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1. 发明授权

US5219814A Catalyst for light cycle oil upgrading 失效
标题翻译：催化剂用于轻循环油升级
公开(公告)号：US5219814A
公开(公告)日：1993-06-15
申请号：US629952
申请日：1990-12-19
申请人： Garry W. Kirker , Michael E. Landis , Daria N. Lissy , Sadi Mizrahi , Michael S. Sarli , Stuart S. Shih
发明人： Garry W. Kirker , Michael E. Landis , Daria N. Lissy , Sadi Mizrahi , Michael S. Sarli , Stuart S. Shih
IPC分类号： B01J29/16 , C10G47/20
CPC分类号： C10G47/20 , B01J29/166
摘要： A moderate pressure hydrocracking process in which a highly aromatic, substantially dealkylated feedstock is processed to high octane gasoline and low sulfur distillate by hydrocracking over a catalyst, preferably comprising ultrastable Y and a Group VIII metal and a Group VI metal, in which the amount of the Group VIII metal content is incorporated at specified proportion into the framework aluminum content of the ultrastable Y component. The feedstock which is preferably a light cycle oil has an aromatic content of at least 50, usually at least 60 percent, and an API gravity not more than 25. The hydrocracking typically operates at 400-1000 psig at moderate to high conversion levels to maximize the production of monocyclic aromatics which provide the requisite octane value to the product gasoline. The distillate products from the hydrocracker are reduced in their sulfur content.
摘要翻译：中等压力加氢裂化方法，其中高度芳香的，基本上脱烷基化的原料通过催化剂上的加氢裂化加工成高辛烷值汽油和低硫馏分，优选包括超稳定Y和VIII族金属和第VI族金属，其中第VIII族金属含量以规定比例掺入超稳Y组分的骨架铝含量中。优选轻循环油的原料具有至少50，通常至少60％的芳烃含量，API重力不超过25.加氢裂化通常在中等至高转化率的400-1000psig下操作，以使生产提供产品汽油必需辛烷值的单环芳烃。来自加氢裂化器的馏出物的硫含量降低。

2. 发明授权

US5000839A Hydrocracking process for producing a high density jet fuel 失效
标题翻译：用于生产高密度喷气燃料的加氢裂化工艺
公开(公告)号：US5000839A
公开(公告)日：1991-03-19
申请号：US479789
申请日：1990-02-14
申请人： Garry W. Kirker , Sadi Mizrahi , Stuart S. Shih
发明人： Garry W. Kirker , Sadi Mizrahi , Stuart S. Shih
IPC分类号： B01J29/14 , B01J29/16 , B01J29/70 , B01J29/74 , B01J29/80 , C10G65/10 , C10G65/12
CPC分类号： B01J29/7038 , B01J29/146 , B01J29/166 , B01J29/7088 , B01J29/7415 , B01J29/7476 , B01J29/80 , C10G65/10 , C10G65/12 , B01J2229/16 , B01J2229/26 , B01J2229/42
摘要： A two-stage hydrocracking process for producing high density jet fuel from an aromatic feedstock using a synthetic zeolite catalyst. The feedstock is hydrotreated in the first stage to convert heteroatoms. After removal of sulfur and nitrogen compounds, the feed is directed to a hydrocracker where it contacted with MCM-22 zeolite.
摘要翻译：使用合成沸石催化剂从芳族原料生产高密度喷气燃料的两阶段加氢裂化方法。原料在第一阶段加氢处理以转化杂原子。在除去硫和氮化合物之后，将进料引导至与MCM-22沸石接触的加氢裂化器。

3. 发明授权

US4968402A Process for upgrading hydrocarbons 失效
标题翻译：碳氢化合物升级方法
公开(公告)号：US4968402A
公开(公告)日：1990-11-06
申请号：US479799
申请日：1990-02-14
申请人： Garry W. Kirker , Stuart S. Shih
发明人： Garry W. Kirker , Stuart S. Shih
IPC分类号： B01J29/14 , B01J29/16 , B01J29/70 , B01J29/74 , B01J29/80 , C10G65/10 , C10G65/12
CPC分类号： B01J29/7038 , B01J29/146 , B01J29/166 , B01J29/7088 , B01J29/7415 , B01J29/7876 , B01J29/80 , B01J29/86 , C10G65/10 , C10G65/12 , B01J2229/16 , B01J2229/26 , B01J2229/42
摘要： A one stage catalytic process for producing high octane gasoline from a highly aromatic hydrocarbon feedstock. The process comprises hydrocracking the feedstock with an NiW/MCM-22 zeolite catalyst. Fractionation of the hydrocracker effluent provides a high octane gasoline fraction.
摘要翻译：用于从高度芳族烃原料生产高辛烷值汽油的一级催化方法。该方法包括用NiW / MCM-22沸石催化剂加氢裂化原料。加氢裂化器流出物的分馏提供高辛烷值汽油馏分。

4. 发明授权

US09719034B2 Co-production of lubricants and distillate fuels 有权
公开(公告)号：US09719034B2
公开(公告)日：2017-08-01
申请号：US14546565
申请日：2014-11-18
申请人： Stuart S. Shih , Gary P. Schleicher , Michael B. Carroll , Timothy L. Hilbert , Stephen J. McCarthy , William J. Novak
发明人： Stuart S. Shih , Gary P. Schleicher , Michael B. Carroll , Timothy L. Hilbert , Stephen J. McCarthy , William J. Novak
IPC分类号： C10G45/64 , C10G69/02 , C10M103/06 , B01J35/10 , C10G65/04 , C10G65/12 , B01J23/883 , B01J23/888 , B01J29/78
CPC分类号： C10G69/02 , B01J23/883 , B01J23/888 , B01J29/78 , B01J29/7846 , B01J29/7861 , B01J29/7884 , B01J29/7892 , B01J35/1014 , B01J2229/186 , B01J2229/20 , B01J2229/42 , C10G65/043 , C10G65/12 , C10G2300/1048 , C10G2300/203 , C10G2300/301 , C10G2300/302 , C10G2300/307 , C10G2400/04 , C10G2400/10 , C10M103/06
摘要： Methods are provided for processing a gas oil boiling range feedstock, such as a vacuum gas oil, in a single reaction stage and/or without performing intermediate separations. The methods are suitable for forming lubricants and distillate fuels while reducing or minimizing the production of lower boiling products such as naphtha and light ends. The methods can provide desirable yields of distillate fuels and lubricant base oils without requiring separate catalyst beds or stages for dewaxing and hydrocracking. The methods are based in part on use of a dewaxing catalyst that is tolerant of sour processing environments while still providing desirable levels of activity for both feed conversion and feed isomerization.

5. 发明授权

US09487714B2 Hydrocracking process selective for improved distillate and improved lube yield and properties 有权
公开(公告)号：US09487714B2
公开(公告)日：2016-11-08
申请号：US14011061
申请日：2013-08-27
申请人： William J. Novak , Robert Allen Bradway , Stuart S. Shih , Timothy Lee Hilbert , Michel Daage
发明人： William J. Novak , Robert Allen Bradway , Stuart S. Shih , Timothy Lee Hilbert , Michel Daage
IPC分类号： C10G47/18 , C10G49/04 , C10G65/10 , C10G65/12
CPC分类号： C10G65/10 , C10G47/18 , C10G49/04 , C10G65/12 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/307 , C10G2300/4018 , C10G2300/4025 , C10G2400/04 , C10G2400/08 , C10G2400/10
摘要： This invention relates to a process involving hydrocracking of a feedstream in which a converted fraction can exhibit relatively high distillate product yields and maintained or improved distillate fuel properties, while an unconverted fraction can exhibit improved properties particularly useful in the lubricant area. In this hydrocracking process, it can be advantageous for the yield of converted/unconverted product for gasoline fuel application to be reduced or minimized, relative to converted distillate fuel and unconverted lubricant. Catalysts and conditions can be chosen to assist in attaining, or to optimize, desirable product yields and/or properties.

6. 发明申请

US20150275106A1 BASESTOCK PRODUCTION FROM FEEDS CONTAINING SOLVENT EXTRACTS 有权
标题翻译：含有溶剂提取物的饲料的基础油生产
公开(公告)号：US20150275106A1
公开(公告)日：2015-10-01
申请号：US14629997
申请日：2015-02-24
申请人： Nicole D. Vaughn , Teck-Mui Hoo , Michael B. Carroll , Stuart S. Shih , Eric D. Joseck , William J. Novak
发明人： Nicole D. Vaughn , Teck-Mui Hoo , Michael B. Carroll , Stuart S. Shih , Eric D. Joseck , William J. Novak
IPC分类号： C10G67/02 , C10M101/02
CPC分类号： C10G67/02 , C10G65/043 , C10G65/12 , C10G2300/1096 , C10G2300/301 , C10G2400/10 , C10M101/02
摘要： Methods are provided for producing Group II/III lubricant base oil products where at least a portion of the feedstock for forming the lubricant base oil product is a solvent extract fraction from a Group I lubricant production facility. This can increase the overall volume of feedstock available for production of Group II/III lubricant base oils by using a lower value stream (Group I solvent extract) as a portion of the feedstock. The solvent extract fraction can be added to a full range lubricant feedstock or to a portion of a lubricant feedstock, such as adding an extract fraction to a higher viscosity portion (such as a heavy neutral portion) of a feedstock for lubricant production, while a lower viscosity portion (such as a light neutral portion) is processed without addition of an extract fraction.
摘要翻译：提供用于生产组II / III润滑剂基础油产品的方法，其中用于形成润滑剂基础油产品的原料的至少一部分是来自第I组润滑剂生产设备的溶剂提取物部分。这可以通过使用较低价值的流（I类溶剂提取物）作为原料的一部分来增加可用于生产II / III族润滑油基础油的原料的总体积。可以将溶剂萃取馏分加入到全润滑油原料中或一部分润滑剂原料中，例如将提取物馏分加入用于润滑剂生产的原料的较高粘度部分（例如重中性部分），而低粘度部分（如轻中性部分）被加工而不添加萃取部分。

7. 发明授权

US08852425B2 Two stage hydroprocessing with divided wall column fractionator 有权
$Two stage hydroprocessing with divided wall column fractionator$
标题翻译：两级加氢处理与分段壁柱分馏塔
公开(公告)号：US08852425B2
公开(公告)日：2014-10-07
申请号：US12946353
申请日：2010-11-15
申请人： Benjamin S. Umansky , Berne K. Stober , Carlos N. Lopez , Stuart S. Shih , Timothy L. Hilbert , Andre T. Sims , William J. Tracy, III , Akira Murata , Paul W. Kamienski
发明人： Benjamin S. Umansky , Berne K. Stober , Carlos N. Lopez , Stuart S. Shih , Timothy L. Hilbert , Andre T. Sims , William J. Tracy, III , Akira Murata , Paul W. Kamienski
IPC分类号： C10B57/02 , C10G51/02 , B01D3/14 , C10G7/00 , C10G65/04 , C10G45/02 , C10G47/00 , C10G65/12
CPC分类号： C10G45/02 , B01D3/141 , C10G7/00 , C10G47/00 , C10G65/043 , C10G65/12 , C10G2300/1014 , C10G2300/1018 , C10G2300/1037 , C10G2300/202 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/04 , Y02P30/20
摘要： A divided wall column allows for fractionation of multiple streams while maintaining separate product qualities. Effluents from multiple stages of a reaction system can be processed in a single divided wall column. The divided wall column can produce multiple cuts from each separated area, as well as at least one output from a common area.
摘要翻译：分隔壁柱允许分离多个流，同时保持单独的产品质量。来自反应体系的多个阶段的流出物可以在单个分隔壁塔中进行处理。分隔壁柱可以从每个分离的区域产生多个切割，以及从公共区域产生至少一个输出。

8. 发明授权

US08557106B2 Hydrocracking process selective for improved distillate and improved lube yield and properties 有权
标题翻译：加氢裂化过程选择性改善馏出物和改善润滑油产量和性能
公开(公告)号：US08557106B2
公开(公告)日：2013-10-15
申请号：US13237361
申请日：2011-09-20
申请人： William J. Novak , Robert A. Bradway , Stuart S. Shih , Timothy L. Hilbert , Michel Daage
发明人： William J. Novak , Robert A. Bradway , Stuart S. Shih , Timothy L. Hilbert , Michel Daage
IPC分类号： C10G47/02 , C10G45/62 , C10G45/64 , C10G45/12
CPC分类号： C10G65/10 , C10G47/18 , C10G49/04 , C10G65/12 , C10G2300/1074 , C10G2300/202 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/307 , C10G2300/4018 , C10G2300/4025 , C10G2400/04 , C10G2400/08 , C10G2400/10
摘要： This invention relates to a process involving hydrocracking of a feedstream in which a converted fraction can exhibit relatively high distillate product yields and maintained or improved distillate fuel properties, while an unconverted fraction can exhibit improved properties particularly useful in the lubricant area. In this hydrocracking process, it can be advantageous for the yield of converted/unconverted product for gasoline fuel application to be reduced or minimized, relative to converted distillate fuel and unconverted lubricant. Catalysts and conditions can be chosen to assist in attaining, or to optimize, desirable product yields and/or properties.
摘要翻译：本发明涉及一种包含进料流加氢裂化的方法，其中转化馏分可表现出相对较高的馏出物产物产率和维持或改善的馏出物燃料性质，而未转化的馏分可表现出在润滑剂区域特别有用的改进的性能。在该加氢裂化过程中，相对于转化的馏出物燃料和未转化的润滑剂，可以有利于减少或最小化汽油燃料应用的转化/未转化产物的产率。可以选择催化剂和条件以帮助实现或优化所需的产物产率和/或性能。

9. 发明申请

US20120000817A1 Production of Low Color Middle Distillate Fuels 审中-公开
标题翻译：生产低色中间馏分燃料
公开(公告)号：US20120000817A1
公开(公告)日：2012-01-05
申请号：US13169170
申请日：2011-06-27
申请人： Stuart S. Shih
发明人： Stuart S. Shih
IPC分类号： C10G49/00
CPC分类号： C10G65/04 , C10G45/10 , C10G45/12 , C10G2300/1048 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/4018 , C10G2400/04 , C10G2400/08
摘要： In a process for producing a low color diesel and/or kerosene fuel, a middle distillate feed can be supplied to a reactor having at least one first catalyst bed containing a first desulfurization and/or isomerization catalyst and at least one second catalyst bed containing a decolorization catalyst downstream from the first catalyst bed(s). The feed can be reacted with the hydrogen in the presence of the first catalyst at a temperature from about 290° C. to about 430° C. to produce a first liquid effluent, which can be cooled by about 10° C. to about 40° C. with a quench medium and cascaded to the at least one second catalyst bed. The cooled first liquid effluent can then be reacted with hydrogen in the presence of the decolorization catalyst at a temperature from about 280° C. to about 415° C. to produce a second effluent having an ASTM color less than 2.5.
摘要翻译：在生产低色柴油和/或煤油燃料的方法中，中间馏分料可以供给至具有至少一个含有第一脱硫和/或异构化催化剂的第一催化剂床和至少一个含有脱色催化剂从第一催化剂床下游。在约290℃至约430℃的温度下，进料可以在第一催化剂存在下与氢反应，以产生第一液体流出物，其可被冷却约10℃至约40℃ ℃，并与骤冷介质并级联至至少一个第二催化剂床。然后在约280℃至约415℃的温度下，将冷却的第一液体流出物在脱色催化剂存在下与氢气反应，以产生ASTM颜色小于2.5的第二流出物。

10. 发明授权

US5591326A Catalytic process for crude oil desalting 失效
标题翻译：原油脱盐催化过程
公开(公告)号：US5591326A
公开(公告)日：1997-01-07
申请号：US347934
申请日：1994-12-01
申请人： Stuart S. Shih
发明人： Stuart S. Shih
IPC分类号： C10G45/12 , C10G45/00
CPC分类号： C10G45/12
摘要： A catalytic desalting process for processing whole crude oils. The desalting process uses an M41S catalyst to remove salts from the whole crude. Solids may also be removed from the whole crude using a porous material having a pore size greater than about 10 microns. The catalytic desalting process does not generate waste water.
摘要翻译：一种用于加工全部原油的催化脱盐方法。脱盐方法使用M41S催化剂从整个原油中除去盐。也可以使用孔径大于约10微米的多孔材料，从整个原料中除去固体。催化脱盐过程不会产生废水。

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