Vapor-liquid equilibrium measurements and modeling of the n-butane plus ethanol system from 323 to 423 K - Mines Paris Accéder directement au contenu
Article Dans Une Revue Fluid Phase Equilibria Année : 2009

Vapor-liquid equilibrium measurements and modeling of the n-butane plus ethanol system from 323 to 423 K

Résumé

Vapor-liquid equilibrium (VLE) data are presented for the n-butane + ethanol system in the temperature range from 323 to 423 K. Measurements were performed using a "static-analytic" apparatus, equipped with two electromagnetic ROLSI (TM) capillary samplers, and thermally regulated via an air bath. This work presents vapor compositions which have not been explicitly measured previously. The modeling of the data was performed using two models: the Peng-Robinson equation of state with the Wong and Sandler mixing rule and NRTL excess function (PR/WS/NRTL); and the perturbed-chain statistical associating fluid theory (PC-SAFT) equation of state. To assess the effect of dipole-dipole interactions present, a dipolar contribution developed by Jog and Chapman (1999)[20] was tested with the second model. Temperature dependent binary interaction parameters have been adjusted to the new data. The PR/WS/NRTL equation of state shows good correlation with the results, while the PC-SAFT is slightly less accurate.

Dates et versions

hal-00508609 , version 1 (04-08-2010)

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Chien-Bin Soo, Elise El Ahmar, Christophe Coquelet, Deresh Ramjugernath, Dominique Richon. Vapor-liquid equilibrium measurements and modeling of the n-butane plus ethanol system from 323 to 423 K. Fluid Phase Equilibria, 2009, 286 (1), pp.79-87. ⟨10.1016/j.fluid.2009.08.007⟩. ⟨hal-00508609⟩
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