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

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

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

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

URI: http://hdl.handle.net/123456789/744

Fecha: 2013

Resumen:

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.

Descripción:

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.

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