[1] A. Afsharpour, A. Haghtalab, Simultaneous measurement absorption of CO2 and H2S mixture into aqueous solutions containing diisopropanolamine blended with 1-butyl-3-methylimidazolium acetate ionic liquid, Int. J. Greenh. Gas Control. 58 (2017) 71-80 [2] A. Haghtalab, A. Afsharpour, Solubility of CO2 + H2S gas mixture into different aqueous N-methyldiethanolamine solutions blended with 1-butyl-3-methylimidazolium acetate ionic liquid, Fluid Phase Equilibria 406 (2015) 10-20 [3] R. Macías-Salinas, J.A. Chávez-Velasco, M.A. Aquino-Olivos, J.L. Mendoza de la Cruz, J.C. Sánchez-Ochoa, Accurate modeling of CO2 solubility in ionic liquids using a cubic EoS, Ind. Eng. Chem. Res. 52 (22) (2013) 7593-7601 [4] E. Voutsas, C. Perakis, G. Pappa, D. Tassios, An evaluation of the performance of the Cubic-Plus-Association equation of state in mixtures of non-polar, polar and associating compounds:Towards a single model for non-polymeric systems, Fluid Phase Equilibria 261 (1-2) (2007) 343-350 [5] X.Y. Ji, C. Held, G. Sadowski, Modeling imidazolium-based ionic liquids with ePC-SAFT, Fluid Phase Equilibria 335 (2012) 64-73 [6] X.Y. Ji, C. Held, G. Sadowski, Modeling imidazolium-based ionic liquids with ePC-SAFT. Part II. Application to H2S and synthesis-gas components, Fluid Phase Equilibria 363 (2014) 59-65 [7] H. Soltani Panah, Modeling H2S and CO2 solubility in ionic liquids using the CPA equation of state through a new approach, Fluid Phase Equilibria 437 (2017) 155-165 [8] A. Shojaeian, Thermodynamic modeling of solubility of hydrogen sulfide in ionic liquids using Peng Robinson-Two State equation of state, J. Mol. Liq. 229 (2017) 591-598 [9] A. Afsharpour, Application of reaction equilibrium thermodynamic model for correlation of H2S solubility in ionic liquids[emim] [Ace] and[hmim] [Ace] using CPA equation of state, Petroleum Sci. Technol. 37 (14) (2019) 1648-1654 [10] A. Afsharpour, A. Kheiri, Implementation of CPA EoS for simultaneous solubility modeling of CO2 and H2S in ionic liquid[OMIM] [Tf2N, Petroleum Sci. Technol. 36 (4) (2018) 280-286 [11] A. Afsharpour, A. Kheiri, The solubility of acid gases in the ionic liquid[C8mim] [PF6, Petroleum Sci. Technol. 36 (3) (2018) 232-238 [12] A. Kheiri, A. Afsharpour, The CPA EoS application to model CO2 and H2S simultaneous solubility in ionic liquid[C2mim] [PF6, Petroleum Sci. Technol. 36 (13) (2018) 944-950 [13] A. Kheiri, A. Afsharpour, M.B.Z. Talavaki, Modeling of acid gases solubility in ionic liquid[BMIM] [MeSO4] using CPA EoS, Petroleum Sci. Technol. 36 (4) (2018) 319-325 [14] K. Huang, D.N. Cai, Y.L. Chen, Y.T. Wu, X.B. Hu, Z.B. Zhang, Thermodynamic validation of 1-alkyl-3-methylimidazolium carboxylates as task-specific ionic liquids for H2S absorption, AIChE J. 59 (6) (2013) 2227-2235 [15] G.M. Kontogeorgis, G.K. Folas, Thermodynamic Models for Industrial Applications:From Classical and Advanced Mixing Rules to Association Theories, Wiley, USA, 2009 [16] M.B. Shiflett, A. Yokozeki, Separation of CO2 and H2S using room-temperature ionic liquid[bmim] [PF6], Fluid Phase Equilibria 294 (1-2) (2010) 105-113 [17] J.O. Valderrama, P.A. Robles, Critical properties, normal boiling temperatures, and acentric factors of fifty ionic liquids, Ind. Eng. Chem. Res. 46 (4) (2007) 1338-1344 [18] J.Y. Wang, H.C. Jiang, Y.M. Liu, Y.Q. Hu, Density and surface tension of pure 1-ethyl-3-methylimidazolium l-lactate ionic liquid and its binary mixtures with water, J. Chem. Thermodyn. 43 (5) (2011) 800-804 [19] X.X. Ma, J. Wei, Q.B. Zhang, F. Tian, Y.Y. Feng, W. Guan, Prediction of thermophysical properties of acetate-based ionic liquids using semiempirical methods, Ind. Eng. Chem. Res. 52 (27) (2013) 9490-9496 [20] J.L. Shereshefsky, Surface tension of saturated vapors and the equation of eötvös, J. Phys. Chem. 35 (6) (1931) 1712-1720 [21] E.A. Guggenheim, The Principle of Corresponding States, The Journal of Chemical Physics, 13 (1945) 253-261 [22] M. Hong, A. Sun, Q. Yang, W. Guan, J. Tong, J.Z. Yang, Studies on properties of ionic liquids 1-alkyl-3-methylimidazolium lactate at temperatures from (288.15 to 333.15) K, J. Chem. Thermodyn. 67 (2013) 91-98 [23] M. Hong, A. Sun, C. Liu, W. Guan, J. Tong, J.Z. Yang, Physico-chemical properties of 1-alkyl-3-methylimidazolium propionate ionic liquids {[Cnmim] [pro](n=3, 4, 5, 6)} from 288.15 K to 328.15 K, Ind. Eng. Chem. Res. 52 (44) (2013) 15679-15683 [24] J. Tong, X. Ma, Y.X. Kong, Y. Chen, W. Guan, J.Z. Yang, Ionic parachor and its application II. ionic liquid homologues of 1-alkyl-3-methylimidazolium propionate {[Cnmim] [pro] (n=2-6)}, J. Phys. Chem. B 116 (20) (2012) 5971-5976 [25] I. Tsivintzelis, G.M. Kontogeorgis, M.L. Michelsen, E.H. Stenby, Modeling phase equilibria for acid gas mixtures using the CPA equation of state. I. Mixtures with H2S, AIChE J. 56 (11) (2010) 2965-2982 |