The Redlich-Kwong equation of State was used to calculate liquid and vapour phase fuga- cities of Acetic acid (l)-n. Heptane (2) and Acetic acid (l)-Benzene (2) Systems for predicting isothermal vapour-Iiquid equilibria. The binary interaction coefficients were obtained by a mi- nimization technique with the help of a Computer. The agreement, between the predicted and experimental equilibrium data allows the calculation of isothermal vapour-liquid data for Sys¬tems containing both polar and non-polar compounds.
Primary Language | English |
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Subjects | Chemical Engineering |
Journal Section | Research Article |
Authors | |
Publication Date | January 1, 1899 |
Published in Issue | Year 1988 Volume: 34 Issue: 01.02 |
Communications Faculty of Sciences University of Ankara Series B Chemistry and Chemical Engineering
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