Highly active slurry catalyst composition
    1.
    发明授权
    Highly active slurry catalyst composition 有权
    高活性浆料催化剂组合物

    公开(公告)号:US07678732B2

    公开(公告)日:2010-03-16

    申请号:US12212483

    申请日:2008-09-17

    IPC分类号: B01J27/051

    摘要: The instant invention is directed to the preparation of a slurry catalyst composition. The slurry catalyst composition is prepared in a series of steps, involving mixing a Group VIB metal oxide and aqueous ammonia to form an aqueous mixture and sulfiding the mixture to form a slurry. The slurry is then promoted with a Group VIII metal. Subsequent steps involve mixing the slurry with a hydrocarbon oil, and combining the resulting mixture with hydrogen gas (under conditions which maintain the water in a liquid phase) to produce the active slurry catalyst.

    摘要翻译: 本发明涉及制备淤浆催化剂组合物。 浆料催化剂组合物是以一系列步骤制备的,包括将VIB族金属氧化物与氨水混合以形成含水混合物并硫化混合物以形成浆料。 然后用VIII族金属促进该浆料。 随后的步骤包括将浆料与烃油混合,并将所得混合物与氢气(在将水保持在液相中的条件下)组合以产生活性淤浆催化剂。

    Crude oil desulfurization
    10.
    发明授权
    Crude oil desulfurization 失效
    原油脱硫

    公开(公告)号:US06841062B2

    公开(公告)日:2005-01-11

    申请号:US09896224

    申请日:2001-06-28

    申请人: Bruce E. Reynolds

    发明人: Bruce E. Reynolds

    CPC分类号: C10G65/12 C10G65/00 C10G65/14

    摘要: This invention relates to a crude oil desulfurization process which comprises hydrodesulfurizing a crude oil feed in a crude desulfurization unit. The desulfurized crude oil is then separated into a light gas oil fraction, a vacuum gas oil fraction and a vacuum residuum fraction. The vacuum gas oil is hydrocracked to form at least one low sulfur fuel product. The light gas oil fraction is hydrotreated. The vacuum gas oil may be hydrocracked in one or more stages. Hydrocracking in the second stage, if present, will convert of at least 20% of the first zone effluent, to create a low sulfur light gas oil fraction. The light gas oil fraction may then be hydrotreated.

    摘要翻译: 本发明涉及一种原油脱硫方法,其包括对粗脱硫装置中的原油进料进行加氢脱硫。 然后将脱硫的原油分离成轻瓦斯油馏分,减压瓦斯油馏分和真空渣油馏分。 减压瓦斯油被加氢裂化以形成至少一种低硫燃料产物。 轻油馏分被加氢处理。 减压瓦斯油可以在一个或多个阶段加氢裂化。 第二阶段的加氢裂化(如果存在)将转化至少20%的第一区流出物,以产生低硫轻瓦斯油馏分。 然后轻油馏分可以进行加氢处理。