Issue
Korean Journal of Chemical Engineering,
Vol.31, No.9, 1656-1660, 2014
Experimental determination and prediction of phase behavior for 1-butyl-3-methylimidazolium nonafluorobutyl sulfonate and carbon dioxide
The vapor-liquid equilibrium of the binary system CO2+1-butyl-3-methylimidazolium nonafluorobutyl sulfonate ([BMIM][NfO]) was measured over a temperature range of 298.2-323.2 K at intervals of 5.0 K for CO2 mole fraction ranging from 0.137 to 0.900 using a high-pressure variable-volume view cell. The Peng-Robinson equation of state was then applied with two-parameter mixing rules over the same range and the results compared with the experimentally obtained data. Increasing the alkyl chain length in perfluorinated sulfonate from methyl to butyl markedly increased the CO2 solubility. To investigate the effect of the number of fluorine atoms in the anion on the phase behavior of imidazolium based ionic liquid, these experimental results were then compared with those reported in previous experimental studies of 1-alkyl-3-methylimidazolium cations and with modeling data. It looks likely that both the number of fluorine atoms in the anion and the presence of S=O groups play an important role in designing CO2-philic molecules.
[References]
  1. Privalova E, Nurmi M, Maranon MS, Murzina EV, Maki-Arvela P, Eranen K, Murzin DY, Mikkola JP, Sep. Purif. Technol., 97, 42, 2012
  2. Kodama D, Kanakubo M, Kokubo M, Ono T, Kawanami H, Yokoyama T, Nanjo H, Kato M, J. Supercrit. Fluids, 52(2), 189, 2010
  3. Wappel D, Gronald G, Kalb R, Draxler J, Int’l. J. Greenhouse Gas Control, 4, 486, 2010
  4. Seo DW, Lim YD, Lee SH, Ur SC, Kim WG, Bull. Korean Chem. Soc., 32, 2633, 2011
  5. Shannon MS, Bara JE, Ind. Eng. Chem. Res., 50(14), 8665, 2011
  6. Hwang S, Park Y, Park K, J. Chem. Thermodyn., 43(3), 339, 2011
  7. Aki SNVK, Mellein BR, Saurer EM, Brennecke JF, J. Phys. Chem. B, 108(52), 20355, 2004
  8. Shin EK, Lee BC, J. Chem. Eng. Data, 53(12), 2728, 2008
  9. Hwang S, Park Y, Park K, J. Chem. Eng. Data, 57(8), 2160, 2012
  10. Bell PW, Thote AJ, Park Y, Gupta RB, Roberts CB, Ind. Eng. Chem. Res., 42(25), 6280, 2003
  11. Gaikwad DS, Park Y, Pore DM, Tetrahedron Lett., 53, 3077, 2012
  12. http://webbook.nist.gov/chemistry/fluid accessed on 28 December, 2012
  13. Valderrama JO, Robles PA, Ind. Eng. Chem. Res., 46(4), 1338, 2007
  14. Pfohl O, Petkov S, Brunner G, PE 2000-A powerful tool to correlate phase equilibria, Herbert Utx Verlag, Muchen, 2000
  15. Ren W, Scurto AM, Rev. Sci. Instrum., 78, 125104, 2007
  16. Yazdizadeh M, Rahmani F, Forghani AA, Korean J. Chem. Eng., 28(1), 246, 2011
  17. Wang X, Chen J, Mi JG, Ind. Eng. Chem. Res., 52(2), 954, 2013
  18. Shariati A, Gutkowski K, Peters CJ, AIChE J., 51(5), 1532, 2005
  19. Kim YS, Choi WY, Jang JH, Yoo KP, Lee CS, Fluid Phase Equilib., 228, 439, 2005
  20. Muldoon MJ, Aki SNVK, Anderson JL, Dixon JK, Brennecke JF, J. Phys. Chem. B, 111(30), 9001, 2007
  21. Valderrama JO, Sanga WW, Lazzus JA, Ind. Eng. Chem. Res., 47(4), 1318, 2008