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1. 发明授权

US5489732A Fluidized solid bed motor fuel alkylation process 失效
标题翻译：流化床固体床机油燃料烷基化工艺
公开(公告)号：US5489732A
公开(公告)日：1996-02-06
申请号：US323437
申请日：1994-10-14
申请人： Scott Y. Zhang , Christopher D. Gosling , Paul A. Sechrist , Gregory A. Funk
发明人： Scott Y. Zhang , Christopher D. Gosling , Paul A. Sechrist , Gregory A. Funk
IPC分类号： B01J8/28 , B01J38/10 , B01J38/58 , C07C2/58 , C07C2/66 , C07C2/86 , C10G50/00
CPC分类号： C10G50/00 , B01J38/10 , B01J38/58 , B01J8/28 , C07C2/58 , C07C2/66 , C07C2/864 , Y02P20/584
摘要： Hydrocarbons are alkylated in a fluidized riser-reactor using a solid catalyst which is regenerated within the process by contact with hydrogen. The alkylation and regeneration steps are separated to prevent the admixture of hydrogen and any olefins present in the process. Two separate modes of regeneration are performed simultaneously: a mild liquid-phase washing and a vapor-phase hot hydrogen stripping operation.
摘要翻译：碳氢化合物在使用固体催化剂的流化提升管 - 反应器中烷基化，所述固体催化剂在该方法中通过与氢接触而再生。分离烷基化和再生步骤以防止氢气与该方法中存在的任何烯烃的混合物。同时进行两种分离的再生模式：温和的液相洗涤和气相热氢提取操作。

2. 发明授权

US06486374B1 Method and apparatus for alkylation using solid catalyst particles in a transport reactor 失效
标题翻译：在运输反应器中使用固体催化剂颗粒进行烷基化的方法和装置
公开(公告)号：US06486374B1
公开(公告)日：2002-11-26
申请号：US09249749
申请日：1999-02-12
申请人： William H. Radcliffe , Wesley L. Kiel , Christopher D. Gosling , Paul A. Sechrist , Paul Anderson
发明人： William H. Radcliffe , Wesley L. Kiel , Christopher D. Gosling , Paul A. Sechrist , Paul Anderson
IPC分类号： C07C15067
CPC分类号： C07C2/58 , Y10S585/921 , Y10S585/924 , Y10S585/926
摘要： A method and apparatus for alkylating an alkylation substrate with an alkylating agent in the presence of solid catalyst particles in a transport reactor is disclosed. Solid catalyst particles in the transport reactor effluent recirculate to the inlet of the transport reactor through one or more conduits. The rate through each conduit is regulated by fluid-controlled valves that use the alkylation substrate as the regulating fluid. This method and apparatus help ensure uniform or symmetric flow of catalyst from the effluent of the transport reactor to the bottom of the transport reactor. This method and apparatus also help ensure uniform or symmetric flow of alkylation substrate to the bottom of the transport reactor with minimal bypassing by the alkylating agent around of the transport reactor. This invention finds use in the production of motor fuels by the alkylation of liquid hydrocarbons in the presence of solid catalyst particles.
摘要翻译：公开了一种在运输反应器中在固体催化剂颗粒存在下用烷基化剂烷基化底物的方法和装置。运输反应器流出物中的固体催化剂颗粒通过一个或多个导管再循环到输送反应器的入口。通过每个管道的速率由使用烷基化底物作为调节流体的流体控制阀调节。该方法和设备有助于确保催化剂从输送反应器的流出物到输送反应器底部的均匀或对称流动。该方法和装置还有助于确保烷基化底物均匀或对称地流动到运输反应器的底部，同时通过运输反应器周围的烷基化剂的最小旁路。本发明用于在固体催化剂颗粒存在下通过液体烃的烷基化来生产汽车燃料。

3. 发明授权

US5565617A Process for purifying an alkylate stream 失效
标题翻译：纯化烷基化物流的方法
公开(公告)号：US5565617A
公开(公告)日：1996-10-15
申请号：US445619
申请日：1995-05-22
申请人： Robert J. Schmidt , Paul A. Sechrist , Paul T. Barger , Christopher D. Gosling
发明人： Robert J. Schmidt , Paul A. Sechrist , Paul T. Barger , Christopher D. Gosling
IPC分类号： C07C7/00 , C07C9/16
CPC分类号： C07C9/16 , C07C7/005
摘要： A process for purifying an alkylate feedstream is disclosed. The feedstream contains hydrogen, hydrogen chloride, C.sub.2 -C.sub.7+ alkanes, C.sub.2 -C.sub.6 alkenes and C.sub.2 -C.sub.6 alkyl halides. The process involves flowing the alkylate through a series of separation zones and a reaction zone to provide a halide free alkylate stream.
摘要翻译：公开了一种纯化烷基化物进料流的方法。进料流含有氢，氯化氢，C 2 -C 7 +烷烃，C 2 -C 6烯烃和C 2 -C 6烷基卤化物。该方法包括使烷基化物流过一系列分离区和反应区，以提供无卤化物的烷基化物流。

4. 发明授权

US06814943B2 Apparatus for alkylation using solid catalyst particles in a transport reactor 失效
标题翻译：在运输反应器中使用固体催化剂颗粒进行烷基化的装置
公开(公告)号：US06814943B2
公开(公告)日：2004-11-09
申请号：US10299885
申请日：2002-11-19
申请人： William H. Radcliffe , Wesley L. Kiel , Christopher D. Gosling , Paul A. Sechrist , Paul Anderson
发明人： William H. Radcliffe , Wesley L. Kiel , Christopher D. Gosling , Paul A. Sechrist , Paul Anderson
IPC分类号： B01J800
CPC分类号： C07C2/58 , Y10S585/921 , Y10S585/924 , Y10S585/926
摘要： A method and apparatus for alkylating an alkylation substrate with an alkylating agent in the presence of solid catalyst particles in a transport reactor is disclosed. Solid catalyst particles in the transport reactor effluent recirculate to the inlet of the transport reactor through one or more conduits. The rate through each conduit is regulated by fluid-controlled valves that use the alkylation substrate as the regulating fluid. This method and apparatus help ensure uniform or symmetric flow of catalyst from the effluent of the transport reactor to the bottom of the transport reactor. This method and apparatus also help ensure uniform or symmetric flow of alkylation substrate to the bottom of the transport reactor with minimal bypassing by the alkylating agent around of the transport reactor. This invention finds use in the production of motor fuels by the alkylation of liquid hydrocarbons in the presence of solid catalyst particles.

5. 发明授权

US6036845A Modified riser-reactor reforming process with prereactor 失效
标题翻译：改进的提升管反应器重整过程与预反应器
公开(公告)号：US6036845A
公开(公告)日：2000-03-14
申请号：US72444
申请日：1998-05-04
申请人： Gregory A. Funk , Christopher D. Gosling , Paula L. Bogdan
发明人： Gregory A. Funk , Christopher D. Gosling , Paula L. Bogdan
IPC分类号： B01J23/14 , B01J23/40 , B01J23/96 , C10G35/10 , C10G35/14 , C10G35/04 , B01J23/90 , C10G35/06
CPC分类号： B01J23/40 , B01J23/14 , B01J23/96 , C10G35/10 , C10G35/14
摘要： A catalytic reforming process comprises a prereactor which provides an intermediate stream to a riser reactor with multiple catalyst injection points to obtain high aromatics yields from a naphtha feedstock. Product from the riser reactor typically is discharged into a fluidized-bed reforming reactor, in which the reforming reaction is completed and catalyst is separated from hydrogen and hydrocarbons. Hydrocarbons from the reactor are separated to recover an aromatized product. Catalyst is regenerated to remove coke and reduced for reuse in the reforming process.
摘要翻译：催化重整方法包括一个预反应器，该预反应器提供具有多个催化剂注入点的提升管反应器的中间物流，以获得来自石脑油原料的高芳族化合物产率。来自提升管反应器的产物通常被排放到流化床重整反应器中，其中重整反应完成并且催化剂与氢气和烃分离。将来自反应器的烃分离以回收芳构化产物。再生催化剂以除去焦炭并在重整过程中减少再利用。

6. 发明授权

US5565090A Modified riser-reactor reforming process 失效
标题翻译：改进的提升管反应器重整过程
公开(公告)号：US5565090A
公开(公告)日：1996-10-15
申请号：US345057
申请日：1994-11-25
申请人： Christopher D. Gosling , Scott Y. Zhang , Paula L. Bogdan
发明人： Christopher D. Gosling , Scott Y. Zhang , Paula L. Bogdan
IPC分类号： C10G35/06 , C10G35/14 , C10G35/10
CPC分类号： C10G35/06 , C10G35/14 , Y10S585/955
摘要： A catalytic reforming process uses a riser reactor with multiple catalyst injection points to obtain high aromatics yields from a naphtha feedstock. Product from the riser reactor typically is discharged into a fluidized-reforming reactor, in which the reforming reaction is completed and catalyst is separated from hydrogen and hydrocarbons. Hydrocarbons from the reactor are separated to recover an aromatized product. Catalyst is regenerated to remove coke and reduced for reuse in the reforming process.
摘要翻译：催化重整方法使用具有多个催化剂注入点的提升管反应器以获得来自石脑油原料的高芳族化合物产率。来自提升管反应器的产物通常被排放到流化重整反应器中，其中重整反应完成并且催化剂与氢气和烃分离。将来自反应器的烃分离以回收芳构化产物。再生催化剂以除去焦炭并在重整过程中减少再利用。

7. 发明授权

US08691077B2 Process for converting a hydrocarbon stream, and optionally producing a hydrocracked distillate 有权
标题翻译：用于转化烃流和任选地生产加氢裂化馏出物的方法
公开(公告)号：US08691077B2
公开(公告)日：2014-04-08
申请号：US13418788
申请日：2012-03-13
申请人： Clayton C. Sadler , Christopher D. Gosling
发明人： Clayton C. Sadler , Christopher D. Gosling
IPC分类号： C10G47/26 , C10G65/10 , C10G9/00 , C10G69/06
CPC分类号： C10G45/58 , C10G47/26 , C10G65/10 , C10G65/12 , C10G69/04 , C10G2400/02 , C10G2400/30
摘要： One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.
摘要翻译：一个示例性实施方案可以是用于转化烃流的方法。该方法可以包括使具有一个或多个C 40 +烃的烃流通过浆料加氢裂化区获得具有一个或多个C 9 -C 22烃的馏出物烃流，并将馏出物烃流送入加氢裂化区，以选择性加氢裂化芳族化合物，包括至少两个环获得经处理的馏出物。

8. 发明申请

US20130240406A1 PROCESS FOR CONVERTING A HYDROCARBON STREAM, AND OPTIONALLY PRODUCING A HYDROCRACKED DISTILLATE 有权
标题翻译：转化烃流的方法，并可选择生产水解馏分
公开(公告)号：US20130240406A1
公开(公告)日：2013-09-19
申请号：US13418788
申请日：2012-03-13
申请人： Clayton C. Sadler , Christopher D. Gosling
发明人： Clayton C. Sadler , Christopher D. Gosling
IPC分类号： C10G65/10
CPC分类号： C10G45/58 , C10G47/26 , C10G65/10 , C10G65/12 , C10G69/04 , C10G2400/02 , C10G2400/30
摘要： One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.
摘要翻译：一个示例性实施方案可以是用于转化烃流的方法。该方法可以包括使具有一个或多个C 40 +烃的烃流通过浆料加氢裂化区获得具有一个或多个C 9 -C 22烃的馏出物烃流，并将馏出物烃流送入加氢裂化区，以选择性加氢裂化芳族化合物，包括至少两个环获得经处理的馏出物。

9. 发明授权

US08003834B2 Integrated process for oil extraction and production of diesel fuel from biorenewable feedstocks 有权
标题翻译：从生物可再生原料中提取和生产柴油的综合工艺
公开(公告)号：US08003834B2
公开(公告)日：2011-08-23
申请号：US12193191
申请日：2008-08-18
申请人： Terry L. Marker , Graham D. Ellis , Christopher D. Gosling
发明人： Terry L. Marker , Graham D. Ellis , Christopher D. Gosling
IPC分类号： C10L1/16 , C07C1/00
CPC分类号： C10G45/58 , C10G3/46 , C10G3/50 , C10G45/02 , C10G2300/1014 , C10G2300/1018 , C10G2300/1022 , C10G2300/1037 , C10G2300/4081 , C10G2400/02 , C10G2400/04 , C10G2400/28 , C10L1/08 , Y02E50/13 , Y02P30/20
摘要： An integrated process has been developed for producing diesel boiling range fuel from renewable feedstocks such as animal and plant oils and using a byproduct naphtha as an extraction solvent in the generation of the renewable feedstock. The process involves treating a renewable feedstock by hydrogenating and deoxygenating to provide a hydrocarbon fraction useful as a diesel fuel or diesel boiling range fuel blending component. A byproduct naphtha stream is used as an extraction solvent in a process for the generation of the renewable feedstock. 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动植物油生产柴油沸点燃料并且在副产生可再生原料中使用副产物石脑油作为提取溶剂的综合方法。该方法包括通过氢化和脱氧处理可再生原料以提供用作柴油燃料或柴油沸程燃料调配组分的烃馏分。在生成可再生原料的方法中使用副产物石脑油流作为萃取溶剂。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

US20100224534A1 Process for Preventing Metal Catalyzed Coking 有权
标题翻译：防止金属催化焦化工艺
公开(公告)号：US20100224534A1
公开(公告)日：2010-09-09
申请号：US12397647
申请日：2009-03-04
申请人： Keith A. Couch , Christopher D. Gosling
发明人： Keith A. Couch , Christopher D. Gosling
IPC分类号： C10G11/00
CPC分类号： C10G11/18 , C10G2300/202 , C10G2300/207 , C10G2300/708 , C10G2400/20
摘要： A process and apparatus is disclosed in which a sulfiding agent is added to a catalytic conversion reactor to prevent metal catalyzed coking. The catalytic reactor may be downstream from a first fluid catalytic cracking reactor that provides C10-hydrocarbons as feed to the downstream catalytic reactor.
摘要翻译：公开了一种方法和装置，其中将硫化剂加入到催化转化反应器中以防止金属催化焦化。催化反应器可以在第一流化催化裂化反应器的下游提供作为进料到下游催化反应器的C10烃。

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