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dc.contributor.authorKirbaslar, SI
dc.date.accessioned2021-03-04T19:39:38Z
dc.date.available2021-03-04T19:39:38Z
dc.date.issued2006
dc.identifier.citationKirbaslar S., "(Liquid plus liquid) equilibria of the (water plus butyric acid plus dodecanol) ternary system", JOURNAL OF CHEMICAL THERMODYNAMICS, cilt.38, ss.696-700, 2006
dc.identifier.issn0021-9614
dc.identifier.otherav_90db667d-3df6-4767-9311-0e3c95fccabd
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/97757
dc.identifier.urihttps://doi.org/10.1016/j.jct.2005.07.025
dc.description.abstract(Liquid + liquid) equilibrium (LLE) data for the (water + butyric acid + dodecanol) ternary system have been determined experimentally at T = (298.2, 308.2 and 318.2) K. Complete phase diagrams were obtained by determining binodal curves and tie lines. The reliability of the experimental tie lines was confirmed by using the Othmer-Tobias correlation. The UNIFAC method was used to predict the phase equilibrium in the ternary system using the interaction parameters determined from experimental data of CH3, CH2, COOH, OH and H2O functional groups. Distribution coefficients and separation factors were evaluated for the immiscibility region. (C) 2005 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 the (water plus butyric acid plus dodecanol) ternary system
dc.typeMakale
dc.relation.journalJOURNAL OF CHEMICAL THERMODYNAMICS
dc.contributor.departmentİstanbul Üniversitesi , İstanbul Üniversitesi, Mühendislik Fakültesi , Kimya Müh. Bölümü
dc.identifier.volume38
dc.identifier.issue6
dc.identifier.startpage696
dc.identifier.endpage700
dc.contributor.firstauthorID178773


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