Please use this identifier to cite or link to this item: http://hdl.handle.net/10553/52124
DC FieldValueLanguage
dc.contributor.authorOrtega, Juan-
dc.contributor.authorGalván, Salvador-
dc.contributor.otherOrtega, Juan-
dc.date.accessioned2018-11-25T17:40:04Z-
dc.date.available2018-11-25T17:40:04Z-
dc.date.issued1995-
dc.identifier.issn0021-9568-
dc.identifier.urihttp://hdl.handle.net/10553/52124-
dc.description.abstractIsobaric vapor-liquid equilibria were measured for propyl butanoate + ethanol, + 1-propanol, and + 1-butanol at 101.32 kPa using a dynamic still with circulation in both phases. After nonideality of the vapor phase was accounted for, the systems studied were thermodynamically consistent and they were correlated by different equations. No azeotrope was found in these mixtures. The predictions of the activity coefficients and of the vapor phase compositions show moderate agreement with the ASOG model and a recent version of UNIFAC. Densities of the above mixtures were also determined at 298.15 K. © 1995, American Chemical Society. All rights reserved.-
dc.publisher0021-9568-
dc.relation.ispartofJournal of Chemical & Engineering Data-
dc.sourceJournal Of Chemical And Engineering Data[ISSN 0021-9568],v. 40 (3), p. 699-703-
dc.subject.otherUnifac Group Contribution-
dc.subject.otherActivity-Coefficients-
dc.subject.otherExtension-
dc.subject.otherMixtures-
dc.subject.otherRevision-
dc.subject.otherEthanol-
dc.subject.otherEthyl-
dc.titleVapor-Liquid Equilibria and Densities for Propyl Butanoate + Normal Alcohols at 101.32 kPa-
dc.typeinfo:eu-repo/semantics/Article-
dc.typeArticle-
dc.identifier.doi10.1021/je00019a037-
dc.identifier.scopus0343909298-
dc.identifier.isiA1995QY26500037-
dcterms.isPartOfJournal Of Chemical And Engineering Data-
dcterms.sourceJournal Of Chemical And Engineering Data[ISSN 0021-9568],v. 40 (3), p. 699-703-
dc.contributor.authorscopusid7402623992-
dc.contributor.authorscopusid6602077961-
dc.description.lastpage703-
dc.identifier.issue3-
dc.description.firstpage699-
dc.relation.volume40-
dc.type2Artículo-
dc.identifier.wosWOS:A1995QY26500037-
dc.contributor.daisngid170099-
dc.contributor.daisngid4922939-
dc.identifier.investigatorRIDN-3335-2014-
dc.contributor.wosstandardWOS:ORTEGA, J-
dc.contributor.wosstandardWOS:GALVAN, S-
dc.date.coverdateMayo 1995-
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-
Appears in Collections:Artículos
Show simple item record

SCOPUSTM   
Citations

18
checked on Aug 7, 2022

WEB OF SCIENCETM
Citations

19
checked on Aug 7, 2022

Page view(s)

27
checked on Jul 30, 2022

Google ScholarTM

Check

Altmetric


Share



Export metadata



Items in accedaCRIS are protected by copyright, with all rights reserved, unless otherwise indicated.