Hydrocracking catalyst for the production of middle distillates
    5.
    发明授权
    Hydrocracking catalyst for the production of middle distillates 失效
    用于生产中间馏分的加氢裂化催化剂

    公开(公告)号:US4738941A

    公开(公告)日:1988-04-19

    申请号:US041946

    申请日:1987-04-24

    CPC分类号: B01J29/106 C10G47/16

    摘要: The invention relates to a new hydrocarbon hydroconversion catalyst, which is a mixture of an amorphous matrix, a zeolite and at least one metal of Group VIII and optionally of Group VI, the zeolite having a SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio of about between 8 and 70, a sodium content of less than 0.15% by weight, a unit mesh parameter a.sub..degree. of between 24.55 and 24.24.times.10.sup.-10 m, a sodium ion recovery capacity C.sub.Na, expressed in grams of sodium per 100 grams of modified zeolite, greater than 0.85, a specific surface area greater than 400 m.sup.2 g.sup.-1, a water vapor adsorption capacity at 25.degree. C. (with a P/Po ratio of 0.10) greater than 6% by weight, a pore distribution between 1 and 20% of the pore volume contained essentially in pores of diameters between 20 and 80.times.10.sup.-10m, the remaining pore volume being contained essentially in pores of diameters less than 20.times.10.sup.-10 m, the matrix being characterized by the following textural properties:S.gtoreq.100 m.sup.2.g.sup.-1Vpt.gtoreq.0.4 cm.sup.3.g.sup.-1V.sub.75 .gtoreq.0.25 cm.sup.3.g.sup.-1V.sub.75 /Vpt.gtoreq.0.5.

    摘要翻译: 本发明涉及一种新的烃加氢转化催化剂,其是无定形基体,沸石和至少一种第VIII族金属和任选的第VI族的混合物,SiO 2 / Al 2 O 3摩尔比约为8至70的沸石 ,钠含量小于0.15重量%,单位网格参数a DEG在24.55和24.24x10-10微米之间,钠离子回收能力CNa以每克克改变的沸石表示的钠,大于0.85 ,比表面积大于400m2g-1,25℃下的水蒸汽吸附容量(P / Po比为0.10)大于6重量%,孔隙分布在孔的1〜20% 体积基本上包含在20至80×10 -10 m之间的直径的孔中,剩余的孔体积基本上包含在小于20×10 -10 m的直径的孔中,该基质的特征在于以下织构性质:S> = 100m 2·g -1 Vpt> / = 0.4 cm3.g-1 V75> / = 0.25 cm3.g-1 V75 / Vpt> / = 0.5。

    Process for the preparation of a pollution control catalyst for internal
combustion engine exhaust system/catalytic converter
    10.
    发明授权
    Process for the preparation of a pollution control catalyst for internal combustion engine exhaust system/catalytic converter 失效
    内燃机排气系统/催化转化器污染控制催化剂的制备工艺

    公开(公告)号:US4581343A

    公开(公告)日:1986-04-08

    申请号:US610498

    申请日:1984-05-15

    摘要: A pollution control catalyst for a catalytic converter in the exhaust system of an internal combustion engine, which catalyst comprises a support impregnated with (i) at least one platinum group precious metal, and with (ii) cerium base metal, or a combination of cerium and at least one other base metal, is facilely prepared by (1) impregnating a catalyst support with precursor compounds of said cerium base metal, or of said cerium base metal and of at least one other base metal, (2) activating said impregnated support, under a neutral or oxidizing atmosphere, at a temperature ranging from 120.degree. to 800.degree. C., (3) impregnating said catalyst support with precursor compounds of said at least one platinum group precious metal, together with a delayed-action organic reducing agent, inactive under cold conditions, which effects reduction of said platinum group precious metal precursor compounds, but not of any cerium or other base metal precursor compounds, under the conditions of the step (4) below, and (4) activating said impregnated catalyst, also under a neutral or oxidizing atmosphere, at a temperature ranging from 300.degree. to 800.degree. C.

    摘要翻译: 一种用于内燃机排气系统中的催化转化器的污染控制催化剂,该催化剂包括浸渍有(i)至少一种铂族贵金属和(ii)铈贱金属或铈组合的载体 和至少一种其它贱金属,通过(1)用催化剂载体浸渍所述铈贱金属或所述铈贱金属和至少一种其它贱金属的前体化合物来容易地制备,(2)活化所述浸渍的载体 在中性或氧化性气氛下,在120℃至800℃的温度下,(3)用所述至少一种铂族贵金属的前体化合物浸渍所述催化剂载体以及延迟作用的有机还原剂 在寒冷条件下无活性,其在锡的条件下还原所述铂族贵金属前体化合物而不是任何铈或其它贱金属前体化合物 p(4),以及(4)在中性或氧化性气氛下,在300〜800℃的温度下活化所述浸渍的催化剂。