Deep learning based combining rule for the estimation of vapor-liquid equilibrium

dc.contributor.authorÖzmen, Atilla
dc.contributor.authorOzmen, Dilek
dc.contributor.authorOzmen, Atilla
dc.date.accessioned2023-10-19T15:12:46Z
dc.date.available2023-10-19T15:12:46Z
dc.date.issued2023
dc.department-temp[Bekri, Sezin] Istanbul Univ Cerrahpasa, Dept Chem Engn, Istanbul, Turkiye; [Ozmen, Dilek] Yalova Univ, Dept Chem Engn, Yalova, Turkiye; [Ozmen, Atilla] Kadir Has Univ, Dept Elect & Elect Engn, Istanbul, Turkiyeen_US
dc.description.abstractVapor-liquid equilibrium (VLE) data plays a vital role in the design, modeling and control of process equipment. In this study, to estimate the VLE data of binary systems, a deep neural network (DNN)-based combining rule was proposed based on the cross-term parameter (a(ij)) in the two-parameter Peng-Robinson cubic equation of state (PR-EoS) combined with the one-parameter classical van der Waals mixing and combining rule (1PVDW). Experimental VLE data of alternative binary refrigerant systems selected from the literature were calculated using both the PR + 1PVDW and the DNN-based model. Vapor phase mole fractions (y(i)) and equilibrium pressures (P) obtained from the proposed DNN-based and PR + 1PVDW models were compared in the terms of average percent deviations. For the DNN-based model, the vapor phase mole fractions give at least as good results as the models in the literature, and also it has been shown that a much better estimate of the equilibrium pressure (P) is obtained when compared with that of the literature. Results obtained using the proposed DNN-based model are presented with tables and graphs. For the equilibrium pressure, while the average percent deviation errors (Delta P/P%) calculated in the literature are less than 7.739, the errors obtained with the proposed DNN-based model are smaller than 3.455. And also, for vapor phase mole fractions, while the maximum error (Delta(y1)/(y1) %) in the literature is obtained as 6.142, the largest error calculated with DNN-based model is 3.545. It has been seen that the proposed DNN-based model makes more practical and less error-prone estimations than the methods in the literature.en_US
dc.identifier.citation0
dc.identifier.doi10.1007/s43153-023-00377-0en_US
dc.identifier.issn0104-6632
dc.identifier.issn1678-4383
dc.identifier.scopus2-s2.0-85168655119en_US
dc.identifier.scopusqualityQ3
dc.identifier.urihttps://doi.org/10.1007/s43153-023-00377-0
dc.identifier.urihttps://hdl.handle.net/20.500.12469/5526
dc.identifier.wosWOS:001063519200001en_US
dc.identifier.wosqualityN/A
dc.khas20231019-WoSen_US
dc.language.isoenen_US
dc.publisherSpringer Heidelbergen_US
dc.relation.ispartofBrazilian Journal of Chemical Engineeringen_US
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanıen_US
dc.rightsinfo:eu-repo/semantics/closedAccessen_US
dc.subjectEquation-Of-StateEn_Us
dc.subjectBinary Interaction ParametersEn_Us
dc.subjectArtificial Neural-NetworksEn_Us
dc.subjectPeng-RobinsonEn_Us
dc.subjectPhase-EquilibriaEn_Us
dc.subjectRefrigerant MixturesEn_Us
dc.subjectPentafluoroethane R125En_Us
dc.subjectCubic EquationsEn_Us
dc.subjectMixing RulesEn_Us
dc.subjectVle DataEn_Us
dc.subjectEquation-Of-State
dc.subjectBinary Interaction Parameters
dc.subjectArtificial Neural-Networks
dc.subjectPeng-Robinson
dc.subjectPhase-Equilibria
dc.subjectRefrigerant Mixtures
dc.subjectVapor-liquid equilibrium (VLE)en_US
dc.subjectPentafluoroethane R125
dc.subjectDeep neural network (DNN)en_US
dc.subjectCubic Equations
dc.subjectPeng-Robinson equation of state (PR-EoS)en_US
dc.subjectMixing Rules
dc.subjectVan der Waals mixing and combining ruleen_US
dc.subjectVle Data
dc.subjectRefrigerant mixturesen_US
dc.titleDeep learning based combining rule for the estimation of vapor-liquid equilibriumen_US
dc.typeArticleen_US
dspace.entity.typePublication
relation.isAuthorOfPublicationcf8f9e05-3f89-4ab6-af78-d0937210fb77
relation.isAuthorOfPublication.latestForDiscoverycf8f9e05-3f89-4ab6-af78-d0937210fb77

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