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dc.contributor.authorBilgin, M
dc.contributor.authorKirbaslar, SI
dc.contributor.authorBatr, D
dc.date.accessioned2021-03-05T19:52:31Z
dc.date.available2021-03-05T19:52:31Z
dc.date.issued2005
dc.identifier.citationKirbaslar S., Bilgin M., Batr D., "(Liquid plus liquid) equilibria of (water plus butyric acid plus cyclohexyl acetate) ternary system", JOURNAL OF CHEMICAL THERMODYNAMICS, cilt.37, ss.175-180, 2005
dc.identifier.issn0021-9614
dc.identifier.otherav_d154dba6-c893-4fb9-bba8-39e03f9b2972
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/138368
dc.identifier.urihttps://doi.org/10.1016/j.jct.2004.09.002
dc.description.abstract(Liquid + liquid) equilibrium (LLE) data for the ternary system (water + butyric acid + cyclohexyl acetate) have been determined experimentally at T = (298.15, 308.15 and 318.15) K. Complete phase diagrams were obtained by determining solubility and the tie-line data. Tie-line compositions were correlated by the Othmer-Tobias method. The UNIFAC method was used to predict the phase equilibrium in the system using the interaction parameters determined from experimental data between CH, CH2, CH3, COOH, CH3COO and H2O groups. It is found that UNIFAC group interaction parameters used for LLE could not provide a good prediction. Distribution coefficients and separation factors were evaluated for the immiscibility region. (C) 2004 Elsevier Ltd. All rights reserved.
dc.language.isoeng
dc.subjectMühendislik ve Teknoloji
dc.subjectKimya
dc.subjectTemel Bilimler
dc.subjectTemel Bilimler (SCI)
dc.subjectFizikokimya
dc.subjectKİMYA, FİZİKSEL
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik
dc.subjectTERMODİNAMİK
dc.title(Liquid plus liquid) equilibria of (water plus butyric acid plus cyclohexyl acetate) ternary system
dc.typeMakale
dc.relation.journalJOURNAL OF CHEMICAL THERMODYNAMICS
dc.contributor.department, ,
dc.identifier.volume37
dc.identifier.issue2
dc.identifier.startpage175
dc.identifier.endpage180
dc.contributor.firstauthorID174247


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