Issue
Korean Journal of Chemical Engineering,
Vol.26, No.4, 1130-1136, 2009
High-pressure solubility of carbon dioxide in imidazolium-based ionic liquids with anions [PF6] and [BF4]
The solubility of carbon dioxide in three ionic liquids (ILs) under supercritical fluid condition was measured at pressures up to 32 MPa and at temperatures of 313.15, 323.15, and 333.15 K in a high-pressure view cell. The imidazolium-derivative ionic liquids 1-butyl-3-methylimidazolium hexafluorophosphate ([bmim][PF6]), 1-butyl-3-methylimidazolium tetrafluoroborate ([bmim][BF4]), and 1-octyl-3-methylimidazolium tetrafluoroborate ([omim][BF4]) were employed in this research. The effects of pressure, temperature, nature of anion and cation as well as the water content on the solubility of CO2 in the ILs were investigated experimentally. The solubility of CO2 in the IL was higher for the ILs with longer cationic alkyl group and for the ILs with lower anion polarity. The lower the water content or the lower the temperature as well as the higher the pressure, the higher was the solubility of CO2.
[References]
  1. Keskin S, Kayrak-Talay D, Akman U, Hortacsu O, J. Supercrit. Fluids, 43(1), 150, 2007
  2. Kim HS, Kim YJ, News. Inf. Chem. Eng., 21, 200, 2003
  3. Cadena C, Anthony JL, Shah JK, Morrow TI, Brennecke JF, Maginn EJ, J. Am. Chem. Soc., 126(16), 5300, 2004
  4. Dupont J, de Souza RF, Suarez PAZ, Chem. Rev., 102(10), 3667, 2002
  5. Welton T, Chem. Rev., 99(8), 2071, 1999
  6. Olivier-Bourbigou H, Magna L, J. Mol. Catal. A-Chem., 182(1), 419, 2002
  7. Aki SNVK, Mellein BR, Saurer EM, Brennecke JF, J. Phys. Chem. B, 108(52), 20355, 2004
  8. Wu W, Zhang J, Han B, Chen J, Liu Z, Jiang T, He J, Li W, Chem. Commun., 1412, 2003
  9. Blanchard LA, Brennecke JF, Ind. Eng. Chem. Res., 40(1), 287, 2001
  10. Blanchard LA, Gu ZY, Brennecke JF, J. Phys. Chem. B, 105(12), 2437, 2001
  11. Muldoon MJ, Aki SNVK, Anderson JL, Dixon JK, Brennecke JF, J. Phys. Chem. B, 111(30), 9001, 2007
  12. Fu D, Sun X, Pu J, Zhao S, J. Chem. Eng. Data, 51, 371, 2006
  13. Gutkowski KI, Shariati A, Peters CJ, J. Supercrit. Fluids, 39(2), 187, 2006
  14. Perez-Salado Kamps A, Tuma D, Xia J, Maurer G, J. Chem. Eng. Data, 48, 746, 2003
  15. Kumelan J, Perez-Salado Kamps A, Tuma D, Maurer G, J. Chem. Eng. Data, 51, 1802, 2006
  16. Chen YH, Zhang SJ, Yuan XL, Zhang YQ, Zhang XP, Dai WB, Mori R, Thermochim. Acta, 441(1), 42, 2006
  17. Kim YS, Choi WY, Jang JH, Yoo KP, Lee CS, Fluid Phase Equilib., 228, 439, 2005
  18. Shiflett MB, Yokozeki A, Ind. Eng. Chem. Res., 44(12), 4453, 2005
  19. Liu Z, Wu W, Han B, Dong Z, Zhao G, Wang J, Jiang T, Yang G, Chem. Eur. J., 9, 3897, 2003
  20. Lim BH, Shim JJ, Clean Technol., 14(4), 248, 2008
  21. Ely JF, CO2PAC: A Computer Program to Calculate Physical Properties of Pure CO2, National Institute of Science and Technology: Boulder, CO, 1986
  22. Cammarata L, Kazarian SG, Salter PA, Welton T, Phys. Chem. Chem. Phys., 3, 5192, 2001
  23. Kazarian SG, Briscoe BJ, Welton T, Chem. Commun., 2047, 2000