Modeling vapor liquid equilibrium of ionic liquids + gas binary systems at high pressure with cubic equations of state

Brazilian Journal of Chemical Engineering

Volumn 30, Issue 1, 2013, Pages 63-73

  Freitas, A C D ^a   Cunico, L P ^a   Aznar, M ^a   Guirardello, R ^a  

^a UNIVERSITY OF CAMPINAS   (Brazil)

Author keywords

Ionic liquids; PR and SRK Eos; Vapor liquid equilibria

Indexed keywords

AVERAGE ABSOLUTE RELATIVE DEVIATIONS; BINARY INTERACTION PARAMETER; CUBIC EQUATIONS OF STATE; ENVIRONMENTALLY BENIGN; SRK EOS; TEMPERATURE INCREASE; VAN DER WAALS MIXING RULE; VAPOR-LIQUID EQUILIBRIUM;

EQUATIONS OF STATE OF GASES; IONIC LIQUIDS; PHASE EQUILIBRIA; SYSTEMS (METALLURGICAL); VAN DER WAALS FORCES; VAPORS;

BINARY MIXTURES;

EID: 84875417272     PISSN: 01046632     EISSN: None     Source Type: Journal    
DOI: 10.1590/S0104-66322013000100008     Document Type: Conference Paper

References (58)

1. Alvarez, V. H., Larico, R., Ianos, Y., Aznar, M., Parameter estimation for VLE calculation by global minimization: the genetic algorithm. Braz. J. Chem. Eng., 25,409(2008).
2. 2 in 1-hexyl-3-methylpyridinium bis (trifluoromethylsulfonyl) imide: comparison to other ionic liquids. Acc. Chem. Res., 40,1208(2007).
3. Anthony, J. L., Anderson, J. L., Maginn, E. J., Brennecke, J. F., Anion effects on gas solubility in ionic liquids. J. Phys. Chem., B, 109,6366(2005).
4. Anthony, J. L., Maginn, E. J., Brennecke, J. F., Solubilities and thermodynamics properties of gases in the ionic liquid 1-n-butyl-3- methylimidazolium hexafluorophosphate. J. Phys. Chem., B, 106,7315(2002).
5. Anthony, J. L., Maginn, E. J., Brennecke, J. F., Solution thermodynamics of imidazolium based ionic liquids and water. J. Phys. Chem., B, 105,10942(2001).
6. Arce, P. F., Robles, P. A., Graber, T. A., Aznar, M., Modeling of high-pressure vapor-liquid equilibrium in ionic liquids + gas systems using the PRSV equation of state. Fluid Phase Equilib., 295,9(2010).
7. Bermudez, M. D., Jiménez, A. E., Sanes, J., Carrion. J. F., Ionic liquid as advanced lubricant fluids. Molecules, 14,2888(2009).
8. Blanchard, L. A., Brennecke, J. F., Recovery of organic products from ionic liquids using supercritical carbon dioxide. Ind. Eng. Chem. Res., 40,287(2001).
9. 2 systems. J. Phys. Chem., B, 105,2437(2001).
10. 2. Nature, 399,28(1999).
11. 2 so soluble in imidazolium based ionic liquids? J. Am. Chem. Soc., 126,5300(2004).
12. Carvalho, P. J., Álvarez, V. H., Machado, J. J. B., Pauly, J., Daridon, J. L., Marrucho, I. M., Aznar, M., Coutinho, J. A. P. High pressure phase behavior of carbon dioxide in 1-alkyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide ionic liquids. J. Supercrit. Fluids, 48,99(2009b).
13. Carvalho, P. J., Álvarez, V. H., Marrucho, I. M., Aznar, M., Coutinho, J. A. P., High pressure phase behavior of carbon dioxide in 1-butyl-3-methylimidazolium bis (trifluormethylsulfonyl) imide and 1-butyl-3methylimidazolium dicyanamide ionic liquids. J. Supercrit. Fluids, 50, 105 (2009a).
14. 2 + imidazolium ionic liquids based on bis [(trifluoromethyl) sulfonyl] imide anion. J. Eng. Thermophys., 20,487(2011).
15. DIADEM Public v. 1.2 - DIPPR® - Design Institute for Physical Property Data. Information and Data Evaluation Manager (2000).
16. Fadeev, A. G., Meagher, M. M. Opportunities for ionic liquids in recovery of biofuels. Chem. Commun., 295,295(2001).
17. Florusse, L. J., Raeissi, S., Peters, C. J., High-pressure phase behavior of ethane with 1-hexyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide. J. Chem. Eng. Data, 53,1283(2008).
18. Gamse, T., Marr, R., High-pressure phase equilibria of the binary systems carvone-carbon dioxide and limonene-carbon dioxide at 30, 40 and 50 °C. Fluid Phase Equilib., 171,165(2000).
19. Gamse, T., Marr, R., Phase equilibrium properties of the 1-phenylethanol-carbon dioxide and 2-octanol-carbon dioxide binary system at 303.15, 313.15 and 323.15 K. J. Chem. Eng. Data, 46,117(2001).
20. Hermann, W. A., Bohn, V. P. W., Heck reaction catalized by phospha-palladacycles in nonaqueous ionic liquids. J. Organomet. Chem., 572,141(1999).
21. Hert, D. G., Anderson, J. L., Aki, S. N. V. K., Brennecke, J. F., Enhancement of oxygen and methane solubility in 1-hexyl-3-methylimidaxolium bis (trifluoromethylsulfonyl) imide using carbon dioxide. Chem. Comm., 20,2603(2005).
22. 2+1-butyl-3-methylimidazolium chloride system. Fluid Phase Equilib., 299,216(2010).
23. Jessop, P. G., Leitner, W., Chemical Synthesis Using Supercritical Fluids. Wiley-VCH: Weinheim (1999).
24. Kroon, M. C., Shariati, A., Costantini, M., van Spronsen, J., Witkamp, G. J., Sheldon, R. A., Peters, C. J., 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, 50,173(2005).
25. 6]/methanol system at elevated pressure. Chem. Eur. J., 9,3897(2003).
26. Nelder, J. A., Mead, R., A Simplex method for function minimization. Comput. J., 7,308(1965).
27. 2 for 1-hexyl-3methylimidazolium bromide with 1-bromohexane and 1 methylimidazolium. J. Supercrit. Fluids, 51,1(2009).
28. Peng, D. Y., Robinson, D. B., A new two-constant equation of state. Ind. Eng. Chem. Res., 15,59(1976).
29. Petkov, S., Pfohl, O., Brunner, G., PE 2000 allows for implementation of EOS by users. 18th European Seminar on Applied Thermodynamics; KutnáHora, Czech Republic, June 8-11, 2000. Abstract 2 (2000).
30. PFohl, O., Petkov, S., Brunner, G., PE2000: A Powerful Tool to Correlate Phase Equilibrium. Herbert UtzVerlag, München (2000).
31. Ren, W., Scurto, A. M., Global phase behavior of imidazolium ionic liquids in compressed 1,1,1, 2-tetrafluoroethane (R-134a). AIChE J., 55,486(2009b).
32. Ren, W., Scurto, A. M., Phase equilibria of imidazolium ionic liquids and the refrigerant gas 1,1,1, 2 - tetrafluoroethane (R-134a). Fluid Phase Equilib., 286,1(2009a).
33. 2) +n-alkylimidazolium bis (trifluoromethylsulfonyl) amide} ionic liquids. J. Chem. Thermodyn., 42,305(2010).
34. Schwarz, C. E., Nieuwoudt, L., Phase equilibrium of propane and alkanes. Part II: Hexatriacontane through hexacontane. J. Supercrit. Fluid, 27,145(2003a).
35. Schwarz, C. E., Nieuwoudt, L., Phase equilibrium of propane and alkanes. Part I. Experimental procedures, dotriacontane equilibrium and EOS modeling. J. Supercrit. Fluid, 27,133(2003b).
36. Scurto, A. M., Leitner, W., Expanding the useful range of ionic liquids: melting point depression of organic salts with carbon dioxide for biphasic catalytic reactions. Chem. Comm., 35,3681(2006).
37. 2: Phase equilibria. Ind. Eng. Chem. Res., 47,493(2008).
38. Seddon, K. R., Room temperature ionic liquids: Neoteric solvents for clean catalysis. Kinet. Catal., 37,693(1995).
39. Shariati, A., Peters, C. J., High pressure phase behavior of systems with ionic liquids: Measurements and modeling of the binary systems fluoroform + 1-ethyl-3-methylimidazolium hexafluorophosphate. J. Supercrit. Fluids, 25,109(2003).
40. Shariati, A., Gutkowski, K., Peters, C. J., Comparison of the phase behavior of some selected binary systems with ionic liquids. Phys. Chem. Mol. Thermodyn., 51,1532(2005).
41. Shariati, A., Peters, C. J., High pressure phase equilibria of systems with ionic liquids. J. Supercrit. Fluids, 34,171(2005).
42. Shariati, A., Peters, C. J., High-pressure phase behavior of systems with ionic liquids: Part III. The binary system carbon dioxide + 1-hexyl-3-methylimidazolium hexafluorophosphate. J. Supercrit. Fluids, 30,139(2004).
43. Shin, E. K., Lee, B. C., Lim, J. S., High pressure solubilities of carbon dioxide in ionic liquids: 1-alkil-3-methylimidazolium bis (trifluoromethylsulfonyl) imide. J. Supercrit. Fluids, 45,282(2008).
44. Soave, G., Equilibrium constants from a modified Redlich-Kwong equation of state. Chem. Eng. Sci., 27,1197(1972).
45. Solinas, M., Pfaltz, A., Cozzi, P. G., Leitner, W., Enantio-selective hydrogenation of imines in ionic liquid/carbon dioxide media. J. Am. Chem. Soc., 126,16142(2004).
46. Souza, R. F., Padilha, J. C., Gonçalves, R. S., Dupont, J., Room temperature dialkylimidazolium ionic liquids-based fuel cells. Electrochem. Comm., 5,728(2003).
47. Teodorescu, M., Lugo, L., Fernandez, J., Modeling of gas solubility data for HFCs-lubricant oil binary systems by means of the SRK equation of state. Int. J. Thermophys., 24,1043(2003).
48. Valderrama, J. O., Urbina, F., Faúndez, C. A., Gas Liquid equilibrium modeling of mixtures containing supercritical carbon dioxide and an ionic liquid. J. Supercrit. Fluids, 64,32(2012).
49. Valderrama, J. O., Reategui, A., Sanga, W. W., Thermodynamic consistency test of vapor-liquid equilibrium data for mixtures containing ionic liquids. Ind. Eng. Chem. Res., 47,1318(2008b).
50. Valderrama, J. O., Robles, P. A., Critical properties, normal boiling temperatures, and acentric factors of fifty ionic liquids. Ind. Eng. Chem. Res., 46,1338(2007).
51. Valderrama, J. O., Rojas, R. E., Critical properties of ionic liquids revisited. Ind. Eng. Chem. Res., 48,6890(2009).
52. Valderrama, J. O., Sanga, W. W., Lazzús, J. A., Critical properties, normal boiling temperature, and acentric factor of another 200 ionic liquids. Ind. Eng. Chem. Res., 47,1318(2008a).
53. Visser, A. E., Swatloskim, W. M., Reichert, W. M., Griffin, S. T., Rogers, R. D., Traditional extractants in nontraditional solvents: groups 1 and 2 extraction by crown ethers in room temperature ionic liquids. Ind. Eng. Chem. Res., 39,3596(2000).
54. Welton, T., Room temperature ionic liquids. Solvents for synthesis and catalysis. Chem. Rev., 99,2071(1999).
55. Wong, D. S. H., Sandler, S. I., A theoretically correct mixing rule for cubic equations of state. AIChE J., 38,671(1992).
56. 2 Route. Green Chem., 7,701(2005).
57. 2 using ionic liquids. Catal. Today, 115,61(2006).
58. Zhou, Z., Wang, T., Xing, H., Butyl-3-methylimidazolium chloride preparation in supercritical carbon dioxide. Ind. Eng. Chem. Res., 45,525(2006).