Abstract
The vapour—liquid equilibrium compositions and temperatures covering the entire composition range were determined experimentally under isobaric conditions of 760 mm Hg pressure for the ternary system ethyl acetate — benzene — cyclohexane and its three constituent binaries. A continuous recirculating equilibrium still combining the best features of Jones and Gillespie stills was used. Values of activity coefficients and their ratios were correlated by Redlich—Kister equations. A modification of these equations was introduced to satisfy the Gibbs—Duhem equation at constant pressure.
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