Articles & Issues
- Language
- English
- Conflict of Interest
- In relation to this article, we declare that there is no conflict of interest.
- Publication history
-
Received December 22, 2004
Accepted September 7, 2005
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.
All issues
Hydrotalcites for adsorption of CO2 at high temperature
Separation Process Research Center, Korea Institute of Energy Research, 71-2, Jang-dong, Yusung-gu, Daejeon 305-343, Korea
jnkim@kier.re.kr
Korean Journal of Chemical Engineering, January 2006, 23(1), 77-80(4), 10.1007/BF02705695
Download PDF
Abstract
Adsorption of carbon dioxide by hydrotalcites was investigated by using a gravimetric method at 450 ℃. Hydrotalcites possessed higher adsorption capacity of CO2 than other basic materials such as MgO and Al2O3. Two different preparation methods of hydrotalcite with varying Mg/Al ratio were employed to determine their effects on the adsorption capacity of CO2. In addition, varying amounts of K2CO3 were impregnated on the hydrotalcite to further increase its adsorption capacity of CO2. The hydrotalcite prepared by the high supersaturation method with Mg/Al=2 showed the most favorable adsorption-desorption pattern with high adsorption capacity of CO2. K2CO3 impregnation on the hydrotalcite increased the adsorption capacity of CO2 because it changed both the chemical and the physical properties of the hydrotalcite. The optimum amount of K2CO3 impregnation was 20 wt%. The hydrotalcite prepared by the high supersaturation method with Mg/Al=2 and 20 wt% K2CO3 impregnation has the highest adsorption capacity of CO2 with 0.77 mmol CO2/g at 450 ℃ and 800 mmHg.
References
Cativiela C, Figueras F, Fraile JM, Garcia JI, Mayoral JA, Tetrahedron Lett., 36, 4125 (1995)
Corma A, Iborra S, Primo J, Rey F, Appl. Catal. A: Gen., 114(2), 215 (1994)
Hoffman JS, Pennline HW, Investigation of CO2 capture using regenerable sorbents, Proc. of the 17th Annual International Pittsburgh Coal Conference (2000)
Hufton JR, Mayorga S, Sircar S, AIChE J., 45(2), 248 (1999)
Hufton JR, Mayorga S, Gaffiney T, Nataraj S, Rao M, Sircar S, Proc. U.S. DOE Hydrogen Program Rev, 693 (1998)
Mckenzie AL, Fishel CT, Davis RJ, J. Catal., 138, 547 (1992)
Narayanan S, Krishna K, Appl. Catal. A: Gen., 174(1-2), 221 (1998)
Parida K, Das J, J. Mol. Catal. A-Chem., 151, 185 (2000)
Reichle WT, J. Catal., 63, 295 (1980)
Reichle WT, Appl. Catal. A: Gen., 47, 69 (1996)
Schaper H, Berg-Slot JJ, Stork WHJ, Appl. Catal. A: Gen., 54, 79 (1989)
Velu S, Swamy CS, Appl. Catal. A: Gen., 145(1-2), 141 (1996)
Yong Z, Mata V, Rodriguez AE, Ind. Eng. Chem. Res., 40(1), 204 (2001)
Corma A, Iborra S, Primo J, Rey F, Appl. Catal. A: Gen., 114(2), 215 (1994)
Hoffman JS, Pennline HW, Investigation of CO2 capture using regenerable sorbents, Proc. of the 17th Annual International Pittsburgh Coal Conference (2000)
Hufton JR, Mayorga S, Sircar S, AIChE J., 45(2), 248 (1999)
Hufton JR, Mayorga S, Gaffiney T, Nataraj S, Rao M, Sircar S, Proc. U.S. DOE Hydrogen Program Rev, 693 (1998)
Mckenzie AL, Fishel CT, Davis RJ, J. Catal., 138, 547 (1992)
Narayanan S, Krishna K, Appl. Catal. A: Gen., 174(1-2), 221 (1998)
Parida K, Das J, J. Mol. Catal. A-Chem., 151, 185 (2000)
Reichle WT, J. Catal., 63, 295 (1980)
Reichle WT, Appl. Catal. A: Gen., 47, 69 (1996)
Schaper H, Berg-Slot JJ, Stork WHJ, Appl. Catal. A: Gen., 54, 79 (1989)
Velu S, Swamy CS, Appl. Catal. A: Gen., 145(1-2), 141 (1996)
Yong Z, Mata V, Rodriguez AE, Ind. Eng. Chem. Res., 40(1), 204 (2001)