Article ID Journal Published Year Pages File Type
202838 Fluid Phase Equilibria 2014 10 Pages PDF
Abstract

In this work Vidal equation of state formulation (EOS-qE) was evaluated for vapor/liquid equilibria (VLE) isothermal calculations of binary and ternary mixtures, using NRTL model with 2 and 3 parameters for qE representation in the low to high pressure range, resulting at least as convenient and accurate in application as the gamma/phi formulation and Redlich–Kister expansion; and better than using Huron/Vidal and Wong/Sandler mixing rules EOS-GE formulation. Compared with referenced models, satisfactory predictions of VLE at temperatures different than that, at what correlation was obtained. Finally, isobaric VLE was correlated in the experimental error precision range.

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Physical Sciences and Engineering Chemical Engineering Chemical Engineering (General)
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