We present a simple treatment of supercritical fluid extraction for bi
nary (solvent-solute) and ternary (solvent-solute-cosolvent) systems.
Solubility predictions are made using the virial equation of state. Th
e solute chemical potential is calculated up to fourth order in the fl
uid density. There are no adjustable parameters: the pressure mixture
virial coefficients B-alpha beta, C-alpha beta gamma and D-alpha beta
gamma delta are computed directly from the potentials representing the
interactions of solvent, solute and cosolvent molecules. For the purp
oses of illustration we assume these are of Lennard-Jones form; howeve
r, the method is considerably more general, and may be applied even wh
en the potentials are anisotropic. Computer simulations have also been
performed, and confirm the accuracy of this approach at densities up
to twice the critical density. Our analysis of ternary systems helps t
o identify the nature of the interactions primarily responsible for en
trainer effects.