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1. 发明申请

WO2010002903A2 MULTI-STAGED HYDROPROCESSING PROCESS AND APPARATUS 审中-公开
标题翻译：多阶段加氢处理和装置
公开(公告)号：WO2010002903A2
公开(公告)日：2010-01-07
申请号：PCT/US2009/049277
申请日：2009-06-30
申请人： UOP LLC , KOKAYEFF, Peter , LUEBKE, Charles, P. , PETRI, John, A. , MURTY, Vedula, K.
发明人： KOKAYEFF, Peter , LUEBKE, Charles, P. , PETRI, John, A. , MURTY, Vedula, K.
IPC分类号： C10G65/02 , C10G69/02
CPC分类号： C10G65/00 , C10G65/12
摘要： Methods and apparatuses of processing a hydrocarbonaceous feedstock flows are provided. In one aspect, the method includes providing two or more hydroprocessing stages disposed in sequence, each hydroprocessing stage having a hydroprocessing reaction zone with a hydrogen requirement and each stage in fluid communication with the preceding stage. A hydrogen source is provided substantially free of hydrogen from a hydrogen recycle compressor. The hydrocarbonaceous feedstock flow is separated into portions of fresh feed for each hydroprocessing stage, and the first portion of fresh feed. In an embodiment, only the first hydroprocessing stage is heated. The heated first portion of fresh feed is supplied with hydrogen in an amount satisfying substantially all of the hydrogen requirements of the hydroprocessing stages to a first hydroprocessing zone. The second portion of fresh feed is admixed with effluent from previous stage before entering a second stage.
摘要翻译：提供了处理含烃原料流的方法和装置。一方面，该方法包括提供依次设置的两个或多个加氢处理阶段，每个加氢处理阶段具有氢需求的加氢处理反应区，每个阶段与前一阶段流体连通。从氢循环压缩机中提供基本上不含氢气的氢源。将烃原料流分离成每个加氢处理阶段的新鲜进料部分和新鲜进料的第一部分。在一个实施方案中，仅加热第一加氢处理阶段。将加热的第一部分新鲜进料以基本上满足加氢处理阶段的所有氢气需求量的氢气供应给第一加氢处理区。新鲜饲料的第二部分与前一阶段的流出物混合，然后进入第二阶段。

2. 发明申请

WO2012050766A2 TWO-STAGE HYDROPROCESSING APPARATUS AND PROCESS WITH COMMON FRACTIONATION 审中-公开
标题翻译：两级加氢处理装置和常用分级法
公开(公告)号：WO2012050766A2
公开(公告)日：2012-04-19
申请号：PCT/US2011/052473
申请日：2011-09-21
申请人： UOP LLC , PETRI, John A. , MURTY, Vedula K. , KOKAYEFF, Peter
发明人： PETRI, John A. , MURTY, Vedula K. , KOKAYEFF, Peter
IPC分类号： C10G65/02 , C10L1/08
CPC分类号： C10L1/08 , C10G45/02 , C10G47/16 , C10G47/18 , C10G47/20 , C10G65/12 , C10G2300/1055 , C10G2300/202 , C10G2400/04
摘要： Two-stage hydroprocessmg uses a common dividing wall fractionator. Hydroprocessed effluents from both stages of hydroprocessmg are fed to opposite sides of the dividing wall.
摘要翻译：两阶段加氢处理使用普通的分隔壁分馏器。来自两个加氢处理阶段的加氢处理流出物被供给到分隔壁的相对侧。

3. 发明申请

WO2012047573A2 LIQUID PHASE HYDROPROCESSING WITH LOW PRESSURE DROP 审中-公开
标题翻译：低压液相加氢处理
公开(公告)号：WO2012047573A2
公开(公告)日：2012-04-12
申请号：PCT/US2011/053205
申请日：2011-09-26
申请人： UOP LLC , PETRI, John A. , KOKAYEFF, Peter , SECHRIST, Paul A.
发明人： PETRI, John A. , KOKAYEFF, Peter , SECHRIST, Paul A.
IPC分类号： C10G45/04 , C10G47/02
CPC分类号： C10G65/04 , C10G65/10 , C10G65/12
摘要： A process for hydroprocessing a hydrocarbonaceous feedstock in a continuous liquid phase utilizes a hydroprocessing catalyst comprising pills that have a largest dimension that averages no more than 1.27 mm (1/20 inch) and more than 100 nm to produce a hydrocarbonaceous product stream.
摘要翻译：在连续液相中加氢处理含烃原料的方法利用包含丸粒的加氢处理催化剂，所述丸粒具有平均不大于1.27mm（1/20英寸）和大于100nm至生产含烃产品流。

4. 发明申请

WO2010077395A1 PRODUCTION OF FUEL FROM RENEWABLE FEEDSTOCKS USING A FINISHING REACTOR 审中-公开
标题翻译：使用整理反应器从可再生的原料生产燃料
公开(公告)号：WO2010077395A1
公开(公告)日：2010-07-08
申请号：PCT/US2009/057273
申请日：2009-09-17
申请人： UOP LLC , KOKAYEFF, Peter , MARKER, Terry, L. , PETRI, John, A.
发明人： KOKAYEFF, Peter , MARKER, Terry, L. , PETRI, John, A.
IPC分类号： C10G69/04 , C10G69/06
CPC分类号： C10G3/50 , C10G3/46 , C10G45/58 , C10G65/043 , C10G2300/1014 , C10G2300/1018 , C10G2300/1022 , C10G2300/1037 , C10G2300/304 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/28 , C10L1/02 , Y02P30/20
摘要： A process has been developed for producing fuel from renewable feedstocks such as plant and animal oils and greases. The process involves treating a first portion of a renewable feedstock by hydrogenating and deoxygenating in a first reaction zone and a second portion of a renewable feedstock by hydrogenating and deoxygenating in a second reaction zone and treating the effluents in a finishing reaction zone to provide a diesel boiling point range fuel hydrocarbon product. If desired, the hydrocarbon product can be isomerized to improve cold flow properties. A portion of the hydrocarbon product is recycled to the first reaction zone to increase the hydrogen solubility of the reaction mixture.
摘要翻译：已经开发了用于从可再生原料如植物油和动物油和油脂生产燃料的方法。该方法包括通过在第一反应区和第二部分可再生原料中的氢化和脱氧来处理可再生原料的第一部分，通过在第二反应区中进行氢化和脱氧并在整理反应区中处理废水以提供柴油沸点范围燃料烃产品。如果需要，烃产物可被异构化以改善冷流动性能。一部分烃产物再循环到第一反应区以提高反应混合物的氢溶解度。

5. 发明申请

WO2010002545A2 THREE-PHASE HYDROPROCESSING WITHOUT A RECYCLE GAS COMPRESSOR 审中-公开
标题翻译：没有回收气体压缩机的三相加氢处理
公开(公告)号：WO2010002545A2
公开(公告)日：2010-01-07
申请号：PCT/US2009/046534
申请日：2009-06-08
申请人： UOP LLC , KOKAYEFF, Peter , PETRI, John, A.
发明人： KOKAYEFF, Peter , PETRI, John, A.
IPC分类号： C10G65/14 , C10G45/02
CPC分类号： C10G65/02
摘要： In general, methods of hydroprocessing a hydrocarbonaceous feed stock (12) are provided that do not use a costly recycle gas compressor, but are still able to use the more efficient reaction systems provided in a substantially three-phase hydroprocessing zone (36). The method combines a substantially liquid-phase hydroprocessing zone (20) with the substantially three-phase hydroprocessing zone (36) in a manner so that the hydrogen requirements for both reaction zones (20, 36) can be provided from an external source thereto without the use of a hydrogen recycle or recycle gas compressor to the substantially three-phase reaction zone (36).
摘要翻译：一般而言，提供了加氢处理含烃原料（12）的方法，其不使用昂贵的再循环气体压缩机，但仍能够使用基本上三维地提供的更有效的反应体系，相加氢处理区（36）。该方法将基本上液相的加氢处理区（20）与基本上三相加氢处理区（36）组合以使得两个反应区（20,36）的氢需求可以从外部源提供到其中而无需氢再循环或再循环气体压缩机用于基本上三相的反应区（36）。

6. 发明申请

WO2009052004A1 HYDROISOMERIZATION PROCESS 审中-公开
标题翻译：水解过程
公开(公告)号：WO2009052004A1
公开(公告)日：2009-04-23
申请号：PCT/US2008/079305
申请日：2008-10-09
申请人： UOP LLC , KOKAYEFF, Peter , LEONARD, Laura, E.
发明人： KOKAYEFF, Peter , LEONARD, Laura, E.
IPC分类号： C10G65/12 , C10G55/06 , C07C5/03
CPC分类号： C10G45/58 , C10G2400/04
摘要： A process (10) is provided for improving the cold flow properties of a hydrocarbon stream (14) employing a substantially liquid-phase continuous hydroisomerization zone (12) where the reaction zone has a substantially constant level of dissolved hydrogen throughout without the addition of additional hydrogen external to the reaction zone.
摘要翻译：提供了一种方法（10），用于改进使用基本上液相的连续加氢异构化区（12）的烃流（14）的冷流性质，其中反应区具有基本上恒定的溶解氢水平，而不添加额外的反应区外部的氢。

7. 发明申请

WO2008014150A2 HYDROCRACKING PROCESS 审中-公开
标题翻译：加氢裂化工艺
公开(公告)号：WO2008014150A2
公开(公告)日：2008-01-31
申请号：PCT/US2007/073708
申请日：2007-07-17
申请人： UOP LLC , LEONARD, Laura E. , KOKAYEFF, Peter
发明人： LEONARD, Laura E. , KOKAYEFF, Peter
IPC分类号： C10G11/00
CPC分类号： C10G65/12 , C10G2300/1011 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/207 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4081 , Y02P30/20
摘要： A catalytic hydrocracking process wherein a liquid phase stream comprising a hydrocarbonaceous feedstock (1), a liquid phase effluent from a hydrocracking zone (16), and hydrogen in a sufficiently low hydrogen concentration to maintain a liquid phase continuous system is fed into a hydrotreating zone (4) to produce a first hydrocarbonaceous stream comprising hydrocarbons having a reduced level of sulfur and nitrogen. The resulting hydrocarbons having a reduced level of sulfur and nitrogen are introduced into a hydrocracking zone (13) with a sufficiently low hydrogen concentration to maintain a liquid phase continuous system to produce a hydrocracking zone effluent (16) which provides lower boiling range hydrocarbons.
摘要翻译：（1），来自加氢裂化区（16）的液相流出物和氢气浓度足够低的氢气以保持液相的催化加氢裂化方法将连续体系加入加氢处理区（4）以产生包含具有降低的硫和氮含量的烃的第一含烃流。将所得具有降低的硫和氮含量的烃引入具有足够低氢浓度的加氢裂化区（13）中以保持液相连续体系以产生提供低沸程烃的加氢裂化区流出物（16） / p>

8. 发明申请

WO2009052017A2 HYDROCRACKING PROCESS 审中-公开
标题翻译：水力过程
公开(公告)号：WO2009052017A2
公开(公告)日：2009-04-23
申请号：PCT/US2008/079445
申请日：2008-10-10
申请人： UOP LLC , KOKAYEFF, Peter , DZIABALA, Bart , LEONARD, Laura E.
发明人： KOKAYEFF, Peter , DZIABALA, Bart , LEONARD, Laura E.
IPC分类号： C10G55/04 , C10G55/06
CPC分类号： C10G65/12 , C10G2300/42
摘要： Methods (10, 110, 210) of hydrocracking hydrocarbon streams (12, 112, 212) are provided that employ substantially liquid-phase continuous hydroprocessing conditions. In one aspect, the method includes a separate hydrotreating and hydrocracking system where the hydrocracking zone (24) is a substantially liquid-phase continuous system. In another aspect, the method includes a two stage hydrocracking system where one or both of the hydrocracking zones (113, 124) (213, 224) are a substantially liquid-phase continuous reaction system.
摘要翻译：提供了加氢裂化烃流（12,112,212）的方法（10,110,210），其采用基本上液相连续的加氢处理条件。一方面，该方法包括单独的加氢处理和加氢裂化系统，其中加氢裂化区（24）是基本上液相连续的系统。另一方面，该方法包括两阶段加氢裂化系统，其中一个或两个加氢裂化区（113,124）（213,224）是基本上液相的连续反应系统。

9. 发明申请

WO2009039347A1 PRODUCTION OF DIESEL FUEL FROM BIORENEWABLE FEEDSTOCKS WITH LOWER HYDROGEN CONSUMPTION 审中-公开
标题翻译：从具有较低氢消耗量的可再生原料生产柴油燃料
公开(公告)号：WO2009039347A1
公开(公告)日：2009-03-26
申请号：PCT/US2008/076972
申请日：2008-09-19
申请人： UOP LLC , ENI, S.p.A. , MARKER, Terry L. , KOKAYEFF, Peter , ABDO, Suheil F. , BALDIRAGHI, Franco , SABATINO, Luigina M. F.
发明人： MARKER, Terry L. , KOKAYEFF, Peter , ABDO, Suheil F. , BALDIRAGHI, Franco , SABATINO, Luigina M. F.
IPC分类号： C10L1/08 , C10L1/18 , C10G3/00 , C07C5/22 , C10G73/44
CPC分类号： C10L1/08 , C01B3/16 , C01B3/50 , C01B2203/0415 , C01B2203/043 , C01B2203/0455 , C01B2203/0475 , C01B2203/0485 , C01B2203/148 , C10G3/46 , C10G3/50 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/202 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/28 , Y02E50/13 , Y02P30/20
摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant and animal fats and oils. The process involves treating a renewable feedstock by hydrogenating and deoxygenating i.e. decarboxylating, decarbonylating, and hydrodeoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel. A sulfur containing component is added to drive the conversion preferentially through carbonylation and carbonylation with reduced hydrodeoxygenation. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties.
摘要翻译：已经开发了用于从可再生原料如植物和动物脂肪和油生产柴油沸点燃料的方法。该方法包括通过氢化和脱氧处理可再生原料，即脱羧，脱羰和加氢脱氧以提供可用作柴油沸程燃料的烃馏分。加入含硫组分以优先通过羰基化和羰基化优化以减少加氢脱氧。如果需要，烃馏分可以被异构化以改善冷流动性能。

10. 发明申请

WO2009039335A1 PRODUCTION OF DIESEL FUEL FROM RENEWABLE FEEDSTOCKS WITH REDUCED HYDROGEN CONSUMPTION 审中-公开
标题翻译：从可再生能源生产柴油燃料，减少氢消耗
公开(公告)号：WO2009039335A1
公开(公告)日：2009-03-26
申请号：PCT/US2008/076947
申请日：2008-09-19
申请人： UOP LLC , ENI, S.p.A. , MARKER, Terry, L. , KOKAYEFF, Peter , FARACI, Giovanni , BALDIRAGHI, Franco
发明人： MARKER, Terry, L. , KOKAYEFF, Peter , FARACI, Giovanni , BALDIRAGHI, Franco
IPC分类号： C10L1/08 , C10L1/18 , C10G3/00 , C07C5/22 , C10G73/44
CPC分类号： C10L1/08 , C01B3/16 , C01B3/50 , C01B2203/0415 , C01B2203/043 , C01B2203/0455 , C01B2203/0475 , C01B2203/0485 , C01B2203/148 , C10G3/46 , C10G3/52 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/28 , Y02E50/13 , Y02P30/20
摘要： A process has been developed for producing diesel boiling range fuel from renewable feedstocks such as plant and animal fats and oils. The process involves treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel boiling range fuel. Water is added to the deoxygenation reaction to drive carbon monoxide and water to react to form hydrogen and carbon dioxide. The hydrogen is then consumed by the reactions. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties.
摘要翻译：已经开发了用于从可再生原料如植物和动物脂肪和油生产柴油沸点燃料的方法。该方法包括通过氢化和脱氧处理可再生原料以提供可用作柴油沸程燃料的烃馏分。将水加入脱氧反应中以驱使一氧化碳和水反应形成氢气和二氧化碳。然后氢被反应消耗。如果需要，烃馏分可以被异构化以改善冷流动性能。

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