,0.0000367289,0.000041299827,0.0001625961,0.00061359146],"genre_scores_gemma":[0.95946956,0.00015793093,0.039454095,0.000017123803,0.000005864668,0.0000247344,0.000033579483,0.000026201182,0.0008109382],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99979335,0.000057719353,0.000011076906,0.000045317014,0.00007133713,0.000021133177],"domain_scores_gemma":[0.99913615,0.00046691412,0.00020425026,0.000042827225,0.000105112755,0.00004469367],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006424914,0.00026770783,0.0002156743,0.0003276049,0.00016455895,0.00030368974,0.00021994856,0.0003136359,0.00053942075],"category_scores_gemma":[0.0017737562,0.00018470177,0.00010587921,0.00022862131,0.00038278077,0.0005605894,0.00019346277,0.00042290764,0.00011618139],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00015487945,0.000015512562,0.00089333963,0.000018982551,0.0000031193017,0.000049116086,0.000045567445,0.00045049327,0.99419373,0.00011235485,0.000025336138,0.0040375567],"study_design_scores_gemma":[0.000011030097,0.00024347044,0.0056517147,0.0000025695574,0.000010209075,0.00013696533,0.000033634202,0.018159175,0.9752357,0.000050897455,0.0004499451,0.000014743539],"about_ca_topic_score_codex":0.00041959272,"about_ca_topic_score_gemma":0.00036611073,"teacher_disagreement_score":0.0006424914,"about_ca_system_score_codex":0.00023334824,"about_ca_system_score_gemma":0.00019897336,"threshold_uncertainty_score":0.003397882},"labels":[],"label_agreement":null},{"id":"W2097685028","doi":"10.1002/ceat.201400452","title":"Two‐Parameter Continuation and Bifurcation Strategies for Oscillatory Behavior Elimination from a <i>Zymomonas mobilis</i> Fermentation System","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Nonlinear Dynamics and Pattern Formation","field":"Computer Science","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Zymomonas mobilis; Bifurcation; Dilution; Control theory (sociology); Industrial fermentation; Steady state (chemistry); Hopf bifurcation; Fermentation; Ethanol fuel; Chemistry; Bioreactor; Biological system; Mechanics; Mathematics; Thermodynamics; Physics; Computer science; Biochemistry; Nonlinear system; Biology; Control (management)","score_opus":0.012221756975842954,"score_gpt":0.23437817142695314,"score_spread":0.22215641445111017,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2097685028","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.17343533,0.00014938005,0.8229349,0.0000894932,0.000015798794,0.00009338315,0.00002279935,0.00019575412,0.0030631437],"genre_scores_gemma":[0.92262006,0.00011029537,0.075502075,0.000013216947,0.000003842743,0.00017789203,0.00002512356,0.000017486745,0.0015301617],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99992085,0.000033750493,0.0000060142747,0.000011735939,0.000017792776,0.000009888193],"domain_scores_gemma":[0.99984825,0.00007705858,0.00002999195,0.000011934104,0.000025000398,0.000007682256],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00040320394,0.00063480664,0.0004512259,0.00039506718,0.00032926977,0.00043290685,0.00032283794,0.0003776597,0.0008866594],"category_scores_gemma":[0.000520423,0.00021020774,0.0005833621,0.00012959412,0.0002919899,0.00028666842,0.0004752523,0.00038238868,0.0001203463],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019834748,0.000103268896,0.0016556777,0.00025318994,0.00007277511,0.000377205,0.00056974293,0.7591319,0.1354597,0.027869124,0.00033533422,0.073973656],"study_design_scores_gemma":[0.000009323986,0.00004579607,0.00010673994,0.0000065789645,0.000008782914,0.00001649308,0.000016202312,0.9930906,0.0045963894,0.0017781425,0.0003182117,0.0000067066376],"about_ca_topic_score_codex":0.0018380738,"about_ca_topic_score_gemma":0.00094556995,"teacher_disagreement_score":0.0018380738,"about_ca_system_score_codex":0.00040242076,"about_ca_system_score_gemma":0.00042304513,"threshold_uncertainty_score":0.003654778},"labels":[],"label_agreement":null},{"id":"W2098240901","doi":"10.1002/ceat.201100236","title":"Fabrication of Homogenous Polymer‐Zeolite Nanocomposites as Mixed‐Matrix Membranes for Gas Separation","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Membrane Separation and Gas Transport","field":"Engineering","cited_by":40,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Iran Nanotechnology Initiative Council","keywords":"Zeolite; Membrane; Gas separation; Polyimide; Chemical engineering; Polymer; Materials science; Fabrication; Nanocomposite; Selectivity; Semipermeable membrane; Void (composites); Polymer chemistry; Chemistry; Organic chemistry; Composite material; Layer (electronics); Catalysis","score_opus":0.0061250747604129855,"score_gpt":0.23414417320941222,"score_spread":0.22801909844899923,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2098240901","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9799958,0.0008904595,0.017714646,0.000041974792,0.000029900722,0.000058691414,0.00013373303,0.0001663933,0.000968521],"genre_scores_gemma":[0.98488426,0.00049464527,0.0131638935,0.000013528996,0.00000597329,0.000045791578,0.00011312155,0.000021096823,0.0012576219],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99986875,0.000016671993,0.000009442683,0.000029583947,0.000052330917,0.000023278199],"domain_scores_gemma":[0.9998901,0.00002194737,0.000027948237,0.000009229561,0.000026650496,0.000024169705],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002671907,0.00040469068,0.00023143957,0.00023895211,0.00013410636,0.000324524,0.0002557081,0.0003058664,0.000479544],"category_scores_gemma":[0.00018130794,0.0002278127,0.00029448338,0.00011866163,0.00015433747,0.00028938922,0.00021806755,0.0003560903,0.00028862958],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000013962298,0.000005500654,0.00002807856,0.000016474341,0.0000022674146,0.000010249571,0.0000044720387,0.000050730905,0.99948126,0.000024248508,0.0000045000997,0.00035835165],"study_design_scores_gemma":[0.0000040655877,0.00003431591,0.00032749862,0.0000015771717,0.000005597529,0.00001756817,0.000005162487,0.00058202434,0.998705,0.000007281384,0.0003081745,0.0000016224327],"about_ca_topic_score_codex":0.0003595407,"about_ca_topic_score_gemma":0.0010460388,"teacher_disagreement_score":0.000479544,"about_ca_system_score_codex":0.00027000534,"about_ca_system_score_gemma":0.00017235054,"threshold_uncertainty_score":0.0019590855},"labels":[],"label_agreement":null},{"id":"W2099701415","doi":"10.1002/ceat.200800433","title":"Hydrophilicity Enhancement of High‐Density Polyethylene Film by Ozonation","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Electrospun Nanofibers in Biomedical Applications","field":"Materials Science","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Polymerization; High-density polyethylene; Contact angle; Ozone; Polyethylene; Aqueous solution; Distilled water; Chemistry; Chemical engineering; Monomer; Polymer chemistry; Peroxide; Fourier transform infrared spectroscopy; Materials science; Polymer; Organic chemistry; Chromatography","score_opus":0.0022285578085163614,"score_gpt":0.19393722015659098,"score_spread":0.19170866234807463,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2099701415","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9973953,0.00044108584,0.0014847232,0.000022243412,0.000009801098,0.000012325344,0.000034020464,0.000015710459,0.0005848143],"genre_scores_gemma":[0.99740297,0.0004692208,0.0011992067,0.000017608345,0.000005537267,0.000008856473,0.000058417834,0.000005732277,0.0008324445],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999577,0.0000062046834,0.000002226232,0.000008357535,0.00001413026,0.00001131029],"domain_scores_gemma":[0.9999287,0.00002088852,0.000020164744,0.0000026803532,0.000014993858,0.000012558951],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0000974109,0.00037447884,0.000113428585,0.00011777356,0.00006772626,0.0001251413,0.00007319339,0.0001402689,0.0010406664],"category_scores_gemma":[0.00012633957,0.00009882518,0.0001164829,0.000074366006,0.00012686217,0.00022232646,0.00012998385,0.00020821833,0.0001214931],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000018843704,0.000003339467,0.000027290282,0.000014215255,9.852353e-7,0.0000135491255,0.00000459888,0.000016564994,0.99959,0.000009990308,0.000004296753,0.00029634184],"study_design_scores_gemma":[0.000007866686,0.00014372844,0.0010527463,0.0000021167932,0.0000053723297,0.000042421747,0.000009259583,0.000257133,0.9980925,0.000008059241,0.00037686885,0.0000019711688],"about_ca_topic_score_codex":0.00021581605,"about_ca_topic_score_gemma":0.000295866,"teacher_disagreement_score":0.0010406664,"about_ca_system_score_codex":0.00008479018,"about_ca_system_score_gemma":0.000072032955,"threshold_uncertainty_score":0.003481388},"labels":[],"label_agreement":null},{"id":"W2100969127","doi":"10.1002/ceat.200900367","title":"Optimization of Parameters for Synthesis of MFI Nanoparticles by Taguchi Robust Design","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Zeolite Catalysis and Synthesis","field":"Chemistry","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Sharif University of Technology","keywords":"Taguchi methods; Crystallization; Particle size; Materials science; Orthogonal array; Particle-size distribution; Chemical engineering; Design of experiments; Nanocrystal; Nanoparticle; Zeolite; Particle (ecology); Aluminium; Nanotechnology; Composite material; Mathematics; Chemistry; Organic chemistry","score_opus":0.008445574078564892,"score_gpt":0.1854307789119835,"score_spread":0.17698520483341862,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2100969127","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.079643026,0.0006797575,0.9156613,0.0000556844,0.00004605511,0.0010983129,0.00020810707,0.0007174927,0.0018902251],"genre_scores_gemma":[0.3795143,0.0003616413,0.6162385,0.000040155726,0.000010055594,0.0029428767,0.00022219878,0.00009216807,0.0005781346],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99839836,0.0005808471,0.0001470603,0.000222314,0.00048317495,0.00016817477],"domain_scores_gemma":[0.99889463,0.0006415868,0.00017523103,0.000046960868,0.00021595697,0.000025517042],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0036463179,0.0015790513,0.001382831,0.0007417794,0.0003486355,0.0008988304,0.0010654711,0.00082362077,0.0013919233],"category_scores_gemma":[0.0037654673,0.0006926205,0.0007844656,0.0006272263,0.00035808433,0.0003483166,0.0003633979,0.0008292261,0.0005762277],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0009615505,0.0008625944,0.0016603417,0.002203424,0.00019609195,0.00013985274,0.00029983587,0.16948535,0.65159756,0.002971766,0.000766279,0.16885537],"study_design_scores_gemma":[0.000333137,0.0026279234,0.003929124,0.00008402011,0.00026627613,0.0000990968,0.0000832837,0.44139245,0.54307723,0.0009963434,0.0069681066,0.00014293543],"about_ca_topic_score_codex":0.0010623144,"about_ca_topic_score_gemma":0.0018563264,"teacher_disagreement_score":0.0036463179,"about_ca_system_score_codex":0.0006637182,"about_ca_system_score_gemma":0.001038926,"threshold_uncertainty_score":0.019283772},"labels":[],"label_agreement":null},{"id":"W2100994295","doi":"10.1002/ceat.201100668","title":"A Modified Approach for Generating Column Grand Composite Curves","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Process Optimization and Integration","field":"Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China; Centre in Green Chemistry and Catalysis","keywords":"Reboiler; Stage (stratigraphy); Column (typography); Condenser (optics); Stripping (fiber); Section (typography); Fractionating column; Mathematics; Process engineering; Chemistry; Computer science; Engineering; Mechanical engineering; Heat exchanger; Chromatography; Physics; Geology; Geometry; Distillation","score_opus":0.009627797155773216,"score_gpt":0.20186029490150964,"score_spread":0.19223249774573642,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2100994295","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00814943,0.000032704284,0.9882615,0.000027298416,0.000025390962,0.00007283362,0.000120082,0.0011562036,0.0021545528],"genre_scores_gemma":[0.18104255,0.00006709611,0.81463194,0.000034073128,0.000019777908,0.00023095733,0.00049084047,0.00056860625,0.0029142206],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9995684,0.000080572114,0.000014590412,0.0000704909,0.00023536327,0.00003060854],"domain_scores_gemma":[0.99934036,0.00020718879,0.000033867826,0.00009978953,0.00029985394,0.0000189202],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006533338,0.00081513834,0.00045595068,0.0009909832,0.00048366,0.0006783052,0.00081961375,0.00051865657,0.004875142],"category_scores_gemma":[0.0016828977,0.00034602807,0.0007508035,0.0011506239,0.0002514283,0.00059127994,0.000591597,0.0007517604,0.0011859818],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019587018,0.00007309355,0.0011652919,0.0002437165,0.000053322176,0.00011517459,0.00014134949,0.55634606,0.047586028,0.021910133,0.0031353282,0.3690346],"study_design_scores_gemma":[0.000008688061,0.000057172423,0.00031448793,0.0000051335587,0.000010533208,0.000031382955,0.00001059931,0.9749996,0.016398016,0.002122656,0.006018409,0.000023250766],"about_ca_topic_score_codex":0.0037780667,"about_ca_topic_score_gemma":0.0034594298,"teacher_disagreement_score":0.004875142,"about_ca_system_score_codex":0.00048811204,"about_ca_system_score_gemma":0.0010748242,"threshold_uncertainty_score":0.016309023},"labels":[],"label_agreement":null},{"id":"W2105775946","doi":"10.1002/ceat.201000251","title":"Simulation of Polymerization Kinetics and Molecular Weight Development in the Microwave‐Activated Emulsion Polymerization of Styrene using EMULPOLY<sup>®</sup>","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Microwave-Assisted Synthesis and Applications","field":"Chemistry","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Dirección General de Asuntos del Personal Académico, Universidad Nacional Autónoma de México; Consejo Nacional de Ciencia y Tecnología","keywords":"Emulsion polymerization; Styrene; Microwave; Kinetics; Polymerization; Monomer; Emulsion; Polymer chemistry; Materials science; Reaction rate constant; Chemistry; Chemical engineering; Copolymer; Polymer; Organic chemistry; Physics","score_opus":0.0058464698879047,"score_gpt":0.20840679869791282,"score_spread":0.20256032881000813,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2105775946","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97861916,0.00007874215,0.014376327,0.00008852408,0.000014445441,0.000048086124,0.00039862268,0.00017786141,0.0061981943],"genre_scores_gemma":[0.99251163,0.00008212702,0.00553603,0.000020778272,0.000002461327,0.000076614044,0.00023793994,0.00002674607,0.0015056786],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99992454,0.000023886802,0.0000027294457,0.000010082094,0.000020948242,0.000017814506],"domain_scores_gemma":[0.9995191,0.00034435518,0.0000385927,0.000016038046,0.000056790544,0.00002507331],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00030429923,0.00035159328,0.00037088373,0.00025463884,0.00030415104,0.00040387138,0.0004924907,0.00063678087,0.0016283488],"category_scores_gemma":[0.00096998847,0.00026584396,0.0003577629,0.00036030397,0.0003204244,0.00033678356,0.00018469438,0.00038032935,0.00016218322],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00008415744,0.00003916929,0.00084085553,0.000018921242,0.0000085381,0.000053595642,0.000025014491,0.9937756,0.0030198398,0.00069557765,0.00010559432,0.0013329749],"study_design_scores_gemma":[0.000018208146,0.000029939587,0.00022425225,0.000001834246,0.0000035686705,0.0000045418333,0.0000068789964,0.9973224,0.0021505796,0.00008553986,0.00014939431,0.0000027749456],"about_ca_topic_score_codex":0.012673235,"about_ca_topic_score_gemma":0.0064776028,"teacher_disagreement_score":0.012673235,"about_ca_system_score_codex":0.0009771427,"about_ca_system_score_gemma":0.0007626042,"threshold_uncertainty_score":0.025198936},"labels":[],"label_agreement":null},{"id":"W2106516709","doi":"10.1002/ceat.201000290","title":"Semi‐Continuous Emulsion Copolymerization of Styrene‐Butyl Acrylate with Methacrylic Acid: Box‐Behnken Design of Experiments","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Polymer Synthesis and Characterization","field":"Chemistry","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Box–Behnken design; Methacrylic acid; Styrene; Copolymer; Materials science; Particle size; Butyl acrylate; Polymer; Polymer chemistry; Polycarbonate; Acrylate; Chemical engineering; Emulsion; Response surface methodology; Chemistry; Chromatography; Composite material","score_opus":0.005326902360982743,"score_gpt":0.20858067010104556,"score_spread":0.20325376774006282,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2106516709","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9180429,0.0003957038,0.07568952,0.000031257594,0.00018988628,0.0045905747,0.00033081227,0.00018196202,0.0005474666],"genre_scores_gemma":[0.8170749,0.00061421376,0.15940575,0.0000836917,0.000065659,0.019071858,0.0004083629,0.00010869211,0.0031668362],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9971577,0.0007835136,0.00029187757,0.0005979845,0.00073889585,0.00043014332],"domain_scores_gemma":[0.99740964,0.0011144403,0.00067626074,0.00020560116,0.00038765726,0.00020646218],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.003921039,0.00150322,0.0024029457,0.0007080417,0.00049544714,0.0010524773,0.0012041786,0.0010489979,0.0026745712],"category_scores_gemma":[0.002142616,0.00067654945,0.0011995371,0.00046014247,0.00084662094,0.00044239743,0.0004181283,0.0010482665,0.0003904769],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.03303101,0.0057282476,0.0012342462,0.0012112842,0.0003108728,0.00007295903,0.00020218694,0.011729163,0.9243686,0.0011092437,0.00012660453,0.020875597],"study_design_scores_gemma":[0.0043831994,0.06819752,0.0062087392,0.00004002423,0.0005435553,0.000046086418,0.000059198934,0.053176902,0.8630548,0.0005664249,0.003599372,0.00012426788],"about_ca_topic_score_codex":0.0006450188,"about_ca_topic_score_gemma":0.00062191364,"teacher_disagreement_score":0.003921039,"about_ca_system_score_codex":0.0008050926,"about_ca_system_score_gemma":0.0012279085,"threshold_uncertainty_score":0.020736635},"labels":[],"label_agreement":null},{"id":"W2106962368","doi":"10.1002/ceat.201500105","title":"Kinetics and Reactor Modeling of the Steam Reforming of Methanol over a Mn‐Promoted Cu/Al Catalyst","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Methanol; Catalysis; Chemistry; Steam reforming; Mass transfer; Kinetics; Chemical engineering; Packed bed; Thermodynamics; Chemical kinetics; Adsorption; Physical chemistry; Chromatography; Organic chemistry; Hydrogen production","score_opus":0.013355551639594579,"score_gpt":0.22702917281542914,"score_spread":0.21367362117583455,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2106962368","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9845503,0.00023613557,0.012053186,0.000051789062,0.000015363852,0.000033973003,0.00020584662,0.00013631358,0.002717068],"genre_scores_gemma":[0.9974093,0.000104216924,0.0014326603,0.0000043707482,0.0000018123134,0.000023330884,0.00006608245,0.00000936866,0.0009489991],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9999194,0.000015443535,0.000005676263,0.000017416769,0.000022263963,0.000019668501],"domain_scores_gemma":[0.99982494,0.00009368643,0.000023900371,0.000011999939,0.00003475594,0.000010608477],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026422145,0.00040290426,0.00052971445,0.0002761558,0.00034818528,0.0006350048,0.0007454111,0.0006769361,0.0009985651],"category_scores_gemma":[0.00041235407,0.00033409218,0.0005237165,0.00022140858,0.00030980192,0.00035305927,0.00015583221,0.00038180657,0.00027298855],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00043479248,0.0001228867,0.0021093837,0.00017008638,0.00004499939,0.0002048691,0.00006730304,0.88930476,0.103138745,0.0011924715,0.000107375,0.003102288],"study_design_scores_gemma":[0.000015800537,0.00005578267,0.00043023433,0.0000019667452,0.000009294763,0.000008141258,0.000009095456,0.9809156,0.01838341,0.00004457586,0.00012062957,0.000005422161],"about_ca_topic_score_codex":0.025675287,"about_ca_topic_score_gemma":0.010543323,"teacher_disagreement_score":0.025675287,"about_ca_system_score_codex":0.0014055449,"about_ca_system_score_gemma":0.0007067254,"threshold_uncertainty_score":0.051051676},"labels":[],"label_agreement":null},{"id":"W2114916365","doi":"10.1002/ceat.201400225","title":"Using Coal Fly Ash and Wastewater for Microwave Synthesis of LTA Zeolite","year":2014,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Chemical Synthesis and Characterization","field":"Environmental Science","cited_by":69,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Fly ash; Zeolite; Sodium aluminate; Thermogravimetric analysis; Chemical engineering; Crystallinity; Materials science; Wastewater; Sodium hydroxide; Effluent; Waste management; Chemistry; Metallurgy; Catalysis","score_opus":0.0059562319357061725,"score_gpt":0.18322590528336885,"score_spread":0.17726967334766267,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2114916365","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9925477,0.0006251623,0.0053594373,0.000045042387,0.00002041418,0.00004229513,0.00020765173,0.00005502622,0.0010971491],"genre_scores_gemma":[0.99603075,0.00026691714,0.0029018421,0.000009973931,0.000004056565,0.000015509911,0.00015515792,0.000014020606,0.00060177094],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99990153,0.000016242659,0.000011875904,0.000021446036,0.000027298762,0.000021548603],"domain_scores_gemma":[0.999949,0.000011826917,0.00001062559,0.0000062829663,0.000011535002,0.0000107451215],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017205089,0.00033614188,0.000343381,0.0002808079,0.00015587338,0.0002472475,0.00018081418,0.00024996453,0.00053314783],"category_scores_gemma":[0.00017698984,0.00012436237,0.00029258485,0.00027064348,0.00011758975,0.0002158541,0.00019413113,0.00027431105,0.00028417094],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000032719327,0.00001618231,0.00012878889,0.000047220503,0.0000044746653,0.000025048048,0.00000999527,0.00011060448,0.9981693,0.000034380064,0.000006668999,0.0014146453],"study_design_scores_gemma":[0.000011387713,0.000095139156,0.00093233224,0.00000362942,0.00000855357,0.000040768682,0.000014995644,0.0007489714,0.99751127,0.000025514944,0.00060385175,0.0000035541495],"about_ca_topic_score_codex":0.00085087446,"about_ca_topic_score_gemma":0.001698183,"teacher_disagreement_score":0.00085087446,"about_ca_system_score_codex":0.00018387203,"about_ca_system_score_gemma":0.00019712881,"threshold_uncertainty_score":0.0017834902},"labels":[],"label_agreement":null},{"id":"W2115082485","doi":"10.1002/ceat.201400606","title":"Comparison of Overall Gas‐Phase Mass Transfer Coefficient for CO<sub>2</sub> Absorption between Tertiary Amines in a Randomly Packed Column","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Carbon Dioxide Capture Technologies","field":"Engineering","cited_by":41,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Regina","funders":"","keywords":"Mass transfer; Mass transfer coefficient; Amine gas treating; Chemistry; Volumetric flow rate; Inert gas; Absorption (acoustics); Packed bed; Analytical Chemistry (journal); Inert; Raschig ring; Structured packing; Solvent; Chromatography; Materials science; Thermodynamics; Organic chemistry; Composite material","score_opus":0.016580963356878847,"score_gpt":0.25638691344447806,"score_spread":0.23980595008759922,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2115082485","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99506027,0.00045593007,0.003918665,0.000030753818,0.000010106503,0.000012484271,0.00006631956,0.000097156466,0.0003484103],"genre_scores_gemma":[0.9958326,0.0003678087,0.003152892,0.000024852518,0.000005495794,0.000020200849,0.00010715967,0.00001979104,0.0004691744],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997489,0.000063433756,0.000011014233,0.000053064967,0.00006096962,0.00006260266],"domain_scores_gemma":[0.99937135,0.00041293137,0.000058894613,0.000025335332,0.00010028225,0.00003118767],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00048239977,0.00041889588,0.00036198652,0.0003131647,0.00021176136,0.0003521795,0.00050067744,0.0004189512,0.00081430026],"category_scores_gemma":[0.0009063166,0.00023974011,0.00019318683,0.00022395168,0.0003093076,0.00042229707,0.0001533998,0.00037664777,0.00037742325],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00021086118,0.000021969847,0.0002532118,0.00004286937,0.000010057311,0.000015521728,0.000020146636,0.00030311756,0.9978586,0.00002573616,0.00002217792,0.0012156421],"study_design_scores_gemma":[0.000005269062,0.00014340652,0.0011717041,0.0000014118737,0.000010084921,0.000017339446,0.000010233541,0.0027441096,0.99581236,0.000006028302,0.00007398928,0.0000040630935],"about_ca_topic_score_codex":0.0023901102,"about_ca_topic_score_gemma":0.002139457,"teacher_disagreement_score":0.0023901102,"about_ca_system_score_codex":0.00051749736,"about_ca_system_score_gemma":0.00027131574,"threshold_uncertainty_score":0.004752338},"labels":[],"label_agreement":null},{"id":"W2117562397","doi":"10.1002/ceat.200800361","title":"Direct Measurements of Instantaneous Solid Flux in a CFB Riser using a Novel Multifunctional Optical Fiber Probe","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Fluidized bed combustion; Flux (metallurgy); Materials science; Mechanics; Particle (ecology); Particle velocity; Fiber; Flow (mathematics); Transient (computer programming); Fluidized bed; Thermodynamics; Physics; Composite material","score_opus":0.014642597537686257,"score_gpt":0.21670052889092126,"score_spread":0.202057931353235,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2117562397","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9872557,0.00012972786,0.012152412,0.000025242893,0.0000068610393,0.000011323317,0.000045570523,0.00007235538,0.0003008274],"genre_scores_gemma":[0.98864657,0.000074204254,0.010857059,0.000015004882,0.0000048967613,0.00001048531,0.00003105498,0.0000068876902,0.00035382796],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997315,0.000032215466,0.000008022466,0.00007534911,0.00012340113,0.000029564235],"domain_scores_gemma":[0.99974805,0.00007943048,0.000060556864,0.000019187197,0.00007068346,0.000022123895],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003135737,0.00022462638,0.000249128,0.00040111705,0.00023922315,0.00023866545,0.00026982135,0.00030202774,0.00029709897],"category_scores_gemma":[0.0004192459,0.00014479527,0.00009701877,0.00023458876,0.00046930052,0.00035890404,0.00017991611,0.00026333673,0.00006549492],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000104206825,0.00001575414,0.0017709442,0.000017816943,0.0000021816695,0.000024336647,0.00004229485,0.00024505742,0.99324363,0.00008024399,0.000020834332,0.0044327956],"study_design_scores_gemma":[0.000021364458,0.0004207742,0.012712959,0.000005418916,0.000013165537,0.00012561247,0.00006938548,0.015565687,0.9703648,0.00006148051,0.0006208453,0.000018348503],"about_ca_topic_score_codex":0.0018457965,"about_ca_topic_score_gemma":0.0016183802,"teacher_disagreement_score":0.0018457965,"about_ca_system_score_codex":0.00045251704,"about_ca_system_score_gemma":0.00024593298,"threshold_uncertainty_score":0.0036700964},"labels":[],"label_agreement":null},{"id":"W2118230338","doi":"10.1002/ceat.200600048","title":"Newtonian and Non‐Newtonian Low Re Number Flow Through Bead Packings","year":2006,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Rheology and Fluid Dynamics Studies","field":"Chemical Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Deutsche Forschungsgemeinschaft","keywords":"Bead; Newtonian fluid; Non-Newtonian fluid; Porous medium; Materials science; Displacement (psychology); Flow (mathematics); Porosity; Rheology; Tube (container); Mechanics; Composite material; Physics","score_opus":0.0028823029997498543,"score_gpt":0.1898151847505072,"score_spread":0.18693288175075737,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2118230338","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99486035,0.00019739696,0.0044491203,0.000008200633,0.000002368429,0.0000034147072,0.000014996039,0.00002849197,0.0004356443],"genre_scores_gemma":[0.9978656,0.000095244235,0.0016430076,0.0000031554168,0.0000017129056,0.0000020390162,0.000025445917,0.0000036032452,0.00036024055],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99985206,0.000022213791,0.0000062015197,0.000026315254,0.00005602139,0.00003716535],"domain_scores_gemma":[0.9995408,0.00023134756,0.000117733674,0.000023314236,0.00004363685,0.000043221473],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024520952,0.000115574214,0.00016856626,0.0003833044,0.00015669552,0.00038594307,0.00012959918,0.00012714641,0.0003476302],"category_scores_gemma":[0.0008752104,0.00009435782,0.0000747689,0.00016410345,0.00046431992,0.0003654738,0.00014176778,0.00014444045,0.00005512443],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00019285279,0.000034139826,0.0020517348,0.0000592244,0.000007737327,0.0000469996,0.00012199725,0.0066953194,0.9806599,0.0018985935,0.0000630301,0.00816853],"study_design_scores_gemma":[0.000040047988,0.00031287762,0.010905791,0.000012130876,0.000017724777,0.00008758904,0.00006283326,0.09290825,0.893725,0.00084274705,0.0010644079,0.00002066864],"about_ca_topic_score_codex":0.0018950062,"about_ca_topic_score_gemma":0.0012075843,"teacher_disagreement_score":0.0018950062,"about_ca_system_score_codex":0.00035395855,"about_ca_system_score_gemma":0.00017588706,"threshold_uncertainty_score":0.0037679672},"labels":[],"label_agreement":null},{"id":"W2118918593","doi":"10.1002/ceat.201100492","title":"Optimization of the Cementation Process for the Removal of Copper in Process Effluent Discharges","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Recycling and Waste Management Techniques","field":"Environmental Science","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Cementation (geology); Factorial experiment; Copper; Metallurgy; Effluent; Design of experiments; Process (computing); MATLAB; Materials science; Process engineering; Engineering; Mathematics; Waste management; Computer science; Statistics; Cement","score_opus":0.007689978641424208,"score_gpt":0.242110344401283,"score_spread":0.2344203657598588,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2118918593","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9946833,0.00046222907,0.0042012776,0.000029226037,0.0000068509535,0.00003575089,0.00006442056,0.000037681,0.00047912737],"genre_scores_gemma":[0.99565494,0.00043350604,0.0035073948,0.0000065104837,0.0000020577427,0.000018345449,0.000046776742,0.000014470473,0.000315951],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99939525,0.00016243641,0.00007130227,0.00008685652,0.00021570695,0.00006839823],"domain_scores_gemma":[0.9996264,0.00014303044,0.00010829915,0.00002657845,0.00007459117,0.000021103548],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008426388,0.0005643694,0.0007814555,0.00036972057,0.00031044945,0.0007644676,0.00034472105,0.00033613836,0.0005213152],"category_scores_gemma":[0.0012633998,0.0002948115,0.0005571353,0.0005740826,0.00031507923,0.0003216404,0.00030986604,0.00048320217,0.00017392251],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0004985938,0.00021191407,0.0008760613,0.00025539787,0.000031493528,0.00006125942,0.000051314077,0.011281253,0.9776775,0.000104836865,0.00004888967,0.0089015355],"study_design_scores_gemma":[0.0000264226,0.0008916472,0.0033862095,0.000009172042,0.000043857013,0.000029281535,0.000027396192,0.012708475,0.9822958,0.000040829786,0.00052627636,0.000014518432],"about_ca_topic_score_codex":0.0020053259,"about_ca_topic_score_gemma":0.0035118253,"teacher_disagreement_score":0.0020053259,"about_ca_system_score_codex":0.00065253815,"about_ca_system_score_gemma":0.0005509174,"threshold_uncertainty_score":0.004734516},"labels":[],"label_agreement":null},{"id":"W2119165776","doi":"10.1002/ceat.201000234","title":"Free‐Radical Acrylic Polymerization Kinetics at Elevated Temperatures","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Polymer Synthesis and Characterization","field":"Chemistry","cited_by":41,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Queen's University","funders":"","keywords":"Copolymer; Polymer chemistry; Monomer; Polymerization; Chemistry; Radical; Radical polymerization; Kinetics; Acrylate; Styrene; Methacrylate; Polymer; Butyl acrylate; Chain transfer; Kinetic chain length; Photochemistry; Organic chemistry","score_opus":0.0027144897239155443,"score_gpt":0.1854135622265654,"score_spread":0.18269907250264986,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2119165776","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.867874,0.07158122,0.029888313,0.00021836809,0.00027815698,0.000142303,0.00094529445,0.00063938834,0.028432945],"genre_scores_gemma":[0.94831204,0.02833681,0.0072029643,0.00007251127,0.00007143095,0.00006963147,0.00048627224,0.000119628654,0.015328724],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9996766,0.000033914814,0.000017025473,0.00007470049,0.00013827159,0.000059499707],"domain_scores_gemma":[0.9997651,0.00008145879,0.000048693895,0.000013768212,0.00007171163,0.000019187231],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035474126,0.0004613382,0.00036600867,0.0002704663,0.00015354819,0.00046960145,0.00026593474,0.00028727038,0.00302286],"category_scores_gemma":[0.00040499383,0.00023065733,0.00035565978,0.00028008863,0.00016247452,0.00061379094,0.00014170521,0.0007487715,0.0019717943],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00014767663,0.000023840526,0.00024547614,0.0005580402,0.000017656896,0.000087084176,0.000074824246,0.0015907211,0.98474574,0.0008290677,0.000267064,0.011412925],"study_design_scores_gemma":[0.0000057638595,0.00019685985,0.0011983085,0.000041887222,0.000023300592,0.00012185292,0.000011793862,0.0016231129,0.9881561,0.0001927189,0.008415461,0.00001278384],"about_ca_topic_score_codex":0.0005606386,"about_ca_topic_score_gemma":0.0004265505,"teacher_disagreement_score":0.00302286,"about_ca_system_score_codex":0.0003450742,"about_ca_system_score_gemma":0.0002760547,"threshold_uncertainty_score":0.010112464},"labels":[],"label_agreement":null},{"id":"W2120215863","doi":"10.1002/ceat.200800590","title":"Changes in Limestone Sorbent Morphology during CaO‐CaCO<sub>3</sub> Looping at Pilot Scale","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Chemical Looping and Thermochemical Processes","field":"Engineering","cited_by":30,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa; Natural Resources Canada","funders":"","keywords":"Sorbent; Calcination; Thermogravimetric analysis; Chemical engineering; Porosimetry; Fluidized bed; Materials science; Calcium looping; Mineralogy; Flue gas; Chemistry; Porosity; Adsorption; Composite material; Porous medium; Organic chemistry","score_opus":0.004631415820253988,"score_gpt":0.1798351209694394,"score_spread":0.17520370514918543,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2120215863","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9992367,0.000024859137,0.00046803337,0.000006372049,0.000002140256,0.000018184575,0.00004798918,0.000027673877,0.00016812493],"genre_scores_gemma":[0.9987143,0.000043331365,0.00069594465,0.000011479403,0.0000015214432,0.0000125203205,0.000080166625,0.000013807098,0.0004268666],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997948,0.000028374123,0.000012063292,0.000035871602,0.00007985651,0.000049050126],"domain_scores_gemma":[0.9996972,0.00011678082,0.000052743268,0.000027113112,0.00006861264,0.00003751693],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002633317,0.00038596094,0.0003894505,0.00021816092,0.00025090505,0.00035514496,0.0003143837,0.0003470206,0.0009454425],"category_scores_gemma":[0.0005589371,0.00021790524,0.00029139812,0.00015322145,0.00036536128,0.00034392308,0.00023890269,0.00028450735,0.00022547545],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023492213,0.000045350775,0.00046268242,0.000023742454,0.000004635476,0.000052377734,0.000032322452,0.00019557212,0.9981079,0.0000066906555,0.000009501924,0.0008243802],"study_design_scores_gemma":[0.000012334812,0.00047779054,0.0049408562,0.0000016177762,0.000009826969,0.000044845434,0.000028210226,0.0007695302,0.99358374,0.000007665289,0.00011856624,0.0000050363237],"about_ca_topic_score_codex":0.0017398454,"about_ca_topic_score_gemma":0.0019667821,"teacher_disagreement_score":0.0017398454,"about_ca_system_score_codex":0.00027996852,"about_ca_system_score_gemma":0.00015663262,"threshold_uncertainty_score":0.0034594536},"labels":[],"label_agreement":null},{"id":"W2121288298","doi":"10.1002/ceat.200700006","title":"Using CFD and Ultrasonic velocimetry to Study the Mixing of Pseudoplastic Fluids with a Helical Ribbon Impeller","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":58,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Particle image velocimetry; Laminar flow; Mechanics; Computational fluid dynamics; Agitator; Materials science; Shear thinning; Mixing (physics); Ribbon; Velocimetry; Axial compressor; Mechanical engineering; Turbulence; Rheology; Engineering; Physics; Composite material; Gas compressor","score_opus":0.006030042218766946,"score_gpt":0.21069717717798064,"score_spread":0.2046671349592137,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2121288298","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.836013,0.000278344,0.16030164,0.0001362312,0.000055228204,0.000114706796,0.000104616185,0.00057541835,0.0024207667],"genre_scores_gemma":[0.9520511,0.00010040626,0.047031116,0.0000117941645,0.000008750431,0.00004813325,0.000051834282,0.00001943374,0.0006774211],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99982315,0.00003796732,0.000014140666,0.000026217778,0.000070575465,0.00002794173],"domain_scores_gemma":[0.99951816,0.00030044004,0.00006921524,0.000034143435,0.000055536082,0.000022567347],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00049760274,0.00039367107,0.00048849813,0.00060187146,0.0003295037,0.00049184985,0.000364645,0.0006908038,0.0006833988],"category_scores_gemma":[0.001030921,0.00028739774,0.00036509926,0.00040170233,0.0004893356,0.00043648205,0.00030518568,0.00035276686,0.00017087393],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00054513256,0.00019180625,0.0067091594,0.00012234553,0.000023160212,0.00046347824,0.00017456664,0.58871126,0.3688725,0.0037818828,0.00022752772,0.030177137],"study_design_scores_gemma":[0.000027032667,0.00014908762,0.0014630734,0.0000038059998,0.0000065001145,0.000050893177,0.000015786145,0.9321048,0.065525934,0.00017953085,0.00045889206,0.000014614105],"about_ca_topic_score_codex":0.0025314484,"about_ca_topic_score_gemma":0.001065021,"teacher_disagreement_score":0.0025314484,"about_ca_system_score_codex":0.00052798295,"about_ca_system_score_gemma":0.00069090124,"threshold_uncertainty_score":0.005033493},"labels":[],"label_agreement":null},{"id":"W2122099104","doi":"10.1002/ceat.200900543","title":"Controlled Synthesis of a Thin LTL Zeolitic Membrane Using Nano‐Sized Seeds: Characterization and Permeation Performance","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Zeolite Catalysis and Synthesis","field":"Chemistry","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Membrane; Zeolite; Permeation; Materials science; Chemical engineering; Aluminosilicate; Hydrothermal synthesis; Nanoparticle; Characterization (materials science); Selectivity; Porosity; Hydrothermal circulation; Nanotechnology; Chemistry; Organic chemistry; Composite material; Catalysis","score_opus":0.003973861661704047,"score_gpt":0.18047424902024853,"score_spread":0.17650038735854448,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2122099104","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9934772,0.000388682,0.005209679,0.000046240642,0.000009367044,0.000023756902,0.00016865769,0.00010826836,0.0005681183],"genre_scores_gemma":[0.99523574,0.00016753528,0.003947569,0.000011002808,0.0000024587534,0.000016647733,0.00010505579,0.000027125734,0.00048683086],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999256,0.000009515597,0.000008221785,0.000019593681,0.00002197894,0.000015166763],"domain_scores_gemma":[0.9998191,0.00004063295,0.000059394566,0.000018920566,0.00003065563,0.000031386437],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017060807,0.00023444678,0.00024884715,0.00019864163,0.00014921419,0.0003010417,0.000186693,0.00029994905,0.0003826071],"category_scores_gemma":[0.00024821685,0.00018879764,0.0001933053,0.00013723367,0.000204441,0.00022795744,0.00016067569,0.00025282495,0.00029517122],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000009962368,0.0000023738687,0.00003141602,0.0000093461485,0.0000012978918,0.000010633698,0.000005707386,0.000022492826,0.99975806,0.0000134998845,0.000004458519,0.00013065104],"study_design_scores_gemma":[0.0000049847567,0.000020246785,0.00031787314,9.997143e-7,0.000002802068,0.000018036979,0.0000043816353,0.0004669212,0.9989531,0.0000050199014,0.00020387482,0.0000016593029],"about_ca_topic_score_codex":0.0007424311,"about_ca_topic_score_gemma":0.00088951626,"teacher_disagreement_score":0.0007424311,"about_ca_system_score_codex":0.00036646146,"about_ca_system_score_gemma":0.00016529445,"threshold_uncertainty_score":0.0026589036},"labels":[],"label_agreement":null},{"id":"W2122143464","doi":"10.1002/ceat.201000079","title":"Biological Nutrient Removal Using a Novel Laboratory‐Scale Twin Fluidized‐Bed Bioreactor","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Wastewater Treatment and Nitrogen Removal","field":"Environmental Science","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Effluent; Bioreactor; Fluidized bed; Phosphorus; Chemistry; Nitrogen; Wastewater; Nutrient; Organic matter; Yield (engineering); Pulp and paper industry; Environmental engineering; Environmental science; Materials science; Organic chemistry; Metallurgy","score_opus":0.008554665020844439,"score_gpt":0.19912560085853093,"score_spread":0.1905709358376865,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2122143464","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9520588,0.00077759207,0.04564139,0.00010564209,0.0000966382,0.00006064351,0.00015986277,0.0004582085,0.000641252],"genre_scores_gemma":[0.96159637,0.00048028823,0.0360566,0.00004588431,0.000026343538,0.00006319619,0.0003836874,0.000027936047,0.0013196986],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997148,0.000039955168,0.000030356285,0.000064539156,0.000120666366,0.000029631825],"domain_scores_gemma":[0.9998791,0.000019131676,0.000026173004,0.000013533489,0.000033859855,0.000028089069],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00032877197,0.0004976056,0.0005742876,0.0003329758,0.00023889402,0.00061665825,0.00085880735,0.0005247179,0.0003966582],"category_scores_gemma":[0.00029220962,0.00020485779,0.00060384313,0.0002704655,0.00018499135,0.0004964198,0.00031361525,0.0004037607,0.00038128154],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000051050025,0.000043734162,0.00014862548,0.00003546869,0.0000045293013,0.000033855787,0.000006116834,0.00037008774,0.99745816,0.000026531701,0.00002831645,0.0017935256],"study_design_scores_gemma":[0.00003513784,0.0004963177,0.0013062432,0.0000064092324,0.000029450488,0.0002586827,0.000019659423,0.014737791,0.9816523,0.00003694553,0.0014036844,0.00001735054],"about_ca_topic_score_codex":0.0020515916,"about_ca_topic_score_gemma":0.0014636284,"teacher_disagreement_score":0.0020515916,"about_ca_system_score_codex":0.00045798512,"about_ca_system_score_gemma":0.00051462196,"threshold_uncertainty_score":0.0040792823},"labels":[],"label_agreement":null},{"id":"W2124357374","doi":"10.1002/ceat.201200348","title":"Multiphase reacting flow studies of bubble column ozonation reactor for water remediation","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Fundação para a Ciência e a Tecnologia","keywords":"Volume of fluid method; Ozone; Bubble; Chemistry; Surface tension; Volume (thermodynamics); Environmental remediation; Multiphase flow; Mechanics; Flow (mathematics); Thermodynamics; Organic chemistry","score_opus":0.012354884862708509,"score_gpt":0.2300715582270123,"score_spread":0.2177166733643038,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2124357374","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96810883,0.00039952446,0.030538082,0.00007731253,0.000015665646,0.000046470166,0.00010054609,0.000073508076,0.0006401014],"genre_scores_gemma":[0.9958872,0.00019437773,0.0033831415,0.000009740831,0.0000027946567,0.000020545764,0.000043815704,0.000006621002,0.00045177477],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999242,0.000013706623,0.0000030376646,0.000014775486,0.000029907596,0.00001443207],"domain_scores_gemma":[0.9999199,0.00003568293,0.000017196377,0.0000036908805,0.000015733727,0.0000077881805],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021365377,0.0003258183,0.0003238768,0.00021716185,0.0001412557,0.00028833828,0.00027523344,0.0003115554,0.00047266157],"category_scores_gemma":[0.0002166525,0.00014149296,0.00022047073,0.000106265914,0.00017933395,0.00027693994,0.00018310852,0.0003201435,0.00007939558],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013303978,0.000060884555,0.0007558416,0.0000634608,0.000007524031,0.00006494658,0.00003141456,0.025080182,0.96969515,0.00093196775,0.000048511272,0.0031270003],"study_design_scores_gemma":[0.00002299771,0.00023903564,0.0010870175,0.0000033784993,0.000008750784,0.00003192508,0.000022744263,0.4336595,0.5641525,0.00021252719,0.00054833235,0.000011356672],"about_ca_topic_score_codex":0.0034842435,"about_ca_topic_score_gemma":0.0017306727,"teacher_disagreement_score":0.0034842435,"about_ca_system_score_codex":0.00040774295,"about_ca_system_score_gemma":0.00028372806,"threshold_uncertainty_score":0.0069279075},"labels":[],"label_agreement":null},{"id":"W2125159395","doi":"10.1002/ceat.201300409","title":"Experiments and Simulations on Bidisperse Solids Suspension in a Mixing Tank","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Impeller; Baffle; Suspension (topology); Lattice Boltzmann methods; Turbulence; Mechanics; Mixing (physics); Eulerian path; Large eddy simulation; Materials science; Mechanical engineering; Engineering; Physics; Lagrangian; Mathematics","score_opus":0.004988852719870079,"score_gpt":0.19825378282043954,"score_spread":0.19326493010056947,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2125159395","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99680305,0.000024212493,0.0021198895,0.00003847961,0.000009180591,0.000023018543,0.00010322495,0.000065571476,0.0008133771],"genre_scores_gemma":[0.9971534,0.000029875506,0.0020838515,0.000009120408,0.0000024221108,0.00003168256,0.00012328084,0.000011109306,0.000555299],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99968195,0.00004490544,0.000025519625,0.000046216504,0.000101780366,0.00009965557],"domain_scores_gemma":[0.9990889,0.00050580315,0.00006521836,0.0000617336,0.00014115122,0.00013712666],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006388157,0.000499898,0.000785481,0.00042923386,0.00088813575,0.0007937454,0.000699012,0.0009590197,0.0021291513],"category_scores_gemma":[0.00097348535,0.0002772744,0.0004721322,0.0005232403,0.00064189156,0.00057382305,0.00062612916,0.0007042684,0.00024960874],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0016463179,0.0010486948,0.0072631543,0.00020086931,0.00006928775,0.0005047028,0.0005020821,0.7370216,0.24342115,0.001764131,0.00024254108,0.006315437],"study_design_scores_gemma":[0.00027050255,0.0013396781,0.002334381,0.000009047726,0.000034248165,0.000028814446,0.00016146993,0.8939885,0.101074055,0.00029335456,0.00042634568,0.00003956919],"about_ca_topic_score_codex":0.0059551806,"about_ca_topic_score_gemma":0.0027523888,"teacher_disagreement_score":0.0059551806,"about_ca_system_score_codex":0.0009323934,"about_ca_system_score_gemma":0.0007962294,"threshold_uncertainty_score":0.011841059},"labels":[],"label_agreement":null},{"id":"W2126164989","doi":"10.1002/ceat.201000297","title":"Development of a Computational Framework to Model the Scale‐up of High‐Solid‐Content Polymer Latex Reactors","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Rheology and Fluid Dynamics Studies","field":"Chemical Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal; Queen's University","funders":"","keywords":"Computational fluid dynamics; Laminar flow; Mixing (physics); Rheology; Scale (ratio); Flow (mathematics); Materials science; Population; Mechanics; Process engineering; Mechanical engineering; Engineering; Physics; Composite material","score_opus":0.008953504211940102,"score_gpt":0.21684993269289476,"score_spread":0.20789642848095466,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2126164989","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.0612197,0.00017493677,0.92981976,0.0002742887,0.0000698983,0.0003464843,0.00033654692,0.0012067587,0.006551623],"genre_scores_gemma":[0.5457707,0.0003794866,0.4469317,0.00010968834,0.00005778059,0.0013539789,0.0005241294,0.00037646212,0.0044960985],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99969363,0.000078526726,0.000020068388,0.00004677004,0.00011461148,0.000046372723],"domain_scores_gemma":[0.9994898,0.00023425114,0.000055109005,0.000061956816,0.00009932694,0.000059492675],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0008177099,0.00085390365,0.0010414147,0.00048166284,0.0011312378,0.0013225449,0.002566022,0.0017667573,0.0023353582],"category_scores_gemma":[0.0013936483,0.00074606563,0.001343957,0.00038045517,0.0010452893,0.0009221516,0.0011918537,0.0015451317,0.00044019968],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000013998373,0.000030861236,0.00028703344,0.00001640717,0.000009803029,0.000038784638,0.000017960114,0.99087864,0.0019785475,0.004770965,0.000120469595,0.0018365734],"study_design_scores_gemma":[0.000006473551,0.0000063821713,0.0000323987,0.0000018951968,0.0000019250529,0.000003830313,0.000002489876,0.99882835,0.00041004727,0.00039164972,0.00031114015,0.00000342849],"about_ca_topic_score_codex":0.019425573,"about_ca_topic_score_gemma":0.0080198655,"teacher_disagreement_score":0.019425573,"about_ca_system_score_codex":0.0013686736,"about_ca_system_score_gemma":0.0030189997,"threshold_uncertainty_score":0.038625002},"labels":[],"label_agreement":null},{"id":"W2127600166","doi":"10.1002/ceat.201500305","title":"Efficiency Factors in Photocatalytic Reactors: Quantum Yield and Photochemical Thermodynamic Efficiency Factor","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Photocatalysis Techniques","field":"Energy","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"Western University","funders":"","keywords":"Chemistry; Photocatalysis; Human decontamination; Yield (engineering); Enthalpy; Quantum yield; Photon; Kinetics; Photochemistry; Thermodynamics; Waste management; Organic chemistry; Optics; Catalysis","score_opus":0.013749293850360885,"score_gpt":0.2387692719758537,"score_spread":0.22501997812549282,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2127600166","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.5271395,0.015494361,0.43142137,0.00051101216,0.00014976528,0.00044246667,0.0015730723,0.0012044536,0.022064129],"genre_scores_gemma":[0.9678684,0.0022687973,0.024455398,0.000061615974,0.000023412586,0.00024231333,0.0005281086,0.00016927558,0.004382788],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99656576,0.0006559076,0.00022763801,0.00040161476,0.0019293767,0.00021966184],"domain_scores_gemma":[0.9972038,0.001691994,0.00026834392,0.0002093082,0.00057711767,0.000049445258],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0053912755,0.00079080666,0.00078598235,0.0017897673,0.0003879139,0.0013874004,0.0011771634,0.0009707758,0.0014480051],"category_scores_gemma":[0.0068499837,0.00055457663,0.0007172009,0.0019705635,0.0010892983,0.0024814974,0.0007187743,0.0008800153,0.0009105838],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0007174062,0.00050035765,0.021009207,0.0013538508,0.00025223638,0.00030196313,0.00035398678,0.068372004,0.7705199,0.025442278,0.0016494483,0.109527454],"study_design_scores_gemma":[0.000021885915,0.00031273963,0.011671509,0.000051918927,0.000053067488,0.00018532603,0.00008460628,0.04426347,0.93325746,0.0040352778,0.005997142,0.00006552373],"about_ca_topic_score_codex":0.0019627102,"about_ca_topic_score_gemma":0.0013800799,"teacher_disagreement_score":0.0053912755,"about_ca_system_score_codex":0.0018985188,"about_ca_system_score_gemma":0.0005107365,"threshold_uncertainty_score":0.02851212},"labels":[],"label_agreement":null},{"id":"W2128817243","doi":"10.1002/ceat.201200029","title":"Simulation of a Compact Multichannel Membrane Reactor for the Production of Pure Hydrogen via Steam Methane Reforming","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":23,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Fonds de recherche du Québec – Nature et technologies; Natural Sciences and Engineering Research Council of Canada","keywords":"Steam reforming; Membrane reactor; Isothermal process; Hydrogen production; Methane; Methane reformer; Hydrogen; Chemistry; Combustion; Catalysis; Plug flow reactor model; Chemical engineering; Nuclear engineering; Syngas; Thermodynamics; Materials science; Waste management; Continuous stirred-tank reactor; Engineering; Organic chemistry; Physical chemistry; Physics","score_opus":0.014594544571841958,"score_gpt":0.24973616788175484,"score_spread":0.2351416233099129,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2128817243","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96075374,0.00015717538,0.026988335,0.0002658211,0.00003966152,0.00008311133,0.0006785474,0.00028727562,0.010746455],"genre_scores_gemma":[0.99185014,0.000059781385,0.005275468,0.000026527932,0.0000049991513,0.00010728025,0.00018650772,0.000023929584,0.002465323],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99989486,0.000023251805,0.0000038280014,0.000020324149,0.000025613917,0.000032125274],"domain_scores_gemma":[0.99960345,0.0002527254,0.000032358166,0.000022403377,0.000050384533,0.00003859993],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00031322174,0.00045110073,0.00080016814,0.00029471202,0.0005926275,0.0007124599,0.0008848592,0.0016219683,0.0034478647],"category_scores_gemma":[0.00062331377,0.00041233812,0.00086741755,0.0002837267,0.0006288005,0.0004627048,0.00042300377,0.0005817439,0.00019511931],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006447959,0.00003342539,0.0005372162,0.000020800228,0.000009511838,0.00004668261,0.000018000103,0.9957211,0.0023251926,0.0005616019,0.000083439525,0.00057855796],"study_design_scores_gemma":[0.000018429246,0.000023401963,0.00019656718,0.000001347687,0.000002366557,0.000003817392,0.0000066079065,0.9989359,0.00064456044,0.00006486203,0.00009851016,0.000003674891],"about_ca_topic_score_codex":0.023095896,"about_ca_topic_score_gemma":0.0087182345,"teacher_disagreement_score":0.023095896,"about_ca_system_score_codex":0.0013552158,"about_ca_system_score_gemma":0.001219281,"threshold_uncertainty_score":0.045922935},"labels":[],"label_agreement":null},{"id":"W2131296596","doi":"10.1002/ceat.200800131","title":"Development of an Industrial Multi‐Injection Microreactor for Fast and Exothermic Reactions – Part II","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Innovative Microfluidic and Catalytic Techniques Innovation","field":"Engineering","cited_by":69,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Microreactor; Exothermic reaction; Yield (engineering); Mixing (physics); Chemistry; Process engineering; Materials science; Organic chemistry; Engineering; Catalysis; Metallurgy","score_opus":0.02808168006868822,"score_gpt":0.2291030019387868,"score_spread":0.20102132187009858,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2131296596","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.3534117,0.0036229454,0.62845397,0.00038453174,0.0003061194,0.0013620737,0.00068948703,0.007185243,0.004583975],"genre_scores_gemma":[0.4743147,0.0008502661,0.5202242,0.00008603852,0.000043593216,0.0005032045,0.00039067966,0.00020092477,0.0033863739],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99950373,0.000059472968,0.00004393374,0.00012208741,0.00019614468,0.000074589625],"domain_scores_gemma":[0.99975544,0.000054037777,0.000049622005,0.00004472436,0.00005545965,0.000040823088],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012491917,0.00065543014,0.00074652646,0.0004212718,0.00032060593,0.000496808,0.00080409786,0.00050146336,0.0013022467],"category_scores_gemma":[0.0004896534,0.00046879263,0.0004869379,0.00021945355,0.00042173892,0.00045460855,0.0003866717,0.00069860177,0.0006326929],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000059388363,0.00003218786,0.00012643916,0.00009531885,0.000006555071,0.000025141388,0.00001777471,0.0006266966,0.9882995,0.0007012307,0.0001507921,0.009858956],"study_design_scores_gemma":[0.000019214727,0.00025878404,0.0005685692,0.0000048129814,0.00001117257,0.00008431266,0.000003410764,0.006241114,0.9883829,0.000053709668,0.0043580323,0.000013982278],"about_ca_topic_score_codex":0.00076419185,"about_ca_topic_score_gemma":0.0006326573,"teacher_disagreement_score":0.0013022467,"about_ca_system_score_codex":0.0006971844,"about_ca_system_score_gemma":0.00092623173,"threshold_uncertainty_score":0.0066064596},"labels":[],"label_agreement":null},{"id":"W2133611001","doi":"10.1002/ceat.200407041","title":"Modeling of Methane Oxidative Coupling under Periodic Operation by Neural Network","year":2005,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysis and Oxidation Reactions","field":"Chemical Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Oxidative coupling of methane; Artificial neural network; Methane; Catalysis; Biological system; Coupling (piping); Selectivity; Ethylene; Chemistry; Set (abstract data type); Control theory (sociology); Thermodynamics; Computer science; Engineering; Organic chemistry; Physics; Artificial intelligence; Mechanical engineering","score_opus":0.008568822376332287,"score_gpt":0.222960851349122,"score_spread":0.21439202897278972,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2133611001","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.78735274,0.00025058215,0.20760925,0.00012885216,0.000033378306,0.000036807676,0.000150761,0.00032409315,0.0041134623],"genre_scores_gemma":[0.99502486,0.00004291846,0.0040480345,0.000004637002,0.0000021204933,0.000022770291,0.00003764612,0.000004404987,0.00081251486],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998969,0.000025657266,0.0000047061253,0.000023729659,0.00003212497,0.000016854181],"domain_scores_gemma":[0.9998272,0.0000870671,0.000026796988,0.0000130428325,0.00003794937,0.000008032062],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026967525,0.00038183862,0.0003245429,0.00021771915,0.00016470415,0.00033869356,0.00044714086,0.00055193494,0.00082104857],"category_scores_gemma":[0.0006932727,0.0002383319,0.00032402412,0.00016549,0.0002861829,0.0004787872,0.00018213272,0.00030150067,0.00009770683],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000029157953,0.000013368645,0.00047296827,0.00001182021,0.000009333458,0.000018237133,0.0000071354807,0.99410903,0.0022692229,0.00027133233,0.00003527265,0.0027531423],"study_design_scores_gemma":[9.0552186e-7,0.0000059885283,0.00009982271,3.9197525e-7,8.9317564e-7,0.0000011158597,6.700073e-7,0.9994199,0.0003845016,0.000069781585,0.000015300398,8.366757e-7],"about_ca_topic_score_codex":0.0063942587,"about_ca_topic_score_gemma":0.0036581096,"teacher_disagreement_score":0.0063942587,"about_ca_system_score_codex":0.0005643524,"about_ca_system_score_gemma":0.00037535126,"threshold_uncertainty_score":0.012714088},"labels":[],"label_agreement":null},{"id":"W2134487794","doi":"10.1002/ceat.200800296","title":"Electropolishing of Vertical Plates under Intensified Mass Transfer Conditions in a Gas Stirred, Modified Parallel Plate Reactor","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Electrodeposition and Electroless Coatings","field":"Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Electropolishing; Mass transfer; Chemistry; Cathode; Limiting current; Electrochemistry; Analytical Chemistry (journal); Polishing; Diffusion; Mass transfer coefficient; Range (aeronautics); Materials science; Thermodynamics; Electrode; Metallurgy; Electrolyte; Composite material; Chromatography","score_opus":0.008471823543352065,"score_gpt":0.1942797461617548,"score_spread":0.18580792261840273,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2134487794","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9913446,0.000390135,0.007595014,0.000019871768,0.000021053022,0.000027665154,0.000050430033,0.00011070938,0.0004405206],"genre_scores_gemma":[0.98726857,0.00034775084,0.010658945,0.00001333715,0.000012935738,0.000016363583,0.000089846726,0.000022329283,0.0015698677],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99981433,0.000019398887,0.000009943062,0.000053746557,0.00007227542,0.000030385201],"domain_scores_gemma":[0.99979,0.000059883216,0.000070086324,0.000034482087,0.000023572267,0.000021911172],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025301496,0.0005215754,0.0004281209,0.00018566658,0.00011719158,0.00040742647,0.00049912214,0.00030528664,0.0004546725],"category_scores_gemma":[0.0004617832,0.00031516695,0.0002965316,0.00024904724,0.0002837321,0.00032362,0.00027328255,0.0005115735,0.00016538937],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000049927123,0.000010907722,0.00006520884,0.000027472373,0.0000034960563,0.000031025298,0.000009087342,0.00018999245,0.99854124,0.000027534537,0.000008166236,0.0010359974],"study_design_scores_gemma":[0.0000053751646,0.000099653735,0.0006501105,0.0000010941524,0.000005421101,0.00003403701,0.00000455829,0.00087732146,0.9980946,0.000008282628,0.00021709989,0.0000023731418],"about_ca_topic_score_codex":0.0007167069,"about_ca_topic_score_gemma":0.0006707668,"teacher_disagreement_score":0.0007167069,"about_ca_system_score_codex":0.00028341336,"about_ca_system_score_gemma":0.00023068128,"threshold_uncertainty_score":0.0020563602},"labels":[],"label_agreement":null},{"id":"W2135477332","doi":"10.1002/ceat.201100119","title":"Biodiesel Production from the Lipid of Wastewater Sludge Using an Acidic Heterogeneous Catalyst","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Biodiesel Production and Applications","field":"Engineering","cited_by":29,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada; Snap","keywords":"Catalysis; Biodiesel; Mesoporous material; Biodiesel production; Microreactor; Scanning electron microscope; Wastewater; Nuclear chemistry; Yield (engineering); Materials science; Heterogeneous catalysis; Chemical engineering; Chemistry; Pulp and paper industry; Waste management; Organic chemistry; Composite material","score_opus":0.024558380184107737,"score_gpt":0.20210352232632287,"score_spread":0.17754514214221512,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2135477332","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9966388,0.00039606378,0.0020957398,0.00003074212,0.000011541342,0.000012216446,0.00006918507,0.000030194069,0.00071558566],"genre_scores_gemma":[0.9965191,0.000301404,0.0019953828,0.00000962407,0.0000040475225,0.000005948548,0.00010602367,0.000008946885,0.0010495031],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99987626,0.000016988515,0.000010752315,0.000027111142,0.00004387657,0.000025064193],"domain_scores_gemma":[0.9999336,0.000009542464,0.000011670015,0.0000060562184,0.000018941311,0.000020113735],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018251169,0.00042419884,0.00034966087,0.00028699933,0.00014871592,0.00037615834,0.00021601429,0.00023609394,0.00040852357],"category_scores_gemma":[0.00016571439,0.00019223812,0.00027929345,0.00022119674,0.00018385643,0.00021633254,0.00030762193,0.0002657748,0.00028114786],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000030408588,0.0000082753795,0.00006779896,0.000017254777,0.0000027353406,0.000024450397,0.0000045121287,0.00007034368,0.99919266,0.00001822292,0.000004987964,0.0005583302],"study_design_scores_gemma":[0.000007645946,0.00007385379,0.0005449646,0.0000021458468,0.0000071177847,0.000032440512,0.000009320707,0.0006327524,0.9983943,0.000009146009,0.0002841064,0.0000022337463],"about_ca_topic_score_codex":0.0009584333,"about_ca_topic_score_gemma":0.0014092476,"teacher_disagreement_score":0.0009584333,"about_ca_system_score_codex":0.00024586968,"about_ca_system_score_gemma":0.00022229805,"threshold_uncertainty_score":0.0019057393},"labels":[],"label_agreement":null},{"id":"W2135601132","doi":"10.1002/ceat.200700158","title":"Intensification of Rate of Diffusion Controlled Reactions in a Parallel Plate Electrochemical Reactor Stirred by a Curtain of Electrochemically Generated Gas Bubbles","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Corrosion Behavior and Inhibition","field":"Materials Science","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"","keywords":"Mass transfer; Electrolyte; Limiting current; Chemistry; Electrochemistry; Oxygen; Diffusion; Mass transfer coefficient; Analytical Chemistry (journal); Confined space; Chemical engineering; Materials science; Electrode; Thermodynamics; Chromatography","score_opus":0.005553308024898647,"score_gpt":0.21767867096810453,"score_spread":0.2121253629432059,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2135601132","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97802436,0.0007166759,0.01943652,0.00012095601,0.000082368184,0.00004936681,0.000110393004,0.00041094716,0.0010483366],"genre_scores_gemma":[0.98381686,0.00045672577,0.012797288,0.000034709617,0.000026558375,0.000035316854,0.000114756636,0.0000486397,0.0026691544],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99960536,0.00005363278,0.000024322604,0.00012048539,0.00014666967,0.00004957341],"domain_scores_gemma":[0.9995869,0.00014684722,0.00008475917,0.000042944477,0.000099791505,0.00003890752],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00047191783,0.00074872904,0.0005416571,0.00018823071,0.00010102305,0.00047287022,0.00066298834,0.00044031884,0.0008997914],"category_scores_gemma":[0.0006759585,0.00035907535,0.0003217094,0.00016497073,0.0002730768,0.0004965864,0.00025584977,0.00057797274,0.0003207955],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006396615,0.000012135719,0.00003675832,0.00002282633,0.000002114571,0.000010921559,0.000009600218,0.000097818054,0.9987815,0.000024804604,0.000015338032,0.00092229526],"study_design_scores_gemma":[0.000008608832,0.000109606015,0.00022899454,9.603182e-7,0.0000043454033,0.000015225831,0.0000034549785,0.0022317476,0.99713147,0.000008774977,0.0002534763,0.0000033102758],"about_ca_topic_score_codex":0.0010116287,"about_ca_topic_score_gemma":0.0010583516,"teacher_disagreement_score":0.0010116287,"about_ca_system_score_codex":0.000490164,"about_ca_system_score_gemma":0.0002548268,"threshold_uncertainty_score":0.0035563707},"labels":[],"label_agreement":null},{"id":"W2138240948","doi":"10.1002/ceat.200800511","title":"CFD Investigation of the Mixing of Yield‐Pseudoplastic Fluids with Anchor Impellers","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":62,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Computational fluid dynamics; Shear thinning; Mixing (physics); Mechanics; Slip factor; Homogenization (climate); Materials science; Rheology; Agitator; Power consumption; Turbulence; Mechanical engineering; Thermodynamics; Engineering; Power (physics); Physics; Composite material","score_opus":0.0030456887065002398,"score_gpt":0.15016043180607705,"score_spread":0.1471147430995768,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2138240948","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9868102,0.00017806645,0.011526112,0.00004688315,0.000020407388,0.00002487356,0.000076147364,0.00007088474,0.0012464797],"genre_scores_gemma":[0.9949798,0.00008613837,0.0043941922,0.000006802194,0.0000050975436,0.0000085256825,0.000055668595,0.000008310825,0.00045545536],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9997987,0.000035032426,0.000015398495,0.0000251471,0.00008617651,0.00003955115],"domain_scores_gemma":[0.99969316,0.00015553326,0.00005332504,0.000020592855,0.00005340963,0.000024101331],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00039164658,0.00032083434,0.00042753038,0.00050806307,0.00031817696,0.0004760816,0.00026893168,0.00047362692,0.0007971161],"category_scores_gemma":[0.0009067087,0.00016412379,0.00033282727,0.00041070994,0.00034033525,0.00039032675,0.00028854757,0.00031542094,0.00015651363],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0013856662,0.00023098379,0.0100975055,0.00021681873,0.00003228032,0.0010618867,0.0001964131,0.14072573,0.8228289,0.0019350533,0.00030841515,0.020980401],"study_design_scores_gemma":[0.00008885186,0.00065916416,0.008670357,0.000011544758,0.000028567774,0.0001809224,0.00009304316,0.58787245,0.40033576,0.00023216059,0.0017929375,0.000034262765],"about_ca_topic_score_codex":0.0023085757,"about_ca_topic_score_gemma":0.0011640571,"teacher_disagreement_score":0.0023085757,"about_ca_system_score_codex":0.0004248915,"about_ca_system_score_gemma":0.0003616273,"threshold_uncertainty_score":0.0045902133},"labels":[],"label_agreement":null},{"id":"W2139408248","doi":"10.1002/ceat.201200445","title":"Wastewater Minimization in Pulp and Paper Industries through Energy‐Efficient Reverse‐Osmosis Membrane Processes","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Process Optimization and Integration","field":"Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Reverse osmosis; Wastewater; Waste management; Environmental science; Reverse osmosis plant; Desalination; Kraft process; Paper mill; Kraft paper; Engineering; Environmental engineering; Pulp and paper industry; Chemistry; Effluent; Membrane","score_opus":0.004646981459910275,"score_gpt":0.16801621189762003,"score_spread":0.16336923043770976,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2139408248","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95912325,0.0014475706,0.035579085,0.00016955115,0.000021073758,0.000030373427,0.000046703375,0.00004410466,0.003538354],"genre_scores_gemma":[0.99118537,0.0005294691,0.0070838025,0.00001092838,0.0000033007757,0.000019215002,0.000024585033,0.0000041104763,0.0011391137],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999068,0.000020116746,0.0000050296753,0.000019031064,0.000027460035,0.000021639184],"domain_scores_gemma":[0.9999479,0.000018258152,0.000015066719,0.0000032757798,0.000010507317,0.0000050124613],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021741774,0.00029119954,0.00044848656,0.00026805748,0.00018852402,0.0006303305,0.00031593078,0.0004061948,0.0004765361],"category_scores_gemma":[0.00015733586,0.00017034523,0.0005175763,0.00027387202,0.00016151916,0.00037877544,0.00028550514,0.000273953,0.00010277789],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003266487,0.0004017217,0.001198594,0.00049306423,0.000050397284,0.00025318615,0.00005594192,0.2846369,0.6752308,0.004658912,0.00031341903,0.032380495],"study_design_scores_gemma":[0.00007750939,0.0005348515,0.0014930307,0.000018123394,0.000053869873,0.000071404174,0.00006268485,0.58081824,0.41206235,0.0024209907,0.0023681158,0.000018778734],"about_ca_topic_score_codex":0.0013652185,"about_ca_topic_score_gemma":0.0017785161,"teacher_disagreement_score":0.0013652185,"about_ca_system_score_codex":0.00051826175,"about_ca_system_score_gemma":0.00039584754,"threshold_uncertainty_score":0.0037602782},"labels":[],"label_agreement":null},{"id":"W2140677120","doi":"10.1002/ceat.201000302","title":"Computational Fluid Dynamics Simulation of Pilot‐Plant‐Scale Two‐Phase Separators","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Cyclone Separators and Fluid Dynamics","field":"Engineering","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Computational fluid dynamics; Volume of fluid method; Pilot plant; Mechanics; Mist; Volume (thermodynamics); Scale (ratio); SCALE-UP; Simulation; Mechanical engineering; Engineering; Thermodynamics; Meteorology; Physics; Flow (mathematics); Waste management","score_opus":0.0080493187024596,"score_gpt":0.22097854182964957,"score_spread":0.21292922312718998,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2140677120","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97984344,0.00006411651,0.016671488,0.0001123429,0.000026620692,0.00006822173,0.00020512879,0.00013301756,0.0028755818],"genre_scores_gemma":[0.9948979,0.000037136073,0.0040595676,0.00001118385,0.0000028242675,0.00006733099,0.00011830487,0.000009378552,0.0007963965],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998673,0.000035940982,0.000006294195,0.000018038581,0.00003776186,0.00003460507],"domain_scores_gemma":[0.99926096,0.00048791312,0.00004540914,0.000038803915,0.00010537652,0.0000615163],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002666357,0.00043564138,0.0005431434,0.00032924308,0.0006785102,0.0005707489,0.0007381025,0.0010278544,0.0015564797],"category_scores_gemma":[0.00082774035,0.00028873057,0.0005128202,0.00031550726,0.0006246206,0.00037792927,0.00033028275,0.0006822158,0.00016577444],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00022062301,0.0001684362,0.0024303286,0.000037794427,0.000015020859,0.00017323125,0.000067078625,0.985213,0.00789118,0.0006920549,0.000234328,0.0028568825],"study_design_scores_gemma":[0.00004796963,0.000069744965,0.0006437394,0.0000020795346,0.0000032275125,0.000010859892,0.000019935156,0.9951747,0.0036558616,0.00012324538,0.00024213492,0.0000066262414],"about_ca_topic_score_codex":0.017003592,"about_ca_topic_score_gemma":0.0068098987,"teacher_disagreement_score":0.017003592,"about_ca_system_score_codex":0.0008817872,"about_ca_system_score_gemma":0.0012871939,"threshold_uncertainty_score":0.033809245},"labels":[],"label_agreement":null},{"id":"W2140816614","doi":"10.1002/ceat.200900297","title":"Pipeline Flow Behavior of Water‐in‐Oil Emulsions with and without a Polymeric Additive in the Aqueous Phase","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Rheology and Fluid Dynamics Studies","field":"Chemical Engineering","cited_by":43,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Drag; Emulsion; Shell (structure); Phase (matter); Aqueous solution; Aqueous two-phase system; Turbulence; Chemistry; Oil droplet; Chemical engineering; Chromatography; Materials science; Composite material; Thermodynamics; Organic chemistry; Physics; Engineering","score_opus":0.0034500904480844535,"score_gpt":0.21389432962181715,"score_spread":0.2104442391737327,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2140816614","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9953055,0.0002670091,0.0036605673,0.000014813629,0.00001471275,0.000018977878,0.000091583104,0.00004887703,0.00057788845],"genre_scores_gemma":[0.9950059,0.00024143535,0.0032429474,0.000017084993,0.0000059246427,0.000021913895,0.00018646788,0.000019422709,0.0012589422],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998697,0.000018137642,0.000011932357,0.000030209934,0.000036233254,0.000033732424],"domain_scores_gemma":[0.99975425,0.00008115704,0.00007382671,0.000009482281,0.000055263183,0.000026043856],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003330628,0.00036006395,0.00017911897,0.000278448,0.00016620463,0.00023366458,0.00015095065,0.00020886617,0.0008201059],"category_scores_gemma":[0.00036812032,0.00010861183,0.00023285084,0.00017055048,0.00024676824,0.00035056326,0.00012251489,0.00033302468,0.00013235182],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012489445,0.000019359966,0.00018820123,0.000020792688,0.0000031541647,0.000027456636,0.000021443699,0.00013092058,0.99857855,0.000036409394,0.0000096376525,0.0008392853],"study_design_scores_gemma":[0.000007953634,0.0003517495,0.0011689318,0.000003640689,0.0000084588355,0.000018364284,0.000017475024,0.0012327303,0.99688524,0.0000139892345,0.00028661825,0.000004866422],"about_ca_topic_score_codex":0.0013415874,"about_ca_topic_score_gemma":0.00069837976,"teacher_disagreement_score":0.0013415874,"about_ca_system_score_codex":0.00030873224,"about_ca_system_score_gemma":0.00021435854,"threshold_uncertainty_score":0.0027434826},"labels":[],"label_agreement":null},{"id":"W2144447559","doi":"10.1002/ceat.201200425","title":"Using Tomography to Characterize the Mixing of Non‐Newtonian Fluids with a Maxblend Impeller","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":19,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Baffle; Impeller; Mixing (physics); Shear thinning; Non-Newtonian fluid; Materials science; Mechanics; Reynolds number; Newtonian fluid; Xanthan gum; Agitator; Rheology; Composite material; Turbulence; Mechanical engineering; Physics; Engineering","score_opus":0.00467002533603709,"score_gpt":0.1749667396293537,"score_spread":0.1702967142933166,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2144447559","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.8636324,0.00046089364,0.13485783,0.000100929545,0.0000157786,0.00006990439,0.00009335705,0.00026846718,0.0005004126],"genre_scores_gemma":[0.9012287,0.00019854664,0.09775959,0.000026159749,0.000009825767,0.000040280764,0.00007438359,0.000032801727,0.0006296863],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998393,0.000039391452,0.000010312149,0.000035337223,0.00005751161,0.00001798584],"domain_scores_gemma":[0.9991585,0.0004790246,0.00017454903,0.00006417155,0.00008865738,0.000035211768],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00069955416,0.00041826267,0.00025940547,0.00045535603,0.00012970365,0.00032052404,0.00035214156,0.00037716748,0.0007685353],"category_scores_gemma":[0.0014998834,0.00026085708,0.00019891532,0.00029626398,0.00037015593,0.00080420624,0.00024361046,0.00037273878,0.00010857341],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00013984434,0.000013581498,0.0008671923,0.000021743404,0.0000035989651,0.0000397043,0.000025152458,0.0005368365,0.9939486,0.0000864834,0.000018429011,0.0042989175],"study_design_scores_gemma":[0.000017703283,0.00027004984,0.005993738,0.000003262092,0.000013004986,0.00020370109,0.00002013904,0.024235945,0.9686794,0.00004721402,0.00049771287,0.000018094333],"about_ca_topic_score_codex":0.00060029206,"about_ca_topic_score_gemma":0.0005644606,"teacher_disagreement_score":0.0007685353,"about_ca_system_score_codex":0.0002983496,"about_ca_system_score_gemma":0.00022839037,"threshold_uncertainty_score":0.0036996007},"labels":[],"label_agreement":null},{"id":"W2145181833","doi":"10.1002/ceat.200500237","title":"Experimental Investigation of Ethanol Enrichment Behavior in Batch and Continuous Feed Ultrasonic Atomization Systems","year":2006,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Electrohydrodynamics and Fluid Dynamics","field":"Engineering","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"National Research Council Canada","funders":"","keywords":"Ultrasonic sensor; Alcohol; Mist; Chemistry; Materials science; Ethanol; Chemical engineering; Chromatography; Analytical Chemistry (journal); Organic chemistry; Acoustics","score_opus":0.00233792362933375,"score_gpt":0.17324735267695432,"score_spread":0.17090942904762058,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2145181833","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9959054,0.0003037002,0.0029195745,0.000024334959,0.0000112186335,0.000053172564,0.00016588965,0.00007042105,0.0005463179],"genre_scores_gemma":[0.9942526,0.00028359672,0.0044280943,0.000022094151,0.000010494915,0.00008370912,0.00019848303,0.000021302598,0.000699577],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9994369,0.00007290596,0.00004100663,0.00011091934,0.00022825402,0.00011002531],"domain_scores_gemma":[0.99884963,0.0006087494,0.0000940476,0.00008632582,0.00030976822,0.00005139376],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005469999,0.00042483135,0.00055833627,0.00031873013,0.0005501382,0.00038222558,0.00060936564,0.0006176299,0.0012413587],"category_scores_gemma":[0.0011809669,0.0002846197,0.00022207985,0.00041548087,0.0004373332,0.00037168828,0.00030657172,0.0006330907,0.00028053523],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00038780388,0.00015462551,0.00061230594,0.00009108135,0.000008962852,0.00005332779,0.00012026993,0.0004079642,0.99585754,0.00004689902,0.000041720887,0.0022175733],"study_design_scores_gemma":[0.000020935675,0.0007158622,0.0014314172,0.0000034396905,0.000012110852,0.000022758493,0.00003266938,0.001867635,0.9956044,0.000011424323,0.00026833572,0.0000090611675],"about_ca_topic_score_codex":0.0027884648,"about_ca_topic_score_gemma":0.0026968084,"teacher_disagreement_score":0.0027884648,"about_ca_system_score_codex":0.00075665995,"about_ca_system_score_gemma":0.00028744378,"threshold_uncertainty_score":0.0055444837},"labels":[],"label_agreement":null},{"id":"W2149477305","doi":"10.1002/ceat.200800565","title":"Mapping of the Operating Conditions for an Interconnected Fluidized Bed Reactor for CO<sub>2</sub> Separation by Chemical Looping Combustion","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Chemical Looping and Thermochemical Processes","field":"Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Ministry of Economy","keywords":"Chemical looping combustion; Combustion; Fluidized bed; Nuclear engineering; Chemical reactor; Process engineering; Fluidized bed combustion; Fluidization; Air separation; Waste management; Chemistry; Oxygen; Environmental science; Chemical engineering; Engineering","score_opus":0.008792638039207547,"score_gpt":0.237431951610784,"score_spread":0.22863931357157646,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2149477305","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99570775,0.00012493486,0.0034990811,0.000023545885,0.0000050338613,0.00001565641,0.00010760459,0.00009632412,0.00042017334],"genre_scores_gemma":[0.99841607,0.00004260716,0.0013666668,0.000003723565,0.0000010464336,0.000010031627,0.000056951856,0.000008648941,0.00009422183],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9997862,0.000033752513,0.0000118162225,0.000058473714,0.00007261691,0.000037183825],"domain_scores_gemma":[0.9996866,0.000144541,0.00006359917,0.000024416593,0.00005791902,0.00002295394],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003154363,0.0004006382,0.0004288126,0.00044044587,0.00044156492,0.0008124065,0.00036307276,0.00038143044,0.0007038376],"category_scores_gemma":[0.00065229565,0.00030930614,0.00026571297,0.00022309409,0.00044729328,0.0005327508,0.00031344994,0.00034678186,0.00016420173],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005218371,0.00007255088,0.00240982,0.00006547735,0.000009711635,0.00006545343,0.0000792285,0.0036869599,0.98890775,0.0001114026,0.0000737092,0.0039961096],"study_design_scores_gemma":[0.000023617116,0.0003444115,0.005364894,0.0000063154207,0.000018374198,0.000042957516,0.00006051641,0.017644627,0.97604066,0.00006686021,0.00037095035,0.000015743151],"about_ca_topic_score_codex":0.0017906696,"about_ca_topic_score_gemma":0.0020134682,"teacher_disagreement_score":0.0017906696,"about_ca_system_score_codex":0.00048366576,"about_ca_system_score_gemma":0.00034962854,"threshold_uncertainty_score":0.0035604239},"labels":[],"label_agreement":null},{"id":"W2149567944","doi":"10.1002/ceat.200900440","title":"Computational Fluid Dynamics Study of a Styrene Polymerization Reactor","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":24,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Toronto Metropolitan University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Continuous stirred-tank reactor; Computational fluid dynamics; Styrene; Homogeneity (statistics); Polymerization; Materials science; Mixing (physics); Mechanics; Chemical reactor; Volumetric flow rate; Plug flow reactor model; Chemical engineering; Thermodynamics; Chemistry; Polymer; Composite material; Engineering; Copolymer; Physics; Computer science","score_opus":0.0021230090143584987,"score_gpt":0.175469551606,"score_spread":0.1733465425916415,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2149567944","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.93343556,0.00018573318,0.054626517,0.0003814919,0.000087824556,0.00013863624,0.00038648225,0.0002234843,0.010534279],"genre_scores_gemma":[0.98678255,0.00007467692,0.0109478505,0.000029559376,0.000009178102,0.00010334153,0.0001744568,0.000020539426,0.001857936],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998498,0.000034415687,0.000007255842,0.000026379419,0.000049864084,0.000032250016],"domain_scores_gemma":[0.9995653,0.00027544476,0.000032029013,0.000025736355,0.000066922286,0.000034531924],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00032613653,0.00039477786,0.0007381179,0.00034930056,0.00080946623,0.0007648967,0.0005255603,0.0010994938,0.0017976125],"category_scores_gemma":[0.00083907525,0.00027001667,0.0006111891,0.00028285646,0.0006953799,0.00040194325,0.00037629248,0.00074256054,0.00019291],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00012281608,0.00011185113,0.0011831541,0.00004043997,0.000016440728,0.00017190845,0.00006218185,0.97626716,0.01671678,0.002377613,0.00019347349,0.002736207],"study_design_scores_gemma":[0.00001867575,0.000026593736,0.00026398775,0.0000022262288,0.0000023788043,0.000009275237,0.0000084946505,0.99629813,0.002977118,0.0001338149,0.0002543796,0.000004875221],"about_ca_topic_score_codex":0.01144339,"about_ca_topic_score_gemma":0.0029414503,"teacher_disagreement_score":0.01144339,"about_ca_system_score_codex":0.0008957146,"about_ca_system_score_gemma":0.0015547882,"threshold_uncertainty_score":0.022753537},"labels":[],"label_agreement":null},{"id":"W2151459745","doi":"10.1002/ceat.200700459","title":"Modeling of Flow Burst, Flow Timing in Lab‐on‐a‐CD Systems and Its Application in Digital Chemical Analysis","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Microfluidic and Capillary Electrophoresis Applications","field":"Engineering","cited_by":25,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Flow (mathematics); Computer science; Function (biology); Data flow model; Simulation; Process engineering; Mechanics; Control engineering; Engineering; Physics","score_opus":0.005789552381648393,"score_gpt":0.1811503486843146,"score_spread":0.1753607963026662,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2151459745","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.3300995,0.0002428841,0.6623794,0.00027730272,0.000032040407,0.00008227633,0.0001197214,0.00073400454,0.0060328697],"genre_scores_gemma":[0.978488,0.00010626887,0.01912858,0.00002519333,0.0000043914088,0.000071058304,0.000037340185,0.000021165299,0.0021179304],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998745,0.000026381178,0.0000048119723,0.000026819323,0.00005004764,0.000017467117],"domain_scores_gemma":[0.99966073,0.00023266334,0.000030322757,0.000023881685,0.000034903813,0.000017536417],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034443956,0.00024652318,0.00031589344,0.0003471222,0.0003193159,0.0004498419,0.0005328816,0.00064942084,0.0011211728],"category_scores_gemma":[0.0010026414,0.00020686422,0.00020671063,0.00019908305,0.00064951245,0.00055761053,0.00024459098,0.0003282671,0.0001319949],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00005694084,0.000055757926,0.0007874756,0.000022674594,0.0000056417252,0.000040904048,0.000027964534,0.97219557,0.013297781,0.007653439,0.00019737065,0.0056585213],"study_design_scores_gemma":[0.0000025841193,0.0000054483385,0.000036906655,5.2428425e-7,5.122159e-7,0.0000026243601,0.0000010808784,0.99805295,0.0015475026,0.00025705103,0.000091799746,9.730537e-7],"about_ca_topic_score_codex":0.0054188985,"about_ca_topic_score_gemma":0.0015884489,"teacher_disagreement_score":0.0054188985,"about_ca_system_score_codex":0.0012062232,"about_ca_system_score_gemma":0.00085600995,"threshold_uncertainty_score":0.010774732},"labels":[],"label_agreement":null},{"id":"W2152682329","doi":"10.1002/ceat.201100351","title":"Design Criteria for Oilfield Separators Improved by Computational Fluid Dynamics","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Calgary","funders":"","keywords":"Computational fluid dynamics; Separator (oil production); Entrainment (biomusicology); Mechanics; Fluid dynamics; Petroleum engineering; Thermodynamics; Chemistry; Materials science; Engineering; Physics","score_opus":0.008882757187639402,"score_gpt":0.20133834107681783,"score_spread":0.19245558388917844,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2152682329","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.14879896,0.00044347675,0.8437767,0.0001560689,0.00003722006,0.00018561642,0.00009653228,0.0005072518,0.0059980857],"genre_scores_gemma":[0.8928861,0.00019392958,0.10409201,0.000028978444,0.000016759239,0.0002807315,0.000112521855,0.0000724246,0.0023165785],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9993919,0.0001696217,0.000043181135,0.00006672856,0.00027352286,0.000055033765],"domain_scores_gemma":[0.9987697,0.00050843816,0.00018135432,0.000052035397,0.00044636967,0.0000420824],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0013840972,0.0008730324,0.0007334519,0.0009229242,0.0005937967,0.0011610516,0.0006661313,0.0008411169,0.0015193368],"category_scores_gemma":[0.003202558,0.0005065451,0.00038411008,0.00035333922,0.00034774424,0.0005824238,0.0006652514,0.00044097565,0.00040276445],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00028712853,0.00008191728,0.0012782309,0.00024711082,0.00002204059,0.00013761032,0.00010258906,0.89517176,0.05580941,0.008004108,0.00076316827,0.038095005],"study_design_scores_gemma":[0.000016159232,0.00006385216,0.00016778102,0.000012178962,0.000009773498,0.000016104741,0.000013007114,0.9835723,0.014169099,0.0008000027,0.0011478246,0.000011803625],"about_ca_topic_score_codex":0.0018032179,"about_ca_topic_score_gemma":0.0015890026,"teacher_disagreement_score":0.0018032179,"about_ca_system_score_codex":0.00094025285,"about_ca_system_score_gemma":0.0011346682,"threshold_uncertainty_score":0.0073198676},"labels":[],"label_agreement":null},{"id":"W2154099584","doi":"10.1002/ceat.200800387","title":"Kinetics of Catalytic Ozonation of Methyl <b><i>tert</i></b>‐Butyl Ether in the Presence of Perfluorooctyl Alumina","year":2009,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalytic Processes in Materials Science","field":"Materials Science","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Catalysis; Chemistry; Methyl tert-butyl ether; Kinetics; Ozone; Ether; Reaction mechanism; Reaction rate; Chemical kinetics; Batch reactor; Heterogeneous catalysis; Organic chemistry; Inorganic chemistry","score_opus":0.006745459842616238,"score_gpt":0.23057293554271177,"score_spread":0.22382747570009554,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2154099584","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99624544,0.0008585522,0.0019868729,0.000025911717,0.000014849412,0.00001227896,0.00015849603,0.00002348462,0.00067404954],"genre_scores_gemma":[0.9983834,0.00039170677,0.00050616625,0.000006760293,0.0000019661552,0.0000074343516,0.00013829436,0.000006757077,0.0005575131],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998479,0.000015537562,0.000009186802,0.000025722822,0.00005806376,0.000043646425],"domain_scores_gemma":[0.99987924,0.00004267375,0.000030877978,0.000006482748,0.00002551147,0.000015191972],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0002385863,0.000331946,0.00029152457,0.00021623685,0.00013833202,0.00030448323,0.00024969087,0.00029252435,0.0008207107],"category_scores_gemma":[0.00035877374,0.00016320897,0.00028811104,0.00014391953,0.00017036925,0.0003356321,0.00014193781,0.000310345,0.00020969626],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0002528404,0.000018652341,0.0006867132,0.000064176194,0.000017491615,0.00004932032,0.000032372798,0.00065774855,0.9962239,0.00009581576,0.000030762192,0.0018702102],"study_design_scores_gemma":[0.000006936933,0.00012293828,0.0020631358,0.0000045211864,0.000011961371,0.00003672841,0.00002637729,0.0043917256,0.9928861,0.000027836071,0.00041560794,0.0000061204614],"about_ca_topic_score_codex":0.002037594,"about_ca_topic_score_gemma":0.0014050383,"teacher_disagreement_score":0.002037594,"about_ca_system_score_codex":0.0002675012,"about_ca_system_score_gemma":0.00020763213,"threshold_uncertainty_score":0.004051447},"labels":[],"label_agreement":null},{"id":"W2155545694","doi":"10.1002/ceat.201000282","title":"Optimization of Methanol Yield from a Lurgi Reactor","year":2011,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalysts for Methane Reforming","field":"Chemical Engineering","cited_by":128,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Methanol; Yield (engineering); Chemistry; Syngas; Methanol reformer; Steam reforming; Chemical engineering; Waste management; Process engineering; Catalysis; Thermodynamics; Organic chemistry; Hydrogen production; Engineering","score_opus":0.015550475319962192,"score_gpt":0.20085526151411429,"score_spread":0.18530478619415208,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2155545694","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97850454,0.0011315005,0.012511234,0.00016141443,0.000021081953,0.000079482525,0.00056591566,0.00032737755,0.006697346],"genre_scores_gemma":[0.9901876,0.0004982583,0.007885133,0.0000133201265,0.0000042806555,0.00005525785,0.0003674124,0.00006609993,0.0009227137],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997143,0.00004554635,0.00001757074,0.00006302959,0.000106706815,0.00005296202],"domain_scores_gemma":[0.9998814,0.000042687436,0.000022929224,0.000011017816,0.000032739707,0.000009259924],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005364285,0.00058561837,0.00074588857,0.00038889714,0.00031244985,0.00068011734,0.00054545596,0.00046225928,0.0011424925],"category_scores_gemma":[0.0005735745,0.00027374935,0.00040161118,0.000474557,0.00017624164,0.0003222257,0.00029315893,0.00047601986,0.0005408858],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00072449516,0.0001540915,0.000861132,0.00028812967,0.00004766363,0.00011790811,0.000045173867,0.028640753,0.95808184,0.0005841327,0.00033611036,0.010118717],"study_design_scores_gemma":[0.000059393693,0.00046034867,0.0013599603,0.000009121216,0.000051884635,0.00003373684,0.00001776061,0.02888473,0.9669498,0.00008657238,0.0020692253,0.000017490627],"about_ca_topic_score_codex":0.00107775,"about_ca_topic_score_gemma":0.001356374,"teacher_disagreement_score":0.0011424925,"about_ca_system_score_codex":0.00083424884,"about_ca_system_score_gemma":0.00037023306,"threshold_uncertainty_score":0.0060528517},"labels":[],"label_agreement":null},{"id":"W2156306974","doi":"10.1002/ceat.200401821","title":"Radial Particle Profiles in a Liquid‐Solid CFB with Varying Viscosity","year":2004,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":20,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Mechanics; Viscosity; Fluidized bed combustion; Particle (ecology); Flow (mathematics); Range (aeronautics); Materials science; Viscous liquid; Two-phase flow; Thermodynamics; Particle size; Phase (matter); Particle-size distribution; Chemistry; Fluidized bed; Physics; Composite material; Geology","score_opus":0.003695489583164693,"score_gpt":0.1802574891973537,"score_spread":0.17656199961418903,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2156306974","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99540687,0.0001345201,0.0039488734,0.000022981218,0.0000049029613,0.000008890181,0.000054725937,0.00006563794,0.00035269235],"genre_scores_gemma":[0.9975993,0.000048378402,0.0020037082,0.0000086418495,0.000002107754,0.0000068435056,0.000076498065,0.000008668295,0.0002458039],"study_design_codex":"bench_or_experimental","study_design_gemma":"observational","domain_scores_codex":[0.99986994,0.000015448955,0.000006045573,0.000034939294,0.000046289602,0.00002729454],"domain_scores_gemma":[0.9997017,0.00006559999,0.00006580557,0.000015122309,0.00008691224,0.00006495808],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026244693,0.00015017911,0.0002728712,0.00045150987,0.00030709975,0.0005183356,0.00017793539,0.0002626965,0.00034898933],"category_scores_gemma":[0.00039729357,0.00015606194,0.00013325257,0.00025091082,0.0003483616,0.00025901422,0.00014395385,0.0002869017,0.00010816976],"study_design_candidate":"observational","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00032398524,0.00003927273,0.0028821684,0.000022306423,0.0000067845385,0.00008837527,0.000075792705,0.0029380429,0.9888959,0.00036026537,0.00005406406,0.004313126],"study_design_scores_gemma":[0.00005421959,0.00093108247,0.032929808,0.000012045035,0.000030602478,0.00013393383,0.00011938274,0.07615491,0.888405,0.00018545194,0.001004886,0.000038588023],"about_ca_topic_score_codex":0.0030293425,"about_ca_topic_score_gemma":0.0013567253,"teacher_disagreement_score":0.0030293425,"about_ca_system_score_codex":0.0005223896,"about_ca_system_score_gemma":0.00027893158,"threshold_uncertainty_score":0.006023407},"labels":[],"label_agreement":null},{"id":"W2157840128","doi":"10.1002/ceat.201500071","title":"Power Draw and Gas‐Liquid Mass Transfer Characteristics of a Stirred‐Tank Reactor with Draft Tube Configuration","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dow Chemical (Canada)","funders":"Dow Chemical Company","keywords":"Draft tube; Impeller; Continuous stirred-tank reactor; Airlift; Mass transfer; Aeration; Sparging; Bioreactor; Rushton turbine; Turbine; Mixing (physics); Mass transfer coefficient; Mechanics; Tube (container); Mechanical engineering; Nuclear engineering; Chemistry; Engineering; Chemical engineering; Waste management; Chromatography; Physics","score_opus":0.003506691391144615,"score_gpt":0.1653559517743619,"score_spread":0.16184926038321729,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2157840128","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99631363,0.00013522455,0.0027256026,0.000042016967,0.000014880398,0.000014850994,0.00018397029,0.00012103996,0.00044888846],"genre_scores_gemma":[0.9984598,0.00007778155,0.00075546186,0.000007895261,0.0000039149995,0.000012026236,0.0001740068,0.000011058555,0.00049805304],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997875,0.000046511326,0.000017823008,0.000048277074,0.00006595334,0.00003391427],"domain_scores_gemma":[0.9995561,0.00022009521,0.00006242058,0.000023722883,0.000097117925,0.0000405069],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034792846,0.00046077056,0.0003768864,0.00031560447,0.00023496238,0.0004755369,0.00036487068,0.00044446765,0.0015560212],"category_scores_gemma":[0.0005444187,0.00016611225,0.00030478035,0.000344342,0.00028652282,0.0004540836,0.00018686877,0.0004916729,0.00047034284],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.001050316,0.00010904505,0.0009994367,0.000045202378,0.000008496015,0.000068724155,0.00005939123,0.0016644131,0.9923537,0.000059621867,0.00011722648,0.0034643938],"study_design_scores_gemma":[0.00005288283,0.0015699132,0.0052630114,0.00000390816,0.000022362847,0.00004916733,0.000051564428,0.01769004,0.97481966,0.000034031244,0.00042611838,0.000017372195],"about_ca_topic_score_codex":0.0013850181,"about_ca_topic_score_gemma":0.00064115116,"teacher_disagreement_score":0.0015560212,"about_ca_system_score_codex":0.00041493768,"about_ca_system_score_gemma":0.00023386384,"threshold_uncertainty_score":0.005205393},"labels":[],"label_agreement":null},{"id":"W2160209271","doi":"10.1002/ceat.201300285","title":"Kinetic Modeling of Methane Hydrate Formation in the Presence of Low‐Dosage Water‐Soluble Ionic Liquids","year":2013,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Methane Hydrates and Related Phenomena","field":"Environmental Science","cited_by":35,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Hydrate; Isochoric process; Chemistry; Methane; Clathrate hydrate; Nucleation; Dissociation (chemistry); Kinetic energy; Ionic bonding; Inorganic chemistry; Thermodynamics; Physical chemistry; Organic chemistry; Ion","score_opus":0.005322982464248926,"score_gpt":0.18166007134835316,"score_spread":0.17633708888410424,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2160209271","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9516272,0.0003703357,0.04608582,0.000060434602,0.000012077795,0.000028316512,0.00021158523,0.00016775627,0.0014365269],"genre_scores_gemma":[0.9956649,0.00020945728,0.003365829,0.000004178601,0.0000015159414,0.000024726778,0.0001009545,0.000010131691,0.00061821315],"study_design_codex":"bench_or_experimental","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99993,0.000012976441,0.0000058666933,0.000013062698,0.00002392998,0.000014117895],"domain_scores_gemma":[0.9998435,0.000092657436,0.000025396323,0.000009215518,0.00002283646,0.000006383901],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00023499082,0.00032950245,0.00026870792,0.00019890186,0.00010581664,0.00023775108,0.000416674,0.0002656266,0.0005761003],"category_scores_gemma":[0.00037074657,0.00016790854,0.00038194293,0.00015707055,0.00018258391,0.00029091426,0.00012328084,0.00025338965,0.00016216436],"study_design_candidate":"simulation_or_modeling","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0005220505,0.000073098905,0.0033077325,0.00026061147,0.000034741704,0.00013778073,0.000084709965,0.29131725,0.69527465,0.0017365891,0.00008484111,0.007165935],"study_design_scores_gemma":[0.000013029056,0.00009610859,0.000722015,0.0000031885957,0.000011176251,0.000014209585,0.000012025226,0.69007975,0.3086161,0.00009607478,0.00032573918,0.00001058459],"about_ca_topic_score_codex":0.0035355403,"about_ca_topic_score_gemma":0.0017675034,"teacher_disagreement_score":0.0035355403,"about_ca_system_score_codex":0.00048678665,"about_ca_system_score_gemma":0.0002852026,"threshold_uncertainty_score":0.007029891},"labels":[],"label_agreement":null},{"id":"W2163863799","doi":"10.1002/ceat.201300163","title":"Catalytic Ozone Decomposition in a Gas‐Solids Circulating Fluidized‐Bed Riser","year":2014,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":10,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Fluid catalytic cracking; Computational fluid dynamics; Catalysis; Fluidized bed combustion; Reaction rate; Fluidized bed; Decomposition; Particle (ecology); Thermodynamics; Chemistry; Mechanics; Materials science; Chemical engineering; Engineering; Physics; Organic chemistry; Geology","score_opus":0.003345511504958651,"score_gpt":0.1903467755817743,"score_spread":0.18700126407681564,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2163863799","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9801717,0.00020892065,0.017469982,0.000118885444,0.00004113629,0.000036069774,0.000088760455,0.000222815,0.0016418259],"genre_scores_gemma":[0.9950805,0.0000613057,0.0039543738,0.000013003734,0.0000037430616,0.000010457507,0.00006498191,0.000011854045,0.0007997361],"study_design_codex":"simulation_or_modeling","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997656,0.0000417881,0.000009927966,0.00005326613,0.00007743557,0.000052073174],"domain_scores_gemma":[0.99985933,0.00006284354,0.000015092419,0.000012055513,0.000022396722,0.000028176084],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00034494675,0.0005607564,0.0011655393,0.0003020358,0.0006594974,0.000914199,0.00081104203,0.0010405282,0.00080433424],"category_scores_gemma":[0.00045596284,0.0002993622,0.00054831326,0.00023193043,0.00062094646,0.0004982739,0.00042566544,0.00059687527,0.00015869779],"study_design_candidate":"bench_or_experimental","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008284781,0.00046484673,0.0041984166,0.00020759297,0.00004446786,0.0012193924,0.00019670538,0.6694276,0.30419737,0.0036101262,0.0005306565,0.015074312],"study_design_scores_gemma":[0.00010887514,0.0002046196,0.001098314,0.000004176003,0.000012508997,0.000061825165,0.000028528986,0.9565412,0.041300856,0.00020312426,0.00041847702,0.000017458822],"about_ca_topic_score_codex":0.014903003,"about_ca_topic_score_gemma":0.0042350506,"teacher_disagreement_score":0.014903003,"about_ca_system_score_codex":0.001270144,"about_ca_system_score_gemma":0.0010742054,"threshold_uncertainty_score":0.029632509},"labels":[],"label_agreement":null},{"id":"W2164864766","doi":"10.1002/ceat.201000247","title":"Investigations on Azeotropy in Multicomponent Polymerizations","year":2010,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Polymer Synthesis and Characterization","field":"Chemistry","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Waterloo","funders":"","keywords":"Ternary operation; Work (physics); Thermodynamics; Composition (language); Point (geometry); Chemistry; Mathematics; Computer science; Physics; Geometry","score_opus":0.004550496532180656,"score_gpt":0.1991994507937777,"score_spread":0.19464895426159706,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2164864766","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.91669255,0.0026315677,0.069556005,0.00008921346,0.000050714054,0.00009956733,0.00006937728,0.00015259603,0.010658454],"genre_scores_gemma":[0.9740016,0.0008451552,0.023383042,0.0000127213825,0.000009884225,0.000029171122,0.000025991989,0.00002315935,0.0016692576],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99975914,0.000023302035,0.000013614503,0.000049328566,0.00013301945,0.000021627737],"domain_scores_gemma":[0.99965847,0.00019864885,0.000057517223,0.000036198835,0.00003266979,0.000016440503],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045846406,0.0002870059,0.00044410935,0.00049987494,0.00029690273,0.00046540113,0.00028667037,0.00033856105,0.0016196234],"category_scores_gemma":[0.0007865596,0.00017739584,0.00020859907,0.0003518845,0.00052631553,0.000580799,0.0005772251,0.0005874903,0.00034956922],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000103683415,0.000063997984,0.0005036885,0.0002497628,0.000006218134,0.00022249452,0.00015387601,0.008181191,0.97474706,0.0063419156,0.000048352416,0.009377738],"study_design_scores_gemma":[0.000018158324,0.00013617017,0.00088308693,0.000024607278,0.0000099393765,0.00021804635,0.000043421856,0.04719275,0.9474679,0.0017197418,0.002274827,0.000011247675],"about_ca_topic_score_codex":0.00014708564,"about_ca_topic_score_gemma":0.00020847918,"teacher_disagreement_score":0.0016196234,"about_ca_system_score_codex":0.00020067593,"about_ca_system_score_gemma":0.00018516465,"threshold_uncertainty_score":0.005418241},"labels":[],"label_agreement":null},{"id":"W2167097137","doi":"10.1002/ceat.200700011","title":"CFD Simulation of Mass Transfer Efficiency and Pressure Drop in a Structured Packed Distillation Column","year":2007,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Process Optimization and Integration","field":"Engineering","cited_by":53,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Pressure drop; Computational fluid dynamics; Packed bed; Structured packing; Mass transfer; Distillation; Fractionating column; Mechanics; Drop (telecommunication); Chemistry; Theoretical plate; Reactive distillation; Chromatography; Materials science; Thermodynamics; Analytical Chemistry (journal); Mechanical engineering; Engineering; Physics","score_opus":0.0027381673624485227,"score_gpt":0.19165875216788797,"score_spread":0.18892058480543944,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2167097137","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9701076,0.00010164147,0.02447759,0.0001264957,0.000026908712,0.000053169366,0.00027924482,0.00024784612,0.0045793396],"genre_scores_gemma":[0.99353397,0.000047484693,0.0051250495,0.000018563751,0.00000289397,0.00003665311,0.00011691481,0.00001628353,0.0011021738],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998665,0.000019391722,0.0000060849775,0.000021150892,0.000044955166,0.00004188081],"domain_scores_gemma":[0.99949694,0.00033469292,0.000028901557,0.000021179383,0.00008122705,0.000037015256],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026101008,0.00037255368,0.00064472074,0.0003610412,0.00057478563,0.0006584774,0.0005352777,0.0010377587,0.0014321575],"category_scores_gemma":[0.0007129367,0.0003775337,0.00052876986,0.0003126969,0.00062173104,0.00035371043,0.0003020669,0.0004910888,0.00021372121],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000116398856,0.00006241081,0.0014509355,0.00003430423,0.0000108585045,0.00012464276,0.000049715258,0.98173356,0.013656001,0.0006610072,0.00014192534,0.001958271],"study_design_scores_gemma":[0.000015153306,0.00002537999,0.000301667,0.0000018216745,0.0000022821348,0.0000059617614,0.0000067935625,0.99595624,0.0035628397,0.000053156113,0.000064477725,0.0000040576006],"about_ca_topic_score_codex":0.025073167,"about_ca_topic_score_gemma":0.008096858,"teacher_disagreement_score":0.025073167,"about_ca_system_score_codex":0.0011331965,"about_ca_system_score_gemma":0.0013836714,"threshold_uncertainty_score":0.049854457},"labels":[],"label_agreement":null},{"id":"W2171031853","doi":"10.1002/ceat.200700485","title":"Comparative Study of Flow Structure in Circulating Fluidized Bed Risers with FCC and Sand Particles","year":2008,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Granular flow and fluidized beds","field":"Engineering","cited_by":25,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Institute of Engineering Research, Seoul National University; National Natural Science Foundation of China","keywords":"Nozzle; Distributor; Materials science; Flow (mathematics); Particle (ecology); Fluidized bed combustion; Mechanics; Fluidization; Range (aeronautics); Fluidized bed; Composite material; Geology; Thermodynamics; Physics","score_opus":0.0078639940789791,"score_gpt":0.19198348082620903,"score_spread":0.18411948674722994,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2171031853","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9980482,0.000049512142,0.0016038523,0.000006830177,0.0000024773997,0.000007897125,0.000019158628,0.00006193517,0.00020029313],"genre_scores_gemma":[0.9982666,0.000019266776,0.0014042347,0.0000035024686,0.0000013298475,0.000003523666,0.000045301393,0.0000068014424,0.00024937047],"study_design_codex":"bench_or_experimental","study_design_gemma":"observational","domain_scores_codex":[0.99975854,0.00003627348,0.0000139981485,0.000050650408,0.00009310423,0.000047470156],"domain_scores_gemma":[0.99955064,0.0001592694,0.000066982786,0.00002537199,0.00014853045,0.000049185404],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00036814803,0.00021572039,0.00047071872,0.0005274824,0.00031233134,0.00062071625,0.00028500665,0.00027129063,0.0005816574],"category_scores_gemma":[0.00075577496,0.00018805689,0.000263785,0.00027808026,0.00052002707,0.0003030153,0.00014988541,0.00024538446,0.000109773624],"study_design_candidate":"observational","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008263911,0.00012240103,0.012151049,0.00007052233,0.00002021815,0.00038299456,0.00037388408,0.0099023,0.96017826,0.0004680717,0.000075397016,0.015428457],"study_design_scores_gemma":[0.000091922804,0.0009498127,0.07692744,0.000013134456,0.000048333688,0.00025494184,0.00045855666,0.10887739,0.81143427,0.00016872883,0.0007102011,0.0000652199],"about_ca_topic_score_codex":0.0048294812,"about_ca_topic_score_gemma":0.0028023685,"teacher_disagreement_score":0.0048294812,"about_ca_system_score_codex":0.0009253329,"about_ca_system_score_gemma":0.00032873402,"threshold_uncertainty_score":0.0096027255},"labels":[],"label_agreement":null},{"id":"W2172206025","doi":"10.1002/ceat.201100723","title":"Multiscale Aspects of Modeling Gas‐Phase Nanoparticle Synthesis","year":2012,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Coagulation and Flocculation Studies","field":"Environmental Science","cited_by":27,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institute of Particle Physics","funders":"","keywords":"Aerosol; Multiscale modeling; Mesoscale meteorology; Gas phase; Nanoparticle; Scale (ratio); Nanotechnology; Physics; Materials science; Chemistry; Meteorology; Thermodynamics; Computational chemistry","score_opus":0.01241566299235697,"score_gpt":0.22930696979097678,"score_spread":0.21689130679861982,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2172206025","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.1291822,0.008708561,0.8229836,0.002880053,0.0005161359,0.00016154624,0.0007028306,0.00048001183,0.034385048],"genre_scores_gemma":[0.86876583,0.008475133,0.11071361,0.00029807523,0.0005981708,0.00068271963,0.0006054389,0.0002986922,0.009562358],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998047,0.00006224253,0.0000144075875,0.000038876824,0.000054531276,0.000025252271],"domain_scores_gemma":[0.9996486,0.00018345677,0.000052193755,0.000034522156,0.00004693571,0.000034342305],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00041933695,0.0007733808,0.00097217795,0.00041329523,0.0005538339,0.0012453693,0.0012886985,0.0016937185,0.0015464136],"category_scores_gemma":[0.0012716202,0.00055019563,0.0012981318,0.00040964945,0.00092248066,0.0012084616,0.0009719715,0.001068431,0.0002738668],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000021962105,0.000031603482,0.00056840904,0.00014963058,0.000061029357,0.00012547085,0.00008112974,0.91477734,0.0073086033,0.07213807,0.0005197783,0.004217058],"study_design_scores_gemma":[0.0000055676865,0.000009152378,0.0002232511,0.000010572326,0.00000919011,0.000015901182,0.0000068301088,0.985151,0.0003307894,0.0129097225,0.0013206135,0.0000073890815],"about_ca_topic_score_codex":0.008228277,"about_ca_topic_score_gemma":0.0033307532,"teacher_disagreement_score":0.008228277,"about_ca_system_score_codex":0.0012273899,"about_ca_system_score_gemma":0.0007901272,"threshold_uncertainty_score":0.01636076},"labels":[],"label_agreement":null},{"id":"W2252396427","doi":"10.1002/ceat.201500239","title":"Reduced Graphene Oxide Composite of Gallium Zinc Oxynitride Photocatalyst with Improved Activity for Overall Water Splitting","year":2015,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Advanced Photocatalysis Techniques","field":"Energy","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"","keywords":"Graphene; Photocatalysis; Materials science; Composite number; Nanocomposite; Oxide; Chemical engineering; Visible spectrum; Zinc; Water splitting; Gallium; Nanotechnology; Composite material; Optoelectronics; Chemistry; Catalysis; Metallurgy; Organic chemistry","score_opus":0.009417056729163617,"score_gpt":0.22794408778934133,"score_spread":0.2185270310601777,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2252396427","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99582833,0.0008847383,0.0018796261,0.00005010061,0.00003316916,0.000012823732,0.00013359882,0.0000837335,0.001093949],"genre_scores_gemma":[0.9963923,0.0002917153,0.0019109085,0.000014182367,0.00000420302,0.000006395353,0.00015968255,0.00000934163,0.0012113521],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999386,0.0000042311617,0.0000041273015,0.000015177478,0.000024011502,0.000013799787],"domain_scores_gemma":[0.9999759,0.0000025912598,0.0000053259832,0.0000021419778,0.000006812192,0.0000071293935],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00006602677,0.00030435523,0.00015759276,0.0003011218,0.00007918696,0.00016983111,0.00023511182,0.00028190072,0.00060894643],"category_scores_gemma":[0.00007063799,0.00012147758,0.00024643837,0.00018413486,0.000092251896,0.00015568934,0.00012334988,0.000211724,0.00011931427],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000026298936,0.000007229904,0.00004976085,0.000024073956,0.000003742289,0.000021499516,0.0000031766542,0.000056787012,0.9990195,0.000029721468,0.00001669446,0.00074147026],"study_design_scores_gemma":[0.00000887258,0.00007604984,0.0013767972,0.0000021960989,0.000019158433,0.000042993124,0.0000064732612,0.001116429,0.99662375,0.000011689066,0.00071244256,0.0000031354452],"about_ca_topic_score_codex":0.0010816832,"about_ca_topic_score_gemma":0.0032841645,"teacher_disagreement_score":0.0010816832,"about_ca_system_score_codex":0.00019508546,"about_ca_system_score_gemma":0.00011278512,"threshold_uncertainty_score":0.0021508336},"labels":[],"label_agreement":null},{"id":"W2271320187","doi":"10.1002/ceat.201400433","title":"Multivariate Modeling of a Chemical Toner Manufacturing Process","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fault Detection and Control Systems","field":"Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Guelph; University of Waterloo","funders":"","keywords":"Principal component analysis; Process (computing); Multivariate statistics; Latent variable; Process engineering; Process control; Computer science; Process modeling; Partial least squares regression; Identification (biology); Product (mathematics); Matrix (chemical analysis); Batch processing; Process analytical technology; Unit operation; Process optimization; Work in process; Engineering; Artificial intelligence; Machine learning; Mathematics; Chemistry; Chromatography","score_opus":0.004886595472889019,"score_gpt":0.19683285257243802,"score_spread":0.191946257099549,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2271320187","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.38213417,0.00016027807,0.6140125,0.00022070584,0.000027287173,0.00007813743,0.0003215569,0.0007936958,0.0022516516],"genre_scores_gemma":[0.98156667,0.000105308616,0.016285548,0.000015787866,0.000010431033,0.000056207835,0.00014868495,0.000034275312,0.0017772135],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9995696,0.00013746165,0.000016499196,0.00011260368,0.0001128051,0.0000510607],"domain_scores_gemma":[0.9994435,0.00031037035,0.00009782223,0.000045519333,0.00008291747,0.000019940846],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00083329703,0.0006186739,0.0005900737,0.00043680967,0.00035046198,0.0008188339,0.0005725897,0.0005201795,0.0011407738],"category_scores_gemma":[0.0011473169,0.0002818416,0.0006993102,0.00044086546,0.00040469266,0.00040165655,0.00036168573,0.00070126425,0.00018230766],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000061409344,0.00005664825,0.0011141498,0.000022146103,0.000023411481,0.00004788566,0.000027217115,0.98677397,0.0045351875,0.0014679238,0.00009038019,0.0057795737],"study_design_scores_gemma":[0.0000012810547,0.0000136249855,0.00028149883,3.589079e-7,0.0000019299935,0.0000028892148,0.0000015405354,0.9991997,0.00034348943,0.00011316098,0.000038259586,0.0000022420002],"about_ca_topic_score_codex":0.010908978,"about_ca_topic_score_gemma":0.004322691,"teacher_disagreement_score":0.010908978,"about_ca_system_score_codex":0.000650752,"about_ca_system_score_gemma":0.0006901319,"threshold_uncertainty_score":0.021690965},"labels":[],"label_agreement":null},{"id":"W2290772979","doi":"10.1002/ceat.201500331","title":"Benchmarking of Gas‐Assisted Atomization Systems for Liquid Disintegration","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Heat Transfer","field":"Engineering","cited_by":7,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Institute of Particle Physics","funders":"Ministerium für Wissenschaft, Forschung und Kunst Baden-Württemberg; Deutsche Forschungsgemeinschaft; Karlsruhe Institute of Technology","keywords":"Mixing (physics); Chemistry; Superheating; Polymer; Drop (telecommunication); Pressure drop; Nozzle; Analytical Chemistry (journal); Chromatography; Thermodynamics; Mechanical engineering; Organic chemistry; Engineering; Physics","score_opus":0.004666267439277547,"score_gpt":0.18032156508330308,"score_spread":0.17565529764402554,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2290772979","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9925942,0.00063822046,0.005514519,0.000030770658,0.000020962843,0.000102392354,0.000105828076,0.00019302755,0.00080010557],"genre_scores_gemma":[0.9867489,0.0006640091,0.011200507,0.00001480176,0.000011267857,0.000084711224,0.00020103122,0.000051582818,0.001023259],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9995994,0.00006727633,0.00002994622,0.00007481556,0.00016098401,0.0000676842],"domain_scores_gemma":[0.99968934,0.000108684144,0.000057696565,0.000041176463,0.00007702187,0.000026152667],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00045737176,0.00057796255,0.00040879316,0.00042869488,0.00025026716,0.00043591345,0.00058313005,0.0003941106,0.001783257],"category_scores_gemma":[0.00075596804,0.00022788353,0.00021431848,0.0002733206,0.00030461096,0.00044818933,0.0004812906,0.00036045807,0.00028289907],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00050691626,0.000095989286,0.00039874084,0.0001285573,0.000019915646,0.000039130362,0.000058943708,0.0010699346,0.9896175,0.0000967212,0.000070800415,0.007896753],"study_design_scores_gemma":[0.000020068792,0.00066081656,0.00092597975,0.0000029527428,0.000015714963,0.000024673453,0.000015326497,0.0029692806,0.9944846,0.000008492962,0.000863761,0.000008261609],"about_ca_topic_score_codex":0.00061970163,"about_ca_topic_score_gemma":0.0008284347,"teacher_disagreement_score":0.001783257,"about_ca_system_score_codex":0.00038110116,"about_ca_system_score_gemma":0.00025838503,"threshold_uncertainty_score":0.0059655905},"labels":[],"label_agreement":null},{"id":"W2301885296","doi":"10.1002/ceat.201500639","title":"Palladium Supported on Carbon Nanotubes for Methane Catalytic Oxidation","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalytic Processes in Materials Science","field":"Materials Science","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"National Natural Science Foundation of China; Ontario Council on Graduate Studies, Council of Ontario Universities","keywords":"Catalysis; Carbon nanotube; Palladium; Methane; Dispersion (optics); Anaerobic oxidation of methane; Chemical engineering; Redox; Carbon fibers; Oxygen; Materials science; Inorganic chemistry; Chemistry; Nanotechnology; Composite material; Organic chemistry; Composite number","score_opus":0.00844343522624913,"score_gpt":0.22674272384290017,"score_spread":0.21829928861665104,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2301885296","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9822197,0.004584036,0.008771037,0.0001698101,0.00012124558,0.00005407029,0.00021384134,0.0001790947,0.0036872227],"genre_scores_gemma":[0.99060154,0.0016101336,0.005240958,0.00003340655,0.000014389012,0.00001947918,0.00018194024,0.000023493418,0.0022746283],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99985194,0.000019498013,0.000011932054,0.000024733201,0.000070591566,0.000021286813],"domain_scores_gemma":[0.99993694,0.000013051979,0.000011454271,0.000006452368,0.00002033877,0.000011778084],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012031773,0.0003245596,0.00021205473,0.00047307083,0.00016335501,0.00020188696,0.00032949523,0.00035137864,0.00066047296],"category_scores_gemma":[0.00023418649,0.00017552653,0.0001852494,0.0002197689,0.000108096145,0.0002011819,0.00019994062,0.00028271787,0.00032867325],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000043293,0.00002069083,0.00006701611,0.000078841316,0.0000070459128,0.000043649277,0.0000068328263,0.00025445677,0.99601597,0.000095591255,0.00006905631,0.0032975068],"study_design_scores_gemma":[0.000006081835,0.000079578684,0.0003322467,0.000004447063,0.000010468029,0.000039850423,0.000003945779,0.001194715,0.9968135,0.000023574887,0.0014891336,0.0000025103388],"about_ca_topic_score_codex":0.00046018237,"about_ca_topic_score_gemma":0.0011568399,"teacher_disagreement_score":0.00066047296,"about_ca_system_score_codex":0.00024896226,"about_ca_system_score_gemma":0.00010958525,"threshold_uncertainty_score":0.0022095442},"labels":[],"label_agreement":null},{"id":"W2319420829","doi":"10.1002/ceat.201500413","title":"Feedstock Characterization and Suitability Assessment for Dry Anaerobic Batch Digestion","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Anaerobic Digestion and Biogas Production","field":"Engineering","cited_by":12,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Alberta Innovates","funders":"Alberta Innovates; Alberta Innovates - Technology Futures","keywords":"Raw material; Anaerobic digestion; Straw; Materials science; Porosity; Permeability (electromagnetism); Bulk density; Biogas; Pulp and paper industry; Waste management; Chemical engineering; Chemistry; Environmental science; Composite material; Methane; Soil water","score_opus":0.005010878873358979,"score_gpt":0.20271319513849562,"score_spread":0.19770231626513662,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2319420829","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99329007,0.00025587677,0.004281361,0.000023366656,0.0000087799035,0.00012245834,0.0007837247,0.000045179753,0.0011891428],"genre_scores_gemma":[0.9903999,0.0003939476,0.0073796036,0.000020993562,0.000004356204,0.00011504757,0.0007465033,0.000027676826,0.00091208145],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9995871,0.00006517793,0.000056561556,0.00007346814,0.00017401314,0.00004369734],"domain_scores_gemma":[0.9997501,0.0000607408,0.000041925243,0.000026867183,0.0000963894,0.000023966963],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0005405559,0.00046155747,0.00046858753,0.0005605096,0.00034100492,0.0006801258,0.0003090491,0.00036852006,0.00085818843],"category_scores_gemma":[0.0007710599,0.00017912222,0.00027611156,0.0005867464,0.00021596425,0.00040756146,0.00024775317,0.00033034038,0.0003258382],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033604205,0.00007144894,0.0013157884,0.000098428085,0.000006941517,0.000058297086,0.00001417499,0.00054465036,0.99410146,0.000020165407,0.000025965743,0.003406538],"study_design_scores_gemma":[0.000014772888,0.0005310597,0.0099992165,0.000010849467,0.000022581286,0.00008510442,0.00006360558,0.0019461942,0.9865849,0.00002297209,0.00070877076,0.0000099252575],"about_ca_topic_score_codex":0.0024205763,"about_ca_topic_score_gemma":0.0050711273,"teacher_disagreement_score":0.0024205763,"about_ca_system_score_codex":0.00043622145,"about_ca_system_score_gemma":0.00036958008,"threshold_uncertainty_score":0.0048130155},"labels":[],"label_agreement":null},{"id":"W2322672973","doi":"10.1002/ceat.201500622","title":"Fabrication of Chitosan Membranes with High Flux by Magnetic Alignment of In Situ Generated Fe<sub>3</sub>O<sub>4</sub>","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Membrane Separation and Gas Transport","field":"Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"National Science Fund for Distinguished Young Scholars; Project 211; National Natural Science Foundation of China","keywords":"Pervaporation; Membrane; Crystallinity; Magnetic field; Chitosan; Materials science; Fabrication; In situ; Dehydration; Chemical engineering; Glutaraldehyde; Ion; Analytical Chemistry (journal); Characterization (materials science); Magnetic flux; Flux (metallurgy); Chemistry; Nanotechnology; Chromatography; Composite material; Organic chemistry; Physics","score_opus":0.003299777480160708,"score_gpt":0.1660022924359328,"score_spread":0.1627025149557721,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2322672973","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9589152,0.0010054208,0.03516825,0.00031786365,0.00010799822,0.000102802805,0.00034224163,0.00034932906,0.0036909578],"genre_scores_gemma":[0.9523224,0.00078100804,0.04249334,0.00011115145,0.000024484449,0.000063456784,0.00020514346,0.000056746518,0.003942259],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99991965,0.000006929738,0.000006615846,0.000016539496,0.00003435919,0.000015847116],"domain_scores_gemma":[0.9998847,0.0000131402685,0.000038790313,0.000009065026,0.000037871214,0.000016378473],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013785785,0.00054062007,0.00021188777,0.00024210445,0.00023177743,0.00023821351,0.00026442637,0.0005670768,0.00059079315],"category_scores_gemma":[0.00015966724,0.00021580183,0.00031135706,0.00023891978,0.00018744661,0.00039651585,0.0002343136,0.0003376194,0.00024950595],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000011441094,0.000003710382,0.000025069514,0.000021416301,0.0000031044005,0.000019714855,0.0000053046024,0.000052306637,0.9991991,0.000051871877,0.000031132997,0.0005759102],"study_design_scores_gemma":[0.000008573822,0.000029950705,0.00051641936,0.000001989385,0.000009189889,0.00005292165,0.000008483702,0.0006392458,0.99767274,0.000015077147,0.0010398772,0.0000055122327],"about_ca_topic_score_codex":0.0019594997,"about_ca_topic_score_gemma":0.0032271806,"teacher_disagreement_score":0.0019594997,"about_ca_system_score_codex":0.00053759426,"about_ca_system_score_gemma":0.0003012013,"threshold_uncertainty_score":0.003900528},"labels":[],"label_agreement":null},{"id":"W2508574426","doi":"10.1002/ceat.201600046","title":"Mechanochemical Synthesis of CPM‐5: A Green Method","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Corrosion Behavior and Inhibition","field":"Materials Science","cited_by":18,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University; University of Northern British Columbia; Concordia University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Grinding; Materials science; Porosity; Dimethylformamide; Chemical engineering; Specific surface area; Oscillation (cell signaling); Process engineering; Metallurgy; Composite material; Solvent; Chemistry; Organic chemistry; Catalysis; Engineering","score_opus":0.007232890294206916,"score_gpt":0.2283116175057485,"score_spread":0.22107872721154156,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2508574426","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.91723406,0.0057818107,0.064083755,0.00023300275,0.00022871433,0.00016723189,0.00045278802,0.00031504745,0.0115035875],"genre_scores_gemma":[0.97648823,0.00084427244,0.02057861,0.000048794027,0.000011908737,0.000039942966,0.00016664203,0.000012898538,0.0018086699],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998895,0.000011056703,0.000005633151,0.000019414114,0.000048123544,0.000026246362],"domain_scores_gemma":[0.9999583,0.0000062352,0.00001175856,0.000004672622,0.000010000987,0.000008987512],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010605584,0.00023794541,0.00015883463,0.0002159451,0.00010912925,0.000107895015,0.00022098867,0.00028494524,0.0008558362],"category_scores_gemma":[0.00012461081,0.00009991317,0.00018733082,0.00016967572,0.00013386832,0.000128522,0.00017820299,0.00031195756,0.00025349547],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000010449635,0.000013142539,0.000062627296,0.00011283163,0.000004270226,0.000056515466,0.00000822814,0.00017278778,0.99514633,0.00043181505,0.000074829426,0.003906127],"study_design_scores_gemma":[0.0000034799227,0.00013367677,0.00069250044,0.000008015919,0.000005235414,0.000117429656,0.000006676308,0.0006234183,0.994321,0.00006117863,0.0040222136,0.000005263519],"about_ca_topic_score_codex":0.00039924032,"about_ca_topic_score_gemma":0.0011119642,"teacher_disagreement_score":0.0008558362,"about_ca_system_score_codex":0.00017642135,"about_ca_system_score_gemma":0.00023875764,"threshold_uncertainty_score":0.0028630495},"labels":[],"label_agreement":null},{"id":"W2521080280","doi":"10.1002/ceat.201600380","title":"Ultrasound‐Assisted Synthesis of Cu and Cu/Ni Nanoparticles on NaP Zeolite Support as Antibacterial Agents","year":2016,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Nanoparticles: synthesis and applications","field":"Materials Science","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Northern British Columbia","funders":"","keywords":"Antibacterial activity; Ethylene glycol; Bacillus subtilis; Nanoparticle; Nuclear chemistry; Zeolite; PEG ratio; Chemistry; Materials science; Metal; Substrate (aquarium); Central composite design; Response surface methodology; Nanotechnology; Chromatography; Bacteria; Catalysis; Organic chemistry","score_opus":0.009014190838229772,"score_gpt":0.2229141783850488,"score_spread":0.21389998754681902,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2521080280","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9941736,0.00074404746,0.003458466,0.000021795688,0.00002090868,0.000029378516,0.00011014733,0.0000859362,0.0013558022],"genre_scores_gemma":[0.9935794,0.00036133768,0.004604238,0.00000922614,0.0000060046173,0.00003250005,0.00012518259,0.000017443437,0.0012646321],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999081,0.0000123226455,0.000009738826,0.00001606638,0.000033179193,0.000020559113],"domain_scores_gemma":[0.999931,0.000012861589,0.00001757173,0.000006793034,0.000018991344,0.000012902377],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00011705276,0.0002380682,0.00022921259,0.0001960981,0.00010424663,0.00017121936,0.00021646167,0.00023241344,0.00052959635],"category_scores_gemma":[0.0001706066,0.00016825955,0.0001760651,0.00013683358,0.00011425348,0.00013894966,0.00014194309,0.00016895954,0.00020993793],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000035928704,0.000005564919,0.00002616605,0.00003885616,0.0000020022362,0.00001871284,0.000007597882,0.0000747525,0.9989349,0.000028562317,0.000011385655,0.000815521],"study_design_scores_gemma":[0.000006730097,0.00008278623,0.00053891324,0.0000028998447,0.000006202587,0.00002282885,0.00000812938,0.0009822075,0.99764085,0.000009023247,0.0006964501,0.0000029851697],"about_ca_topic_score_codex":0.0007317425,"about_ca_topic_score_gemma":0.00149988,"teacher_disagreement_score":0.0007317425,"about_ca_system_score_codex":0.00016931693,"about_ca_system_score_gemma":0.0001385953,"threshold_uncertainty_score":0.0017716289},"labels":[],"label_agreement":null},{"id":"W2604530422","doi":"10.1002/ceat.201600725","title":"Influence of Solution Composition and Temperature on the Crystal Form of Sodium Dehydroacetate","year":2017,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Crystallization and Solubility Studies","field":"Materials Science","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Supersaturation; Hydrate; Chemistry; Solubility; Solvent; Sodium; Methanol; Slurry; Aqueous solution; Composition (language); Water content; Inorganic chemistry; Chemical engineering; Thermodynamics; Organic chemistry; Geology","score_opus":0.0074123791805556765,"score_gpt":0.2165863843995245,"score_spread":0.2091740052189688,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2604530422","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9958553,0.0007711273,0.0012104851,0.0000442853,0.000023401859,0.00004504941,0.0001770642,0.000029011342,0.0018443792],"genre_scores_gemma":[0.9973072,0.0005218951,0.0012043933,0.000024415669,0.0000072967,0.000024137682,0.000120881596,0.000027603824,0.00076230493],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997937,0.00004242692,0.0000230654,0.000047261863,0.000061024537,0.000032523734],"domain_scores_gemma":[0.999655,0.00015600924,0.00005351394,0.000015300437,0.000091670074,0.000028502931],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00027945088,0.00026254202,0.00035912945,0.00017515186,0.0001477814,0.0003106564,0.00020096221,0.00018632381,0.0014384887],"category_scores_gemma":[0.0007676921,0.0002065345,0.00017558293,0.00021206646,0.00025556455,0.00025571688,0.00015290825,0.0003676318,0.00024988304],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00017174853,0.000013472014,0.00028758214,0.00005724637,0.0000074803206,0.00003112992,0.00003563142,0.00011142611,0.99819654,0.000034196866,0.000014580034,0.0010389944],"study_design_scores_gemma":[0.0000074643467,0.00017402004,0.0011922375,0.0000033568363,0.0000095874,0.000020161984,0.000019913696,0.00048707018,0.99769825,0.000009254337,0.0003752898,0.0000032939095],"about_ca_topic_score_codex":0.0014111404,"about_ca_topic_score_gemma":0.0019264303,"teacher_disagreement_score":0.0014384887,"about_ca_system_score_codex":0.00021032021,"about_ca_system_score_gemma":0.00030334422,"threshold_uncertainty_score":0.0048122406},"labels":[],"label_agreement":null},{"id":"W2605618526","doi":"10.1002/ceat.201700073","title":"Offshore Floating Packed‐Bed Reactors: Key Challenges and Potential Solutions","year":2017,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Heat and Mass Transfer in Porous Media","field":"Engineering","cited_by":17,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Helmholtz-Zentrum Dresden-Rossendorf; Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Packed bed; Pressure drop; Saturation (graph theory); Mechanics; Submarine pipeline; Porous medium; Porosity; Materials science; Geology; Chemistry; Geotechnical engineering; Chromatography; Physics","score_opus":0.01463524881793739,"score_gpt":0.20587701271439496,"score_spread":0.19124176389645756,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2605618526","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.20426731,0.42839098,0.24132809,0.086897545,0.002889301,0.00035819627,0.0007179221,0.0009175063,0.0342332],"genre_scores_gemma":[0.5321865,0.27394533,0.17209408,0.0026615108,0.0017679802,0.00044601425,0.00090273155,0.000080442165,0.015915355],"study_design_codex":"design_other","study_design_gemma":"theoretical_or_conceptual","domain_scores_codex":[0.9996314,0.00008386288,0.000018983013,0.000074420735,0.00011104783,0.00008029582],"domain_scores_gemma":[0.99948716,0.00014852599,0.000065629894,0.00003865637,0.00016116824,0.00009874036],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0016686791,0.00058552966,0.0007871872,0.0003589229,0.0005412563,0.0022252866,0.0015962077,0.00208522,0.0047015734],"category_scores_gemma":[0.00095562905,0.00030840363,0.00043870858,0.0005601101,0.00096031075,0.002498738,0.0012147432,0.0013383593,0.001363541],"study_design_candidate":"theoretical_or_conceptual","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00055427686,0.0008828532,0.0034085372,0.0078051225,0.00018077693,0.001994009,0.00039078883,0.044406053,0.11930377,0.058796503,0.027352909,0.7349243],"study_design_scores_gemma":[0.00032997946,0.0057933144,0.0066931793,0.0028740726,0.00028074186,0.002832056,0.009395473,0.13526984,0.11656604,0.14530644,0.57428616,0.00037269143],"about_ca_topic_score_codex":0.0009231006,"about_ca_topic_score_gemma":0.0019456752,"teacher_disagreement_score":0.0047015734,"about_ca_system_score_codex":0.00056890736,"about_ca_system_score_gemma":0.0017179749,"threshold_uncertainty_score":0.015728354},"labels":[],"label_agreement":null},{"id":"W2737217315","doi":"10.1002/ceat.201600523","title":"Analysis of In Situ Microscopy Images of Flocculated Sediment Volumes","year":2017,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Minerals Flotation and Separation Techniques","field":"Environmental Science","cited_by":21,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of British Columbia","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Fractal dimension; Flocculation; Materials science; Settling; In situ; Biological system; Fractal; Chemical engineering; Chemistry; Mathematics; Engineering; Environmental engineering","score_opus":0.004997218059088055,"score_gpt":0.24835490472522345,"score_spread":0.2433576866661354,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2737217315","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9644822,0.000397423,0.0325647,0.000038479684,0.00003860447,0.000052801995,0.0006274535,0.00035567363,0.0014426257],"genre_scores_gemma":[0.97175276,0.00026071997,0.025722388,0.00003753714,0.000022461056,0.000053058066,0.00037930644,0.00006961726,0.0017020472],"study_design_codex":"bench_or_experimental","study_design_gemma":"observational","domain_scores_codex":[0.99992585,0.0000055769137,0.0000047241947,0.000019974877,0.000030332796,0.000013566403],"domain_scores_gemma":[0.99973696,0.00007390349,0.00005357772,0.00001917703,0.00008832487,0.00002801937],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014541554,0.00020985928,0.00014645781,0.0008468457,0.0001816445,0.00023239858,0.00018805922,0.00022450605,0.0009107379],"category_scores_gemma":[0.00022899675,0.000118701115,0.0001272637,0.0003244436,0.00014845436,0.00019213533,0.00011574582,0.000364359,0.00015404196],"study_design_candidate":"observational","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000035469446,0.000011118229,0.0006139402,0.000024385023,0.0000046334676,0.00003426083,0.00003396485,0.00012448388,0.99674255,0.000037155078,0.000029118857,0.0023088523],"study_design_scores_gemma":[0.0000072446446,0.00015524088,0.04866353,0.000007602902,0.00002925437,0.00023404288,0.0001315693,0.008424993,0.94149846,0.000065852335,0.0007691701,0.000013020802],"about_ca_topic_score_codex":0.0011028921,"about_ca_topic_score_gemma":0.0016452569,"teacher_disagreement_score":0.0011028921,"about_ca_system_score_codex":0.00024118679,"about_ca_system_score_gemma":0.00010893908,"threshold_uncertainty_score":0.0030466914},"labels":[],"label_agreement":null},{"id":"W2749982975","doi":"10.1002/ceat.201700138","title":"Esterification of Palm Fatty Acid Distillate Using a Sulfonated Mesoporous CuO‐ZnO Mixed Metal Oxide Catalyst","year":2017,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Biodiesel Production and Applications","field":"Engineering","cited_by":33,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Institute of Population and Public Health; King Saud University","keywords":"Catalysis; Mesoporous material; Methanol; Chemistry; Chemical engineering; Oxide; Mixed oxide; Materials science; Nuclear chemistry; Organic chemistry","score_opus":0.01505067864594122,"score_gpt":0.2250887494660422,"score_spread":0.21003807082010098,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2749982975","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99165,0.0010761352,0.0053390884,0.000047309437,0.000033234708,0.000016135047,0.00017886248,0.00011409944,0.0015451721],"genre_scores_gemma":[0.9947332,0.00041321744,0.0036883517,0.00000834512,0.0000052297632,0.000005932884,0.00012300111,0.000015743464,0.0010069689],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999056,0.000005535592,0.000009095386,0.000026221016,0.000031642972,0.000022000184],"domain_scores_gemma":[0.9999584,0.0000058458772,0.000010750573,0.0000031497189,0.000009806149,0.0000120686955],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00009462445,0.00026852454,0.00023463731,0.00022868802,0.00009098502,0.00020138765,0.00019282226,0.0001661015,0.00047986343],"category_scores_gemma":[0.00012631055,0.00013962876,0.00023287439,0.00017282994,0.00009585438,0.00024256263,0.00015005101,0.00017506453,0.00018274868],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000036593796,0.0000073989313,0.00010147481,0.000025134412,0.0000034892464,0.00003073102,0.000004649124,0.00011916561,0.99857414,0.000043057546,0.000016723372,0.0010375008],"study_design_scores_gemma":[0.0000062916447,0.00003962719,0.00078871835,0.0000022086172,0.00000846669,0.000044012013,0.0000057415755,0.0018823633,0.99668854,0.000012444455,0.0005188843,0.0000027727003],"about_ca_topic_score_codex":0.0024432403,"about_ca_topic_score_gemma":0.0046828804,"teacher_disagreement_score":0.0024432403,"about_ca_system_score_codex":0.00031912752,"about_ca_system_score_gemma":0.0001836672,"threshold_uncertainty_score":0.0048580766},"labels":[],"label_agreement":null},{"id":"W2790714629","doi":"10.1002/ceat.201700613","title":"Cyanidation of Gold Associated with Silver Minerals in Sulfide Mineral Matrices","year":2018,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Metal Extraction and Bioleaching","field":"Engineering","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université Laval","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Stibnite; Gold cyanidation; Dissolution; Sulfide minerals; Pyrite; Chemistry; Mineral; Sphalerite; Sulfide; Galena; Inorganic chemistry; Mineralogy; Cyanide","score_opus":0.005845644898047179,"score_gpt":0.1981233054147384,"score_spread":0.19227766051669123,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2790714629","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99696034,0.00014772554,0.0016293944,0.000019359883,0.000008252342,0.000012271704,0.00004122977,0.000026792264,0.0011545689],"genre_scores_gemma":[0.9915685,0.0002421939,0.0042744773,0.000014588689,0.0000036361457,0.000011603331,0.000118520235,0.00002292465,0.003743639],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99989855,0.000018286699,0.0000063191355,0.000024102836,0.00003370175,0.000019040364],"domain_scores_gemma":[0.99991274,0.000022774424,0.00001485686,0.0000076752385,0.00002897254,0.000012899975],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00021751372,0.0002691415,0.0001677084,0.00016590649,0.00017553607,0.00021253912,0.0001668474,0.00014400162,0.00082217436],"category_scores_gemma":[0.0002417527,0.00018784398,0.00011019775,0.00012978865,0.00015879588,0.00016293873,0.0002335492,0.00020742751,0.0002436295],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00003673445,0.0000026361927,0.00009409644,0.000015374466,0.0000017599558,0.000016439713,0.00001755613,0.000040957344,0.99921393,0.000021199834,0.000009611045,0.0005297548],"study_design_scores_gemma":[0.0000016875485,0.000045500175,0.00033810042,0.0000014267862,0.000001811686,0.000014993267,0.0000090679905,0.00027511574,0.99911433,0.000005066807,0.00019199746,9.415222e-7],"about_ca_topic_score_codex":0.0014966939,"about_ca_topic_score_gemma":0.0046602874,"teacher_disagreement_score":0.0014966939,"about_ca_system_score_codex":0.0002764996,"about_ca_system_score_gemma":0.0002199171,"threshold_uncertainty_score":0.0029759407},"labels":[],"label_agreement":null},{"id":"W2804110560","doi":"10.1002/ceat.201700341","title":"Transient Energy and Exergy Analyses of a Multistage Hydrogen Compression and Storage System","year":2018,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Refrigeration and Air Conditioning Technologies","field":"Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Gas compressor; Exergy; Transient (computer programming); Hydrogen storage; Compression (physics); Compression ratio; Solver; Overall pressure ratio; Nuclear engineering; Process engineering; Energy storage; Thermodynamics; Hydrogen; Mechanical engineering; Engineering; Computer science; Chemistry; Mathematics; Physics; Mathematical optimization","score_opus":0.008604070285187311,"score_gpt":0.21751254104834758,"score_spread":0.20890847076316027,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2804110560","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.97094774,0.0001410327,0.024459604,0.00006263429,0.000011874166,0.00005213375,0.00022699751,0.0003265611,0.0037713288],"genre_scores_gemma":[0.99853504,0.000018669065,0.00076930114,0.0000028051377,7.372395e-7,0.000012149769,0.000053336254,0.0000070023825,0.00060105586],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99992025,0.000013744529,0.0000053429526,0.000012511314,0.00003275766,0.000015296382],"domain_scores_gemma":[0.99990535,0.00005052545,0.000008515525,0.000009355266,0.000018135848,0.000008209788],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00016312355,0.0002969667,0.0005187211,0.00038721523,0.00039278864,0.00037942163,0.00035410468,0.00032574128,0.002235315],"category_scores_gemma":[0.0002328919,0.00017505302,0.00033623242,0.00026387154,0.0003364487,0.0004083235,0.00028507566,0.00025489632,0.00016865018],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0008336318,0.00020515361,0.0052991672,0.00025545017,0.00006649782,0.00074910006,0.00018741172,0.73655415,0.23319389,0.0025626367,0.00045050005,0.019642405],"study_design_scores_gemma":[0.000033028587,0.00027947812,0.0031718605,0.0000049487226,0.000015169514,0.000050566057,0.000048071073,0.947924,0.04767079,0.00033237418,0.00045630056,0.000013405472],"about_ca_topic_score_codex":0.004549704,"about_ca_topic_score_gemma":0.002328685,"teacher_disagreement_score":0.004549704,"about_ca_system_score_codex":0.0006202778,"about_ca_system_score_gemma":0.0004149774,"threshold_uncertainty_score":0.009046435},"labels":[],"label_agreement":null},{"id":"W2883196275","doi":"10.1002/ceat.201700489","title":"Tertiary Amine‐Naphthenic Acid Self‐Assembled Surfactants for Viscosity Reduction of Crude Oil","year":2018,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":13,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Agriculture","funders":"National Natural Science Foundation of China","keywords":"Naphthenic acid; Emulsion; Chemistry; Crude oil; Pulmonary surfactant; Viscosity; Enhanced oil recovery; Light crude oil; Amine gas treating; Organic chemistry; Chromatography; Chemical engineering; Petroleum engineering; Materials science; Corrosion; Geology","score_opus":0.005077579715696306,"score_gpt":0.21637473937086235,"score_spread":0.21129715965516604,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2883196275","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95233285,0.004474707,0.0392738,0.00017709915,0.000120861565,0.000108047294,0.000113281414,0.0003047008,0.0030946787],"genre_scores_gemma":[0.9731013,0.0017396982,0.020199716,0.000042928008,0.000015537013,0.00005677061,0.00012076335,0.000036039066,0.0046872664],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998934,0.000015274982,0.000011651166,0.000017255816,0.000045454304,0.000016905056],"domain_scores_gemma":[0.999926,0.000010669049,0.000020649673,0.0000050569565,0.000022045746,0.000015675292],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018759948,0.00029010995,0.00016638094,0.00022686181,0.00012609176,0.00014663681,0.0002188954,0.00021224265,0.0006823384],"category_scores_gemma":[0.00015716073,0.00017076447,0.00018713714,0.00014612025,0.00009083322,0.00022296651,0.00017939006,0.00029637048,0.00026560912],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000012464813,0.000011672347,0.000014458346,0.000023572517,0.0000020764526,0.0000115468165,0.0000058040005,0.000051779356,0.998719,0.000053366282,0.000019680929,0.001074652],"study_design_scores_gemma":[0.0000056539734,0.000053764175,0.000118133794,0.0000014469499,0.0000048482634,0.000012137494,0.0000022586464,0.0011377096,0.99802303,0.000008573513,0.0006308748,0.0000014814244],"about_ca_topic_score_codex":0.0006014211,"about_ca_topic_score_gemma":0.001351218,"teacher_disagreement_score":0.0006823384,"about_ca_system_score_codex":0.00021561858,"about_ca_system_score_gemma":0.00018259679,"threshold_uncertainty_score":0.0022826195},"labels":[],"label_agreement":null},{"id":"W2884044775","doi":"10.1002/ceat.201800184","title":"Temperature Effects on Concentration Polarization Thickness in Thin‐Film Composite Reverse Osmosis Membranes","year":2018,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Membrane Separation Technologies","field":"Environmental Science","cited_by":6,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Ottawa","funders":"","keywords":"Membrane; Thin-film composite membrane; Reverse osmosis; Concentration polarization; Polyamide; Forward osmosis; Osmotic power; Pressure-retarded osmosis; Chemical engineering; Permeation; Materials science; Composite number; Chromatography; Chemistry; Composite material; Engineering","score_opus":0.003464131477589345,"score_gpt":0.19718848636982597,"score_spread":0.19372435489223663,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2884044775","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9973889,0.0005848482,0.0013974383,0.000024870713,0.000014998766,0.000009779309,0.0000610545,0.00003058336,0.00048746882],"genre_scores_gemma":[0.99805045,0.0003695328,0.0011665241,0.000013527432,0.000004001261,0.000009033911,0.000035741774,0.000015151103,0.00033599528],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9996842,0.00006166868,0.000026320826,0.000060371825,0.000120134726,0.000047338966],"domain_scores_gemma":[0.9990742,0.00040876746,0.00020864593,0.000049433795,0.000219074,0.000039845614],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00046869696,0.00026989105,0.00029028868,0.00016349807,0.0001792707,0.00046915602,0.0002005931,0.00031041514,0.00062959024],"category_scores_gemma":[0.00093843247,0.00036890147,0.00029236765,0.00015951521,0.00023993428,0.00043553798,0.00016137245,0.0005029251,0.00018969372],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007808328,0.0000092007085,0.00020367248,0.000026518705,0.0000062480826,0.000022789676,0.00002305018,0.00021742216,0.9988348,0.000013154593,0.0000081939625,0.0005569381],"study_design_scores_gemma":[0.0000031842553,0.000081773695,0.0012420038,0.0000022347315,0.000007786334,0.000018449431,0.000013536899,0.000753903,0.9977665,0.000003837273,0.000103807695,0.0000029669286],"about_ca_topic_score_codex":0.0006538691,"about_ca_topic_score_gemma":0.00056880084,"teacher_disagreement_score":0.0006538691,"about_ca_system_score_codex":0.00028993186,"about_ca_system_score_gemma":0.00015801573,"threshold_uncertainty_score":0.0024787784},"labels":[],"label_agreement":null},{"id":"W2903808278","doi":"10.1002/ceat.201800260","title":"Performance Characteristics of a Suspended‐Catalyst Oscillatory Membrane Photocatalytic Reactor","year":2018,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Solar-Powered Water Purification Methods","field":"Energy","cited_by":4,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Catalysis; Membrane; Membrane reactor; Filtration (mathematics); Chemical engineering; Photocatalysis; Sedimentation; Materials science; Suspension (topology); Mixing (physics); Reaction rate; Chemistry; Organic chemistry","score_opus":0.01061318673801509,"score_gpt":0.22859116997119522,"score_spread":0.21797798323318013,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2903808278","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9928046,0.00045674708,0.005855003,0.00004224407,0.000016941976,0.000018762095,0.00015396635,0.00016455397,0.00048724163],"genre_scores_gemma":[0.99661875,0.00020987258,0.0022356145,0.000014005115,0.000006418727,0.000017236971,0.00014100138,0.000020992211,0.00073611736],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99971145,0.00003760383,0.000022834427,0.00006635005,0.00010983387,0.00005180195],"domain_scores_gemma":[0.9996141,0.00015857247,0.000057562687,0.000030461913,0.00009870291,0.000040610754],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00035873184,0.00040329696,0.00045426548,0.00024671247,0.0002318033,0.000504429,0.00045698084,0.0006585788,0.0008733469],"category_scores_gemma":[0.00058459106,0.00018516695,0.00035190478,0.00021010214,0.00015521738,0.00034352703,0.00019186182,0.0004072127,0.00040411882],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00020299808,0.00002838741,0.0002819344,0.000031536496,0.000007692283,0.00002567535,0.0000129467,0.0003425983,0.9969811,0.000023606908,0.000025068648,0.0020363699],"study_design_scores_gemma":[0.000014372247,0.00046879036,0.0018820259,0.0000042536417,0.00002069187,0.000048070237,0.000013172902,0.0060807574,0.9911227,0.000011781027,0.00032537009,0.000008039097],"about_ca_topic_score_codex":0.0015931089,"about_ca_topic_score_gemma":0.00070088083,"teacher_disagreement_score":0.0015931089,"about_ca_system_score_codex":0.00036013295,"about_ca_system_score_gemma":0.00029139506,"threshold_uncertainty_score":0.0031676888},"labels":[],"label_agreement":null},{"id":"W2906374250","doi":"10.1002/ceat.201800208","title":"Aerosol Generation of Nonspherical Particles by Desublimation of Copper Phthalocyanine","year":2018,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Particle Dynamics in Fluid Flows","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"Deutsche Forschungsgemeinschaft","keywords":"Scanning mobility particle sizer; Aerosol; Scanning electron microscope; Copper; Nozzle; Particle (ecology); Adiabatic process; Differential mobility analyzer; Analytical Chemistry (journal); Materials science; Particle size; Particle-size distribution; Chemistry; Composite material; Metallurgy; Chromatography; Thermodynamics; Physical chemistry","score_opus":0.010458836928096234,"score_gpt":0.21030518733329892,"score_spread":0.19984635040520268,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2906374250","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9719464,0.00036905223,0.025672674,0.000045397468,0.00004470605,0.00018732324,0.00011915724,0.00028502318,0.0013301963],"genre_scores_gemma":[0.9880953,0.000103889965,0.010496203,0.000022519393,0.0000130445405,0.0000665209,0.00009198454,0.000051160743,0.0010593846],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998246,0.000024873596,0.000007896791,0.000040182385,0.00008125903,0.000021181133],"domain_scores_gemma":[0.99984825,0.00005076957,0.000033345674,0.000018790673,0.000027442302,0.000021382933],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00024294037,0.00025268784,0.00023268418,0.00019948513,0.00010380322,0.00020420586,0.00034985307,0.00020531853,0.0006476362],"category_scores_gemma":[0.00027062363,0.00009402873,0.00014714006,0.00008639034,0.0002405291,0.000209069,0.0002441581,0.0002615923,0.00015794071],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0000313434,0.00002535682,0.00016507466,0.000031608484,0.000002959785,0.00007019741,0.000015447144,0.00018917584,0.9973908,0.00014416588,0.000052980766,0.0018808095],"study_design_scores_gemma":[0.000013674643,0.0001325572,0.00068797945,0.000001232501,0.0000022667214,0.000048266396,0.0000038053631,0.0020863665,0.99640083,0.000018109533,0.00060246,0.0000024243068],"about_ca_topic_score_codex":0.00016412252,"about_ca_topic_score_gemma":0.00017423322,"teacher_disagreement_score":0.0006476362,"about_ca_system_score_codex":0.0002202495,"about_ca_system_score_gemma":0.00013133965,"threshold_uncertainty_score":0.0021665692},"labels":[],"label_agreement":null},{"id":"W2913686478","doi":"10.1002/ceat.201800205","title":"Colorimetric Methods for Determining Fe, V, and Ni Contents in Coke and Anodes","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Analytical chemistry methods development","field":"Chemistry","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université du Québec à Chicoutimi","funders":"Natural Sciences and Engineering Research Council of Canada; Université du Québec à Chicoutimi","keywords":"Coke; Anode; Petroleum coke; Carbon fibers; Raw material; Impurity; Reagent; Metallurgy; Materials science; Coal tar; Coal; Metal; Chemistry; Electrode; Composite material; Organic chemistry","score_opus":0.017206522141453472,"score_gpt":0.29665794455166283,"score_spread":0.27945142241020937,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2913686478","genre_codex":"methods","genre_gemma":"methods","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"methods","genre_consensus":"methods","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.16368696,0.013721718,0.8044443,0.00052726886,0.0010071449,0.0007665606,0.0011206984,0.0024850187,0.012240366],"genre_scores_gemma":[0.4222016,0.0076266383,0.5553083,0.00022728107,0.00008141479,0.00082919514,0.00070444087,0.0000792914,0.012941862],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99820733,0.00038500043,0.0001397028,0.00032180262,0.0008478007,0.00009827267],"domain_scores_gemma":[0.9990866,0.00028636988,0.00017789286,0.00007960733,0.00029683765,0.000072648974],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0012984272,0.0011230032,0.0002823082,0.0022339309,0.0004407781,0.000578458,0.0010690958,0.0009497161,0.0010933538],"category_scores_gemma":[0.0016910543,0.00046578457,0.00033384387,0.0006917736,0.00046980806,0.00058705965,0.0004972798,0.0010950153,0.0009148621],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000053245996,0.00007863569,0.00072761404,0.0002820955,0.00001871663,0.00007480628,0.000060784136,0.00031605797,0.9750097,0.0008049976,0.00041066855,0.022162758],"study_design_scores_gemma":[0.0000041054127,0.000092500726,0.0007146951,0.000018469576,0.000012713083,0.00016815194,0.00004320942,0.0021680663,0.9934278,0.00018393526,0.003148369,0.000017998611],"about_ca_topic_score_codex":0.00045049138,"about_ca_topic_score_gemma":0.0013749662,"teacher_disagreement_score":0.0022339309,"about_ca_system_score_codex":0.00035850637,"about_ca_system_score_gemma":0.00041965072,"threshold_uncertainty_score":0.0068668127},"labels":[],"label_agreement":null},{"id":"W2917669850","doi":"10.1002/ceat.201800563","title":"Mixing of Oil in Water Through Electrical Resistance Tomography and Response Surface Methodology","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Electrical and Bioimpedance Tomography","field":"Engineering","cited_by":16,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"Natural Sciences and Engineering Research Council of Canada","keywords":"Impeller; Mixing (physics); Dispersion (optics); Materials science; Viscosity; Volume fraction; Volume (thermodynamics); Petroleum engineering; Composite material; Mechanical engineering; Engineering; Thermodynamics; Optics; Physics","score_opus":0.006636220995822409,"score_gpt":0.20266713509977727,"score_spread":0.19603091410395485,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2917669850","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.80891967,0.00051313324,0.18845464,0.00009791559,0.00003109198,0.00016920603,0.00010318057,0.00040404798,0.0013072412],"genre_scores_gemma":[0.8533659,0.00050099014,0.14429109,0.000027592821,0.000012321694,0.00013233458,0.000097436234,0.00005570641,0.0015167076],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9996132,0.000119403085,0.00001845374,0.00005720828,0.00016219317,0.000029551096],"domain_scores_gemma":[0.99968755,0.000164324,0.00006134954,0.000021371505,0.000054871987,0.000010549698],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00080706284,0.0004462594,0.00033700885,0.00040557532,0.00013173022,0.00037206546,0.00031737745,0.00035334495,0.00061663974],"category_scores_gemma":[0.0008495783,0.00022767136,0.00025256572,0.0004327814,0.00039750952,0.00046136454,0.00027219614,0.00039843045,0.00017502313],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006735829,0.00002115498,0.00011254709,0.000037877373,0.000003118643,0.000015388667,0.0000309045,0.00077118917,0.99363977,0.0001236161,0.000014909077,0.0051621757],"study_design_scores_gemma":[0.0000071540567,0.00017024946,0.00036784023,0.000001760806,0.000005984807,0.000019553188,0.000019475863,0.019205905,0.9797869,0.00003727749,0.00037006644,0.000007960942],"about_ca_topic_score_codex":0.00044487373,"about_ca_topic_score_gemma":0.00064974034,"teacher_disagreement_score":0.00080706284,"about_ca_system_score_codex":0.00018916956,"about_ca_system_score_gemma":0.00017460242,"threshold_uncertainty_score":0.004268229},"labels":[],"label_agreement":null},{"id":"W2937137023","doi":"10.1002/ceat.201800752","title":"Blend Time Measurement in the Confined Impeller Stirred Tank","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":11,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"Natural Sciences and Engineering Research Council of Canada; Syncrude","keywords":"Impeller; Mixing (physics); Materials science; Reynolds number; Viscosity; Mechanics; Composite material; Physics; Turbulence","score_opus":0.0034234962787026034,"score_gpt":0.1527042535700865,"score_spread":0.14928075729138388,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2937137023","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9624269,0.0002721234,0.035951857,0.00003332795,0.000025177062,0.00002778588,0.00018354515,0.00027128027,0.0008080702],"genre_scores_gemma":[0.98241144,0.00017823081,0.015510034,0.00002327617,0.000008653042,0.000038033177,0.00019383263,0.000026470356,0.0016100752],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99980086,0.000014508961,0.000007930467,0.00005715684,0.000096720265,0.000022700258],"domain_scores_gemma":[0.99978477,0.000037153495,0.000058561804,0.000017037646,0.000063919004,0.0000386601],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018118057,0.0002732518,0.00034947458,0.00030728162,0.00018152018,0.00039938572,0.00031684685,0.00036146617,0.0008424794],"category_scores_gemma":[0.00031162373,0.00012605186,0.0002127439,0.00034343734,0.00018593567,0.00047701283,0.00028476762,0.00045483588,0.00026644918],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007973207,0.0000103192715,0.0003085483,0.000014297217,0.0000023528992,0.000024459385,0.000018670451,0.000111352514,0.9975116,0.000023996367,0.00001841417,0.0018760711],"study_design_scores_gemma":[0.000013140538,0.00030562998,0.005298628,0.000002800916,0.000014076311,0.00007389886,0.0000424776,0.006995533,0.9865628,0.000029291507,0.0006468095,0.00001492171],"about_ca_topic_score_codex":0.001042102,"about_ca_topic_score_gemma":0.00096426456,"teacher_disagreement_score":0.001042102,"about_ca_system_score_codex":0.00029489188,"about_ca_system_score_gemma":0.00025680094,"threshold_uncertainty_score":0.0028184056},"labels":[],"label_agreement":null},{"id":"W2981839501","doi":"10.1002/ceat.201900404","title":"Effect of Substrate Characteristics and Process Fluid Percolation on Dry Anaerobic Digestion Processes","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Landfill Environmental Impact Studies","field":"Environmental Science","cited_by":8,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Alberta Medical Association","funders":"Bundesministerium für Wirtschaft und Energie","keywords":"Anaerobic digestion; Compaction; Methane; Materials science; Percolation (cognitive psychology); Permeability (electromagnetism); Pulp and paper industry; Chemistry; Waste management; Chemical engineering; Composite material; Organic chemistry; Engineering; Biochemistry","score_opus":0.0022374801552789607,"score_gpt":0.1904555232843606,"score_spread":0.18821804312908164,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2981839501","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99907446,0.00017041208,0.00041844303,0.0000106699,0.000004056574,0.000014656275,0.000058958933,0.000009995951,0.00023848805],"genre_scores_gemma":[0.9992638,0.00012710858,0.00039526692,0.000010978066,0.0000030077174,0.000010110189,0.000062573,0.0000084601415,0.00011878789],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99938285,0.00019949918,0.00006090883,0.00009533521,0.00015966283,0.000101774465],"domain_scores_gemma":[0.9983656,0.001086709,0.00027649556,0.000049639766,0.000114279035,0.00010735656],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004374282,0.00049423,0.00043323464,0.0003343742,0.00032800244,0.0007842881,0.0002368271,0.00029931142,0.0011002147],"category_scores_gemma":[0.0018193419,0.0003026137,0.00023684901,0.00049644866,0.0004093407,0.0008297014,0.0004218923,0.00047175636,0.00013290689],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0019662282,0.00021586102,0.0028131872,0.00020219272,0.00002862732,0.00021324975,0.00010465159,0.001961108,0.98882324,0.000065586864,0.00003457075,0.0035715012],"study_design_scores_gemma":[0.000048218128,0.0025301466,0.01566429,0.000018452132,0.00006532348,0.00018028035,0.00015067958,0.0022978259,0.9784023,0.000063562526,0.0005528185,0.000026096432],"about_ca_topic_score_codex":0.0010393456,"about_ca_topic_score_gemma":0.0010548588,"teacher_disagreement_score":0.0011002147,"about_ca_system_score_codex":0.00039207315,"about_ca_system_score_gemma":0.0002962188,"threshold_uncertainty_score":0.0036805868},"labels":[],"label_agreement":null},{"id":"W2989803937","doi":"10.1002/ceat.201970125","title":"Experimental and CFD Investigations of Biomass Thermochemical Conversion: Fundamental Mechanisms, Practical Application, and Advanced Design","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Thermochemical Biomass Conversion Processes","field":"Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal","funders":"","keywords":"Computational fluid dynamics; Biochemical engineering; Biomass (ecology); Process engineering; Environmental science; Thermodynamics; Engineering; Physics; Geology","score_opus":0.00623952193660888,"score_gpt":0.20652031787113503,"score_spread":0.20028079593452616,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2989803937","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.95476747,0.0024172803,0.018444896,0.00047696318,0.00016586487,0.00018837192,0.0016212378,0.00018866696,0.02172915],"genre_scores_gemma":[0.99042577,0.0009541085,0.0059674196,0.000028253735,0.000025208217,0.000059029444,0.000450948,0.00002944914,0.0020597188],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9996196,0.000055401797,0.000028674393,0.000056510875,0.0001830874,0.000056681274],"domain_scores_gemma":[0.9990466,0.0005343873,0.00004323576,0.00012295022,0.0002177312,0.000035028912],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00083593297,0.0005070345,0.00064834696,0.0004711214,0.0010458411,0.0006737075,0.00071273634,0.0007270468,0.006575064],"category_scores_gemma":[0.0017282353,0.00034963788,0.00044182365,0.00095936155,0.00081095315,0.0012101844,0.0005217439,0.0008753568,0.000528754],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.001588575,0.001403985,0.004359103,0.0011736053,0.000037274254,0.00026183992,0.0004849958,0.031322077,0.92120874,0.006155176,0.0013315271,0.030673048],"study_design_scores_gemma":[0.00013416601,0.00055290014,0.003945971,0.00003364091,0.000027322336,0.00015126409,0.00017932503,0.056168307,0.9330104,0.0008917967,0.004859264,0.000045640547],"about_ca_topic_score_codex":0.0035990654,"about_ca_topic_score_gemma":0.0032096056,"teacher_disagreement_score":0.006575064,"about_ca_system_score_codex":0.00091381615,"about_ca_system_score_gemma":0.00076450617,"threshold_uncertainty_score":0.021995842},"labels":[],"label_agreement":null},{"id":"W2991006719","doi":"10.1002/ceat.201900096","title":"Evolving an Accurate Decision Tree‐Based Model for Predicting Carbon Dioxide Solubility in Polymers","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Polymer Foaming and Composites","field":"Materials Science","cited_by":23,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"","keywords":"Solubility; Polymer; Decision tree; Compatibility (geochemistry); Boosting (machine learning); Carbon dioxide; Gradient boosting; Computer science; Process engineering; Chemistry; Materials science; Thermodynamics; Biological system; Machine learning; Organic chemistry; Random forest; Engineering; Physics; Composite material","score_opus":0.008380845600628751,"score_gpt":0.2284517533786518,"score_spread":0.22007090777802307,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2991006719","genre_codex":"methods","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":null,"domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.39755648,0.00078434235,0.59827495,0.00037103065,0.00009624082,0.00008960141,0.0003136925,0.00061618804,0.0018974842],"genre_scores_gemma":[0.9680882,0.00014718088,0.030416964,0.00006454628,0.000027968896,0.00010653418,0.00021945492,0.000017059501,0.0009120615],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.99970144,0.000101202764,0.000020458683,0.00007187611,0.00005542615,0.000049591607],"domain_scores_gemma":[0.99889696,0.0007321419,0.000075018885,0.000027739154,0.00022806696,0.000040120533],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.001746323,0.00073039375,0.0013971266,0.000638651,0.00036757626,0.000679474,0.00083463127,0.0011231852,0.00088018476],"category_scores_gemma":[0.002051499,0.00048702725,0.0007762841,0.00044582022,0.0002956951,0.00066664576,0.0004630909,0.0010119684,0.0002151196],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000038767685,0.00003986471,0.00088522624,0.000013121812,0.000018755141,0.00001561921,0.0000075400967,0.9888769,0.00062588457,0.00028002556,0.00013839988,0.009059846],"study_design_scores_gemma":[8.759119e-7,0.000003614407,0.000033840275,4.4027408e-7,0.0000012707827,5.749775e-7,3.179254e-7,0.9998567,0.000051096024,0.00004186347,0.00000881422,6.7454533e-7],"about_ca_topic_score_codex":0.011681256,"about_ca_topic_score_gemma":0.0055587483,"teacher_disagreement_score":0.011681256,"about_ca_system_score_codex":0.00071594305,"about_ca_system_score_gemma":0.0010522412,"threshold_uncertainty_score":0.02322656},"labels":[],"label_agreement":null},{"id":"W2995475639","doi":"10.1002/ceat.201900231","title":"Polyvinyl Alcohol/Alginate/Zeolite Nanohybrid for Removal of Metals","year":2019,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Adsorption and biosorption for pollutant removal","field":"Environmental Science","cited_by":36,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Winnipeg; University of Manitoba","funders":"","keywords":"Adsorption; Zeolite; Polyvinyl alcohol; Fourier transform infrared spectroscopy; Metal ions in aqueous solution; Langmuir adsorption model; Desorption; Nuclear chemistry; Scanning electron microscope; Materials science; Chemistry; Chemical engineering; Inorganic chemistry; Metal; Catalysis; Organic chemistry; Metallurgy; Composite material","score_opus":0.005526527428772653,"score_gpt":0.20664979792208135,"score_spread":0.2011232704933087,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W2995475639","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9881947,0.0011480729,0.009498218,0.000093096925,0.000048604077,0.000023101698,0.00012688548,0.00021767923,0.0006495238],"genre_scores_gemma":[0.9936373,0.00036743318,0.0041921968,0.000044841436,0.000010280407,0.000014790607,0.00010312307,0.00002147293,0.0016086164],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998579,0.000013090536,0.0000116876645,0.000025927075,0.000055649718,0.000035705125],"domain_scores_gemma":[0.9999312,0.0000112509515,0.00001532473,0.000005347293,0.000020827823,0.00001597604],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.000108517204,0.00037956037,0.00035168495,0.0003254951,0.00014021367,0.00028320833,0.000226304,0.00033503186,0.00064486766],"category_scores_gemma":[0.00012339611,0.00017138172,0.0004559622,0.00018162961,0.00013867488,0.00024168956,0.00025170558,0.00032151438,0.0002496273],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000016015625,0.000008193464,0.000031575262,0.000023540724,0.0000035741893,0.000011688186,0.0000032276284,0.00004717829,0.99929905,0.000013055775,0.000009092487,0.0005339117],"study_design_scores_gemma":[0.000008351448,0.00009289667,0.0011260571,0.0000025529132,0.000021961458,0.000066548346,0.000010671115,0.0015430971,0.99628145,0.000016564196,0.0008195444,0.000010292951],"about_ca_topic_score_codex":0.001825684,"about_ca_topic_score_gemma":0.0033688564,"teacher_disagreement_score":0.001825684,"about_ca_system_score_codex":0.00031449492,"about_ca_system_score_gemma":0.0001557652,"threshold_uncertainty_score":0.0036301017},"labels":[],"label_agreement":null},{"id":"W3000739589","doi":"10.1002/ceat.201900452","title":"Biohydrogen Production Through Dark Fermentation","year":2020,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Anaerobic Digestion and Biogas Production","field":"Engineering","cited_by":283,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"","keywords":"Biohydrogen; Dark fermentation; Biofuel; Biomass (ecology); Fermentation; Lignocellulosic biomass; Renewable energy; Hydrogen production; Waste management; Pulp and paper industry; Fermentative hydrogen production; Environmental science; Chemistry; Hydrogen; Biochemical engineering; Engineering; Food science; Agronomy; Organic chemistry; Ecology; Biology","score_opus":0.00914441645081477,"score_gpt":0.1915945876852097,"score_spread":0.18245017123439494,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3000739589","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.81710523,0.07092728,0.07091571,0.0007744548,0.000699072,0.00017988257,0.0015860879,0.0005961467,0.037216134],"genre_scores_gemma":[0.95699495,0.023282325,0.010275803,0.00012892556,0.00004563205,0.000047214962,0.00086266856,0.00003711346,0.008325405],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998685,0.000020271174,0.000009568314,0.00003820426,0.00004062961,0.00002278265],"domain_scores_gemma":[0.99996626,0.000004556028,0.0000074547215,0.000003977687,0.000010828137,0.0000068566887],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00014987956,0.0005455953,0.00025996726,0.00032037095,0.00013151334,0.00060810574,0.00026469954,0.00032688733,0.0008291747],"category_scores_gemma":[0.000118987264,0.000145271,0.00032722877,0.00042261442,0.00012466976,0.00054722204,0.00048237585,0.00059331924,0.0006741635],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010740801,0.0000996548,0.00032220912,0.0009005698,0.000027134087,0.00020986774,0.000035235957,0.0005642074,0.9639763,0.0015702074,0.00059478544,0.031592354],"study_design_scores_gemma":[0.000008420894,0.0001993973,0.0005282301,0.00004518426,0.00001949309,0.00012628964,0.000031004616,0.0009271151,0.98517364,0.00033317372,0.012596644,0.000011385301],"about_ca_topic_score_codex":0.00035302472,"about_ca_topic_score_gemma":0.000418953,"teacher_disagreement_score":0.0008291747,"about_ca_system_score_codex":0.00028792926,"about_ca_system_score_gemma":0.00019693549,"threshold_uncertainty_score":0.0027738214},"labels":[],"label_agreement":null},{"id":"W3002211997","doi":"10.1002/ceat.201900339","title":"Catalytic Hydrogen Production from Methane Partial Oxidation: Mechanism and Kinetic Study","year":2020,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalytic Processes in Materials Science","field":"Materials Science","cited_by":116,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"","funders":"Bryden Centre, Queen's University Belfast; Engineering and Physical Sciences Research Council; Interreg; European Commission; Queen's University; Queen's University Belfast; Department for the Economy","keywords":"Catalysis; Partial oxidation; Methane; Chemistry; Oxide; Chemical engineering; Hydrogen production; Hydrogen; Coke; Inorganic chemistry; Transition metal; Noble metal; Combustion; Physical chemistry; Organic chemistry","score_opus":0.01049430049283335,"score_gpt":0.21525850423916057,"score_spread":0.20476420374632723,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3002211997","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.96793145,0.015913239,0.010716398,0.00017523377,0.000040646453,0.00005107381,0.0003935354,0.00008923534,0.004689134],"genre_scores_gemma":[0.9948304,0.00301191,0.0011081238,0.000008986629,0.000010899092,0.000010926235,0.00017464711,0.0000036526746,0.0008403869],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999915,0.000014171666,0.000003912529,0.000013733935,0.000031258012,0.000021932537],"domain_scores_gemma":[0.9999442,0.000025817119,0.0000091591055,0.000005879335,0.000010335483,0.0000045605616],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025933943,0.0003409921,0.0003180129,0.00020881798,0.000102003825,0.0001937964,0.0005133083,0.00031217295,0.0010682101],"category_scores_gemma":[0.00024210791,0.00013821785,0.0002583567,0.00021271022,0.00016259945,0.00030955276,0.0002248533,0.0003445865,0.00022419608],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0003999458,0.00010729006,0.0014011804,0.0011811483,0.000056719942,0.00025915177,0.00007981275,0.0031372982,0.9699953,0.0034350161,0.0004087025,0.019538317],"study_design_scores_gemma":[0.00002654503,0.000469409,0.004203612,0.000028530607,0.000044603996,0.00036553395,0.000053288877,0.034887966,0.954587,0.00059831934,0.004711638,0.000023548158],"about_ca_topic_score_codex":0.0011751876,"about_ca_topic_score_gemma":0.00083451875,"teacher_disagreement_score":0.0011751876,"about_ca_system_score_codex":0.00032785893,"about_ca_system_score_gemma":0.00014665122,"threshold_uncertainty_score":0.0035734773},"labels":[],"label_agreement":null},{"id":"W3002255986","doi":"10.1002/ceat.201900461","title":"A Comparative Study of Hydroxyapatite‐ and Alumina‐Based Catalysts in Dry Reforming of Methane","year":2020,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Catalytic Processes in Materials Science","field":"Materials Science","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"","keywords":"Catalysis; Calcination; Carbon dioxide reforming; Methane; Sintering; Chemical engineering; Metal; Nickel; Particle size; Materials science; Chemistry; Methane reformer; Inorganic chemistry; Syngas; Metallurgy; Steam reforming; Hydrogen production; Organic chemistry","score_opus":0.014733554043367314,"score_gpt":0.25134483523055967,"score_spread":0.23661128118719235,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3002255986","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9969933,0.0011921162,0.0007601629,0.000015386804,0.000010422507,0.000013231076,0.00006828181,0.000019091329,0.0009279762],"genre_scores_gemma":[0.99862254,0.0002492004,0.00045190362,0.0000064752735,0.0000044394365,0.000005072104,0.00009757098,0.000007489482,0.00055530627],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99976295,0.00003686342,0.000017414128,0.000030902404,0.00009792146,0.000053976943],"domain_scores_gemma":[0.9997861,0.00008714966,0.000032219064,0.000020822139,0.00004385773,0.00002987479],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00025842444,0.00021908164,0.00035527296,0.00037364886,0.00015988784,0.00035202794,0.0003154393,0.00030433637,0.00083957426],"category_scores_gemma":[0.00047734194,0.00014579708,0.00027824097,0.00024483877,0.00026031645,0.00023720381,0.00017383878,0.00027415523,0.00017036503],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00023164398,0.00002322597,0.00031504332,0.00009752868,0.00001386283,0.00006039211,0.000035646877,0.00014044881,0.99694437,0.000049367944,0.00001148029,0.0020770235],"study_design_scores_gemma":[0.000010466011,0.00028709514,0.0031328865,0.0000038620014,0.00001959768,0.00006876452,0.000035910638,0.0006752256,0.99509406,0.00001098274,0.00065622036,0.0000049489163],"about_ca_topic_score_codex":0.0012302996,"about_ca_topic_score_gemma":0.0018547887,"teacher_disagreement_score":0.0012302996,"about_ca_system_score_codex":0.00019538068,"about_ca_system_score_gemma":0.00014340748,"threshold_uncertainty_score":0.0028086305},"labels":[],"label_agreement":null},{"id":"W3047001839","doi":"10.1002/ceat.201900469","title":"Hybrid Extraction of Oily Sludge by Tertiary Amines and Protonated Tertiary Amines","year":2020,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Petroleum Processing and Analysis","field":"Chemistry","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ministry of Agriculture","funders":"National Natural Science Foundation of China","keywords":"Protonation; Chemistry; Solvent; Extraction (chemistry); Solvent extraction; Tertiary amine; Wetting; Absorption (acoustics); Organic chemistry; Chromatography; Nuclear chemistry; Ion; Chemical engineering; Materials science","score_opus":0.0041581056553420944,"score_gpt":0.19811274691494707,"score_spread":0.193954641259605,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3047001839","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.98367554,0.0009016126,0.013470751,0.00005241757,0.000045777182,0.00004726401,0.00016548001,0.00013764853,0.0015035075],"genre_scores_gemma":[0.9893757,0.0004278223,0.0073931217,0.000039936964,0.000009791847,0.000027999307,0.00014347261,0.00002357497,0.0025586777],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999879,0.000014278952,0.0000106925645,0.00002768071,0.000042453208,0.000025900785],"domain_scores_gemma":[0.9999341,0.000011143877,0.000015843145,0.000006357418,0.000017799917,0.000014790563],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00016771958,0.00044497676,0.00034285372,0.0002906692,0.00012678356,0.00024462596,0.00015462824,0.00036098354,0.0008138062],"category_scores_gemma":[0.00013217462,0.00018640501,0.00038302442,0.00021541762,0.00017340816,0.0004041292,0.00033946228,0.00032002782,0.00040459065],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000045893583,0.000008010851,0.000047943562,0.000048275968,0.000006665868,0.00003781921,0.000009888364,0.00007964624,0.998464,0.000040619965,0.000012007903,0.0011991414],"study_design_scores_gemma":[0.0000068875697,0.00009218209,0.0004221626,0.0000029925218,0.0000104037,0.00006906523,0.000010696343,0.0009375822,0.997664,0.000022225673,0.0007566782,0.0000052403566],"about_ca_topic_score_codex":0.0003028518,"about_ca_topic_score_gemma":0.0006946507,"teacher_disagreement_score":0.0008138062,"about_ca_system_score_codex":0.00015586743,"about_ca_system_score_gemma":0.00012132663,"threshold_uncertainty_score":0.0027225018},"labels":[],"label_agreement":null},{"id":"W3126952440","doi":"10.1002/ceat.202000525","title":"Comparative Study of the Combined Supersonic Separator and Vortex Tube Performance for Hydrocarbon Gas Drying","year":2021,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Ranque-Hilsch vortex tube","field":"Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":false,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":true,"ca_institutions":"","funders":"Russian Academy of Sciences","keywords":"Separator (oil production); Nozzle; Vortex tube; Vortex; Supersonic speed; Mechanics; Moisture; Hydrocarbon; Chemistry; Materials science; Thermodynamics; Nuclear engineering; Composite material; Physics; Engineering","score_opus":0.007506868573534015,"score_gpt":0.2066400075188057,"score_spread":0.19913313894527168,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3126952440","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9949581,0.0007012096,0.003567498,0.000015084696,0.000016582662,0.000012784524,0.00006898355,0.000067551104,0.00059226574],"genre_scores_gemma":[0.9945471,0.0003177146,0.0039830883,0.000008982545,0.000008100686,0.000014483695,0.00014300963,0.000029654035,0.00094789796],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99974686,0.000038284514,0.000016724245,0.000045576508,0.00011455224,0.000038006296],"domain_scores_gemma":[0.9995988,0.00013040556,0.00005204151,0.000022419752,0.00016088493,0.00003545918],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0006180327,0.00033914318,0.0003600243,0.00039622225,0.00019642859,0.00041702564,0.00027317522,0.0002633907,0.00095317385],"category_scores_gemma":[0.00061136245,0.00015752246,0.0002049207,0.00033922595,0.0001586692,0.0004904079,0.00018579567,0.00021465284,0.00029900682],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00031665995,0.000036315785,0.00084376207,0.00008488119,0.000012997849,0.000030180207,0.000045678793,0.0005913838,0.99147075,0.00008530822,0.000064436405,0.006417562],"study_design_scores_gemma":[0.000011007474,0.000456987,0.0029517515,0.000004029184,0.00002348812,0.00003006151,0.000021322008,0.0036442068,0.99204284,0.000006940427,0.0008000803,0.000007255693],"about_ca_topic_score_codex":0.00048824976,"about_ca_topic_score_gemma":0.00141347,"teacher_disagreement_score":0.00095317385,"about_ca_system_score_codex":0.00019894948,"about_ca_system_score_gemma":0.00025634398,"threshold_uncertainty_score":0.0032684803},"labels":[],"label_agreement":null},{"id":"W3163798384","doi":"10.1002/ceat.202000262","title":"Mixing Time and Scale‐up Investigation of a Moving‐Baffle Oscillatory Baffled Column","year":2021,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Thin Films","field":"Engineering","cited_by":5,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Lakehead University","funders":"","keywords":"Baffle; Dimensionless quantity; Mixing (physics); Mechanics; SCALE-UP; Oscillation (cell signaling); Scale (ratio); Reynolds number; Work (physics); Amplitude; Column (typography); Paddle; Computational fluid dynamics; Materials science; Chemistry; Physics; Thermodynamics; Mathematics; Classical mechanics; Turbulence; Geometry; Optics; Composite material","score_opus":0.0025607978654104443,"score_gpt":0.15472037259449775,"score_spread":0.1521595747290873,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3163798384","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.994456,0.00011765321,0.004939274,0.000041988445,0.000009140773,0.000009559351,0.00007033345,0.00007144111,0.0002846699],"genre_scores_gemma":[0.9979085,0.0000370051,0.001790958,0.000007303001,0.0000021743772,0.000006667664,0.000041447853,0.000008573068,0.00019733972],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999045,0.000008790748,0.000004251711,0.000018811705,0.000040774896,0.000022771826],"domain_scores_gemma":[0.9995956,0.00021303378,0.000043375472,0.000024532936,0.000078407975,0.0000451346],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018431034,0.00015714171,0.0002571812,0.00026177868,0.00028773415,0.00040107366,0.000180697,0.00022062803,0.0007559922],"category_scores_gemma":[0.00062769663,0.00009547963,0.00014115067,0.00018457536,0.00023462028,0.00021083863,0.00012332517,0.00037904672,0.000092723036],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00011514975,0.000031863634,0.0008022868,0.000016861946,0.000005888505,0.000030079515,0.000028783044,0.0014076323,0.99416417,0.000091717084,0.000036109566,0.0032694363],"study_design_scores_gemma":[0.000014208456,0.0002883341,0.008339854,0.0000030692122,0.000017829863,0.000030321866,0.00003570609,0.05151772,0.93900764,0.0000548154,0.00067054457,0.000019960691],"about_ca_topic_score_codex":0.0018156845,"about_ca_topic_score_gemma":0.0010394785,"teacher_disagreement_score":0.0018156845,"about_ca_system_score_codex":0.00032984506,"about_ca_system_score_gemma":0.0001760824,"threshold_uncertainty_score":0.0036101937},"labels":[],"label_agreement":null},{"id":"W3170214889","doi":"10.1002/ceat.202000497","title":"Performance Assessment Study on the Na‐O‐H Thermochemical Water Splitting Cycle for Hydrogen Generation","year":2021,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Chemical Looping and Thermochemical Processes","field":"Engineering","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Hydrogen production; Thermochemical cycle; Hydrogen; Chemistry; Decomposition; Water splitting; Hydrogen purifier; Oxygen; Sodium; Inorganic chemistry; Thermodynamics; Catalysis; Organic chemistry","score_opus":0.011019425821542868,"score_gpt":0.21862176172104117,"score_spread":0.2076023358994983,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3170214889","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99632204,0.00025322245,0.00180612,0.000022360391,0.00000583654,0.000017785891,0.0001050663,0.000051687162,0.0014160379],"genre_scores_gemma":[0.99908316,0.00006351793,0.0003739431,0.0000024569974,7.4796384e-7,0.0000043625455,0.00004175022,0.000004767699,0.00042529372],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998914,0.00001823189,0.0000046820023,0.000018473986,0.000048147736,0.00001912735],"domain_scores_gemma":[0.9998902,0.000027451202,0.000008703908,0.000009715451,0.000053905667,0.000010079961],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00026641996,0.00026996416,0.0004453141,0.0003231258,0.00029827052,0.00029577911,0.0003356988,0.00027848463,0.0013476792],"category_scores_gemma":[0.0002546988,0.00010180462,0.00029501505,0.00021734228,0.000120876735,0.00035601834,0.00017024617,0.00014806249,0.00019111724],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.002480369,0.00040003457,0.0100235855,0.00049086707,0.000074187126,0.00020702557,0.00010925349,0.09871225,0.8302253,0.0007792946,0.0005314264,0.05596639],"study_design_scores_gemma":[0.0000500799,0.0030916715,0.0089496495,0.000008826839,0.000054526583,0.00005193569,0.00007643595,0.21148679,0.77460015,0.00015536985,0.0014525033,0.000022055896],"about_ca_topic_score_codex":0.0036189952,"about_ca_topic_score_gemma":0.0037932284,"teacher_disagreement_score":0.0036189952,"about_ca_system_score_codex":0.00037916147,"about_ca_system_score_gemma":0.00026129442,"threshold_uncertainty_score":0.0071958303},"labels":[],"label_agreement":null},{"id":"W3175308254","doi":"10.1002/ceat.202100180","title":"Advanced Evaluation of a Biomass Externally Fired Hydrogen Production Combined Cycle","year":2021,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Thermodynamic and Exergetic Analyses of Power and Cooling Systems","field":"Engineering","cited_by":0,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Ontario Tech University","funders":"","keywords":"Exergy; Gas compressor; Exergy efficiency; Process engineering; Combined cycle; Wood gas generator; Environmental science; Hydrogen production; Gas turbines; Hydrogen; Biomass (ecology); Turbine; Thermodynamics; Waste management; Nuclear engineering; Engineering; Chemistry; Mechanical engineering; Physics","score_opus":0.005393908812886113,"score_gpt":0.2097745378991865,"score_spread":0.20438062908630036,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3175308254","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9915656,0.00012820275,0.004333399,0.000014373569,0.0000134454085,0.000034903984,0.00013965668,0.00003884511,0.0037315553],"genre_scores_gemma":[0.99866605,0.000034259087,0.0006708553,0.0000018067693,0.0000012190775,0.000009003855,0.0000549156,0.0000042287843,0.00055777276],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9997522,0.000045263707,0.000009056152,0.00003723522,0.00012908703,0.000027136233],"domain_scores_gemma":[0.9998222,0.00006470436,0.0000114855075,0.000016097652,0.000066080356,0.000019521081],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00038149426,0.0004341425,0.00048360837,0.0006826645,0.0003322959,0.00054274,0.00046625474,0.0004553504,0.002024758],"category_scores_gemma":[0.00045599352,0.00015381811,0.00046681607,0.000542747,0.00033422696,0.00042529468,0.00052905246,0.0003869311,0.00023746042],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.0038615104,0.00060533243,0.016042165,0.0008806275,0.00020062782,0.0010860877,0.00010909798,0.51594484,0.38220865,0.0023396,0.0004262278,0.07629526],"study_design_scores_gemma":[0.00016649281,0.0046779956,0.019493444,0.000020515336,0.00013254548,0.0001624057,0.000108694425,0.65000063,0.3222808,0.00073916576,0.0021776112,0.000039680188],"about_ca_topic_score_codex":0.0023292557,"about_ca_topic_score_gemma":0.0029486907,"teacher_disagreement_score":0.0023292557,"about_ca_system_score_codex":0.0005960214,"about_ca_system_score_gemma":0.0003039284,"threshold_uncertainty_score":0.0067735314},"labels":[],"label_agreement":null},{"id":"W3198506156","doi":"10.1002/ceat.202100295","title":"Metal Ion Adsorption Using Coconut Shell Powder Activated by Chemical and Physical Treatments","year":2021,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Adsorption and biosorption for pollutant removal","field":"Environmental Science","cited_by":9,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Université de Sherbrooke","funders":"Universidade Federal do Rio Grande do Norte","keywords":"Adsorption; Chemistry; Desorption; Metal ions in aqueous solution; Langmuir; Langmuir adsorption model; Microemulsion; Metal; Materials science; Chemical engineering; Nuclear chemistry; Chromatography; Organic chemistry; Pulmonary surfactant","score_opus":0.006103790033126182,"score_gpt":0.20672483096025038,"score_spread":0.20062104092712418,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W3198506156","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99616253,0.0009142655,0.0013685403,0.000031601972,0.000030540104,0.000023659079,0.000120171,0.000065077584,0.0012836725],"genre_scores_gemma":[0.9954652,0.0005052463,0.0017882308,0.000026341502,0.00001276937,0.000018178762,0.00021504443,0.000028220338,0.0019406803],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9997758,0.00003101588,0.00001570656,0.000045232977,0.00007909284,0.000053102493],"domain_scores_gemma":[0.9998746,0.00002585568,0.000022322345,0.000011542904,0.000044970413,0.000020791993],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00017729387,0.0006959533,0.0005900613,0.0005419641,0.00026282578,0.00043864042,0.00026042468,0.00031891614,0.0016136012],"category_scores_gemma":[0.0002462218,0.00016928448,0.00036669493,0.00051271636,0.00030392085,0.00021348536,0.00019064531,0.00020540625,0.00030192785],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000110759654,0.00001955054,0.00012326743,0.00008522377,0.0000067068604,0.000026903946,0.00000993898,0.000067115216,0.9984074,0.000012127564,0.000012607089,0.0011183822],"study_design_scores_gemma":[0.000005338149,0.00028167033,0.0018655913,0.0000041583935,0.000020502635,0.000039117745,0.000017814018,0.0005342203,0.996781,0.000004903487,0.00044169812,0.000003909077],"about_ca_topic_score_codex":0.002700741,"about_ca_topic_score_gemma":0.0032311173,"teacher_disagreement_score":0.002700741,"about_ca_system_score_codex":0.0002452046,"about_ca_system_score_gemma":0.00023836459,"threshold_uncertainty_score":0.0053979754},"labels":[],"label_agreement":null},{"id":"W4200274951","doi":"10.1002/ceat.202100437","title":"Highly Efficient and Low‐Cost Clay‐Based Adsorbent for Glyphosate Removal from Contaminated Water","year":2021,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Pesticide and Herbicide Environmental Studies","field":"Environmental Science","cited_by":15,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Northern British Columbia","funders":"Mitacs; University of Northern British Columbia","keywords":"Bentonite; Adsorption; Sepiolite; Sorption; Zeolite; Langmuir adsorption model; Chemistry; Clay minerals; Correlation coefficient; Contamination; Environmental engineering; Environmental chemistry; Environmental science; Mineralogy; Mathematics; Geology; Geotechnical engineering; Organic chemistry","score_opus":0.004624740663703371,"score_gpt":0.1832360684051451,"score_spread":0.17861132774144176,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4200274951","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99791557,0.00044656274,0.0011956209,0.000019464667,0.0000054790844,0.000012911528,0.00006784074,0.000016225524,0.00032032878],"genre_scores_gemma":[0.99672383,0.00035675685,0.0018720651,0.000009466404,0.000002293504,0.000009036231,0.00013180425,0.0000036112347,0.0008911291],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9998965,0.000015375113,0.0000072430103,0.000014114096,0.000046518748,0.000020244577],"domain_scores_gemma":[0.9999604,0.0000072617954,0.000007747027,0.0000029311332,0.0000130017215,0.0000086628315],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00010098721,0.0002837413,0.00028521512,0.00026660517,0.0001475803,0.00022793635,0.0001657743,0.00024699466,0.00041520136],"category_scores_gemma":[0.00010345559,0.000102718026,0.0002677007,0.00015181878,0.00009688665,0.00014401905,0.00017224556,0.00016101664,0.00017293099],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000058758284,0.00001790337,0.00019168964,0.000053225063,0.0000067254655,0.000025395804,0.0000036591919,0.00019424409,0.99847573,0.000009610907,0.000010310339,0.0009525653],"study_design_scores_gemma":[0.000010355536,0.0003589177,0.0040370077,0.0000046081036,0.00002407523,0.00008895845,0.000017545797,0.0020303745,0.9928294,0.000009183626,0.0005828176,0.0000068538275],"about_ca_topic_score_codex":0.0017288695,"about_ca_topic_score_gemma":0.004319447,"teacher_disagreement_score":0.0017288695,"about_ca_system_score_codex":0.00019971009,"about_ca_system_score_gemma":0.00017904589,"threshold_uncertainty_score":0.0034376383},"labels":[],"label_agreement":null},{"id":"W4210766546","doi":"10.1002/ceat.202100517","title":"Extraction of Sugars and Cellulose Fibers from <i>Cannabis</i> Stems by Hydrolysis, Pulping, and Bleaching","year":2022,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Lignin and Wood Chemistry","field":"Engineering","cited_by":14,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Department of Science and Technology, Ministry of Science and Technology, India","keywords":"Hemicellulose; Cellulose; Lignin; Chemistry; Hydrolysis; Crystallinity; Extraction (chemistry); Yield (engineering); Thermal stability; Nuclear chemistry; Chromatography; Organic chemistry; Materials science; Composite material","score_opus":0.001686976667478158,"score_gpt":0.15776863820925938,"score_spread":0.1560816615417812,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4210766546","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9931583,0.0008278587,0.0030776083,0.000027341843,0.000011878607,0.000043982276,0.00033933352,0.000043383145,0.002470414],"genre_scores_gemma":[0.9911248,0.0006514056,0.005601414,0.00002483842,0.000008454506,0.000029674788,0.0005852048,0.000035443663,0.0019386439],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999946,0.0000051429593,0.000003700627,0.000012973666,0.00001811909,0.000014009588],"domain_scores_gemma":[0.9999522,0.0000061184364,0.000012496354,0.000004453138,0.000010744633,0.000013930166],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00008557786,0.00052016636,0.00022732583,0.00040816763,0.00029667496,0.0002254331,0.00013821875,0.00015057158,0.0008163627],"category_scores_gemma":[0.00009010476,0.00015793546,0.0003324201,0.00031405658,0.00020026613,0.00024434648,0.0001436415,0.00038268007,0.000195872],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000043124266,0.00000549218,0.00014232875,0.000034440964,0.000004458026,0.000036997608,0.0000082932065,0.00005112818,0.9987337,0.00002564649,0.000008993154,0.0009054837],"study_design_scores_gemma":[0.0000032186747,0.000049758408,0.004302672,0.0000068979443,0.000014354986,0.00006715409,0.00001675233,0.00029895018,0.9945332,0.000028815153,0.00067009864,0.000008157063],"about_ca_topic_score_codex":0.0021311399,"about_ca_topic_score_gemma":0.004285802,"teacher_disagreement_score":0.0021311399,"about_ca_system_score_codex":0.00023520981,"about_ca_system_score_gemma":0.0003221667,"threshold_uncertainty_score":0.0042375326},"labels":[],"label_agreement":null},{"id":"W4210857845","doi":"10.1002/ceat.202100365","title":"Synthesis and Characterization of Hausmannite‐Activated Carbon Nanocomposites for Removal of Lead from Aqueous Solutions","year":2022,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Adsorption and biosorption for pollutant removal","field":"Environmental Science","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Ministry of Higher Education","keywords":"Adsorption; Endothermic process; Activated carbon; Chemistry; Aqueous solution; Sorption; Sorbent; Desorption; Nanocomposite; Nuclear chemistry; Kinetics; Inorganic chemistry; Chemical engineering; Physical chemistry","score_opus":0.006729515470049275,"score_gpt":0.17942818189863177,"score_spread":0.1726986664285825,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4210857845","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99356997,0.0005621856,0.004894761,0.00002039212,0.000011773254,0.000026816318,0.00009491709,0.00006196775,0.0007572837],"genre_scores_gemma":[0.9948118,0.00021374068,0.0040078773,0.000009707363,0.000004484696,0.000021908909,0.00008478649,0.0000104840965,0.00083519897],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.9999099,0.000008650786,0.000008560886,0.000018945142,0.00003964316,0.00001422173],"domain_scores_gemma":[0.9999037,0.000018479112,0.000025237772,0.000007806644,0.000027873395,0.000016841057],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00012517543,0.00030151245,0.00016018128,0.0003985241,0.00012400144,0.00020155209,0.00013169329,0.00022135329,0.00035930806],"category_scores_gemma":[0.0001702155,0.00012590254,0.00018915151,0.00014936068,0.000120371784,0.00014854682,0.00009947349,0.00017730553,0.000100638346],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.000017718918,0.0000077740615,0.00007028777,0.000020086842,0.0000027866697,0.000011930777,0.0000047037365,0.00011063875,0.9989662,0.000017107644,0.0000051209354,0.00076556246],"study_design_scores_gemma":[0.0000026245598,0.000058874484,0.0015052446,0.0000012354934,0.0000063193434,0.00002344958,0.000005795367,0.00077990623,0.99734664,0.000007959638,0.00025951458,0.0000023791968],"about_ca_topic_score_codex":0.0007429966,"about_ca_topic_score_gemma":0.0021611247,"teacher_disagreement_score":0.0007429966,"about_ca_system_score_codex":0.00021214088,"about_ca_system_score_gemma":0.00014319445,"threshold_uncertainty_score":0.0015392303},"labels":[],"label_agreement":null},{"id":"W4213385952","doi":"10.1002/ceat.202100503","title":"A Review of Biomass Resources and Thermochemical Conversion Technologies","year":2022,"lang":"en","type":"review","venue":"Chemical Engineering & Technology","topic":"Thermochemical Biomass Conversion Processes","field":"Engineering","cited_by":129,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Saskatchewan","funders":"Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Biomass (ecology); Torrefaction; Biofuel; Renewable energy; Environmental science; Greenhouse gas; Waste management; Pyrolysis; Liquefaction; Renewable resource; Bioenergy; Engineering; Agronomy","score_opus":0.012155802862272903,"score_gpt":0.2267630774054184,"score_spread":0.2146072745431455,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4213385952","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00034972228,0.99579227,0.00031398167,0.00011708528,0.00021975192,0.000008745742,0.0000784633,0.000012874229,0.0031070022],"genre_scores_gemma":[0.0010257611,0.9968299,0.00032922797,0.00008631393,0.00010431394,0.000008257198,0.000093567876,0.0000026020264,0.001520065],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.99978787,0.000019785235,0.00002923427,0.000044133296,0.00009719317,0.00002191386],"domain_scores_gemma":[0.99984586,0.000055848686,0.000031510965,0.0000072458147,0.000048318674,0.000011303289],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0003200382,0.0011420964,0.0012103767,0.0031913465,0.00037352223,0.0011591547,0.0006838119,0.00072952587,0.007854982],"category_scores_gemma":[0.0003592866,0.0004170519,0.0006535561,0.004681078,0.00024352269,0.001455178,0.0005468185,0.0011529998,0.0034731077],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00006315254,0.00013389796,0.00017318616,0.054845538,0.00011483106,0.00023959728,0.00008403665,0.00092513027,0.0096665565,0.0074836933,0.032988615,0.89328176],"study_design_scores_gemma":[0.00000418285,0.00006277558,0.0004288075,0.0034996816,0.00007511769,0.00045171697,0.000034897443,0.00010069839,0.0014162373,0.00126715,0.9926438,0.000015010993],"about_ca_topic_score_codex":0.001097537,"about_ca_topic_score_gemma":0.001517312,"teacher_disagreement_score":0.007854982,"about_ca_system_score_codex":0.00045420614,"about_ca_system_score_gemma":0.0010115085,"threshold_uncertainty_score":0.026277483},"labels":[],"label_agreement":null},{"id":"W4246704254","doi":"10.1002/1521-4125(200109)24:9<913::aid-ceat913>3.3.co;2-8","title":"Flow Patterns in Rheologically Evolving Model Fluids Produced by Hybrid Dual Mixing Systems","year":2001,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Fluid Dynamics and Mixing","field":"Engineering","cited_by":2,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Polytechnique Montréal; Natural Sciences and Engineering Research Council of Canada","funders":"","keywords":"Impeller; Turbine; Agitator; Mechanics; Vortex; Mixing (physics); Froude number; Rushton turbine; Shear thinning; Dimensionless quantity; Flow (mathematics); Thermodynamics; Entrainment (biomusicology); Rotational speed; Viscosity; Materials science; Physics; Chemistry; Classical mechanics","score_opus":0.004199554721337889,"score_gpt":0.1701934178935703,"score_spread":0.1659938631722324,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4246704254","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.9957957,0.00006175662,0.0037854991,0.000016088346,0.000004677571,0.000010194776,0.000031431904,0.000041150044,0.0002535032],"genre_scores_gemma":[0.99356353,0.000051033025,0.00595578,0.000009643497,0.0000036360123,0.000018366616,0.0000730158,0.000010759914,0.00031422472],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.999908,0.000019574509,0.00000874585,0.000019279432,0.000021267713,0.000023252973],"domain_scores_gemma":[0.9997801,0.00005339283,0.00007120562,0.000016248492,0.00003463477,0.00004438604],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00018633196,0.00022575984,0.00028756054,0.0005003201,0.0002569055,0.00061646727,0.00016887531,0.00028276857,0.00035412918],"category_scores_gemma":[0.0005720041,0.00015232919,0.00017251793,0.00024603243,0.0004327765,0.0003105569,0.00028714113,0.00026204437,0.0000922871],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033152697,0.00004635741,0.0016443362,0.000028630575,0.000010473583,0.00010688475,0.00010730207,0.010743211,0.9825806,0.0007063034,0.000044754608,0.0036497526],"study_design_scores_gemma":[0.00011762797,0.0004626676,0.005528581,0.000011673667,0.000024545168,0.00015706562,0.00010872212,0.22306536,0.76872426,0.00062684226,0.001132985,0.000039613118],"about_ca_topic_score_codex":0.00051648146,"about_ca_topic_score_gemma":0.00031196827,"teacher_disagreement_score":0.00061646727,"about_ca_system_score_codex":0.00031251332,"about_ca_system_score_gemma":0.00014085812,"threshold_uncertainty_score":0.0022674203},"labels":[],"label_agreement":null},{"id":"W4398206348","doi":"10.1002/ceat.202400026","title":"Influence of Unzipped Multiwalled Carbon Nanotube Oxides‐Epoxy Paint on the Corrosion Rate of Mild Steel in Marine Environment","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Material Properties and Applications","field":"Materials Science","cited_by":1,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":false,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Western University","funders":"","keywords":"Epoxy; Corrosion; Materials science; Carbon nanotube; Nanotube; Chemical engineering; Composite material; Metallurgy","score_opus":0.006554468367587214,"score_gpt":0.1881769290367214,"score_spread":0.18162246066913418,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4398206348","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.99901426,0.00029557184,0.00042681769,0.000009477504,0.000009957376,0.00000573391,0.00004339107,0.00000965962,0.0001850153],"genre_scores_gemma":[0.9984743,0.00024617347,0.0007836829,0.000010100043,0.0000031245327,0.0000053579115,0.000047197107,0.0000060226084,0.0004239195],"study_design_codex":"bench_or_experimental","study_design_gemma":"bench_or_experimental","domain_scores_codex":[0.99982846,0.000032607262,0.0000137198,0.00003391521,0.00006151228,0.00002979164],"domain_scores_gemma":[0.9997621,0.00005592571,0.00007500678,0.00001405344,0.000065324326,0.000027583666],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00013646808,0.00031520694,0.0002208747,0.00012202313,0.000091903756,0.00018977966,0.00012742946,0.00019458182,0.00044131203],"category_scores_gemma":[0.00040008366,0.00011347282,0.00018914827,0.00010161103,0.0001321445,0.0001425112,0.00012630971,0.00019364475,0.00009834836],"study_design_candidate":"bench_or_experimental","study_design_consensus":"bench_or_experimental","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00010603866,0.000012072639,0.00032861042,0.000040969087,0.0000059520626,0.000032591743,0.000014889021,0.00012673579,0.99834764,0.0000065752515,0.000010283692,0.0009675785],"study_design_scores_gemma":[0.0000016751816,0.0004001597,0.0038961202,0.0000037138498,0.000010553512,0.000018978595,0.000024413288,0.00081796345,0.99458957,0.0000031392499,0.00022985584,0.0000039452825],"about_ca_topic_score_codex":0.0011892625,"about_ca_topic_score_gemma":0.0026576866,"teacher_disagreement_score":0.0011892625,"about_ca_system_score_codex":0.00014390692,"about_ca_system_score_gemma":0.00009379267,"threshold_uncertainty_score":0.0023647547},"labels":[],"label_agreement":null},{"id":"W4402560660","doi":"10.1002/ceat.202300523","title":"Improved Heat Transfer Capabilities of Nanofluids—An Assessment Through CFD Analysis","year":2024,"lang":"en","type":"article","venue":"Chemical Engineering & Technology","topic":"Nanofluid Flow and Heat Transfer","field":"Engineering","cited_by":3,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"University of Alberta","funders":"University of Alberta; Pakistan Institute of Engineering and Applied Sciences","keywords":"Nanofluid; Computational fluid dynamics; Heat transfer; Environmental science; Thermodynamics; Materials science; Nuclear engineering; Engineering; Physics","score_opus":0.005757903108945398,"score_gpt":0.23477239744617667,"score_spread":0.22901449433723128,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4402560660","genre_codex":"empirical","genre_gemma":"empirical","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"empirical","genre_consensus":"empirical","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.955152,0.00068202376,0.039057497,0.00014575524,0.000055766985,0.00006838712,0.00024232302,0.00023872498,0.0043575442],"genre_scores_gemma":[0.9900197,0.00015406485,0.009215077,0.000007980177,0.000003943484,0.000033446075,0.00006817639,0.000010387963,0.00048727306],"study_design_codex":"simulation_or_modeling","study_design_gemma":"simulation_or_modeling","domain_scores_codex":[0.9998976,0.000016821245,0.000008862025,0.000013844962,0.000043036314,0.000019834393],"domain_scores_gemma":[0.9997197,0.0001401439,0.000034330442,0.000017801414,0.00007747685,0.0000106221405],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.00040469805,0.0003096127,0.00030515192,0.00041871026,0.0003495807,0.00046734518,0.0002809,0.00040903897,0.00060296815],"category_scores_gemma":[0.000686843,0.0001927357,0.0005009474,0.00025056727,0.00036335047,0.00054519554,0.00029806586,0.00028772836,0.00010731784],"study_design_candidate":"simulation_or_modeling","study_design_consensus":"simulation_or_modeling","about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00033595107,0.00018733685,0.0072908215,0.00037507212,0.00003177995,0.00021923461,0.00021369783,0.6456986,0.31584665,0.0032890574,0.00055365654,0.02595805],"study_design_scores_gemma":[0.000020643061,0.000118718315,0.0012782571,0.000014030208,0.000012526347,0.00001889109,0.000032267737,0.91754615,0.079896584,0.00021964713,0.00082786917,0.000014423237],"about_ca_topic_score_codex":0.0038826412,"about_ca_topic_score_gemma":0.0019413208,"teacher_disagreement_score":0.0038826412,"about_ca_system_score_codex":0.0006773317,"about_ca_system_score_gemma":0.00043180684,"threshold_uncertainty_score":0.007720113},"labels":[],"label_agreement":null},{"id":"W4403730480","doi":"10.1002/ceat.202400217","title":"Decarbonization of Metallurgy and Steelmaking Industries Using Biochar: A Review","year":2024,"lang":"en","type":"review","venue":"Chemical Engineering & Technology","topic":"Thermochemical Biomass Conversion Processes","field":"Engineering","cited_by":26,"is_retracted":false,"has_abstract":true,"route_ca_aff":true,"route_ca_fund":true,"route_ca_venue":false,"route_about_ca":false,"ca_institutions":"Dalhousie University","funders":"Research Nova Scotia; Natural Sciences and Engineering Research Council of Canada; Canada Research Chairs","keywords":"Steelmaking; Biochar; Coke; Waste management; Coal; Ferroalloy; Greenhouse gas; Fossil fuel; Blast furnace; Environmental science; Metallurgy; Engineering; Materials science","score_opus":0.021386302120541552,"score_gpt":0.26054071810246016,"score_spread":0.2391544159819186,"validation_status":"score_only:v0-immature-baseline","prediction":{"id":"W4403730480","genre_codex":"review","genre_gemma":"review","domain_codex":null,"domain_gemma":null,"model_version":"metacan-v3-hybrid-931329e0061c","genre_candidate":"review","genre_consensus":"review","domain_candidate":null,"domain_consensus":null,"prediction_status":"machine_predicted_unvalidated","genre_scores_codex":[0.00031410903,0.997962,0.00014699505,0.00013484419,0.00012581405,0.000007682687,0.00004334471,0.0000074855698,0.0012577075],"genre_scores_gemma":[0.0010644165,0.9982305,0.00013956528,0.00006995245,0.00003729965,0.0000057598713,0.000032967873,0.0000010681928,0.0004184677],"study_design_codex":"design_other","study_design_gemma":"not_applicable","domain_scores_codex":[0.9998324,0.000020247335,0.000024857025,0.000035772857,0.00006822035,0.000018472474],"domain_scores_gemma":[0.999716,0.0001239226,0.000060447488,0.000008424052,0.00007118211,0.00002002966],"candidate_categories":[],"consensus_categories":[],"category_scores_codex":[0.0004209276,0.0009505357,0.0011876521,0.002545553,0.00035148516,0.0010370738,0.0005992556,0.0007731602,0.004358095],"category_scores_gemma":[0.00056173996,0.000335503,0.0007838327,0.0030953207,0.00023655246,0.0010124765,0.00055257924,0.000873977,0.0013109116],"study_design_candidate":"not_applicable","study_design_consensus":null,"about_ca_topic_candidate":false,"about_ca_topic_consensus":false,"about_ca_system_candidate":false,"about_ca_system_consensus":false,"study_design_scores_codex":[0.00007649527,0.00013376072,0.00032324222,0.14626132,0.00032988793,0.00033509167,0.0001353244,0.0010478948,0.007112459,0.006098898,0.025663415,0.81248224],"study_design_scores_gemma":[0.000009883478,0.00012316332,0.00091440056,0.011962506,0.00041901195,0.000682876,0.00008889575,0.00015437287,0.001590227,0.0014899942,0.98254055,0.000024072493],"about_ca_topic_score_codex":0.0013452952,"about_ca_topic_score_gemma":0.0025953094,"teacher_disagreement_score":0.004358095,"about_ca_system_score_codex":0.00039730323,"about_ca_system_score_gemma":0.0014439299,"threshold_uncertainty_score":0.0145792365},"labels":[],"label_agreement":null}]}