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    • 3. 发明申请
    • FUEL CELL EMPLOYING HYDRATED NON-PERFLUORINATED HYDROCARBON LON EXCHANGE MEMBRANE
    • 采用水化非全氟化烃交换膜的燃料电池
    • WO2007139550A1
    • 2007-12-06
    • PCT/US2006/020982
    • 2006-05-30
    • UTC FUEL CELLS, LLCDARLING, Robert, M.PROTSAILO, Lesia, V.GUPTA, Shruti, Modi
    • DARLING, Robert, M.PROTSAILO, Lesia, V.GUPTA, Shruti, Modi
    • H01M4/86
    • H01M8/023H01M4/8605H01M4/921H01M8/04126H01M8/1007H01M2008/1095
    • Fuel cells (9) include unitized electrode assemblies (12) having a non- perfluorinated hydrocarbon ionomer exchange membrane (26) with anode and cathode catalysts (27, 28) disposed on opposite sides thereof. Adjacent the catalysts, respective optional sublayers (29, 30) may be supported by corresponding gas diffusion layers (31, 32), with adjacent porous, hydrophilic, water transferring reactant gas flow field plates (13, 14) having respective fuel (17) and oxidant (23) reactant gas flow field channels. Water channels (18, 19, 20) hydrate the membrane (26), clear the product water from the cathode (28, 30, 32), flush peroxide radicals, and may also cool the fuel cells. Improved performance (124) (higher voltage at higher current densities) is achieved along with elimination of a propensity for degradation from peroxide decomposition products resulting from oxygen solubility of perfluorinated membranes. Platinum/ruthenium alloy anode catalysts improve performance without degradation which occurs with perfluorinated membranes.
    • 燃料电池(9)包括具有设置在其相对侧上的阳极和阴极催化剂(27,28)的非全氟化烃离聚物交换膜(26)的单元化电极组件(12)。 邻近催化剂,相应的可选择的子层(29,30)可以由相应的气体扩散层(31,32)支撑,具有相应的具有相应燃料(17)的多孔,亲水的水转移反应气体流场板(13,14) 和氧化剂(23)反应气体流场通道。 水通道(18,19,20)使膜(26)水合,从阴极(28,30,32)清除产物水,冲洗过氧化物自由基,还可以冷却燃料电池。 实现了改进的性能(124)(更高的电流密度下的更高的电压),同时消除了由全氟化膜的氧气溶解度引起的过氧化物分解产物降解的倾向。 铂/钌合金阳极催化剂改善了性能,而不会随着全氟化膜发生降解。