SummaryThe use of the basic relations for the calculation of the weight fraction activity coefficient ~]~ and the FloryHuggins interaction parameter )CT2 requires the knowledge of the density and the molecular mass of the stationary phase. As these data are often inaccessible the use of a simplified equation is examined. The errors generated during the calculation of ~z and solubility parameter 5 2 are presented and discussed. All experimental data were collected for the series of fractions separated from high-boiling vacuum distillation residues of petroleum.