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Combination of a Zeolite-Based SCR Catalyst with a Manganese-Based SCR Catalyst in the Bypass

机译:旁路中沸石基SCR催化剂与锰基SCR催化剂的组合

摘要

The invention relates to an exhaust-gas aftertreatment system for selective catalytic reduction with a plurality of SCR catalytic converters, which exhaust-gas aftertreatment system is able to reduce NOx in a large temperature range and can store SOx. The invention further relates to a method for treating an exhaust gas flow, in which method the exhaust-gas aftertreatment system according to the invention is used. The system comprises a high-temperature SCR catalyst for temperature ranges between 250° C. and 750° C. and a low-temperature SCR catalyst arranged downstream thereof for temperature ranges between 60° C. and less than 250° C. There is a reductant supply system directly upstream of the high-temperature SCR catalyst. The high-temperature SCR catalyst is designed to reduce NOx in exhaust gas that has a temperature above a temperature threshold value and to store SOx in the temperature range below the threshold value. The low-temperature SCR catalyst reduces NOx in the temperature range below the threshold value. In each case, the exhaust gas flows through the high-temperature SCR catalyst. An exhaust-gas bypass valve or flow control valve is arranged directly upstream of the low-temperature SCR catalyst. If the temperature of the exhaust gas is greater than or equal to the temperature threshold value, the exhaust gas is completely conducted past the low-temperature SCR catalyst. The high-temperature SCR catalyst advantageously contains a molecular sieve as a catalytically active layer, and the catalytically active layer of the low-temperature SCR catalyst is preferably a manganese-containing mixed oxide.
机译:本发明涉及一种具有多个SCR催化转化器的用于选择性催化还原的废气后处理系统,该废气后处理系统能够在较大的温度范围内还原NOx并能够存储SOx。本发明还涉及一种用于处理废气流的方法,其中使用了根据本发明的废气后处理系统。该系统包括用于温度范围在250℃至750℃之间的高温SCR催化剂和布置在其下游的用于温度范围在60℃至小于250℃之间的低温SCR催化剂。还原剂供应系统直接位于高温SCR催化剂的上游。高温SCR催化剂被设计成还原具有高于温度阈值的温度的排气中的NOx,并且将SOx存储在低于阈值的温度范围内。低温SCR催化剂在低于阈值的温度范围内还原NOx。在每种情况下,废气流过高温SCR催化剂。排气旁通阀或流量控制阀直接布置在低温SCR催化剂的上游。如果废气的温度大于或等于温度阈值,则废气被完全引导通过低温SCR催化剂。高温SCR催化剂有利地包含分子筛作为催化活性层,并且低温SCR催化剂的催化活性层优选为含锰的混合氧化物。

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