Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/53780
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dc.contributor.authorRios-Santana, R.en_US
dc.contributor.authorSosa-Rosario, A.en_US
dc.contributor.authorSusial, P.en_US
dc.contributor.otherRios, Raul-
dc.date.accessioned2019-02-04T18:15:00Z-
dc.date.available2019-02-04T18:15:00Z-
dc.date.issued2011en_US
dc.identifier.issn0104-6632en_US
dc.identifier.urihttp://hdl.handle.net/10553/53780-
dc.description.abstractThis paper reports experimental data of the isobaric vapor-liquid equilibria (VLE) for the mixture methyl acetate + ethanol at 0.3 and 0.7 MPa, determined using a copper still ebulliometer. The activity coefficients obtained from the experimental data were correlated by using different thermodynamic mathematical models. All the binary systems show a positive consistency when subjected to the point-to-point test of Van Ness. The prediction of VLE data obtained with the UNIFAC and ASOG methods has been verified with experimental data.en_US
dc.languageengen_US
dc.publisher0104-6632-
dc.relation.ispartofBrazilian Journal of Chemical Engineeringen_US
dc.sourceBrazilian Journal Of Chemical Engineering[ISSN 0104-6632],v. 28 (2), p. 325-332en_US
dc.subject3303 ingeniería y tecnología químicasen_US
dc.subject.otherVLE isobaric dataen_US
dc.subject.otherActivity coefficienten_US
dc.subject.otherEthanolen_US
dc.subject.otherMethyl esteren_US
dc.titleVapor-liquid equilibrium measurements for the binary system methyl acetate+ethanol at 0.3 and 0.7 MPaen_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1590/S0104-66322011000200017en_US
dc.identifier.scopus79960508870-
dc.identifier.isi000291123900017-
dcterms.isPartOfBrazilian Journal Of Chemical Engineering-
dcterms.sourceBrazilian Journal Of Chemical Engineering[ISSN 0104-6632],v. 28 (2), p. 325-332-
dc.contributor.authorscopusid55884533900-
dc.contributor.authorscopusid36440502500-
dc.contributor.authorscopusid36440519900-
dc.description.lastpage332-
dc.identifier.issue2-
dc.description.firstpage325-
dc.relation.volume28-
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.identifier.wosWOS:000291123900017-
dc.contributor.daisngid1346331-
dc.contributor.daisngid3946930
dc.contributor.daisngid5955493-
dc.contributor.daisngid6079255-
dc.identifier.investigatorRIDM-3753-2014-
dc.utils.revisionen_US
dc.contributor.wosstandardWOS:Susial, P
dc.contributor.wosstandardWOS:Rios-Santana, R
dc.contributor.wosstandardWOS:Sosa-Rosario, A
dc.date.coverdateAbril-Junio 2011
dc.identifier.ulpgces
dc.description.sjr0,401
dc.description.jcr0,637
dc.description.sjrqQ2
dc.description.jcrqQ3
item.fulltextCon texto completo-
item.grantfulltextopen-
crisitem.author.deptIngeniería Química y Tecnología-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.deptIngeniería Química y Tecnología-
crisitem.author.deptDepartamento de Ingeniería de Procesos-
crisitem.author.orcid0000-0002-6960-6487-
crisitem.author.parentorgDepartamento de Ingeniería de Procesos-
crisitem.author.parentorgDepartamento de Ingeniería de Procesos-
crisitem.author.fullNameSusial Badajoz, Pedro-
crisitem.author.fullNameRios Santana, Raul Jorge-
crisitem.author.fullNameSusial Badajoz, Pedro-
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Vapor-liquid equilibrium measurements for the binary system methyl acetate+ethanol at 0.3 and 0.7 MPa
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