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    • 1. 发明专利
    • Catalyst for converting carbon monoxide
    • 用于转化一氧化碳的催化剂
    • JPS6121733A
    • 1986-01-30
    • JP14226384
    • 1984-07-11
    • Hiroshima Gas KkMitsubishi Heavy Ind Ltd
    • OBAYASHI YOSHIAKIMITSUOKA SHIGEAKISERA TOSHIKUNISHIMOMURA MASAHITOSAITOU MASAHIROMIHO TADANOBUMIURA KOUZOU
    • B01D53/94B01J35/10B01J37/02
    • PURPOSE: To prevent the increase in the pressure loss in a catalyst bed with the elapse of time while keeping initial activity over a long period of time, by molding a monolithic catalyst for converting carbon monoxide so as to set the thickness of a catalyst activator layer to 0.5mm or more.
      CONSTITUTION: A base material consisting of a plurality of parallel plates, a plurality of cylindrical base materials or a base material having a honeycomb shape is coated or impregnated with an effective catalyst component or the effective catalyst component and a sticking component are mixed and molded to obtain a monolithic catalyst for converting carbon monoxide wherein the thickness of a catalyst activation-containing layer is set to 0.5mm or more, pref., 0.7mm or more. This catalyst shows activity not inferior as compared with a conventional pellet catalyst and is effective for reducing power cost required in transferring gas. Further, this catalyst is effective even in aqueous gas converting reaction for preparing hydrogen for a fuel battery or ammonia synthesis.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:为了防止在长时间保持初始活性的同时催化剂床中的压力损失增加,通过模制用于转化一氧化碳的整体式催化剂以便设定催化剂活化剂层的厚度 至0.5mm。 或者更多。 构成:将由多个平行板,多个圆柱形基材或具有蜂窝形状的基材组成的基材涂覆或浸渍有效催化剂组分或有效催化剂组分,并将粘合组分混合并模制成 得到将催化剂活化层的厚度设定为0.5mm的一氧化碳转换用整体式催化剂。 以上,优选0.7mm。 或者更多。 该催化剂显示与常规颗粒催化剂相比不逊色的活性,并且对于降低转移气体所需的动力成本是有效的。 此外,即使在用于制备用于燃料电池或氨合成的氢气的水性气体转化反应中,该催化剂也是有效的。
    • 5. 发明专利
    • GAS DENITRATION PROCESS
    • JP2000093749A
    • 2000-04-04
    • JP27126798
    • 1998-09-25
    • MITSUBISHI HEAVY IND LTD
    • IIDA KOZONOJIMA SHIGERUOBAYASHI YOSHIAKIMORII ATSUSHI
    • B01D53/94B01D53/86B01J23/40
    • PROBLEM TO BE SOLVED: To provide an exhaust gas denitration process keeping the exhaust gas dentration rate at 90% or more while controlling the exhaustion of unreacted ammonia to the atmosphere to 0.1 ppm or less. SOLUTION: In an exhaust gas denitration process in which nitrogen oxide containing exhaust gas is introduced into a catalyst filling reactor and excessive ammonia as a reducer is added thereto to catalytically remove the nitrogen oxide, the exhaust gas and ammonia are introduced into a first denitration catalyst layer formed on the upstream side of gas flow to remove the nitrogen oxide, and a first ammonia decomposition catalyst layer provided with the function of decomposing unreacted ammonia into nitrogen and nitrogen oxide is formed on the downstream of the first denitration catalyst layer and the ammonia content is so adjusted as to fit for the denitration treatment in the following stage. Then a second denitration catalyst layer is formed on the downstream of the first denitration catalyst layer, and further a second ammonia decomposition catalyst layer provided with a catalyst for oxidative decomposing residual ammonia into nitrogen or nitrogen oxide or a catalyst for oxidative decomposing residual ammonia into oxide is disposed on the downstream of the second denitration catalyst layer to remove the residual ammonia.