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1. 发明申请

US20100116712A1 COMBINATION OF MILD HYDROTREATING AND HYDROCRACKING FOR MAKING LOW SULFUR DIESEL AND HIGH OCTANE NAPHTHA 有权
标题翻译：用于制造低硫柴油和高OCTONE NAPHTHA的混合加氢和水解混合
公开(公告)号：US20100116712A1
公开(公告)日：2010-05-13
申请号：US12268048
申请日：2008-11-10
申请人： Bart Dziabala , Vasant P. Thakkar , Suheil F. Abdo
发明人： Bart Dziabala , Vasant P. Thakkar , Suheil F. Abdo
IPC分类号： C10G45/00
CPC分类号： C10G65/12 , C10G2300/1037 , C10G2300/202 , C10G2300/301 , C10G2300/305 , C10G2300/4018 , C10G2400/02 , C10G2400/04
摘要： Methods are disclosed for the hydrotreating and hydrocracking of highly aromatic distillate feeds such as light cycle oil (LCO) to produce ultra low sulfur gasoline and diesel fuel. Optimization of hydrotreater severity improves the octane quality of the gasoline or naphtha fraction. In particular, the operation of the hydrotreater at reduced severity to allow at least about 20 ppm by weight of organic nitrogen into the hydrocracker feed is shown to lead to these important benefits. Post-treating of the hydrocracker effluent over an additional hydrotreating catalyst bed may be desired to meet specifications for ultra low sulfur fuel components.
摘要翻译：公开了用于加氢处理和加氢裂解高芳烃馏出物如轻循环油（LCO）以产生超低硫汽油和柴油燃料的方法。加氢处理剂严重性的优化提高了汽油或石脑油馏分的辛烷值。特别地，加氢处理器以较低的苛刻度运行，使至少约20ppm重量的有机氮进入加氢裂化器进料显示出这些重要的益处。在另外的加氢处理催化剂床上后处理加氢裂化器流出物可能需要满足超低硫燃料组分的规格。

2. 发明申请

US20090193709A1 Production of Diesel Fuel from Biorenewable Feedstocks with Lower Hydrogen Consumption 有权
标题翻译：生产可燃低原料的生物可利用原料柴油
公开(公告)号：US20090193709A1
公开(公告)日：2009-08-06
申请号：US12193120
申请日：2008-08-18
申请人： Terry L. Marker , Peter Kokayeff , Suheil F. Abdo , Franco Baldiraghi , Luigina M.F. Sabatino
发明人： Terry L. Marker , Peter Kokayeff , Suheil F. Abdo , Franco Baldiraghi , Luigina M.F. Sabatino
IPC分类号： C10L1/18
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。

3. 发明授权

US07097347B2 Static mixer and process for mixing at least two fluids 失效
公开(公告)号：US07097347B2
公开(公告)日：2006-08-29
申请号：US10717336
申请日：2003-11-19
申请人： Kurt M. Vanden Bussche , Suheil F. Abdo , Volker Hessel , Holger Löwe , Steffen Hardt
发明人： Kurt M. Vanden Bussche , Suheil F. Abdo , Volker Hessel , Holger Löwe , Steffen Hardt
IPC分类号： B01F5/04 , B01F13/00 , B81B1/00
CPC分类号： B01F5/04 , B01F5/0604 , B01F5/064 , B01F13/0064 , B01F13/0066 , B01F13/0094 , B01F2005/0014 , B01F2005/002 , B01J19/0093 , B01J19/249 , B01J2219/00835 , B01J2219/247 , B01J2219/2474 , B01J2219/2488 , B01J2219/2493
摘要： A novel mixing apparatus and process for mixing at least two fluids are disclosed. Excellent mixing and superior pressure drop characteristics are achieved in a device comprising at least two supply channels to feed a mixing chamber and create a vortex. The alignment of the supply channels is such that fluids are introduced into the chamber at both tangential and radial directions. In the case of gas/liquid mixing, particularly advantageous is the injection of the liquid stream tangentially and the gas stream radially. When two liquid streams are mixed, it is desirable to distribute them into fine, interdigitated channels prior to introduction into a supply channel and finally into the chamber. The mixed stream is generally withdrawn from the center of the swirling vortex and in a direction perpendicular to the plane of the vortex.

4. 发明授权

US06863867B2 Apparatus for mixing and reacting at least two fluids 失效
标题翻译：用于混合和反应至少两种流体的装置
公开(公告)号：US06863867B2
公开(公告)日：2005-03-08
申请号：US09850439
申请日：2001-05-07
申请人： Kurt M. Vanden Bussche , Suheil F. Abdo , Volker Hessel , Holger Löwe , Steffen Hardt
发明人： Kurt M. Vanden Bussche , Suheil F. Abdo , Volker Hessel , Holger Löwe , Steffen Hardt
IPC分类号： B01F5/00 , B01F5/04 , B01F5/06 , B01F13/00 , B01J19/00 , B01J19/24 , B01J10/00
CPC分类号： B01F13/0066 , B01F5/04 , B01F5/0604 , B01F5/064 , B01F13/0064 , B01F13/0094 , B01F2005/0014 , B01F2005/002 , B01J19/0093 , B01J19/249 , B01J2219/00835 , B01J2219/2453 , B01J2219/2456 , B01J2219/247 , B01J2219/2474 , B01J2219/2488 , B01J2219/2493
摘要： A novel apparatus for mixing and reacting at least two fluids are disclosed. Excellent mixing and superior pressure drop characteristics are achieved in a device comprising at least two supply channels to feed a mixing chamber and create a vortex. The alignment of the supply channels is such that fluids are introduced into the chamber at both tangential and radial directions. In the case of gas/liquid mixing, particularly advantageous is the injection of the liquid stream tangentially and the gas stream radially. Reaction of the fluids can take place within the mixing chamber or in a separate reactor in fluid communication with the mixing chamber outlet. The mixer/reactor apparatus is especially useful for reactions where rapid diffusion is critical.
摘要翻译：公开了用于混合和反应至少两种流体的新型装置。在包括至少两个供应通道的装置中实现优异的混合和优异的压降特性以供入混合室并产生涡流。供应通道的对准使得流体在切向和径向方向上被引入腔室。在气/液混合的情况下，特别有利的是液体流切向注入和气流径向喷射。流体的反应可以在混合室内或在与混合室出口流体连通的单独的反应器中进行。混合器/反应器装置对于快速扩散至关重要的反应特别有用。

5. 发明授权

US06409939B1 Method for producing a hydrogen-rich fuel stream 失效
标题翻译：富氢燃料流的制造方法
公开(公告)号：US06409939B1
公开(公告)日：2002-06-25
申请号：US09583618
申请日：2000-05-31
申请人： Suheil F. Abdo , Cynthia A. DeBoy , Geralyn F. Schroeder
发明人： Suheil F. Abdo , Cynthia A. DeBoy , Geralyn F. Schroeder
IPC分类号： C07C102
CPC分类号： C01B3/583 , B01J23/462 , C01B2203/044 , C01B2203/047
摘要： Disclosed is a hydrogen generation process for use with fuel cells which includes a preferential oxidation step to reduce the concentration of carbon monoxide. The preferential oxidation step includes contacting a fuel stream comprising hydrogen and carbon monoxide in the presence of an oxygen at a preferential oxidation temperature of between about 70° and about 160° C. with preferential oxidation catalyst for reducing the concentration of carbon monoxide to produce a treated fuel gas stream comprising less than about 50 ppm-vol carbon monoxide. The preferential oxidation catalyst comprises ruthenium metal dispersed on a shaped alumina carrier, wherein at least 60 percent of the ruthenium metal is present in a band extending from the surface towards the center and having a width of about 50 percent of the distance from the surface to the center of the shaped alumina carrier. Superior performance at low preferential oxidation temperatures below 130° C. was observed when the band comprised 50 percent of the alumina carrier and contained at least 60 percent of the ruthenium metal. The preferential oxidation catalyst may be employed to reduce carbon monoxide in fuel gas streams supplied to fuel cells wherein carbon monoxide will poison the active noble metal membrane and higher preferential oxidation temperatures may reduce the hydrogen content of the gas stream.
摘要翻译：公开了一种用于燃料电池的氢气生成方法，其包括优先氧化步骤以降低一氧化碳的浓度。优选氧化步骤包括在优选氧化温度为约70°至约160℃之间的氧气存在下使包含氢气和一氧化碳的燃料流与优先氧化催化剂接触，以降低一氧化碳的浓度，从而产生处理的燃料气流包含小于约50ppm体积的一氧化碳。优选的氧化催化剂包括分散在成形氧化铝载体上的钌金属，其中至少60％的钌金属存在于从表面朝向中心延伸的带中，其宽度为从表面到成型氧化铝载体的中心。当带包含50％的氧化铝载体并且含有至少60％的钌金属时，观察到在低于130℃的低优先氧化温度下的优异性能。可以使用优先氧化催化剂来减少供应到燃料电池的燃料气流中的一氧化碳，其中一氧化碳将中毒活性贵金属膜，并且较高的优先氧化温度可降低气流的氢含量。

6. 发明授权

US5906731A Process for hydroprocessing hydrocarbons 失效
标题翻译：加氢处理烃的方法
公开(公告)号：US5906731A
公开(公告)日：1999-05-25
申请号：US901354
申请日：1997-07-28
申请人： Suheil F. Abdo , Howard D. Simpson , Pradeep S. Iyer
发明人： Suheil F. Abdo , Howard D. Simpson , Pradeep S. Iyer
IPC分类号： B01J23/85 , B01J23/883 , B01J27/188 , B01J27/19 , B01J37/02 , C10G45/08 , C10G49/04 , B01J21/04
CPC分类号： C10G45/08 , B01J23/85 , B01J23/883 , B01J27/188 , B01J27/19 , B01J37/0205 , C10G49/04
摘要： A hydroprocess catalyzed by a catalyst composition comprising a porous refractory oxide, a molybdenum component, a phosphorus component and an underbedded nickel component, the composition characterized by a Raman spectrum comprising at least one Raman band in each of the regions of (1) about 240 cm.sup.-1 to about 250 cm.sup.-1, and (2) about 595 cm.sup.-1 to about 605 cm.sup.-1. The catalyst is prepared by sequential incorporation of the nickel metal followed by the additional catalytic promoters including a molybdenum component and a phosphorus component.
摘要翻译：该催化剂组合物由包含多孔难熔氧化物，钼组分，磷组分和嵌入镍组分的催化剂组合物催化的加氢处理，该组合物的特征在于拉曼光谱，其包括在（1）的每个区域中的至少一个拉曼带，约240 cm-1至约250cm -1，（2）约595cm -1至约605cm -1。催化剂是通过依次掺入镍金属，然后是另外的催化促进剂，包括钼组分和磷组分来制备的。

7. 发明授权

US5036033A Alkylation catalyst and processes for preparing 失效
标题翻译：烷基化催化剂及其制备方法
公开(公告)号：US5036033A
公开(公告)日：1991-07-30
申请号：US358432
申请日：1989-05-26
申请人： Martin West , Suheil F. Abdo
发明人： Martin West , Suheil F. Abdo
IPC分类号： B01J29/08 , C07B61/00 , C07C2/66 , C07C15/073 , C07C15/085
CPC分类号： B01J29/084 , C07C2/66 , C07C2529/08 , Y02P20/52
摘要： A composition useful for catalyzing alkylation and transalkylation reactions comprises a molecular sieve having alkylation and/or transalkylation activity, an inorganic refractory oxide component and greater than about 250 ppmw ammonium ions, calculated as (NH.sub.4).sub.2 O on a volatiles-free basis. Such a catalyst has been found to be highly selective for the production of cumene in an intergrated process in which benzene is alkylated with propylene and transalkylated with diisopropylbenzene. The catalyst can also be used to selectively produce ethylbenzene via an intergrated process in which benzene is alkylated with ethylene and transalkylated with diethylbenzene.
摘要翻译：用于催化烷基化和烷基转移反应的组合物包含具有烷基化和/或烷基转移活性的分子筛，无机难熔氧化物组分和大于约250ppmw的铵离子，以无挥发物计算为（NH 4）2。已经发现，这种催化剂对于在丙烷中用苯烷基化并用二异丙基苯烷基化的整体方法中生产枯烯是高选择性的。催化剂也可用于通过其中苯与乙烯烷基化并用二乙基苯烷基化的整合方法选择性地生产乙苯。

8. 发明授权

US4923836A Ni/Cu absorbent/catalyst for desulfurization and isomerization of N-paraffins 失效
标题翻译：用于脱硫和N-链烷烃异构化的Ni / Cu吸收剂/催化剂
公开(公告)号：US4923836A
公开(公告)日：1990-05-08
申请号：US413396
申请日：1989-09-27
申请人： Peter Kokayeff , Suheil F. Abdo
发明人： Peter Kokayeff , Suheil F. Abdo
IPC分类号： B01J29/072 , B01J29/08 , B01J29/14 , B01J29/76 , C10G47/20
CPC分类号： C10G47/20 , B01J29/072 , B01J29/084 , B01J29/146 , B01J29/76 , B01J2229/16
摘要： A dual-function catalyst containing both Group VIII and Group IB metals which is effective for simultaneously absorbing sulfur and isomerizing a hydrocarbon feedstock.
摘要翻译：含有同时吸收硫和异构化烃原料的VIII族和IB族金属的双功能催化剂。

9. 发明授权

US4871445A Hydrocarbon conversion 失效
标题翻译：烃转化
公开(公告)号：US4871445A
公开(公告)日：1989-10-03
申请号：US243709
申请日：1988-09-13
申请人： Jeffery W. Koepke , Suheil F. Abdo
发明人： Jeffery W. Koepke , Suheil F. Abdo
IPC分类号： B01J23/20 , B01J23/85 , B01J29/04 , B01J29/076 , C10G47/16
CPC分类号： C10G47/16 , B01J23/20 , B01J23/85 , B01J29/04 , B01J29/076
摘要： A hydrocracking process, of especial use in producing high octane gasoline from gas oils and the like, comprises contacting a gas oil or other hydrocarbon feedstock under hydrocracking conditions with a novel catalyst comprising at least one niobium component and a support material comprising a cracking component.
摘要翻译：特别用于从瓦斯油等生产高辛烷值汽油的加氢裂化方法包括在加氢裂化条件下将瓦斯油或其它烃原料与包含至少一种铌组分的新催化剂和包含裂化组分的载体材料接触。

10. 发明授权

US4844792A Hydroprocessing with a specific pore sized catalyst containing non-hydrolyzable halogen 失效
标题翻译：用含有不可水解卤素的特定孔径的催化剂进行加氢处理
公开(公告)号：US4844792A
公开(公告)日：1989-07-04
申请号：US921350
申请日：1986-10-20
申请人： Suheil F. Abdo , Eric L. Moorehead
发明人： Suheil F. Abdo , Eric L. Moorehead
IPC分类号： B01J29/70 , C10G49/08
CPC分类号： B01J29/064 , B01J29/076 , B01J29/166 , B01J35/1061 , C10G49/08 , B01J2229/42
摘要： A catalyst containing a non-hydrolyzable halogen component and an amorphous refractory oxide having controlled pore sizes is employed to hydroprocess a hydrocarbon oil.
摘要翻译：使用含有不可水解的卤素组分和具有可控孔径的无定形耐火氧化物的催化剂来加氢烃油。

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