Hydrodesulfurization of a vacuum gas oil and vacuum residuum
    1.
    发明授权
    Hydrodesulfurization of a vacuum gas oil and vacuum residuum 失效
    真空气体和真空残留物的氢化

    公开(公告)号:US3617526A

    公开(公告)日:1971-11-02

    申请号:US3617526D

    申请日:1969-09-05

    Applicant: TEXACO INC

    CPC classification number: C10G65/16

    Abstract: Hydrodesulfurization of an atmospheric residuum is effected by separating it into a vacuum gas oil and vacuum residuum and desulfurizing the gas oil fraction under less severe conditions than the heavy fraction. The vacuum residuum is contacted initially with a catalyst containing a Group VI metal and Group VIII metal or their sulfides on an alumina support containing 2-4 weight percent silica, a surface area of at least 250 m2/g. and a pore volume of at least 0.6 cc./g.; the effluent from the first zone is mixed with the gas oil fraction and the resulting mixture is then contacted with the catalyst at a lower temperature than the effluent temperature from said first zone.

    Hydrodesulfurization and blending of residue-containing petroleum oil
    2.
    发明授权
    Hydrodesulfurization and blending of residue-containing petroleum oil 失效
    含油石油的水化和混合

    公开(公告)号:US3691152A

    公开(公告)日:1972-09-12

    申请号:US3691152D

    申请日:1971-03-10

    Applicant: TEXACO INC

    CPC classification number: C10G65/04 C10G2300/107

    Abstract: Petroleum oils of reduced sulfur content are produced by introducing into a catalytic hydrodesulfurization zone a residuecontaining petroleum oil of which at least 10 volume per cent boils below 1,000*F. separating the hydrodesulfurization zone effluent into a fraction boiling below about 1,000*F. and a fraction boiling above about 1,000*F. desulfurizing the fraction boiling below about 1,000*F. and combining the product with the fraction boiling above about 1,000*F. The catalyst in the first hydrodesulfurization should have a surface area of at least 250 m2/g., a pore volume of at least 0.6 cc/g and should contain at least 2 percent by weight silica.

    Abstract translation: 降低硫含量的石油是通过向催化加氢脱硫区引入至少10体积沸腾至1000°F以下的含残油的石油,从而将加氢脱硫区流出物分成沸点低于约1000°F的馏分来生产的。 沸点高于约1000°F的馏分将沸点低于约1000°F的馏分脱硫,并将产物与沸点高于约1000°F的馏分结合。第一加氢脱硫中的催化剂的表面积应至少为250平方米 孔体积至少为0.6cc / g,并且应含有至少2重量%的二氧化硅。

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