RESIDUE HYDROCRACKING PROCESSING
    11.
    发明申请
    RESIDUE HYDROCRACKING PROCESSING 审中-公开
    残留加氢处理

    公开(公告)号:US20140221713A1

    公开(公告)日:2014-08-07

    申请号:US13758429

    申请日:2013-02-04

    Abstract: A process for upgrading residuum hydrocarbons and decreasing tendency of the resulting products toward asphaltenic sediment formation in downstream processes is disclosed. The process may include: contacting a residuum hydrocarbon fraction and hydrogen with a hydroconversion catalyst in a hydrocracking reaction zone to convert at least a portion of the residuum hydrocarbon fraction to lighter hydrocarbons; recovering an effluent from the hydrocracking reaction zone; contacting hydrogen and at least a portion of the effluent with a resid hydrotreating catalyst; and separating the effluent to recover two or more hydrocarbon fractions.

    Abstract translation: 公开了一种用于提高残油烃的方法,并且降低了所得产物在下游方法中形成沥青沉淀物形成的趋势。 该方法可以包括:在加氢裂化反应区中将残油烃馏分和氢气与加氢转化催化剂接触以将至少一部分残油烃馏分转化成轻质烃; 从加氢裂化反应区回收污水; 用残渣加氢处理催化剂使氢气和至少一部分流出物接触; 并分离出流出物以回收两种或多种烃馏分。

    CONVERSION OF ASPHALTENIC PITCH WITHIN AN EBULLATED BED RESIDUUM HYDROCRACKING PROCESS
    12.
    发明申请
    CONVERSION OF ASPHALTENIC PITCH WITHIN AN EBULLATED BED RESIDUUM HYDROCRACKING PROCESS 有权
    浸渍床残留水解过程中的ASPHALTENIC PITCH的转化

    公开(公告)号:US20140197069A1

    公开(公告)日:2014-07-17

    申请号:US13743936

    申请日:2013-01-17

    Abstract: A process for upgrading residuum hydrocarbons including: feeding pitch, hydrogen, and a partially spent catalyst recovered from a hydrocracking reactor to an ebullated bed pitch hydrocracking reactor; contacting the pitch, hydrogen, and the catalyst in the ebullated bed pitch hydrocracking reactor at reaction conditions of temperature and pressure sufficient to convert at least a portion of the pitch to distillate hydrocarbons; and separating the distillate hydrocarbons from the catalyst. In some embodiments, the process may include selecting the ebullated bed pitch hydrocracking reactor reaction conditions to be at or below the level where sediment formation would otherwise become excessive and prevent continuity of operations.

    Abstract translation: 一种用于升级残油烃的方法,包括:将沥青,氢气和从加氢裂化反应器回收的部分废催化剂进料到沸腾床沥青加氢裂化反应器; 在沸腾床沥青加氢裂化反应器中的沥青,氢气和催化剂在足以将至少一部分沥青转化成馏出物烃的温度和压力的反应条件下接触; 并将馏出物烃与催化剂分离。 在一些实施方案中,该方法可以包括选择沸腾床沥青加氢裂化反应器反应条件处于或低于沉淀物形成否则将变得过大并防止操作连续性的水平。

    UPGRADING RAW SHALE-DERIVED CRUDE OILS TO HYDROCARBON DISTILLATE FUELS
    19.
    发明申请
    UPGRADING RAW SHALE-DERIVED CRUDE OILS TO HYDROCARBON DISTILLATE FUELS 审中-公开
    将原始石油衍生的原油升华至油气馏分燃料

    公开(公告)号:US20150307790A1

    公开(公告)日:2015-10-29

    申请号:US14793045

    申请日:2015-07-07

    Abstract: Integrated processes for upgrading crude shale-derived oils, such as those produced by oil shale retorting or by in situ extraction or combinations thereof. Processes disclosed provide for a split-flow processing scheme to upgrade whole shale oil. The split flow concepts described herein, i.e., naphtha and kerosene hydrotreating in one or more stages and gas oil hydrotreating in one or more stages, requires additional equipment as compared to the alternative approach of whole oil hydrotreating. While contrary to conventional wisdom as requiring more capital equipment to achieve the same final product specifications, the operating efficiency vis a vis on-stream time efficiency and product quality resulting from the split flow concept far exceed in value the somewhat incrementally higher capital expenditure costs.

    Abstract translation: 用于改进粗页岩衍生油的综合方法,例如通过油页岩蒸煮或原位萃取或其组合生产的那些。 所公开的方法提供了用于升级整个页岩油的分流处理方案。 本文所述的分流流动概念,即在一个或多个阶段中加氢处理的石脑油和煤油,以及一个或多个阶段加氢处理的瓦斯油,与全油加氢处理的替代方法相比,需要额外的设备。 虽然与传统智慧相反,要求更多的资本设备实现相同的最终产品规格,但是由分拆流程概念导致的运行效率和产品质量的运营效率远远超过了价值上的一些逐渐增加的资本支出成本。

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