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In relation to this article, we declare that there is no conflict of interest.
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Received August 30, 2006
Accepted October 2, 2006
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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Low-temperature catalytic reduction of nitrogen oxides with ammonia over supported manganese oxide catalysts

Department of Applied Chemistry, Division of Biotechnology and Nanotechnology, Ajou University, Suwon 443-749, Korea 1Department of Chemical Engineering, Division of Chemical Engineering and Materials Engineering,Division of Energy Systems Research, Ajou University, Suwon 443-749, Korea
Korean Journal of Chemical Engineering, January 2007, 24(1), 191-195(5), 10.1007/s11814-007-5031-2
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Abstract

MnOx supported on γ-Al2O3, TiO2, Y-ZrO2 and SiO2 was prepared by an impregnation and a depositionprecipitation method, and their catalytic activities for the low-temperature selective catalytic reduction (SCR) of NOx with NH3 in the presence of excess O2 were examined. The catalytic activity of the catalysts prepared by a depositionprecipitation method was higher than that of catalysts prepared by an impregnation method. The activity follows in the order: MnOx/TiO2.MnOx/γ-Al2O3>MnOx/SiO2>MnOx/Y-ZrO2. Supported MnOx catalysts prepared by a deposition-precipitation method appeared to have an amorphous manganese oxide phase and those prepared by an impregnation method exhibited a crystalline MnO2 phase, respectively. The addition of SO2 with H2O in the feeding gas slightly deactivates the SCR activity of MnOx/TiO2 catalysts.

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