[1] Pacheco M.A., Rochelle G.T., Rate-Based Modeling of Reactive Absorption of CO2 and H2S into Aqueous Methyldiethanolamine, Ind. Eng. Chem. Res., 37, p. 4107 (1998).
[2] Bolhar N., Friedl A., Koss U., Tork T., Modeling SelectiveH2S Absorption and Desorption in an Aqueous MDEA-Solution Using a Rate-Based Nonequilibrium Approach, Chem. Eng. Proc., 43, p. 701 (2004).
[3] Pandya J.D., Adiabatic Gas Absorption and Stripping with Chemical Reaction in Packed Towers, Chem. Eng. Commun., 19, p. 343 (1983).
[4] Tontiwachwuthikul P., Meisen, A., Lim CJ., CO2 Absorption by NaOH- Monoethanolamine and 2-Amino-2-Methyl-1-Propanol Solutions in a Packed Column, Chem Eng Sci., 47, p. 381 (1992).
[5] Gabrielsen J., Michelsen M.L., Stenby E.H., Kontogeorgis G.M., Modeling of CO2 Absorber Using an AMP Solution, AIChE J., 52, p. 3443 (2006).
[6] Mandal B. P., Biswas A. K., Bandyopadhyay S.S., Selective Absorption of H2S from Gas Streams Containing H2S and CO2 in Aqueous Solutions of N-Methyldiethanolamine and 2-Amino-2-Methyl-1-Propanol., Sep. Purif. Technol., 35, p. 191 (2004).
[7] Posey M.L., Rochelle G.T., A Thermodynamic Model of Methyldiethanolamine-CO2-H2S-Water, Ind. Eng. Chem. Res., 36 (9), p. 3944 (1997).
[8] Posey M., "Thermodynamic Model for Acid Gas Loaded Aqueous Alkanolamine Solutions", Ph.D. Dissertation, the University of Texas at Austin, Austin, TX, (1996).
[9] Al-Ghawas H.A., Hagewiesche D.P., Ruiz-Ibanez G., Sandall O.C., Physicochemical Properties Important for Carbon Dioxide Absorption in Aqueous Methyldiethanolamine, J. Chem. Eng. Data, 34(4), p. 385 (1989).
[10] Little R.J., Van Swaaij W.P.M., Versteeg G.F., Kinetics of CO2 with Tertiary Amines in Aqueous Solutions, AIChE J., 3 (11), p. 1633 (1990).
[11] Meng-Hui Li., Jiun-Jie KO., Kinetics of Absorption of Carbon Dioxide into Solutions of N-Methyldiethanolamine+Water, Chem. Eng. Sci., 55, p. 4139 (2000).
[12] Jamal A., Meisen A., Jim C., Kinetics of Carbon Dioxide Absorption and Desorption in Aqueous Alkanolamine Solutions Using a Novel Hemispherical Contactor-II. Experimental Results and Parameter Estimation, Chem. Eng. Sci., 61, p. 6590 (2006).
[13] Mandal B., Shyamalendu S., Bandyopadhyay S., Simultaneous Absorption of CO2 and H2S into Aqueous Blends of N-Methyldiethanolamine and Diethanolamine, Environ. Sci. Technol., 40 (19), p. 6076 (2006).
[14] Onda K., Takeuchi H., Okumoto Y., Mass Transfer Coefficients between Gas and Liquid Phases in Packed Columns, J.Chem. Eng. Jpn., 1, p. 56 (1968).
[15] Bird R.B., Stewart, W.E., Lightfoot E.N., “Transport Phenomena”, John Wiley & Sons, New York, (1960).
[16] Ayyaz M., Abdul Mutalib M., Wilfred C., Murugesan T., ShafeeqA., Viscosity, Refractive Index, Surface Tension, and Thermal Decomposition of Aqueous N-Methyldiethanolamine Solutions from 298.15 to 338.15 K., J. Chem. Eng. Data, 53, p. 2226 (2008).
[17] Rinker E.B., Hanna O.T., Sandall O.C., Asymptotic Models for H2S Absorption into Single and Blended Aqueous Amines, AIChE J., 43(1), p. 58 (1997).
[18] Snijder E.D., Te Riel, M.J.M., Versteeg G.F., van Swaaij W.P.M., Diffusion Coefficients of Several Aqueous AlkanolamineSolutions, J. Chem. Eng. Data, 38, p. 475 (1993).
[19] Reid R.C., Poling BE., “The Properties of Gases and Liquids”, 4th Ed., New York, McGraw-Hill, (1987).
[20] Design Institute for Physical Properties, “DIPPR Evaluated Pure Component Database”, American Institute of Chemical Engineers, New York, (2005).
[21] Chiu L-F., Liu H-F., Li M-H., Heat Capacity of Alkanolamines by Differential Scanning Calorimetry., J. Chem. Eng. Data, 44, p. 631 (1999).
[22] "Engineering Data Book, Physical Properties", 12th ed., Sec. 23, Gas Processors Supply Association, Tulsa, Oklahoma, (2004).
[23] Barbara M., Hvard L., Sandall C., Physical Solubility of Hydrogen Sulfide in Aqueous Solutions of 2-(tert-Butylaminoo PDF) ethanol, J. Chem. Eng. Data, 45 (6), p. 1201 (2000).
[24] Afkhamipour M., Khorrami Z., Gholizadeh A., Rate-Based Modeling for CO2 Absorption into AMP Solution in a Random Packed Column., IPCBEE, 14, p. 135 (2011).
[25] "Operating Manual of Refinery Phases 4&5 of South Pars Gas Company".
[26] Kasiri N., Ghayyem M.A.,Rate Based Model in H2S and CO2 Absorption Column Using Alkanolamine Solutions., Int. J. Eng. Sci., 19, p. 89 (2008).