In the present work, the group contribution-associating-equation of st
ate (GCA-EOS) is applied for modeling high pressure phase equilibrium
of mixtures containing gases and associating fluids. The GCA performan
ce is compared with other group contribution local composition EOS. Ba
sed on extensive testing, it is concluded that the GCA-EOS is a reliab
le method for modeling the extraction and dehydration of alcohols from
aqueous solutions using gases at near critical conditions as solvents
(dehyextract process). The parameter tables for the GCA-EOS model hav
e been revised and extended. (C) 1997 Elsevier Science B.V.