Phase equilibrium data for mixtures involving 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane between 312 and 343 K

作者: Shalendra Clinton Subramoney , Wayne Michael Nelson , Paramespri Naidoo , Christophe Coquelet , Dominique Richon

DOI: 10.1016/J.FLUID.2015.07.039

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摘要: Abstract Isothermal vapour–liquid equilibrium data are presented for binary mixtures of 1,1,2,3,3,3-hexafluoro-1-propene with either propane or n-butane in the (312–343) K temperature range. The experimental phase were measured using an apparatus based on “static-analytic” method. correlated a thermodynamic model comprising Peng–Robinson equation state Mathias–Copeman alpha function, Wong–Sandler mixing rule, and Non-Random Two-Liquid activity coefficient model. provided very satisfactory correlation both systems.

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