The applicability of a temperature dependent Soave-Redlich-Kwong model to vapour-liquid equilibrium calculations of alkane binaries.

Author(s) : SERBANOVIC S., SERBULA S., DJORDJEVIC B.

Type of article: Article

Summary

In the work the vapour-liquid equilibrium calculation of 10 alkane binaries is presented using three Soave-Redlich-Kwong models which include: a) a temperature-dependent interaction parameter; b) a constant value of the interaction parameter; and c) the zero value of the interaction parameter. The 10 alkanes include: methane-ethane, methane-n-hexane, methane-n-heptane, methane-n-octane, methane-n-nonane, methane-decane methane-n-propane, ethane-n-pentane, propane-n-pentane, n-butane-n-decane.

Details

Original title: The applicability of a temperature dependent Soave-Redlich-Kwong model to vapour-liquid equilibrium calculations of alkane binaries.
Record ID : 1996-0052
Languages: English
Source: J. serbian chem. Soc. - vol. 60 - n. 4
Publication date: 1995
Document available for consultation in the library of the IIR headquarters only.

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Indexing

Themes: Thermodynamics and changes of state
Keywords: Pentane; Hexane; Equilibrium; Calculation; Butane; Methane; Adaptation; Simulation; Propane; Binary mixture; Pressure; Hydrocarbon; Heptane; Ethane; Equation of state