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公开(公告)号:US20090260808A1
公开(公告)日:2009-10-22
申请号:US12425240
申请日:2009-04-16
申请人: Scott Lee Wellington , Mahendra Ladharam Joshi , Jingyu Cui , Stanley Nemec Milam , Michael Anthony Reynolds
发明人: Scott Lee Wellington , Mahendra Ladharam Joshi , Jingyu Cui , Stanley Nemec Milam , Michael Anthony Reynolds
CPC分类号: E21B43/2408 , C09K8/592 , E21B36/02 , E21B43/20 , E21B43/2406 , E21B43/305
摘要: Methods of generating subsurface heat for treating a hydrocarbon containing formation are described herein. The methods include providing a stream that includes water to a plurality of wellbores. Fuel and oxidant is provided to one or more flameless distributed combustors positioned in at least one of the wellbores. The fuel and oxidant is mixed to form a fuel/oxidant mixture. At least a portion of the mixture is flamelessly combusted in at least one of the flameless distributed combustors to generate heat. The fuel includes at least 0.1% hydrogen sulfide by volume.
摘要翻译: 本文描述了产生用于处理含烃地层的地下热的方法。 所述方法包括向多个井筒提供包括水的流。 燃料和氧化剂被提供给位于至少一个井筒中的一个或多个无焰分布式燃烧器。 将燃料和氧化剂混合以形成燃料/氧化剂混合物。 至少一部分混合物在至少一个无焰分布式燃烧器中无焰燃烧以产生热量。 燃料包括至少0.1体积%的硫化氢。
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公开(公告)号:US20110111315A1
公开(公告)日:2011-05-12
申请号:US12797538
申请日:2010-06-09
申请人: Jingyu CUI , Erik Edwin Engwall , John William Johnston , Mahendra Ladharam Joshi , Scott Lee Wellington
发明人: Jingyu CUI , Erik Edwin Engwall , John William Johnston , Mahendra Ladharam Joshi , Scott Lee Wellington
IPC分类号: H01M8/06
CPC分类号: H01M8/0618 , H01M8/0662 , H01M8/14 , H01M2008/147 , Y02E60/526
摘要: The present invention is directed to systems and processes for operating molten carbonate fuel cell systems. A process for operating the molten carbonate fuel cell includes providing a hydrogen-containing stream comprising molecular hydrogen to a molten carbonate fuel cell anode; heating a hydrocarbon stream, at least a majority of which is comprised of hydrocarbons that are liquid at 20° C. and atmospheric pressure, with a heat source comprising an anode exhaust from the molten carbonate fuel cell anode; contacting at least a portion of the heated hydrocarbon stream with a catalyst to produce a steam reforming feed comprising gaseous hydrocarbons, hydrogen, and at least one carbon oxide; separating at least a portion of the molecular hydrogen from the steam reforming feed; and providing at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the stream comprising molecular hydrogen.
摘要翻译: 本发明涉及用于操作熔融碳酸盐燃料电池系统的系统和方法。 用于操作熔融碳酸盐燃料电池的方法包括向熔融碳酸盐燃料电池阳极提供包含分子氢的含氢流; 加热烃流,其至少大部分由在20℃和大气压下为液体的烃组成,热源包括来自熔融碳酸盐燃料电池阳极的阳极排气; 使至少一部分加热的烃流与催化剂接触以产生包含气态烃,氢和至少一种碳氧化物的蒸汽重整进料; 从蒸汽重整进料中分离至少一部分分子氢; 并且将至少一部分分离的分子氢提供给熔融碳酸盐燃料电池阳极,作为包含分子氢的物流的至少一部分。
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公开(公告)号:US20090155644A1
公开(公告)日:2009-06-18
申请号:US12335387
申请日:2008-12-15
IPC分类号: H01M8/04
CPC分类号: H01M8/0618 , C01B3/384 , C01B2203/0233 , C01B2203/0244 , C01B2203/0283 , C01B2203/0405 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0495 , C01B2203/06 , C01B2203/066 , C01B2203/0805 , C01B2203/0811 , C01B2203/1047 , C01B2203/1058 , C01B2203/142 , C01B2203/84 , H01M8/04097 , H01M8/04164 , H01M8/04462 , H01M8/04514 , H01M8/04746 , H01M8/04753 , H01M8/0631 , H01M8/0662 , H01M8/0687 , H01M2008/1293
摘要: The present invention relates to a process for generating electricity with a solid oxide fuel cell system. A liquid hydrocarbon feed is cracked in a first reaction zone, and fed as a gaseous feed to a second reaction zone. The feed is steam reformed in the second reaction zone to provide a reformed product gas containing hydrogen. Hydrogen is separated from the reformed product gas and is fed as a fuel to the anode of a solid oxide fuel cell. Electricity is generated in the fuel cell by oxidizing the hydrogen in the fuel. An anode exhaust stream containing hydrogen and steam is fed back into the first reaction zone to provide heat to drive the endothermic reactions in the first and second reaction zone, and to recycle unused hydrogen back to the fuel cell.
摘要翻译: 本发明涉及一种用固体氧化物燃料电池系统发电的方法。 液体烃进料在第一反应区中裂解,并作为气态进料进料至第二反应区。 进料在第二反应区中进行蒸汽重整,以提供含有氢的重整产物气体。 氢气与重整产物气体分离,并作为燃料供入固体氧化物燃料电池的阳极。 通过氧化燃料中的氢,在燃料电池中产生电。 含有氢气和蒸汽的阳极废气流被反馈到第一反应区以提供热量以驱动第一和第二反应区中的吸热反应,并将未使用的氢气再循环回燃料电池。
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公开(公告)号:US08563186B2
公开(公告)日:2013-10-22
申请号:US12797538
申请日:2010-06-09
申请人: Jingyu Cui , Erik Edwin Engwall , John William Johnston , Mahendra Ladharam Joshi , Scott Lee Wellington
发明人: Jingyu Cui , Erik Edwin Engwall , John William Johnston , Mahendra Ladharam Joshi , Scott Lee Wellington
IPC分类号: H01M8/06
CPC分类号: H01M8/0618 , H01M8/0662 , H01M8/14 , H01M2008/147 , Y02E60/526
摘要: The present invention is directed to systems and processes for operating molten carbonate fuel cell systems. A process for operating the molten carbonate fuel cell includes providing a hydrogen-containing stream comprising molecular hydrogen to a molten carbonate fuel cell anode; heating a hydrocarbon stream, at least a majority of which is comprised of hydrocarbons that are liquid at 20° C. and atmospheric pressure, with a heat source comprising an anode exhaust from the molten carbonate fuel cell anode; contacting at least a portion of the heated hydrocarbon stream with a catalyst to produce a steam reforming feed comprising gaseous hydrocarbons, hydrogen, and at least one carbon oxide; separating at least a portion of the molecular hydrogen from the steam reforming feed; and providing at least a portion of the separated molecular hydrogen to the molten carbonate fuel cell anode as at least a portion of the stream comprising molecular hydrogen.
摘要翻译: 本发明涉及用于操作熔融碳酸盐燃料电池系统的系统和方法。 用于操作熔融碳酸盐燃料电池的方法包括向熔融碳酸盐燃料电池阳极提供包含分子氢的含氢流; 加热烃流,其至少大部分由在20℃和大气压下为液体的烃组成,热源包括来自熔融碳酸盐燃料电池阳极的阳极排气; 使至少一部分加热的烃流与催化剂接触以产生包含气态烃,氢和至少一种碳氧化物的蒸汽重整进料; 从蒸汽重整进料中分离至少一部分分子氢; 并且将至少一部分分离的分子氢提供给熔融碳酸盐燃料电池阳极,作为包含分子氢的物流的至少一部分。
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公开(公告)号:US20110200493A1
公开(公告)日:2011-08-18
申请号:US13092280
申请日:2011-04-22
IPC分类号: B01J19/00
CPC分类号: C01B3/384 , C01B3/48 , C01B3/505 , C01B2203/0233 , C01B2203/0288 , C01B2203/041 , C01B2203/043 , C01B2203/0445 , C01B2203/0475 , C01B2203/0816 , C01B2203/1058 , C01B2203/1211 , C01B2203/1223 , C01B2203/1241 , C01B2203/1288 , C01B2203/86 , Y02P20/129 , Y02P30/30
摘要: This invention relates to a process and apparatus for the production of pure hydrogen by steam reforming. The process integrates the steam reforming and shift reaction to produce pure hydrogen with minimal production of CO and virtually no CO in the hydrogen stream, provides for CO2 capture for sequestration, employs a steam reforming membrane reactor, and is powered by heat from the convection section of a heater.
摘要翻译: 本发明涉及通过蒸汽重整生产纯氢的方法和装置。 该方法集成了蒸汽重整和转移反应,以最少的CO产生和氢流中实际上没有CO,提供CO 2捕集用于封存,采用蒸汽重整膜反应器,并且由来自对流段的热量 的加热器。
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公开(公告)号:US20090260809A1
公开(公告)日:2009-10-22
申请号:US12425248
申请日:2009-04-16
申请人: Scott Lee WELLINGTON , Mahendra Ladharam Joshi , Jingyu Cui , Stanly Nemec Milam , Michael Anthony Reynolds
发明人: Scott Lee WELLINGTON , Mahendra Ladharam Joshi , Jingyu Cui , Stanly Nemec Milam , Michael Anthony Reynolds
CPC分类号: E21B43/243 , E21B36/02
摘要: Methods of generating subsurface heat for treatment of a hydrocarbon containing formation are described herein. Methods include providing steam to at least a portion of a hydrocarbon containing formation from a plurality of locations in a wellbore. The steam is hotter than a temperature of the portion. The steam is heated in the wellbore by combusting a stream comprising hydrogen sulfide in the wellbore. Heat from the combustion transfers to the steam. The steam provided the portion at a first location in the wellbore is hotter than steam provided at a second location in the wellbore along the length of the wellbore, where the first location is further from a surface of the formation than the second location along the length of the wellbore.
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公开(公告)号:US20090155649A1
公开(公告)日:2009-06-18
申请号:US12335375
申请日:2008-12-15
IPC分类号: H01M8/18
CPC分类号: H01M8/0618 , H01M8/04007 , H01M8/04097 , H01M8/04223 , H01M8/04225 , H01M8/0631 , H01M8/0687 , H01M8/243 , H01M8/2432 , H01M2008/1293 , H01M2250/10 , Y02B90/14 , Y02E60/525
摘要: The present invention relates to a solid oxide fuel cell system. The system includes a pre-reforming reactor, a reforming reactor, a hydrogen separation apparatus and a solid oxide fuel cell. The anode exhaust outlet of the solid oxide fuel cell is operatively connected to an inlet of the pre-reforming reactor so anode exhaust from the fuel cell may enter the pre-reforming reactor. The pre-reforming reactor also has an inlet for a hydrocarbon feed precursor. The reforming reactor is operatively coupled to the pre-reforming reactor so that a feed produced in the pre-reforming reactor from the feed precursor may be fed to the reforming reactor. The reforming reactor is operatively connected to the hydrogen separation apparatus so that hydrogen produced in the reforming reactor may be separated from the reformed product gases. The anode inlet of the solid oxide fuel cell is operatively connected to the hydrogen separation apparatus so hydrogen may be fed from the hydrogen separation apparatus as fuel to the solid oxide fuel cell.
摘要翻译: 本发明涉及一种固体氧化物燃料电池系统。 该系统包括预重整反应器,重整反应器,氢分离装置和固体氧化物燃料电池。 固体氧化物燃料电池的阳极排气出口可操作地连接到预重整反应器的入口,从而来自燃料电池的阳极排气可以进入预重整反应器。 预重整反应器还具有用于烃进料前体的入口。 重整反应器可操作地耦合到预重整反应器,使得在来自进料前体的预重整反应器中产生的进料可以进料到重整反应器。 重整反应器可操作地连接到氢分离装置,使得在重整反应器中产生的氢可以与重整产物气体分离。 固体氧化物燃料电池的阳极入口可操作地连接到氢气分离装置,从而可以从氢气分离装置将氢气作为燃料供给到固体氧化物燃料电池。
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公开(公告)号:US09017434B2
公开(公告)日:2015-04-28
申请号:US13092280
申请日:2011-04-22
CPC分类号: C01B3/384 , C01B3/48 , C01B3/505 , C01B2203/0233 , C01B2203/0288 , C01B2203/041 , C01B2203/043 , C01B2203/0445 , C01B2203/0475 , C01B2203/0816 , C01B2203/1058 , C01B2203/1211 , C01B2203/1223 , C01B2203/1241 , C01B2203/1288 , C01B2203/86 , Y02P20/129 , Y02P30/30
摘要: This invention relates to a process and apparatus for the production of pure hydrogen by steam reforming. The process integrates the steam reforming and shift reaction to produce pure hydrogen with minimal production of CO and virtually no CO in the hydrogen stream, provides for CO2 capture for sequestration, employs a steam reforming membrane reactor, and is powered by heat from the convection section of a heater.
摘要翻译: 本发明涉及通过蒸汽重整生产纯氢的方法和装置。 该方法集成了蒸汽重整和转移反应,以最少的CO产生和氢流中实际上没有CO,提供CO 2捕集用于封存,采用蒸汽重整膜反应器,并且由来自对流段的热量 的加热器。
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公开(公告)号:US20090180949A1
公开(公告)日:2009-07-16
申请号:US12353588
申请日:2009-01-14
CPC分类号: C01B3/384 , C01B3/48 , C01B3/505 , C01B2203/0233 , C01B2203/0288 , C01B2203/041 , C01B2203/043 , C01B2203/0445 , C01B2203/0475 , C01B2203/0816 , C01B2203/1058 , C01B2203/1211 , C01B2203/1223 , C01B2203/1241 , C01B2203/1288 , C01B2203/86 , Y02P20/129 , Y02P30/30
摘要: This invention relates to a process and apparatus for the production of pure hydrogen by steam reforming. The process integrates the steam reforming and shift reaction to produce pure hydrogen with minimal production of CO and virtually no CO in the hydrogen stream, provides for CO2 capture for sequestration, employs a steam reforming membrane reactor, and is powered by heat from the convection section of a heater.
摘要翻译: 本发明涉及通过蒸汽重整生产纯氢的方法和装置。 该方法集成了蒸汽重整和转移反应,以最少的CO产生和氢流中实际上没有CO,提供CO 2捕集用于封存,采用蒸汽重整膜反应器,并且由来自对流段的热量 的加热器。
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公开(公告)号:US07959897B2
公开(公告)日:2011-06-14
申请号:US12353588
申请日:2009-01-14
CPC分类号: C01B3/384 , C01B3/48 , C01B3/505 , C01B2203/0233 , C01B2203/0288 , C01B2203/041 , C01B2203/043 , C01B2203/0445 , C01B2203/0475 , C01B2203/0816 , C01B2203/1058 , C01B2203/1211 , C01B2203/1223 , C01B2203/1241 , C01B2203/1288 , C01B2203/86 , Y02P20/129 , Y02P30/30
摘要: This invention relates to a process and apparatus for the production of pure hydrogen by steam reforming. The process integrates the steam reforming and shift reaction to produce pure hydrogen with minimal production of CO and virtually no CO in the hydrogen stream, provides for CO2 capture for sequestration, employs a steam reforming membrane reactor, and is powered by heat from the convection section of a heater.
摘要翻译: 本发明涉及通过蒸汽重整生产纯氢的方法和装置。 该方法集成了蒸汽重整和转移反应,以最少的CO产生和氢流中实际上没有CO,提供CO 2捕集用于封存,采用蒸汽重整膜反应器,并且由来自对流段的热量 的加热器。
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