Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/52129
DC FieldValueLanguage
dc.contributor.authorOrtega, Juan-
dc.contributor.authorLegido, José Luis-
dc.contributor.otherOrtega, Juan-
dc.contributor.otherLEGIDO, JOSE LUIS-
dc.date.accessioned2018-11-25T17:42:23Z-
dc.date.available2018-11-25T17:42:23Z-
dc.date.issued1994-
dc.identifier.issn0378-3812-
dc.identifier.urihttp://hdl.handle.net/10553/52129-
dc.description.abstractJ. Ortega and J.L. Legido, 1994. Application of the UNIFAC and Nitta-Chao models to describing the behavior of methyl ester/alkane mixtures, and experimental data for (methyl n-alkanoates+n-heptadecane) binary mixtures. Fluid Phase Equilibria, 95: 175-214. Excess molar properties, hE and vE, were determined based on the composition of binary mixtures of fourteen methyl esters (from ethanoate to n-pentadecanoate) and n-heptadecane at 298.15 K. The results showed all the mixtures to be endothermic and to undergo positive changes in excess volume. Both these effects decreased in a quasi-regular manner with the chain length of the methyl alkanoate. The excess enthalpies of the mixtures were compared with the values estimated by two group-contribution models, two different versions of the UNIFAC model, and the model of Nitta et al. [Nitta, T., Turek, E.A., Greenkorn, R.A. and Chao, K.C., 1977. A group contribution molecular model of liquids and solutions. AIChE J., 23: 144-160]. Using the UNIFAC model, the best prediction was achieved when all the methyl esters were considered to be alkyl ethanoates, which yielded a mean overall error of less than 5%. Application of the model of Nitta et al. to the mixtures considered yielded hE and vE values that differed substantially from the experimental values, with mean overall errors of 14% for the hE values and 34% for the vE values. Therefore, a comprehensive database of thermodynamic quantities for 368 binary mixtures was used to recalculate the alkane-ester interaction parameters and group parameters, which were then reapplied in the above-mentioned molecular model. This substantially improved the estimates of the properties for the pure components as well as those for the mixing quantities, achieving mean errors of less than 4% for hE and 17% for vE. © 1994.-
dc.publisher0378-3812-
dc.relation.ispartofFluid Phase Equilibria-
dc.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 95, p. 175-214-
dc.subject.otherExcess Molar Enthalpies-
dc.subject.other(A Propyl Ester-
dc.subject.otherThermodynamic Properties-
dc.subject.otherPrimary Parameters-
dc.subject.otherNormal-Pentane-
dc.subject.otherAcetate +-
dc.subject.otherVolumes-
dc.subject.other298.15-K-
dc.subject.otherPrediction-
dc.subject.otherEthanoate-
dc.titleApplication of the UNIFAC and Nitta-Chao models to describing the behavior of methyl ester/alkane mixtures, and experimental data for (methyl n-alkanoates + n-heptadecane) binary mixtures-
dc.typeinfo:eu-repo/semantics/Article-
dc.typeArticle-
dc.identifier.doi10.1016/0378-3812(94)80069-3-
dc.identifier.scopus0028768218-
dc.identifier.isiA1994NK30500013-
dcterms.isPartOfFluid Phase Equilibria-
dcterms.sourceFluid Phase Equilibria[ISSN 0378-3812],v. 95, p. 175-214-
dc.contributor.authorscopusid7402623992-
dc.contributor.authorscopusid56757682400-
dc.description.lastpage214-
dc.description.firstpage175-
dc.relation.volume95-
dc.type2Artículo-
dc.identifier.wosWOS:A1994NK30500013-
dc.contributor.daisngid170099-
dc.contributor.daisngid121633-
dc.identifier.investigatorRIDN-3335-2014-
dc.identifier.investigatorRIDL-7322-2014-
dc.contributor.wosstandardWOS:ORTEGA, J-
dc.contributor.wosstandardWOS:LEGIDO, JL-
dc.date.coverdateAbril 1994-
dc.identifier.ulpgc-
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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