CO2 Separation with Ionic Liquids

PDF Publication Title:

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

Previous Page View | Next Page View | Return to Search List

Text from PDF Page: 136

80 Y. Xie et al. / Applied Energy 175 (2016) 69–81 [4] Lantz M. The economic performance of combined heat and power from biogas produced from manure in Sweden – a comparison of different CHP technologies. Appl Energy 2012;98:502–11. [5] Kao CY, Chiu SY, Huang TT, Dai L, Hsu LK, Lin CS. Ability of a mutant strain of the microalga Chlorella sp. to capture carbon dioxide for biogas upgrading. Appl Energy 2012;93:176–83. [6] Bauer F, Hulteberg C, Persson T, Tamm D. Biogas upgrading-review of commercial technologies. SGC Rapport 2013;270. [7] Cozma P, Ghinea C, Ma ̆ ma ̆ liga ̆ I, Wukovits W, Friedl A, Gavrilescu M. Environmental impact assessment of high pressure water scrubbing biogas upgrading technology. CLEAN–Soil Air Water 2013;41:917–27. [8] Cozma P, Wukovits W, Mamaliga I, Friedl A, Gavrilescu M. Modeling and simulation of high pressure water scrubbing technology applied for biogas upgrading. Clean Technol Environ Pol 2014:1–19. [9] Blanchard LA, Gu Z, Brennecke JF. High-pressure phase behavior of ionic liquid/ CO2 systems. J Phys Chem B 2001;105:2437–44. [10] 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. [11] Anthony JL, Anderson JL, Maginn EJ, Brennecke JF. Anion effects on gas solubility in ionic liquids. J Phys Chem B 2005;109:6366–74. [12] Jacquemin J, Husson P, Majer V, Gomes MFC. Influence of the cation on the solubility of CO2 and H2 in ionic liquids based on the bis (trifluoromethylsulfonyl) imide anion. J Solut Chem 2007;36:967–79. [13] Almeida HF, Teles ARR, Lopes-da-Silva JA, Freire MG, Coutinho JA. Influence of the anion on the surface tension of 1-ethyl-3-methylimidazolium-based ionic liquids. J Chem Thermodyn 2012;54:49–54. [14] 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 Solut Chem 2007;36:967–79. [15] Xie Y, Zhang Y, Lu X, Ji X. Energy consumption analysis for CO2 separation using imidazolium-based ionic liquids. Appl Energy 2014;136:325–35. [16] Basha OM, Heintz YJ, Keller MJ, Luebke DR, Resnik KP, Morsi BI. Development of a conceptual process for selective capture of CO2 from fuel gas streams using two TEGO ionic liquids as physical solvents. Indust Eng Chem Res 2014;53:3184–95. [17] Basha OM, Keller MJ, Luebke DR, Resnik KP, Morsi BI. Development of a conceptual process for selective CO2 capture from fuel gas streams using [hmim][Tf2N] ionic liquid as a physical solvent. Energy Fuels 2013;27:3905–17. [18] Huang Y, Zhang X, Zhang X, Dong H, Zhang S. Thermodynamic modeling and assessment of ionic liquid-based CO2 capture processes. Indust Eng Chem Res 2014;53:11805–17. [19] Shiflett MB, Shiflett AD, Yokozeki A. Separation of tetrafluoroethylene and carbon dioxide using ionic liquids. Separ Purif Technol 2011;79:357–64. [20] Xu Y, Huang Y, Wu B, Zhang X, Zhang S. Biogas upgrading technologies: energetic analysis and environmental impact assessment. Chin J Chem Eng. 2015;23:247–54. [21] Ma C, Xie Y, Liu C, Ji X, Lu X. Modeling and simulation of biogas upgrading using aqueous choline chloride/urea. In: The 8th Sino-US joint conference of chemical engineering, shanghai, China; 2015. [22] Valderrama J, Robles P. Critical properties, normal boiling temperatures, and acentric factors of fifty ionic liquids. Indust Eng Chem Res 2007;46:1338–44. [23] Valderrama JO, Rojas RE. Critical properties of ionic liquids Revisited. Indust Eng Chem Res 2009;48:6890–900. [24] Kilaru P, Baker GA, Scovazzo P. Density and surface tension measurements of imidazolium-, quaternary phosphonium-, and ammonium-based room- temperature ionic liquids: data and correlations. J Chem Eng Data 2007;52:2306–14. [25] Ghatee MH, Zolghadr AR. Surface tension measurements of imidazolium- based ionic liquids at liquid–vapor equilibrium. Fluid Phase Equil 2008;263:168–75. [26] 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. [27] Holbrey J, Reichert WM, Reddy RG, Rogers RD. Heat capacities of ionic liquids and their applications as thermal fluids; 2010. [28] Ahosseini A, Sensenich B, Weatherley LR, Scurto AM. Phase equilibrium, volumetric, and interfacial properties of the ionic liquid, 1-hexyl-3- methylimidazolium bis (trifluoromethylsulfonyl) amide and 1-octene. J Chem Eng Data 2009;55:1611–7. [29] De Azevedo RG, Esperanca J, Szydlowski J, Visak Z, Pires P, Guedes H, et al. Thermophysical and thermodynamic properties of ionic liquids over an extended pressure range:[bmim][NTf2] and [Hmim][NTf2]. J Chem Thermodyn 2005;37:888–99. [30] Esperança JM, Guedes HJ, Lopes JNC, Rebelo LPN. Pressure􏰐Density􏰐Temperature (p􏰐q􏰐T) surface of [C6mim][NTf2]. J Chem Eng Data 2008;53:867–70. [31] González EJ, Domínguez Á, Macedo EA. Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide ionic liquid and polar organic compounds. J Chem Thermodyn 2012;47:300–11. [32] Kandil ME, Marsh KN, Goodwin AR. Measurement of the viscosity, density, and electrical conductivity of 1-hexyl-3-methylimidazolium bis (trifluorosulfonyl) imide at temperatures between (288 and 433) K and pressures below 50 MPa. J Chem Eng Data 2007;52:2382–7. [33] Muhammad A, Mutalib MA, Wilfred C, Murugesan T, Shafeeq A. Thermophysical properties of 1-hexyl-3-methyl imidazolium based ionic liquids with tetrafluoroborate, hexafluorophosphate and bis (trifluoromethylsulfonyl) imide anions. J Chem Thermodyn 2008;40:1433–8. [34] Tokuda H, Hayamizu K, Ishii K, Susan MABH, Watanabe M. Physicochemical properties and structures of room temperature ionic liquids. 2. Variation of alkyl chain length in imidazolium cation. J Phys Chem B 2005;109:6103–10. [35] Widegren JA, Magee JW. Density, viscosity, speed of sound, and electrolytic conductivity for the ionic liquid 1-hexyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide and its mixtures with water. J Chem Eng Data 2007;52:2331–8. [36] Ahosseini A, Scurto AM. Viscosity of imidazolium-based ionic liquids at elevated pressures: cation and anion effects. Int J Thermophys 2008;29:1222–43. [37] Ahosseini A, Weatherley LR, Scurto AM. Viscosity and diffusivity for the ionic liquid 1-hexyl-3-methyl-imidazolium bis (trifluoromethylsulfonyl) amide with 1-octene. J Chem Eng Data 2011;56:3715–21. [38] Tokuda H, Tsuzuki S, Susan MABH, Hayamizu K, Watanabe M. How ionic are room-temperature ionic liquids? An indicator of the physicochemical properties. J Phys Chem B 2006;110:19593–600. [39] Carvalho PJ, Freire MG, Marrucho IM, Queimada AJ, Coutinho JA. Surface tensions for the 1-alkyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide ionic liquids; 2008. [40] Klomfar J, Soucˇková M, Pátek J. Surface tension measurements with validated accuracy for four 1-alkyl-3-methylimidazolium based ionic liquids. J Chem Thermodyn 2010;42:323–9. [41] 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. [42] Shimizu Y, Ohte Y, Yamamura Y, Saito K, Atake T. Low-temperature heat capacity of room-temperature ionic liquid, 1-hexyl-3-methylimidazolium bis (trifluoromethylsulfonyl) imide. J Phys Chem B 2006;110:13970–5. [43] de Castro CAN, Langa E, Morais AL, Lopes MLM, Lourenço MJ, Santos FJ, et al. Studies on the density, heat capacity, surface tension and infinite dilution diffusion with the ionic liquids [C4mim][NTf2],[C4mim][dca],[C2mim][EtOSO3] and [Aliquat][dca]. Fluid Phase Equil 2010;294:157–79. [44] Jacquemin J, Husson P, Mayer V, Cibulka I. High-pressure volumetric properties of imidazolium-based ionic liquids: effect of the anion. J Chem Eng Data 2007;52:2204–11. [45] Katsuta S, Shiozawa Y, Imai K, Kudo Y, Takeda Y. Stability of ion pairs of bis (trifluoromethanesulfonyl) amide-based ionic liquids in dichloromethane. J Chem Eng Data 2009;55:1588–93. [46] Troncoso J, Cerdeiriña CA, Sanmamed YA, Romaní L, Rebelo LPN. Thermodynamic properties of imidazolium-based ionic liquids: densities, heat capacities, and enthalpies of fusion of [Bmim][PF6] and [bmim][NTf2]. J Chem Eng Data 2006;51:1856–9. [47] Vranes M, Dozic S, Djeric V, Gadzuric S. Physicochemical characterization of 1- butyl-3-methylimidazolium and 1-butyl-1-methylpyrrolidinium bis (trifluoromethylsulfonyl) imide. J Chem Eng Data 2012;57:1072–7. [48] Wandschneider A, Lehmann JK, Heintz A. Surface tension and density of pure ionic liquids and some binary mixtures with 1-propanol and 1-butanol. J Chem Eng Data 2008;53:596–9. [49] Jacquemin J, Husson P, Padua AA, Majer V. Density and viscosity of several pure and water-saturated ionic liquids. Green Chem 2006;8:172–80. [50] Geppert-Rybczyn ́ska M, Lehmann JK, Safarov J, Heintz A. Thermodynamic surface properties of [BMIm][NTf2] or [EMIm][NTf2] binary mixtures with tetrahydrofuran, acetonitrile or dimethylsulfoxide. J Chem Thermodyn 2013;62:104–10. [51] 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. [52] Chaudhary GR, Bansal S, Mehta S, Ahluwalia A. Thermophysical and spectroscopic studies of room temperature ionic liquid, 1-butyl-3- methylimidazolium hexafluorophosphate in Tritons. J Chem Thermodyn 2012;50:63–70. [53] Fan W, Zhou Q, Sun J, Zhang S. Density, excess molar volume, and viscosity for the methyl methacrylate + 1-butyl-3-methylimidazolium hexafluorophosphate ionic liquid binary system at atmospheric pressure. J Chem Eng Data 2009;54:2307–11. [54] Gu Z, Brennecke JF. Volume expansivities and isothermal compressibilities of imidazolium and pyridinium-based ionic liquids. J Chem Eng Data 2002;47:339–45. [55] Huo Y, Xia S, Ma P. Densities of ionic liquids, 1-butyl-3-methylimidazolium hexafluorophosphate and 1-butyl-3-methylimidazolium tetrafluoroborate, with benzene, acetonitrile, and 1-propanol at T = (293.15 to 343.15) K. J Chem Eng Data 2007;52:2077–82. [56] Kumar A. Estimates of internal pressure and molar refraction of imidazolium based ionic liquids as a function of temperature. J Solut Chem 2008; 37:203–14. [57] Pereiro AB, Legido JL, Rodrı A. Physical properties of ionic liquids based on 1-alkyl-3-methylimidazolium cation and hexafluorophosphate as anion and temperature dependence. J Chem Thermodyn 2007;39:1168–75. [58] Seddon KR, Stark A, Torres MJ. Viscosity and density of 1-alkyl-3- methylimidazolium ionic liquids. Clean Solv 2002;819:34–49.

PDF Image | CO2 Separation with Ionic Liquids

PDF Search Title:

CO2 Separation with Ionic Liquids

Original File Name Searched:

co2-separation-ionic-liquids.pdf

DIY PDF Search: Google It | Yahoo | Bing

NFT (Non Fungible Token): Buy our tech, design, development or system NFT and become part of our tech NFT network... More Info

IT XR Project Redstone NFT Available for Sale: NFT for high tech turbine design with one part 3D printed counter-rotating energy turbine. Be part of the future with this NFT. Can be bought and sold but only one design NFT exists. Royalties go to the developer (Infinity) to keep enhancing design and applications... More Info

Infinity Turbine IT XR Project Redstone Design: NFT for sale... NFT for high tech turbine design with one part 3D printed counter-rotating energy turbine. Includes all rights to this turbine design, including license for Fluid Handling Block I and II for the turbine assembly and housing. The NFT includes the blueprints (cad/cam), revenue streams, and all future development of the IT XR Project Redstone... More Info

Infinity Turbine ROT Radial Outflow Turbine 24 Design and Worldwide Rights: NFT for sale... NFT for the ROT 24 energy turbine. Be part of the future with this NFT. This design can be bought and sold but only one design NFT exists. You may manufacture the unit, or get the revenues from its sale from Infinity Turbine. Royalties go to the developer (Infinity) to keep enhancing design and applications... More Info

Infinity Supercritical CO2 10 Liter Extractor Design and Worldwide Rights: The Infinity Supercritical 10L CO2 extractor is for botanical oil extraction, which is rich in terpenes and can produce shelf ready full spectrum oil. With over 5 years of development, this industry leader mature extractor machine has been sold since 2015 and is part of many profitable businesses. The process can also be used for electrowinning, e-waste recycling, and lithium battery recycling, gold mining electronic wastes, precious metals. CO2 can also be used in a reverse fuel cell with nafion to make a gas-to-liquids fuel, such as methanol, ethanol and butanol or ethylene. Supercritical CO2 has also been used for treating nafion to make it more effective catalyst. This NFT is for the purchase of worldwide rights which includes the design. More Info

NFT (Non Fungible Token): Buy our tech, design, development or system NFT and become part of our tech NFT network... More Info

Infinity Turbine Products: Special for this month, any plans are $10,000 for complete Cad/Cam blueprints. License is for one build. Try before you buy a production license. May pay by Bitcoin or other Crypto. Products Page... More Info

CONTACT TEL: 608-238-6001 Email: greg@infinityturbine.com (Standard Web Page)