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    • 6. 发明授权
    • Fuel cell with convoluted MEA
    • 燃料电池与复杂的MEA
    • US06663994B1
    • 2003-12-16
    • US09694386
    • 2000-10-23
    • Gerald W. FlyBrian K. Brady
    • Gerald W. FlyBrian K. Brady
    • H01M802
    • H01M8/2483H01M8/0228H01M8/0232H01M8/0234H01M8/0254H01M8/0258H01M8/1007H01M8/2415H01M2008/1095
    • A proton exchange membrane fuel cell including a membrane electrode assembly comprising a proton transmissive membrane, a catalytic anode layer on one face of the membrane, and a catalytic cathode layer on the other face of the membrane. The fuel cell further includes a gas distribution layer on each of the cathode and anode layers defining a gas flow field extending over each of the catalytic layers. The membrane electrode assembly has a convoluted configuration whereby to increase the ratio of membrane area to planar fuel cell area and thereby increase the electrical output of the fuel cell for a given planar area size fuel cell. The convoluted configuration of the membrane electrode assembly also facilitates the division of the gas distribution layers into separate parallel channels thereby allowing the use of an inexpensive foam material for the gas distribution layers irrespective of the inherent variations in porosity of foam materials.
    • 一种质子交换膜燃料电池,其包括膜电极组件,所述膜电极组件包括质子传递膜,所述膜的一个面上的催化阳极层和所述膜的另一面上的催化阴极层。 燃料电池还包括在每个阴极层和阳极层上的气体分布层,其限定了在每个催化层上延伸的气流场。 膜电极组件具有卷曲结构,从而增加膜面积与平面燃料电池面积的比率,从而增加给定平面面积尺寸燃料电池的燃料电池的电输出。 膜电极组件的回旋结构也有助于将气体分布层划分成单独的平行通道,从而允许使用廉价的泡沫材料用于气体分配层,而与泡沫材料的孔隙率的固有变化无关。
    • 9. 发明授权
    • Fuel cell with variable porosity gas distribution layers
    • 具有可变气孔分布层的燃料电池
    • US06566004B1
    • 2003-05-20
    • US09651934
    • 2000-08-31
    • Gerald W. FlyBrian K. Brady
    • Gerald W. FlyBrian K. Brady
    • H01M804
    • H01M8/0232H01M8/0234H01M8/0247H01M8/0258H01M8/0265H01M8/0267H01M8/04029H01M8/04074H01M8/0612H01M8/1007H01M8/241H01M8/2483H01M16/006H01M2300/0082
    • A proton exchange membrane fuel cell comprising a proton transmissive membrane, a catalytic anode layer on one face of the membrane, a catalytic cathode layer on the other face of the membrane, and a gas distribution layer on each of the cathode and anode layers defining a gas flow field extending over each of the catalytic layers. Each of the gas distribution layers comprises a layer of open cell conductive foam material which is divided into a plurality of generally parallel segments extending from one edge of the fuel cell to an opposite edge of the fuel cell whereby to define a plurality of generally parallel porous reactant paths extending across each catalytic layer. The segments may be defined by selectively varying the porosity of the foam material or selectively varying the thickness of the foam material. Reactant gases are delivered to the foam gas distribution layers via a manifold structure in which the reactant gases are moved upwardly along an edge of the fuel cell stack in parallel paths and selectively distributed within the stack at the desired cathode or anode levels by selective baffling and partitioning structures. A coolant layer may also be provided utilizing the same segmented foam construction utilized in the anode and cathode layers. The resultant fuel cell is lighter, smaller, and less expensive than prior art cells having comparable per surface area unit electrical energy output.
    • 一种质子交换膜燃料电池,包括质子传递膜,膜的一个面上的催化阳极层,膜的另一个表面上的催化阴极层,以及每个阴极层和阳极层上的气体分布层, 气体流场在每个催化层上延伸。 每个气体分配层包括开孔单元导电泡沫材料层,其分为从燃料电池的一个边缘延伸到燃料电池的相对边缘的多个大致平行的段,由此限定多个大致平行的多孔 反应物路径延伸穿过每个催化层。 可以通过选择性地改变泡沫材料的孔隙率或选择性地改变泡沫材料的厚度来限定段。 反应物气体经由歧管结构输送到泡沫气体分布层,其中反应物气体沿平行路径沿着燃料电池堆的边缘向上移动,并且通过选择性挡板在期望的阴极或阳极水平下选择性地分布在堆叠内, 分区结构。 还可以使用在阳极层和阴极层中使用的相同的分段泡沫结构来提供冷却剂层。 所得到的燃料电池比现有技术的具有相当于每个表面积单位电能输出的电池更轻,更小,更便宜。