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Carbon Dioxide Removal from Flue Gas Using Amine-Based Hybrid Solvent Absorption
Authors: Supitcha Rinprasertmeechai, Sumaeth Chavadej, Pramoch Rangsunvigit, Santi Kulprathipanja
Abstract:
This study was to investigate the performance of hybrid solvents blended between primary, secondary, or tertiary amines and piperazine (PZ) for CO2 removal from flue gas in terms of CO2 absorption capacity and regeneration efficiency at 90 oC. Alkanolamines used in this work were monoethanolamine (MEA), diethanolamine (DEA), and triethanolamine (TEA). The CO2 absorption was experimentally examined under atmospheric pressure and room temperature. The results show that MEA blend with PZ provided the maximum CO2 absorption capacity of 0.50 mol CO2/mol amine while TEA provided the minimum CO2 absorption capacity of 0.30 mol CO2/mol amine. TEA was easier to regenerate for both first cycle and second cycle with less loss of absorption capacity. The regeneration efficiency of TEA was 95.09 and 92.89 %, for the first and second generation cycles, respectively.Keywords: CO2 absorption capacity, regeneration efficiency, CO2 removal, flue gas
Digital Object Identifier (DOI): doi.org/10.5281/zenodo.1332828
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[1] Yeh, A.C., and Bai, H. (1999). Comparison of ammonia and monoethanolamine solvents to reduce CO2 greenhouse gas emissions. The Science of the Total Environment, 228, 3121-133.
[2] Zhang, P., Yao, S., Jianwen, W., Zhao, W., and QingY.(2008). Regeneration of 2-amino-2-methyl-1-propanol used for carbon dioxide absorption. Journal of Environmental Sciences, 20, 39-44.
[3] Kyoto Protocol, (2009). Status of Ratification. United Nations Framework Convention on Climate Change. 2009-01-14.
[4] Aroonwilas, A., and Veawab, A. (2004). Characterization and comparison of the CO2 absorption performance into single and blended alkanolamines in a packed column. Industrial & Engineering Chemistry Research, 43, 2228-2237.
[5] Ritter, J.A., and Ebner, A.D. (2004). Carbon Dioxide Separation Technology: R&D Needs For the Chemical and Petrochemical Industries:
[6] Charkravarty, T., Phukan, U.K., and Weiland, R.H. (1985). Reaction of acid gases with mixtures of amines. Chemical Engineering Progress, 81, 32-36.
[7] Cavenati, S., Grand, C.A., and Rodrigues, A.E. (2006). Removal of carbon dioxide from natural gas by vacuum pressure swing adsorption. Thermochimica Acta, 410, 23-26.
[8] Kotowicz, J.,Chmielniak, T., and Szymanska, K.J. (2010). The influence of membrane CO2 separation on the efficiency of a coal-fired power plant. Energy, 35, 841-850.
[9] White, C.M., Strazisar, B.R., Granite, E.J., Hoffman, J.S., and Pennline, H.W. (2003). Separation and capture of CO2 from large stationary sources and sequestration in geological formations - Coalbeds and deep saline. Journal of The Air & Waste Management Association, 53, 645-715.
[10] Kohl, A.L., and Reisenfeld, F.C. (1985). Gas Purification. Houston, Texas: Gulf Publishing.
[11] Park, S.W., Choi, B.S., and Lee, J.W. (2006). Chemical absorption of carbon dioxide with triethanolamine in non aqueous solutions. Korean Journal Chemical Engineering, 23(1), 138-143.
[12] Astarita, G., Savage, D.W., and Bisio, A. (1983) Gas Treating with Chemical Solvents, New York: John Wiley.
[13] Polasek, J., and Bullin J.A. (2006). Selecting amines for sweetening units. Bryan Research and Engineering, 1-9.
[14] Xu, G.W., Zhang, C.F., Qin, S.J., and Wang, Y.W. (1992). Kinetics study on absorption of carbon dioxide into solutions of activated methyldiethanolamine. Industrial & Engineering Chemistry Research, 31, 921-927.
[15] Tobiesen, F.A., and Svendsen H. F. (2006). Study of a modified aminebased regeneration unit. Industrial & Engineering Chemistry Research, 45, 2489-2496.
[16] Closmann, F., Nguyen, T., and Rochelle, G.T. (2009) MDEA/Piperazine as a solvent for CO2 cupture. Energy Procedia, 1, 1351-1357
[17] Choi, W.J., Seo, J.B., Jung, J.H., and Oh, K.J. (2009) Removal characteristics of CO2 using aqueous MEA/AMP solutions in the absorption and regeneration process. Chemical Engineering Progress, 81, 32-36.
[18] Ali, B.S., and Aroua, M.K. (2004) Effect of Piperazine on CO2 Loading in Aqueous Solutions of MDEA at Low Pressure. International Journal of Thermophysics, 25, 1863-1869.
[19] Freeman, S.A., Dugas, R., Wagener, D.V., Nguyen, T., and Rochelle, G.T. (2009) Carbon dioxide capture with concentrated, aqueous piperazine. Energy Procedia, 1, 1489-1496.
[20] Appl, M., Wagner U., Henrici H. J., Kuessner K., Volkamer F., and Neust N. E. (1982). Removal of CO and/or H2S and/or COS From Gases Containing These Constituents, U.S. Patent No. 4336233
[21] Strazisar, B.R., Anderson, R.R., and White, C.M. Degradation of MEA Used in Carbon Dioxide Capture from Flue Gas of a Coal-fired Electric Power Generating Station. National Energy Technology Laboratory, Pittsburgh.
[22] Abdi, M.A., and Meisen, A. (2001) Amine Degradation: Problems, Review of Research Achievements, Recovery Techniques.