The design and development of processes involving supercritical fluids depend on how easy the phase equilibrium can be accurately modelled and predicted. In the work described herein, the supercritical fluid-solid equilibrium has been considered. Modelling the fluid-solid equilibrium is associated with a number of drawbacks, even when it is possible to obtain the experimental solubility data for the solute in the supercritical fluid. In most cases it is necessary to introduce additional adjustment parameters into the model. The developed program, realized in Visual Basic((R)) language, is based on the fitting of two parameters - the binary interaction parameter (k(12)) and the solid sublimation pressure (P-2(sat)). This program can be used for any fluid-solid equilibrium even when both parameters are known or supposed. The model has been applied to several systems and, as example, in this work, the Penicillin G-CO2 phase equilibrium data are shown. The results obtained allow affirm that the thermodynamic model applied to fluid-solid equilibrium calculations is useful to predict the behaviour of this system. (c) 2005 Elsevier Ltd. All rights reserved.