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    Start-up method of bubble column slurry bed reactor
    7.
    发明授权
    Start-up method of bubble column slurry bed reactor 有权
    鼓泡塔浆床反应器启动方法

    公开(公告)号：US09376352B2

    公开(公告)日：2016-06-28

    申请号：US14387391

    申请日：2013-03-27

    申请人： Japan Oil, Gas and Metals National Corporation ,  Inpex Corporation ,  JX Nippon Oil & Energy Corporation ,  Japan Petroleum Exploration Co., Ltd. ,  Cosmo Oil Co., Ltd. ,  Nippon Steel & Sumikin Engineering Co., Ltd.

    发明人： Kazuhiko Tasaka

    IPC分类号： C07C1/04 ,  C10G2/00

    CPC分类号： C07C1/0485 ,  C10G2/342 ,  C10G2300/4031

    摘要： A start-up method of a bubble column slurry bed reactor for producing hydrocarbons includes: a first step that fills into a reactor a slurry in which a Fischer-Tropsch synthesis reaction catalyst particles are suspended in a slurry preparation oil with a 5% distillation point of 120 to 270° C., a 95% distillation point of 330 to 650° C., and a sulfur component and an aromatic component of 1 mass ppm or less, and a second step that, in a state where synthesis gas that is primarily hydrogen and carbon monoxide is introduced into the slurry filled into the reactor, raises the temperature of the reactor and starts the Fischer-Tropsch synthesis reaction. As the slurry preparation oil, one containing predetermined components in preset amounts is used. In the first step, the slurry is filled into the reactor in an amount in which airborne droplets do not flow out.

    摘要翻译： 用于生产烃的鼓泡塔淤浆床反应器的启动方法包括：第一步骤，向反应器中填充一种浆料，其中费 - 托合成反应催化剂颗粒悬浮在具有5％蒸馏点的浆料制备油中 120〜270℃，95％蒸馏点为330〜650℃，硫成分和1质量ppm以下的芳香族成分，第二工序为：在合成气为 主要将氢和一氧化碳引入填充到反应器中的浆料中，升高反应器的温度并开始费 - 托合成反应。 作为浆料制备油，使用含有预定量的预定组分的油。 在第一步骤中，将浆料以空气中的液滴不会流出的量装入反应器中。

    Hydroprocessing initializing process and apparatus relating thereto
    8.
    发明授权
    Hydroprocessing initializing process and apparatus relating thereto 有权
    加氢处理初始化过程和与其相关的装置

    公开(公告)号：US09359563B2

    公开(公告)日：2016-06-07

    申请号：US13863068

    申请日：2013-04-15

    申请人： UOP, LLC

    发明人： Christopher Lepine Standing

    IPC分类号： C10G65/12 ,  C10G47/36

    CPC分类号： C10G65/12 ,  C10G47/36 ,  C10G2300/4031

    摘要： One exemplary embodiment can be a process for initializing hydroprocessing. Generally, the process can include providing a hydrocarbon feed to a hydrotreating zone within which the hydrotreating temperature is catalytically limited, passing an effluent from the hydrotreating zone to a hydrocracking zone, and adding a gas to the effluent that has a higher temperature than the effluent. Thus, the temperature of the effluent may be raised, facilitating hydrocracking reactions within the hydrocracking zone.

    摘要翻译： 一个示例性实施例可以是用于初始化加氢处理的过程。 通常，该方法可以包括向加氢处理区提供烃进料，加氢处理温度在该加氢处理区内被催化限制，将流出物从加氢处理区传递到加氢裂化区，并向流出物中加入气体，该流出物的温度高于流出物 。 因此，可以提高流出物的温度，从而促进加氢裂化区内的加氢裂化反应。

    FLUIDIZED BED UNIT STARTUP
    9.
    发明申请
    FLUIDIZED BED UNIT STARTUP 审中-公开
    流化床单元启动

    公开(公告)号：US20160060542A1

    公开(公告)日：2016-03-03

    申请号：US14827505

    申请日：2015-08-17

    申请人： Masaaki SUGITA ,  Christopher Gordon SMALLEY ,  George Phillip CHARLES ,  Robert Gerard TINGER ,  Terrance Charles OSBY ,  Allen Scott GAWLIK

    发明人： Masaaki SUGITA ,  Christopher Gordon SMALLEY ,  George Phillip CHARLES ,  Robert Gerard TINGER ,  Terrance Charles OSBY ,  Allen Scott GAWLIK

    IPC分类号： C10G11/20 ,  C07C2/86 ,  C10G11/05 ,  C07C1/20

    CPC分类号： C10G11/05 ,  C07C1/20 ,  C07C2/864 ,  C07C2529/40 ,  C10G3/42 ,  C10G3/49 ,  C10G11/18 ,  C10G2300/4031 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30 ,  C07C11/02 ,  C07C15/08

    摘要： The startup of a fluidized bed process unit uses an air heater to raise the temperature of the unit to the level necessary for operation of the unit to be self-sustaining in its normal operating regime without the use of torch oil. This startup sequence is particularly useful for fluidized bed units which utilize a circulating catalyst with particular emphasis on endothermic conversion units such as FCC and Resid Catalytic Cracking (RCC), but also on other catalytic units with circulating catalyst inventories such as various exothermic conversion, e.g. methanol conversion, processes. Elimination of the torch oil injection enables catalyst selectivity/activity to be retained during startup and at any other time that the heat requirement of the unit cannot be met by the internal functioning of the process, e.g. by coke generation during the reaction and combustion during regeneration of the catalysts or during the reaction itself.

    摘要翻译： 流化床处理单元的启动使用空气加热器将单元的温度升高到在其正常操作状态下自动维持单元的操作所需的水平，而不使用割炬油。 该启动顺序对于利用循环催化剂，特别强调吸热转化单元如FCC和残余催化裂化（RCC）的流化床单元特别有用，而且对于具有循环催化剂存量的其它催化单元，例如各种放热转化，例如， 甲醇转化，工艺。 消除割炬油注射使得催化剂选择性/活性在起动期间以及在任何其它时间保持单元的热量需求不能被过程的内部功能所满足。 在催化剂再生期间或在反应本身期间在反应和燃烧期间产生焦炭。

    PROCESS FOR REMOVING CATALYST FINES FROM A LIQUID STREAM FROM A FIXED BED REACTOR
    10.
    发明申请
    PROCESS FOR REMOVING CATALYST FINES FROM A LIQUID STREAM FROM A FIXED BED REACTOR 有权
    从固定床反应器中去除液体流中的催化剂成分的方法

    公开(公告)号：US20150360151A1

    公开(公告)日：2015-12-17

    申请号：US14303864

    申请日：2014-06-13

    申请人： UOP LLC

    发明人： Daniel James Pintar ,  Dorothy Richmond ,  John J. Jeanneret ,  Richard Hoehn

    IPC分类号： B01D29/56 ,  B01D29/52

    CPC分类号： B01D29/56 ,  B01D29/52 ,  B01J8/006 ,  B01J8/0453 ,  B01J8/0457 ,  B01J2208/00716 ,  B01J2208/00769 ,  C10G31/09 ,  C10G49/002 ,  C10G53/02 ,  C10G2300/4031 ,  C22B7/009 ,  Y02P10/214

    摘要： A process for filtering a liquid stream from a fixed bed reaction zone in order to remove catalyst fines contained in the stream. The effluent stream is passed to a filtering section which may contain at least two filtering vessels. Each filtering vessel includes at least two differently filtering sections, each section designed to collect differently sized particles. If a pressure drop occurs in one of the filtering vessels, it may be taken offline to remove the filtering sections and recover the metal in the particles collected on the filtering sections. The other filtering vessel can remain online to allow the filtering process to be continuous. Metal on the catalyst fines may be recovered.

    摘要翻译： 用于从固定床反应区过滤液体流以便除去流中所含的催化剂细粉的方法。 流出物流被传送到可以包含至少两个过滤容器的过滤部分。 每个过滤容器包括至少两个不同的过滤部分，每个部分被设计成收集不同尺寸的颗粒。 如果在其中一个过滤容器中发生压降，则可以离线以除去过滤部分并回收在过滤部分上收集的颗粒中的金属。 另一个过滤容器可以保持联机，以使过滤过程连续。 催化剂细粉上的金属可能被回收。