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    • 44. 发明授权
    • Process for preparing a catalyst
    • 催化剂的制备方法
    • US06342465B1
    • 2002-01-29
    • US09205280
    • 1998-12-04
    • Harald KleinJürgen LeyrerRainer DomesleEgbert LoxThomas Kreuzer
    • Harald KleinJürgen LeyrerRainer DomesleEgbert LoxThomas Kreuzer
    • B01J2342
    • B01J23/40B01J37/0248
    • A process for preparing a catalyst which has a catalytically active coating of high surface area finely divided materials and catalytically active components on an inert carrier structure. A powder mixture of the finely divided materials used is impregnated with a solution of precursor compounds of the catalytically active components. By suitable combination of the finely divided materials and the precursor compounds and appropriate management of the impregnation process, a highly dispersed deposition and adsorption of the catalytically active components is ensured on the finely divided materials. Then ai aqueous coating dispersion is produced using the impregnated powder mixture and the carrier structure is coated therewith. The coating is then dried and calcined.
    • 一种在惰性载体结构上制备具有高表面积细碎材料和催化活性组分的催化活性涂层的催化剂的方法。 所使用的细碎材料的粉末混合物用催化活性组分的前体化合物的溶液浸渍。 通过精细分散的材料和前体化合物的合适组合以及浸渍过程的适当管理,在精细分散的材料上确保高度分散的催化活性组分的沉积和吸附。 然后使用浸渍的粉末混合物制备ai水性涂料分散体,并用其涂覆载体结构。 然后将涂层干燥并煅烧。
    • 45. 发明授权
    • Process for the operation of a nitrogen oxides storage catalyst
    • 氮氧化物储存催化剂的操作方法
    • US06171565B2
    • 2001-01-09
    • US09227589
    • 1999-01-08
    • J{umlaut over (u)}rgen HöhneWolfgang StrehlauEgbert LoxThomas Kreuzer
    • J{umlaut over (u)}rgen HöhneWolfgang StrehlauEgbert LoxThomas Kreuzer
    • B01D5356
    • B01D53/9445B01D53/9495B01D2255/91F01N3/0842F01N3/085F01N9/005F01N11/00F01N11/007F01N2550/03F01N2570/04F01N2570/16F01N2900/0422F02D41/0275F02D41/028F02D2200/0806F02D2200/0808Y02A50/2341Y02T10/22Y02T10/24Y02T10/47
    • A process of operating a nitrogen oxides storage catalyst of an exhaust gas treatment system is described. The process relates to the cycling of the normalized air/fuel ratio &lgr;-value of the exhaust gas exiting the engine, in which a lambda value greater than 1 represents oxygen-rich, lean burn conditions in which a sorption phase for the sorption of nitrogen oxides takes place; and in which a lambda value less than 1 represents oxygen-poor, rich burn conditions in which a desorption and conversion phase for the desorption and conversion of nitrogen oxides takes place. The &lgr;-value of the exhaust gas downstream from the storage catalyst is monitored during the desorption and conversion phase to determine the end of the desorption and conversion phase based on the &lgr;-value falling below a predetermined threshold value. Advantages of the process described include the ability to distinguish permanent from temporary damage to the nitrogen oxides storage catalyst, the ability to compensate for the slow deterioration in storage capacity, and the ability to determine when the storage capacity of the catalyst falls below a certain minimum capacity after which the storage catalyst must be either replaced or thermally treated while still installed in the exhaust gas treatment system.
    • 描述了操作废气处理系统的氮氧化物存储催化剂的方法。 该过程涉及离开发动机的废气的归一化空气/燃料比率lambd值的循环,其中大于1的λ值表示富氧的稀燃条件,其中用于吸附氮的吸附相 氧化物发生; 并且其中小于1的λ值表示氧贫,富氧燃烧条件,其中发生用于解吸和转化氮氧化物的解吸和转化相。 在解吸和转化阶段期间监测从储存催化剂下游排出的废气的羔羊值,以基于羔羊值低于预定阈值确定解吸和转化阶段的结束。 所述方法的优点包括将永久物与临时损伤区分为氮氧化物储存催化剂的能力,补偿储存容量缓慢劣化的能力以及确定催化剂的储存容量何时低于某一最低值的能力 容量之后,储存催化剂必须被替换或热处理,同时仍然安装在废气处理系统中。