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Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon plus toluene plus gamma-butyrolactone) at 298.2 K and atmospheric pressure

dc.contributor.authorSevgili, Lutfullah Muhammed
dc.date.accessioned2021-03-06T08:45:04Z
dc.date.available2021-03-06T08:45:04Z
dc.date.issued2010
dc.identifier.citationSevgili L. M. , "Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon plus toluene plus gamma-butyrolactone) at 298.2 K and atmospheric pressure", FLUID PHASE EQUILIBRIA, cilt.287, ss.106-110, 2010
dc.identifier.issn0378-3812
dc.identifier.otherav_e27c3352-599f-415e-9ceb-daab0993dea0
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/149077
dc.identifier.urihttps://doi.org/10.1016/j.fluid.2009.09.019
dc.description.abstractLiquid-liquid equilibrium (LLE) data for three ternary systems consisting of {n-heptane or n-hexane or cyclohexane (I) + toluene (2) + gamma-butyrolactone (3)} were measured at 298.2 K and atmospheric pressure. The reliability of the experimental tie-line data was verified by using the Othmer-Tobias correlation. Distribution coefficients, separation factors and selectivity were evaluated for the immiscibility region. The experimental tie-line data were correlated by the UNIQUAC equation and also predicted with the UNIFAC model. The calculated results were compared with the experimental data. Better agreement with the experimental data was obtained by the UNIQUAC equation. The UNIFAC model does not provide reasonable correlations. (C) 2009 Elsevier B.V. All rights reserved.
dc.language.isoeng
dc.subjectTemel Bilimler (SCI)
dc.subjectTERMODİNAMİK
dc.subjectMühendislik
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectKİMYA, FİZİKSEL
dc.subjectMühendislik ve Teknoloji
dc.subjectTemel Bilimler
dc.subjectFizikokimya
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectKimya
dc.titleLiquid phase equilibria for mixtures of (an aliphatic hydrocarbon plus toluene plus gamma-butyrolactone) at 298.2 K and atmospheric pressure
dc.typeMakale
dc.relation.journalFLUID PHASE EQUILIBRIA
dc.contributor.departmentİstanbul Üniversitesi , Mühendislik Fakültesi , Kimya Mühendisliği
dc.identifier.volume287
dc.identifier.issue2
dc.identifier.startpage106
dc.identifier.endpage110
dc.contributor.firstauthorID70182


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