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1. 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。

2. 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>

3. 发明申请

WO2010002545A3 THREE-PHASE HYDROPROCESSING WITHOUT A RECYCLE GAS COMPRESSOR 审中-公开
标题翻译：没有循环气体压缩机的三相氢化
公开(公告)号：WO2010002545A3
公开(公告)日：2010-02-25
申请号：PCT/US2009046534
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：通常，提供加氢处理烃原料（12）的方法，其不使用昂贵的循环气体压缩机，但仍然能够使用在基本上三相的加氢处理区（36）中提供的更有效的反应系统。该方法将基本上液相的加氢处理区域（20）与基本上三相的加氢处理区域（36）结合，使得两个反应区域（20,36）的氢气需求可以从外部来源提供，而没有将氢循环或再循环气体压缩机用于基本上三相的反应区（36）。

4. 发明申请

WO2009052017A3 HYDROCRACKING PROCESS 审中-公开
标题翻译：加氢裂化工艺
公开(公告)号：WO2009052017A3
公开(公告)日：2009-06-18
申请号：PCT/US2008079445
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：提供加氢裂化烃物流（12,112,212）的方法（10,110,210），其基本上采用液相连续加氢处理条件。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）基本上是液相连续系统。另一方面，该方法包括两阶段加氢裂化系统，其中加氢裂化区（113,124）（213,224）中的一个或两个基本上是液相连续反应系统。

5. 发明申请

WO2008014150A3 HYDROCRACKING PROCESS 审中-公开
标题翻译：水力过程
公开(公告)号：WO2008014150A3
公开(公告)日：2008-10-16
申请号：PCT/US2007073708
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： C10G47/02
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：一种催化加氢裂化方法，其中将包含烃原料（1），来自加氢裂化区（16）的液相流出物和维持液相连续系统的足够低氢浓度的氢气的液相料流进料到加氢处理区（4）以产生包含具有降低的硫和氮水平的烃的第一烃流。将具有降低的硫和氮水平的所得烃引入到具有足够低的氢浓度的加氢裂化区（13）中以保持液相连续系统以产生提供较低沸点烃的加氢裂化区流出物（16）。

6. 发明申请

WO2012047573A3 LIQUID PHASE HYDROPROCESSING WITH LOW PRESSURE DROP 审中-公开
标题翻译：低压液相液相加氢
公开(公告)号：WO2012047573A3
公开(公告)日：2012-08-09
申请号：PCT/US2011053205
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：用于在连续液相中加氢处理烃原料的方法使用包含平均不大于1.27mm（1/20英寸）且大于100nm的最大尺寸的丸剂的加氢处理催化剂以产生烃产物流。

7. 发明申请

WO2012051130A3 METHODS FOR PRODUCING DIESEL RANGE MATERIALS HAVING IMPROVED COLD FLOW PROPERTIES 审中-公开
标题翻译：生产具有改进的冷流动性能的柴油范围材料的方法
公开(公告)号：WO2012051130A3
公开(公告)日：2012-07-19
申请号：PCT/US2011055666
申请日：2011-10-11
申请人： UOP LLC , KOKAYEFF PETER , ABDO SUHEIL F
发明人： KOKAYEFF PETER , ABDO SUHEIL F
IPC分类号： C10G67/02 , C10G2/00 , C10G29/00 , C10L1/02 , C10L1/08
CPC分类号： C10G45/60 , C10G3/42 , C10G3/50 , C10G45/58 , C10G2300/1014 , C10G2300/1018 , C10G2300/1022 , C10G2300/1055 , C10G2300/202 , C10G2300/304 , C10G2300/70 , C10G2400/04 , C10L1/026 , C10L1/08 , Y02P30/20
摘要： Embodiments of a method for producing a diesel range material having improved cold flow properties are provided. In one embodiment, the method includes the steps of providing a waxy diesel range feedstock, producing an intermediary product stream containing a predetermined amount of oxygenated organocompounds from the waxy diesel range feedstock, and contacting the intermediary product stream with a dewaxing catalyst under process conditions at which the oxygenated organocompounds chemically interact with the dewaxing catalyst to convert a portion of the n-paraffins within the intermediary product stream to iso-paraffins while minimizing cracking of the diesel range material.
摘要翻译：提供了用于生产具有改进的低温流动性能的柴油范围材料的方法的实施例。在一个实施方案中，所述方法包括以下步骤：提供蜡质柴油范围给料，从含蜡柴油范围给料中产生含有预定量的含氧有机组分的中间产物料流，并使中间产物料流与脱蜡催化剂在其中含氧有机化合物与脱蜡催化剂化学相互作用以将中间产物流内的一部分正链烷烃转化为异链烷烃，同时使柴油范围材料的裂化最小化。

8. 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。

9. 发明申请

WO2009052025A2 HYDROCARBON CONVERSION PROCESS 审中-公开
标题翻译：石油转化过程
公开(公告)号：WO2009052025A2
公开(公告)日：2009-04-23
申请号：PCT/US2008079549
申请日：2008-10-10
申请人： UOP LLC , LEONARD LAURA E , KOKAYEFF PETER , SMITH MICHAEL R
发明人： LEONARD LAURA E , KOKAYEFF PETER , SMITH MICHAEL R
IPC分类号： C07C4/06 , B01J8/00 , C10G11/18
CPC分类号： C10G65/12
摘要： Methods of hydroprocessing hydrocarbon streams are provided that employ substantially liquid-phase hydroprocessing conditions. In one aspect, the method includes directing a hydrocarbonaceous feed stock (12) to a first substantially liquid-phase hydroprocessing zone (20) wherein an effluent (28) from the first substantially liquid-phase hydroprocessing zone (20) is directed to a second substantially liquid-phase hydroprocessing zone (34) generally undiluted with other hydrocarbon streams. In another aspect, the method recycles (14) a liquid portion of a liquid hydrocarbonaceous effluent (50) from the second substantially liquid-phase hydroprocessing zone (34), which preferably includes an amount of hydrogen dissolved therein, to the hydrocarbonaceous feed stock (12) so that the feed (18) to the first substantially liquid-phase hydroprocessing zone (20) has a relatively larger concentration of dissolved hydrogen relative to the hydrocarbonaceous feed stock (12).
摘要翻译：提供加氢处理烃流的方法，其采用基本上液相加氢处理条件。一方面，该方法包括将含烃原料（12）引导到第一基本上液相的加氢处理区（20），其中来自第一基本液相加氢处理区（20）的流出物（28）被引导至第二基本上液相加氢处理区（34）通常用其它烃流未稀释。另一方面，该方法从第二基本上液相加氢处理区（34）再循环（14）液体烃流出物（50）的液体部分，该第二基本液相加氢处理区（34）优选包含一定量的溶解在其中的氢气至烃类原料（ 12），使得到第一基本液相加氢处理区（20）的进料（18）相对于含烃原料（12）具有相对较大的溶解氢浓度。

10. 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。

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