Key words: supercritical fluid, solubility of supercritical fluid in hydrocarbons, empirical dependence, equation of state
A method is proposed for describing the solubility of supercritical fluids in hydrocarbons using empirical parameters determined by the error function minimization method. The solubility of supercritical CO2 in cyclohexane and kerosene at 313 K at various pressures is calculated. The standard deviation of the calculated data from the experimental ones according to the proposed method was no more than 8.2%.