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dc.contributor.authorSenol, A
dc.date.accessioned2021-03-06T08:39:24Z
dc.date.available2021-03-06T08:39:24Z
dc.identifier.citationSenol A., "Liquid-liquid equilibria for the system (water plus carboxylic acid plus chloroform): Thermodynamic modeling", FLUID PHASE EQUILIBRIA, cilt.243, ss.51-56, 2006
dc.identifier.issn0378-3812
dc.identifier.othervv_1032021
dc.identifier.otherav_e2053893-1fe0-471f-891e-cc64376e85f6
dc.identifier.urihttp://hdl.handle.net/20.500.12627/148790
dc.identifier.urihttps://doi.org/10.1016/j.fluid.2006.02.017
dc.description.abstractLiquid-liquid equilibrium (LLE) data of the solubility curves and tie-line end compositions are presented for mixtures of [water (1) + acetic acid, or pyruvic acid, or valeric acid (2) + chloroform (3)] at T = 293.15 K and atmospheric pressure. Among the studied ternary systems, the largest separation factors give valeric acid. A solvation energy relation (SERLAS) has been used to estimate the liquid-liquid equilibria of associated systems containing a protic solvent. The tie-lines were also predicted through the UNIFAC-original model. The reliability of both models has been analyzed against the LLE data with respect to the distribution ratio and separation factor. SERLAS matches LLE data relatively accurately, yielding a mean error of 18.5% for all the systems considered. (c) 2006 Elsevier B.V. All rights reserved.
dc.language.isoeng
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectFizikokimya
dc.subjectTemel Bilimler
dc.subjectMühendislik ve Teknoloji
dc.subjectTemel Bilimler (SCI)
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectKimya
dc.subjectKİMYA, FİZİKSEL
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik
dc.subjectTERMODİNAMİK
dc.titleLiquid-liquid equilibria for the system (water plus carboxylic acid plus chloroform): Thermodynamic modeling
dc.typeMakale
dc.relation.journalFLUID PHASE EQUILIBRIA
dc.contributor.department, ,
dc.identifier.volume243
dc.identifier.startpage51
dc.identifier.endpage56
dc.contributor.firstauthorID178491


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