Abstract
Abstract For the design of separation processes with supercritical dense gases, referred to as vapour phase extraction processes, high-pressure vapour-liquid equilibria have to be known. In the present investigation the Redlich-Kwong equation of state has been applied to a parametric study of high-pressure phase equilibria. The study has developed a generalized description of the phase behaviour of binary and multicomponent systems and provided general rules for the design of vapour phase extraction processes.
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