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dc.contributor.authorKirbaslar, S. I.
dc.date.accessioned2021-03-03T14:42:14Z
dc.date.available2021-03-03T14:42:14Z
dc.date.issued2006
dc.identifier.citationKirbaslar S. I. , "Liquid-liquid equilibria of the water plus butyric acid plus decanol ternary system", BRAZILIAN JOURNAL OF CHEMICAL ENGINEERING, cilt.23, sa.3, ss.365-374, 2006
dc.identifier.issn0104-6632
dc.identifier.othervv_1032021
dc.identifier.otherav_3b03bf88-e827-4f25-84e0-cb20adcc35c5
dc.identifier.urihttp://hdl.handle.net/20.500.12627/43637
dc.identifier.urihttps://doi.org/10.1590/s0104-66322006000300010
dc.description.abstractLiquid-liquid equilibrium (LLE) data for the water + butyric acid + decanol ternary system were determined experimentally at temperatures of 298.15, 308.15 and 318.15 K. Complete phase diagrams were obtained by determining the solubility curve and the tie lines. The reliability of the experimental tie line data was confirmed with the Othmer-Tobias correlation. The UNIFAC method was used to predict the phase equilibrium of the system using the interaction parameters for groups CH3, CH2, COOH, OH and H2O determined experimentally. Distribution coefficients and separation factors were evaluated for the immiscibility region.
dc.language.isoeng
dc.subjectMühendislik
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectMühendislik ve Teknoloji
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.titleLiquid-liquid equilibria of the water plus butyric acid plus decanol ternary system
dc.typeMakale
dc.relation.journalBRAZILIAN JOURNAL OF CHEMICAL ENGINEERING
dc.contributor.departmentİstanbul Üniversitesi , İstanbul Üniversitesi, Mühendislik Fakültesi , Kimya Müh. Bölümü
dc.identifier.volume23
dc.identifier.issue3
dc.identifier.startpage365
dc.identifier.endpage374
dc.contributor.firstauthorID48807


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