2009Russian Journal of Applied ChemistryRequires access

Calculation of the limiting activity coefficients of components in a solution from isothermal data on the equilibrium compositions of liquid and vapor phases

А. Н. Мариничев

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Abstract

The method of calculating the limiting activity coefficients of components was developed and illustrated by a number of examples. Isothermal binary data on the compositions of the solution and vapor coexisting phases were fitted to the Porter, Margules, Van Laar, Wilson, Redlich-Kister, and NRTL interpolation equations. In this method, nonideality of a vapor phase is directly taken into account and the composition of the azeotrope in the system, if exists, may be calculated.

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The method of calculating the limiting activity coefficients of components was developed and illustrated by a number of examples. Isothermal binary data on the compositions of the solution and vapor coexisting phases were fitted to the Porter, Margules, Van Laar, Wilson, Redlich-Kister, and NRTL interpolation equations. In this method, nonideality of a vapor phase is directly taken into account and the composition of the azeotrope in the system, if exists, may be calculated.

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Available abstract

The method of calculating the limiting activity coefficients of components was developed and illustrated by a number of examples. Isothermal binary data on the compositions of the solution and vapor coexisting phases were fitted to the Porter, Margules, Van Laar, Wilson, Redlich-Kister, and NRTL interpolation equations. In this method, nonideality of a vapor phase is directly taken into account and the composition of the azeotrope in the system, if exists, may be calculated.

Key concepts: Non-random two-liquid model, Chemistry, Azeotrope, Activity coefficient, Isothermal process, Thermodynamics, Limiting, Binary number

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