In this work, the aqueous electrolyte equation of state (EOS) of Furst and
Renon [AIChE J. 39 (1993) 335] has been extended to mixed solvent electroly
te systems. At first, the extended EOS has been used to represent vapor pre
ssures for binary nonaqueous halide electrolyte mixtures with the average a
bsolute deviation (AAD) of 0.88% and mean activity coefficients for 12 tern
ary water-cosolvent-halide electrolyte systems with the AAD of 2.73%. Then
the extended EOS has been applied to predict VLE of 31 ternary mixed solven
t halide/acetate-electrolyte systems except propanol-water-salt systems and
methanol/ethanol-water systems containing Ca2+ for which VLE cannot be rel
iably predicted with the binary parameters determined from binary VLE data.
The deviations of the calculated VLE by the extended EOS are comparable to
those by the models of Sander et al. [Chem. Eng. Sci. 41 (1986) 1171] and
Macedo et al. [Chem. Eng. Sci. 45 (1990) 875]. However, no parameters of th
e extended EOS have been adjusted to match the experimental VLE data of ter
nary systems. Finally, VLE of eight propanol-water-salt systems, three meth
anol/ethanol-water systems containing Ca2+ and six systems containing NO3-
have been correlated by use of 15 adjustable parameters determined by fitti
ng the measured ternary VLE data and the calculated results are satisfactor
y. (C) 2000 Elsevier Science B.V. All rights reserved.