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    Separator plate configuration for a fuel cell
    2.
    发明授权
    Separator plate configuration for a fuel cell 有权
    燃料电池分离板配置

    公开(公告)号：US08507137B2

    公开(公告)日：2013-08-13

    申请号：US12922724

    申请日：2008-04-23

    申请人： Glenn Michael Allen ,  Gennady Resnick

    发明人： Glenn Michael Allen ,  Gennady Resnick

    IPC分类号： H01M8/04

    CPC分类号： H01M8/0204 ,  H01M8/023 ,  H01M8/0258 ,  H01M8/0267 ,  H01M8/04104 ,  H01M8/04119

    摘要： A fuel cell includes a membrane electrode assembly comprised of a membrane sandwiched between anode and cathode catalyst structures. An anode separator plate and a cathode separator plate are arranged adjacent to the membrane electrode assembly opposite from one another. The anode and cathode separator plates include opposing sides in which one of the opposing sides of the anode and cathode respectively have fuel and oxidant flow fields in communication with the membrane. The anode separator plate is a structure having a first water permeability and is configured to permit passage of water between its opposing sides and with its flow field, and the cathode separator plate comprises a structure having a second water permeability less than the first water permeability of the anode separator plate. In one example, the anode is provided by a porous separator plate, and the cathode is provided by a non-porous, or solid, plate.

    摘要翻译： 燃料电池包括由夹在阳极和阴极催化剂结构之间的膜构成的膜电极组件。 阳极隔板和阴极隔板相邻地布置在膜电极组件的附近。 阳极和阴极隔板包括相对的侧面，阳极和阴极的相对侧中的一个分别具有与膜连通的燃料和氧化剂流场。 阳极隔板是具有第一透水性的结构，其构造成允许水在其相对侧和其流场之间通过，并且阴极隔板包括具有小于第一透水性的第二透水性的结构 阳极隔板。 在一个实例中，阳极由多孔隔板提供，阴极由无孔或固体板提供。

    POROUS PLATE FOR A FUEL CELL
    3.
    发明申请
    POROUS PLATE FOR A FUEL CELL 审中-公开
    用于燃料电池的多孔板

    公开(公告)号：US20080160366A1

    公开(公告)日：2008-07-03

    申请号：US11617999

    申请日：2006-12-29

    申请人： Glenn M. Allen ,  Gennady Resnick

    发明人： Glenn M. Allen ,  Gennady Resnick

    IPC分类号： H01M2/16

    CPC分类号： H01M8/0234 ,  H01M8/04059 ,  H01M8/04074 ,  H01M8/04164 ,  H01M2008/1095 ,  Y02P70/56

    摘要： In one example, a fuel cell utilizes a non-carbonized, non-graphitized porous polymer water transport plate having a water permeability of less than 30×10−17 m2. The water transport plate is part of a fuel cell that employs an evaporative cooling loop. In one example, the water transport plate has a bubble pressure of less than 5 psig. The water transport plate is less costly and easier to manufacture.

    摘要翻译： 在一个实例中，燃料电池利用具有小于30×10 -6平方厘米的透水性的非碳化的非石墨化多孔聚合物水输送板。 水输送板是采用蒸发冷却回路的燃料电池的一部分。 在一个示例中，水输送板的气泡压力小于5psig。 水运板价格低廉，制造容易。

    Initiating operation of an electric vehicle or other load powered by a fuel cell at sub-freezing temperature
    5.
    发明授权
    Initiating operation of an electric vehicle or other load powered by a fuel cell at sub-freezing temperature 有权
    在次冷冻温度下启动由燃料电池供电的电动车辆或其他负载

    公开(公告)号：US06673481B1

    公开(公告)日：2004-01-06

    申请号：US10390439

    申请日：2003-03-17

    申请人： Carl A. Reiser ,  Gennady Resnick ,  Neil A. Popovich

    发明人： Carl A. Reiser ,  Gennady Resnick ,  Neil A. Popovich

    IPC分类号： H01M804

    CPC分类号： H01M8/04223 ,  H01M8/0258 ,  H01M8/0267 ,  H01M8/04022 ,  H01M8/04156 ,  H01M8/04302 ,  H01M8/241 ,  H01M8/2457

    摘要： A vehicle (150) includes a fuel cell stack (151) started when the stack is below freezing, by connection (158) to the vehicle propulsion system (159) within a few seconds of starting the flow of fuel (179) and oxidant (173), or when open circuit voltage (155, 156) is detected. The fuel is in excess of stochiometry requirement and the oxidant is in excess of at least twice stochiometric requirement, either may be at about atmospheric pressure or at 4 kPa (0.6 psi) or more above the pressure of any water in said water passages, and either may be below freezing. Water transport plates (84, 86, 88, 89) have water passages connected to a water circulation loop (170) including a reservoir (164) having an auxiliary heater (161) connected (160) to the stack. Warming of cell stack materials and ice in the water transport plates, heat of fusion of melting ice, warming of melted water, and evaporative cooling of water melted in the water transport plates keep the fuel cell cool until liquid coolant can be circulated.

    摘要翻译： 车辆（150）包括当起动燃料（179）和氧化剂（179）的流动的几秒钟内，通过在车辆推进系统（159）上连接（158）而在堆栈低于冰点时启动的燃料电池堆（151） 173），或者当检测到开路电压（155,156）时。 燃料超过了化学计量要求，氧化剂超过了至少两次化学计量要求，可能处于大气压或高于所述水通道中任何水的压力的4kPa（0.6psi）或更高，以及 可能低于冰点。 水输送板（84,86,88,89）具有连接到水循环回路（170）的水通道，水循环回路（170）包括具有与堆叠连接（160）的辅助加热器（161）的储存器（164）。 水输送板中的电池堆料和冰的变暖，熔化冰融化的热量，熔融水的升温以及在水输送板中熔化的水的蒸发冷却使得燃料电池冷却直到液体冷却剂可循环。

    Method and apparatus for the operation of a cell stack assembly during subfreezing temperatures
    6.
    发明授权
    Method and apparatus for the operation of a cell stack assembly during subfreezing temperatures 失效
    在解冻温度期间操作细胞堆叠组件的方法和装置

    公开(公告)号：US07282285B2

    公开(公告)日：2007-10-16

    申请号：US10473989

    申请日：2002-04-05

    申请人： Harold T. Couch ,  Carl A. Reiser ,  Gennady Resnick ,  Deliang Yang ,  Emily A. Dykeman ,  David A. Condit

    发明人： Harold T. Couch ,  Carl A. Reiser ,  Gennady Resnick ,  Deliang Yang ,  Emily A. Dykeman ,  David A. Condit

    IPC分类号： H01M8/04

    CPC分类号： H01M8/04253 ,  H01M8/0267 ,  H01M8/04029 ,  H01M8/04303 ,  H01M8/2457 ,  H01M8/2465

    摘要： A cell stack assembly (102) coolant system comprises a coolant exhaust conduit (110) in fluid communication with a coolant exhaust manifold (108) and a coolant pump (112). A coolant inlet conduit (120) enables transportation of the coolant to the coolant inlet manifold. The coolant system further includes a bypass conduit (132) in fluid communication with the coolant exhaust manifold and the coolant inlet manifold, while a bleed valve (130) is in fluid communication with the coolant exhaust conduit and a source of gas. Operation of the bleed valve enables venting of the coolant from the coolant channels, and through a shut down conduit (124). An increased pressure differential between the coolant and reactant gases forces water out of the pores in the electrode substrates (107,109). An ejector (250) prevents air form inhibiting the pump. Pulsed air is blown (238,239,243,245) through the coolant channels to remove more water.

    摘要翻译： 电池堆组件（102）冷却剂系统包括与冷却剂排气歧管（108）和冷却剂泵（112）流体连通的冷却剂排放导管（110）。 冷却剂入口管道（120）能够将冷却剂输送到冷却剂入口歧管。 冷却剂系统还包括与冷却剂排出歧管和冷却剂入口歧管流体连通的旁通管道（132），而排放阀（130）与冷却剂排放管道和气体源流体连通。 泄放阀的操作使冷却剂从冷却剂通道排出，并通过关闭导管（124）。 冷却剂和反应气体之间的增加的压差迫使水从电极基板（107,109）中的孔隙中流出。 喷射器（250）防止空气形式阻止泵。 脉冲空气通过冷却剂通道吹出（238,239,243,245）以除去更多的水。

    Method of using graphite for making hydrophilic articles
    7.
    发明申请
    Method of using graphite for making hydrophilic articles 审中-公开
    使用石墨制造亲水制品的方法

    公开(公告)号：US20070147187A1

    公开(公告)日：2007-06-28

    申请号：US11320517

    申请日：2005-12-28

    申请人： Gennady Resnick ,  Glenn M. Allen

    发明人： Gennady Resnick ,  Glenn M. Allen

    IPC分类号： B32B9/00 ,  C09C1/44 ,  G11B11/00

    CPC分类号： H01M8/0234 ,  H01M8/0258 ,  H01M8/0267 ,  H01M8/0276 ,  Y02P70/56 ,  Y10T428/30

    摘要： A water transport plate assembly that is useful in fuel cells includes at least one hydrophilic article such as a flow field layer. A method of making the hydrophilic article includes establishing a hydrophilicity of the article by including a plurality of graphite particles (112) having a particular physical characteristic that imparts the hydrophilicity to the article. In one disclosed example, the selected graphite particles (112) have a wettability ratio of a hydrophilic surface area to a total surface area that is sufficient to make the article hydrophilic. In a disclosed example, the wettability ratio is more than 0.10. In a disclosed example, the graphite particles are selected based upon a percentage of prismatic surface area of the total surface area.

    摘要翻译： 可用于燃料电池的水输送板组件包括至少一个亲水制品，如流场层。 制备亲水制品的方法包括通过包括具有赋予制品亲水性的特定物理特性的多个石墨颗粒（112）来确定制品的亲水性。 在一个公开的实施例中，所选择的石墨颗粒（112）具有足以使制品亲水的亲水表面积与总表面积的润湿性比。 在公开的实施例中，润湿性比大于0.10。 在公开的示例中，基于总表面积的棱镜表面积的百分比来选择石墨颗粒。

    End-cell thermal distancing for fuel cell system
    8.
    发明授权
    End-cell thermal distancing for fuel cell system 有权
    燃料电池系统的终端热隔离

    公开(公告)号：US06824901B2

    公开(公告)日：2004-11-30

    申请号：US10225527

    申请日：2002-08-21

    申请人： Carl A. Reiser ,  Gennady Resnick

    发明人： Carl A. Reiser ,  Gennady Resnick

    IPC分类号： H01M802

    CPC分类号： H01M8/04029 ,  H01M8/0234 ,  H01M8/04228 ,  H01M8/04253 ,  H01M8/04303 ,  H01M8/241 ,  H01M8/248

    摘要： A PEM fuel cell system includes a plurality of PEM fuel cells arranged in a stack having two opposed, outwardly facing end surfaces; pressure plates positioned relative to said end surfaces for securing said PEM fuel cells in said stack; and spacer members between said end surfaces and said pressure plates for thermally insulating said end surfaces from said pressure plates.

    摘要翻译： PEM燃料电池系统包括布置在具有两个相对的面向外的端面的堆叠中的多个PEM燃料电池; 相对于所述端面定位的压板，用于将所述PEM燃料电池固定在所述堆叠中; 以及在所述端面和所述压板之间的间隔件，用于将所述端面与所述压板绝热。

    Performance recovery process for PEM fuel cells
    9.
    发明授权
    Performance recovery process for PEM fuel cells 有权
    PEM燃料电池的性能恢复过程

    公开(公告)号：US06709777B2

    公开(公告)日：2004-03-23

    申请号：US10103584

    申请日：2002-03-20

    申请人： Patrick L. Hagans ,  Gennady Resnick

    发明人： Patrick L. Hagans ,  Gennady Resnick

    IPC分类号： H01M800

    CPC分类号： H01M8/04119 ,  H01M8/0258 ,  H01M8/0267 ,  H01M8/04223 ,  H01M8/241 ,  H01M8/2484

    摘要： Recovery of PEM fuel cell performance is achieved by evacuating (61, 62) or by flowing water absorbing gas (46) through, or both, the fuel flow field (12, 13, 19, 20), the air flow field (25, 26, 30, 31), and the water flow field (36, 39), while resistance of the individual cells, or of the fuel cell stack, is measured; the dry out process is continued until the resistance of the cells (or the resistance per cell, measured across the fuel cell stack as a whole), has increased by at least 5 to 1 (preferably 10 to 1) over the normal resistance of the cells. The water absorbing gas may be air (23) or nitrogen (47); it may be at ambient temperature or heated (50).

    摘要翻译： PEM燃料电池性能的恢复是通过抽空（61,62）或使吸水气体（46）流过燃料流场（12,13,19,20），或者两者都通过气流场（25， 26,30,31）和水流场（36,39），同时测量各个电池或燃料电池堆的电阻; 干燥过程继续进行，直到细胞的电阻（或整个燃料电池堆上测量的每个电池的电阻）与正常电阻相比增加至少5至1（优选10至1） 细胞。 吸水气体可以是空气（23）或氮气（47）; 它可能在环境温度或加热（50）。