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1. 发明授权

US09472822B2 Fuel cell power plant control 有权
标题翻译：燃料电池发电厂控制
公开(公告)号：US09472822B2
公开(公告)日：2016-10-18
申请号：US14005762
申请日：2011-03-29
申请人： Jonathan Daniel O'Neill , Timothy W. Patterson, Jr.
发明人： Jonathan Daniel O'Neill , Timothy W. Patterson, Jr.
IPC分类号： H01M8/06 , H01M8/04 , G05F1/575
CPC分类号： H01M8/0488 , G05F1/575 , H01M8/04589 , H01M8/0491 , H01M8/04952 , Y02E60/50
摘要： An example method of controlling a fuel cell power plant based on provided power includes selectively varying an electrical resistance of the variable resistive device responsive to at least one of a power provided by the fuel cell power plant, a current provided by the fuel cell power plant, or a voltage decay rate.
摘要翻译：基于提供的功率来控制燃料电池发电厂的示例性方法包括响应于由燃料电池发电厂提供的功率，由燃料电池发电厂提供的电流中的至少一个选择性地改变可变电阻装置的电阻，或电压衰减率。

2. 发明授权

US08277991B2 Hydrogen passivation shut down system for a fuel cell power plant 有权
标题翻译：用于燃料电池发电厂的氢钝化关闭系统
公开(公告)号：US08277991B2
公开(公告)日：2012-10-02
申请号：US12386950
申请日：2009-04-24
申请人： Carl A. Reiser , Tommy Skiba , Timothy W. Patterson, Jr.
发明人： Carl A. Reiser , Tommy Skiba , Timothy W. Patterson, Jr.
IPC分类号： H01M8/04 , H01M2/02
CPC分类号： H01M8/04228 , H01M8/04097 , H01M8/04201 , H01M8/04216 , H01M8/04223 , H01M8/04303 , H01M8/0687 , H01M2008/1095
摘要： The invention is a hydrogen passivation shut down system for a fuel cell power plant (10, 200). During shut down of the plant (10, 200), hydrogen fuel is permitted to transfer between an anode flow path (24, 24′) and a cathode flow path (38, 38′). A passive hydrogen bleed line (202) permits passage of a smallest amount of hydrogen into the fuel cell (12′) necessary to maintain the fuel cell (12′) in a passive state. A diffusion media (204) may be secured in fluid communication with the bleed line (202) to maintain a constant, slow rate of diffusion of the hydrogen into the fuel cell (12′) despite varying pressure differentials between the shutdown fuel cell (12′) and ambient atmosphere adjacent the cell (12′).
摘要翻译：本发明是用于燃料电池发电厂（10,200）的氢钝化关闭系统。在工厂（10,200）关闭期间，允许氢燃料在阳极流动路径（24,24'）和阴极流动路径（38,38'）之间传递。被动氢气排放管线（202）允许将最小量的氢气通入维持燃料电池（12'）处于被动状态所必需的燃料电池（12'）中。扩散介质（204）可以被固定成与排放管线（202）流体连通，以保持氢气进入燃料电池（12'）的恒定的慢速扩散速率，尽管关闭燃料电池（12 '）和邻近电池（12'）的环境气氛。

3. 发明授权

US06309768B1 Process for regenerating a carbon monoxide oxidation reactor 失效
标题翻译：再生一氧化碳氧化反应器的方法
公开(公告)号：US06309768B1
公开(公告)日：2001-10-30
申请号：US09346888
申请日：1999-07-02
申请人： Timothy W. Patterson, Jr. , Roger R. Lesieur
发明人： Timothy W. Patterson, Jr. , Roger R. Lesieur
IPC分类号： H01M800
CPC分类号： H01M8/0662 , B01J8/001 , B01J8/025 , B01J8/0285 , B01J2208/00088 , B01J2208/00141 , B01J2208/021
摘要： A process for regenerating a selective oxidizer bed, by the introduction of oxygen is provided. In a single oxidizer bed environment, regeneration may be carried out on shut-down or on start-up. On start-up, the process includes providing a selective oxidizer bed as well a fuel processor. The selective oxidizer bed is heated to approximately 180° F. Air is passed through the selective oxidizer bed while maintaining the selective oxidizer bed at a temperature of approximately 180° F. for 1-2 minutes. The selective oxidizer is then purged with steam to remove residual air therefrom. Fuel is then introduced from the fuel processor into the selective oxidizer. On shut-down, residual fuel is purged from the oxidizer bed and then air is passed therethrough while maintaining the bed at a temperature between approximately 180° F. to approximately 220° F. The oxidizer is allowed to cool to ambient temperature and then heated to 180° F. Residual air is then purged from the oxidizer for subsequent introduction of fuel. Multiple oxidizer beds may be provided in parallel to one another to enable continuous, uninterrupted operation with bed remaining operation at all times while the other is being regenerated. Regeneration may also be carried out by thermal cycling of the selective oxidizer bed.
摘要翻译：提供了通过引入氧来再生选择性氧化剂床的方法。在单个氧化剂床环境中，可以在关闭或启动时进行再生。在启动时，该过程包括提供选择性氧化床以及燃料处理器。将选择性氧化剂床加热至约180°F。将空气通过选择性氧化器床，同时将选择性氧化剂床保持在约180°F的温度下1-2分钟。然后用蒸汽吹扫选择性氧化剂以从其中除去残留的空气。燃料然后从燃料处理器引入选择性氧化器。关闭时，残留燃料从氧化剂床清除，然后空气通过，同时将床保持在约180°F至约220°F之间的温度。将氧化剂冷却至环境温度，然后加热至180°F。然后从氧化器中清除残余空气，以便随后引入燃料。可以彼此平行地设置多个氧化器床，以使得能够在任何时候进行床保持操作以及另一个再生时的连续的，不间断的操作。再生还可以通过选择性氧化床的热循环进行。

4. 发明申请

US20140011108A1 FUEL CELL POWER PLANT CONTROL 有权
标题翻译：燃油电池发电厂控制
公开(公告)号：US20140011108A1
公开(公告)日：2014-01-09
申请号：US14005762
申请日：2011-03-29
申请人： Jonathan Daniel O'Neill , Timothy W. Patterson, JR.
发明人： Jonathan Daniel O'Neill , Timothy W. Patterson, JR.
IPC分类号： H01M8/04
CPC分类号： H01M8/0488 , G05F1/575 , H01M8/04589 , H01M8/0491 , H01M8/04952 , Y02E60/50
摘要： An example method of controlling a fuel cell power plant based on provided power includes selectively varying an electrical resistance of the variable resistive device responsive to at least one of a power provided by the fuel cell power plant, a current provided by the fuel cell power plant, or a voltage decay rate.
摘要翻译：基于提供的功率来控制燃料电池发电厂的示例性方法包括响应于由燃料电池发电厂提供的功率，由燃料电池发电厂提供的电流中的至少一个选择性地改变可变电阻装置的电阻，或电压衰减率。

5. 发明申请

US20110318666A1 FUEL CELL STACK ASSEMBLY SEAL 审中-公开
标题翻译：燃油电池堆组件密封
公开(公告)号：US20110318666A1
公开(公告)日：2011-12-29
申请号：US13126054
申请日：2008-10-22
申请人： Timothy W. Patterson, Jr. , Tommy Skiba , David D. Jayne
发明人： Timothy W. Patterson, Jr. , Tommy Skiba , David D. Jayne
IPC分类号： H01M8/04 , H01M8/00 , H01M8/10
CPC分类号： H01M8/0273 , H01M8/0258 , H01M8/0267 , H01M8/0271 , H01M8/0284 , H01M8/0286 , H01M8/0297 , H01M8/241 , H01M8/2457 , H01M8/2475 , H01M8/2483 , H01M8/2485 , H01M2008/1095
摘要： A fuel cell is disclosed that includes an electrode assembly arranged between a cathode and an anode. The anode and cathode have lateral surfaces adjoining lateral surface of the electrode assembly and respectively include fuel and oxidant flow fields. Interfacial seals are not arranged between the lateral surfaces. Instead, a sealant is applied to the anode, the cathode and the electrode assembly to fluidly separate the fuel and oxidant flow fields. In one example, the adjoining lateral surfaces are in abutting engagement with one another. The sealant is applied in a liquid, uncured state to perimeter surfaces of the electrode assembly, the anode and the cathode that surround the lateral surfaces.
摘要翻译：公开了一种燃料电池，其包括布置在阴极和阳极之间的电极组件。阳极和阴极具有邻接电极组件的侧表面的侧表面，并且分别包括燃料和氧化剂流场。界面密封件不设置在侧面之间。相反，将密封剂施加到阳极，阴极和电极组件以流体地分离燃料和氧化剂流场。在一个示例中，邻接的侧表面彼此邻接。将密封剂以液体未固化状态施加到围绕侧表面的电极组件，阳极和阴极的周边表面。

6. 发明申请

US20110104582A1 TAILORING LIQUID WATER PERMEABILITY OF DIFFUSION LAYERS IN FUEL CELL STACKS 审中-公开
标题翻译：在燃料电池堆中定量扩散层的渗透性渗透性
公开(公告)号：US20110104582A1
公开(公告)日：2011-05-05
申请号：US12734636
申请日：2008-12-11
申请人： Timothy W. Patterson, JR. , Gennady Resnick , Ryan J. Balliet , Nikunj Gupta , Cynthia A. York , Carl A. Reiser , Robert M. Darling , Jesse M. Marzullo , Jeremy P. Meyers
发明人： Timothy W. Patterson, JR. , Gennady Resnick , Ryan J. Balliet , Nikunj Gupta , Cynthia A. York , Carl A. Reiser , Robert M. Darling , Jesse M. Marzullo , Jeremy P. Meyers
IPC分类号： H01M8/04 , H01M8/24
CPC分类号： H01M8/04253 , H01M8/023 , H01M8/04149 , H01M8/04171 , H01M8/04225 , H01M8/04291 , H01M8/04303 , H01M8/241
摘要： A fuel cell stack (31) includes a plurality of fuel cells (9) each having an electrolyte such as a PEM (10), anode and cathode catalyst layers (13, 14), anode and cathode gas diffusion layers (16, 17), and water transport plates (21, 28) adjacent the gas diffusion layers. The cathode diffusion layer of cells near the cathode end (36) of the stack have a high water permeability, such as greater than 3×10−4 g/(Pa s m) at about 80° C. and about 1 atmosphere, whereas the cathode gas diffusion layer in cells near the anode end (35) have water vapor permeance greater than 3×10−4 g/(Pa s m) at about 80° C. and about 1 atmosphere. In one embodiment, the anode gas diffusion layer of cells near the anode end (35) of the stack have a higher liquid water permeability than the anode gas diffusion layer in cells near the cathode end; a second embodiment reverses that relationship.
摘要翻译：燃料电池堆（31）包括多个具有诸如PEM（10），阳极和阴极催化剂层（13,14），阳极和阴极气体扩散层（16,17）的电解质的燃料电池（9）和与气体扩散层相邻的水输送板（21,28）。在堆叠的阴极端（36）附近的电池的阴极扩散层在约80℃和约1个大气压下具有高的透水性，例如大于3×10-4g /（Pa·sm），而在阳极端（35）附近的电池中的阴极气体扩散层在约80℃和约1个大气压下具有大于3×10-4g /（Pa·sm）的水蒸汽渗透性。在一个实施例中，在堆叠的阳极端（35）附近的电池的阳极气体扩散层在靠近阴极端的电池中具有比阳极气体扩散层更高的液体水渗透性; 第二个实施例反转了这种关系。

7. 发明授权

US09966612B2 Avoiding fuel starvation of anode end fuel cell 有权
公开(公告)号：US09966612B2
公开(公告)日：2018-05-08
申请号：US14378314
申请日：2012-02-24
申请人： Timothy W. Patterson, Jr. , Robert M. Darling
发明人： Timothy W. Patterson, Jr. , Robert M. Darling
IPC分类号： H01M8/02 , H01M8/026 , H01M8/241 , H01M8/2465 , H01M8/10
CPC分类号： H01M8/026 , H01M8/0267 , H01M8/04225 , H01M8/10 , H01M8/241 , H01M8/2465
摘要： The fuel flow channels (20a) of the end fuel cell (9a) at the anode end (34) of a fuel cell stack are significantly deeper than the fuel flow field channels (20) of the remaining fuel cells (9) in the stack, whereby fuel starvation caused by ice in the fuel flow channels is avoided during cold startup. The fuel flow field channels of the end cell (9) at the anode end of the stack is between about 0.15 mm and about 1.5 mm deeper than the fuel flow field channels in the remaining fuel cells of the stack, or between about 35% and about 65% deeper than the fuel flow field channels in the remaining fuel cells of the stack.

8. 发明申请

US20150004515A1 AVOIDING FUEL STARVATION OF ANODE END FUEL CELL 有权
标题翻译：避免阳极燃料电池的燃料启动
公开(公告)号：US20150004515A1
公开(公告)日：2015-01-01
申请号：US14378314
申请日：2012-02-24
申请人： Timothy W. Patterson, JR. , Robert M. Darling
发明人： Timothy W. Patterson, JR. , Robert M. Darling
IPC分类号： H01M8/02
CPC分类号： H01M8/026 , H01M8/0267 , H01M8/04225 , H01M8/10 , H01M8/241 , H01M8/2465
摘要： The fuel flow channels (20a) of the end fuel cell (9a) at the anode end (34) of a fuel cell stack are significantly deeper than the fuel flow field channels (20) of the remaining fuel cells (9) in the stack, whereby fuel starvation caused by ice in the fuel flow channels is avoided during cold startup. The fuel flow field channels of the end cell (9) at the anode end of the stack is between about 0.15 mm and about 1.5 mm deeper than the fuel flow field channels in the remaining fuel cells of the stack, or between about 35% and about 65% deeper than the fuel flow field channels in the remaining fuel cells of the stack.
摘要翻译：在燃料电池堆的阳极端（34）处的端部燃料电池（9a）的燃料流动通道（20a）比堆叠中的剩余燃料电池（9）的燃料流场通道（20）明显更深从而在冷启动期间避免了由燃料流动通道中的冰引起的燃料不足。在堆叠的阳极端处的端电池（9）的燃料流场通道比堆叠的剩余燃料电池中的燃料流场通道更深，在约0.15mm和约1.5mm之间，或者在约35％和比堆叠的剩余燃料电池中的燃料流场通道深65％。

9. 发明申请

US20120315558A1 HYDROGEN PASSIVATION SHUT DOWN SYSTEM FOR A FUEL CELL POWER PLANT 审中-公开
标题翻译：用于燃料电池的氢气灭火系统
公开(公告)号：US20120315558A1
公开(公告)日：2012-12-13
申请号：US13592937
申请日：2012-08-23
申请人： Carl A. REISER , Tommy SKIBA , Timothy W. PATTERSON, JR.
发明人： Carl A. REISER , Tommy SKIBA , Timothy W. PATTERSON, JR.
IPC分类号： H01M8/04 , H01M8/06
CPC分类号： H01M8/0656 , C25B1/04 , H01M8/04097 , H01M8/04201 , H01M8/04223 , H01M8/04228 , H01M8/04303 , H01M8/04447 , H01M8/04455 , H01M8/04552 , H01M8/04753 , H01M8/04761 , H01M2008/1095 , Y02E60/366
摘要： The invention is a hydrogen passivation shut down system for a fuel cell power plant (10, 200). During shut down of the plant (10, 200), hydrogen fuel is permitted to transfer between an anode flow path (24, 24′) and a cathode flow path (38, 38′) while a low-pressure hydrogen generator (202) selectively generates an adequate amount of hydrogen and directs flow of the low-pressure hydrogen into the fuel cell (12′) downstream from a hydrogen inlet valve (52′) to maintain the fuel cell (12′) in a passive state.
摘要翻译：本发明是用于燃料电池发电厂（10,200）的氢钝化关闭系统。在工厂（10,200）关闭期间，允许氢燃料在阳极流路（24,24'）和阴极流路（38,38'）之间传递，同时低压氢气发生器（202）选择性地产生足够量的氢气并且引导低压氢气进入氢气入口阀（52'）下游的燃料电池（12'），以将燃料电池（12'）保持在被动状态。

10. 发明授权

US07442453B1 Decontamination procedure for a fuel cell power plant 有权
标题翻译：燃料电池发电厂的净化程序
公开(公告)号：US07442453B1
公开(公告)日：2008-10-28
申请号：US11023148
申请日：2004-12-27
申请人： Timothy W. Patterson, Jr. , Michael L. Perry , Tommy Skiba , Ping Yu , Thomas D. Jarvi , James A. Leistra , Hiroshi Chizawa , Tsutomu Aoki
发明人： Timothy W. Patterson, Jr. , Michael L. Perry , Tommy Skiba , Ping Yu , Thomas D. Jarvi , James A. Leistra , Hiroshi Chizawa , Tsutomu Aoki
IPC分类号： H01M8/10
CPC分类号： H01M16/006 , H01M8/04097 , H01M8/04223 , H01M8/04238 , H01M8/043 , H01M8/04559 , H01M8/04679 , H01M8/04708 , H01M8/04731 , H01M8/04753 , H01M8/0488 , H01M8/0491 , H01M2250/10 , H01M2250/20 , H01M2250/30 , Y02B90/14 , Y02B90/18 , Y02P70/56 , Y02T90/32
摘要： A decontamination procedure for a fuel cell power plant (10) includes operating the plant to produce electrical power for an operating period, and then terminating operation of the plant (10) for a decontamination period, and then, whenever optimal electrical production of a plant fuel cell (12) is reduced by at least 5% by contaminants adsorbed by fuel cell electrodes (24, 42), decontaminating the fuel cell (12) of the plant (10) during the decontamination period by oxidizing contaminants adsorbed by electrodes (24, 42) of the fuel cell. Oxidizing the contaminants may be accomplished by various steps including exposing the electrodes (24, 42) to flowing oxygen; to heated flowing oxygen; to a sequence of start-stop cycles; and, to varying controlled potentials.
摘要翻译：燃料电池发电厂（10）的净化程序包括操作工厂以在运行期间产生电力，然后终止工厂（10）的去污时间段的操作，然后在工厂的最佳电力生产燃料电池（12）通过被燃料电池电极（24,42）吸附的污染物减少至少5％，在净化期间通过氧化被电极吸附的污染物（24）净化植物（10）的燃料电池（12），42）燃料电池。可以通过包括将电极（24,42）暴露于氧气的各种步骤来实现氧化污染物; 加热流动的氧气; 到一个开始 - 停止循环的序列; 并改变受控电位。

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