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dc.contributor.authorGilani, H. Ghanadzadeh
dc.contributor.authorGok, Asli
dc.contributor.authorKirbaslar, S. Ismail
dc.contributor.authorUslu, Hasan
dc.date.accessioned2021-03-05T11:36:26Z
dc.date.available2021-03-05T11:36:26Z
dc.date.issued2011
dc.identifier.citationGok A., Kirbaslar S. I. , Uslu H., Gilani H. G. , "Liquid-liquid equilibria of (water plus butyric acid plus diethyl succinate or diethyl glutarate or diethyl adipate) ternary systems", FLUID PHASE EQUILIBRIA, cilt.303, ss.71-75, 2011
dc.identifier.issn0378-3812
dc.identifier.otherav_a8f1eaf8-993d-4e5e-8b34-ca024a668cea
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/112893
dc.identifier.urihttps://doi.org/10.1016/j.fluid.2011.01.012
dc.description.abstractLiquid-liquid equilibrium (LLE) data of the solubility (binodal) curves and tie-line end compositions were examined for mixtures of [(water (1)+ butyric acid (2) + diethyl succinate or diethyl glutarate or diethyl adipate (3)1 at 298.2 K and 101.3 +/- 0.7 kPa. The relative mutual solubility of butyric acid is higher in the diethyl succinate or diethyl glutarate or diethyl adipate layers than water layers. The consistency of the experimental tie-lines was determined through the Othmer-Tobias correlation equation. The LLE data were correlated with NRTL model, indicating the reliability of the NRTL equations for these ternary systems. The best results were achieved with the NRTL equation, using non-randomness parameter (alpha = 0.3) for the correlation. Distribution coefficients and separation factors were measured to evaluate the extracting capability of the solvents. (C) 2011 Elsevier B.V. All rights reserved.
dc.language.isoeng
dc.subjectFizikokimya
dc.subjectTemel Bilimler
dc.subjectMühendislik ve Teknoloji
dc.subjectTemel Bilimler (SCI)
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectKimya
dc.subjectKİMYA, FİZİKSEL
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectMühendislik
dc.subjectTERMODİNAMİK
dc.titleLiquid-liquid equilibria of (water plus butyric acid plus diethyl succinate or diethyl glutarate or diethyl adipate) ternary systems
dc.typeMakale
dc.relation.journalFLUID PHASE EQUILIBRIA
dc.contributor.departmentBeykent Üniversitesi , ,
dc.identifier.volume303
dc.identifier.issue1
dc.identifier.startpage71
dc.identifier.endpage75
dc.contributor.firstauthorID48736


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