Issue
Korean Journal of Chemical Engineering,
Vol.33, No.7, 2191-2204, 2016
Volumetric properties of binary mixtures of 1-butyl-3-methylimidazolium halides with water, methanol or ethanol at 293.15 to 318.15 K
Densities of nine binary solutions made of one of three 1-butyl-3-methylimidazolium ([bmim]) halides with water, methanol, or ethanol were measured at atmospheric pressure. The compositions of an ionic liquid ([bmim]Cl, [bmim]Br, or [bmim]I) were increased up to 0.4 as a mole fraction at a given temperature within a range of 293.15 to 318.15 K. The measured values were correlated by a quadratic equation to obtain a temperature dependency of the respective systems. Furthermore, the equation was used to obtain the volume expansivity, which would be used for a pressure-volume-temperature behavior of a condensed phase. The apparent molar volumes were also calculated from the experimental data. The remarkable distinction of the volumetric property behavior between aqueous and nonaqueous solutions was found and attributed to strong ion.solvent interactions in the aqueous systems.
[References]
  1. Kirchner B, Ed., Ionic Liquids, Springer, New York (2010).
  2. Anthony JL, Maginn EJ, Brennecke JF, J. Phys. Chem. B, 105(44), 10942, 2001
  3. Dupont J, de Souza RF, Suarez PAZ, Chem. Rev., 102(10), 3667, 2002
  4. Hayyan M, Mjalli FS, Hashim MA, AlNashef IM, Mei TX, J. Ind. Eng. Chem., 19(1), 106, 2013
  5. Betz D, Altmann P, Cokoja M, Herrmann WA, Kuhn FE, Coord. Chem. Rev., 255, 1518, 2011
  6. Tian D, Han Y, Lu C, Zhang X, Yuan G, Carbohydr. Polym., 113, 83, 2014
  7. Chen WJ, Lou WT, Yu CY, Wu H, Zong MH, Smith TJ, J. Biotechnol., 162, 183, 2012
  8. Kim KS, Park SY, Choi S, Lee H, J. Power Sources, 155(2), 385, 2006
  9. Shin BS, Kim ES, Kwak SK, Lim JS, Kim KS, Kang JW, Fluid Phase Equilib., 382, 270, 2014
  10. Jayakumar M, Venkatesan KA, Srinivasan TG, Electrochim. Acta, 53(6), 2794, 2008
  11. Baj S, Krawczyk T, Dabrowska A, Siewniak A, Sobolewski A, Korean J. Chem. Eng., 32(11), 2295, 2015
  12. Kim KS, Shin BK, Lee H, Ziegler F, Fluid Phase Equilib., 218(2), 215, 2004
  13. Fan GZ, Liao CJ, Fang T, Wang M, Song GS, Fuel Process. Technol., 116, 142, 2013
  14. He XK, Hou BL, Li C, Zhu QY, Jiang YM, Wu LY, Electrochim. Acta, 130, 245, 2014
  15. Bonhote P, Dias AP, Papageorgiou N, Kalyanasundaram K, Gratzel M, Inorg. Chem., 35(5), 1168, 1996
  16. Domanska U, Marciniak A, J. Chem. Eng. Data, 48(3), 451, 2003
  17. Domanska U, Bogel-Lukasik E, Bogel-Lukasik R, J. Phys. Chem. B, 107(8), 1858, 2003
  18. Swatloski RP, Visser AE, Reichert WM, Broker GA, Farina LM, Holbrey JD, Rogers RD, Green Chem., 4, 81, 2002
  19. Letcher TM, Deenadayalu N, Soko B, Ramjugernath D, Naicker PK, J. Chem. Eng. Data, 48(4), 904, 2003
  20. Huddleston JG, Visser AE, Reichert WM, Willauer HD, Broker GA, Rogers RD, Green Chem., 3, 156, 2001
  21. Yang QW, Zhang H, Su BG, Yang YW, Ren QL, Xing HB, J. Chem. Eng. Data, 55(4), 1750, 2010
  22. Lal B, Sahin M, Ayranci E, J. Chem. Thermodyn., 54, 142, 2012
  23. Matkowska D, Hofman T, J. Mol. Liq., 177, 301, 2013
  24. Sadeghi R, Shekaari H, Hosseini R, J. Chem. Thermodyn., 41(2), 273, 2009
  25. Sastry NV, Vaghela NM, Macwan PM, J. Mol. Liq., 180, 12, 2013
  26. Zafarani-Moattar MT, Shekaari H, J. Chem. Thermodyn., 37(10), 1029, 2005
  27. Wen W, Saito S, J. Phys. Chem., 68, 2639, 1964