Catalyst system for hydrotreating hydrocarbons
    1.
    发明授权
    Catalyst system for hydrotreating hydrocarbons 失效
    用于加氢处理碳氢化合物的催化剂体系

    公开(公告)号:US5071805A

    公开(公告)日:1991-12-10

    申请号:US592240

    申请日:1990-10-03

    摘要: This invention provides a layered catalyst system for hydro-denitrification of hydrocarbons, such as vacuum gas oil, used for hydrocracking to produce various fuels. The layered catalyst system of this invention comprises a first layer of a nickel-molybdenum-phosphorus/alumina catalyst or a cobalt-molybdenum-phosphorus/alumina catalyst and a second layer catalyst comprising a nickel-tungsten/silica-alumina-zeolite or a nickel-molybdenum/silica-alumina-zeolite catalyst. The preferred aspects of the combination of the layered catalysts disclosed herein are: (a) the first layer alumina catalyst has a molybdenum content greater than about 14% by wt.; (b) the first layer alumina catalyst has a relatively large pore size, such as at least about 60 .ANG.; and (c) the second layer catalyst contains at least about 2% of a zeolite component. The layered catalyst system of this invention and the attendant process produces improved denitrification of feedstocks, improved catalyst life and other advantages.

    摘要翻译: 本发明提供了一种用于烃的加氢脱氮的层状催化剂体系,例如用于加氢裂化以生产各种燃料的减压瓦斯油。 本发明的层状催化剂体系包括第一层镍 - 钼 - 磷/氧化铝催化剂或钴 - 钼 - 磷/氧化铝催化剂和第二层催化剂,其包含镍 - 钨/二氧化硅 - 氧化铝 - 沸石或镍 钼/二氧化硅 - 氧化铝 - 沸石催化剂。 本文公开的层状催化剂的组合的优选方面是:(a)第一层氧化铝催化剂具有大于约14重量%的钼含量; (b)第一层氧化铝催化剂具有较大的孔径,例如至少约60安培; 和(c)第二层催化剂含有至少约2%的沸石组分。 本发明的层状催化剂体系和伴随的方法产生了原料的改进的脱氮,改善的催化剂寿命和其它优点。

    Process for hydrodenitrogenating hydrocarbon oils
    4.
    发明授权
    Process for hydrodenitrogenating hydrocarbon oils 失效
    加氢脱氮烃油的工艺

    公开(公告)号:US4990243A

    公开(公告)日:1991-02-05

    申请号:US349848

    申请日:1989-05-10

    摘要: This invention provides a layered catalyst system for hydro-denitrification of hydrocarbons, such as vacuum gas oil, used for hydrocracking to produce various fuels. The layered catalyst system of this invention comprises a first layer of a nickel-molybdenum-phosphorus/alumina catalyst or a cobalt-molybdenum-phosphorus/alumina catalyst and a second layer catalyst comprising a nickel-tungsten/silica-alumina-zeolite or a nickel-molybdenum/silica-alumina-zeolite catalyst. The preferred aspects of the combination of the layered catalysts disclosed herein are: (a) the first layer alumina catalyst has a molybdenum content greater than about 14% by wt.; (b) the first layer alumina catalyst has a relatively large pore size, such as at least about 60 .ANG.; and (c) the second layer catalyst contains at least about 2% of a zeolite component. The layered catalyst system of this invention and the attendant process produces improved denitrification of feedstocks, improved catalyst life and other advantages.

    摘要翻译: 本发明提供了一种用于烃的加氢脱氮的层状催化剂体系,例如用于加氢裂化以生产各种燃料的减压瓦斯油。 本发明的层状催化剂体系包括第一层镍 - 钼 - 磷/氧化铝催化剂或钴 - 钼 - 磷/氧化铝催化剂和第二层催化剂,其包含镍 - 钨/二氧化硅 - 氧化铝 - 沸石或镍 钼/二氧化硅 - 氧化铝 - 沸石催化剂。 本文公开的层状催化剂的组合的优选方面是:(a)第一层氧化铝催化剂具有大于约14重量%的钼含量; (b)第一层氧化铝催化剂具有较大的孔径,例如至少约60安培; 和(c)第二层催化剂含有至少约2%的沸石组分。 本发明的层状催化剂体系和伴随的方法产生了原料的改进的脱氮,改善的催化剂寿命和其它优点。

    Process for upgrading arsenic-containing oils
    5.
    发明授权
    Process for upgrading arsenic-containing oils 失效
    升级含砷油的工艺

    公开(公告)号:US4141820A

    公开(公告)日:1979-02-27

    申请号:US825872

    申请日:1977-08-18

    CPC分类号: C10G1/002 C10G45/22 C10G65/04

    摘要: A method is provided for avoiding feed-transfer-line plugging by a deposit comprising arsenic in hydroprocessing an oil containing an arsenic contaminant. In the method, a mixture of hydrogen gas and the oil is formed in situ in a bed of porous particulate contact material.

    摘要翻译: 提供了一种用于在加氢处理含有砷污染物的油的情况下避免包含砷的沉积物的进料传输线堵塞的方法。 在该方法中,在多孔颗粒接触材料床中原位形成氢气和油的混合物。