Modeling phase equilibria for acid gas mixtures using the CPA equation of state. Part II: Binary mixtures with CO2

被引:171
作者
Tsivintzelis, Ioannis [1 ]
Kontogeorgis, Georgios M. [1 ]
Michelsen, Michael L. [1 ]
Stenby, Erling H. [2 ]
机构
[1] Tech Univ Denmark, Dept Chem & Biochem Engn, CERE, DK-2800 Lyngby, Denmark
[2] Tech Univ Denmark, Dept Chem, CERE, DK-2800 Lyngby, Denmark
关键词
Equations of state; CPA; Acid gases; Association; CO2; VAPOR-LIQUID-EQUILIBRIA; ASSOCIATING FLUID THEORY; PLUS CARBON-DIOXIDE; ACCOUNT DIPOLAR INTERACTIONS; MOLECULAR-ORBITAL THEORY; PERTURBED-CHAIN SAFT; PENG-ROBINSON EOS; OF-STATE; AB-INITIO; MIXING RULES;
D O I
10.1016/j.fluid.2011.02.006
中图分类号
O414.1 [热力学];
学科分类号
摘要
In Part I of this series of articles, the study of H2S mixtures has been presented with CPA. In this study the phase behavior of CO2 containing mixtures is modeled. Binary mixtures with water, alcohols, glycols and hydrocarbons are investigated. Both phase equilibria (vapor-liquid and liquid-liquid) and densities are considered for the mixtures involved. Different approaches for modeling pure CO2 and mixtures are compared. CO2 is modeled as non self-associating fluid, or as self-associating component having two, three and four association sites. Moreover, when mixtures of CO2 with polar compounds (water, alcohols and glycols) are considered, the importance of cross-association is investigated. The cross-association is accounted for either via combining rules or using a cross-solvation energy obtained from experimental spectroscopic or calorimetric data or from ab initio calculations. In both cases two adjustable parameters are used when solvation is explicitly accounted for. The performance of CPA using the various modeling approaches for CO2 and its interactions is presented and discussed, comparatively to various recent published investigations. It is shown that overall very good correlation is obtained for binary mixtures of CO2 and water or alcohols when the solvation between CO2 and the polar compound is explicitly accounted for, whereas the model is less satisfactory when CO2 is treated as self-associating compound. (C) 2011 Elsevier B.V. All rights reserved.
引用
收藏
页码:38 / 56
页数:19
相关论文
共 117 条
[1]   Development of a universal group contribution equation of state III. Prediction of vapor-liquid equilibria, excess enthalpies, and activity coefficients at infinite dilution with the VTPR model [J].
Ahlers, J ;
Gmehling, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (23) :5890-5899
[2]   Corrosion electrochemistry of fuel element materials in pond storage conditions [J].
Burrows, R ;
Harris, S ;
Stevens, NPC .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2005, 83 (A7) :887-892
[3]   High-pressure (vapor plus liquid) equilibrium in binary mixtures of (carbon dioxide plus water or acetic acid) at temperatures from 313 to 353 K [J].
Bamberger, A ;
Sieder, G ;
Maurer, G .
JOURNAL OF SUPERCRITICAL FLUIDS, 2000, 17 (02) :97-110
[4]   Predictive use of a SAFT EOS for phase equilibria of some hydrocarbons and their binary mixtures [J].
Benzaghou, S ;
Passarello, JP ;
Tobaly, P .
FLUID PHASE EQUILIBRIA, 2001, 180 (1-2) :1-26
[5]   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
[6]   TERNARY PHASE-EQUILIBRIA FOR ACETIC ACID-WATER MIXTURES WITH SUPERCRITICAL CARBON-DIOXIDE [J].
BRIONES, JA ;
MULLINS, JC ;
THIES, MC ;
KIM, BU .
FLUID PHASE EQUILIBRIA, 1987, 36 :235-246
[7]  
BRUNNER G, 1986, GER CHEM ENG, V9, P246
[8]   SAFT prediction of vapour-liquid equilibria of mixtures containing carbon dioxide and aqueous monoethanolamine or diethanolamine [J].
Button, JK ;
Gubbins, KE .
FLUID PHASE EQUILIBRIA, 1999, 158 :175-181
[9]   A new apparatus for the determination of P-x-y diagrams and Henry's constants in high pressure alcohols with critical carbon dioxide [J].
Chang, CMJ ;
Chiu, KL ;
Day, CY .
JOURNAL OF SUPERCRITICAL FLUIDS, 1998, 12 (03) :223-237
[10]   Modification of PSRK mixing rules and results for vapor-liquid equilibria, enthalpy of mixing and activity coefficients at infinite dilution [J].
Chen, J ;
Fischer, K ;
Gmehling, J .
FLUID PHASE EQUILIBRIA, 2002, 200 (02) :411-429