Publication:
(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.contributor.authorsSENOL, A; ALPTEKIN, G; SAYAR, AA
dc.date.accessioned2022-03-12T16:56:44Z
dc.date.accessioned2026-01-11T06:01:05Z
dc.date.available2022-03-12T16:56:44Z
dc.date.issued1995
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.identifier.doi10.1006/jcht.1995.0053
dc.identifier.issn0021-9614
dc.identifier.urihttps://hdl.handle.net/11424/226830
dc.identifier.wosWOS:A1995RB46700007
dc.language.isoeng
dc.publisherACADEMIC PRESS (LONDON) LTD
dc.relation.ispartofJOURNAL OF CHEMICAL THERMODYNAMICS
dc.rightsinfo:eu-repo/semantics/closedAccess
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.typearticle
dspace.entity.typePublication
oaire.citation.endPage529
oaire.citation.issue5
oaire.citation.startPage525
oaire.citation.titleJOURNAL OF CHEMICAL THERMODYNAMICS
oaire.citation.volume27

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