نمایش مختصر رکورد

dc.contributor.authorOrouj, Rezaen_US
dc.contributor.authorAbolghasemi, Hoseinen_US
dc.contributor.authorVatani, Zohaen_US
dc.contributor.authorMahdavian, Mohammaden_US
dc.date.accessioned1399-07-09T05:33:23Zfa_IR
dc.date.accessioned2020-09-30T05:33:23Z
dc.date.available1399-07-09T05:33:23Zfa_IR
dc.date.available2020-09-30T05:33:23Z
dc.date.issued2011-04-01en_US
dc.date.issued1390-01-12fa_IR
dc.identifier.citationOrouj, Reza, Abolghasemi, Hosein, Vatani, Zoha, Mahdavian, Mohammad. (2011). New Method for Calculation Mixing Rule and Modification Semi-empirical Models for Solubility Modeling in Supercritical Solvent. Journal of Chemical and Petroleum Engineering, 44(1), 63-72. doi: 10.22059/jchpe.2011.22349en_US
dc.identifier.issn2423-673X
dc.identifier.issn2423-6721
dc.identifier.urihttps://dx.doi.org/10.22059/jchpe.2011.22349
dc.identifier.urihttps://jchpe.ut.ac.ir/article_22349.html
dc.identifier.urihttps://iranjournals.nlai.ir/handle/123456789/284293
dc.description.abstractThe critical properties of a solute are required for modeling of the solubility by the equation of state. For many compounds, the critical properties are not available. So, group contribution method is utilized as a common method to estimate these properties. But, it leads to the consecutive errors in calculations of the solubility modeling. In this study, Soave-Redlish-Kowang (SRK) and Peng-Robinson equation of states with Huran-Vidal mixing rules were used for modeling of the solubility. A new method for evaluating of C2 (Huran-Vidal mixing rule parameter) is recommended as a function of temperature and pressure. For solubility modeling by semi-empirical correlation, the new forms of Chrastil and Mendez equations were used. Finally, the modeling of solubility for 20 compounds by these methods has been investigated. Results show that the AARD% for the models with semi-empirical equations (Charstil, Aguilera, Gordillo, Mendez, modified Charstil and modified Mendez) are 12.07, 11.71, 34.89, 19.89, 11.17 and 15.70 respectively; and for SRK, PR EOS are 14, 19.85 respectively.en_US
dc.format.extent205
dc.format.mimetypeapplication/pdf
dc.languageEnglish
dc.language.isoen_US
dc.publisherUniversity of Tehranen_US
dc.relation.ispartofJournal of Chemical and Petroleum Engineeringen_US
dc.relation.isversionofhttps://dx.doi.org/10.22059/jchpe.2011.22349
dc.titleNew Method for Calculation Mixing Rule and Modification Semi-empirical Models for Solubility Modeling in Supercritical Solventen_US
dc.typeTexten_US
dc.contributor.departmentسازمان انرژی اتمیen_US
dc.contributor.departmentمهندسی شیمیen_US
dc.contributor.departmentمهندسی شیمیen_US
dc.contributor.departmentمهندسی شیمیen_US
dc.citation.volume44
dc.citation.issue1
dc.citation.spage63
dc.citation.epage72


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