CO2 Separation with Ionic Liquids

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CO2 Separation with Ionic Liquids ( co2-separation-with-ionic-liquids )

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[21] Redlich O, Kwong J. On the thermodynamics of solutions. V. An equation of state. Fugacities of gaseous solutions. Chem Rev 1949;44:233–44. [22] Lemmon E, McLinden M, Friend D. Thermophysical properties of fluid systems. NIST chemistry webbook. NIST standard reference database; 2005. p. 69. [23] Renon H, Prausnitz JM. Local compositions in thermodynamic excess functions for liquid mixtures. AIChE J 1968;14:135–44. [24] Kenarsari SD, Yang D, Jiang G, Zhang S, Wang J, Russell AG, et al. Review of recent advances in carbon dioxide separation and capture. RSC Adv 2013;3:22739–73. [25] Kim Y, Choi W, Jang J, Yoo KP, Lee C. Solubility measurement and prediction of carbon dioxide in ionic liquids. Fluid Phase Equilib 2005;228:439–45. [26] Soriano AN, Doma Jr BT, Li MH. Solubility of carbon dioxide in 1-ethyl-3- methylimidazolium tetrafluoroborate. J Chem Eng Data 2008;53:2550–5. [27] Lei Z, Yuan J, Zhu J. Solubility of CO2 in propanone, 1-ethyl-3- methylimidazolium tetrafluoroborate, and their mixtures. J Chem Eng Data 2010;55:4190–4. [28] Hwang S, Park Y, Park K. Measurement and prediction of phase behaviour for 1-alkyl-3-methylimidazolium tetrafluoroborate and carbon dioxide: effect of alkyl chain length in imidazolium cation. J Chem Thermodyn 2011;43:339–43. [29] Husson-Borg P, Majer V, Costa Gomes MF. Solubilities of oxygen and carbon dioxide in butyl methyl imidazolium tetrafluoroborate as a function of temperature and at pressures close to atmospheric pressure. J Chem Eng Data 2003;48:480–5. [30] Aki SN, Mellein BR, Saurer EM, Brennecke JF. High-pressure phase behavior of carbon dioxide with imidazolium-based ionic liquids. J Phys Chem B 2004;108:20355–65. [31] Cadena C, Anthony JL, Shah JK, Morrow TI, Brennecke JF, Maginn EJ. Why is CO2 so soluble in imidazolium-based ionic liquids? J Am Chem Soc 2004;126:5300–8. [32] Anthony JL, Anderson JL, Maginn EJ, Brennecke JF. Anion effects on gas solubility in ionic liquids. J Phys Chem B 2005;109:6366–74. [33] Kroon MC, Shariati A, Costantini M, van Spronsen J, Witkamp GJ, Sheldon RA, et al. High-pressure phase behavior of systems with ionic liquids: Part V. The binary system carbon dioxide + 1-butyl-3-methylimidazolium tetrafluoroborate. J Chem Eng Data 2005;50:173–6. [34] Shiflett MB, Yokozeki A. Solubilities and diffusivities of carbon dioxide in ionic liquids: [bmim][PF6] and [bmim][BF4]. Ind Eng Chem Res 2005;44:4453–64. [35] Chen Y, Zhang S, Yuan X, Zhang Y, Zhang X, Dai W, et al. Solubility of CO2 in imidazolium-based tetrafluoroborate ionic liquids. Thermochim Acta 2006;441:42–4. [36] Revelli AL, Mutelet F, Jaubert JN. High carbon dioxide solubilities in imidazolium-based ionic liquids and in poly (ethylene glycol) dimethylether. J Phys Chem B 2010;114:12908–13. [37] Costantini M, Toussaint VA, Shariati A, Peters CJ, Kikic I. High-pressure phase behavior of systems with ionic liquids: Part IV. Binary system carbon dioxide + 1-hexyl-3-methylimidazolium tetrafluoroborate. J Chem Eng Data 2005;50:52–5. [38] Yim JH, Lim JS. CO2 solubility measurement in 1-hexyl-3-methylimidazolium ([HMIM]) cation based ionic liquids. Fluid Phase Equilib 2013;352:67–74. [39] Blanchard LA, Gu Z, Brennecke JF. High-pressure phase behavior of ionic liquid/ CO2 systems. J Phys Chem B 2001;105:2437–44. [40] Gutkowski K, Shariati A, Peters C. High-pressure phase behavior of the binary ionic liquid system 1-octyl-3-methylimidazolium tetrafluoroborate + carbon dioxide. J Supercrit Fluids 2006;39:187–91. [41] Shariati A, Peters C. High-pressure phase behavior of systems with ionic liquids: II, The binary system carbon dioxide + 1-ethyl-3-methylimidazolium hexafluorophosphate. J Supercrit Fluids 2004;29:43–8. [42] Anthony JL, Maginn EJ, Brennecke JF. Solubilities and thermodynamic properties of gases in the ionic liquid 1-n-butyl-3-methylimidazolium hexafluorophosphate. J Phys Chem B 2002;106:7315–20. [43] Liu Z, Wu W, Han B, Dong Z, Zhao G, Wang J, et al. Study on the phase behaviors, viscosities, and thermodynamic properties of CO2/[C4mim][PF6]/ methanol system at elevated pressures. Chem Eur J 2003;9:3897–903. [44] Perez-Salado Kamps A, Tuma D, Xia J, Maurer G. Solubility of CO2 in the ionic liquid [bmim][PF6]. J Chem Eng Data 2003;48:746–9. [45] Shariati A, Gutkowski K, Peters CJ. Comparison of the phase behavior of some selected binary systems with ionic liquids. AIChE J 2005;51:1532–40. [46] Zhang S, Yuan X, Chen Y, Zhang X. Solubilities of CO2 in 1-butyl-3- methylimidazolium hexafluorophosphate and 1, 1, 3, 3- tetramethylguanidium lactate at elevated pressures. J Chem Eng Data 2005;50:1582–5. [47] Kumelan J, Kamps ÁPS, Tuma D, Maurer G. Solubility of CO2 in the ionic liquids [bmim][CH3SO4] and [bmim][PF6]. J Chem Eng Data 2006;51:1802–7. [48] Kim JE, Lim JS, Kang JW. Measurement and correlation of solubility of carbon dioxide in 1-alkyl-3-methylimidazolium hexafluorophosphate ionic liquids. Fluid Phase Equilib 2011;306:251–5. [49] Shariati A, Peters CJ. High-pressure phase behavior of systems with ionic liquids: Part III. The binary system carbon dioxide + 1-hexyl-3- methylimidazolium hexafluorophosphate. J Supercrit Fluids 2004;30:139–44. [50] Jacquemin J, Husson P, Majer V, Gomes MFC. Ntf2-Influence of the cation on the solubility of CO2 and H2 in ionic liquids based on the bis (trifluoromethylsulfonyl) imide anion. J Solution Chem 2007;36:967–79. [51] Schilderman AM, Raeissi S, Peters CJ. Solubility of carbon dioxide in the ionic liquid 1-ethyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide. Fluid Phase Equilib 2007;260:19–22. [52] Shin E-K, Lee B-C, Lim JS. High-pressure solubilities of carbon dioxide in ionic liquids: 1-Alkyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide. J Supercrit Fluids 2008;45:282–92. [53] Carvalho PJ, Álvarez VH, Machado JJ, Pauly J, Daridon JL, Marrucho IM, et al. High pressure phase behavior of carbon dioxide in 1-alkyl-3- methylimidazolium bis (trifluoromethylsulfonyl) imide ionic liquids. J Supercrit Fluids 2009;48:99–107. [54] Ren W, Sensenich B, Scurto AM. High-pressure phase equilibria of (carbon dioxide (CO2) + n-alkyl-imidazolium bis (trifluoromethylsulfonyl) amide) ionic liquids. J Chem Thermodyn 2010;42:305–11. [55] Oh DJ, Lee BC. High-pressure phase behavior of carbon dioxide in ionic liquid 1-butyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide. Korean J Chem Eng 2006;23:800–5. [56] Raeissi S, Peters CJ. Carbon dioxide solubility in the homologous 1-alkyl-3- methylimidazolium bis (trifluoromethylsulfonyl) imide family. J Chem Eng Data 2008;54:382–6. [57] Carvalho PJ, Álvarez VH, Marrucho IM, Aznar M, Coutinho JA. High pressure phase behavior of carbon dioxide in 1-butyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide and 1-butyl-3-methylimidazolium dicyanamide ionic liquids. J Supercrit Fluids 2009;50:105–11. [58] Safarov J, Hamidova R, Stephan M, Schmotz N, Kul I, Shahverdiyev A, et al. Henry constant – carbon dioxide solubility in 1-butyl-3-methylimidazolium- bis (trifluormethylsulfonyl) imide over a wide range of temperatures and pressures. J Chem Thermodyn 2013;67:181–9. [59] Kumełan J, Pérez-Salado Kamps Á, Tuma D, Maurer G. Solubility of CO2 in the ionic liquid [hmim][Tf2N]. J Chem Thermodyn 2006;38:1396–401. [60] Costa Gomes M. Low-pressure solubility and thermodynamics of solvation of carbon dioxide, ethane, and hydrogen in 1-hexyl-3-methylimidazolium bis (trifluoromethylsulfonyl) amide between temperatures of 283 K and 343 K. J Chem Eng Data 2007;52:472–5. [61] Kim Y, Jang J, Lim B, Kang J, Lee C. Solubility of mixed gases containing carbon dioxide in ionic liquids: measurements and predictions. Fluid Phase Equilib 2007;256:70–4. [62] Muldoon MJ, Aki SN, Anderson JL, Dixon JK, Brennecke JF. Improving carbon dioxide solubility in ionic liquids. J Phys Chem B 2007;111:9001–9. [63] Shiflett MB, Yokozeki A. Solubility of CO2 in room temperature ionic liquid [hmim][Tf2N]. J Phys Chem B 2007;111:2070–4. [64] Althuluth M, Mota-Martinez MT, Kroon MC, Peters CJ. Solubility of carbon dioxide in the ionic liquid 1-ethyl-3-methylimidazolium tris (pentafluoroethyl) trifluorophosphate. J Chem Eng Data 2012;57:3422–5. [65] Jalili AH, Shokouhi M, Maurer G, Hosseini-Jenab M. Solubility of CO2 and H2S in the ionic liquid 1-ethyl-3-methylimidazolium tris (pentafluoroethyl) trifluorophosphate. J Chem Thermodyn 2013;67:55–62. [66] Soriano AN, Doma BT, Li MH. Carbon dioxide solubility in 1-ethyl-3- methylimidazolium trifluoromethanesulfonate. J Chem Thermodyn 2009;41:525–9. [67] Jalili AH, Mehdizadeh A, Shokouhi M, Ahmadi AN, Hosseini-Jenab M, Fateminassab F. Solubility and diffusion of CO2 and H2S in the ionic liquid 1- ethyl-3-methylimidazolium ethylsulfate. J Chem Thermodyn 2010;42:1298–303. [68] Jung YH, Jung JY, Jin YR, Lee BC, Baek IH, Kim SH. Solubility of carbon dioxide in imidazolium-based ionic liquids with a methanesulfonate anion. J Chem Eng Data 2012;57:3321–9. [69] Mejía I, Stanley K, Canales R, Brennecke JF. On the high-pressure solubilities of carbon dioxide in several ionic liquids. J Chem Eng Data 2013;58:2642–53. [70] Wilcox J. Carbon capture. Springer; 2012. [71] Sanmamed YA, Navia P, González-Salgado D, Troncoso J, Romaní L. Pressure and temperature dependence of isobaric heat capacity for [Emim][BF4], [Bmim][BF4], [Hmim][BF4], and [Omim][BF4]. J Chem Eng Data 2009;55:600–4. [72] Holbrey JD, Reichert WM, Reddy R, Rogers R. Ionic liquids as green solvents: progress and prospects. In: ACS symposium series. DC: American Chemical Society Washington; 2003. p. 121–33. [73] Kabo GJ, Blokhin AV, Paulechka YU, Kabo AG, Shymanovich MP, Magee JW. Thermodynamic properties of 1-butyl-3-methylimidazolium hexafluorophosphate in the condensed state. J Chem Eng Data 2004;49:453–61. [74] Li JG, Hu YF, Ling S, Zhang JZ. Physicochemical properties of [C6mim][PF6] and [C6mim][(C2F5)3PF3] ionic liquids. J Chem Eng Data 2011;56:3068–72. [75] Ferreira AF, Simões PN, Ferreira AG. Quaternary phosphonium-based ionic liquids: thermal stability and heat capacity of the liquid phase. J Chem Thermodyn 2012;45:16–27. [76] Blokhin AV, Paulechka YU, Strechan AA, Kabo GJ. Physicochemical properties, structure, and conformations of 1-butyl-3-methylimidazolium bis (trifluoromethanesulfonyl) imide [C4mim] [NTf2] ionic liquid. J Phys Chem B 2008;112:4357–64. [77] Hughes TJ, Syed T, Graham BF, Marsh KN, May EF. Heat capacities and low temperature thermal transitions of 1-hexyl and 1-octyl-3-methylimidazolium bis (trifluoromethylsulfonyl) amide. J Chem Eng Data 2011;56:2153–9. [78] Crosthwaite JM, Muldoon MJ, Dixon JK, Anderson JL, Brennecke JF. Phase transition and decomposition temperatures, heat capacities and viscosities of pyridinium ionic liquids. J Chem Thermodyn 2005;37:559–68. Y. Xie et al. / Applied Energy 136 (2014) 325–335 335

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