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    • 11. 发明授权
    • Staged upflow and downflow hydroprocessing with noncatalytic removal of
upflow stage vapor impurities
    • 分阶段上流和下流加氢处理与非催化去除上流阶段蒸汽杂质
    • US5985135A
    • 1999-11-16
    • US177734
    • 1998-10-23
    • Ramesh Gupta
    • Ramesh Gupta
    • C10G65/02C10G45/02C10G45/32C10G45/44C10G45/58C10G47/00C10G67/04C10G73/02C10G25/00C10G17/00
    • C10G67/04Y10S203/06
    • A hydroprocessing process for removing impurities from a feed comprising a hydrocarbonaceous liquid comprises at least one cocurrent, upflow hydroprocessing reaction stage, a vapor-liquid contacting stage and a downflow hydroprocessing reaction stage. The feed and hydrogen react in the upflow stage to produce a partially hydroprocessed liquid and vapor effluent. The vapor contacts a hydrocarbonaceous liquid in the contacting stage, which transfers impurities from the vapor into the liquid. The impurity-enriched contacting liquid mixes with the upflow stage liquid effluent and the combined liquid effluents react with hydrogen in the downflow reaction stage, to form a hydroprocessed product liquid and vapor effluent. Additional product liquid is recovered by cooling and condensing either or both the contacting and downflow stage vapor effluents.
    • 用于从包含烃液体的进料中除去杂质的加氢处理方法包括至少一个并流,向上加氢处理反应阶段,气液接触阶段和下流加氢反应阶段。 进料和氢气在上流阶段反应以产生部分加氢处理的液体和蒸汽流出物。 蒸气在接触阶段接触含烃液体,其将杂质从蒸气转移到液体中。 杂质富集的接触液体与上流阶段液体流出物混合,合并的液体流出物在下流反应阶段与氢气反应,形成加氢处理产物液体和蒸汽流出物。 通过冷却和冷凝接触和下流阶段蒸汽流出物中的任一种或两者来回收额外的产物液体。
    • 12. 发明授权
    • Countercurrent reactor
    • 逆流反应堆
    • US5939031A
    • 1999-08-17
    • US885699
    • 1997-06-30
    • Edward S. EllisJeffrey W. FrederickRamesh GuptaDavid C. DankworthDimitrios M. Tsangaris
    • Edward S. EllisJeffrey W. FrederickRamesh GuptaDavid C. DankworthDimitrios M. Tsangaris
    • B01D3/16B01J8/04B01J19/24C10G45/00C10G45/44C10G47/00C10G49/00C10G65/02
    • B01D3/16B01J8/0453B01J8/0492C10G49/002
    • 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.
    • 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。
    • 13. 发明授权
    • Fluid distribution across a particulate bed
    • 流体分布在颗粒床上
    • US5799877A
    • 1998-09-01
    • US582602
    • 1996-01-03
    • Ramesh GuptaJeffrey W. Frederick
    • Ramesh GuptaJeffrey W. Frederick
    • B01D3/00B01D3/20B01J8/02B01J8/04A62C5/02
    • B01D3/20B01D3/008B01J8/0278B01J8/0492
    • A means and method for spraying liquid and gas onto and across a particulate bed includes a horizontal liquid distribution tray disposed over the bed containing a plurality of gas and liquid spray distributors extending through the tray. The distributors include separate gas and liquid conduits or pipes having an entrance on top and an exit below, with the exits proximate each other underneath the tray. The conduits are coaxial with a portion of the gas conduit surrounded by the liquid conduit to define an annular space between them for the liquid to flow downwardly through. The gas flows down through the gas conduit, exiting as a gas core surrounded by the downflowing liquid. The gas expands and contacts the surrounding liquid to spray it on the matter below. A liquid spray generating device is located below the gas and liquid exit. Siphon caps automatically provide pulse flow of the liquid. Combining the siphon caps with orifices or slots in the liquid conduit below the siphon line automatically provides both continuous and pulse spray of the liquid onto the bed below.
    • 用于将液体和气体喷射到颗粒床上并穿过颗粒床的装置和方法包括设置在床上的水平液体分配盘,其包含延伸穿过托盘的多个气体和液体喷洒分配器。 分配器包括单独的气体和液体管道或管道,其具有在顶部的入口和下面的出口,出口在托盘下方彼此靠近。 导管与由液体管道包围的气体导管的一部分同轴,以在液体管道之间限定一个环形空间,以使液体向下流动。 气体向下流动通过气体管道,作为由下降流体液体围绕的气体芯出口。 气体膨胀并接触周围的液体,以将其喷洒在下面的物质上。 液体喷雾发生装置位于气体和液体出口下方。 虹吸帽自动提供液体的脉冲流。 将虹吸帽与虹吸管下方的液体管道中的孔或槽组合,自动提供液体在下面床上的连续和脉冲喷雾。