Solubility of the Single Gases Carbon Dioxide and Hydrogen in the Ionic Liquid [bmpy][Tf2N]

被引:77
作者
Kumelan, Jacek [1 ]
Tuma, Dirk [1 ]
Kamps, Alvaro Perez-Salado [1 ]
Maurer, Gerd [1 ]
机构
[1] Univ Kaiserslautern, Dept Mech & Proc Engn, D-67653 Kaiserslautern, Germany
关键词
CO2; H-2; TEMPERATURE; PRESSURES;
D O I
10.1021/je900298e
中图分类号
O414.1 [热力学];
学科分类号
摘要
Experimental data for the Solubility of the two single gases carbon dioxide and hydrogen in the ionic liquid 1-n-butyl-l-methylpyrrolidinium bis(trifluoromethylsulfonyl)amide ([bmpy][Tf2N]) are reported for temperatures between (293.1 and 413.2) K. The maximum pressure (the maximum gas molality in the solvent) was 10.8 MPa (4.43 mol.kg(-1)) for carbon dioxide and 8.9 MPa (0.14 mol.kg(-1)) for hydrogen. The experiments were performed using a high-pressure view-cell technique operating oil the synthetic method. The solubility of carbon dioxide in [bmpy][Tf2N] is more than 1 order of magnitude higher than the solubility of hydrogen. Carbon dioxide becomes less Soluble in [bmpy][Tf2N] with increasing temperature, whereas hydrogen shows the opposite effect. An extension of Henry's law is employed to correlate the solubility pressures. The final results for the Henry's constant (Lit zero pressure) of carbon dioxide and hydrogen in [bmpy][Tf2N] (on the molality scale) are represented within the experimental uncertainty (about 0.8 % for carbon dioxide and 1.3 % for hydrogen) by In(k(H.CO2)((0))/MPa) = 8.5128 - 2057/(T/K) - 0.004274.(T/K) and In(k(H,H2)((0))/MPa) = 3.5746 + 343/(T/K) - 0.0008.(T/K), respectively.
引用
收藏
页码:165 / 172
页数:8
相关论文
共 23 条
[1]   High-pressure phase behavior of carbon dioxide with imidazolium-based ionic liquids [J].
Aki, SNVK ;
Mellein, BR ;
Saurer, EM ;
Brennecke, JF .
JOURNAL OF PHYSICAL CHEMISTRY B, 2004, 108 (52) :20355-20365
[2]  
[Anonymous], 2006, THERMOFLUIDS VERSION
[3]  
Anthony JL, 2005, J PHYS CHEM B, V109, P6366, DOI 10.1021/jp0464041
[4]   Determination of hydrogen concentration in ionic liquids and the effect (or lack of) on rates of hydrogenation [J].
Dyson, PJ ;
Laurenczy, G ;
Ohlin, CA ;
Vallance, J ;
Welton, T .
CHEMICAL COMMUNICATIONS, 2003, (19) :2418-2419
[5]   GENERALIZED METHOD FOR PREDICTING 2ND VIRIAL-COEFFICIENTS [J].
HAYDEN, JG ;
OCONNELL, JP .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1975, 14 (03) :209-216
[6]   Solubility of carbon dioxide and ethane in three ionic liquids based on the bis{(trifluoromethyl)sulfonyl}imide anion [J].
Hong, G. ;
Jacquemin, J. ;
Deetlefs, M. ;
Hardacre, C. ;
Husson, P. ;
Gomes, M. F. Costa .
FLUID PHASE EQUILIBRIA, 2007, 257 (01) :27-34
[7]   Experimental measurement of the solubility and diffusivity of CO2 in room-temperature ionic liquids using a transient thin-liquid-film method [J].
Hou, Ying ;
Baltus, Ruth E. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2007, 46 (24) :8166-8175
[8]   Influence of the cation on the solubility of CO2 and H2 in ionic liquids based on the bis(trifluoromethylsulfonyl)imide anion [J].
Jacquemin, Johan ;
Husson, Pascale ;
Majer, Vladimir ;
Gomes, Margarida F. Costa .
JOURNAL OF SOLUTION CHEMISTRY, 2007, 36 (08) :967-979
[9]   Solubility of CO2 in the ionic liquid [bmim][PF6] [J].
Kamps, APS ;
Tuma, D ;
Xia, JZ ;
Maurer, G .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2003, 48 (03) :746-749
[10]   Solubility of H2 in the ionic liquid [bmim][PF6] [J].
Kumelan, J ;
Kamps, APS ;
Tuma, D ;
Maurer, G .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2006, 51 (01) :11-14