CuO-CeO2-MnOx/γ-Al2O3催化剂选择性催化还原NO

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

  • 摘要: 利用溶胶凝胶法制备CuO-CeO2-MnOx/γ-Al2O3催化剂颗粒,在固定床上测试其催化脱硝活性。CuO-CeO2-MnOx/γ-Al2O3催化剂在250℃~400℃脱硝效率保持在90%以上。活性组分氧化铈负载量的增多提高了催化剂在低温区脱硝活性。同时利用程序升温方法研究了催化剂对NH3和NO的氧化性能,随着温度升高NH3被过度氧化生成了NO和N2O。催化剂能将NO氧化生成NO2,但转化程度较低。脱附实验表明,NH3和NO在催化剂表面存在明显的吸附现象。较少的NH3吸附量和NH3过度氧化是高温下脱硝效率降低的主要原因。暂态实验显示,NH3以吸附态参与反应,而NO以气态或弱吸附态参与反应。

     

    Abstract: 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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