Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/53823
DC FieldValueLanguage
dc.contributor.authorOrtega, Juanen_US
dc.contributor.authorPeña, Juan A.en_US
dc.contributor.otherOrtega, Juan-
dc.date.accessioned2019-02-04T18:26:20Z-
dc.date.available2019-02-04T18:26:20Z-
dc.date.issued1994en_US
dc.identifier.issn0021-9592en_US
dc.identifier.urihttp://hdl.handle.net/10553/53823-
dc.description.abstractThe T–x–y data for binary mixtures composed of methyl acetate + (1-chloropentane or 1-chlorohexane) and ethyl acetate + (1-chloropentane or 1-chlorohexane) have been measured ebulliometrically at 101.32 kPa using a dynamic method. In thermodynamic calculations using these data, the vapor phase was considered to be non-ideal, and the four systems studied exhibit positive deviations from Raoult’s law. The activity coefficients and vapor phase compositions have been compared with those predicted by using UNIFAC and ASOG models.en_US
dc.languageengen_US
dc.relation.ispartofJournal of Chemical Engineering of Japanen_US
dc.sourceJournal of Chemical Engineering of Japan [ISSN 0021-9592], v. 27 (3), p. 351-356 (Junio 1994)en_US
dc.subject331005 Ingeniería de procesosen_US
dc.subject2213 Termodinámicaen_US
dc.subject.otherVapor Liquid Equilibriumen_US
dc.subject.otherChloroalkanesen_US
dc.subject.otherEstersen_US
dc.titleVapor-Liquid Equilibria of Methyl or Ethyl Acetate with 1-Chloropentane or 1-Chlorohexane at 101.32 Kpa Pressureen_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1252/jcej.27.351en_US
dc.identifier.scopus85010140250-
dc.identifier.isiA1994NU58900016-
dcterms.isPartOfJournal Of Chemical Engineering Of Japan-
dcterms.sourceJournal Of Chemical Engineering Of Japan[ISSN 0021-9592],v. 27 (3), p. 351-356-
dc.contributor.authorscopusid7402623992-
dc.contributor.authorscopusid24459076900-
dc.description.lastpage356en_US
dc.identifier.issue3-
dc.description.firstpage351en_US
dc.relation.volume27en_US
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.identifier.wosWOS:A1994NU58900016-
dc.contributor.daisngid170099-
dc.contributor.daisngid28306301-
dc.contributor.daisngid832769-
dc.identifier.investigatorRIDN-3335-2014-
dc.utils.revisionen_US
dc.contributor.wosstandardWOS:ORTEGA, J-
dc.contributor.wosstandardWOS:PENA, JA-
dc.date.coverdateJunio 1994en_US
dc.identifier.ulpgcen_US
dc.contributor.buulpgcBU-INGen_US
dc.description.scieSCIE-
item.grantfulltextopen-
item.fulltextCon texto completo-
crisitem.author.deptGIR IDeTIC: División de Ingeniería Térmica e Instrumentación-
crisitem.author.deptIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0002-8304-2171-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.fullNameOrtega Saavedra, Juan-
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