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Catalyst based on ferrierite / iron used for the abatement of N2O and catalytic reduction of nitrous oxide

机译:基于镁碱沸石/铁的催化剂用于减少N2O和催化还原一氧化二氮

摘要

Catalyst for decomposing nitrous oxide (N 2O), comprises agglomerated ferrierite-type zeolite having an initial sodium and potassium form, which is ammonium-substituted and optionally iron-substituted, where the iron, sodium and potassium is present at 0.1-2 wt.%, 0.1 wt.% and 0.7 wt.% of the zeolite, respectively. Independent claims are included for: (1) a preparation of the catalyst comprising setting the catalyst comprising mixing the catalyst with a binder and extrusion of the mixture in the form of agglomerated granules, calcining the granules at a temperature of 350-450[deg] C, ambient cooling followed by a substitution by ammonium salt into aqueous solution at 50-80[deg] C, washing by soaking in demineralized water, followed by partial iron substitution with an aqueous solution of iron salt, washing again by soaking in demineralized water, followed by drying on trays at 80-110[deg] C; (2) a process for treating waste effluents containing N 2O, comprising decomposition of N 2O on a catalytic bed comprising the catalyst for decomposition; and (3) a process of simultaneous reduction of N 2O and nitric oxide (NOx) by ammonia, on a single catalytic bed, using a catalyst as a catalyst for reduction.
机译:用于分解一氧化二氮(N 2 O)的催化剂包括具有初始钠和钾形式的附聚的镁碱沸石型沸石,其被铵取代并且任选地被铁取代,其中铁,钠和钾的含量为0.1-2wt。%。分别为0.1重量%,0.1重量%和0.7重量%的沸石。包括以下独立权利要求:(1)催化剂的制备,其包括固化催化剂,所述方法包括将催化剂与粘合剂混合并以团聚颗粒的形式挤出混合物,在350-450℃的温度下煅烧颗粒。于室温下冷却,然后在50-80℃下用铵盐替代成水溶液,通过浸泡在软化水中进行洗涤,随后用铁盐水溶液进行部分铁替代,再通过浸泡在软化水中进行洗涤,然后在80-110℃的托盘上干燥; (2)处理含N 2 O的废水的方法,包括在含有分解催化剂的催化床上分解N 2 O; (3)使用催化剂作为还原催化剂,在单一催化床上用氨同时还原N 2 O和一氧化氮(NOx)的方法。

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