Identificador persistente para citar o vincular este elemento: http://hdl.handle.net/10553/52116
Campo DC Valoridioma
dc.contributor.authorSoto, Ana
dc.contributor.authorHernández, Pablo
dc.contributor.authorOrtega, J
dc.contributor.otherSoto, Ana
dc.contributor.otherOrtega, Juan
dc.date.accessioned2018-11-25T17:36:09Z-
dc.date.available2018-11-25T17:36:09Z-
dc.date.issued1998
dc.identifier.issn0378-3812
dc.identifier.urihttp://hdl.handle.net/10553/52116-
dc.description.abstractNew experimental VLE data of five binary ethyl methanoate + alkan-1-ol or +alkan-2-ol mixtures are presented which have been obtained isobarically at 101.32 kPa using a dynamic equilibrium apparatus. All systems verify the thermodynamic consistency with one version of the point-to-point test and present a positive deviation from ideality in almost all concentration range, Several equations are used in the treatment of VLE data, and a new correlation employed in this work using temperature-dependent coefficients appear to be also suitable. Activity coefficients calculated from experimental data have been compared with predictions of several group contribution models giving place to a mean error less than 7%. The azeotrope experimentally detected in the mixture ethyl methanoate(1)+ ethanol(2) at x(1) = 0.956, T = 327.2 K was also well predicted by the versions used of UNIFAC. (C) 1998 Elsevier Science B.V. All rights reserved.
dc.publisher0378-3812
dc.relation.ispartofFluid Phase Equilibria
dc.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 146 (1-2), p. 351-370
dc.subject.otherVapor-Liquid-Equilibria
dc.subject.otherButyl Esters Methanoate
dc.subject.otherMethyl Butanoate
dc.subject.otherMixtures
dc.subject.otherDensities
dc.subject.otherEthanol
dc.subject.other1-Propanol
dc.subject.otherCoefficients
dc.subject.other298.15-K
dc.subject.otherFormate
dc.titleExperimental VLE at 101.32 kPa in binary systems composed of ethyl methanoate and alkan-1-ols or alkan-2-ols and treatment of data using a correlation with temperature-dependent parameters
dc.typeinfo:eu-repo/semantics/Articlees
dc.typeArticlees
dc.identifier.scopus0032073238
dc.identifier.isi000074478100026
dcterms.isPartOfFluid Phase Equilibria
dcterms.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 146 (1-2), p. 351-370
dc.contributor.authorscopusid35280670900
dc.contributor.authorscopusid57196517470
dc.contributor.authorscopusid7402623992
dc.description.lastpage370
dc.description.firstpage351
dc.relation.volume146
dc.type2Artículoes
dc.identifier.wosWOS:000074478100026
dc.contributor.daisngid12261
dc.contributor.daisngid6917897
dc.contributor.daisngid170099
dc.identifier.investigatorRIDH-8919-2015
dc.identifier.investigatorRIDN-3335-2014
dc.contributor.wosstandardWOS:Soto, A
dc.contributor.wosstandardWOS:Hernandez, P
dc.contributor.wosstandardWOS:Ortega, J
dc.date.coverdateDiciembre 1998
dc.identifier.ulpgces
dc.description.jcr0,829
dc.description.jcrqQ1
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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