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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。
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2.发明授权Control of flooding in a countercurrent flow reactor by use of temperature of liquid product stream 有权通过使用液体产物流的温度控制逆流流动反应器中的淹水公开(公告)号：US06623621B1
公开(公告)日：2003-09-23
申请号：US09457438
申请日：1999-12-07
申请人： Larry L. Iaccino , Russell D. Sellen , David C. Dankworth , Edward S. Ellis , Jeffrey W. Frederick , Ramesh Gupta , James J. Schorfheide , Louis A. Curcio, Jr.
发明人： Larry L. Iaccino , Russell D. Sellen , David C. Dankworth , Edward S. Ellis , Jeffrey W. Frederick , Ramesh Gupta , James J. Schorfheide , Louis A. Curcio, Jr.
IPC分类号： C10G4500
CPC分类号： C10G49/00 , C10G49/26 , Y10S585/921
摘要： A process for upgrading a liquid petroleum or chemical stream wherein said stream flows countercurrent to the flow of a treat gas, such as a hydrogen-containing gas, in at least one reaction zone. The temperature of at least a portion of the liquid stream in the reactor is used to control the flooding characteristics of the reactor.
摘要翻译： 一种用于升级液体石油或化学物流的方法，其中所述流与至少一个反应区中的处理气体（例如含氢气体）的流动逆流流动。 反应器中液态物流的至少一部分的温度用于控制反应器的淹水特性。
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公开(公告)号：US5770043A
公开(公告)日：1998-06-23
申请号：US697381
申请日：1996-08-23
IPC分类号： C10G7/00 , C10G11/05 , C10G11/18 , C10G35/04 , C10G45/00 , C10G49/04 , C10G69/00 , C10G69/04 , C10G69/06 , C10G69/08 , C10G51/02
摘要： 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.
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。
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4.发明授权公开(公告)号：US06495029B1
公开(公告)日：2002-12-17
申请号：US09385644
申请日：1999-08-27
IPC分类号： C10G4500
CPC分类号： C10G25/003 , C10G45/10 , C10G65/04 , C10G67/06
摘要： A process for the hydrodesulfurization (HDS) of the multiple condensed ring heterocyclic organosulfur compounds present in petroleum and chemical streams. The stream is passed through at least one reaction zone countercurrent to the flow of a hydrogen-containing treat gas, and through at least one sorbent zone. The reaction zone contains a bed of Group VIII metal-containing hydrodesulfurization catalyst and the sorbent zone contains a bed of hydrogen sulfide sorbent material.
摘要翻译： 石油和化学物流中存在的多重稠环杂环有机硫化合物的加氢脱硫（HDS）的方法。 该物流通过与含氢处理气体的流动逆流的至少一个反应区，并通过至少一个吸附区。 反应区含有含Ⅷ族金属的加氢脱硫催化剂床，吸附剂区含有硫化氢吸附剂材料床。
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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。
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6.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
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。
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公开(公告)号：US6123830A
公开(公告)日：2000-09-26
申请号：US222863
申请日：1998-12-30
申请人： Ramesh Gupta , Edward S. Ellis
发明人： Ramesh Gupta , Edward S. Ellis
CPC分类号： C10G69/04
摘要： Disclosed is a catalytic cracking process that includes more than one catalytic cracking reaction step. The process integrates catalytic cracking steps with hydroprocessing in order to maximize olefins production, distillate quality and octane level of the overall cracked product. Preferably, one hydroprocessing step is included between the cat cracking reaction steps, 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： 公开了包括多于一个催化裂化反应步骤的催化裂化方法。 该方法将催化裂化步骤与加氢处理相结合，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，在催化裂化反应步骤和一部分加氢处理产物（即石脑油和中间馏分馏分）之间包括一个加氢处理步骤，与裂化产物结合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。
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公开(公告)号：US6036844A
公开(公告)日：2000-03-14
申请号：US73413
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： C10G51/02 , C10G35/00 , C10G35/10 , C10G45/00 , C10G55/02 , C10G57/00 , C10G65/00 , C10G65/02 , C10G69/02
摘要： A three stage hydroprocessing process includes two liquid and one vapor reaction stages, with a hydrogen containing vapor effluent produced in both liquid stages. The second liquid stage vapor effluent comprises part of the first liquid stage feed and the first liquid stage vapor effluent is the feed for the vapor stage. At least a portion of the hydrogen for the first liquid stage and vapor stage reactions is respectively provided by the hydrogen in the second and first liquid stage vapor effluents.
摘要翻译： 三级加氢处理方法包括两个液相和一个蒸气反应阶段，在两个液相中产生含氢气的蒸气流出物。 第二液相蒸气流出物包括第一液相进料的一部分，第一液段蒸气流出物是用于蒸气阶段的进料。 用于第一液段和蒸气阶段反应的氢的至少一部分分别由第二和第一液相蒸气流出物中的氢提供。
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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
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。
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公开(公告)号：US5582711A
公开(公告)日：1996-12-10
申请号：US292625
申请日：1994-08-17
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。
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