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dc.contributor.authorSenol, A
dc.date.accessioned2021-03-03T15:53:23Z
dc.date.available2021-03-03T15:53:23Z
dc.date.issued2004
dc.identifier.citationSenol A., "Liquid-liquid equilibria for systems of (water plus carboxylic acid plus methylcyclohexanol) at 293.15 k: Modeling considerations", JOURNAL OF CHEMICAL AND ENGINEERING DATA, cilt.49, sa.6, ss.1815-1820, 2004
dc.identifier.issn0021-9568
dc.identifier.otherav_414e6c96-aae5-4398-9746-beef097ee532
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/47633
dc.identifier.urihttps://doi.org/10.1021/je0497606
dc.description.abstractLiquid-liquid equilibrium data of the solubility (binodal) curves and tie-line end compositions are presented for mixtures of [water (1) + formic acid, or acetic acid, or propanoic acid, or pentanoic acid (2) + methylcyclohexanol (3)] at T = 293.15 K and P = 101.3 +/- 0.7 kPa. A log-basis approach SERLAS (solvation energy relation for liquid associated system) has been proposed to estimate the properties and liquid-liquid equilibria (LLE) of associated systems containing proton-donating and -accepting and polar components capable of a physical interaction through hydrogen bonding or dipole-dipole interaction. The tie lines were also correlated using the UNIFAC-original model. The reliability of the models has been analyzed against the LLE data with respect to the distribution ratio and separation factor. The proposed model appears to be an improvement in data fit for the ternary systems, yielding a mean error of 22% for all of the systems considered.
dc.language.isoeng
dc.subjectTemel Bilimler (SCI)
dc.subjectTERMODİNAMİK
dc.subjectMühendislik
dc.subjectMühendislik, Bilişim ve Teknoloji (ENG)
dc.subjectKİMYA, MULTİDİSİPLİNER
dc.subjectKimya
dc.subjectMÜHENDİSLİK, KİMYASAL
dc.subjectKimya Mühendisliği ve Teknolojisi
dc.subjectBiyokimya
dc.subjectAlkoloidler
dc.subjectTemel Bilimler
dc.subjectMühendislik ve Teknoloji
dc.titleLiquid-liquid equilibria for systems of (water plus carboxylic acid plus methylcyclohexanol) at 293.15 k: Modeling considerations
dc.typeMakale
dc.relation.journalJOURNAL OF CHEMICAL AND ENGINEERING DATA
dc.contributor.department, ,
dc.identifier.volume49
dc.identifier.issue6
dc.identifier.startpage1815
dc.identifier.endpage1820
dc.contributor.firstauthorID172985


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