Improving phase equilibrium calculation with the Peng-Robinson EOS for fats and oils related compounds/supercritical CO2 systems

Citation
Me. Araujo et Maa. Meireles, Improving phase equilibrium calculation with the Peng-Robinson EOS for fats and oils related compounds/supercritical CO2 systems, FLU PH EQUI, 169(1), 2000, pp. 49-64
Citations number
50
Categorie Soggetti
Physical Chemistry/Chemical Physics","Chemical Engineering
Journal title
FLUID PHASE EQUILIBRIA
ISSN journal
03783812 → ACNP
Volume
169
Issue
1
Year of publication
2000
Pages
49 - 64
Database
ISI
SICI code
0378-3812(20000303)169:1<49:IPECWT>2.0.ZU;2-R
Abstract
Several predictive methods for normal boiling point, critical temperature, critical pressure, and acentric factor, applied to fatty acids and fatty ac id esters of high molecular weight were evaluated. The properties estimated by the selected methods were used to analyze the ability of the Peng-Robin son equation of state (EOS) to predict the vapor-liquid equilibria of binar y and ternary systems of fats and oils related compounds with CO2. Van der Waals mixing rules with the combining rules proposed by Kwak and Mansoori a nd Park et al. were used. For fatty acids, the method of Constantinou and G ani was selected for the prediction of the critical temperature and that of Somayajulu for the prediction of the critical pressure when experimental b oiling temperatures were available. In the absence of experimental data, th e method of Constantinou and Gani was selected for the prediction of critic al and boiling temperatures, as well as for the critical pressure. For fatt y acid esters, the method of Joback and Reid was chosen for the prediction of the critical and boiling temperatures, and that of Constantinou and Gani was selected for the prediction of the critical pressure. The indirect met hod of Tu was preferred for the prediction of the acentric factors of high molecular weight fatty acids. The correlation of Vetere was chosen for the prediction of the acentric factors of low molecular weight fatty acid ester s, and the indirect method of Tu was selected for the prediction of the ace ntric factors for the methyl ester family. The results for the phase equili bria suggest that the Peng-Robinson equation, with the quadratic mixing rul es for the three combining rules tested, is capable of predicting vapor-liq uid equilibrium with quality comparable to the results obtained with the mi xing rules for more complex models like MHV1 and LCVM. (C) 2000 Elsevier Sc ience B.V. All rights reserved.