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    • 3. 发明申请
    • Reformer assisted lean NOx catalyst aftertreatment system and method
    • 改性助剂辅助NOx催化剂后处理系统及方法
    • US20080053073A1
    • 2008-03-06
    • US11514544
    • 2006-09-01
    • Mohan KalyanaramanPaul W. ParkChristie S. Ragle
    • Mohan KalyanaramanPaul W. ParkChristie S. Ragle
    • F01N3/00F01N3/10
    • B01D53/9409B01D2251/202B01D2251/208B01D2255/104B01D2255/50B01D2258/012F01N3/2066F01N13/0097F01N2240/30F01N2610/03F01N2610/04Y02T10/24
    • A method and apparatus for catalytically processing a gas stream passing therethrough to reduce the presence of NOx therein, wherein the apparatus includes a first catalyst composed of a silver-containing alumina that is adapted for catalytically processing the gas stream at a first temperature range, a second catalyst composed of a copper-containing zeolite located downstream from the first catalyst, wherein the second catalyst is adapted for catalytically processing the gas stream at a lower second temperature range relative to the first temperature range, a hydrocarbon compound for injection into the gas stream upstream of the first catalyst to provide a reductant, and a reformer for reforming a portion of the hydrocarbon compound into H2 and/or oxygenated hydrocarbon for injection into the gas stream upstream of the first catalyst. The second catalyst is adapted to facilitate the reaction of reducing NOx into N2, whereby the intermediates are produced via the first catalyst reacting with NOx and hydrocarbons.
    • 一种用于催化处理通过其中的气流以减少其中的NO x的存在的方法和装置,其中所述装置包括由含银氧化铝组成的第一催化剂,所述含银氧化铝适于催化加工所述气体 在第一温度范围内流动的第二催化剂,由位于第一催化剂下游的含铜沸石组成的第二催化剂,其中第二催化剂适于在相对于第一温度范围的较低的第二温度范围催化加工气流, 用于注入到第一催化剂上游的气流中以提供还原剂的烃化合物,以及用于将一部分烃化合物重整成H 2 N 2和/或用于注入气流的氧化烃的重整器 在第一催化剂的上游。 第二催化剂适于促进将NO x还原成N 2 H 2的反应,由此通过第一催化剂与NO x和烃反应制备中间体。
    • 4. 发明授权
    • Method of preparing doped oxide catalysts for lean NOx exhaust
    • 制备贫NOx排放用掺杂氧化物催化剂的方法
    • US06703343B2
    • 2004-03-09
    • US10022492
    • 2001-12-18
    • Paul W. Park
    • Paul W. Park
    • B01J2104
    • B01D53/9422B01D2255/2094B01D2255/9207B01D2258/012B01J21/04B01J23/06B01J23/08B01J37/036B01J37/038
    • The lean NOx catalyst includes a substrate, an oxide support material, preferably &ggr;-alumina deposited on the substrate and a metal or metal oxide promoter or dopant introduced into the oxide support material. The metal promoters or dopants are selected from the group consisting of indium, gallium, tin, silver, germanium, gold, nickel, cobalt, copper, iron, manganese, molybdenum, chromium cerium, and vanadium, and oxides thereof, and any combinations thereof. The &ggr;-alumina preferably has a pore volume of from about 0.5 to about 2.0 cc/g; a surface area of between 80 and 350 m2/g; an average pore size diameter of between about 3 to 30 nm; and an impurity level of less than or equal to about 0.2 weight percent. In a preferred embodiment the &ggr;-alumina is prepared by a sol-gel method, with the metal doping of the &ggr;-alumina preferably accomplished using an incipient wetness impregnation technique.
    • 贫NOx催化剂包括基底,氧化物载体材料,优选沉积在基底上的γ-氧化铝和引入到氧化物载体材料中的金属或金属氧化物促进剂或掺杂剂。 金属助催化剂或掺杂剂选自铟,镓,锡,银,锗,金,镍,钴,铜,铁,锰,钼,铬铈和钒,及其氧化物及其任意组合 。 γ-氧化铝优选具有约0.5至约2.0cc / g的孔体积; 表面积在80和350m 2 / g之间; 平均孔径直径约3〜30nm; 和小于或等于约0.2重量%的杂质水平。 在优选的实施方案中,通过溶胶 - 凝胶法制备γ-氧化铝,其中γ-氧化铝的金属掺杂优选使用初始湿浸渍技术完成。
    • 6. 发明授权
    • Metal/metal oxide doped oxide catalysts having high deNOx selectivity for lean NOx exhaust aftertreatment systems
    • 金属/金属氧化物掺杂的氧化物催化剂对于贫NOx排放后处理系统具有高脱硝选择性
    • US06706660B2
    • 2004-03-16
    • US10024430
    • 2001-12-18
    • Paul W. Park
    • Paul W. Park
    • B01J2300
    • B01D53/9422B01D2255/2094B01J21/04B01J23/06B01J23/08B01J37/036B01J37/038
    • A lean NOx catalyst and method of preparing the same is disclosed. The lean NOx catalyst includes a ceramic substrate, an oxide support material, preferably &ggr;-alumina, deposited on the substrate and a metal promoter or dopant introduced into the oxide support material. The metal promoters or dopants are selected from the group consisting of indium, gallium, tin, silver, germanium, gold, nickel, cobalt, copper, iron, manganese, molybdenum, chromium, cerium, vanadium, oxides thereof, and combinations thereof. The &ggr;-alumina preferably has a pore volume of from about 0.5 to about 2.0 cc/g; a surface area of between about 80 to 350 m2/g; an average pore size diameter of between about 3 to 30 nm; and an impurity level of less than or equal to 0.2 weight percent. In a preferred embodiment the &ggr;-alumina is prepared by a sol-gel method, with the metal doping of the &ggr;-alumina preferably accomplished using an incipient wetness impregnation technique.
    • 公开了一种贫NOx催化剂及其制备方法。 贫NOx催化剂包括沉积在衬底上的陶瓷衬底,氧化物载体材料,优选γ-氧化铝,以及引入到氧化物载体材料中的金属促进剂或掺杂剂。 金属助剂或掺杂剂选自铟,镓,锡,银,锗,金,镍,钴,铜,铁,锰,钼,铬,铈,钒,氧化物及其组合。 γ-氧化铝优选具有约0.5至约2.0cc / g的孔体积; 约80至350m 2 / g的表面积; 平均孔径直径约3〜30nm; 杂质含量小于或等于0.2重量%。 在优选的实施方案中,通过溶胶 - 凝胶法制备γ-氧化铝,其中γ-氧化铝的金属掺杂优选使用初始湿浸渍技术完成。