Correlation and prediction of vapor-liqu
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David Zudkevitch; Joseph Joffe
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Article
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1970
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American Institute of Chemical Engineers
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English
⚖ 810 KB
A modified Redlich-Kwong equation has been applied to the calculation of phase equilibria in multicomponent systems. The two parameters of the Redlich-Kwong equation are treated as temperature functions. They are obtained for each pure component from experimental vapor pressures and liquid densities