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    Combination cocurrent and countercurrent staged hydroprocessing with a vapor stage
    2.
    发明授权
    Combination cocurrent and countercurrent staged hydroprocessing with a vapor stage 失效
    组合并流和逆流分级加氢处理与蒸气阶段

    公开(公告)号：US6153086A

    公开(公告)日：2000-11-28

    申请号：US73414

    申请日：1998-05-06

    申请人： Ramesh Gupta ,  Henry Jung ,  Edward S. Ellis ,  James J. Schorfheide ,  Larry L. Iaccino

    发明人： Ramesh Gupta ,  Henry Jung ,  Edward S. Ellis ,  James J. Schorfheide ,  Larry L. Iaccino

    IPC分类号： C10G65/12 ,  C10G45/00 ,  C10G47/00 ,  C10G65/00 ,  C10G65/02 ,  C10G69/04 ,  C10G69/06

    CPC分类号： C10G65/12 ,  C10G65/00 ,  C10G69/04 ,  C10G69/06 ,  C10G2300/202 ,  C10G2300/207

    摘要： A hydroprocessing process includes a cocurrent flow liquid reaction stage, a countercurrent flow liquid reaction stage and a vapor reaction stage in which feed components are catalytically hydroprocessed by reacting with hydrogen. Both liquid stages both produce a liquid and a vapor effluent, with the cocurrent stage liquid effluent the feed for the countercurrent stage and the countercurrent stage liquid effluent the hydroprocessed product liquid. Both liquid stage vapor effluents are combined and catalytically reacted with hydrogen in a vapor reaction stage, to form a hydroprocessed vapor. This vapor is cooled to condense and recover a portion of the hydroprocessed hydrocarbonaceous vapor components as additional product liquid. The uncondensed vapor is rich in hydrogen and is cleaned up if necessary, to remove contaminants, and then recycled back into the cocurrent stage as hydrogen-containing treat gas. Fresh hydrogen is introduced into the countercurrent stage and the countercurrent stage effluent contains sufficient, and preferably all of the hydrogen for the vapor stage reaction.

    摘要翻译： 加氢处理方法包括并流流动液体反应阶段，逆流流动反应阶段和蒸气反应阶段，其中进料组分通过与氢反应进行催化加氢处理。 两个液相都产生液体和蒸汽流出物，并流阶段液体流出物是逆流阶段的进料和逆流阶段液体流出加氢产物液体。 两个液相蒸气流出物在蒸气反应阶段中与氢组合并催化反应，形成加氢处理的蒸汽。 将该蒸气冷却以冷凝并回收一部分加氢处理的含烃蒸汽组分作为另外的产物液体。 未冷凝的蒸汽富含氢气，如果需要，将其清除，以除去污染物，然后再循环回到并流阶段作为含氢处理气体。 将新鲜氢气引入逆流阶段，逆流阶段流出物含有足够的，优选全部用于蒸气阶段反应的氢气。

    Countercurrent reactor
    5.
    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
    6.
    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
    9.
    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。

    Production of low sulfur/low aromatics distillates
    10.
    发明授权
    Production of low sulfur/low aromatics distillates 有权
    生产低硫/低芳烃馏分

    公开(公告)号：US06824673B1

    公开(公告)日：2004-11-30

    申请号：US09553374

    申请日：2000-04-20

    申请人： Edward S. Ellis ,  Henry Jung ,  William E. Lewis ,  Larry L. Iaccino ,  Michele S. Touvelle ,  Gordon F. Stuntz

    发明人： Edward S. Ellis ,  Henry Jung ,  William E. Lewis ,  Larry L. Iaccino ,  Michele S. Touvelle ,  Gordon F. Stuntz

    IPC分类号： C10G4500

    CPC分类号： C10G65/12

    摘要： A process for producing distillate boiling range streams that are low in both sulfur and aromatics. A distillate feedstock is treated in a first hydrodesulfurization stage in the presence of a hydrogen-containing treat gas and a hydrodesulfurization catalyst, thereby resulting in partial desufurization of the stream. The partially desulfurized distillate stream is then treated in a second hydrodesulfurization stage, also in the presence of a hydrogen-containing treat gas and a hydrodesulfurization catalyst. The hydrogen-containing treat gas is cascaded from the next downstream reaction stage, which is an aromatics hydrogenation stage.

    摘要翻译： 一种生产硫和芳烃含量低的馏出物沸腾物流的方法。 在含氢处理气体和加氢脱硫催化剂的存在下，在第一加氢脱硫阶段处理馏出物原料，从而导致料流的部分脱硫。 然后在第二加氢脱硫阶段，在含氢处理气体和加氢脱硫催化剂的存在下处理部分脱硫的馏出物物流。 含氢处理气体从下一个下游反应阶段级联，其是芳族化合物氢化反应阶段。