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    • 74. 发明授权
    • Heat treat configuration for porous carbon-carbon composites
    • 多孔碳 - 碳复合材料的热处理配置
    • US08357253B2
    • 2013-01-22
    • US12739205
    • 2007-12-17
    • Richard D. Breault
    • Richard D. Breault
    • B29C65/02H01M4/88
    • B65G57/00C04B35/64C04B35/83C04B2235/9623H01M8/0234H01M8/0245H01M8/086H01M2008/1095Y02E60/50
    • A method of heat treating a substrate for a fuel cell includes stacking substrates to form a group. A dimension is determined for a plate corresponding to a resulting mass that is less than a predetermined mass. The plate is arranged above the group to apply a weight of the plate to the group. The resulting masses for spacer plates and intermediate lifting plates, for example, are minimized to reduce the pressure differential between the bottom and top substrates in the heat treat assembly. In another disclosed method, a dimension for a plate, such as a top plate, is determined that corresponds to a resulting mass that is greater than a predetermined mass. The plate is arranged above the group to apply a weight of the plate to the group. The top plate resulting mass is selected to minimize a variation in the average pressure of the substrates throughout the heat treat assembly.
    • 一种用于燃料电池的基板的热处理方法包括堆叠基板以形成一组。 对于对应于小于预定质量的所得质量的板来确定尺寸。 板被布置在组上方以将板的重量施加到组。 例如,用于间隔板和中间提升板的所得质量被最小化以减少热处理组件中的底部和顶部基底之间的压力差。 在另一公开的方法中,确定板的尺寸,例如顶板,其对应于大于预定质量的所得质量。 板被布置在组上方以将板的重量施加到组。 选择顶板产生的质量以最小化整个热处理组件中的基底的平均压力的变化。
    • 77. 发明申请
    • AMMONIA CONTACT SCRUBBER SYSTEM FOR A FUEL CELL
    • 用于燃料电池的AMMONIA接触式SCRUBBER系统
    • US20100024648A1
    • 2010-02-04
    • US12448380
    • 2006-12-20
    • Richard D. Breault
    • Richard D. Breault
    • B01D53/14
    • B01D53/58B01D2251/512B01D2256/16H01M8/0618H01M8/0662Y02A50/2346
    • An ammonia contact scrubber system (10) for removing ammonia from a fuel stream for a fuel cell (16) includes a contact scrubber (12) having a scrubber fuel inlet (14) and a scrubber fuel exhaust (20) for directing flow of the fuel stream through support material (24) within the scrubber (12) and into the fuel cell (16). An acid circulating loop (26) has an acid holding tank (28) holding a liquid acid solution (30), an acid feed line (32) secured in fluid communication between the holding tank (28) and a scrubber acid inlet (36) of the contact scrubber (12), an acid return (38) for returning the acid solution from the scrubber (12) to the acid holding tank (28), and an acid circulation pump (42) for pumping the acid solution (30) through the acid circulating loop (26) and through the support material (24) within the scrubber (12).
    • 用于从用于燃料电池(16)的燃料流中去除氨的氨接触洗涤器系统(10)包括具有洗涤器燃料入口(14)和洗涤器燃料排出口(20)的接触洗涤器(12),用于引导 燃料流通过洗涤器(12)内的支撑材料(24)并进入燃料电池(16)。 酸性循环回路(26)具有保持液体酸性溶液(30)的酸性储存罐(28),在储存罐(28)和洗涤器酸入口(36)之间流体连通的酸性供给管线(32) 的接触洗涤器(12),用于将酸洗液从洗涤器(12)返回到酸储槽(28)的酸回流(38)和用于泵送酸溶液(30)的酸循环泵(42) 通过酸循环回路(26)并通过洗涤器(12)内的支撑材料(24)。
    • 79. 发明授权
    • Fuel cell with thermal conductance of cathode greater than anode
    • 燃料电池的阳极电导率大于阴极
    • US07429429B2
    • 2008-09-30
    • US10859014
    • 2004-06-02
    • Richard D. Breault
    • Richard D. Breault
    • H01M4/00
    • H01M8/1004H01M4/8605H01M4/8636H01M8/0245H01M8/04149
    • In a fuel cell for a fuel cell power plant having a PEM (9), a cathode comprising at least a catalyst (10) and a support substrate (17), possibly with a diffusion layer (16), on one side of the PEM, and an anode comprising at least an anode support substrate (14) and an anode catalyst (11) 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 conductance of the cathode is less than about one-half of the thermal conductance of the anode, and preferably less than one-quarter of the thermal conductance of the anode, to promote flow of water from the cathode to the anode and to the adjacent water transport plate, obviating the need, in some cases, for water or reactant pressure pumps.
    • 在具有PEM(9)的燃料电池发电厂的燃料电池中,至少包含催化剂(10)和支撑基板(17)的阴极,可能具有扩散层(16),在PEM的一侧 ,以及阳极,所述阳极至少包括位于所述PEM相反侧的阳极支撑基板(14)和阳极催化剂(11),以及具有反应气体流场通道(31,32)(21,28)的多孔水输送板 )和所述水输送板中的至少一个中的每个所述支撑基板以及水流通道(22)相邻,所述阴极的热导率小于所述阳极的热导率的约一半,优选地, 小于阴极热导率的四分之一,以促进水从阴极到阳极和相邻的水输送板的流动,从而避免了在某些情况下水或反应物压力泵的需要。