Catalyst for purifying the exhaust gas from the combustion in an engine
or gas turbines and method of making and using the same
    32.
    发明授权
    Catalyst for purifying the exhaust gas from the combustion in an engine or gas turbines and method of making and using the same 失效
    用于净化发动机或燃气轮机中的燃烧中的废气的催化剂及其制造和使用方法

    公开(公告)号:US6033641A

    公开(公告)日:2000-03-07

    申请号:US634233

    申请日:1996-04-18

    摘要: This invention discloses a durable catalyst for internal combustion engine or power plant exhaust gas purification which is comprised of a zeolite as the support and Fe (II) base-exchanged cation as the active component for the NO.sub.x selective catalytic reduction (SCR). It has stable activity with up to 20% H.sub.2 O and up to 250 ppm SO.sub.2 and combinations thereof over many hours in the exhaust stream. It is resistant to temperature excursions up to about 1,000.degree. C. The method of producing this catalyst preferably comprises ion-exchanging the zeolite with Fe (II) in an aqueous solution of iron (II) oxalate, iron (II) citrate or iron (II) formate, or a mixture of oxalic acid, citric acid/salts, formic acid/salts, 2,3,4,5,6-pentahydroxyl caproic acid/salts and iron (II) salts, for example, sulfate, nitrate, chloride, carboxylate, chloride acetate, phosphate and carbonate, in the pH range from 3 to 13 under anaerobic conditions. The catalyst produced in this way shows no noticeable deactivation in its activity for reducing NO.sub.x to N.sub.2 under accelerated aging conditions (up to about 20% H.sub.2 O and up to about 250 ppm SO.sub.2 present in the mixture of NO, HC (iso-butane), and O.sub.2) for at least 2,500 hours which meets the Government standard. A method of using this catalyst is also disclosed. Methane can be used satisfactorily as the reducing agent but in the temperature range of greater than 600.degree. C. but less than 750.degree. C.

    摘要翻译: 本发明公开了一种用于内燃机或发电厂废气净化的耐久性催化剂,其由作为载体的沸石和作为用于NOx选择性催化还原(SCR)的活性成分的Fe(II))碱交换的阳离子组成。 它具有稳定的活性,高达20%的H 2 O和高达250ppm的SO 2及其组合在许多小时内排出。 它可以耐高达约1000℃的温度漂移。制备​​该催化剂的方法优选包括在草酸铁(II),柠檬酸铁(II)或铁(II)的水溶液中与Fe(II)离子交换沸石 II)甲酸盐,或草酸,柠檬酸/盐,甲酸/盐,2,3,4,5,6-五羟基己酸/盐和铁(II)盐的混合物,例如硫酸盐,硝酸盐, 氯化物,羧酸盐,氯化乙酸盐,磷酸盐和碳酸盐,在无氧条件下在3至13的pH范围内。 以这种方式生产的催化剂在加速老化条件下(NO,HC(异丁烷),异丁烷)混合物中存在的高达约20%H 2 O和高达约250ppm的SO 2,在其将NOx还原为N 2的活性中没有明显的失活。 和O2)至少2500小时,符合政府标准。 还公开了使用该催化剂的方法。 甲烷可以令人满意地用作还原剂,但在大于600℃但小于750℃的温度范围内。