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    • 3. 发明申请
    • STABILIZED FUEL CELL FLOW FIELD
    • 稳定燃料电池流场
    • WO2008105751A2
    • 2008-09-04
    • PCT/US2005/047675
    • 2005-12-29
    • UTC POWER CORPORATIONMEYERS, Jeremy, P.
    • MEYERS, Jeremy, P.
    • H01M8/10
    • H01M8/04089H01M4/8642H01M8/0234H01M8/0243H01M8/026H01M8/0267H01M8/04029H01M8/04104H01M8/1004
    • A fuel cell (10) includes a cathode catalyst (26) for receiving a first reactant and an anode catalyst (24) for receiving an expected amount of a second reactant. The cathode catalyst (26) and the anode catalyst (24) respectively catalyze the first reactant and the second reactant to produce an electrochemical reaction that generates a flow of electrons between the cathode catalyst (26) and the anode catalyst (24) The amount of the first reactant consumed in the electrochemical reaction corresponds to a threshold amount of the second reactant needed to generate a forward flow of the electrons from the anode catalyst (24) to the cathode catalyst (26). A portion (42) of a fuel cell flow field includes a feature (54, 60, 80, W 1 , D 1 ) that restricts consumption of the first reactant.
    • 燃料电池(10)包括用于接收第一反应物的阴极催化剂(26)和用于接收预期量的第二反应物的阳极催化剂(24)。 阴极催化剂(26)和阳极催化剂(24)分别催化第一反应物和第二反应物以产生在阴极催化剂(26)和阳极催化剂(24)之间产生电子流的电化学反应。 在电化学反应中消耗的第一反应物对应于产生电子从阳极催化剂(24)向阴极催化剂(26)的向前流动所需的第二反应物的阈值。 燃料电池流场的部分(42)包括限制第一反应物的消耗的特征(54,60,80,W 1,D 1 1)。
    • 8. 发明申请
    • EVAPORATIVE COOLING OF FUEL CELLS EMPLOYING ANTIFREEZE SOLUTION
    • 燃料电池的蒸发冷却采用抗冻解决方案
    • WO2007064338A1
    • 2007-06-07
    • PCT/US2005/043942
    • 2005-12-01
    • UTC FUEL CELLS, LLCMEYERS, Jeremy, P.BALLIET, Ryan, J.
    • MEYERS, Jeremy, P.BALLIET, Ryan, J.
    • H01M8/04
    • H01M8/04029H01M8/04059H01M8/04164H01M8/04253H01M2008/1095
    • A fuel cell power plant (19) has a stack of fuel cells (20) cooled by a mixture of water with a non-volatile, miscible fluid that sufficiently depresses the freezing point, such as polyethylene glycol (PEG). The water and fluid are mixed in a reservoir (21), a small pump (22, 60) flows the mixture through coolant channels (28) in or adjacent water transport plates (29); heat of the catalytic reaction warms the water transport plates causing water to evaporate therefrom thereby cooling the stack. The PEG is non-volatile at stack operating temperature and does not evaporate; concentrated PEG is returned (33) to the reservoir (21). Water in the process air flow channels (41), including evaporated process water, is recovered in a condensation-rate-controlled (53, 54)) condenser (46) in communication (48) with the reservoir (21) for remixture with the concentrated PEG solution. Hydrophobic gas diffusion layers (72) shield the proton exchange membrane (70) from the PEG.
    • 燃料电池发电厂(19)具有由水与具有充分压低凝固点的不挥发性,可混溶的流体(例如聚乙二醇(PEG))的混合物冷却的一堆燃料电池(20)。 水和流体在储存器(21)中混合,小的泵(22,60)将混合物流过水输送板(29)中或其附近的冷却剂通道(28); 催化反应的热量加热水输送板,导致水从其中蒸发,从而冷却堆。 PEG在堆叠工作温度下不挥发,不蒸发; 浓缩的PEG被返回(33)到储存器(21)。 处理过程中的空气流通道(41),包括蒸发的工艺水,在与储存器(21)连通的冷凝速率控制(53,54)冷凝器(46)中回收,用于与 浓缩PEG溶液。 疏水性气体扩散层(72)屏蔽质子交换膜(70)与PEG。