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Prediction and experimental determination of vapour‐liquid equilibria for benzene + Cyclohexane + 1‐Butanol mixtures at 101.325 kPa
Author(s) -
Arce A.,
Bunco A.,
Correa A.,
Tojo J.
Publication year - 1988
Publication title -
the canadian journal of chemical engineering
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.404
H-Index - 67
eISSN - 1939-019X
pISSN - 0008-4034
DOI - 10.1002/cjce.5450660316
Subject(s) - uniquac , unifac , non random two liquid model , cyclohexane , benzene , thermodynamics , activity coefficient , group contribution method , 2 butanol , butanol , chemistry , binary number , organic chemistry , phase equilibrium , mathematics , physics , phase (matter) , aqueous solution , ethanol , arithmetic
This article reports experimentally determined vapour‐liquid equilibrium data for benzene + cyclohexane + 1‐butanol mixtures at constant pressure of 101.325 kPa, and compares the results with those predicted by the group contribution methods ASOG‐KT and UNIFAC and by the Wilson, NRTL and UNIQUAC models after calculation of their adjustable parameters from the corresponding binary systems.