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A Green CeO2 WO3/TiO2 Medium-Low Temperature de-NOx Catalyst for Selective Catalytic Reduction of NOx with NH3

机译:绿色CEO2 WO3/TIO2中低温DE-NONOX催化剂,用于选择性催化NOX用NH3降低NOX

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摘要

A series of CeO2-WO3/TiO2 catalysts were synthesized by the co-precipitation method and used for selective catalytic reduction (SCR) of NO with NH3 under medium-low temperature conditions with metatitanic acid as Ti source. A more reasonable weight ratio of CeO2 and WO3 was explored. The catalytic activity enhanced with the increase of cerium content, but the catalytic activity changed slightly in the temperature range of 240°C to 400°C when the cerium content exceeded 15%. Tungsten could enhance the sulfur resistance by adjust- ing the degree of crystallization, acidity in the SCR process. When the weight ratio of CeO2 to WO3 was 15: 8, the conversion rate of NO was more than 90% in the temperature range of 240°C to 440°C. For 15%CeO2-8%WO3/TiO2 catalyst, the NO conversion was maintained around 84% when the mixed gas was introduced SO2. At the same time, we have optimized the selection of carriers, metatitanic acid as a carrier was better than titanium dioxide.
机译:通过共沉淀法合成了一系列CEO2-WO3/TIO2催化剂,并用于NH3在中低温条件下以替代酸作为TI来源的NH3的选择性催化还原(SCR)。 探索了CEO2和WO3的更合理的重量比。 催化活性随钙含量的增加而增强,但是当铜含量超过15%时,催化活性在240°C至400°C的温度范围内略有变化。 钨可以通过调整结晶程度,SCR过程中的酸度来增强硫的耐药性。 当CEO2与WO3的重量比为15:8时,NO的转化率在240°C至440°C的温度范围内超过90%。 对于15%CEO2-8%WO3/TIO2催化剂,当混合气体引入SO2时,无需转换约84%。 同时,我们优化了载体的选择,将metatanic酸作为载体优于二氧化钛。

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