Identificador persistente para citar o vincular este elemento: http://hdl.handle.net/10553/52117
Campo DC Valoridioma
dc.contributor.authorHernández, Pabloen_US
dc.contributor.authorOrtega, Juanen_US
dc.contributor.otherOrtega, Juan-
dc.date.accessioned2018-11-25T17:36:40Z-
dc.date.available2018-11-25T17:36:40Z-
dc.date.issued1997en_US
dc.identifier.issn0021-9568en_US
dc.identifier.urihttp://hdl.handle.net/10553/52117-
dc.description.abstractVapor−liquid equilibrium at 101.32 kPa has been measured for the binary systems formed by ethyl ethanoate, propanoate, and butanoate with propan-2-ol and butan-2-ol in an equilibrium still with circulation of both the vapor and liquid phases. The data were correlated by several available equations, and the parameters are reported for each of mixtures studied. Azeotropes were found in the mixtures ethyl ethanoate or propanoate + propan-2-ol and ethyl propanoate + butan-2-ol. Satisfactory results are obtained for the prediction of activity coefficients and the equilibrium compositions with the UNIFAC modified model. The densities for the same mixtures at 298.15 K are also reported.en_US
dc.languageengen_US
dc.publisher0021-9568-
dc.relation.ispartofJournal of Chemical & Engineering Dataen_US
dc.sourceJournal of Chemical and Engineering Data[ISSN 0021-9568],v. 42(6), p. 1090-1100en_US
dc.titleVapor-liquid equilibria and densities for ethyl esters (ethanoate to butanoate) and alkan-2-ol (C-3-C-4) at 101.32 kPaen_US
dc.typeinfo:eu-repo/semantics/articleen_US
dc.typeArticleen_US
dc.identifier.doi10.1021/je970077b-
dc.identifier.scopus0031271960-
dc.identifier.isiA1997YG65900011-
dcterms.isPartOfJournal Of Chemical And Engineering Data-
dcterms.sourceJournal Of Chemical And Engineering Data[ISSN 0021-9568],v. 42 (6), p. 1090-1100-
dc.contributor.authorscopusid57196517470-
dc.contributor.authorscopusid7402623992-
dc.description.lastpage1100en_US
dc.identifier.issue6-
dc.description.firstpage1090en_US
dc.relation.volume42en_US
dc.investigacionIngeniería y Arquitecturaen_US
dc.type2Artículoen_US
dc.identifier.wosWOS:A1997YG65900011-
dc.contributor.daisngid6917897-
dc.contributor.daisngid170099-
dc.identifier.investigatorRIDN-3335-2014-
dc.utils.revisionen_US
dc.identifier.ulpgcen_US
dc.contributor.buulpgcBU-INGen_US
dc.description.jcr0,885
dc.description.jcrqQ1
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-
Colección:Artículos
Vista resumida

Citas SCOPUSTM   

33
actualizado el 14-abr-2024

Citas de WEB OF SCIENCETM
Citations

33
actualizado el 25-feb-2024

Visitas

46
actualizado el 17-feb-2024

Google ScholarTM

Verifica

Altmetric


Comparte



Exporta metadatos



Los elementos en ULPGC accedaCRIS están protegidos por derechos de autor con todos los derechos reservados, a menos que se indique lo contrario.