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公开(公告)号：US10213732B2
公开(公告)日：2019-02-26
申请号：US15676149
申请日：2017-08-14
Applicant: General Electric Company
Inventor： Irina Pavlovna Spiry , Benjamin Rue Wood , Surinder Prabhjot Singh , Robert James Perry , John Brian McDermott
Abstract: A method for treatment of a flue gas involves feeding the flue gas and a lean solvent to an absorber. The method further involves reacting the flue gas with the lean solvent within the absorber to generate a clean flue gas and a rich solvent. The method also involves feeding the clean flue gas from the absorber and water from a source, to a wash tower to separate a stripped portion of the lean solvent from the clean flue gas to generate a washed clean flue gas and a mixture of the water and the stripped portion of the lean solvent. The method further involves treating at least a portion of the mixture of the water and the stripped portion of the lean solvent via a separation system to separate the water from the stripped portion of the lean solvent.
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公开(公告)号：US20170159932A1
公开(公告)日：2017-06-08
申请号：US14957738
申请日：2015-12-03
Applicant: General Electric Company
Inventor： Surinder Prabhjot Singh , Dan Hancu , Benjamin Rue Wood , Wei Chen , Dwayne David McDuffie , Mark David Kehmna , Irina Pavlovna Spiry
CPC classification number: F23J15/04 , F22B1/16 , F22D1/003 , F23J2215/50
Abstract: A power generation system includes a power generation plant portion including a feedwater heating system configured to channel a feedwater stream and a carbon dioxide capture portion coupled in flow communication with the power generation plant portion. The carbon dioxide capture portion includes a solvent circuit configured to channel a solvent stream through at least a portion of the carbon dioxide capture portion. The carbon dioxide capture portion also includes a heat recovery system coupled in flow communication with the solvent circuit and the feedwater heating system. The heat recovery system is configured to transfer heat energy from the solvent stream to the feedwater stream and to channel the heated feedwater from the heat recovery system to the feedwater heating system.
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公开(公告)号：US09656205B2
公开(公告)日：2017-05-23
申请号：US13931421
申请日：2013-06-28
Applicant: General Electric Company
Inventor： Surinder Prabhjot Singh , Harish Radhakrishna Acharya , Robert James Perry , John Brian McDermott
CPC classification number: B01D53/62 , B01D53/1406 , B01D53/1475 , B01D53/343 , B01D53/78 , B01D53/83 , B01D2252/2041 , B01D2252/20421 , B01D2252/20484 , B01D2252/20489 , B01D2257/504 , B01D2258/0283 , B01D2259/65 , Y02C10/04 , Y02C10/06
Abstract: A system and method for treatment of a medium is disclosed. The system includes a plurality of separator zones and a plurality of heat transfer zones. Each of the separator zone and the heat transfer zone among the plurality of separator zones and heat transfer zones respectively, are disposed alternatively in a flow duct. Further, each separator zone includes an injector device for injecting a sorbent into the corresponding separator zone. Within the corresponding separator zone, the injected sorbent is reacted with a gaseous medium flowing in the flow duct, so as to generate a reacted gaseous medium and a reacted sorbent. Further, each heat transfer zone exchanges heat between the reacted gaseous medium fed from the corresponding separator zone and a heat transfer medium.
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公开(公告)号：US09217112B2
公开(公告)日：2015-12-22
申请号：US14794918
申请日：2015-07-09
Applicant: General Electric Company
Inventor： Surinder Prabhjot Singh , John Brian McDermott , Lingzhi Zhang
CPC classification number: C10G2/34 , B01J19/245 , B01J2219/00103 , B01J2219/24 , C01B3/36 , C01B3/382 , C01B2203/0244 , C01B2203/0261 , C01B2203/062 , C01B2203/1241 , C10G2/32 , Y10T137/8593
Abstract: A system and method of converting natural gases to liquids is provided. The system includes a catalytic partial oxidation (CPO) system with natural gas, air and steam input, a Fischer-Tropsch (F-T) system taking syngas from the CPO system, and supplying product gases to a power engine (PE), after separation of the product liquids. An F-T steam output line is in fluid communication with the CPO-steam input line. The energy output from the PE is supplied to the compressors and condensers, to provide self-sustainability in energy, for the gas-to-liquid separation system.
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公开(公告)号：US20150132204A1
公开(公告)日：2015-05-14
申请号：US14078815
申请日：2013-11-13
Applicant: General Electric Company
Inventor： Norberto Silvi , Robert James Perry , Surinder Prabhjot Singh , Gary Stephen Balch , Tiffany Elizabeth Pinard Westendorf
CPC classification number: B01D53/62 , B01D53/1425 , B01D53/18 , B01D53/78 , B01D53/96 , B01D2252/204 , B01D2257/104 , B01D2257/404 , B01D2257/502 , B01D2257/504 , B01D2257/80 , B01D2258/0283 , B01D2258/05 , Y02E50/346
Abstract: A system for treatment of a gaseous medium, comprises an extruder having a barrel. The extruder further comprises a first inlet port, a second inlet port, and a plurality of outlet ports coupled to the barrel. The first inlet port is configured for feeding a lean sorbent, the second inlet port is configured for feeding a gaseous medium, and the plurality of outlet ports are configured for releasing a plurality of components removed from the gaseous medium. Further, the extruder comprises a plurality of helical elements coupled to a plurality of kneading elements, mounted on a shaft, and disposed within the barrel. The barrel and the plurality of helical and kneading elements together form an absorption unit and a desorption unit. The first and second inlet ports are formed in the absorption unit and the plurality of outlet ports are formed in the absorption and desorption units.
Abstract translation: 用于处理气体介质的系统包括具有桶的挤出机。 挤出机还包括第一入口端口，第二入口端口和联接到桶筒的多个出口端口。 第一入口端口被配置为供给贫吸收剂，第二入口端口被配置为供给气体介质，并且多个出口端口被配置用于释放从气态介质去除的多个部件。 此外，挤出机包括连接到多个捏合元件的多个螺旋元件，其安装在轴上并且设置在筒内。 桶和多个螺旋和捏合元件一起形成吸收单元和解吸单元。 第一入口和第二入口形成在吸收单元中，并且多个出口形成在吸收和解吸单元中。
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Patent Agency Ranking
公开(公告)号：US20150004082A1
公开(公告)日：2015-01-01
申请号：US13931421
申请日：2013-06-28
Applicant: General Electric Company
Inventor： Surinder Prabhjot Singh , Harish Radhakrishna Acharya , Robert James Perry , John Brian McDermott
IPC: B01D53/62
CPC classification number: B01D53/62 , B01D53/1406 , B01D53/1475 , B01D53/343 , B01D53/78 , B01D53/83 , B01D2252/2041 , B01D2252/20421 , B01D2252/20484 , B01D2252/20489 , B01D2257/504 , B01D2258/0283 , B01D2259/65 , Y02C10/04 , Y02C10/06
Abstract: A system and method for treatment of a medium is disclosed. The system includes a plurality of separator zones and a plurality of heat transfer zones. Each of the separator zone and the heat transfer zone among the plurality of separator zones and heat transfer zones respectively, are disposed alternatively in a flow duct. Further, each separator zone includes an injector device for injecting a sorbent into the corresponding separator zone. Within the corresponding separator zone, the injected sorbent is reacted with a gaseous medium flowing in the flow duct, so as to generate a reacted gaseous medium and a reacted sorbent. Further, each heat transfer zone exchanges heat between the reacted gaseous medium fed from the corresponding separator zone and a heat transfer medium.
Abstract translation: 公开了一种处理介质的系统和方法。 该系统包括多个分隔区和多个传热区。 多个分离器区域和传热区域中的分离器区域和传热区域中的每一个分别设置在流动管道中。 此外，每个分离器区域包括用于将吸附剂注入到相应的分离器区域中的注射器装置。 在相应的分离器区域内，注入的吸附剂与在流动管道中流动的气态介质反应，以产生反应的气态介质和反应的吸附剂。 此外，每个传热区域在从相应的分离器区域供给的反应气体介质与传热介质之间交换热量。
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公开(公告)号：US09890183B2
公开(公告)日：2018-02-13
申请号：US14962199
申请日：2015-12-08
Applicant: GENERAL ELECTRIC COMPANY
Inventor： Irina Pavlovna Spiry , Robert James Perry , Benjamin Rue Wood , Surinder Prabhjot Singh , Rachel Lizabeth Farnum , Sarah Elizabeth Genovese
CPC classification number: C07F7/20 , B01D5/0036 , B01D5/009 , B01D53/002 , B01D53/1425 , B01D53/1475 , B01D53/18 , B01D2252/204 , B01D2256/22 , B01D2257/704 , B01D2257/80 , Y02P70/34
Abstract: The present invention is directed to aminosilicone solvent recovery methods and systems. The methods and systems disclosed herein may be used to recover aminosilicone solvent from a carbon dioxide containing vapor stream, for example, a vapor stream that leaves an aminosilicone solvent desorber apparatus. The methods and systems of the invention utilize a first condensation process at a temperature from about 80° C. to about 150° C. and a second condensation process at a temperature from about 5° C. to about 75° C. The first condensation process yields recovered aminosilicone solvent. The second condensation process yields water.
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公开(公告)号：US09764274B2
公开(公告)日：2017-09-19
申请号：US14567319
申请日：2014-12-11
Applicant: General Electric Company
Inventor： Irina Pavlovna Spiry , Benjamin Rue Wood , Surinder Prabhjot Singh , Robert James Perry , John Brian McDermott
CPC classification number: B01D53/1475 , B01D53/1425 , B01D53/62 , B01D53/96 , B01D2252/2026 , B01D2252/20489 , B01D2252/2053 , B01D2257/504 , B01D2258/0283 , Y02C10/06
Abstract: A method for treatment of a flue gas involves feeding the flue gas and a lean solvent to an absorber. The method further involves reacting the flue gas with the lean solvent within the absorber to generate a clean flue gas and a rich solvent. The method also involves feeding the clean flue gas from the absorber and water from a source, to a wash tower to separate a stripped portion of the lean solvent from the clean flue gas to generate a washed clean flue gas and a mixture of the water and the stripped portion of the lean solvent. The method further involves treating at least a portion of the mixture of the water and the stripped portion of the lean solvent via a separation system to separate the water from the stripped portion of the lean solvent.
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公开(公告)号：US20160272896A1
公开(公告)日：2016-09-22
申请号：US15167440
申请日：2016-05-27
Applicant: General Electric Company
CPC classification number: C10G2/34 , C01B3/34 , C01B3/386 , C01B2203/0205 , C01B2203/0261 , C01B2203/062 , C10G2/32 , C10K3/04
Abstract: A carbon to liquids system comprising: a source of syngas; a first reactor coupled in flow communication with said syngas source and configured to receive a flow of syngas therein, said first reactor comprising a polymeric material, wherein said first reactor reacts the syngas and a catalyst in a Fischer-Tropsch reaction that produces a product comprising steam, wherein the polymeric material is configured to permit the permeation of the steam therethrough; and a recycle path coupled in flow communication with said first reactor, wherein said recycle path is configured to channel the permeated steam to a vessel positioned upstream from said first reactor. A method of operating a carbon to liquids system includes receiving a flow of syngas and reacting the syngas and a catalyst to produce a product including steam. The method also includes recycling the permeated steam to a vessel positioned upstream from the reactor.
Abstract translation: 一种碳对液体系统，包括：合成气源; 第一反应器，其与所述合成气源流动连通并且被配置为在其中接收合成气流，所述第一反应器包括聚合材料，其中所述第一反应器在费 - 托反应中反应合成气和催化剂，其产生包含 蒸汽，其中聚合物材料构造成允许蒸汽渗透通过; 以及与所述第一反应器流动连通地联接的再循环路径，其中所述再循环路径构造成将渗透的蒸汽引导到位于所述第一反应器上游的容器。 操作碳对液体系统的方法包括接收合成气流并使合成气和催化剂反应以产生包括蒸汽的产物。 该方法还包括将渗透的蒸汽再循环到位于反应器上游的容器中。
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公开(公告)号：US20160175770A1
公开(公告)日：2016-06-23
申请号：US14578606
申请日：2014-12-22
Applicant: General Electric Company
Inventor： Irina Pavlovna Spiry , Benjamin Rue Wood , John Brian McDermott , Surinder Prabhjot Singh , Sarah Elizabeth Genovese
CPC classification number: B01D53/62 , B01D19/0036 , B01D53/1425 , B01D53/1475 , B01D53/1493 , B01D53/78 , B01D2252/204 , B01D2256/245 , B01D2257/504 , B01D2258/0283 , Y02C10/04 , Y02C10/06
Abstract: A method for separating carbon dioxide (CO2) from a fluid stream comprising CO2 and a liquid solvent is provided. The method includes receiving the fluid stream at a first flashing means to obtain a first CO2 stream and a first CO2 lean fluid stream enriched in the liquid solvent in comparison with the fluid stream. Further, the method also includes receiving the first CO2 lean fluid stream at a second flashing means to obtain a second CO2 stream and a second CO2 lean fluid stream that is enriched in the liquid solvent in comparison with the first CO2 lean fluid stream.
Abstract translation: 提供了一种从包含CO 2和液体溶剂的流体流中分离二氧化碳（CO 2）的方法。 该方法包括在第一闪蒸装置处接收流体流以获得与流体流相比富含液体溶剂的第一CO 2流和第一CO 2贫流体流。 此外，该方法还包括在第二闪蒸装置处接收第一CO 2贫流体流，以获得与第一贫二氧化碳流体流相比富含液体溶剂的第二CO 2流和第二贫二氧化碳流体流。
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