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dc.contributor.authorSENOL, A
dc.contributor.authorSAYAR, AA
dc.contributor.authorALPTEKIN, G
dc.date.accessioned2021-03-04T12:12:50Z
dc.date.available2021-03-04T12:12:50Z
dc.date.issued1995
dc.identifier.citationSENOL A., ALPTEKIN G., SAYAR A., "(LIQUID PLUS LIQUID) EQUILIBRIA OF SOME (WATER PLUS TETRAHYDROFURAN PLUS SOLVENT) TERNARIES AT THE TEMPERATURE (293.2+/-0.1) K AND PRESSURE (101.3+/-0.7) KPA", JOURNAL OF CHEMICAL THERMODYNAMICS, cilt.27, sa.5, ss.525-529, 1995
dc.identifier.issn0021-9614
dc.identifier.otherav_762915aa-e50b-478f-84d6-57b4f71567c4
dc.identifier.othervv_1032021
dc.identifier.urihttp://hdl.handle.net/20.500.12627/81154
dc.identifier.urihttps://doi.org/10.1006/jcht.1995.0053
dc.description.abstractSolubility curve and tie-line determinations for (water + tetrahydrofuran + cyclohexyl ethanoate), (water + tetrahydrofuran + 1,2-dichloroethane), (water + tetrahydrofuran + cyclohexanone), (water + tetrahydrofuran + 1-octanol), and (water + tetrahydrofuran + phenylmethanol) ternaries at the temperature (293.2 +/- 0.1) K and pressure (101.3 +/- 0.7) kPa are reported. A selectivity diagram on a solvent-free basis was used as comparative performance tests for the investigated extracting agents. It was found that cyclohexyl ethanoate represents the best performance among the studied solvents, if a high-boiling separating agent is to be considered.
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 SOME (WATER PLUS TETRAHYDROFURAN PLUS SOLVENT) TERNARIES AT THE TEMPERATURE (293.2+/-0.1) K AND PRESSURE (101.3+/-0.7) KPA
dc.typeMakale
dc.relation.journalJOURNAL OF CHEMICAL THERMODYNAMICS
dc.contributor.department, ,
dc.identifier.volume27
dc.identifier.issue5
dc.identifier.startpage525
dc.identifier.endpage529
dc.contributor.firstauthorID116157


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