Effect of mixing rule and activity coefficient model on prediction of solid-liquid-gas equilibria for carbon dioxide plus organic compound mixtures using Peng-Robinson equation of state and GE type mixing rule

被引:4
作者
Shimoyama, Yusuke [1 ]
Ng, Brendan [1 ]
机构
[1] Tokyo Inst Technol, Dept Chem Engn, Meguro Ku, Tokyo 1528550, Japan
关键词
Solid-liquid-gas equilibrium; Equation of state; Carbon dioxide; Excess Gibbs free energy mixing rule; Molecular surface charge; PHASE-EQUILIBRIA; BINARY-SYSTEMS; COSMO THEORY; CO2; UNIFAC;
D O I
10.1016/j.fluid.2013.05.024
中图分类号
O414.1 [热力学];
学科分类号
摘要
Solid-liquid-gas equilibria (SLGE) for carbon dioxide + organic compound mixtures were predicted by Peng-Robinson (PR) equation of state with excess Gibbs free energy (G(E)) type mixing rule. Activity coefficient models using molecular surface charge density were applied for the calculation of activity coefficient and GE in the mixing rules. Two types of G(E) type mixing rule, Modified Huron-Vidal (MHV1) and Linear Combination of Vidal and Michelsen (LCVM) mixing rules were applied for the energy and size parameters on PR equation of state. The activity coefficient models used in this work were Conductor-like Screening Model Segment Activity Coefficient (COSMO-SAC) and COSMO-UNIQUAC. In these activity coefficient models, two kinds of the combinatorial equations, Stavermann-Guggenheim (SG) and Flory-Huggins (FH) equations were used. Consequently, the eight combinations with the GE type mixing rule, the activity coefficient model and the combinatorial equation were applied for the prediction of SLVE for carbon dioxide + organic compound mixtures. The organic compounds interested in this work were aromatic hydrocarbons, alcohols and acids. On the SLVE calculation in this work, the temperatures at the phase equilibria were calculated by fixed pressure. The effects of mixing rule and activity coefficient model on the prediction performance of the solid-liquid-gas equilibria were investigated. The combination of MHV1/COSMO-SAC/SG presented the best performance of the SLVE prediction for carbon dioxide + aromatic hydrocarbon systems. The absolute deviation between experimental and predicted result of the temperature at the SLGE was 3.6 K in temperature. For alcohols and acids, the smallest absolute deviations between experimental and predicted results of the temperature at the SLGE were given by the combinations of MHV1/COSMO-SAC/FH and LCVM/COSMO-SAC/FH, respectively. The values of the absolute deviations were 1.1 and 4.1 K for alcohols and acids. (C) 2013 Elsevier B.V. All rights reserved.
引用
收藏
页码:30 / 35
页数:6
相关论文
共 23 条
[1]   Measurement and thermodynamic modeling of solid-liquid-gas equilibrium of some organic compounds in the presence of CO2 [J].
Bertakis, Evangelos ;
Lemonis, Ilias ;
Katsoufis, Stelios ;
Voutsas, Epaminondas ;
Dohrn, Ralf ;
Magoulas, Kostis ;
Tassios, Dimitrios .
JOURNAL OF SUPERCRITICAL FLUIDS, 2007, 41 (02) :238-245
[2]   PREDICTION OF VAPOR-LIQUID-EQUILIBRIUM WITH THE LCVM MODEL - A LINEAR COMBINATION OF THE VIDAL AND MICHELSEN MIXING RULES COUPLED WITH THE ORIGINAL UNIFAC AND THE T-MPR EQUATION OF STATE [J].
BOUKOUVALAS, C ;
SPILIOTIS, N ;
COUTSIKOS, P ;
TZOUVARAS, N ;
TASSIOS, D .
FLUID PHASE EQUILIBRIA, 1994, 92 :75-106
[3]   HIGH-PRESSURE PHASE-EQUILIBRIA FOR BINARY-SYSTEMS INVOLVING A SOLID-PHASE [J].
CHEONG, PL ;
ZHANG, DG ;
OHGAKI, K ;
LU, BCY .
FLUID PHASE EQUILIBRIA, 1986, 29 :555-562
[4]   Phase equilibria of organic solid solutes and supercritical fluids with respect to the RESS process [J].
Diefenbacher, A ;
Türk, M .
JOURNAL OF SUPERCRITICAL FLUIDS, 2002, 22 (03) :175-184
[5]  
Geana D., 1997, J SUPERCRIT FLUID, V15, P97
[6]   CRYSTALLIZATION OF N-OCTACOSANE BY THE RAPID EXPANSION OF SUPERCRITICAL SOLUTIONS [J].
GRISCIK, GJ ;
ROUSSEAU, RW ;
TEJA, AS .
JOURNAL OF CRYSTAL GROWTH, 1995, 155 (1-2) :112-119
[7]   Calculation of Solid-Liquid-Gas Equilibrium for Binary Systems Containing CO2 [J].
Hong, Jindui ;
Chen, Hui ;
Li, Jun ;
Matos, Henrique A. ;
de Azevedo, Edmundo Gomes .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (09) :4579-4586
[8]  
KIamt A., 1993, J CHEM SOC PERK T, V5, P799
[9]   A MODIFIED UNIFAC GROUP-CONTRIBUTION MODEL FOR PREDICTION OF PHASE-EQUILIBRIA AND HEATS OF MIXING [J].
LARSEN, BL ;
RASMUSSEN, P ;
FREDENSLUND, A .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1987, 26 (11) :2274-2286
[10]  
Lemert R.M., 1999, FLUID PHASE EQUILIBR, V45, P265