FURTHER DEVELOPMENT, STATUS AND RESULTS OF THE PSRK METHOD FOR THE PREDICTION OF VAPOR-LIQUID-EQUILIBRIA AND GAS SOLUBILITIES

Since Huron and Vidal (1979) developed the basic idea of so called G(E ) mixing rules, similar models have been proposed by different authors . The aim of all recent developments of G(E) mixing rules is to combin e the successful G(E) models or group contribution methods with equati ons of state to enable the description of vapor-liquid equilibria at h igh temperatures and pressures including supercritical compounds. The group contribution equation of state PSRK (predictive Soave-Redlich-Kw ong) as suggested by Holderbaum and Gmehling (1991) combines the UNIFA C model (Hansen et al., 1991) with the SRK equation of state. In this work the range of applicability of the PSRK method was extended by the introduction of additional,eases and the determination of the missing interaction parameters between the following gases: CH4, CO2, CO, Ar, NH3, H2S, H-2, O-2, N-2 and the original UNIFAC structural groups. Th e VLE results of the PSRK model have been compared with other predicti ve equations of state (MHV2 (Dahl and Michelsen (1990)), Lermite and V idal (1992), LCVM (Boukouvalas et al. (1994)), Wong et al. (1992), UNI WAALS (Gupte et al. (1986), GCEOS (Skjold-Jorgensen (1984), Tochigi et al. (1990)). Furthermore a comparison between experimental and predic ted VLE and Henry coefficients is presented. The PSRK mixing rule can also be used to introduce other G(E) models into the SRK equation of s tate. The results show, that for any G(E) model the parameters derived from VLE can be used to enable reliable predictions of phase equilibr ia, whereby usually excellent results are obtained for a large tempera ture range. The thermodynamic analysis of G(E) mixing rules enables a reduction of all approaches to one general AE mixing rule. From this f ormalism the derivation of the PSRK, and other, G(E) mixing rules can be easier understood.