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1. 发明授权

US06387555B1 Selective oxidizer in cell stack manifold 失效
标题翻译：细胞堆叠歧管中的选择性氧化剂
公开(公告)号：US06387555B1
公开(公告)日：2002-05-14
申请号：US09510697
申请日：2000-02-22
申请人： Douglas J. Wheeler , Thomas J. Corrigan , Leonard J. Bonville , Roger R. Lesieur , Derek W. Hildreth , Carl A. Reiser
发明人： Douglas J. Wheeler , Thomas J. Corrigan , Leonard J. Bonville , Roger R. Lesieur , Derek W. Hildreth , Carl A. Reiser
IPC分类号： H01M804
CPC分类号： H01M8/0662
摘要： An integrated fuel cell stack assembly (26) and selective oxidizer bed assembly (200) is provided. The fuel cell stack assembly (26) also includes a number of fuel cells. A fuel inlet manifold (22) and fuel inlet plenum to cell stack (38) manifold are arranged in fluid communication with the fuel stack assembly (26) for supplying to and exhausting from, respectively, the fuel supply in the fuel cells in the fuel stack assembly (26). The bed resides in said fuel inlet manifold. The bed includes a selective oxidation catalyst with a heat exchange fluid conduit routed therethrough. Oxygen-containing gas is supplied into the bed via the input plenum. The temperature of the internal selective oxidizer bed is controlled by the fluid conduit in the bed to reduce carbon monoxide in the fuel.
摘要翻译：提供了集成的燃料电池堆组件（26）和选择性氧化床床组件（200）。燃料电池堆组件（26）还包括多个燃料电池。燃料入口歧管（22）和燃料入口通风室至电池堆（38）歧管布置成与燃料堆组件（26）流体连通，用于分别供应燃料燃料中的燃料电池中的燃料供应和排出堆叠组件（26）。床位于所述燃料入口歧管中。该床包括选择性氧化催化剂，其中路由有热交换流体导管。含氧气体通过输入增压室供应到床中。内部选择性氧化剂床的温度由床中的流体导管控制，以减少燃料中的一氧化碳。

2. 发明授权

US6140266A Compact and light weight catalyst bed for use in a fuel cell power plant and method for forming the same 有权
标题翻译：用于燃料电池发电厂的紧凑且重量轻的催化剂床及其形成方法
公开(公告)号：US6140266A
公开(公告)日：2000-10-31
申请号：US252154
申请日：1999-02-18
申请人： Thomas J. Corrigan , Leonard J. Bonville, Jr. , Roger R. Lesieur , Derek W. Hildreth , Maria G. Lukianoff
发明人： Thomas J. Corrigan , Leonard J. Bonville, Jr. , Roger R. Lesieur , Derek W. Hildreth , Maria G. Lukianoff
IPC分类号： B01J35/04 , H01M8/06 , B01J35/00 , B01J21/04 , H01M4/86 , H01M4/90
CPC分类号： H01M8/0631 , B01J35/04
摘要： A fuel gas catalyst bed for use in a fuel cell power plant is formed from a monolithic open cell foam component, the open cell lattice of which forms gas passages through the catalyst bed. The monolithic component has a lattice of internal open cells which are both laterally and longitudinally interconnected so as to produce a diffuse gas flow pattern through the catalyst bed. All areas of the monolithic component which form the gas flow pattern are provided with an underlying high porosity wash coat layer. The porous surface of the wash coat layer is provided with a nickel catalyst layer, or a noble metal catalyst layer, such as platinum, rhodium, palladium, or the like, over which the gas stream being treated flows. The base foam lattice can be a metal such as aluminum, stainless steel, a steel-aluminum alloy, a nickel alloy, a ceramic, or the like material which can be wash coated. The use of an open cell lattice as the basis of a catalyst bed enables the formation of very compact, light weight and high surface area catalyst bed with excellent gas flow-through characteristics.
摘要翻译：用于燃料电池发电厂的燃料气体催化剂床由单体开孔泡沫组分形成，其开孔格子形成通过催化剂床的气体通道。整体部件具有内部开孔的格子，其横向和纵向相互连接，以便产生通过催化剂床的扩散气流模式。形成气体流动图案的整体部件的所有区域都设置有下面的高孔隙率洗涤涂层。洗涤涂层的多孔表面设置有镍催化剂层或贵金属催化剂层，例如铂，铑，钯等，待处理的气流在其上流动。基体泡沫格子可以是可以进行洗涂的金属，例如铝，不锈钢，钢 - 铝合金，镍合金，陶瓷等。使用开孔格子作为催化剂床的基础使得能够形成具有优异的气体流通特性的非常紧凑，重量轻和高表面积的催化剂床。

3. 发明授权

US06210821B1 System for implementing operation and start-up of a vehicle which is powered by electricity from a fuel cell power plant 失效
标题翻译：用于实施由燃料电池发电厂供电的车辆的操作和起动的系统
公开(公告)号：US06210821B1
公开(公告)日：2001-04-03
申请号：US09221428
申请日：1998-12-28
申请人： Roger R. Lesieur , Leonard J. Bonville, Jr. , Jay Garow , Thomas J. Corrigan , John L. Preston, Jr.
发明人： Roger R. Lesieur , Leonard J. Bonville, Jr. , Jay Garow , Thomas J. Corrigan , John L. Preston, Jr.
IPC分类号： H01M806
CPC分类号： H01M8/0662 , H01M8/0258 , H01M8/04223 , H01M8/04225 , H01M8/04238 , H01M8/04302 , H01M8/0612 , H01M2250/20 , Y02T90/32
摘要： A fuel gas processing system is operable to remove substantially all of the sulfur present in a hydrocarbon fuel supply used to power a fuel cell power plant in a mobile vehicular environment. The power plant fuel can be gasoline, diesel fuel, kerosene, fuel oil, natural gas, or another fuel which contains relatively high levels of organic sulfur compounds such as mercaptans, sulfides, disulfides, and the like. The hydrocarbon fuel supply is passed through a nickel reactant desulfurizer bed wherein essentially all of the sulfur in the organic sulfur compounds react with the nickel reactant, and are converted to nickel sulfide while the desulfurized fuel continues through the remainder of the fuel processing system. The fuel cell power plant and the processing system can be used to power a mobile vehicle, such an automobile, truck, bus, or the like. An auxiliary supply of hydrogen is provided in order to power the fuel cell power plant during start up of the fuel processing system. A second auxiliary supply of desulfurized fuel is also provided to operate the fuel cell power plant during an interim period until the highest temperature component of the fuel processing system is brought up to operational temperatures during the start up protocol.
摘要翻译：燃料气体处理系统可操作以基本上除去用于为移动车辆环境中的燃料电池发电厂供电的碳氢化合物燃料供应中基本上所有的硫。发电厂燃料可以是汽油，柴油燃料，煤油，燃料油，天然气或含有较高水平的有机硫化合物如硫醇，硫化物，二硫化物等的另一种燃料。烃燃料供应通过镍反应物脱硫器床，其中有机硫化合物中基本上所有的硫与镍反应物反应，并转化为硫化镍，而脱硫燃料继续通过燃料处理系统的其余部分。燃料电池发电厂和处理系统可用于为诸如汽车，卡车，公共汽车等的移动车辆供电。提供辅助氢气供应，以便在燃料处理系统启动期间为燃料电池发电厂供电。还提供了第二辅助的脱硫燃料供应，以在燃料电池发电厂过渡期间操作，直到燃料处理系统的最高温度成分在启动协议期间达到工作温度。

4. 发明授权

US06376114B1 Reformate fuel treatment system for a fuel cell power plant 有权
标题翻译：改革燃料电池发电厂的燃料处理系统
公开(公告)号：US06376114B1
公开(公告)日：2002-04-23
申请号：US09583824
申请日：2000-05-30
申请人： Leonard J. Bonville, Jr. , Ned E. Cipollini , Jay Garow , Roger R. Lesieur , Donald F. Szydlowski , Zebulon D. Vance , Douglas J. Wheeler
发明人： Leonard J. Bonville, Jr. , Ned E. Cipollini , Jay Garow , Roger R. Lesieur , Donald F. Szydlowski , Zebulon D. Vance , Douglas J. Wheeler
IPC分类号： H01M806
CPC分类号： H01M8/0625 , H01M8/04089 , H01M8/04156 , H01M8/0662
摘要： The invention is a reformate fuel treatment system for a fuel cell power plant that includes at least one fuel cell for generating electricity from process oxidant and reducing fluid reactant streams; fuel processing components including a steam supply and a reformer for producing a hydrogen enriched reformate fuel for the fuel cell from a hydrocarbon fuel; and, an ammonia removal apparatus that treats the reformate fuel to make it appropriate for supplying hydrogen to an anode electrode of the fuel cell. The ammonia removal apparatus may be a disposable ammonia scrubber, an ammonia scrubbing cool water bed and an ammonia stripping warm water bed, a pair of first and second regenerable scrubbers, or a single regenerable ammonia scrubber.
摘要翻译：本发明是用于燃料电池发电厂的重整燃料处理系统，其包括至少一个用于从工艺氧化剂发电和减少流体反应物流的燃料电池; 燃料处理部件，包括蒸汽源和重整器，用于从烃燃料生产用于燃料电池的富氢重整油燃料; 以及处理重整燃料使其适合于向燃料电池的阳极供给氢的氨去除装置。氨去除装置可以是一次性氨洗涤器，氨洗涤冷水床和氨汽提温水床，一对第一和第二可再生洗涤器或单个可再生氨洗涤器。

5. 发明授权

US06284206B1 Compact selective oxidizer assemblage for a fuel cell power plant 有权
标题翻译：用于燃料电池发电厂的紧凑型选择性氧化器组合
公开(公告)号：US06284206B1
公开(公告)日：2001-09-04
申请号：US09273735
申请日：1999-03-22
申请人： Roger R. Lesieur , Thomas J. Corrigan , Derek W. Hildreth
发明人： Roger R. Lesieur , Thomas J. Corrigan , Derek W. Hildreth
IPC分类号： F01N300
CPC分类号： H01M8/0631 , C01B3/583 , C01B2203/044 , C01B2203/047 , F28D7/1653 , F28D7/1684 , F28F13/003 , H01M8/0662
摘要： A process gas selective oxidizer assemblage for use in a fuel cell power plant includes one or more catalyzed selective oxidizer process gas flow fields and one or more adjacent non-catalyzed heat exchanger process gas flow fields. The catalyzed selective oxidizer process gas flow fields may be formed with catalyzed pellets or with a monolithic catalyzed open cell foam component. The heat exchanger process gas flow fields are formed by non-catalyzed monolithic open cell foam components which have coolant fluid passages disposed therein. Planar metal sheets form a common wall between the selective oxidizer process gas flow fields and the heat exchanger process gas flow fields. The use of the open cell foam to form the heat exchanger process gas flow fields provides enhanced heat transfer between the reformate gas and the coolant fluid. The use of the foam components in both the heat exchange process gas flow fields and the selective oxidizer process gas flow fields enables the construction of a more compact and lighter weight selective oxidizer assemblage. The repeating components are placed side-by-side in the assemblage, so that one of the catalyzed process gas flow fields operates at a higher temperature than subsequent catalyzed process gas flow fields. The process gas enters the higher temperature catalyzed flow field after it is admixed with air that is injected into the system just prior to the higher temperature flow field. The process gas-air mixture flows through the first higher temperature catalyzed process gas flow field; thence through a non-catalyzed heat exchanger process gas flow field; thence through a lower temperature catalyzed process gas flow field; thence through another heat exchanger process gas flow field; and so on, until the selectively oxidized process gas exits the assemblage.
摘要翻译：用于燃料电池发电厂的工艺气体选择性氧化器组合包括一个或多个催化选择性氧化剂工艺气体流场和一个或多个相邻的非催化热交换器工艺气体流场。催化的选择性氧化剂工艺气体流场可以用催化颗粒或整体催化的开孔泡沫组分形成。热交换器工艺气体流场由其中设置有冷却剂流体通道的非催化单块开孔泡沫组件形成。平面金属片在选择性氧化剂工艺气体流场和热交换器工艺气体流场之间形成公共壁。使用开孔泡沫来形成热交换器工艺气体流场提供了改性气体和冷却剂流体之间的增强的热传递。在热交换过程气体流场和选择性氧化剂处理气体流场中使用泡沫组分能够构建更紧凑和更轻重量的选择性氧化剂组合。重复组分并排放置在组合中，使得催化过程气体流场中的一个在比随后的催化工艺气体流场更高的温度下操作。在较高温度的流场之前，将工艺气体与注入系统的空气混合后，进入较高温度的催化流场。工艺气体 - 空气混合物流过第一较高温度催化的工艺气体流场; 从而通过非催化热交换器工艺的气体流场; 从而通过较低温度催化的工艺气体流场; 从而通过另一个换热器工艺的气体流场; 等等，直到选择性氧化的工艺气体离开组合物。

6. 发明授权

US6159256A Method for desulfurizing a fuel for use in a fuel cell power plant 有权
标题翻译：用于燃料电池发电厂的燃料脱硫方法
公开(公告)号：US6159256A
公开(公告)日：2000-12-12
申请号：US439602
申请日：1999-11-12
申请人： Leonard J. Bonville, Jr. , Charles L. DeGeorge , Peter F. Foley , Jay Garow , Roger R. Lesieur , John L. Preston, Jr. , Donald F. Szydlowski
发明人： Leonard J. Bonville, Jr. , Charles L. DeGeorge , Peter F. Foley , Jay Garow , Roger R. Lesieur , John L. Preston, Jr. , Donald F. Szydlowski
IPC分类号： C01B3/38 , B60K15/00 , C01B3/48 , C01B3/58 , C10G25/00 , C10G29/04 , C10G29/16 , H01M2/10 , H01M8/00 , H01M8/04 , H01M8/06 , H01M16/00 , B01J7/00 , C10G29/00 , C10J1/00
CPC分类号： H01M16/006 , B60K15/00 , C01B3/48 , C01B3/58 , C10G25/003 , C10G29/04 , H01M2/1083 , H01M8/0612 , H01M8/0662 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/044 , C01B2203/0465 , C01B2203/066 , C01B2203/0811 , C01B2203/0844 , C01B2203/0866 , C01B2203/0883 , C01B2203/0894 , C01B2203/1047 , C01B2203/1052 , C01B2203/1082 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/142 , C01B2203/146 , C01B2203/147 , C01B2203/1604 , C01B2203/1685 , C01B2203/169 , C01B2203/82 , H01M2250/20 , H01M2300/0082 , H01M8/00 , H01M8/04029 , Y02T90/32
摘要： A fuel processing system is operable to remove substantially all of the sulfur present in an undiluted hydrocarbon fuel stock supply used to power a fuel cell power plant in a mobile environment, such as an automobile, bus, truck, boat, or the like, or in a stationary environment. The power plant hydrogen fuel source can be gasoline, diesel fuel, naphtha, light hydrocarbon fuels such as butane, propane, natural gas, or other like fuels which contain relatively high levels of organic sulfur compounds such as mercaptans, sulfides, disulfides, and the like. The undiluted hydrocarbon fuel supply is passed through a nickel desulfurizer bed wherein essentially all of the sulfur in the organic sulfur compounds react with the nickel reactant, and are converted to nickel sulfide while the desulfurized organic remnants continue through the remainder of the fuel processing system. The system does not require the addition of steam or a hydrogen source to the fuel stream prior to the desulfurizing step. The system operates at relatively low temperatures and can be used to desulfurize either a liquid or a gaseous fuel stream.
摘要翻译：燃料处理系统可操作以基本上除去用于在诸如汽车，公共汽车，卡车，船等的移动环境中为燃料电池发电厂供电的未稀释的碳氢化合物燃料原料供应中存在的所有硫，或在一个静止的环境中。发电厂氢燃料源可以是汽油，柴油，石脑油，轻烃燃料如丁烷，丙烷，天然气或其它类似燃料，其含有相对高含量的有机硫化合物如硫醇，硫化物，二硫化物，以及喜欢。未稀释的碳氢化合物燃料供应通过镍脱硫器床，其中有机硫化合物中基本上所有的硫与镍反应物反应，并转化成硫化镍，而脱硫的有机残余物继续通过燃料处理系统的其余部分。该系统不需要在脱硫步骤之前向燃料流中添加蒸汽或氢源。该系统在相对低的温度下运行，可用于对液体或气态燃料流进行脱硫。

7. 发明授权

US6156084A System for desulfurizing a fuel for use in a fuel cell power plant 失效
标题翻译：用于在燃料电池发电厂中使用的燃料脱硫的系统
公开(公告)号：US6156084A
公开(公告)日：2000-12-05
申请号：US104254
申请日：1998-06-24
申请人： Leonard J. Bonville, Jr. , Charles L. DeGeorge , Peter F. Foley , Jay Garow , Roger R. Lesieur , John L. Preston, Jr. , Donald F. Szydlowski
发明人： Leonard J. Bonville, Jr. , Charles L. DeGeorge , Peter F. Foley , Jay Garow , Roger R. Lesieur , John L. Preston, Jr. , Donald F. Szydlowski
IPC分类号： C01B3/38 , B60K15/00 , C01B3/48 , C01B3/58 , C10G25/00 , C10G29/04 , C10G29/16 , H01M2/10 , H01M8/00 , H01M8/04 , H01M8/06 , H01M16/00 , B01J7/00 , C10G29/00 , C10J1/00
CPC分类号： H01M16/006 , B60K15/00 , C01B3/48 , C01B3/58 , C10G25/003 , C10G29/04 , H01M2/1083 , H01M8/0612 , H01M8/0662 , C01B2203/0244 , C01B2203/0283 , C01B2203/0415 , C01B2203/044 , C01B2203/0465 , C01B2203/066 , C01B2203/0811 , C01B2203/0844 , C01B2203/0866 , C01B2203/0883 , C01B2203/0894 , C01B2203/1047 , C01B2203/1052 , C01B2203/1082 , C01B2203/1241 , C01B2203/1247 , C01B2203/1288 , C01B2203/142 , C01B2203/146 , C01B2203/147 , C01B2203/1604 , C01B2203/1685 , C01B2203/169 , C01B2203/82 , H01M2250/20 , H01M2300/0082 , H01M8/00 , H01M8/04029 , Y02T90/32
摘要： A fuel processing system is operable to remove substantially all of the sulfur present in an undiluted hydrocarbon fuel stock supply used to power a fuel cell power plant in a mobile environment, such as an automobile, bus, truck, boat, or the like, or in a stationary environment. The power plant hydrogen fuel source can be gasoline, diesel fuel, naphtha, light hydrocarbon fuels such as butane, propane, natural gas, or other like fuels which contain relatively high levels of organic sulfur compounds such as mercaptans, sulfides, disulfides, and the like. The undiluted hydrocarbon fuel supply is passed through a nickel desulfurizer bed wherein essentially all of the sulfur in the organic sulfur compounds react with the nickel reactant, and are converted to nickel sulfide while the desulfurized organic remnants continue through the remainder of the fuel processing system. The system does not require the addition of steam or a hydrogen source to the fuel stream prior to the desulfurizing step. The system operates at relatively low temperatures and can be used to desulfurize either a liquid or a gaseous fuel stream.
摘要翻译：燃料处理系统可操作以基本上除去用于在诸如汽车，公共汽车，卡车，船等的移动环境中为燃料电池发电厂供电的未稀释的碳氢化合物燃料原料供应中存在的所有硫，或在一个静止的环境中。发电厂氢燃料源可以是汽油，柴油，石脑油，轻烃燃料如丁烷，丙烷，天然气或其它类似燃料，其含有相对高含量的有机硫化合物如硫醇，硫化物，二硫化物，以及喜欢。未稀释的碳氢化合物燃料供应通过镍脱硫器床，其中有机硫化合物中基本上所有的硫与镍反应物反应，并转化成硫化镍，而脱硫的有机残余物继续通过燃料处理系统的其余部分。该系统不需要在脱硫步骤之前向燃料流中添加蒸汽或氢源。该系统在相对低的温度下运行，可用于对液体或气态燃料流进行脱硫。

8. 发明授权

US6129835A System and method for desulfurizing gasoline or diesel fuel to produce a low sulfur-content fuel for use in an internal combustion engine 失效
标题翻译：用于将汽油或柴油燃料脱硫以产生用于内燃机的低含硫燃料的系统和方法
公开(公告)号：US6129835A
公开(公告)日：2000-10-10
申请号：US221429
申请日：1998-12-28
申请人： Roger R. Lesieur , Leonard J. Bonville, Jr.
发明人： Roger R. Lesieur , Leonard J. Bonville, Jr.
IPC分类号： C10G25/00 , C10G29/04 , C10G45/00
CPC分类号： C10G29/04 , C10G25/003
摘要： A fuel processing system is operable to remove substantially all of the sulfur present in gasoline or diesel fuel used for operating an internal combustion engine. The fuel supply is passed through a nickel reactant desulfurizer bed wherein essentially all of the sulfur in organic sulfur compounds in the fuel combine with the nickel reactant in the desulfurizer bed, and are converted to nickel sulfide. The desulfurizing system can operate at ambient or elevated pressures. The fuel can be treated either in a liquid phase or in a vapor phase. The sulfur scrubbing operation can be performed either in a vehicle while the latter is being operated, or at the fueling station (gas station) prior to sale to the end user. The amount of sulfur in the fuel can be lowered to less than about 0.05 ppm. This extends the life of the catalytic converters in vehicles, reduces corrosion of parts of the internal combustion engine, and provides an environmentally compatible system.
摘要翻译：燃料处理系统可操作以基本上除去用于操作内燃机的汽油或柴油燃料中基本上所有的硫。燃料供应通过镍反应物脱硫器床，其中燃料中有机硫化合物中的基本上所有的硫与脱硫器床中的镍反应物组合，并转化为硫化镍。脱硫系统可以在环境压力或高压下运行。燃料可以在液相或气相中进行处理。硫洗涤操作可以在车辆操作期间在车辆中执行，或者在向最终用户销售之前在加油站（加油站）执行。燃料中的硫的量可以降低到小于约0.05ppm。这延长了车辆中催化转化器的使用寿命，减少了内燃机部件的腐蚀，并提供了一个环保的系统。

9. 发明授权

US06203587B1 Compact fuel gas reformer assemblage 有权
标题翻译：紧凑型燃气改质机组合
公开(公告)号：US06203587B1
公开(公告)日：2001-03-20
申请号：US09233223
申请日：1999-01-19
申请人： Roger R. Lesieur , Thomas J. Corrigan
发明人： Roger R. Lesieur , Thomas J. Corrigan
IPC分类号： B01J700
CPC分类号： C01B3/384 , B01J19/2485 , B01J19/249 , B01J2219/00117 , B01J2219/00157 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/2479 , B01J2219/2485 , C01B3/48 , C01B3/583 , C01B2203/0233 , C01B2203/0283 , C01B2203/044 , C01B2203/047 , C01B2203/066 , C01B2203/0811 , C01B2203/0844 , C01B2203/0866 , C01B2203/0883 , C01B2203/1023 , C01B2203/1052 , C01B2203/1064 , C01B2203/1082 , H01M8/0631
摘要： A fuel gas reformer assemblage for use in a fuel cell power plant is formed from a composite plate assembly which includes spaced-apart divider plates with interposed monolithic open cell sponge-like members which form gas passages. The monolithic members have a lattice of internal open cells which are both laterally and longitudinally interconnected so as to provide for a diffuse gas flow. The entire surface area of the monolithic components is wash coated with a porous alumina layer, and selected areas of the wash coat are also catalyzed. The reformer assemblage is constructed from a series of repeating sub-assemblies, each of which includes a core of separate regenerator/heat exchanger gas passages. The core in each sub-assembly is sandwiched between a pair of reformer gas passage skins, which complete the subassembly. Adjacent reformer gas/regenerator/reformer gas passage sub-assemblies in the composite plate assembly are separated from each other by burner gas passages. The regenerator/heat exchanger gas passages and the reformer gas passages in each sub-assembly are connected by gas flow return manifolds which form a part of each sub-assembly. The fuel gases flow in one end of the assemblage, through the reformer gas passages, and then reverse their direction of flow in the return manifolds so as to exit the reformer assemblage through the regenerator gas flow passages. The burner gases flow in one end of the reformer assemblage and out the other end.
摘要翻译：用于燃料电池发电厂的燃料气体重整器组件由复合板组件形成，复合板组件包括间隔开的分隔板，其具有形成气体通道的插入的整体开放式海绵状构件。整体构件具有内部开孔的格子，其横向和纵向相互连接，以提供扩散气流。单块组件的整个表面积用多孔氧化铝层进行洗涤，并且洗涤涂层的选定区域也被催化。重整器组合由一系列重复子组件构成，每个重复组件包括单独的再生器/热交换器气体通道的核心。每个子组件中的芯子夹在一对完成子组件的重整器气体通道皮之间。复合板组件中相邻的重整器气体/再生器/重整器气体通道子组件通过燃烧器气体通道相互分离。每个子组件中的再生器/热交换器气体通道和重整器气体通道通过形成每个子组件的一部分的气流返回歧管连接。燃料气体通过重整器气体通道在组合件的一端中流动，然后在回流歧管中反转它们的流动方向，从而通过再生器气体流动通道离开重整器组件。燃烧器气体在重整器组合的一端流动，另一端流出。

10. 发明授权

US5769909A Method and apparatus for desulfurizing fuel gas 失效
标题翻译：燃气脱硫方法和装置
公开(公告)号：US5769909A
公开(公告)日：1998-06-23
申请号：US656568
申请日：1996-05-31
申请人： Stanley P. Bonk , Thomas J. Corrigan , Roger R. Lesieur , Richard A. Sederquist , Donald F. Szydlowski
发明人： Stanley P. Bonk , Thomas J. Corrigan , Roger R. Lesieur , Richard A. Sederquist , Donald F. Szydlowski
IPC分类号： B01D53/86 , B01J8/04 , C01B3/48 , C01B3/58 , C01B17/04 , C10K1/20 , C10L3/10 , H01M8/06 , B01J8/06 , C10L3/06
CPC分类号： H01M8/0631 , B01D53/8603 , B01D53/8618 , B01J8/04 , C01B17/0408 , C01B3/48 , C01B3/58 , H01M8/0662 , B01J2208/00141 , B01J2208/00194 , B01J2208/00495 , B01J2208/0053 , C01B2203/0233 , C01B2203/0283 , C01B2203/0288 , C01B2203/045 , C01B2203/0485 , C01B2203/066 , C01B2203/0844 , C01B2203/0883 , C01B2203/1011 , C01B2203/1241 , C01B2203/127 , C01B2203/1614 , H01M8/0612
摘要： Sulfur and sulfur compounds are removed from a gas stream, such as a hydrocarbon fuel gas stream so as to render the gas stream suitable for use in a fuel cell power plant. Natural gas and recycled hydrogen enters the hydrodesulfurizer assembly at a temperature of about 120.degree. F. The gas stream is heated to a temperature of about 625.degree. F. whereupon it enters a desulfurizing bed formed from a mixture of platinum catalyst deposited on alumina pellets, and a pelletized zinc oxide hydrogen sulfide absorbent. The gas is cooled to an exit temperature of about 525.degree.F. as it passes through the desulfurizer bed. The desulfurizer bed is combined with a shift converter which reduces carbon monoxide in the desulfurized gas stream after the latter has passed through a steam reformer bed.
摘要翻译：硫和硫化合物从诸如烃类燃料气流的气流中除去，以使气流适合用于燃料电池发电厂。天然气和再循环的氢气在约120°F的温度下进入加氢脱硫装置。将气流加热到约625°F的温度，随后进入由沉积在氧化铝颗粒上的铂催化剂的混合物形成的脱硫床，和颗粒状氧化锌硫化氢吸收剂。当气体通过脱硫器床时，气体被冷却至约525°F的出口温度。脱硫器床与一种换档转换器相结合，该换档转换器在脱硫气流通过蒸汽重整床后减少一氧化碳。

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