Deep Learning Based Combining Rule for the Estimation of Vapor-Liquid Equilibrium

dc.contributor.author Bekri, Sezin
dc.contributor.author Özmen, Atilla
dc.contributor.author Ozmen, Dilek
dc.contributor.author Ozmen, Atilla
dc.contributor.other Electrical-Electronics Engineering
dc.date.accessioned 2023-10-19T15:12:46Z
dc.date.available 2023-10-19T15:12:46Z
dc.date.issued 2023
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, Turkiye en_US
dc.description.abstract Vapor-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.citationcount 0
dc.identifier.doi 10.1007/s43153-023-00377-0 en_US
dc.identifier.issn 0104-6632
dc.identifier.issn 1678-4383
dc.identifier.scopus 2-s2.0-85168655119 en_US
dc.identifier.scopusquality Q3
dc.identifier.uri https://doi.org/10.1007/s43153-023-00377-0
dc.identifier.uri https://hdl.handle.net/20.500.12469/5526
dc.identifier.wos WOS:001063519200001 en_US
dc.khas 20231019-WoS en_US
dc.language.iso en en_US
dc.publisher Springer Heidelberg en_US
dc.relation.ispartof Brazilian Journal of Chemical Engineering en_US
dc.relation.publicationcategory Makale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı en_US
dc.rights info:eu-repo/semantics/closedAccess en_US
dc.scopus.citedbyCount 1
dc.subject Equation-Of-State
dc.subject Binary Interaction Parameters
dc.subject Artificial Neural-Networks
dc.subject Peng-Robinson
dc.subject Equation-Of-State En_Us
dc.subject Phase-Equilibria
dc.subject Binary Interaction Parameters En_Us
dc.subject Artificial Neural-Networks En_Us
dc.subject Refrigerant Mixtures
dc.subject Peng-Robinson En_Us
dc.subject Pentafluoroethane R125
dc.subject Phase-Equilibria En_Us
dc.subject Refrigerant Mixtures En_Us
dc.subject Cubic Equations
dc.subject Pentafluoroethane R125 En_Us
dc.subject Mixing Rules
dc.subject Cubic Equations En_Us
dc.subject Vapor-liquid equilibrium (VLE) en_US
dc.subject Deep neural network (DNN) en_US
dc.subject Mixing Rules En_Us
dc.subject Peng-Robinson equation of state (PR-EoS) en_US
dc.subject Vle Data
dc.subject Van der Waals mixing and combining rule en_US
dc.subject Vle Data En_Us
dc.subject Refrigerant mixtures en_US
dc.title Deep Learning Based Combining Rule for the Estimation of Vapor-Liquid Equilibrium en_US
dc.type Article en_US
dc.wos.citedbyCount 1
dspace.entity.type Publication
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