HYDROCRACKING PROCESS
    3.
    发明申请
    HYDROCRACKING PROCESS 审中-公开
    加氢裂化工艺

    公开(公告)号:WO2009052017A3

    公开(公告)日:2009-06-18

    申请号:PCT/US2008079445

    申请日:2008-10-10

    CPC classification number: C10G65/12 C10G2300/42

    Abstract: Methods (10, 110, 210) of hydrocracking hydrocarbon streams (12, 112, 212) are provided that employ substantially liquid-phase continuous hydroprocessing conditions. In one aspect, the method includes a separate hydrotreating and hydrocracking system where the hydrocracking zone (24) is a substantially liquid-phase continuous system. In another aspect, the method includes a two stage hydrocracking system where one or both of the hydrocracking zones (113, 124) (213, 224) are a substantially liquid-phase continuous reaction system.

    Abstract translation: 提供加氢裂化烃物流(12,112,212)的方法(10,110,210),其基本上采用液相连续加氢处理条件。 一方面,该方法包括单独的加氢处理和加氢裂化系统,其中加氢裂化区(24)基本上是液相连续系统。 另一方面,该方法包括两阶段加氢裂化系统,其中加氢裂化区(113,124)(213,224)中的一个或两个基本上是液相连续反应系统。

    HYDROCRACKING PROCESS
    4.
    发明专利

    公开(公告)号:CA2702395C

    公开(公告)日:2015-02-24

    申请号:CA2702395

    申请日:2008-10-10

    Applicant: UOP LLC

    Abstract: Methods (10, 110, 210) of hydrocracking hydrocarbon streams (12, 112, 212) are provided that employ substantially liquid-phase continuous hydroprocessing conditions. In one aspect, the method includes a separate hydrotreating and hydrocracking system where the hydrocracking zone (24) is a substantially liquid-phase continuous system. In another aspect, the method includes a two stage hydrocracking system where one or both of the hydrocracking zones (113, 124) (213, 224) are a substantially liquid-phase continuous reaction system.

    HYDROCRACKING PROCESS
    5.
    发明专利

    公开(公告)号:CA2702395A1

    公开(公告)日:2009-04-23

    申请号:CA2702395

    申请日:2008-10-10

    Applicant: UOP LLC

    Abstract: Methods (10, 110, 210) of hydrocracking hydrocarbon streams (12, 112, 212) are provided that employ substantially liquid-phase continuous hydroprocessing conditions. In one aspect, the method includes a separate hydrotreating and hydrocracking system where the hydrocracking zone (24) is a substantially liquid-phase continuous system. In another aspect, the method includes a two stage hydrocracking system where one or both of the hydrocracking zones (113, 124) (213, 224) are a substantially liquid-phase continuous reaction system.

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