Predicting the Solubility of CO2 in Toluene plus Ionic Liquid Mixtures with PC-SAFT

被引:20
|
作者
Canales, Roberto I. [1 ,2 ]
Held, Christoph [1 ]
Lubben, Michael J. [3 ]
Brennecke, Joan F. [3 ]
Sadowski, Gabriele [1 ]
机构
[1] TU Dortmund, Dept Biochem & Chem Engn, Lab Thermodynam, Emil Figge Str 70, D-44227 Dortmund, Germany
[2] Pontificia Univ Catolica Chile, Dept Ingn Quim & Bioproc, Av Vicuna Mackenna 4860, Santiago, Chile
[3] Univ Notre Dame, Dept Chem & Biomol Engn, Notre Dame, IN 46556 USA
关键词
CARBON-DIOXIDE SOLUBILITY; PRESSURE PHASE-BEHAVIOR; PERTURBED-CHAIN SAFT; ALIPHATIC-HYDROCARBONS; BINARY-SYSTEMS; EQUATION; EQUILIBRIUM; SOLVENT; STATE; BIS(TRIFLUOROMETHYLSULFONYL)IMIDE;
D O I
10.1021/acs.iecr.7b01497
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Perturbed-chain statistical associating fluid theory (PC-SAFT) was applied for modeling the vaporliquid equilibrium of CO2 + toluene + ionic liquid (IL) mixtures and the molar volume of their liquid phases at temperatures between 298.15 K and 333.15 K and at pressures up to 80 bar. ILs used for this study contain the bis(trifluoromethylsulfonylimide) anion ([Tf2N]-) and imidazolium, pyridinium, thiolanium, and phosphonium cations. The pure-IL PC-SAFT parameters were fit to pure-IL liquid density data. Temperature-dependent binary interaction parameters were fit to binary liquidliquid equilibrium data (i.e., toluene + IL) obtained from the literature and some points measured for this work. Temperature independent binary interaction parameters were fit to vaporliquid equilibrium data (CO2 + IL, CO2 + toluene) from the literature. The availability of the pure-IL parameters and binary interaction parameters allowed prediction of CO2 solubility in toluene + IL mixtures with an absolute average relative deviation (AARD) of 6.8%, as well as molar volumes of CO2 + toluene + IL mixtures with an AARD of 5.0%, for the four ternary systems under investigation.
引用
收藏
页码:9885 / 9894
页数:12
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