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    • 6. 发明授权
    • Treating exchaust from a compressed natural gas-fueled engine
    • 从压缩天然气燃料发动机处理可再生能源
    • US5179053A
    • 1993-01-12
    • US789558
    • 1991-11-08
    • Somasundaram SubramanianRobert J. KudlaMohinder S. Chattha
    • Somasundaram SubramanianRobert J. KudlaMohinder S. Chattha
    • B01D53/94B01J23/63B01J29/46B01J29/74B01J37/02
    • B01J37/0246B01D53/945B01J23/63B01J29/46Y02T10/22
    • A catalyst system that converts the exhaust gas of a compressed natural gas (CNG) fueled automotive engine when operated at stoichiometry or slightly lean thereof, at highly enhanced rates, and having: (a) a first stage catalyst comprising a transition metal-containing zeolite (Cu-ZSM5), and (b) a second stage catalyst for treating the effluent of the first stage and comprising palladium supported on high surface area gamma alumina. The second stage catalyst has the alumina support impregnated with an intimate mixture, by weight, of 0.5-20% La.sub.2 O.sub.3 and 0.2-30% palladium.A method of treating exhaust gases from a CNG-fueled engine, comprising: (a) operating the engine at stoichiometry or slightly lean (0.85-1.0 R) thereof; (b) exposing such exhaust gases to a first stage catalyst consisting of a copper-ZSM5 zeolite having at least 3% by weight ion exchange copper; and (c) exposing the effluent from the first stage to a second stage comprising a gamma alumina support catalyst impregnated with palladium and other catalyst enhancing oxides.
    • 一种催化剂体系,其以高度增加的速率将以压缩天然气(CNG)燃料汽车发动机的排气转化为化学计量或轻微倾斜,并具有:(a)第一级催化剂,其包含含过渡金属的沸石 (Cu-ZSM5)和(b)用于处理第一阶段流出物并包含负载在高表面积γ氧化铝上的钯的第二阶段催化剂。 第二阶段催化剂具有以0.5-20%La 2 O 3和0.2-30%钯的重量混合物浸渍的氧化铝载体。 一种处理来自CNG燃料发动机的废气的方法,包括:(a)以化学计量或稍微倾斜(0​​.85-1.0R)操作发动机; (b)将这种废气暴露于由具有至少3重量%离子交换铜的铜-ZSM5沸石组成的第一阶段催化剂; 和(c)将来自第一阶段的流出物暴露于包含浸渍有钯和其它催化剂增强氧化物的γ氧化铝载体催化剂的第二阶段。
    • 7. 发明授权
    • Catalyst system for converting emissions of a lean-burn engine
    • 用于转换稀燃燃烧发动机排放的催化剂系统
    • US5788936A
    • 1998-08-04
    • US917261
    • 1992-07-23
    • Somasundaram SubramanianRobert J. KudlaMohinder S. Chattha
    • Somasundaram SubramanianRobert J. KudlaMohinder S. Chattha
    • B01D53/94B01J21/04F01N3/20F01N13/02B01D53/56B01D53/92
    • F01N3/2066B01D53/9459B01J21/04F01N13/009B01D2251/208B01D2251/21B01D2255/1023B01D53/9418B01D53/944F01N2610/03Y02T10/24
    • A catalyst system for attaining high conversions of NO, HC, and CO in a fuel-lean emission flow (i.e., containing SO.sub.2, H.sub.2 O, H.sub.2, and considerable excess oxygen), the system comprising: (a) a first stage reducing catalyst for treating the nitric oxide emissions, the catalyst containing highly acidic gamma alumina (i.e., with a pH.sub.pzc of less than 3); (b) means for injecting gaseous or liquid reductants into the emission stream prior to entering said first stage catalyst, said first stage catalyst temperature being selected to be in the range of 550.degree.-650.degree. C.; and (c) an oxidation catalyst effective for treating the effluent from the first stage catalyst. Another aspect of this invention is a method of treating the exhaust gas from a fuel-lean emission flow from a fossil-fueled internal combustion engine having a redox ratio of 0.02-0.09, the method comprising: (a) injecting a gaseous or liquid HC or oxygenated HC reductant into the emission stream at a location where the stream is within the temperature range of 550.degree.-650.degree. C.; (b) immediately exposing the injected stream to a first stage catalyst containing acidic gamma alumina with a Ph.sub.pzc of less than 3; and (c) exposing the effluent from the first stage catalyst to an oxidation catalyst that is effective in ensuring that the NO, HC, and CO in the emissions are each converted to at least 80%.
    • 一种用于在贫燃料流(即含有SO 2,H 2 O,H 2和相当多的氧)中获得NO,HC和CO的高转化率的催化剂体系,所述系统包括:(a)第一级还原催化剂 处理一氧化氮排放,含有高酸性γ氧化铝的催化剂(即pHpzc小于3); (b)用于在进入所述第一级催化剂之前将气态或液态还原剂注入所述排放流中的装置,所述第一级催化剂温度选择在550-650℃范围内。 和(c)有效处理来自第一级催化剂的流出物的氧化催化剂。 本发明的另一方面是一种从具有0.02-0.09的氧化还原比的化石燃料内燃机的来自贫燃料的排放流中处理废气的方法,所述方法包括:(a)将气态或液态HC 或氧化的HC还原剂进入流在550-650℃的温度范围内的排放流中。 (b)将注射的流体立即暴露于含有Phpzc小于3的酸性γ氧化铝的第一级催化剂; 和(c)将来自第一阶段催化剂的流出物暴露于有效确保排放物中的NO,HC和CO各自转化为至少80%的氧化催化剂。