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    Countercurrent reactor
    1.
    发明授权
    Countercurrent reactor 失效
    逆流反应堆

    公开(公告)号：US5939031A

    公开(公告)日：1999-08-17

    申请号：US885699

    申请日：1997-06-30

    申请人： Edward S. Ellis ,  Jeffrey W. Frederick ,  Ramesh Gupta ,  David C. Dankworth ,  Dimitrios M. Tsangaris

    发明人： Edward S. Ellis ,  Jeffrey W. Frederick ,  Ramesh Gupta ,  David C. Dankworth ,  Dimitrios M. Tsangaris

    IPC分类号： B01D3/16 ,  B01J8/04 ,  B01J19/24 ,  C10G45/00 ,  C10G45/44 ,  C10G47/00 ,  C10G49/00 ,  C10G65/02

    CPC分类号： B01D3/16 ,  B01J8/0453 ,  B01J8/0492 ,  C10G49/002

    摘要： A reactor is provided for reacting a liquid with a treat gas in the presence of a catalyst, the reactor comprising a continuous wall enclosing a first reaction zone, wherein the first reaction zone includes a catalyst for causing a desired reaction between the liquid and the treat gas; a liquid inlet above the first reaction zone for allowing an unreacted portion of the liquid to enter the reactor; a gas inlet below the first reaction zone for allowing an unreacted portion of the treat gas to enter the reactor; a liquid outlet below the first reaction zone for allowing a reacted portion of the liquid to exit the reactor; a gas outlet above the first reaction zone for allowing a reacted portion of the treat gas to exit the reactor; and a liquid bypass device in the first reaction zone for allowing a portion of the liquid to bypass a portion of the first reaction zone, the liquid bypass device including a liquid bypass regulating device for regulating the amount of liquid which bypasses the first reaction zone. In a preferred embodiment, a plurality of reaction zones are present, and a liquid distribution tray is disposed above each reaction zone. Preferably, the liquid bypass device creates a hydrostatic seal with the liquid accumulating in the distribution tray so that the timing and extent of liquid bypass is self-regulating based on predefined flooding conditions.

    摘要翻译： 提供反应器用于在催化剂存在下使液体与处理气体反应，所述反应器包括包围第一反应区的连续壁，其中第一反应区包括用于在液体和处理之间引起所需反应的催化剂 加油站; 在第一反应区上方的液体入口，用于使未反应的液体部分进入反应器; 位于第一反应区下方的气体入口，用于使未处理部分的处理气体进入反应器; 位于第一反应区下方的液体出口，用于允许液体的反应部分离开反应器; 在第一反应区上方的气体出口，用于使处理气体的反应部分离开反应器; 以及液体旁路装置，其在所述第一反应区中允许所述液体的一部分绕过所述第一反应区的一部分，所述液体旁路装置包括用于调节绕过所述第一反应区的液体量的液体旁路调节装置。 在优选的实施方案中，存在多个反应区，并且在每个反应区上方设置液体分配塔。 优选地，液体旁路装置产生液体密封，液体积聚在分配盘中，使得基于预定的淹水条件，液体旁路的时间和程度是自调节的。

    Countercurrent reactor
    2.
    发明授权
    Countercurrent reactor 失效
    逆流反应堆

    公开(公告)号：US5942197A

    公开(公告)日：1999-08-24

    申请号：US885788

    申请日：1997-06-30

    申请人： Ramesh Gupta ,  Jeffrey W. Frederick ,  Edward S. Ellis ,  David C. Dankworth ,  Dimitrios M. Tsangaris

    发明人： Ramesh Gupta ,  Jeffrey W. Frederick ,  Edward S. Ellis ,  David C. Dankworth ,  Dimitrios M. Tsangaris

    IPC分类号： B01D3/16 ,  B01J8/04 ,  B01J19/24 ,  C10G45/00 ,  C10G45/44 ,  C10G47/00 ,  C10G49/00 ,  C10G65/02

    CPC分类号： B01D3/16 ,  B01J8/0453 ,  B01J8/0492 ,  C10G49/002

    摘要： A reactor is provided for reacting a liquid with a treat gas in the presence of a catalyst, the reactor comprising a continuous wall enclosing a first reaction zone, wherein the first reaction zone includes a catalyst for causing a desired reaction between the liquid and the treat gas; a liquid inlet above the first reaction zone for allowing a portion of the liquid to enter the reactor; a gas inlet below the first reaction zone for allowing a portion of the treat gas to enter the reactor; a liquid outlet below the first reaction zone for allowing a reacted portion of the liquid to exit the reactor; a gas outlet above the first reaction zone for allowing a portion of the treat gas to exit the reactor; and a gas bypass device in the first reaction zone for allowing a portion of the treat gas to bypass a portion of the first reaction zone, the gas bypass device including a gas bypass regulating device for regulating the amount of treat gas which bypasses the first reaction zone. In a preferred embodiment, a plurality of reaction zones are present, and a liquid distribution tray is disposed above each reaction zone. Preferably, the gas bypass device creates a hydrostatic seal with the liquid accumulating in the distribution tray so that the timing and extent of gas bypass is self-regulating based on predefined flooding conditions.

    摘要翻译： 提供反应器用于在催化剂存在下使液体与处理气体反应，所述反应器包括包围第一反应区的连续壁，其中第一反应区包括用于在液体和处理之间引起所需反应的催化剂 加油站; 在第一反应区上方的液体入口，用于使一部分液体进入反应器; 位于第一反应区下方的气体入口，用于使一部分处理气体进入反应器; 位于第一反应区下方的液体出口，用于允许液体的反应部分离开反应器; 在第一反应区上方的气体出口，用于允许一部分处理气体离开反应器; 以及在所述第一反应区域中的气体旁通装置，用于允许所述处理气体的一部分绕过所述第一反应区域的一部分，所述气体旁通装置包括用于调节绕过所述第一反应的处理气体的量的气体旁路调节装置 区。 在优选的实施方案中，存在多个反应区，并且在每个反应区上方设置液体分配塔。 优选地，气体旁通装置产生液体密封，液体积聚在分配盘中，使得基于预定的淹水条件，气体旁路的时间和程度是自调节的。

    Three stage cocurrent liquid and vapor hydroprocessing
    6.
    发明授权
    Three stage cocurrent liquid and vapor hydroprocessing 失效
    三级并流液相加氢处理

    公开(公告)号：US6054041A

    公开(公告)日：2000-04-25

    申请号：US73412

    申请日：1998-05-06

    申请人： Edward S. Ellis ,  William Ernest Lewis ,  David C. Dankworth ,  Ramesh Gupta

    发明人： Edward S. Ellis ,  William Ernest Lewis ,  David C. Dankworth ,  Ramesh Gupta

    IPC分类号： C10G65/04 ,  C10G45/02 ,  C10G65/00 ,  C10G65/02 ,  C10G45/00

    CPC分类号： C10G65/00

    摘要： A hydroprocessing process includes two cocurrent flow liquid reaction stages and one vapor stage, in which feed components are catalytically hydroprocessed by reacting with hydrogen. The liquid stages both produce a liquid and a hydrogen-rich vapor effluent, with most of the hydroprocessing accomplished in the first stage. The first stage vapor is also hydroprocessed. The hydroprocessed vapor and second stage vapor are cooled to condense and recover additional product liquid and produce an uncondensed hydrogen-rich vapor. After cleanup to remove contaminants, the hydrogen-rich vapor is recycled back into the first stage as treat gas. Fresh hydrogen is introduced into the second stage. This is useful for hydrotreating heteroatom-containing hydrocarbons.

    摘要翻译： 加氢处理方法包括两个并流流动液体反应阶段和一个蒸气阶段，其中进料组分通过与氢反应催化加氢处理。 液相都产生液体和富氢蒸汽流出物，大部分加氢处理在第一阶段完成。 第一级蒸气也被加氢处理。 将加氢蒸气和第二级蒸气冷却以冷凝并回收另外的产物液体并产生未冷凝的富氢蒸汽。 净化后清除污染物，富氢蒸汽再循环回第一阶段作为处理气体。 新鲜氢气被引入第二阶段。 这对于加氢处理含杂原子的烃是有用的。

    Multistage removal of heteroatoms and wax from distillate fuel
    7.
    发明授权
    Multistage removal of heteroatoms and wax from distillate fuel 有权
    从馏出燃料中多步去除杂原子和蜡

    公开(公告)号：US07282138B2

    公开(公告)日：2007-10-16

    申请号：US10938301

    申请日：2004-09-10

    申请人： Edward S. Ellis ,  Ramesh Gupta ,  William J. Novak

    发明人： Edward S. Ellis ,  Ramesh Gupta ,  William J. Novak

    IPC分类号： C10G69/02

    CPC分类号： C10G65/043

    摘要： A distillate fuel feed is hydrotreated to remove heteroatoms and then separated into light and heavy hydrotreated fractions, with the heavy fraction catalytically dewaxed to improve low temperature properties. The hydrotreating and dewaxing are conducted in separate stages, which may be in the same reactor vessel. Fresh hydrogen may be passed into the dewaxing stage, with the dewaxing stage gaseous effluent then passed into the hydrotreating stage to provide hydrogen for the hydrotreating. Existing hydrotreating reaction vessels and facilities may be retrofitted to add one or more dewaxing stages.

    摘要翻译： 将馏出物燃料进料加氢处理以除去杂原子，然后分离成轻重和加氢处理的馏分，重馏分催化脱蜡以改善低温性能。 加氢处理和脱蜡在不同的阶段进行，可以在同一个反应器容器中。 新鲜的氢气可以进入脱蜡阶段，脱蜡阶段的气态流出物然后进入加氢处理阶段以提供氢气用于加氢处理。 现有的加氢处理反应容器和设备可以被改装以加入一个或多个脱蜡阶段。

    Integrated staged catalytic cracking and hydroprocessing process
    8.
    发明授权
    Integrated staged catalytic cracking and hydroprocessing process 失效
    综合分级催化裂化加氢处理工艺

    公开(公告)号：US5582711A

    公开(公告)日：1996-12-10

    申请号：US292625

    申请日：1994-08-17

    申请人： Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

    发明人： Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

    IPC分类号： C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G51/02

    CPC分类号： C10G69/04 ,  C10G69/00 ,  C10G69/06

    摘要： Disclosed is a catalytic cracking process which includes more than one catalytic cracking reaction step. The process integrates a hydroprocessing step between the catalytic cracking reaction steps in order to maximize olefins production, distillate quality and octane level of the overall cracked product. Preferably, the hydroprocessing step is included between the reaction stages, and a portion of the hydroprocessed products, i.e., a naphtha and mid distillate fraction, is combined with cracked product for further separation and hydroprocessing. It is also preferred that the first catalytic cracking reaction step be a short contact time reaction step.

    摘要翻译： 公开了一种催化裂解方法，其包括多于一个催化裂化反应步骤。 该方法将催化裂化反应步骤之间的加氢处理步骤整合，以使烯烃的产生最大化，馏出物质量和整个裂解产物的辛烷值达到最大。 优选地，加氢处理步骤包括在反应阶段之间，并且一部分加氢处理产物，即石脑油和中间馏分馏分与裂化产物组合用于进一步分离和加氢处理。 还优选的是，第一催化裂化反应步骤是短接触时间反应步骤。

    Liquid and vapor stage hydroprocessing using once-through hydrogen
    10.
    发明授权
    Liquid and vapor stage hydroprocessing using once-through hydrogen 失效
    使用一次通过氢气的液相和蒸汽级加氢处理

    公开(公告)号：US06224749B1

    公开(公告)日：2001-05-01

    申请号：US09073415

    申请日：1998-05-06

    申请人： Ramesh Gupta ,  Henry Jung ,  Edward S. Ellis ,  Gerald E. Markley

    发明人： Ramesh Gupta ,  Henry Jung ,  Edward S. Ellis ,  Gerald E. Markley

    IPC分类号： C10G6502

    CPC分类号： C10G65/00 ,  B01J8/04 ,  B01J8/0488 ,  B01J2208/00283

    摘要： A three stage hydroprocessing process includes two liquid and one vapor reaction stages, both of which produce an effluent comprising liquid and vapor. Both vapor effluents comprise vaporized hydrocarbonaceous material. Fresh hydrogen is used for the hydroprocessing in both liquid stages. The second stage liquid effluent comprises the product liquid. The first stage liquid effluent is the feed for the second stage. The first stage vapor effluent is hydroprocessed in the vapor stage and then cooled to condense and recover at least a portion of the processed vapor as additional product liquid.

    摘要翻译： 三级加氢处理方法包括两个液体和一个蒸气反应阶段，二者都产生包含液体和蒸汽的流出物。 两种蒸汽流出物都包含蒸发的含烃材料。 新鲜氢气用于两个液体阶段的加氢处理。 第二级液体流出物包括产物液体。 第一阶段液体流出物是第二阶段的进料。 第一级蒸汽流出物在蒸气阶段加氢处理，然后冷却以冷凝并回收至少一部分经处理的蒸气作为另外的产物液体。