Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/52119
DC FieldValueLanguage
dc.contributor.authorGonzález, Eduardoen_US
dc.contributor.authorOrtega, Juanen_US
dc.contributor.otherOrtega, Juan-
dc.contributor.otherGonzalez-Diaz, Eduardo-
dc.date.accessioned2018-11-25T17:37:38Z-
dc.date.available2018-11-25T17:37:38Z-
dc.date.issued1996en_US
dc.identifier.issn0378-3812en_US
dc.identifier.urihttp://hdl.handle.net/10553/52119-
dc.description.abstractVapor-liqiuid equilibrium data for the binaries of butyl alkanoates (from methanoate to butanoate) + butan-2-ol were determined at 101.32 kPa in a small-capacity ebulliometer. The four systems studied were found to be thermodynamically consistent by the point-to-point test and they presented a positive deviation from ideality. The activity coefficients and the magnitudes obtained directly from experimentation were correlated using a suitable equation. An azeotrope was found for the mixture x(1)butyl methanoate + x(2)butan-2-ol at x(1) = 0.248, T = 371.0 K. The application of the ASOG and UNIFAC models to predict the isobaric VLE data and the comparison between the different cases considered are also discussed.en_US
dc.languagespaen_US
dc.publisher0378-3812
dc.relation.ispartofFluid Phase Equilibriaen_US
dc.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 124, p. 161-175en_US
dc.subject.otherUnifac Group Contribution
dc.subject.otherActivity-Coefficients
dc.subject.otherButanoate
dc.subject.otherEthanol
dc.titleVapor-liquid equilibria at 101.32 kPa in mixtures formed by the first four butyl alkanoates and butan-2-olen_US
dc.typeinfo:eu-repo/semantics/Articleen_US
dc.typeArticleen_US
dc.identifier.scopus0030233484-
dc.identifier.isiA1996VU55700012-
dcterms.isPartOfFluid Phase Equilibria
dcterms.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 124 (1-2), p. 161-175
dc.contributor.authorscopusid55682655415-
dc.contributor.authorscopusid7402623992-
dc.description.lastpage175en_US
dc.description.firstpage161en_US
dc.relation.volume124en_US
dc.type2Artículoen_US
dc.identifier.wosWOS:A1996VU55700012-
dc.contributor.daisngid3150887-
dc.contributor.daisngid2090863-
dc.contributor.daisngid170099-
dc.identifier.investigatorRIDN-3335-2014-
dc.identifier.investigatorRIDNo ID-
dc.contributor.wosstandardWOS:Gonzalez, E-
dc.contributor.wosstandardWOS:Ortega, J-
dc.date.coverdateSeptiembre 1996en_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.orcid0000-0002-8304-2171-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.fullNameOrtega Saavedra, Juan-
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