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公开(公告)号：US11967745B2
公开(公告)日：2024-04-23
申请号：US17730942
申请日：2022-04-27
IPC分类号： H01M8/0656 , B01J8/00 , C01B3/26 , C01B32/50 , C25B1/04 , C25B9/65 , C25B9/67 , F01K25/06 , H01M8/12 , H01M8/1233
CPC分类号： H01M8/0656 , B01J8/005 , C01B3/26 , C01B32/50 , C25B1/04 , C25B9/65 , C25B9/67 , F01K25/06 , H01M8/1233 , B01J2208/00106 , C01B2203/0277 , C01B2203/066 , C01B2203/1235 , C01B2203/84 , C01B2203/86 , H01M2008/1293
摘要： A hydrocarbon feed stream is exposed to heat in an absence of oxygen (pyrolysis) to convert the hydrocarbon feed stream into a solids stream and a gas stream. The solids stream includes carbon. The gas stream includes hydrogen. The gas stream is separated into an exhaust gas stream and a first hydrogen stream. The first hydrogen stream includes at least a portion of the hydrogen from the gas stream. The carbon is separated from the solids stream to produce a carbon stream. Electrolysis is performed on a water stream to produce an oxygen stream and a second hydrogen stream. At least a portion of the oxygen of the oxygen stream and at least a portion of the carbon of the carbon stream are combined to generate power and a carbon dioxide stream. At least a portion of the generated power is used to perform the electrolysis on the water stream.
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公开(公告)号：US20230349015A1
公开(公告)日：2023-11-02
申请号：US17731062
申请日：2022-04-27
CPC分类号： C21C5/52 , C01B3/26 , B01J8/005 , F02C1/05 , C01B2203/066 , C01B2203/0277 , B01J2208/00106 , C01B2203/84 , C01B2203/86 , C01B2203/1235 , C25B1/04
摘要： A hydrocarbon feed stream is exposed to heat in an absence of oxygen to the convert the hydrocarbon feed stream into a solids stream and a gas stream. The gas stream is separated into an exhaust gas stream and a first hydrogen stream. The carbon is separated from the solids stream to produce a carbon stream. Electrolysis is performed on a water stream to produce an oxygen stream and a second hydrogen stream. An iron ore is reduced by flowing hydrogen across the iron ore to produce iron. The iron and a first portion of the carbon of the carbon stream are combined to produce steel. At least a portion of the oxygen of the oxygen stream and a second portion of the carbon of the carbon stream are combined to generate power and a carbon dioxide stream.
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3.发明申请公开(公告)号：US20180261861A1
公开(公告)日：2018-09-13
申请号：US15977061
申请日：2018-05-11
发明人： Aqil Jamal , Thang Pham
IPC分类号： H01M8/0612 , B65B1/00 , H01M8/0656 , H01M8/0637 , H01M8/04082 , H01M8/1231 , H01M8/12 , F17C5/06 , B60L11/18 , C01B3/56 , C01B3/48 , C01B3/38
CPC分类号： H01M8/0618 , B60L11/1883 , B65B1/00 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/0455 , C01B2203/0485 , C01B2203/066 , C01B2203/0811 , C01B2203/1258 , C01B2203/1288 , C01B2203/141 , C01B2203/148 , F17C5/06 , H01M8/04097 , H01M8/04201 , H01M8/0637 , H01M8/0656 , H01M8/0662 , H01M8/0668 , H01M8/0675 , H01M8/12 , H01M8/1231 , H01M2008/1293 , H01M2250/10 , H01M2250/20 , H01M2300/0074 , Y02B90/14 , Y02E60/321 , Y02E60/50 , Y02E60/525 , Y02P30/30 , Y02T90/32 , Y02T90/34
摘要： A solid oxide fuel cell (SOFC) system including a steam reformer, a hydrogen purification system, a pre-reformer, and a solid oxide fuel cell.
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公开(公告)号：US09647286B2
公开(公告)日：2017-05-09
申请号：US13678942
申请日：2012-11-16
发明人： Aqil Jamal , Thang Pham , Aadesh Harale
IPC分类号： H01M8/06 , H01M8/0662 , H01M8/0612 , H01M8/18 , E21B43/16 , H01M8/0668 , H01M8/04089 , E21B43/34 , C01B31/20 , C01B3/38 , H01M8/124
CPC分类号： H01M8/0675 , C01B3/38 , C01B3/48 , C01B32/50 , C01B2203/0233 , C01B2203/0261 , C01B2203/0283 , C01B2203/04 , C01B2203/0475 , C01B2203/066 , E21B43/164 , E21B43/34 , E21B43/40 , H01M8/04097 , H01M8/0618 , H01M8/0637 , H01M8/0668 , H01M8/0681 , H01M8/0687 , H01M8/18 , H01M2008/1293 , Y02P90/70
摘要： A method for producing a purified carbon dioxide product suitable for EOR and surplus electricity uses a vaporous hydrocarbon feed and a SOFC system. A SOFC system includes a condensate removal system, an acid gas removal system, a hydrodesulfurization system, a sorption bed system, a pre-reformer, a solid oxide fuel cell, a CO2 separations system and a CO2 dehydration system operable to form the purified carbon dioxide product, where the SOFC system is operable to produce surplus electricity from the electricity produced by the solid oxide fuel cell. A method of operating the pre-reformer to maximize the internal reforming capacity of a downstream solid oxide fuel cell uses a pre-reformer fluidly coupled on the upstream side of a solid oxide fuel cell. A method of enhancing hydrocarbon fluid recovery from a hydrocarbon-bearing formation using a SOFC system.
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公开(公告)号：US20220285712A1
公开(公告)日：2022-09-08
申请号：US17191992
申请日：2021-03-04
发明人： Kunho Lee , Aadesh Harale , Thang Pham , Aqil Jamal , Ahmad O. Khowaiter
IPC分类号： H01M8/0612 , H01M8/0662 , H01M8/1231 , H01M8/04014 , B01D53/04 , B01D53/22 , B01D71/02 , C01B3/48 , B01J23/755 , B01J23/745 , C01B3/56
摘要： A method and a system for the coproduction of hydrogen, electrical power, and heat energy. An exemplary method includes desulfurizing a feed stream to form a desulfurized feed stream, reforming the desulfurized feed stream to form a methane rich gas, and providing the methane rich gas to a membrane separator. A hydrogen stream is produced in a permeate from the membrane separator. A retentate stream from the membrane separator is provided to a solid oxide fuel cell (SOFC). Electrical power is produced in the SOFC from the retentate stream.
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公开(公告)号：US20180048007A1
公开(公告)日：2018-02-15
申请号：US15794947
申请日：2017-10-26
发明人： Aqil Jamal , Thang Pham
CPC分类号： H01M8/0618 , B60L11/1883 , B65B1/00 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/0455 , C01B2203/0485 , C01B2203/066 , C01B2203/0811 , C01B2203/1258 , C01B2203/1288 , C01B2203/141 , C01B2203/148 , F17C5/06 , H01M8/04097 , H01M8/04201 , H01M8/0637 , H01M8/0656 , H01M8/0662 , H01M8/0668 , H01M8/0675 , H01M8/12 , H01M8/1231 , H01M2008/1293 , H01M2250/10 , H01M2250/20 , H01M2300/0074 , Y02B90/14 , Y02E60/321 , Y02E60/50 , Y02E60/525 , Y02P30/30 , Y02T90/32 , Y02T90/34
摘要： Disclosed is an alternative fuel fueling station useful for fueling both electrical and hydrogen alternative fuel vehicles simultaneously. The alternative fuel fueling station includes a solid oxide fuel cell, an electrical conduit, and a compressed hydrogen conduit, such that the alternative fuel fueling station can fuel both the electrical and hydrogen alternative fuel vehicles simultaneously.
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7.发明授权公开(公告)号：US09365131B2
公开(公告)日：2016-06-14
申请号：US13683272
申请日：2012-11-21
发明人： Aqil Jamal , Thang Pham
IPC分类号： H01M8/06 , B65B1/00 , B60L11/18 , C01B3/38 , C01B3/48 , C01B3/56 , F17C5/06 , H01M8/12 , H01M8/04
CPC分类号： H01M8/0618 , B60L11/1883 , B65B1/00 , C01B3/382 , C01B3/384 , C01B3/48 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/0455 , C01B2203/0485 , C01B2203/066 , C01B2203/0811 , C01B2203/1258 , C01B2203/1288 , C01B2203/141 , C01B2203/148 , F17C5/06 , H01M8/04097 , H01M8/04201 , H01M8/0637 , H01M8/0656 , H01M8/0662 , H01M8/0668 , H01M8/0675 , H01M8/12 , H01M8/1231 , H01M2008/1293 , H01M2250/10 , H01M2250/20 , H01M2300/0074 , Y02B90/14 , Y02E60/321 , Y02E60/50 , Y02E60/525 , Y02T90/32 , Y02T90/34
摘要： A SOFC system for producing a refined carbon dioxide product, electrical power and a compressed hydrogen product is presented. Introducing a hydrocarbon fuel and steam to the SOFC system, operating the SOFC system such that the steam-to-carbon molar ratio in the pre-reformer is in a range of from about 3:1 to about 4:1, the oxygen in the reformer combustion chamber is in excess, greater than 90% of the carbon dioxide produced during the process forms the refined carbon dioxide product are steps in the process. An alternative fueling station having a SOFC system is useful for fueling both electrical and hydrogen alternative fuel vehicles. Introducing steam and a hydrocarbon fuel, operating the alternative fueling station, coupling the alternative fuel vehicle to the alternative fueling station, introducing an amount of alternative fuel and decoupling the alternative fuel vehicle are steps in the method of use.
摘要翻译： 提出了一种用于生产精炼二氧化碳产品，电力和压缩氢产品的SOFC系统。 向SOFC系统引入烃燃料和蒸汽，操作SOFC系统，使得预重整器中的蒸汽 - 碳摩尔比在约3:1至约4:1的范围内， 重整器燃烧室过量，在该过程中产生的大于90％的二氧化碳形成精制二氧化碳产物是该过程中的步骤。 具有SOFC系统的替代燃料加油站对于燃料电动和氢替代燃料车辆是有用的。 引入蒸汽和烃燃料，操作备用加油站，将替代燃料车辆连接到替代燃料加油站，引入一定数量的替代燃料和解耦替代燃料车辆是使用方法中的步骤。
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公开(公告)号：US20230163335A1
公开(公告)日：2023-05-25
申请号：US18096956
申请日：2023-01-13
发明人： Kunho Lee , Aadesh Harale , Thang Pham , Aqil Jamal , Ahmad O. Khowaiter
IPC分类号： H01M8/0612 , H01M8/1231 , B01D53/04 , B01D53/22 , B01D71/02 , B01J23/745 , B01J23/755 , C01B3/48 , C01B3/56 , H01M8/04014 , H01M8/0662 , C01B3/50
CPC分类号： H01M8/0618 , H01M8/1231 , B01D53/04 , B01D53/229 , B01D71/021 , B01D71/022 , B01D71/028 , B01J23/745 , B01J23/755 , C01B3/48 , C01B3/56 , H01M8/04014 , H01M8/0687 , H01M8/0675 , C01B3/501 , B01D2256/16 , B01D2257/302 , C01B2203/0233 , C01B2203/0283 , C01B2203/066 , C01B2203/0894 , C01B2203/1058 , C01B2203/1241 , C01B2203/127 , C01B2203/84 , H01M2008/1293
摘要： A method and a system for the coproduction of hydrogen, electrical power, and heat energy. An exemplary method includes desulfurizing a feed stream to form a desulfurized feed stream, reforming the desulfurized feed stream to form a methane rich gas, and providing the methane rich gas to a membrane separator. A hydrogen stream is produced in a permeate from the membrane separator. A retentate stream from the membrane separator is provided to a solid oxide fuel cell (SOFC). Electrical power is produced in the SOFC from the retentate stream.
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公开(公告)号：US10014541B2
公开(公告)日：2018-07-03
申请号：US15474805
申请日：2017-03-30
发明人： Aqil Jamal , Thang Pham , Aadesh Harale
IPC分类号： H01M8/06 , H01M8/0662 , H01M8/0612 , H01M8/18 , E21B43/16 , H01M8/0668 , H01M8/04089 , E21B43/34 , C01B3/38 , C01B3/48 , E21B43/40 , H01M8/0637 , C01B32/50 , H01M8/124
CPC分类号： H01M8/0675 , C01B3/38 , C01B3/48 , C01B32/50 , C01B2203/0233 , C01B2203/0261 , C01B2203/0283 , C01B2203/04 , C01B2203/0475 , C01B2203/066 , E21B43/164 , E21B43/34 , E21B43/40 , H01M8/04097 , H01M8/0618 , H01M8/0637 , H01M8/0668 , H01M8/0681 , H01M8/0687 , H01M8/18 , H01M2008/1293 , Y02P90/70
摘要： A method for producing a purified carbon dioxide product suitable for EOR and surplus electricity uses a vaporous hydrocarbon feed and a SOFC system. A SOFC system includes a condensate removal system, an acid gas removal system, a hydrodesulfurization system, a sorption bed system, a pre-reformer, a solid oxide fuel cell, a CO2 separations system and a CO2 dehydration system operable to form the purified carbon dioxide product, where the SOFC system is operable to produce surplus electricity from the electricity produced by the solid oxide fuel cell. A method of operating the pre-reformer to maximize the internal reforming capacity of a downstream solid oxide fuel cell uses a pre-reformer fluidly coupled on the upstream side of a solid oxide fuel cell. A method of enhancing hydrocarbon fluid recovery from a hydrocarbon-bearing formation using a SOFC system.
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公开(公告)号：US20240222669A1
公开(公告)日：2024-07-04
申请号：US18608089
申请日：2024-03-18
IPC分类号： H01M8/0656 , B01J8/00 , C01B3/26 , C01B32/50 , C25B1/04 , C25B9/65 , C25B9/67 , F01K25/06 , H01M8/12 , H01M8/1233
CPC分类号： H01M8/0656 , B01J8/005 , C01B3/26 , C01B32/50 , C25B1/04 , C25B9/65 , C25B9/67 , F01K25/06 , H01M8/1233 , B01J2208/00106 , C01B2203/0277 , C01B2203/066 , C01B2203/1235 , C01B2203/84 , C01B2203/86 , H01M2008/1293
摘要： A hydrocarbon feed stream is exposed to heat in an absence of oxygen (pyrolysis) to convert the hydrocarbon feed stream into a solids stream and a gas stream. The solids stream includes carbon. The gas stream includes hydrogen. The gas stream is separated into an exhaust gas stream and a first hydrogen stream. The first hydrogen stream includes at least a portion of the hydrogen from the gas stream. The carbon is separated from the solids stream to produce a carbon stream. Electrolysis is performed on a water stream to produce an oxygen stream and a second hydrogen stream. At least a portion of the oxygen of the oxygen stream and at least a portion of the carbon of the carbon stream are combined to generate power and a carbon dioxide stream. At least a portion of the generated power is used to perform the electrolysis on the water stream.
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