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Use of a catalyst based on modified zeolite, charged with one or more metals from the group consisting of Fe, Cu, Ni and Co, in the SCR process

机译:在SCR工艺中使用基于改性沸石的催化剂,该催化剂中含有一种或多种选自Fe,Cu,Ni和Co的金属

摘要

By the use of a catalyst based on modified zeolite of the Y or mordenite type, charged with one or more elements from the group consisting of Fe, Cu, Ni, Co and K, a sequential DeNOx/DeNH3 catalytic action can be achieved in the SCR process for NOx reduction in furnace exhaust gases. These catalysts have the property of simultaneously catalysing two reactions, that is the NOx reduction with NH3 and the NH3 oxidation with oxygen, depending on the concentration of NOx in the gas to be treated, in such a manner that at high NOx concentrations, the NOx reduction with NH3 is preferentially catalysed and at low NOx concentrations, the NH3 oxidation is preferentially catalysed. These catalysts permit NH3/NO ratios up to 1.2 times the stoichiometric amount, convert up to 98% of the NO and ensure an NH3 slip below 5 ppm via the sequentially preceding oxidation of the residual NH3. For treating SO2-free gases in the SCR process, the use of the catalyst at gas temperatures in the range between about 80@C and about 500@C is suitable, and when treating SO2-containing gases, the gas temperature range between about 200@C and 500@C is suitable.
机译:通过使用基于Y或丝光沸石类型的改性沸石的催化剂,该催化剂中含有一种或多种选自Fe,Cu,Ni,Co和K的元素,可以在催化剂中实现连续的DeNOx / DeNH3催化作用。 SCR工艺用于减少炉内废气中的NOx。这些催化剂具有同时催化两个反应的特性,即取决于要处理的气体中NOx的浓度,用NH3还原NOx和用氧气氧化NH3的方式是,在高NOx浓度下,NOx NH 3的还原优先被催化,而在低NOx浓度下,NH 3的氧化优先被催化。这些催化剂允许NH3 / NO比例高达化学计量的1.2倍,最多转化98%的NO,并通过顺序进行残留NH3的氧化来确保NH3泄漏至5 ppm以下。为了在SCR工艺中处理不含SO 2的气体,在约80℃至约500℃的气体温度下使用催化剂是合适的,并且当处理含SO 2的气体时,该气体温度在约200℃至200℃之间。 @C和500 @ C是合适的。

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