Please use this identifier to cite or link to this item:
http://hdl.handle.net/10553/53868
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Gonzalez, E | en_US |
dc.contributor.author | Ortega, Juan | en_US |
dc.contributor.other | Ortega, Juan | - |
dc.contributor.other | Gonzalez-Diaz, Eduardo | - |
dc.date.accessioned | 2019-02-04T18:36:30Z | - |
dc.date.available | 2019-02-04T18:36:30Z | - |
dc.date.issued | 1996 | en_US |
dc.identifier.issn | 0021-9592 | en_US |
dc.identifier.uri | http://hdl.handle.net/10553/53868 | - |
dc.description.abstract | The concentrations of the vapor-liquid equilibria have been measured in a small capacity recirculating still for the binaries composed of four butyl esters (from methanoate to butanoate) and propan-2-ol at a constant pressure of 101.32 kPa. VLE data were thermodynamically verified with the point-to-point test and the predictions made using several group-contribution models were acceptable but with some exceptions, An azeotrope was found for (x(1)butyl methanoate+x(2)propan-2-ol) at x(1) = y(1) = 0.038 and T = 351.9 K. | en_US |
dc.language | spa | en_US |
dc.publisher | 0021-9592 | |
dc.relation.ispartof | Journal of Chemical Engineering of Japan | en_US |
dc.source | Journal Of Chemical Engineering Of Japan[ISSN 0021-9592],v. 29 (2), p. 294-299 | en_US |
dc.subject.other | Unifac Group-Contribution | |
dc.subject.other | Coefficients | |
dc.subject.other | Prediction | |
dc.subject.other | Model | |
dc.title | Vapor liquid equilibria at 101.32 kPa mixtures of butyl esters and propan-2-ol | en_US |
dc.type | info:eu-repo/semantics/Article | en_US |
dc.type | Article | en_US |
dc.identifier.doi | 10.1252/jcej.29.294 | en_US |
dc.identifier.scopus | 0345632719 | - |
dc.identifier.isi | A1996UJ10100014 | - |
dcterms.isPartOf | Journal Of Chemical Engineering Of Japan | |
dcterms.source | Journal Of Chemical Engineering Of Japan[ISSN 0021-9592],v. 29 (2), p. 294-299 | |
dc.contributor.authorscopusid | 55682655415 | - |
dc.contributor.authorscopusid | 7409599792 | - |
dc.description.lastpage | 299 | en_US |
dc.identifier.issue | 2 | - |
dc.description.firstpage | 294 | en_US |
dc.relation.volume | 29 | en_US |
dc.type2 | Artículo | en_US |
dc.identifier.wos | WOS:A1996UJ10100014 | - |
dc.contributor.daisngid | 2090863 | - |
dc.contributor.daisngid | 3150887 | - |
dc.contributor.daisngid | 170099 | - |
dc.identifier.investigatorRID | N-3335-2014 | - |
dc.identifier.investigatorRID | No ID | - |
dc.contributor.wosstandard | WOS:Gonzalez, E | - |
dc.contributor.wosstandard | WOS:Ortega, J | - |
dc.date.coverdate | Enero 1996 | en_US |
dc.identifier.ulpgc | Sí | es |
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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