[1] R. Deshmukh, A. E. Mather, “A mathematical model for equilibrium solubility of hydrogen sulfide and carbon dioxide in aqueous alkanolamine solutions,” Journal of Chemical Engineering Science, vol. 36, pp. 355-362, 1981.
[2] M. Posey, K. G. Tapperson, G. T. Rochelle, “A simple model for prediction of acid gas solubilities in alkanolamines,” Journal of Gas Separation and Purification, vol. 1, pp. 181-186, 1996.
[3] P. Patil, Z. Malik, M. Jobson, “Prediction of CO2 and H2S Solubility in aqueous MDEA solutions using an extended Kent and Eisenberg model,” Institution of Chemical Engineers Symposium Series, vol. 152, pp. 498-510, 2006.
[4] P. Huttenhuis, N. J. Agrawal, G. F. Versteeg, “Solubility of Carbon Dioxide and Hydrogen Sulfide in Aqueous N-Methyldiethanolamine Solutions,” Journal of Industrial and Engineering Chemistry, vol. 48, pp. 4051–4059, 2009.
[5] Y. Zhang, H. Que, C. C. Chen, “Thermodynamic modelling for CO2 absorption in Aqueous MEA Solution with electrolyte NRTL model,” Journal of Fuel and Energy Abstracts, vol. 311, pp. 67-75, 2011.
[6] Y. Zhang, C. C. Chen, “Thermodynamic modelling for CO2 absorption in Aqueous MDEA Solution with electrolyte NRTL model,” Journal of Industrial and Engineering Chemistry, vol. 50, pp. 163-175, 2011.
[7] E. Hansen, “Aspen HYSYS and Aspen Plus simulation programs for CO2 absorption,” Master's thesis, Telemark University College, Faculty of Technology, 2011.
[8] L. E. Øi, “Removal of CO2 from exhaust gas,” M. C. Melaaen, revision of Ph.D. Dissertation Telemark University College Faculty of Technolo at porsgrumm, Norway, 2012.
[9] L. E. Øi, “Comparison of Aspen HYSYS and Aspen Plus simulation of CO2 absorption into MEA from atmospheric gas,” Journal of Energy procedia, vol. 23, pp. 360-369, 2012.
[10] Optimize the entire gas process with acid gas cleaning. Available at: http://www.Aspentech .com/ products/V8-releash-prior, August 2013.
[11] C. C. Chen, H. I. Britt, J. F. Boston, L. B. Evans, “Local composition model for excess Gibbs energy of electrolyte systems,” AIChE Journal, vol. 28, pp. 588, 1982.
[12] ASPEN Physical Property system, Physical Property Methods and Models, chap.11.1.
[13] M. L. Posey, G. T. Rochelle, “A Thermodynamic Model of Methyldiethanolamine-CO2-H2S-Water,” Industrial & Engineering Chemistry Research, vol. 36, pp. 3944-3953, 1997.
[14] R. S. Boumedine, S. Horstmann, K. Fischer, E. Provost, W. Furst, J. Gmehling, “Experimental determination of carbon dioxide solubility data in aqueous alkanolamine solutions,” Fluid Phase Equilibria, vol. 218, pp. 85-94, 2004.
[15] R. S. Boumedine, S. Horstmann, K. Fischer, E. Provost, W. Furst, J. Gmehling, “Experimental determination of hydrogen sulfide solubility data in aqueous alkanolamine solutions,” Fluid Phase Equilibria, vol. 218, pp. 149-155, 2004.
[16] M. Dicko, C. Coquelet, C. Jarne, S. Northrop, D. Richon, “Acid gases partial pressures above a 50 wt% aqueous methyldiethanolamine solution: Experimental work and modelling,” Fluid Phase Equilibria, vol. 289, pp. 99-109, 2010.
[17] F. Y. Jou, F. Otto, A. Mather, “The solubility of mixtures of H2S and CO2 in an MDEA solution,” The Canadian Journal of Chemical Engineering, vol. 75, pp. 1138-1141, 1997.
[18] P. Huttenhuis, N. J. Agrawal, G. F. Versteeg, “Solubility of carbon dioxide and hydrogen sulfide in aqueous N-methyldiethanolamine solutions,” Industrial & Engineering Chemistry Research, vol. 48, pp. 4051-4059, 2009.
[19] B. S. Ali, M. K. Aroua, “Effect of piperazine on CO2 loading in aqueous solutions of MDEA at low pressure,” International Journal of Thermophysics, vol. 25, pp. 1863-1870, 2004.
[20] S. Bishnoi, G. T. Rochelle, “Thermodynamics of piperazine/methyldiethanolamine/water/ carbon dioxide,” Industrial & Engineering Chemistry Research, vol. 41, pp. 604-612, 2002.
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