Identificador persistente para citar o vincular este elemento:
http://hdl.handle.net/10553/53801
| Campo DC | Valor | idioma |
|---|---|---|
| dc.contributor.author | Ortega, Juan | en_US |
| dc.contributor.author | Susial, Pedro | en_US |
| dc.contributor.other | Ortega, Juan | - |
| dc.date.accessioned | 2019-02-04T18:21:20Z | - |
| dc.date.available | 2019-02-04T18:21:20Z | - |
| dc.date.issued | 1990 | en_US |
| dc.identifier.issn | 0021-9592 | en_US |
| dc.identifier.uri | http://hdl.handle.net/10553/53801 | - |
| dc.description.abstract | Isobaric vapor–liquid equilibrium data at two pressures (114.66 and 127.99 kPa) over the entire range of compositions were obtained by using a recirculating equilibrium still for the binary systems formed by methyl acetate and either ethanol or propan-1-ol. In all cases, the systems studied exhibit positive deviations from ideal solution behavior. Methyl acetate + ethanol system shows an azeotrope at 114.66 kPa of x = y = 0.954 and T = 333.4 K and x = y = 0.948 and T = 336.7 K at 127.99 kPa. Once thermodynamic consistency was verified, prediction of data by several methods was carried out. Good predictions were obtained for all systems by the UNIFAC and ASOG methods, with mean error of about 5% as expected, but the calculated values for activity coefficients using the modified UNIFAC showed higher deviations | en_US |
| dc.language | eng | 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. 23 (5), p. 621-626 | en_US |
| dc.subject | 3303 ingeniería y tecnología químicas | en_US |
| dc.subject.other | Propan-l-ol | en_US |
| dc.subject.other | Methyl Acetate | en_US |
| dc.subject.other | Ethanol | en_US |
| dc.subject.other | Vapor-Liquid Equilibrium | en_US |
| dc.title | Vle at 114: 66 and 127: 99 kpa for the systems methyl acetate + ethanol and methyl acetate + propan-1-ol: Measurements and prediction | en_US |
| dc.type | info:eu-repo/semantics/Article | en_US |
| dc.type | Article | en_US |
| dc.identifier.doi | 10.1252/jcej.23.621 | en_US |
| dc.identifier.scopus | 85008072193 | - |
| dc.identifier.isi | A1990EE83100017 | - |
| dcterms.isPartOf | Journal Of Chemical Engineering Of Japan | - |
| dcterms.source | Journal Of Chemical Engineering Of Japan[ISSN 0021-9592],v. 23 (5), p. 621-626 | - |
| dc.contributor.authorscopusid | 7402623992 | - |
| dc.contributor.authorscopusid | 55884533900 | - |
| dc.description.lastpage | 626 | - |
| dc.identifier.issue | 5 | - |
| dc.description.firstpage | 621 | - |
| dc.relation.volume | 23 | - |
| dc.investigacion | Ingeniería y Arquitectura | en_US |
| dc.type2 | Artículo | en_US |
| dc.identifier.wos | WOS:A1990EE83100017 | - |
| dc.contributor.daisngid | 170099 | - |
| dc.contributor.daisngid | 1346331 | - |
| dc.identifier.investigatorRID | N-3335-2014 | - |
| dc.utils.revision | Sí | en_US |
| dc.contributor.wosstandard | WOS:ORTEGA, J | |
| dc.contributor.wosstandard | WOS:SUSIAL, P | |
| dc.date.coverdate | Octubre 1990 | |
| dc.identifier.ulpgc | Sí | es |
| dc.description.scie | SCIE | |
| item.fulltext | Con texto completo | - |
| item.grantfulltext | open | - |
| 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.dept | GIR IUNAT: Fotocatálisis y espectroscopía para aplicaciones medioambientales. | - |
| crisitem.author.dept | IU de Estudios Ambientales y Recursos Naturales | - |
| crisitem.author.orcid | 0000-0002-8304-2171 | - |
| crisitem.author.orcid | 0000-0002-6719-3084 | - |
| crisitem.author.parentorg | IU para el Desarrollo Tecnológico y la Innovación | - |
| crisitem.author.parentorg | IU de Estudios Ambientales y Recursos Naturales | - |
| crisitem.author.fullName | Ortega Saavedra, Juan | - |
| crisitem.author.fullName | Susial Badajoz, Pedro | - |
| Colección: | Artículos | |
Vle at 114 66 and 127 99 kpa for the systems methyl acetate + ethanol and methyl acetate + propan-1-ol Measurements and prediction
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