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    • 1. 发明申请
    • MITIGATING ELECTRODE EROSION IN HIGH TEMPERATURE PEM FUEL CELL
    • 在高温PEM燃料电池中减轻电极腐蚀
    • US20120115058A1
    • 2012-05-10
    • US13261129
    • 2009-08-28
    • Robert M. DarlingParavastu BadrinarayananCarl A. Reiser
    • Robert M. DarlingParavastu BadrinarayananCarl A. Reiser
    • H01M8/04
    • H01M8/0432H01M8/04559H01M8/04753H01M8/0488H01M8/0491H01M2008/1095
    • A method of operating a fuel cell power plant (10) including a stack (11) of fuel cells having an anode catalyst layer and a cathode electrode (15) including a catalyst layer disposed on catalyst support material is characterized by, during normal operation of said power plant, adjusting the voltage of the stack to be substantially equal to or less than a predetermined maximum voltage for the temperature of the stack. Further, said step of adjusting comprises adjusting the stack voltage to the lesser of: a) a predetermined voltage above which corrosion of catalyst support material is significant and below which corrosion of catalyst support material is insignificant at the temperature of the stack; and b) a predetermined voltage above which dissolution of catalyst is significant and below which dissolution of the catalyst is insignificant at the temperature of the stack.
    • 一种操作包括具有阳极催化剂层的燃料电池堆(11)和包括设置在催化剂载体材料上的催化剂层的阴极电极(15)的燃料电池发电厂(10)的方法,其特征在于,在正常运行期间, 所述发电厂将所述堆的电压调整为基本上等于或小于所述堆的温度的预定最大电压。 此外,所述调节步骤包括将堆叠电压调整为较小的一个:a)预定电压,在该预定电压之上,催化剂载体材料的腐蚀是显着的,低于该预定电压,催化剂载体材料的腐蚀在堆叠温度下不显着; 和b)预定电压,其上催化剂的溶解是显着的,低于该电压时,催化剂的溶解在叠层的温度下是不显着的。
    • 7. 发明申请
    • REDUCED THERMAL CONDUCTIVITY IN PEM FUEL CELL GAS DIFFUSION LAYERS
    • 在PEM燃料电池气体扩散层中降低热导率
    • US20120202134A1
    • 2012-08-09
    • US13261250
    • 2009-10-08
    • Paravastu BadrinarayananRobert M. DarlingJonathan D. O'Neill
    • Paravastu BadrinarayananRobert M. DarlingJonathan D. O'Neill
    • H01M8/10
    • H01M8/0202H01M2008/1095
    • A fuel cell for a fuel cell power plant having gas diffusion layers which do not have microporous layers, includes a PEM (9), a cathode comprising at least a cathode catalyst (10) and a gas diffusion layer (17) on one side of the PEM, and an anode comprising at least an anode catalyst (11) and a gas diffusion layer (14) on the opposite side of the PEM, and a porous water transport plate having reactant gas flow field channels (31, 32) (21, 28) adjacent to each of said support substrates as well as water flow channels (22) in at least one of said water transport plates. The thermal conductivity of the cathode and/or the anode gas dif- fusion layers is less than about one-quarter of the thermal conductivity of conventional gas diffusion layers, less than about 0.25 W/m/K, to promote flow of water from the cathodes to the anodes and to the adjacent water transport plates, during start-up at normal ambient temperatures (lower than normal PEM fuel cell operating temperatures).
    • 一种具有不具有微孔层的气体扩散层的燃料电池发电厂的燃料电池,包括PEM(9),至少包含阴极催化剂(10)的阴极和在一侧的气体扩散层(17) 所述PEM和在所述PEM相反侧的至少包含阳极催化剂(11)和气体扩散层(14)的阳极和具有反应气体流场通道(31,32)(21,32)的多孔水输送板 ,28),以及至少一个所述水输送板中的水流通道(22)。 阴极和/或阳极气体扩散层的热导率小于常规气体扩散层的热传导率的约四分之一,小于约0.25W / m / K,以促进水从 在正常环境温度(低于正常的PEM燃料电池工作温度)的启动期间,阳极和相邻的水输送板的阴极。
    • 10. 发明申请
    • FUEL CELL WITH PURGE MANIFOLD
    • 燃料电池与灌注歧管
    • US20120003551A1
    • 2012-01-05
    • US13256326
    • 2009-03-18
    • Paravastu BadrinarayananKazuki Amemiya
    • Paravastu BadrinarayananKazuki Amemiya
    • H01M8/06H01M8/04
    • H01M8/0232H01M8/0267H01M8/04179H01M8/04223H01M8/04225H01M8/04228H01M8/2483
    • A fuel cell includes an electrode assembly having an electrolyte between an anode and a cathode for generating an electric current and byproduct water. A porous plate is located adjacent to the electrode and includes reactant gas channels for delivering a reactant gas to the electrode assembly. A separator plate is located adjacent the porous plate such that the porous plate is between the electrode assembly and the separator plate. The separator plate includes a reactant gas inlet manifold and a reactant gas outlet manifold in fluid connection with the reactant gas channels, and a purge manifold in fluid connection with the porous plate such that limiting flow of the reactant gas from the reactant gas outlet manifold and opening the purge manifold under a pressure of the reactant gas in the reactant gas channels drives the byproduct water toward the purge manifold for removal from the fuel cell.
    • 燃料电池包括在阳极和阴极之间具有电解质以产生电流和副产物水的电极组件。 多孔板位于电极附近,并且包括用于将反应气体输送到电极组件的反应气体通道。 分隔板位于多孔板附近,使得多孔板位于电极组件和分隔板之间。 隔板包括反应物气体入口歧管和与反应物气体通道流体连接的反应物气体出口歧管,以及与多孔板流体连接的净化歧管,从而限制反应气体从反应气体出口歧管和 在反应气体通道中的反应气体的压力下打开吹扫歧管,驱动副产物水朝向清洗歧管,以从燃料电池中移出。