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dc.contributor.authorInce, E
dc.contributor.authorKirbaslar, I
dc.date.accessioned2021-03-03T16:17:18Z
dc.date.available2021-03-03T16:17:18Z
dc.date.issued2002
dc.identifier.citationInce E., Kirbaslar I., "Liquid-liquid equilibria of the water-ethanol-dimethyl succinate ternary system", CHINESE JOURNAL OF CHEMICAL ENGINEERING, cilt.10, sa.5, ss.597-603, 2002
dc.identifier.issn1004-9541
dc.identifier.othervv_1032021
dc.identifier.otherav_4365578d-1399-4bab-9fcf-d6e1a128a2cd
dc.identifier.urihttp://hdl.handle.net/20.500.12627/49025
dc.description.abstractLiquid-liquid equilibrium (LLE) data for the ternary system water-ethanol-dimethyl succinate have been determined experimentally at temperatures ranging from 298.15 to 318.15 K at 5 K intervals. Complete phase diagrams were obtained by determining solubility and the tie-line data. Tie-line compositions were correlated by Othmer-Tobias method. The universal quasichemical functional group activity coefficient (UNIFAC) and modified UNIFAC methods were used to predict the phase equilibrium in the system using the interaction parameters determined from experimental data between groups CH3, CH2, OH, CH3COO and H2O. It is found that UNIFAC and modified UNIFAC group interaction parameters used for LLE could not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region.
dc.language.isoeng
dc.subjectMühendislik
dc.subjectMühendislik ve Teknoloji
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.titleLiquid-liquid equilibria of the water-ethanol-dimethyl succinate ternary system
dc.typeMakale
dc.relation.journalCHINESE JOURNAL OF CHEMICAL ENGINEERING
dc.contributor.department, ,
dc.identifier.volume10
dc.identifier.issue5
dc.identifier.startpage597
dc.identifier.endpage603
dc.contributor.firstauthorID166088


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