Abstract
Isothermal vapour-liquid equilibrium data were measured for the binary acetonitrile-isobutanol and ternary acetonitrile-isobutanol-benzene systems at 60° C by using a vapour-recirculating equilibrium still. The experimental data were correlated by the extended UNIQUAC and UNIQUAC associated-solution models. The UNIQUAC associated-solution model gives better predicted values for the ternary system.
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