The feasibility of alcohol dehydration by the use of light hydrocarbon
solvents has been recently confirmed by pilot plant and bench scale e
xperiments. In this regard the study of vapor liquid equilibria (VLE)
for alcohol - water - non polar gas mixtures is of interest for the de
hydration of alcohols by high pressure entrainers. The potential for w
ater entrainment of a given gas can be obtained from binary informatio
n alone; however, ternary data are required in order to know to wich e
xtent the entrainment effect is affected by the presence of the alcoho
l. Experimental studies carried out with propane, propylene and carbon
dioxide, indicate that the water-gas relative volatility in mixtures
with alcohol is poorly predicted by the group contribution equation of
state (GC-EOS). In the present work new experimental data are present
ed for the binary isopropanol-isobutane, and for the ternary isopropan
ol-isobutane-water. An extension of the GC-EOS model is proposed for d
ealing with the problem of associating mixtures.