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dc.contributor.authorRubio Gallego, Jorge 
dc.contributor.authorMoreau Ortega, Alejandro 
dc.contributor.authorSegovia Puras, José Juan 
dc.contributor.authorVillamañán Olfos, Miguel Ángel 
dc.contributor.authorMartín González, María del Carmen 
dc.date.accessioned2025-01-13T11:45:06Z
dc.date.available2025-01-13T11:45:06Z
dc.date.issued2020
dc.identifier.citationJournal of Molecular Liquids, 2020, 303, 112404es
dc.identifier.issn0167-7322es
dc.identifier.urihttps://uvadoc.uva.es/handle/10324/73730
dc.descriptionProducción Científicaes
dc.description.abstractIsothermal VLEdata for(cyclohexanone+2-heptanone)and(cyclohexanone+hexanal)mixturesarereported at T =(313.15,333.15,353.15,393.15)K,which weremeasuredusingastatictechnique.Equilibrium properties are measured directly, and their expanded uncertainties (k = 2) are: injected volume 0.06 mL, temperature 20 mK,andtotal pressure0.1%. The non-idealityof thevapor phasewastakeninto accountusingthevirialequation of state. VLE data were correlated using Margules, Wilson, NRTL and UNIQUAC equations obtaining goodresults. Thebinarymixture(cyclohexanone+2 heptanone)presentsamaximumpressureazeotropewhichisbrokenat 393.15 K.es
dc.format.mimetypeapplication/pdfes
dc.language.isoenges
dc.publisherElSevieres
dc.rights.accessRightsinfo:eu-repo/semantics/openAccesses
dc.subject.classificationVLE, Cyclohexanone, 2-Heptanone, Hexanal, Azeotropees
dc.titleVapor-liquid equilibria of the binary systems (cyclohexanone + 2-heptanone) and (cyclohexanone + hexanal) at different temperatureses
dc.typeinfo:eu-repo/semantics/articlees
dc.rights.holder© Elsevier B.Ves
dc.identifier.doi10.1016/J.MOLLIQ.2019.112404es
dc.identifier.publicationfirstpage112404es
dc.identifier.publicationtitleJournal of Molecular Liquidses
dc.identifier.publicationvolume303es
dc.peerreviewedSIes
dc.description.projectUBE Chemicalses
dc.description.projectEuropean Social Fundes
dc.description.projectJunta de Castilla y Leónes
dc.type.hasVersioninfo:eu-repo/semantics/submittedVersiones


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