Commenced in January 2007
Frequency: Monthly
Edition: International
Paper Count: 33104
Modeling of CO2 Removal from Gas Mixtureby 2-amino-2-methyl-1-propanol (AMP) Using the Modified Kent Eisenberg Model
Authors: H. Pahlavanzadeh, A.R.Jahangiri, I. Noshadi
Abstract:
In this paper, the solubility of CO2 in AMP solution have been measured at temperature range of ( 293, 303 ,313,323) K.The amine concentration ranges studied are (2.0, 2.8, and 3.4) M. A solubility apparatus was used to measure the solubility of CO2 in AMP solution on samples of flue gases from Thermal and Central Power Plants of Esfahan Steel Company. The modified Kent Eisenberg model was used to correlate and predict the vapor-liquid equilibria of the (CO2 + AMP + H2O) system. The model predicted results are in good agreement with the experimental vapor-liquid equilibrium measurements.Keywords: AMP, Carbon dioxide; loading, Flue gases, Modified Kent Eisenberg model
Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1063310
Procedia APA BibTeX Chicago EndNote Harvard JSON MLA RIS XML ISO 690 PDF Downloads 2479References:
[1] S. van Loo, E.P. van Elk, G.F. Versteeg, Journal of Petroleum Science and Engineering, 135-145, 55,( 2007).
[2] Masoud Mofarahi, Yaser Khojasteh, Hiwa Khaledi, Arsalan Farahnak, , Energy, 131-145,42(2009).
[3] B.P. Mandal, S.S. Bandyopadhyayb, Chemical Engineering Science, 5440 - 5447, 61(2006).
[4] Sartori, G., Savage, D.W. Industrial and Engineering Chemistry Fundamentals , 239-249, 22(1983).
[5] Kent, R. L. and Eisenberg, B., Hydrocarbon Process, ,(2): 87, 55(1976).
[6] Kritpiphat,W. and Tontiwachwuthikul, P, Chem Eng Comm, 144: 73, (1996).
[7] M.L. Posey, K.G. Tapperson, G.T. Rochelle, Gas. Sep. Purif. 181-186, 10 (1996).
[8] S.H. Park, K.B. Lee, J.C. Hyun, S.H. Kim, Ind. Eng. Chem. Res. 1658- 1665 , 41 (2002).
[9] J. Gabrielsen, M.L. Michelsen, E.H. Stenby, G.M. Kontogeorgis, Ind. Eng. Chem. Res,3348-3354,44 ( 2005).
[10] Deshmukh, R. D. and Mather, A. E.,. Chem Eng Sci, 36: 355( 1981).
[11] Austgen, D. M., Rochelle, G. T., Peng, X. and Chen, C, Ind Eng Chem Res, 28: 1060(1989).
[12] A. Haghtalab and M. Dehghani Tafti, The 11th Iranian Chemical Engineering Congress (ICHEC11), , November 28-30 ( 2006).
[13] G.R. Pazukia, , H. Pahlevanzadeh, A. Mohseni Ahooei, , 27-32, 30 ( 2006).
[14] Hassan Pahlavanzadeh and Masoumeh Farazar, Korean J. Chem. Eng, 1112-111826(4), (2009).
[15] Danckwerts, P. V. and McNeil, K. M, Trans IChemE, 45: T31(1967).
[16] M. Z. Haji-sulaiman, M. K. Aroua and A. Benamor , Institution of Chemical Engineers Trans IChemE, Part A ,76(1998).
[17] Haji-Sulaiman, M. Z. and Aroua, M. K.,. Chem Eng Comm, , 140: 157. (1996).
[18] M.K. Aroua, M.Z. Haji-Sulaiman, K. Ramasamy, Separation and Purification Technology, 153-162, 29 (2002).