Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/49709
DC FieldValueLanguage
dc.contributor.authorOrtega, Juan
dc.contributor.authorEspiau, Fernando
dc.contributor.authorDieppa, Ruth
dc.contributor.otherEspiau, Fernando
dc.contributor.otherOrtega, Juan
dc.date.accessioned2018-11-24T10:04:11Z-
dc.date.available2018-11-24T10:04:11Z-
dc.date.issued2004
dc.identifier.issn0378-3812
dc.identifier.urihttp://hdl.handle.net/10553/49709-
dc.description.abstractThis article is a theoretical-experimental study on the binary systems ethyl methanoate + alkanes (hexane to decane). Vapour-liquid equilibrium (VLE) data at a pressure of 101.32 kPa are presented for the five systems studied and all were consistent with a point-to-point test. The only azeotropic binary system is ethyl methanoate + hexane, with azeotropic coordinates at x(az) = 0.709, T-az = 323.21 K. Also, for the same group of systems the excess properties H-m(E) and V-m(E), measured at 318.15 K, are presented and an interpretation of the results obtained for these is carried out. The excess properties are correlated with a new polynomial equation that is also proposed for the treatment of equilibrium data and is included as an acceptable part of a more complete data processing.For the five binary mixtures studied, the equilibrium thermodynamic property estimation for several group contribution models is performed. (C) 2003 Elsevier B.V. All rights reserved.
dc.publisher0378-3812
dc.relation.ispartofFluid Phase Equilibria
dc.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 215, p. 175-186
dc.subject.otherBinary-Systems
dc.subject.otherUnifac Model
dc.subject.otherN-Alkane
dc.subject.otherPlus
dc.subject.otherEnthalpies
dc.subject.otherTemperature
dc.subject.otherParameters
dc.subject.otherFormate
dc.subject.otherC-7
dc.titleMeasurement and correlation of isobaric vapour-liquid equilibrium data and excess properties of ethyl methanoate with alkanes (hexane to decane)
dc.typeinfo:eu-repo/semantics/Articlees
dc.typeArticlees
dc.identifier.doi10.1016/j.fluid.2003.08.003
dc.identifier.scopus0742269718
dc.identifier.isi000188973600006
dcterms.isPartOfFluid Phase Equilibria
dcterms.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 215 (2), p. 175-186
dc.contributor.authorscopusid7402623992
dc.contributor.authorscopusid6603650584
dc.contributor.authorscopusid6603444241
dc.description.lastpage186
dc.description.firstpage175
dc.relation.volume215
dc.type2Artículoes
dc.identifier.wosWOS:000188973600006
dc.contributor.daisngid170099
dc.contributor.daisngid2841610
dc.contributor.daisngid6667042
dc.identifier.investigatorRIDI-2923-2015
dc.identifier.investigatorRIDN-3335-2014
dc.contributor.wosstandardWOS:Ortega, J
dc.contributor.wosstandardWOS:Espiau, F
dc.contributor.wosstandardWOS:Dieppa, R
dc.date.coverdateFebrero 2004
dc.identifier.ulpgces
dc.description.jcr1,356
dc.description.jcrqQ1
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.deptGIR IDeTIC: División de Ingeniería Térmica e Instrumentación-
crisitem.author.deptIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.orcid0000-0002-8304-2171-
crisitem.author.orcid0000-0002-2481-8873-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.parentorgIU para el Desarrollo Tecnológico y la Innovación-
crisitem.author.fullNameOrtega Saavedra, Juan-
crisitem.author.fullNameEspiau Castellano,Fernando-
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