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    PROCESS AND APPARATUS FOR RECOVERING PRODUCTS FROM TWO REACTORS
    23.
    发明申请
    PROCESS AND APPARATUS FOR RECOVERING PRODUCTS FROM TWO REACTORS 审中-公开
    从两个反应器回收产品的方法和设备

    公开(公告)号：WO2011056691A3

    公开(公告)日：2011-09-22

    申请号：PCT/US2010054385

    申请日：2010-10-28

    Applicant: UOP LLC ,  LEONARD LAURA E ,  QAFISHEH JIBREEL A ,  MEHLBERG ROBERT L

    Inventor： LEONARD LAURA E ,  QAFISHEH JIBREEL A ,  MEHLBERG ROBERT L

    IPC: C10G11/18 ,  B01J8/26

    CPC classification number: C10G11/18 ,  C10G51/026 ,  C10G2300/1044

    Abstract: An apparatus and process are disclosed for catalytically converting two feed streams. The feed to a first catalytic reactor may be contacted with product from a second catalytic reactor to effect heat exchange between the two streams and to transfer catalyst from the product stream to the feed stream. The feed to the second catalytic reactor may be a portion of the product from the first catalytic reactor.

    Abstract translation: 公开了用于催化转化两种进料流的装置和方法。 到第一催化反应器的进料可以与来自第二催化反应器的产物接触以实现两个流之间的热交换并且将催化剂从产物流转移到进料流。 第二催化反应器的进料可以是来自第一催化反应器的产物的一部分。

    HYDROCRACKING PROCESS
    24.
    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

    Applicant: UOP LLC ,  KOKAYEFF PETER ,  DZIABALA BART ,  LEONARD LAURA E

    Inventor： KOKAYEFF PETER ,  DZIABALA BART ,  LEONARD LAURA E

    IPC: C10G55/04 ,  C10G55/06

    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
    25.
    发明申请
    HYDROCRACKING PROCESS 审中-公开
    水力过程

    公开(公告)号：WO2008014150A3

    公开(公告)日：2008-10-16

    申请号：PCT/US2007073708

    申请日：2007-07-17

    Applicant: UOP LLC ,  LEONARD LAURA E ,  KOKAYEFF PETER

    Inventor： LEONARD LAURA E ,  KOKAYEFF PETER

    IPC: C10G47/02

    CPC classification number: C10G65/12 ,  C10G2300/1011 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4081 ,  Y02P30/20

    Abstract: A catalytic hydrocracking process wherein a liquid phase stream comprising a hydrocarbonaceous feedstock (1), a liquid phase effluent from a hydrocracking zone (16), and hydrogen in a sufficiently low hydrogen concentration to maintain a liquid phase continuous system is fed into a hydrotreating zone (4) to produce a first hydrocarbonaceous stream comprising hydrocarbons having a reduced level of sulfur and nitrogen. The resulting hydrocarbons having a reduced level of sulfur and nitrogen are introduced into a hydrocracking zone (13) with a sufficiently low hydrogen concentration to maintain a liquid phase continuous system to produce a hydrocracking zone effluent (16) which provides lower boiling range hydrocarbons.

    Abstract translation: 一种催化加氢裂化方法，其中将包含烃原料（1），来自加氢裂化区（16）的液相流出物和维持液相连续系统的足够低氢浓度的氢气的液相料流进料到加氢处理区 （4）以产生包含具有降低的硫和氮水平的烃的第一烃流。 将具有降低的硫和氮水平的所得烃引入到具有足够低的氢浓度的加氢裂化区（13）中以保持液相连续系统以产生提供较低沸点烃的加氢裂化区流出物（16）。

    PYROLYTIC REACTOR AND METHOD OF USING
    28.
    发明专利
    PYROLYTIC REACTOR AND METHOD OF USING 未知

    公开(公告)号：AU2019202603A1

    公开(公告)日：2019-05-02

    申请号：AU2019202603

    申请日：2019-04-15

    Applicant: UOP LLC

    Inventor： GATTUPALLI RAJESWAR ,  KUCHANA VINAYENDER ,  LEONARD LAURA E ,  KOLLATI VIGHNESWARA R ,  SATTAR AZIZ ,  MOSTOFI-ASHTIANI MOHAMMAD R ,  SHAFE PETER

    IPC: B01J3/08 ,  B01J19/26 ,  C07C2/00 ,  C07C11/22

    Abstract: Methods and apparatus to produce alkynes are described. The method includes combusting fuel and an oxidizer in a combustion zone to create a carrier gas stream, which is accelerated to supersonic speed in an expansion zone. A feedstock material is injected into a feedstock injection zone using two or more pluralities of injection nozzles. The injection nozzles are arranged annularly. The carrier gas stream is transitioned from supersonic speed to subsonic speed to create a shockwave in a reaction zone. The reaction zone is directly connected to the feedstock injection zone, and the shockwave is created adjacent to the feedstock injection zone. The carrier gas stream and the feedstock material are simultaneously mixed and reacted. Q)~ coN No CN ) C N C co 0)

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