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In relation to this article, we declare that there is no conflict of interest.
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Received February 13, 2007
Accepted July 27, 2007
articles 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.
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High temperature desulfurization over nano-scale high surface area ceria for application in SOFC

The Joint Graduate School of Energy and Environment, King Mongkut’s University of Technology Thonburi, Bangkok 10140, Thailand 1Center of Excellence in Catalysis and Catalytic Reaction Engineering, Department of Chemical Engineering,Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand
navadol_l@jgsee.kmutt.ac.th
Korean Journal of Chemical Engineering, March 2008, 25(2), 223-230(8), 10.1007/s11814-008-0040-3
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Abstract

In the present work, suitable absorbent material for high temperature desulfurization was investigated in order to apply internally in solid oxide fuel cells (SOFC). It was found that nano-scale high surface area CeO2 has useful desulfurization activity and enables efficient removal of H2S from feed gas between 500 to 850 ℃. In this range of temperature, compared to the conventional low surface area CeO2, 80-85% of H2S was removed by nano-scale high surface area CeO2, whereas only 30-32% of H2S was removed by conventional low surface area CeO2. According to the XRD studies, the product formed after desulfurization over nano-scale high surface area CeO2 was Ce2O2S. EDS mapping also suggested the uniform distribution of sulfur on the surface of CeO2. Regeneration experiments were then conducted by temperature programmed oxidation (TPO) experiment. Ce2O2S can be recovered to CeO2 after exposure in the oxidation condition at temperature above 600 ℃. It should be noted that SO2 is the product from this regeneration process. According to the SEM/EDS and XRD measurements, all Ce2O2S forming is converted to CeO2 after oxidative regeneration. As the final step, a deactivation model considering the concentration and temperature dependencies on the desulfurization activity of CeO2 was applied and the experimental results were fitted in this model for later application in the SOFC model.

References

Park DW, Hwang BH, Ju WD, Kim MI, Kim KH, Woo HC, Korean J. Chem. Eng., 22(2), 190 (2005)
Lee JD, Jun JH, Park NK, Ryu SO, Lee TJ, Korean J. Chem. Eng., 22(1), 36 (2005)
Westmoreland PR, Harrison DP, Environ. Sci. Technol., 10, 559 (1976)
Jang HT, Kim SB, Doh DS, Korean J. Chem. Eng., 20(1), 116 (2003)
Gardener TH, Fuel, 81, 2157 (2002)
Swisher JH, Schwerdtfeger K, J. Mater. Eng. Perform., 1, 399 (1992)
Patrick V, Gavalas GR, Ind. Eng. Chem. Res., 28, 931 (1989)
Meng VV, Kay DAR, High technology ceramics, Elsevier, Amsterdam, 2247 (1987)
Kay DAR, Wilson WG, Jalan V, J. Alloy. Compd., 192, 11 (1993)
Kim KH, Lee SY, Yoon KJ, Korean J. Chem. Eng., 23(3), 356 (2006)
Kim KH, Lee SY, Nam SW, Lim TH, Hong SA, Yoon KJ, Korean J. Chem. Eng., 23(1), 17 (2006)
Abbasian J, Hill AH, Flytzani-Stephanopoulos M, Li Z, Final Report, DE-FC22-92PC92521 (1994)
Li ZJ, Flytzanistephanopoulos M, Ind. Eng. Chem. Res., 36(1), 187 (1997)
Zeng Y, Zhang S, Groves FR, Harrison DP, Chem. Eng. Sci., 54(15-16), 3007 (1999)
Laosiripojana N, Assabumrungrat S, Appl. Catal. B: Environ., 60(1-2), 107 (2005)
Orbey N, Dogu G, Dogu T, Can. J. Chem. Eng., 60, 314 (1982)
Fogler HS, Elements of chemical reaction engineering, Prentice-Hall Inc, Englewood Cliffs, New Jersey 07632, ISBN 0-13-263476-7 (1986)
Cal MP, Strickler BW, Lizzio AA, Carbon, 38, 1757 (2000)
Fertizz RM, Gorte RJ, Vohs JM, Appl. Catal. B: Environ., 43(3), 273 (2003)
Wang Z, Flytzani-Stephanopoulos M, Energy Fuels, 19, 2093 (2005)
Flytzani-Stephanopoulos M, Surgenor AD, Report, NASA/TM-2007-214686
Yasyerli S, Dogu G, Dogu T, Catal. Today, 117(1-3), 271 (2006)
Ziolek M, J. Mol. Catal. A-Chem., 97, 49 (1995)
Dogu T, Chem. Eng. J., 21, 213 (1981)
Suyadal Y, Erol M, Oguz H, Ind. Eng. Chem. Res., 39(3), 724 (2000)

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