CeO2-WO3催化剂表面酸性和氧化还原性能在脱硝反应中的研究

Investigation of the surface acidity and redox on the CeO2-WO3 catalyst for selective catalytic reduction with NH3

  • 摘要: 本研究利用原位合成法成功制备CeO2-WO3催化剂并用于脱硝反应,焙烧温度为550 ℃的CW-550催化剂活性最佳,200 ℃时CW-550脱硝活性达到90%以上。CW-550催化剂具有优越的催化剂性能可归结为较大的比表面积、较多的Ce3 + 物种、丰富的表面酸性和优越的氧化还原性能。Ce3 + 增多,有利于氧空位的形成,可促进氧化还原性能。WO3的引入,在550 ℃的焙烧条件下可显著提升催化剂的Brönsted酸量,有利于氨气的吸附与活化,提升其催化性能。CW催化剂上吸附的NH3物种能与气态的NO反应,而吸附态的NH3与吸附态的NOx不能进行高效反应,因此,CW催化剂的SCR反应主要遵循Eley-Rideal反应机理。

     

    Abstract: CeO2-WO3 catalysts were successfully prepared by in-situ synthesis and used in the denitrification reaction. The best activity of CW-550 catalyst was achieved at a roasting temperature of 550 ℃, and the denitrification activity of CW-550 reached over 90% at 200 ℃. The superior catalytic performance of CW-550 catalyst can be attributed to the large specific surface area, more Ce3+ species, abundant surface acidity and superior redox performance. The increased Ce3+ facilitates the formation of oxygen vacancies and promotes redox performance. The introduction of WO3, into CeO2 can enhance the amounts of Brönsted acid, which contributes to the improvement of the adsorption and activation of ammonia, resulting in the excellent catalytic performance. The NH3-adsorbed species can react with gaseous NO. However, both of NH3-adsorbed and NO-adsorbed sepcies cannot participate in the SCR reaction effectively. Therefore, the SCR reaction of CW catalysts mainly follows the Eley-Rideal mechanism.

     

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