Isobaric Vapor−Liquid Equilibria for the Systems Propionic Acid + Butyric Acid, Isobutyric Acid + Butyric Acid, Butyric Acid + Isovaleric Acid, and Butyric Acid + Hexanoic Acid at 14 kPa
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Isobaric vapor-liquid equilibria were measured at 14 kPa for the binary systems propionic acid + butyric acid, isobutyric acid + butyric acid, butyric acid + isovaleric acid, and butyric acid + hexanoic acid. The experimental data were modeled using the γ-φ approach as discussed by Raal and Muhlbauer. The proposed model uses the NRTL equation for correlation of the liquid-phase activity coefficient. The vapor-phase fugacity coefficient was calculated by the chemical theory, which treats binary mixtures containing associating species. The data were deemed thermodynamically consistent using a test proposed by Van Ness.
[1] H. C. Van Ness,et al. Thermodynamics in the treatment of vapor/liquid equilibrium (VLE) data , 1995 .
[2] John P. O'Connell,et al. A Generalized Method for Predicting Second Virial Coefficients , 1975 .
[3] J. Prausnitz,et al. Generalized Correlation for Fugacity Coefficients in Mixtures at Moderate Pressures. Application of Chemical Theory of Vapor Imperfections , 1973 .
[4] D. Marquardt. An Algorithm for Least-Squares Estimation of Nonlinear Parameters , 1963 .