DocumentCode :
3359291
Title :
Selective Catalytic Reduction of NO by NH3 Over Fresh and Sulfated CuO/gamma-Al2O3 Catalysts
Author :
Zhao, Qingsen ; Sun, Lushi ; Xiang, Jun ; Shi, JinMing ; Su, Sheng ; Hu, Song
Author_Institution :
State Key Lab. of Coal Combustion, Huazhong Univ. of Sci. & Technol., Wuhan
fYear :
2009
fDate :
27-31 March 2009
Firstpage :
1
Lastpage :
4
Abstract :
CuO/gamma-Al2O3 granular catalysts were synthesized by the sol-gel method. Performance of the CuO/gamma-Al2O3 catalysts for the selective catalytic reduction (SCR) was explored in a fixed bed adsorption system. The optimum temperature ranges for SCR of NO over the fresh CuO/gamma-Al2O3 catalyst are 250~450degC. The maximum activity maintains near to 99% at 350degC. The operating temperature range is increased on the sulfated catalysts. The oxidation property becomes weak when the catalysts are sulfated. The transient behaviors of NH3 and NO were also studied; it was found that the SCR reaction was zero order with respect to NH3 and first order with respect to NO. The sulfation on the catalysts improves the adsorption capacity of NH3 and reduces the adsorption capacity of NO. The adsorbed of NO has little influence on denitrification activity in the actual SCR process.
Keywords :
adsorption; alumina; ammonia; catalysts; chemical reactors; copper compounds; oxidation; reduction (chemical); sol-gel processing; CuO-Al2O3; adsorption capacity; denitrification activity; fixed bed adsorption system; granular catalysts; oxidation; selective catalytic reduction; sol-gel method; sulfated catalysts; Atmospheric measurements; Flue gases; Inductors; Nitrogen; Oxidation; Pollution measurement; Steady-state; Sun; Temperature distribution; Thyristors;
fLanguage :
English
Publisher :
ieee
Conference_Titel :
Power and Energy Engineering Conference, 2009. APPEEC 2009. Asia-Pacific
Conference_Location :
Wuhan
Print_ISBN :
978-1-4244-2486-3
Electronic_ISBN :
978-1-4244-2487-0
Type :
conf
DOI :
10.1109/APPEEC.2009.4918735
Filename :
4918735
Link To Document :
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