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    Countercurrent reactor
    12.
    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

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

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

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

    CPC classification number: B01D3/16 ,  B01J8/0453 ,  B01J8/0492 ,  C10G49/002

    Abstract: 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.

    Abstract translation: 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。

    Integrated staged catalytic cracking and hydroprocessing process (JHT-9614)
    13.
    发明授权
    Integrated staged catalytic cracking and hydroprocessing process (JHT-9614) 失效
    综合分级催化裂化加氢处理工艺（JHT-9614）

    公开(公告)号：US5770044A

    公开(公告)日：1998-06-23

    申请号：US702347

    申请日：1996-08-23

    Applicant: Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

    Inventor： Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

    IPC: C10G7/00 ,  C10G11/05 ,  C10G11/18 ,  C10G35/04 ,  C10G45/00 ,  C10G49/04 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/08 ,  C10G51/02

    CPC classification number: C10G69/00 ,  C10G69/04 ,  C10G69/06

    Abstract: 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.

    Abstract translation: 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。

    Hydroprocessing reactor with enhanced product selectivity
    14.
    发明授权
    Hydroprocessing reactor with enhanced product selectivity 失效
    加氢反应器具有增强的产品选择性

    公开(公告)号：US5670116A

    公开(公告)日：1997-09-23

    申请号：US567450

    申请日：1995-12-05

    Applicant: Ramesh Gupta ,  Edward S. Ellis

    Inventor： Ramesh Gupta ,  Edward S. Ellis

    IPC: B01J8/04 ,  C10G49/00

    CPC classification number: C10G49/002 ,  B01J8/0453 ,  B01J8/0492 ,  B01J2208/00849

    Abstract: Petroleum reactors are provided which are comprised of one or more serially disposed reaction zones, each zone containing a suitable catalyst, wherein each reaction zone is followed by a non-reaction zone. One or more of said reaction zones contains a vapor by-pass means such that the vapor from one or more upstream non-reaction zones by-passes one or more downstream reaction zones and is introduced into a downstream non-reaction zone.

    Abstract translation: 提供石油反应器，其由一个或多个连续设置的反应区组成，每个区域含有合适的催化剂，其中每个反应区域之后是非反应区。 所述反应区中的一个或多个包含蒸气旁路装置，使得来自一个或多个上游非反应区的蒸汽旁路一个或多个下游反应区并引入下游非反应区。

    Integrated staged catalytic cracking and hydroprocessing process
    16.
    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：US5770043A

    公开(公告)日：1998-06-23

    申请号：US697381

    申请日：1996-08-23

    Applicant: Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

    Inventor： Edward S. Ellis ,  Ramesh Gupta ,  Martin G. Bienstock

    IPC: C10G7/00 ,  C10G11/05 ,  C10G11/18 ,  C10G35/04 ,  C10G45/00 ,  C10G49/04 ,  C10G69/00 ,  C10G69/04 ,  C10G69/06 ,  C10G69/08 ,  C10G51/02

    CPC classification number: C10G69/04 ,  C10G69/00 ,  C10G69/06

    Abstract: Disclosed is a catalytic cracking process which includes more than one catalytic cracking reaction step. The process integrates a hydroprocessing process step between the catalytic cracking reaction steps in order to maximize olefins production, mid-distillate quality and naphtha octane level in the cracked products. Preferably, a first cracked hydrocarbon product is obtained from a first cracking stage and separated into a mid-distillate and gas oil containing fraction having an initial boiling point of at least 300.degree. F., the distillate and gas oil containing fraction is hydroprocessed, and a naphtha fraction and a gas oil containing bottoms fraction of the hydroprocessed material are cracked in a second cracking stage.

    Abstract translation: 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。 该过程在催化裂化反应步骤之间整合加氢处理步骤，以使裂化产物中的烯烃生产，中间馏分质量和石脑油辛烷值达到最大。 优选地，从第一裂解阶段获得第一裂化烃产物，并将其分离成具有初馏点至少为300°F的中间馏分和含瓦斯油的馏分，加氢处理馏出物和瓦斯油馏分， 石脑油馏分和加氢处理材料的含有塔底馏分的瓦斯油在第二裂解阶段裂化。

    Countercurrent reactor with interstage stripping of NH3 and H2S in gas/liquid contacting zones
    17.
    发明授权
    Countercurrent reactor with interstage stripping of NH3 and H2S in gas/liquid contacting zones 有权
    逆流反应器，在气/液接触区域内具有级间汽提NH3和H2S

    公开(公告)号：US06241952B1

    公开(公告)日：2001-06-05

    申请号：US09373255

    申请日：1999-08-12

    Applicant: Edward S. Ellis ,  Ramesh Gupta

    Inventor： Edward S. Ellis ,  Ramesh Gupta

    IPC: B01J804

    CPC classification number: C10G49/002 ,  B01J8/0492

    Abstract: A reactor for reacting liquid petroleum or chemical streams wherein the liquid stream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas. The reactor is comprised of at least one vertically disposed reaction zone, each containing a bed of catalyst, wherein each reaction zone may contain vapor bypass means, and wherein each reaction zone is immediately preceded by a non-reaction zone, and wherein each non-reaction zone contains a gas/liquid contacting zone for stripping gaseous by-products, such as NH3 and H2S, from the liquid stream.

    Abstract translation: 用于使液体石油或化学物流反应的反应器，其中液体流与处理气体的流动例如含氢气体逆流流动。 反应器由至少一个垂直设置的反应区组成，每个反应区各自含有催化剂床，其中每个反应区可以含有蒸气旁路装置，并且其中每个反应区紧接在非反应区之前， 反应区包含用于从液体流中汽提气态副产物如NH 3和H 2 S的气/液接触区。

    Two stage hydroprocessing with vapor-liquid interstage contacting for vapor heteroatom removal
    20.
    发明授权
    Two stage hydroprocessing with vapor-liquid interstage contacting for vapor heteroatom removal 有权
    双级加氢处理，气 - 液间级接触气相除去杂原子

    公开(公告)号：US5968346A

    公开(公告)日：1999-10-19

    申请号：US153921

    申请日：1998-09-16

    Applicant: Henry Jung ,  Ramesh Gupta ,  Edward S. Ellis ,  William E. Lewis

    Inventor： Henry Jung ,  Ramesh Gupta ,  Edward S. Ellis ,  William E. Lewis

    IPC: C10G65/02 ,  C10G45/02 ,  C10G65/04 ,  C10G65/10 ,  C10G65/12 ,  C10G70/06

    CPC classification number: C10G65/12 ,  C10G65/04 ,  C10G65/10 ,  C10G70/06

    Abstract: A hydroprocessing process includes two hydroprocessing reaction stages, both of which produce a liquid and a vapor effluent, and a liquid-vapor contacting stage. The first stage vapor effluent contains impurities, such as heteroatom compounds, which are removed from the vapor by contact with processed liquid effluent derived from one or both reaction stages and, optionally, also liquid recovered from processed vapor. The first and contact stage liquid effluents are passed into the second stage to finish the hydoprocessing. The contact and second stage vapor effluents are cooled to recover additional hydroprocessed product liquid.

    Abstract translation: 加氢处理方法包括两个加氢处理反应阶段，它们都产生液体和蒸汽流出物，以及液 - 气接触阶段。 第一级蒸汽流出物含有诸如杂原子化合物的杂质，其通过与来自一个或两个反应级的处理液体流出物接触而从蒸气中除去，并且任选地还含有从经处理的蒸气回收的液体。 第一阶段和接触阶段的液体流出物进入第二阶段以完成加氢处理。 将接触和第二级蒸汽流出物冷却以回收另外的加氢处理产物液体。

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