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公开(公告)号：US06106789A
公开(公告)日：2000-08-22
申请号：US176612
申请日：1993-12-30
Applicant: Max W. Thompson , John S. Olson
Inventor： Max W. Thompson , John S. Olson
CPC classification number: C07C2/62 , B01J19/24 , B01J2219/00085 , C07C2527/054 , Y10S165/429
Abstract: The invention provides an improved alkylation process and reactor apparatus. The invention utilizes a vessel containing a riser-reactor conduit, an acid settler and an acid cooler. Hydrocarbons are introduced beneath said riser-reactor conduit, mixed with acid catalyst, and passed generally upwards through the riser-reactor conduit to enter the acid settler. Within the acid settler, alkylate is separate from the acid catalyst and is removed from the vessel. Acid catalyst from the acid settler is cooled in the internal acid coolers and returned to the region beneath the riser-reactor conduit.
Abstract translation: 本发明提供改进的烷基化方法和反应器装置。 本发明利用了一种容器，该容器含有提升管反应器管道，酸沉降器和酸性冷却器。 将碳氢化合物引入所述提升管 - 反应器管道下方，与酸催化剂混合，并通常向上通过提升管 - 反应器管道进入酸沉降器。 在酸沉降器中，烷基化物与酸催化剂分离，并从容器中除去。 来自酸沉降器的酸催化剂在内部酸性冷却器中冷却并返回到提升管 - 反应器管道下方的区域。
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公开(公告)号：US4948405A
公开(公告)日：1990-08-14
申请号：US456393
申请日：1989-12-26
Applicant: Max W. Thompson
Inventor： Max W. Thompson
IPC: F25J3/02
CPC classification number: F25J3/0233 , F25J3/0209 , F25J3/0257 , F25J2200/04 , F25J2200/74 , F25J2200/78 , F25J2205/04 , F25J2220/64 , F25J2235/60 , F25J2240/02 , F25J2240/40 , F25J2245/02 , F25J2270/02 , Y10S62/927
Abstract: An improved process and apparatus is disclosed for rejecting nitrogen from a gaseous nitrogen-methane mixture while the nitrogen content of the mixture varies widely. The process, which is especially suited for recovery of nitrogen in an enhanced oil reservoir flooding project which employs nitrogen for flooding the reservoir; utilizes a modified dual distillation column arrangement including a relatively high pressure fractionator which lacks a conventional reboiler and a low pressure fractionator which lacks a conventional overhead condenser for liquid reflux.
Abstract translation: 公开了一种改进的方法和装置，用于从气态氮 - 甲烷混合物中排除氮气，同时混合物的氮含量变化很大。 该过程特别适用于采用氮气淹没水库的强化油藏淹水工程中的氮回收; 利用改进的双蒸馏塔装置，其包括缺少常规再沸器的相对高压分馏塔和缺少用于液体回流的常规塔顶冷凝器的低压分馏塔。
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公开(公告)号：US07959829B2
公开(公告)日：2011-06-14
申请号：US12640226
申请日：2009-12-17
Applicant: David L. Breton , Albert C. Tsang , Max W. Thompson
Inventor： David L. Breton , Albert C. Tsang , Max W. Thompson
CPC classification number: C10J3/54 , C10J2300/0909 , C10J2300/093 , C10J2300/1823 , Y02P20/129
Abstract: A system and process for gasifying carbonaceous feedstock with staged slurry addition in order to prevent the formation of tar that causes deposition problems. Dry solid carbonaceous material is partially combusted, then pyrolyzed along with a first slurry stream comprising carbonaceous material in two separate reactor sections, thereby producing mixture products comprising synthesis gas. The second slurry stream comprising particulate carbonaceous material is fed to a drying unit downstream of a heat recovery zone along with the mixture product exiting the heat recovery zone. The resulting final temperature of the second stage mixture products and dried particulate carbonaceous material is between 450° F. and 550° F., a temperature range that is typically not conducive to the emission of heavy molecular-weight tar species.
Abstract translation: 用分级浆料气化碳质原料以防止形成沉淀问题的焦油的系统和方法。 干固体碳质材料部分燃烧，然后与包含碳质材料的第一浆料流在两个分离的反应器部分中热解，从而产生包含合成气的混合物。 包含颗粒状碳质材料的第二浆料流与离开热回收区的混合物一起进料到热回收区的下游的干燥单元。 所得到的第二阶段混合物产物和干燥颗粒状碳质材料的最终温度在450°F至550°F之间，通常不利于重质分子量焦油物质的排放的温度范围。
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公开(公告)号：US20090283448A1
公开(公告)日：2009-11-19
申请号：US11537715
申请日：2006-10-02
Applicant: Victor G. Hoover , Max W. Thompson , Darrin D. Barnes , Joe D. Cox , Philip L. Collins , Christopher J. Lafrancois , Ricky E. Snelling , Jean B. Thesee , Robert Zapata
Inventor： Victor G. Hoover , Max W. Thompson , Darrin D. Barnes , Joe D. Cox , Philip L. Collins , Christopher J. Lafrancois , Ricky E. Snelling , Jean B. Thesee , Robert Zapata
CPC classification number: C10G25/09 , C10G25/12 , C10G2300/202 , C10G2300/4018
Abstract: A hydrocarbon desulfurization system that circulates fluidizable solid particles through a fluidized bed reactor, a fluidized bed regenerator, and a fluidized bed reducer to thereby provide for substantially continuous desulfurization of a hydrocarbon-containing fluid stream and substantially continuous regeneration of the solid particles. A novel transport system is employed for transporting the solid particles between the reactor, the regenerator, and the reducer. The transport system uses close-coupled vessels and gravity flow between various vessels to minimize equipment cost and particle attrition.
Abstract translation: 一种烃类脱硫系统，其使可流化的固体颗粒循环通过流化床反应器，流化床再生器和流化床还原剂，从而提供含烃流体物流的基本上连续的脱硫和固体颗粒的基本上连续的再生。 采用新颖的输送系统将固体颗粒输送到反应器，再生器和还原剂之间。 运输系统使用紧密耦合的容器和各种容器之间的重力流动，以最小化设备成本和颗粒磨损。
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公开(公告)号：US09074149B2
公开(公告)日：2015-07-07
申请号：US12652318
申请日：2010-01-05
Applicant: Albert C. Tsang , Max W. Thompson , Rick Q. Honaker
Inventor： Albert C. Tsang , Max W. Thompson , Rick Q. Honaker
CPC classification number: C10J3/52 , B03B9/04 , C10J2300/1631 , C10J2300/1807
Abstract: The current invention discloses a novel process and system to improve the quality of the slag product from a gasification process, thereby producing low-carbon marketable aggregate product. The inventive processes and systems employ a hindered-bed settler in conjunction with optional disengager and de-watering devices. A slag slurry stream from a gasification process is de-watered and the solids content is increased from less than 5% to greater than 30% via the de-waterer before being conveyed to a hindered-bed settler, wherein the carbon content is reduced from as much as 70% to less than 5%. Particles with a high carbon content are conveyed to a gravity settler, whereby they are concentrated and then recycled to the gasification reactor.
Abstract translation: 本发明公开了一种提高来自气化工艺的炉渣产品质量的新方法和系统，从而生产低碳可销售的聚合物产品。 本发明的方法和系统采用受阻床沉降器结合可选的脱水装置和脱水装置。 来自气化过程的渣浆料流被脱水，并且在输送到受阻床沉降器之前，固体含量通过脱水器从小于5％增加到大于30％，其中碳含量从 多达70％至小于5％。 将具有高碳含量的颗粒输送至重力沉降器，由此将其浓缩，然后再循环至气化反应器。
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Patent Agency Ranking
公开(公告)号：US08088188B2
公开(公告)日：2012-01-03
申请号：US13078461
申请日：2011-04-01
Applicant: David L. Breton , Albert C. Tsang , Max W. Thompson
Inventor： David L. Breton , Albert C. Tsang , Max W. Thompson
IPC: C10J3/00
CPC classification number: C10J3/54 , C10J2300/0909 , C10J2300/093 , C10J2300/1823 , Y02P20/129
Abstract: A system and process for gasifying carbonaceous feedstock with staged slurry addition in order to prevent the formation of tar that causes deposition problems. Dry solid carbonaceous material is partially combusted, then pyrolyzed along with a first slurry stream comprising carbonaceous material in two separate reactor sections, thereby producing mixture products comprising synthesis gas. The second slurry stream comprising particulate carbonaceous material is fed to a drying unit downstream of a heat recovery zone along with the mixture product exiting the heat recovery zone The resulting final temperature of the second stage mixture products and dried particulate carbonaceous material is between 450° F. and 550° F., a temperature range that is typically not conducive to the emission of heavy molecular-weight tar species.
Abstract translation: 用分级浆料气化碳质原料以防止形成沉淀问题的焦油的系统和方法。 干固体碳质材料部分燃烧，然后与包含碳质材料的第一浆料流在两个分离的反应器部分中热解，从而产生包含合成气的混合物。 包含颗粒状含碳材料的第二浆料流与离开热回收区的混合物一起被供给到热回收区下游的干燥单元。第二阶段混合物产物和干燥的颗粒状含碳材料的最终温度为450°F 和550°F，通常不利于重分子量焦油物质的排放的温度范围。
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公开(公告)号：US07182918B2
公开(公告)日：2007-02-27
申请号：US10798821
申请日：2004-03-11
Applicant: Victor G. Hoover , Max W. Thompson , Darrin D. Barnes , Joe D. Cox , Philip L. Collins , Christopher J. Lafrancois , Ronald E. Miranda , Ricky E. Snelling , Jean B. Thesee , Robert Zapata
Inventor： Victor G. Hoover , Max W. Thompson , Darrin D. Barnes , Joe D. Cox , Philip L. Collins , Christopher J. Lafrancois , Ronald E. Miranda , Ricky E. Snelling , Jean B. Thesee , Robert Zapata
IPC: B01J8/08
CPC classification number: C10G25/09 , C10G25/12 , C10G2300/202 , C10G2300/4018
Abstract: A hydrocarbon desulfurization system that circulates fluidizable solid particles through a fluidized bed reactor, a fluidized bed regenerator, and a fluidized bed reducer to thereby provide for substantially continuous desulfurization of a hydrocarbon-containing fluid stream and substantially continuous regeneration of the solid particles. A novel transport system is employed for transporting the solid particles between the reactor, the regenerator, and the reducer. The transport system uses close-coupled vessels and gravity flow between various vessels to minimize equipment cost and particle attrition.
Abstract translation: 一种烃类脱硫系统，其使可流化的固体颗粒循环通过流化床反应器，流化床再生器和流化床还原剂，从而提供含烃流体物流的基本上连续的脱硫和固体颗粒的基本上连续的再生。 采用新颖的输送系统将固体颗粒输送到反应器，再生器和还原剂之间。 运输系统使用紧密耦合的容器和各种容器之间的重力流动，以最小化设备成本和颗粒磨损。
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公开(公告)号：US07172685B2
公开(公告)日：2007-02-06
申请号：US10120700
申请日：2002-04-11
Applicant: Max W. Thompson , Behzad Jazayeri , Robert Zapata , Manuel Hernandez
Inventor： Max W. Thompson , Behzad Jazayeri , Robert Zapata , Manuel Hernandez
CPC classification number: C10G45/02 , B01D53/047 , B01D53/08 , B01D53/12 , B01D2253/1122 , B01D2253/1124 , B01D2253/304 , B01D2256/24 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2259/40009 , B01D2259/40056 , B01D2259/40086 , B01D2259/403 , B01J20/0225 , B01J20/06 , B01J20/08 , B01J20/106 , B01J20/3433 , B01J20/3458 , B01J2220/56 , C10G25/09 , C10G25/12
Abstract: A hydrocarbon desulfurization system employing regenerable solid sorbent particulates in a fluidized bed desulfurization reactor. The sulfur-loaded sorbent particulates are continuously withdrawn from the reactor and transferred to a regenerator. A novel solids transport mechanism provides for the safe and effective transfer of the sulfur-loaded sorbent particulates from the high pressure hydrocarbon environment of the reactor to the low pressure oxygen environment of the regenerator.
Abstract translation: 在流化床脱硫反应器中使用可再生固体吸附剂颗粒的烃脱硫系统。 硫负载的吸附剂颗粒从反应器中连续排出并转移到再生器中。 新颖的固体输送机制提供了将负载硫的吸附剂颗粒从反应器的高压烃环境到再生器的低压氧气环境的安全和有效的转移。
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公开(公告)号：US08460410B2
公开(公告)日：2013-06-11
申请号：US12192471
申请日：2008-08-15
Applicant: Albert C. Tsang , Chancelor L. Williams , Max W. Thompson , David L. Breton
Inventor： Albert C. Tsang , Chancelor L. Williams , Max W. Thompson , David L. Breton
Abstract: The present invention relates to a system and process for gasifying feedstock such as carbonaceous materials. The invention includes partial combustion of dry solids and pyrolysis of carbonaceous material slurry in two separate reactor sections and produce mixture products comprising synthesis gas. The invention employs one or more catalytic or sorbent bed for removing tar from the synthesis gas. The inventive system and process allow a gasification to be carried out under higher slurry feeding rate and lower temperature with the provision to manage the tar being produced, therefore to increase the conversion efficiency of the overall gasification.
Abstract translation: 本发明涉及用于气化诸如碳质材料的原料的系统和方法。 本发明包括干固体的部分燃烧和碳质材料浆料在两个分离的反应器部分中的热解，并产生包含合成气的混合物。 本发明采用一种或多种催化剂或吸附剂床来从合成气中除去焦油。 本发明的系统和方法允许在更高的浆料进料速率和较低温度下进行气化，同时提供管理所生产的焦油，从而提高整体气化的转化效率。
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公开(公告)号：US07666298B2
公开(公告)日：2010-02-23
申请号：US10821161
申请日：2004-04-07
Applicant: Paul F. Meier , Edward L. Sughrue , Jan W. Wells , Douglas W. Hausler , Max W. Thompson , Amos A. Avidan
Inventor： Paul F. Meier , Edward L. Sughrue , Jan W. Wells , Douglas W. Hausler , Max W. Thompson , Amos A. Avidan
IPC: C10G25/00
CPC classification number: B01D53/12 , B01D53/0407 , B01D53/508 , B01D2253/1122 , B01D2253/1124 , B01D2253/304 , B01D2256/24 , B01D2257/30 , B01D2259/40086 , B01D2259/403 , B01D2259/414 , B01J8/0055 , B01J8/1872 , B01J8/26 , B01J8/34 , B01J2208/0084 , B01J2219/00006 , C10G25/003 , C10G25/09 , C10G25/12
Abstract: A method and apparatus for removing sulfur from a hydrocarbon-containing fluid stream wherein desulfurization is enhanced by improving the contacting of the hydrocarbon-containing fluid stream and sulfur-sorbing solid particulates in a fluidized bed reactor.
Abstract translation: 一种用于从含烃流体物流中除去硫的方法和装置，其中通过改进流化床反应器中含烃流体物流和吸附硫的固体颗粒的接触来增强脱硫。
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