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Process for the selective catalytic reduction of nitrogen oxides in industrial effluents, at low temperature.

机译:在低温下选择性催化还原工业废水中氮氧化物的方法。

摘要

The system consists of layers of different catalysts, between which is situated a catalyst with active phase made by interaction of oxides of copper and aluminium, or of copper, nickel and aluminium. This catalyst is made by (a) impregnation of an aluminous support with aq. solns. of mixts. of copper and nickel salts, (b) sepn. of the solid, (c) drying the solid for more than 1 hour, and (d) treatment in air at 400-600 deg.C for 1-6 hours to convert the impregnated salts into the active salts. The support then contains 80-97 wt.% of aluminium oxide and less than 0.05% alkali oxides and alkaline earths. The copper and nickel salts are nitrates with Cu:Ni ratio of 10:1.
机译:该系统由不同催化剂的层组成,在它们之间放置了具有活性相的催化剂,该活性相通过铜和铝的氧化物或铜,镍和铝的氧化物的相互作用而制成。该催化剂是通过(a)用铝水溶液浸渍铝载体制备的。 solns。混合。 (b)sepn。 (c)将固体干燥1小时以上,和(d)在400-600℃的空气中处理1-6小时以将浸渍的盐转化为活性盐。载体然后包含80-97重量%的氧化铝和小于0.05%的碱金属氧化物和碱土金属。铜盐和镍盐是具有10:1的Cu:Ni的硝酸盐。

著录项

  • 公开/公告号ES518430A0

    专利类型

  • 公开/公告日1984-06-01

    原文格式PDF

  • 申请/专利权人 CONSEJO SUPERIOR INVESTIGACIONES CIENTIFICAS;

    申请/专利号ES19820518430

  • 发明设计人

    申请日1982-12-21

  • 分类号B01J21/04;B01J23/70;C01B21/26;

  • 国家 ES

  • 入库时间 2022-08-22 09:07:09

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