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Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/53782
DC FieldValueLanguage
dc.contributor.authorSosa-Rosario, A.en_US
dc.contributor.authorRios-Santana, R.en_US
dc.contributor.authorSusial, P.en_US
dc.contributor.otherRios, Raul-
dc.date.accessioned2019-02-04T18:15:28Z-
dc.date.available2019-02-04T18:15:28Z-
dc.date.issued2010en_US
dc.identifier.issn1004-9541en_US
dc.identifier.urihttp://hdl.handle.net/10553/53782-
dc.description.abstractA new dynamic ebulliometer is used to determine vapor-liquid equilibrium (VLE) data experimentally. In the equipment, both phases are recirculated. Its operation is a consequence of the Cotrell pump effect produced when the mixture is heated in a double-walled inverted vessel. The reliability of the apparatus is tested with the mixtures studied previously by various authors. VLE data for the binary systems of methyl acetate + methanol and the methyl acetate + ethanol at 0.5 MPa are determined. The experimental data are confirmed with the point-to-point test of van Ness, applying the Fortran program of Frendslund et al. In addition, the experimental results are compared with the UNIFAC (including different versions) and ASOG prediction models.en_US
dc.languageengen_US
dc.publisher1004-9541-
dc.relation.ispartofChinese Journal of Chemical Engineeringen_US
dc.sourceChinese Journal Of Chemical Engineering[ISSN 1004-9541],v. 18 (6), p. 1000-1007en_US
dc.subject3303 ingeniería y tecnología químicasen_US
dc.subject.otherVapor-liquid equilibriumen_US
dc.subject.otherVapor-liquid equilibrium apparatusen_US
dc.subject.otherVapor pressureen_US
dc.subject.otherAlcoholen_US
dc.titleVapour-liquid equilibrium with a new ebulliometer: Ester + alcohol system at 0.5 MPaen_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1016/S1004-9541(09)60159-2en_US
dc.identifier.scopus78650813338-
dc.identifier.isi000286172200016-
dcterms.isPartOfChinese Journal Of Chemical Engineering-
dcterms.sourceChinese Journal Of Chemical Engineering[ISSN 1004-9541],v. 18 (6), p. 1000-1007-
dc.contributor.authorscopusid55884533900-
dc.contributor.authorscopusid36440519900-
dc.contributor.authorscopusid36440502500-
dc.description.lastpage1007-
dc.identifier.issue6-
dc.description.firstpage1000-
dc.relation.volume18-
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.identifier.wosWOS:000286172200016-
dc.contributor.daisngid1346331-
dc.contributor.daisngid6079255-
dc.contributor.daisngid5955493-
dc.contributor.daisngid3946930
dc.identifier.investigatorRIDM-3753-2014-
dc.utils.revisionSíen_US
dc.contributor.wosstandardWOS:Susial, P
dc.contributor.wosstandardWOS:Sosa-Rosario, A
dc.contributor.wosstandardWOS:Rios-Santana, R
dc.date.coverdateDiciembre 2010
dc.identifier.ulpgcSíes
dc.description.jcr0,901
dc.description.jcrqQ3
dc.description.scieSCIE
item.grantfulltextnone-
item.fulltextSin texto completo-
crisitem.author.deptGIR Ingeniería Química y Tecnología-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0002-6719-3084-
crisitem.author.orcid0000-0002-6960-6487-
crisitem.author.orcid0000-0002-6960-6487-
crisitem.author.parentorgDepartamento de Ingeniería de Procesos-
crisitem.author.fullNameSusial Badajoz, Pedro-
crisitem.author.fullNameRios Santana, Raul Jorge-
crisitem.author.fullNameRios Santana, Raul Jorge-
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