Vapor–liquid equilibrium for the ternary carbon dioxide–ethanol–nonane and decane systems

Arenas-Quevedoa, Miguel G.; Galicia-Luna, Luis A.; Elizalde-Solis, Octavio

dc.contributor.author	Arenas-Quevedoa, Miguel G.
dc.contributor.author	Galicia-Luna, Luis A.
dc.contributor.author	Elizalde-Solis, Octavio
dc.date.accessioned	2017-04-26T18:42:45Z
dc.date.available	2017-04-26T18:42:45Z
dc.date.issued	2013
dc.identifier	http://doi.org/10.1016/j.fluid.2012.10.012	es_ES
dc.identifier.issn	ISSN: 0378-3812	es_ES
dc.identifier.uri	http://hdl.handle.net/123456789/744
dc.description	In this work, experimental vapor–liquid equilibrium (T, p, xi, yi) data for the ternary carbon dioxide–ethanol–nonane and carbon dioxide–ethanol–decane systems are reported in the temperature range of 313–373K from low pressures to the nearest of the corresponding critical pressure. Measurements were performed in an apparatus based on the static-analytic method with an on-line ROLSI sampler-injector device. Vapor–liquid equilibrium (VLE) data for both ternary systems are predicted using the Peng–Robinson equation of state coupled to the Wong–Sandler, one parameter van der Waals and two parameters van der Waals mixing rules. Binary interaction parameters are obtained from the VLE data of binary mixtures reported in the literature.	es_ES
dc.description.abstract	In this work, experimental vapor-liquid equilibrium (T, p, xi, yi) data for the ternary carbon Dioxide-ethanol-nonane and carbon dioxide-ethanol-decane systems are reported in the temperature Range of 313-373K from low pressures to the nearest of the corresponding critical pressure. Measurements Were performed in an apparatus based on the static-analytic method with an on-line ROLSI Sampler-injector device. Vapor-liquid equilibrium (VLE) data for both ternary systems are predicted Using the Peng-Robinson equation of state coupled with the Wong-Sandler, one parameter van der Waals And two parameters van der Waals mixing rules. Binary interaction parameters are obtained from the VLE data of binary mixtures reported in the literature.	es_ES
dc.language.iso	eng	es_ES
dc.publisher	Fluid Phase Equilibria	es_ES
dc.relation.uri	Público en general	es_ES
dc.rights	info:eu-repo/semantics/openAccess	es_ES
dc.rights.uri	http://creativecommons.org/licenses/by-nc/4.0	es_ES
dc.source	http://www.sciencedirect.com/science/article/pii/S0378381212005109	es_ES
dc.subject	Vapor–liquid equilibrium	es_ES
dc.subject	Carbon dioxide	es_ES
dc.subject	Ethanol	es_ES
dc.subject	Nonane	es_ES
dc.subject	Decane	es_ES
dc.subject.classification	INGENIERÍA Y TECNOLOGÍA [7]	es_ES
dc.title	Vapor–liquid equilibrium for the ternary carbon dioxide–ethanol–nonane and decane systems	es_ES
dc.type	info:eu-repo/semantics/article	es_ES