Predicting the phase equilibria of CO2+ hydrocarbon systems with the PPR78 model (PR EOS and kij calculated through a group contribution method)

被引:195
作者
Vitu, Stephane [1 ]
Privat, Romain [1 ]
Jaubert, Jean-Noel [1 ]
Mutelet, Fabrice [1 ]
机构
[1] Univ Nancy 1, Lab Thermodynam Milieux Polyphases, F-54001 Nancy, France
关键词
equation of state; vapor-liquid equilibrium; predictive model; binary interaction parameters; critical locus; carbon dioxide;
D O I
10.1016/j.supflu.2007.11.015
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
In 2004, we started to develop a group contribution method aimed at estimating the temperature dependent binary interaction parameters (k(ij)(T)) for the widely used Peng-Robinson equation of state (EOS). Because our model relies on the Peng-Robinson EOS as published by Peng and Robinson in 1978 and because the addition of a group contribution method to estimate the kij makes it predictive, this model was called PPR78 (predictive 1978, Peng Robinson EOS). In our previous papers eleven groups were defined: CH3, CH2, CH, C, CH4 (methane), C2H6 (ethane), CHaro, C-aro, C-fused (aromatic rings), CH2,cyclic and CHcyclic = C-cyclic. It was thus possible to estimate the k(ij) for any mixture containing alkanes, aromatics and naphthenes at any temperature. In this study, the PPR78 model is extended to systems containing carbon dioxide. To do so, the group CO2 was added. The results obtained in this study are in many cases accurate. (C) 2007 Elsevier B.V. All rights reserved.
引用
收藏
页码:1 / 26
页数:26
相关论文
共 309 条
[1]   DEW AND BUBBLE POINT MEASUREMENTS FOR CARBON-DIOXIDE PROPANE MIXTURES [J].
ACOSTA, JC ;
HEVIA, E ;
LEIPZIGER, S .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1984, 29 (03) :304-309
[2]   NEW APPARATUS FOR MEASUREMENT OF SUPERCRITICAL FLUID-LIQUID PHASE-EQUILIBRIA [J].
ADAMS, WR ;
ZOLLWEG, JA ;
STREETT, WB ;
RIZVI, SSH .
AICHE JOURNAL, 1988, 34 (08) :1387-1391
[3]   LOW-TEMPERATURE PHASE EQUILIBRIA - CARBON DIOXIDE-PROPANE SYSTEM [J].
AKERS, WW ;
KELLEY, RE ;
LIPSCOMB, TG .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12) :2535-2536
[4]   BUBBLE POINT MEASUREMENTS FOR THE TERNARY-SYSTEM - CARBON-DIOXIDE, CYCLOHEXANE AND NAPHTHALENE [J].
ALSAHHAF, TA ;
ALAMEERI, RS ;
HAMAM, SEM .
FLUID PHASE EQUILIBRIA, 1989, 53 :31-37
[5]   LIQUID + VAPOR EQUILIBRIA IN THE N2+CO2+CH4 SYSTEM [J].
ALSAHHAF, TA ;
KIDNAY, AJ ;
SLOAN, ED .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1983, 22 (04) :372-380
[6]  
ANDERSON JM, 1986, J CHEM ENG DATA, V31, P172
[7]  
[Anonymous], CHEM ENG SUPERCRITIC
[8]  
Arai Y., 1971, J. Chem. Eng. Jpn, V4, P113
[9]   Modeling of critical lines and regions for binary and ternary mixtures using non-cubic and cubic equations of state [J].
Arce, Pedro ;
Aznar, Martin .
JOURNAL OF SUPERCRITICAL FLUIDS, 2007, 42 (01) :1-26
[10]   Computation and modeling of critical phenomena with the perturbed chain-statistical associating fluid theory equation of state [J].
Arce, Pedro F. ;
Aznar, Martin .
JOURNAL OF SUPERCRITICAL FLUIDS, 2008, 43 (03) :408-420