Abstract
The mean-field lattice-gas model in the present form has proven to be well able to describe nearly quantitatively fluid phase behaviour of non-polar and polar pure components and mixtures over a large temperature and pressure range. In our version of the model it is assumed that: all lattice sites have the same volume, independent of temperature and pressure, and that every kind of lattice site has a characteristic interacting surface area. The combinatory entropy of the system is corrected with an empirical parameter. For mixtures the same procedure cart be followed and a description of fluid phase behaviour, based upon the parameters of the pure components and two binary interaction parameters, appear to come out quite reasonably.
The systems CO2 H2O and mixtures thereof are most commonly used in supercritical extraction. It is shown here that the lattice-gas model can quite well deal with these systems. Values of the lattice-gas parameters have been derived in the outlined manner and predict the second-type gas-gas demixing, known to occur in this system, in an essentially correct way.