Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/52123
DC FieldValueLanguage
dc.contributor.authorGonzález, Eduardo-
dc.contributor.authorOrtega, Juan-
dc.contributor.otherOrtega, Juan-
dc.contributor.otherGonzalez-Diaz, Eduardo-
dc.date.accessioned2018-11-25T17:39:35Z-
dc.date.available2018-11-25T17:39:35Z-
dc.date.issued1995-
dc.identifier.issn0021-9568-
dc.identifier.urihttp://hdl.handle.net/10553/52123-
dc.description.abstractVapor-liquid equilibrium and densities at 101.32 kPa have been determined for the binary systems formed by four butyl esters (from methanoate to butanoate) with ethanol. The four systems exhibit positive deviations from ideal behavior, and all data (p-T-x-y) were found to be thermodynamically consistent, The activity coefficients and the dimensionless function G(E)/RT of the solution were correlated with its concentration by different equations. An azeotrope was found in the mixture butyl methanoate (1) + ethanol (2) at T = 350.9 K and x(1) = y(1) = 0.088. The group contribution models ASOG and modified UNIFAC gave fair predictions.
dc.publisher0021-9568-
dc.relation.ispartofJournal of Chemical & Engineering Data-
dc.sourceJournal of Chemical and Engineering Data[ISSN 0021-9568],v. 40, p. 1178-1183-
dc.subject.otherUnifac Group-Contribution
dc.subject.otherExcess Molar Volumes
dc.subject.otherEthyl-Acetate +
dc.subject.otherActivity-Coefficients
dc.subject.otherMethyl Butanoate
dc.subject.otherBinary-Systems
dc.subject.otherPrediction
dc.subject.otherMixtures
dc.subject.otherModel
dc.subject.otherExtension
dc.titleDensities and Isobaric Vapor-Liquid Equilibria of Butyl Esters (Methanoate to Butanoate) with Ethanol at 101.32 kPa-
dc.typeinfo:eu-repo/semantics/Article-
dc.typeArticle-
dc.identifier.doi10.1021/je00022a004
dc.identifier.scopus5244364940-
dc.identifier.isiA1995TF02800004-
dcterms.isPartOfJournal Of Chemical And Engineering Data-
dcterms.sourceJournal Of Chemical And Engineering Data[ISSN 0021-9568],v. 40 (6), p. 1178-1183-
dc.contributor.authorscopusid55682655415-
dc.contributor.authorscopusid7402623992-
dc.description.lastpage1183-
dc.identifier.issue6-
dc.description.firstpage1178-
dc.relation.volume40-
dc.type2Artículo-
dc.identifier.wosWOS:A1995TF02800004-
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.coverdateNoviembre 1995
dc.identifier.ulpgces
dc.description.scieSCIE
item.fulltextSin texto completo-
item.grantfulltextnone-
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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