Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/53846
DC FieldValueLanguage
dc.contributor.authorOrtega, Juanen_US
dc.contributor.authorSusial, Pedroen_US
dc.contributor.authorde Alfonso, Casianoen_US
dc.contributor.otherOrtega, Juan-
dc.date.accessioned2019-02-04T18:31:32Z-
dc.date.available2019-02-04T18:31:32Z-
dc.date.issued1990en_US
dc.identifier.issn0021-9568en_US
dc.identifier.urihttp://hdl.handle.net/10553/53846-
dc.description.abstractBinary T-p-c-y vapor-liquid equilibria (VLE) at 101.32 kPa are reported for methyl butanoate + ethanol or 1-propanol. The experimental VLE data of both systems were verified and found to be thermodynamically consistent. The azeotropic coordinates (mole fraction of the ester and temperature) are 0.091 and 350.97 K, for methyl butanoate + ethanol, and 0.409 and 366.77 K, for methyl butanoate + 1-propanol. The data were then compared with those obtained by using the UNIFAC and ASOG models.en_US
dc.languageengen_US
dc.publisher0021-9568-
dc.relation.ispartofJournal of Chemical & Engineering Dataen_US
dc.sourceJournal Of Chemical And Engineering Data[ISSN 0021-9568],v. 35 (2), p. 216-219en_US
dc.subject3303 ingeniería y tecnología químicasen_US
dc.subject.otherIsobaricen_US
dc.subject.otherVapor-liquid equilibriumen_US
dc.subject.otherMethyl butanoateen_US
dc.subject.otherEthanolen_US
dc.subject.other1-propanolen_US
dc.subject.otherBinary systemsen_US
dc.titleIsobaric Vapor-Liquid Equilibrium of Methyl Butanoate with Ethanol and 1-Propanol Binary Systemsen_US
dc.typeinfo:eu-repo/semantics/articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1021/je00060a037en_US
dc.identifier.scopus0025414921-
dc.identifier.isiA1990CZ76800037-
dcterms.isPartOfJournal Of Chemical And Engineering Data-
dcterms.sourceJournal Of Chemical And Engineering Data[ISSN 0021-9568],v. 35 (2), p. 216-219-
dc.contributor.authorscopusid7402623992-
dc.contributor.authorscopusid55884533900-
dc.contributor.authorscopusid7801359825-
dc.description.lastpage219-
dc.identifier.issue2-
dc.description.firstpage216-
dc.relation.volume35-
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.identifier.wosWOS:A1990CZ76800037-
dc.contributor.daisngid170099-
dc.contributor.daisngid25552911-
dc.contributor.daisngid1846659-
dc.identifier.investigatorRIDN-3335-2014-
dc.utils.revisionen_US
dc.identifier.ulpgces
dc.description.scieSCIE
item.grantfulltextnone-
item.fulltextSin 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.deptGIR Ingeniería Química y Tecnología-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0002-8304-2171-
crisitem.author.orcid0000-0002-6719-3084-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.parentorgDepartamento de Ingeniería de Procesos-
crisitem.author.fullNameOrtega Saavedra, Juan-
crisitem.author.fullNameSusial Badajoz, Pedro-
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