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91. 发明申请

US20100122627A1 MEMBRANE-BASED SYSTEMS AND METHODS FOR HYDROGEN SEPARATION 审中-公开
标题翻译：基于膜的系统和氢分离方法
公开(公告)号：US20100122627A1
公开(公告)日：2010-05-20
申请号：US12270890
申请日：2008-11-14
申请人： Joseph Michael Schwartz , Raymond Francis Drnevich , Jerome Thomas Jankowiak , Dante Patrick Bonaquist
发明人： Joseph Michael Schwartz , Raymond Francis Drnevich , Jerome Thomas Jankowiak , Dante Patrick Bonaquist
IPC分类号： B01D46/46 , B01D53/22
CPC分类号： B01D53/22 , B01D71/028 , B01D2256/16 , B01D2323/08 , B01D2325/22 , C01B3/34 , C01B3/36 , C01B3/38 , C01B3/382 , C01B3/48 , C01B3/501 , C01B3/503 , C01B2203/0205 , C01B2203/0244 , C01B2203/0255 , C01B2203/0261 , C01B2203/0283 , C01B2203/0405 , C01B2203/0445 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0811 , C01B2203/0822 , C01B2203/0883 , C01B2203/0894 , C01B2203/1258 , C01B2203/84 , Y02P20/128
摘要： According to some embodiments, a method and a system are provided to receive hydrogen at a first pressure at a first side of a membrane, receive hydrogen at a second pressure from a second side of the membrane, combine the hydrogen received from the second side of the membrane with a purge stream to produce a permeate stream at the second pressure, and separate hydrogen from the permeate stream at a third pressure. The purge stream is associated with a phase transition temperature range.
摘要翻译：根据一些实施例，提供了一种方法和系统以在膜的第一侧处以第一压力接收氢气，在来自膜的第二侧的第二压力下接收氢气，将从第二侧接收的氢，所述膜具有吹扫流以在第二压力下产生渗透物流，并在第三压力下从渗透物流中分离出氢。吹扫流与相变温度范围相关联。

92. 发明申请

US20100113623A1 SYSTEMS, METHODS, AND COMPOSITIONS FOR PRODUCTION OF SYNTHETIC HYDROCARBON COMPOUNDS 有权
标题翻译：用于生产合成碳氢化合物的系统，方法和组合物
公开(公告)号：US20100113623A1
公开(公告)日：2010-05-06
申请号：US12647121
申请日：2009-12-24
申请人： Alexander J. SEVERINSKY
发明人： Alexander J. SEVERINSKY
IPC分类号： C07C1/12
CPC分类号： C10G2/32 , C10G2/30 , C10G2300/1022 , C10J3/18 , C10J2300/093 , C10J2300/1238 , C10J2300/1659 , C25B1/04 , C25B15/08 , Y02E60/364 , Y02E60/366 , Y02E70/10 , Y02P20/128 , Y02P20/129 , Y02P20/133
摘要： A process and system for producing hydrocarbon compounds or fuels that recycle products of hydrocarbon compound combustion—carbon dioxide or carbon monoxide, or both, and water. The energy for recycling is electricity derived from preferably not fossil based fuels, like from nuclear fuels or from renewable energy. The process comprises electrolysing water, and then using hydrogen to reduce externally supplied carbon dioxide to carbon monoxide, then using so produced carbon monoxide together with any externally supplied carbon monoxide and hydrogen in Fischer-Tropsch reactors, with upstream upgrading to desired specification fuels—for example, gasoline, jet fuel, kerosene, diesel fuel, and others. Energy released in some of these processes is used by other processes. Using adiabatic temperature changes and isothermal pressure changes for gas processing and separation, large amounts of required energy are internally recycled using electric and heat distribution lines. Phase conversion of working fluid is used in heat distribution lines for increased energy efficiency. The resulting use of electric energy is less than 1.4 times the amount of the high heating value of combustion of so produced hydrocarbon compounds when carbon dioxide is converted to carbon monoxide in the invention, and less than 0.84 when carbon monoxide is the source.
摘要翻译：用于生产烃化合物燃烧二氧化碳或一氧化碳或二氧化碳或水的产物的烃化合物或燃料的方法和系统。回收利用的能源是优选不是以化石为基础的燃料，如核燃料或可再生能源。该方法包括电解水，然后使用氢气将外部供应的二氧化碳减少到一氧化碳，然后在费 - 托反应器中使用这样生产的一氧化碳和任何外部提供的一氧化碳和氢气，并将其上游升级为所需规格的燃料 - 用于例如汽油，喷气燃料，煤油，柴油等。在其中一些过程中释放的能量被其他过程所使用。使用绝热温度变化和气体处理和分离的等温压力变化，使用电力和热分配管线在内部回收大量所需的能量。工作流体的相转化用于配电线路，以提高能源效率。所得到的电能的使用量小于本发明中二氧化碳转化成一氧化碳时所产生的碳氢化合物燃烧的高热值的量的1.4倍，当一氧化碳为源时小于0.84。

93. 发明申请

US20100111783A1 SYSTEMS, METHODS, AND COMPOSITIONS FOR PRODUCTION OF SYNTHETIC HYDROCARBON COMPOUNDS 审中-公开
公开(公告)号：US20100111783A1
公开(公告)日：2010-05-06
申请号：US12647178
申请日：2009-12-24
申请人： Alexander J. SEVERINSKY
发明人： Alexander J. SEVERINSKY
IPC分类号： B01J19/00
CPC分类号： C10G2/32 , C10G2/30 , C10G2300/1022 , C10J3/18 , C10J2300/093 , C10J2300/1238 , C10J2300/1659 , C25B1/04 , C25B15/08 , Y02E60/364 , Y02E60/366 , Y02E70/10 , Y02P20/128 , Y02P20/129 , Y02P20/133
摘要： A process and system for producing hydrocarbon compounds or fuels that recycle products of hydrocarbon compound combustion—carbon dioxide or carbon monoxide, or both, and water. The energy for recycling is electricity derived from preferably not fossil based fuels, like from nuclear fuels or from renewable energy. The process comprises electrolysing water, and then using hydrogen to reduce externally supplied carbon dioxide to carbon monoxide, then using so produced carbon monoxide together with any externally supplied carbon monoxide and hydrogen in Fischer-Tropsch reactors, with upstream upgrading to desired specification fuels—for example, gasoline, jet fuel, kerosene, diesel fuel, and others. Energy released in some of these processes is used by other processes. Using adiabatic temperature changes and isothermal pressure changes for gas processing and separation, large amounts of required energy are internally recycled using electric and heat distribution lines. Phase conversion of working fluid is used in heat distribution lines for increased energy efficiency. The resulting use of electric energy is less than 1.4 times the amount of the high heating value of combustion of so produced hydrocarbon compounds when carbon dioxide is converted to carbon monoxide in the invention, and less than 0.84 when carbon monoxide is the source.

94. 发明申请

US20100104499A1 Zero Steam Export With CO2 Recovery In A High Thermal Efficiency Hydrogen Plant 有权
标题翻译：零蒸汽出口在高热效率氢厂的二氧化碳回收
公开(公告)号：US20100104499A1
公开(公告)日：2010-04-29
申请号：US12608573
申请日：2009-10-29
申请人： Bhadra S. Grover
发明人： Bhadra S. Grover
IPC分类号： C01B3/26 , C01B3/24
CPC分类号： C01B3/38 , C01B3/48 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/0816 , C01B2203/0822 , C01B2203/0827 , C01B2203/0894 , C01B2203/1047 , C01B2203/1076 , C01B2203/1241 , C01B2203/1247 , C01B2203/1258 , C01B2203/1294 , C01B2203/148 , C01B2203/86 , Y02P20/128 , Y02P30/30
摘要： A high thermal efficiency process for hydrogen recovery is provided. The present invention includes combusting a first fuel stream to a reforming furnace, producing reforming heat and a hot exhaust stream. Then exchanging heat indirectly between the hot exhaust stream and a first feed water stream, producing a first steam stream. Then providing a hydrocarbon containing stream and a feed steam stream to the reforming furnace, utilizing the reforming heat and producing a hot raw syngas stream. Then exchanging heat indirectly between the hot raw syngas stream and second feedwater stream, producing a second steam stream and a cooled, raw syngas stream. Then introducing the cooled, raw syngas stream to a CO shift converter, producing a shifted syngas stream. Then introducing the shifted syngas stream into a pressure swing adsorption unit, producing a hydrogen product stream and a tail gas stream. Then introducing the tail gas stream to a CO2 removal unit, producing a CO2 stream and a recycle stream; compressing the recycle stream, producing a compressed recycle stream. Then combining the compressed recycle stream with at least one stream selected from the group consisting of the hydrocarbon containing stream, the cooled raw syngas stream, the shifted syngas stream, and the tail gas stream. Then combining the first steam stream and the second steam stream, producing the feed steam stream.
摘要翻译：提供了用于氢回收的高热效率方法。本发明包括将第一燃料流燃烧到重整炉，产生重整热和热排气流。然后间接地在热排气流和第一给水流之间进行热交换，产生第一蒸汽流。然后向重整炉提供含烃流和进料蒸汽流，利用重整热并产生热原始合成气流。然后间接地在热原料合成气流和第二给水流之间进行热交换，产生第二蒸汽流和冷却的原始合成气流。然后将冷却的原始合成气流引入CO移位转换器，产生位移合成气流。然后将转换的合成气流引入变压吸附单元，产生氢产物流和尾气流。然后将尾气流引入CO 2去除单元，产生CO 2流和再循环流; 压缩循环流，产生压缩的再循环流。然后将压缩的再循环料流与选自含烃的料流，冷却的原料合成气物流，转换的合成气物流和尾气流中的至少一种物流组合。然后组合第一蒸汽流和第二蒸汽流，产生进料蒸汽流。

95. 发明授权

US07704485B1 System and method for processing fuel for use by a fuel cell using a micro-channel catalytic hydrogen separator 有权
标题翻译：用于处理使用微通道催化氢分离器的燃料电池使用的燃料的系统和方法
公开(公告)号：US07704485B1
公开(公告)日：2010-04-27
申请号：US11341541
申请日：2006-01-27
申请人： Peter R. Bossard , Jacques Mettes
发明人： Peter R. Bossard , Jacques Mettes
IPC分类号： C01B3/26 , C01B3/24 , C01D7/00
CPC分类号： C01B3/505 , B01D2257/108 , C01B3/32 , C01B3/34 , C01B3/48 , C01B3/501 , C01B3/503 , C01B3/586 , C01B2203/0205 , C01B2203/0283 , C01B2203/0405 , C01B2203/044 , C01B2203/0445 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/066 , C01B2203/0816 , C01B2203/0822 , C01B2203/0827 , C01B2203/085 , C01B2203/1211 , C01B2203/1217 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/1294 , C01B2203/145 , C01B2203/82 , H01M8/04022 , H01M8/04156 , H01M8/0612 , H01M8/0687 , Y02P20/128
摘要： A power generation system and a fuel processor for use within a power generation system. A common hydrocarbon fuel is introduced into the heated reaction chamber along with water vapor. The hydrocarbon fuel and water react, producing less complex resultant gases. The resultant gases are passed into a hydrogen separator. The hydrogen separator separates hydrogen from the resultant gases. The separated hydrogen is used to power a fuel cell. The fuel cell produces electricity and water that can be recycled back into the system. A standard hydrocarbon fuel can therefore be used to power a fuel cell in a highly efficient, singe-step process.
摘要翻译：一种在发电系统内使用的发电系统和燃料处理器。常见的烃类燃料与水蒸气一起被引入加热的反应室中。碳氢化合物燃料和水反应，产生较少复杂的合成气体。将所得气体送入氢气分离器。氢气分离器从产生的气体中分离出氢气。分离的氢气用于为燃料电池供电。燃料电池产生可以再循环回系统的电力和水。因此，标准碳氢化合物燃料可以用于以高效，单步骤过程为燃料电池供电。

96. 发明授权

US07699975B2 Method and system of heating a fluid catalytic cracking unit for overall CO2 reduction 有权
标题翻译：加热流化催化裂化装置以减少总体CO2的方法和系统
公开(公告)号：US07699975B2
公开(公告)日：2010-04-20
申请号：US11962810
申请日：2007-12-21
申请人： Brian W. Hedrick
发明人： Brian W. Hedrick
IPC分类号： C10G51/04
CPC分类号： C10G11/182 , B01J29/90 , B01J38/30 , C01B3/26 , C01B3/30 , C01B2203/0277 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0465 , C01B2203/0475 , C01B2203/0485 , C01B2203/0811 , C01B2203/0822 , C01B2203/0883 , C10G11/185 , C10J3/482 , C10J2300/16 , C10J2300/1618 , C10J2300/1671 , F01K13/00 , Y02E20/344 , Y02P20/128 , Y02P20/52 , Y02P20/584 , Y02P30/30 , Y02P30/446
摘要： In at least one embodiment of the present invention, a method of heating a FCC unit having a regenerator and a reactor for over CO2 reduction is provided. The method comprises compressing syngas to define compressed syngas. CO2 is separated from the compressed syngas to provide a first stream of gas comprising CO2. The first stream of gas is expanded with a second stream of gas comprising O2 to define a feed gas. The feed gas and an injected hydrocarbon feed are introduced to the regenerator having spent catalyst from the reactor. The regenerator is at gasification conditions to burn the injected hydrocarbon feed and coke from the spent catalyst producing the syngas and heat for operating the reactor at reaction temperatures.
摘要翻译：在本发明的至少一个实施方案中，提供了一种加热具有再生器的FCC单元和用于二氧化碳还原的反应器的方法。该方法包括压缩合成气以限定压缩的合成气。 CO 2与压缩的合成气分离以提供包含CO 2的第一气体流。第一气体气体用包含O 2的第二气体气流扩张以限定进料气体。将进料气体和注入的烃进料从反应器引入到具有废催化剂的再生器中。再生器在气化条件下燃烧注入的烃进料和来自废催化剂的焦炭，产生合成气，并在反应温度下操作反应器的热量。

97. 发明授权

US07699907B2 Apparatus and methods for gas separation 失效
标题翻译：气体分离装置和方法
公开(公告)号：US07699907B2
公开(公告)日：2010-04-20
申请号：US11463065
申请日：2006-08-08
申请人： Bhadra S. Grover , Paul Wentink
发明人： Bhadra S. Grover , Paul Wentink
IPC分类号： B01D53/02
CPC分类号： B01D53/047 , B01D2256/16 , B01D2257/502 , B01D2257/504 , B01D2257/702 , B01D2257/7025 , B01D2259/4003 , B01D2259/40052 , B01D2259/40064 , B01D2259/402 , B01D2259/404 , C01B3/384 , C01B3/48 , C01B3/56 , C01B2203/0233 , C01B2203/0283 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0816 , C01B2203/0822 , C01B2203/0827 , C01B2203/1058 , C01B2203/148 , C01B2203/84 , Y02C10/08 , Y02C20/20 , Y02P20/128 , Y02P20/152 , Y02P20/156
摘要： Methods and systems for producing hydrogen are provided. In one embodiment, a method of producing hydrogen comprises reacting a feed source with steam to produce a gas mixture containing hydrogen and a residue gas; introducing the gas mixture into a purification unit; adsorbing the residue gas; and discharging at least a portion of the hydrogen. The method further comprises depressurizing the purification unit; discharging at least a portion of the residue gas during the depressurization; recycling the residue gas to the feed source; and discharging the residue gas remaining in the purification unit. In another embodiment, the method includes discharging a portion of the residue gas during the depressurization such that the residue gas discharged has a higher hydrocarbon content than the secondary product remaining in the purification unit.
摘要翻译：提供了生产氢气的方法和系统。在一个实施方案中，生产氢的方法包括使进料源与蒸汽反应以产生含有氢气和残余气体的气体混合物; 将气体混合物引入净化单元; 吸附残留气体; 并排出至少一部分氢。该方法还包括使净化单元减压; 在减压期间排出至少一部分残余气体; 将残余气体再循环到进料源; 并排出残留在净化单元中的残留气体。在另一个实施方案中，该方法包括在减压期间排出一部分残余气体，使得排出的残余气体的烃含量高于残留在净化单元中的次级产物。

98. 发明申请

US20100086478A1 HYDROGEN-PRODUCING FUEL PROCESSING ASSEMBLIES, HEATING ASSEMBLIES, AND METHODS OF OPERATING THE SAME 有权
标题翻译：生产燃料的加氢装置，加热装置及其操作方法
公开(公告)号：US20100086478A1
公开(公告)日：2010-04-08
申请号：US12636445
申请日：2009-12-11
申请人： David J. Edlund
发明人： David J. Edlund
IPC分类号： C01B3/24
CPC分类号： H01M8/0618 , C01B3/323 , C01B3/38 , C01B3/48 , C01B2203/0233 , C01B2203/0244 , C01B2203/0261 , C01B2203/0283 , C01B2203/04 , C01B2203/0405 , C01B2203/043 , C01B2203/047 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/066 , C01B2203/0811 , C01B2203/0822 , C01B2203/0827 , C01B2203/085 , C01B2203/0866 , C01B2203/1217 , C01B2203/1223 , C01B2203/1229 , C01B2203/1241 , C01B2203/1247 , C01B2203/1252 , C01B2203/1276 , C01B2203/1288 , C01B2203/16 , C01B2203/1604 , C01B2203/169 , C01B2203/1695 , Y02P20/128
摘要： Combustion-based heating assemblies and hydrogen-producing fuel processing assemblies that include at least a reforming region adapted to be heated by the heating assemblies. The heating assembly may include at least one fuel chamber and at least one heating and ignition source. The at least one fuel chamber may be adapted to receive at least one fuel stream at a first temperature. The fuel stream may include a liquid, combustible, carbon-containing fuel having an ignition temperature greater than the first temperature at which the fuel stream is delivered to the fuel chamber. The at least one heating and ignition source may be adapted to heat at least a portion of the fuel chamber to raise the temperature of at least a portion of the carbon-containing fuel to a second temperature at least as great as the ignition temperature and to ignite the carbon-containing fuel. Methods of use are also disclosed.
摘要翻译：基于燃烧的加热组件和产氢燃料处理组件，其至少包括适于被加热组件加热的重整区域。加热组件可以包括至少一个燃料室和至少一个加热和点火源。至少一个燃料室可以适于在第一温度下接收至少一个燃料流。燃料流可以包括具有大于燃料流被输送到燃料室的第一温度的点燃温度的液体可燃的含碳燃料。至少一个加热点火源可以适于加热燃料室的至少一部分以将至少一部分含碳燃料的温度升高至至少与点火温度一样高的第二温度，并且点燃含碳燃料。还公开了使用方法。

99. 发明申请

US20100086477A1 REACTION CHAMBER PROMOTING HEAT EXCHANGE BETWEEN THE REAGENTS AND THE GASES THAT ARE PRODUCED 有权
标题翻译：反应室促进试剂与生产的气体之间的热交换
公开(公告)号：US20100086477A1
公开(公告)日：2010-04-08
申请号：US12573376
申请日：2009-10-05
申请人： Christophe Boyer , Fabrice Giroudiere
发明人： Christophe Boyer , Fabrice Giroudiere
IPC分类号： C01B3/02 , B01J8/06 , C01B3/16
CPC分类号： B01J8/0257 , B01J8/0278 , B01J8/0285 , B01J8/0292 , B01J8/067 , B01J2208/00203 , B01J2208/00495 , B01J2208/00504 , B01J2208/0053 , B01J2208/00769 , B01J2208/00849 , B01J2208/025 , C01B3/323 , C01B3/384 , C01B2203/0233 , C01B2203/0822 , C01B2203/1229 , F28F13/08 , Y02P20/128 , Y02P20/52
摘要： This invention relates to a chamber in which a chemical reaction is carried out in the presence of catalyst and reagents, comprising at least one catalytic tube (10) into which is placed an internal tube (12) for evacuating the gas that is produced, means for introducing reagents (15) and means for introducing the catalyst (16) that are located in the upper portion of the chamber (1), means for heating the catalytic tube (10) that are arranged in the lower portion of the chamber (1), and in which the catalytic tube (10) comprises, in its upper portion above the catalyst (13), means that promote heat exchange between the reagents and the gas that is produced.The invention also relates to the process that uses this chamber.
摘要翻译：本发明涉及一种在催化剂和试剂存在下进行化学反应的室，包括至少一个催化管（10），其中放置有用于抽空所产生气体的内管（12）用于引入试剂（15）和用于引入位于室（1）上部的催化剂（16）的装置，用于加热设置在室（1）的下部的催化剂管（10）的装置），并且其中催化管（10）在其上部在催化剂（13）上方包括促进试剂和所产生气体之间的热交换的装置。本发明还涉及使用该室的方法。

100. 发明申请

US20100080754A1 PROCESS FOR PRODUCING HYDROGEN WITH COMPLETE CAPTURE OF CO2 AND RECYCLING UNCONVERTED METHANE 有权
标题翻译：生产氢气完全捕获二氧化碳和循环甲烷的方法
公开(公告)号：US20100080754A1
公开(公告)日：2010-04-01
申请号：US12568317
申请日：2009-09-28
申请人： Beatrice FISCHER , Fabrice GIROUDIERE , Jean-Louis AMBROSINO , Michel THOMAS
发明人： Beatrice FISCHER , Fabrice GIROUDIERE , Jean-Louis AMBROSINO , Michel THOMAS
IPC分类号： C01B3/24
CPC分类号： C01B3/56 , B01D53/04 , B01D2253/102 , B01D2253/304 , B01D2253/308 , B01D2256/16 , B01D2257/502 , B01D2257/504 , B01D2257/7022 , B01D2259/4009 , C01B3/48 , C01B3/52 , C01B2203/0233 , C01B2203/0283 , C01B2203/0415 , C01B2203/043 , C01B2203/0475 , C01B2203/0822 , C01B2203/0827 , C01B2203/1241 , C01B2203/148 , Y02C10/04 , Y02C10/08 , Y02E60/324 , Y02P20/128 , Y02P20/152 , Y02P30/30
摘要： The present invention concerns a process for producing hydrogen from a hydrocarbon feed and steam, comprising: a step for producing a synthesis gas in a unit for steam reforming the hydrocarbon feed in the presence of steam, with a fuel providing the heat necessary for the reaction; a step for steam converting synthesis gas obtained in the preceding step, producing a stream of hydrogen containing methane and carbon dioxide; a step for capturing carbon dioxide present in the stream obtained from the steam conversion step in order to separate the carbon dioxide from the stream of hydrogen; a step for capturing and recycling the methane and other impurities (CO, CO2) present in the stream of hydrogen to the steam reforming step.
摘要翻译：本发明涉及一种从烃类进料和蒸汽中生产氢气的方法，包括：在蒸汽存在下用于在烃类进料中蒸汽重整的单元中生产合成气的步骤，提供反应所需的热量 ; 在前述步骤中获得的蒸汽转化合成气的步骤，产生含有甲烷和二氧化碳的氢气流; 用于捕获从蒸汽转化步骤获得的物流中存在的二氧化碳以从二氧化碳流中分离二氧化碳的步骤; 将存在于氢气流中的甲烷和其它杂质（CO，CO 2）捕获并再循环到蒸汽重整步骤的步骤。

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