Please use this identifier to cite or link to this item:
http://hdl.handle.net/10553/52116
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Soto, Ana | |
dc.contributor.author | Hernández, Pablo | |
dc.contributor.author | Ortega, J | |
dc.contributor.other | Soto, Ana | |
dc.contributor.other | Ortega, Juan | |
dc.date.accessioned | 2018-11-25T17:36:09Z | - |
dc.date.available | 2018-11-25T17:36:09Z | - |
dc.date.issued | 1998 | |
dc.identifier.issn | 0378-3812 | |
dc.identifier.uri | http://hdl.handle.net/10553/52116 | - |
dc.description.abstract | New 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.publisher | 0378-3812 | |
dc.relation.ispartof | Fluid Phase Equilibria | |
dc.source | Fluid Phase Equilibria[ISSN 0378-3812],v. 146 (1-2), p. 351-370 | |
dc.subject.other | Vapor-Liquid-Equilibria | |
dc.subject.other | Butyl Esters Methanoate | |
dc.subject.other | Methyl Butanoate | |
dc.subject.other | Mixtures | |
dc.subject.other | Densities | |
dc.subject.other | Ethanol | |
dc.subject.other | 1-Propanol | |
dc.subject.other | Coefficients | |
dc.subject.other | 298.15-K | |
dc.subject.other | Formate | |
dc.title | Experimental 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.type | info:eu-repo/semantics/Article | es |
dc.type | Article | es |
dc.identifier.scopus | 0032073238 | |
dc.identifier.isi | 000074478100026 | |
dcterms.isPartOf | Fluid Phase Equilibria | |
dcterms.source | Fluid Phase Equilibria[ISSN 0378-3812],v. 146 (1-2), p. 351-370 | |
dc.contributor.authorscopusid | 35280670900 | |
dc.contributor.authorscopusid | 57196517470 | |
dc.contributor.authorscopusid | 7402623992 | |
dc.description.lastpage | 370 | |
dc.description.firstpage | 351 | |
dc.relation.volume | 146 | |
dc.type2 | Artículo | es |
dc.identifier.wos | WOS:000074478100026 | |
dc.contributor.daisngid | 12261 | |
dc.contributor.daisngid | 6917897 | |
dc.contributor.daisngid | 170099 | |
dc.identifier.investigatorRID | H-8919-2015 | |
dc.identifier.investigatorRID | N-3335-2014 | |
dc.contributor.wosstandard | WOS:Soto, A | |
dc.contributor.wosstandard | WOS:Hernandez, P | |
dc.contributor.wosstandard | WOS:Ortega, J | |
dc.date.coverdate | Diciembre 1998 | |
dc.identifier.ulpgc | Sí | es |
dc.description.jcr | 0,829 | |
dc.description.jcrq | Q1 | |
dc.description.scie | SCIE | |
item.grantfulltext | none | - |
item.fulltext | Sin texto completo | - |
crisitem.author.dept | GIR IDeTIC: División de Ingeniería Térmica e Instrumentación | - |
crisitem.author.dept | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.dept | Departamento de Ingeniería de Procesos | - |
crisitem.author.orcid | 0000-0002-8304-2171 | - |
crisitem.author.parentorg | IU para el Desarrollo Tecnológico y la Innovación | - |
crisitem.author.fullName | Ortega Saavedra, Juan | - |
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