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1. 发明申请

US20110099891A1 HYDROPROCESSING FEEDSTOCK CONTAINING LIPID MATERIAL TO PRODUCE TRANSPORTATION FUEL 审中-公开
标题翻译：包含润滑材料的含水饲料生产运输燃料
公开(公告)号：US20110099891A1
公开(公告)日：2011-05-05
申请号：US12912103
申请日：2010-10-26
申请人： Bal K. Kaul , Patrick L. Hanks , Edward S. Ellis
发明人： Bal K. Kaul , Patrick L. Hanks , Edward S. Ellis
IPC分类号： C10L1/19
CPC分类号： C10G3/46 , C10G3/50 , C10G3/52 , C10G2300/1011 , C10G2300/405 , C10G2300/4081 , C10G2300/42 , C10L1/00 , Y02P30/20
摘要： This invention provides processes for producing fuel, particularly transportation fuel, from biological material, e.g., lipid material. One aspect of the invention involves hydroprocessing a feedstock in a hydroprocessing zone that is maintained at conditions that promote the efficiency of converting the lipid-containing feedstock into transportation fuel. Such conditions include one or more of maintaining CO content of the hydroprocessing zone at a predetermined amount and recycling or providing a hydrogen-containing gas to the hydroprocessing zone that has been treated to remove CO.
摘要翻译：本发明提供从生物材料例如脂质材料生产燃料，特别是运输燃料的方法。本发明的一个方面涉及在加氢处理区中加氢处理原料，该加氢处理区保持在促进将含脂质原料转化为运输燃料的效率的条件。这样的条件包括将加氢处理区的CO含量维持在预定量并将循环或提供含氢气体的一种或多种加到已经被处理以去除CO的加氢处理区。

2. 发明授权

US08853474B2 Hydroprocessing of biocomponent feedstocks with low purity hydrogen-containing streams 有权
标题翻译：生物组分原料与低纯度含氢物流的加氢处理
公开(公告)号：US08853474B2
公开(公告)日：2014-10-07
申请号：US12836771
申请日：2010-07-15
申请人： Patrick L. Hanks , Edward S. Ellis
发明人： Patrick L. Hanks , Edward S. Ellis
IPC分类号： C07C1/00 , C10G3/00 , C10L1/02 , C10G45/02 , C10G45/58
CPC分类号： C10G45/02 , C10G3/46 , C10G3/50 , C10G45/58 , C10G2300/1011 , C10G2300/207 , C10G2300/4018 , C10G2300/701 , C10G2400/04 , C10L1/026 , Y02E50/13 , Y02P30/20
摘要： A biocomponent feedstock can be hydroprocessed using a hydrogen-containing refinery as a source of hydrogen gas. A relatively low cost catalyst, such as a water gas shift catalyst and/or spent hydrotreating catalyst, can be used as a hydrogenation catalyst for the process. The hydroprocessing can allow for olefin saturation and/or deoxygenation of the biocomponent feed by using a relatively low value refinery stream, e.g., containing from about 20 mol % to about 60 mol % hydrogen.
摘要翻译：生物组分原料可以使用含氢精炼厂作为氢气源进行加氢处理。可以使用相对低成本的催化剂，例如水煤气变换催化剂和/或废加氢处理催化剂，作为该方法的氢化催化剂。加氢处理可以通过使用相对低价值的炼油厂物流（例如含有约20mol％至约60mol％的氢气）来允许生物组分进料的烯烃饱和和/或脱氧。

3. 发明申请

US20110155636A1 HYDROPROCESSING OF BIOCOMPONENT FEEDSTOCKS WITH LOW PURITY HYDROGEN-CONTAINING STREAMS 有权
标题翻译：具有低含氢含量的生物活性物料的水解
公开(公告)号：US20110155636A1
公开(公告)日：2011-06-30
申请号：US12836771
申请日：2010-07-15
申请人： Patrick L. Hanks , Edward S. Ellis
发明人： Patrick L. Hanks , Edward S. Ellis
IPC分类号： C10G17/00
CPC分类号： C10G45/02 , C10G3/46 , C10G3/50 , C10G45/58 , C10G2300/1011 , C10G2300/207 , C10G2300/4018 , C10G2300/701 , C10G2400/04 , C10L1/026 , Y02E50/13 , Y02P30/20
摘要： A biocomponent feedstock can be hydroprocessed using a hydrogen-containing refinery as a source of hydrogen gas. A relatively low cost catalyst, such as a water gas shift catalyst and/or spent hydrotreating catalyst, can be used as a hydrogenation catalyst for the process. The hydroprocessing can allow for olefin saturation and/or deoxygenation of the biocomponent feed by using a relatively low value refinery stream, e.g., containing from about 20 mol % to about 60 mol % hydrogen.
摘要翻译：生物组分原料可以使用含氢精炼厂作为氢气源进行加氢处理。可以使用相对低成本的催化剂，例如水煤气变换催化剂和/或废加氢处理催化剂，作为该方法的氢化催化剂。加氢处理可以通过使用相对低价值的炼油厂物流（例如含有约20mol％至约60mol％的氢气）来允许生物组分进料的烯烃饱和和/或脱氧。

4. 发明授权

US06723230B1 Regeneration of iron-based hydrogen sulfide sorbents 失效
标题翻译：铁基硫化氢吸附剂的再生
公开(公告)号：US06723230B1
公开(公告)日：2004-04-20
申请号：US09620796
申请日：2000-07-21
申请人： Jingguang G. Chen , Leo D. Brown , William C. Baird, Jr. , Gary B. McVicker , Edward S. Ellis , Michele S. Touvelle , Darryl P. Klein , David E. W. Vaughan
发明人： Jingguang G. Chen , Leo D. Brown , William C. Baird, Jr. , Gary B. McVicker , Edward S. Ellis , Michele S. Touvelle , Darryl P. Klein , David E. W. Vaughan
IPC分类号： C10G2500
CPC分类号： C10G45/10 , B01J20/0229 , B01J20/06 , B01J20/3204 , B01J20/3236 , B01J20/3433 , B01J20/3458 , B01J20/3466 , B01J23/89 , B01J23/94 , B01J38/06 , B01J2220/56 , C10G25/003 , C10G45/04 , C10G45/62 , C10G65/043
摘要： A process to regenerate iron-based hydrogen sulfide sorbents using steam. The steam is preferably mixed with hydrogen-containing gas and/or an inert gas, such as nitrogen. In a preferred embodiment, the sorbent is first exposed to the steam and then exposed to a hydrogen-containing gas at regeneration conditions.
摘要翻译：使用蒸汽再生铁基硫化氢吸附剂的方法。蒸汽优选与含氢气体和/或惰性气体如氮气混合。在优选的实施方案中，首先将吸附剂暴露于蒸汽，然后在再生条件下暴露于含氢气体。

5. 发明授权

US06623621B1 Control of flooding in a countercurrent flow reactor by use of temperature of liquid product stream 有权
标题翻译：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。

6. 发明授权

US5928498A Desulfurization and ring opening of petroleum streams 失效
公开(公告)号：US5928498A
公开(公告)日：1999-07-27
申请号：US917070
申请日：1997-08-22
申请人： Gary B. McVicker , James J. Schorfheide , William C. Baird, Jr. , Michele S. Touvelle , Michel Daage , Darryl P. Klein , Edward S. Ellis , David E. W. Vaughan , Jingguang G. Chen , Sylvain S. Hantzer
发明人： Gary B. McVicker , James J. Schorfheide , William C. Baird, Jr. , Michele S. Touvelle , Michel Daage , Darryl P. Klein , Edward S. Ellis , David E. W. Vaughan , Jingguang G. Chen , Sylvain S. Hantzer
IPC分类号： C10G25/00 , C10G45/10 , C10G45/62 , C10G65/04 , C10G65/08 , C10G45/00
CPC分类号： C10G25/003 , C10G45/10 , C10G45/62 , C10G65/04 , C10G65/043 , C10G65/08
摘要： A process for the hydrodesulfurization (HDS) of the multiple condensed ring heterocyclic organosulfur compounds and the ring opening of ring compounds present in petroleum and petrochemical streams. The process is conducted in the presence of hydrogen, one or more noble metal catalysts, and a hydrogen sulfide sorbent material.

7. 发明授权

US5770043A Integrated staged catalytic cracking and hydroprocessing process 失效
标题翻译：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
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： C10G7/00 , C10G11/05 , C10G11/18 , C10G35/04 , C10G45/00 , C10G49/04 , C10G69/00 , C10G69/04 , C10G69/06 , C10G69/08 , 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 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。

8. 发明授权

US06495029B1 Countercurrent desulfurization process for refractory organosulfur heterocycles 失效
$Countercurrent desulfurization process for refractory organosulfur heterocycles$
标题翻译：耐火有机硫杂环的逆流脱硫工艺
公开(公告)号：US06495029B1
公开(公告)日：2002-12-17
申请号：US09385644
申请日：1999-08-27
申请人： James J. Schorfheide , Edward S. Ellis , Michele S. Touvelle , Ramesh Gupta
发明人： James J. Schorfheide , Edward S. Ellis , Michele S. Touvelle , Ramesh Gupta
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。

9. 发明授权

US06224749B1 Liquid and vapor stage hydroprocessing using once-through hydrogen 失效
标题翻译：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。

10. 发明授权

US6153086A Combination cocurrent and countercurrent staged hydroprocessing with a vapor stage 失效
标题翻译：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。

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