Volume 37 Issue 03
Jun.  2009
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DIAO Qing-Sen, Zhou-Yang-Biao, Xiang-Jun, Wang-Le-Le, Su-Qing, Hu-Song, SUN Lu-Dan. Selective catalytic reduction of NO over CuO-CeO2-MnOx/γ-Al2O3 catalysts[J]. Journal of Fuel Chemistry and Technology, 2009, 37(03): 360-366.
Citation: DIAO Qing-Sen, Zhou-Yang-Biao, Xiang-Jun, Wang-Le-Le, Su-Qing, Hu-Song, SUN Lu-Dan. Selective catalytic reduction of NO over CuO-CeO2-MnOx/γ-Al2O3 catalysts[J]. Journal of Fuel Chemistry and Technology, 2009, 37(03): 360-366.

Selective catalytic reduction of NO over CuO-CeO2-MnOx/γ-Al2O3 catalysts

  • Received Date: 2008-09-21
  • Rev Recd Date: 2009-01-13
  • Publish Date: 2009-06-30
  • CuO-CeO2-MnOx/γ-Al2O3 granular catalysts were prepared by sol-gel method. Performance of the CuO-CeO2-MnOx/γ-Al2O3 catalyst for the selective catalytic reduction (SCR) was explored in a fixed bed adsorption system. The optimum temperature ranges for SCR of NO over the CuO-CeO2-MnOx/γ-Al2O3 catalysts were 250℃~400℃. The maximum efficiency maintained near to 99% at 350℃. With higher loading of Ce, the SCR activity increased at low temperature range (100℃~300℃). Preliminary tests were carried out to study the behavior of NH3 and NO over catalyst in the presence of oxygen. The NH3 oxidation experiments showed that both NO and N2O were produced gradually with temperature rising. The NO oxidation experiments revealed that NO was oxidized to NO2 over the catalyst. The NH3 and NO desorption experiments showed that NH3 and NO could be adsorbed on CuO-CeO2-MnOx/γ-Al2O3 granular catalysts. The less adsorption capacity and the over-oxidation of NH3 were the main cause of lower activity at high temperature. The transient behavior of NH3 and NO was also studied. It was found that the SCR reaction was zero order to NH3 and first order to NO.
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