In this work P−T−x−y
vapor liquid equilibrium data were obtained for the acetic acid +
octane mixture
at two temperatures, 323.15 and 343.15 K. This mixture is very
nonideal due to the association of acetic
acid, and the data could only be correlated with sufficient accuracy by
using two recently proposed activity
coefficient models that include association in both the liquid and
vapor phases.
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