Distillate hydrocracking catalyst and process for the preparation of the
same
    2.
    发明授权
    Distillate hydrocracking catalyst and process for the preparation of the same 失效
    馏分加氢裂化催化剂及其制备方法

    公开(公告)号:US5972832A

    公开(公告)日:1999-10-26

    申请号:US884815

    申请日:1997-06-30

    摘要: The present invention relates to a hydrocracking catalyst containing nickel, tungsten, fluorine, zeolite as well as alumina, said catalyst is composed of, based on the total weight of the catalyst, 0.5-5.0 wt % fluorine, 2.5-6.0 wt % nickel oxide, 10-38 wt % tungsten oxide, and a catalyst carrier. Said carrier is composed of 20-90 wt % alumina and 10-90 wt % zeolite wherein the zeolite is mesopore or macropore zeolite of an acidity strength value 1.0-2.0 mmol/g determined by NH.sub.3 -TPD, the alumina is the alumina of an acidity strength value 0.5-0.8 mmol/g determined by NH.sub.3 -TPD. Said catalyst possesses good desulfurization activity, denitrogenation activity, and higher selectivity with respect to middle distillates than that of the prior art.

    摘要翻译: 本发明涉及含有镍,钨,氟,沸石以及氧化铝的加氢裂化催化剂,所述催化剂由催化剂的总重量计为0.5-5.0重量%的氟,2.5-6.0重量%的氧化镍 ,10-38重量%的氧化钨和催化剂载体。 所述载体由20-90重量%的氧化铝和10-90重量%的沸石组成,其中沸石是由NH 3 -TPD测定的酸度强度值为1.0-2.0毫摩尔/克的中孔或大孔沸石,氧化铝为 NH3-TPD测定酸度强度值为0.5-0.8 mmol / g。 所述催化剂具有比现有技术更好的脱硫活性,脱氮活性和相对于中间馏分的更高选择性。

    Hydrocracking catalyst, the preparation process and use of the same
    5.
    发明授权
    Hydrocracking catalyst, the preparation process and use of the same 有权
    加氢裂化催化剂,其制备方法和用途相同

    公开(公告)号:US08334231B2

    公开(公告)日:2012-12-18

    申请号:US11919619

    申请日:2006-04-26

    摘要: The present invention provides a hydrocracking catalyst comprising a moulded composite support of a zeolite molecular sieve with alumina, at least one of VIII Group metal components, at least one of VIB Group metal components and an organic additive; said organic additive is one or more compounds selected from the group consisting of oxygen-containing or nitrogen-containing organic compounds; the content of said zeolite molecular sieve is 3˜60 wt %, the content of said alumina is 10˜80 wt %, and the content of said organic additive is 0.1˜40 wt % based on the weight of said catalyst; the content of said VIII Group metal component is 1˜15 wt % and the content of said VIB Group metal component is 5˜40 wt % as calculated on oxide and based on the weight of said catalyst. The present invention relates also to a preparation method of said hydrocracking catalyst and use of the catalyst in the hydrocracking process of hydrocarbon oil. In comparison with the method in existing arts, the hydrocracking catalyst provided according to the present invention has the aromatic-hydrogenation conversion activity increased obviously.

    摘要翻译: 本发明提供一种加氢裂化催化剂,其包括具有氧化铝的沸石分子筛的模塑复合载体,VIII族金属组分,VIB族金属组分和有机添加剂中的至少一种; 所述有机添加剂是选自含氧或含氮有机化合物的一种或多种化合物; 所述沸石分子筛的含量为3〜60重量%,所述氧化铝的含量为10〜80重量%,所述有机添加剂的含量相对于所述催化剂的重量为0.1〜40重量% 所述VIII族金属成分的含量为1〜15重量%,所述VIB族金属成分的含量为氧化物计算为5〜40重量%,基于所述催化剂的重量。 本发明还涉及所述加氢裂化催化剂的制备方法和在烃油加氢裂化过程中催化剂的应用。 与现有技术相比,根据本发明提供的加氢裂化催化剂具有明显的芳香族氢化转化活性。

    Process for reducing sulfur and olefin contents in gasoline
    9.
    发明授权
    Process for reducing sulfur and olefin contents in gasoline 有权
    减少汽油中硫和烯烃含量的方法

    公开(公告)号:US07341657B2

    公开(公告)日:2008-03-11

    申请号:US10740807

    申请日:2003-12-22

    IPC分类号: C10G65/02

    CPC分类号: C10G45/64 C10G2400/02

    摘要: Disclosed is a process for reducing sulfur and olefin contents in gasoline, comprising contacting gasoline feedstock and hydrogen with a hydrorefining catalyst and an paraffin-modification catalyst. The effluent of the process is separated to obtain a hydrotreated gasoline fraction free of mercaptan and having a low content of sulfur, e.g. less than 200 ppm, a low content of olefins, e.g. less than 20% by volume, and little octane loss. The hydrotreated gasoline fraction can be used as blending component of a final gasoline product.

    摘要翻译: 公开了一种降低汽油中硫和烯烃含量的方法,包括使汽油原料和氢气与加氢精制催化剂和石蜡改性催化剂接触。 将该方法的流出物分离以获得不含硫醇并具有低含量硫的加氢处理汽油馏分, 小于200ppm,低含量的烯烃,例如。 小于20体积%,辛烷值损失小。 加氢处理的汽油馏分可用作最终汽油产品的共混组分。

    Process for reducing sulfur and olefin contents in gasoline
    10.
    发明申请
    Process for reducing sulfur and olefin contents in gasoline 有权
    减少汽油中硫和烯烃含量的方法

    公开(公告)号:US20050133410A1

    公开(公告)日:2005-06-23

    申请号:US10740807

    申请日:2003-12-22

    CPC分类号: C10G45/64 C10G2400/02

    摘要: Disclosed is a process for reducing sulfur and olefin contents in gasoline, comprising contacting gasoline feedstock and hydrogen with a hydrorefining catalyst and an paraffin-modification catalyst. The effluent of the process is separated to obtain a hydrotreated gasoline fraction free of mercaptan and having a low content of sulfur, e.g. less than 200 ppm, a low content of olefins, e.g. less than 20% by volume, and little octane loss. The hydrotreated gasoline fraction can be used as blending component of a final gasoline product.

    摘要翻译: 公开了一种降低汽油中硫和烯烃含量的方法,包括使汽油原料和氢气与加氢精制催化剂和石蜡改性催化剂接触。 将该方法的流出物分离以获得不含硫醇并具有低含量硫的加氢处理汽油馏分, 小于200ppm,低含量的烯烃,例如。 小于20体积%,辛烷值损失小。 加氢处理的汽油馏分可用作最终汽油产品的共混组分。