COMPARISON OF 2 PREDICTIVE G(E) MODELS FOR VAPOR-LIQUID-EQUILIBRIUM CALCULATIONS

Citation
S. Dunnebeil et al., COMPARISON OF 2 PREDICTIVE G(E) MODELS FOR VAPOR-LIQUID-EQUILIBRIUM CALCULATIONS, Chemical engineering journal and the biochemical engineering journal, 61(1), 1996, pp. 21-26
Citations number
12
Categorie Soggetti
Engineering, Chemical
ISSN journal
09230467
Volume
61
Issue
1
Year of publication
1996
Pages
21 - 26
Database
ISI
SICI code
0923-0467(1996)61:1<21:CO2PGM>2.0.ZU;2-1
Abstract
Ash (S.N. Ash, P. Ray and B.V. Detta, AIChE J., 31 (1985) 821; S.N. As h, Chem. Eng. J., 48 (1992) 183) has proposed a correlation for calcul ating the binary parameters of the Wilson g(E) model by using only pur e-component parameters: solubility parameters, molar liquid volumes, r elative van der Waals volumes and surfaces, critical properties, acent ric factors and dipole moments. To evaluate the Ash correlation the va pour-liquid equilibria for 75 binary systems, activity coefficients at ininite dilution and excess enthalpies were predicted and compared wi th experimental data and with the modified UNIFAC model (J. Gmehling, J. Li and M. Schiller, Ind. Eng. Chem. Res., 32 (1993) 178). It was fo und that the correlation of Ash and coworkers is significantly inferio r to the modified UNIFAC model and cannot be recommended for phase equ ilibrium predictions for those cases where UNIFAC parameters are avail able.