Modeling gas solubility in ionic liquids with the SAFT-γ group contribution method

被引:39
作者
Ashrafmansouri, Seyedeh-Soghra [1 ]
Raeissi, Sona [1 ]
机构
[1] Shiraz Univ, Sch Chem & Petr Engn, Shiraz, Iran
关键词
CO2; Equation of state (EoS); Statistical associating fluid theory (SAFT); 1-Alkyl-3-methylimidazolium hexafluorophosphate ([C(n)mim][PF6]); 1-Alkyl-3-methylimidazolium tetrafluoroborate ([C(n)mim][BF4]); 1-Alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide ([C(n)mim][Tf2N]); DIRECTIONAL ATTRACTIVE FORCES; PRESSURE PHASE-BEHAVIOR; EQUATION-OF-STATE; THERMODYNAMIC PERTURBATION-THEORY; MULTIPLE BONDING SITES; CARBON-DIOXIDE; ASSOCIATING FLUIDS; CHAIN MOLECULES; VARIABLE RANGE; CO2;
D O I
10.1016/j.supflu.2011.12.014
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
Accurate knowledge of gas solubility is necessary for the development of processes involving ionic liquids (ILs) and gases. In this work, a group contribution approach is used to predict the phase behavior of CO2 + IL systems based on the statistical associating fluid theory (SAFT-gamma) as proposed by Lymperiadis et al. The IL molecule is divided into groups of CH3, CH2, cation head, and the anion. The SAFT-gamma parameters of CO2 + imidazolium-based ionic liquids with either [PF6], [BF4] or [Tf2N] anions are optimized to experimental data. The ability of the model to describe the phase behavior of these systems is demonstrated within a temperature range of 313.15-353.15K and pressures up to 100 bars. Moreover, by using the optimized group parameters, the performance of the model is examined by predicting equilibrium data of some CO2 + IL systems not included in the optimization database. The results show good agreement with experimental data. (C) 2012 Published by Elsevier B.V.
引用
收藏
页码:81 / 91
页数:11
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