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    • 2. 发明授权
    • Fuel cell separator plate assembly
    • 燃料电池分离板组件
    • US08758958B2
    • 2014-06-24
    • US12856732
    • 2010-08-16
    • Richard D. BreaultWarren L. LuomaRobert P. Roche
    • Richard D. BreaultWarren L. LuomaRobert P. Roche
    • H01M8/04H01M8/24
    • H01M8/0213H01M8/0221H01M8/0226H01M8/0228
    • A fuel cell separator plate assembly (20) includes a separator plate layer (22) and flow field layers (24, 26). In one disclosed example, the separator plate layer (22) comprises graphite and a hydrophobic resin. The hydrophobic resin of the separator plate layer (22) serves to secure the separator plate layer to flow field layers on opposite sides of the separator plate layer. In one example, at least one of the flow field layers (24, 26) comprises graphite and a hydrophobic resin such that the flow field layer is hydrophobic and nonporous. In another example, two graphite and hydrophobic resin flow field layers are used on opposite sides of a separator plate layer. One disclosed example includes all three layers comprising graphite and a hydrophobic resin.
    • 燃料电池分离器板组件(20)包括隔板层(22)和流场层(24,26)。 在一个公开的示例中,隔板层(22)包括石墨和疏水性树脂。 隔板层(22)的疏水性树脂用于将隔板层固定在隔板层的相对侧上的流场层。 在一个示例中,流场层(24,26)中的至少一个包括石墨和疏水性树脂,使得流场层是疏水且无孔的。 在另一个实例中,在隔板层的相对侧上使用两个石墨和疏水树脂流场层。 一个公开的示例包括包括石墨和疏水性树脂的所有三个层。
    • 3. 发明申请
    • FUEL CELL SEPARATOR PLATE ASSEMBLY
    • 燃油电池分离板组件
    • US20100307681A1
    • 2010-12-09
    • US12856732
    • 2010-08-16
    • Richard D. BreaultWarren L. LuomaRobert P. Roche
    • Richard D. BreaultWarren L. LuomaRobert P. Roche
    • H01M2/00
    • H01M8/0213H01M8/0221H01M8/0226H01M8/0228
    • A fuel cell separator plate assembly (20) includes a separator plate layer (22) and flow field layers (24, 26). In one disclosed example, the separator plate layer (22) comprises graphite and a hydrophobic resin. The hydrophobic resin of the separator plate layer (22) serves to secure the separator plate layer to flow field layers on opposite sides of the separator plate layer. In one example, at least one of the flow field layers (24, 26) comprises graphite and a hydrophobic resin such that the flow field layer is hydrophobic and nonporous. In another example, two graphite and hydrophobic resin flow field layers are used on opposite sides of a separator plate layer. One disclosed example includes all three layers comprising graphite and a hydrophobic resin.
    • 燃料电池分离器板组件(20)包括隔板层(22)和流场层(24,26)。 在一个公开的示例中,隔板层(22)包括石墨和疏水性树脂。 隔板层(22)的疏水性树脂用于将隔板层固定在隔板层的相对侧上的流场层。 在一个示例中,流场层(24,26)中的至少一个包括石墨和疏水性树脂,使得流场层是疏水且无孔的。 在另一个实例中,在隔板层的相对侧上使用两个石墨和疏水树脂流场层。 一个公开的示例包括包括石墨和疏水性树脂的所有三个层。
    • 7. 发明授权
    • Integrated fuel cell stack shunt current prevention arrangement
    • 集成燃料电池堆分流电流防止装置
    • US5079104A
    • 1992-01-07
    • US670845
    • 1991-03-18
    • Robert P. RocheMichael P. Nowak
    • Robert P. RocheMichael P. Nowak
    • H01M8/02H01M8/24
    • H01M8/2415H01M8/0271H01M8/0297
    • A fuel cell stack includes a plurality of fuel cells juxtaposed with one another in the stack and each including a pair of plate-shaped anode and cathode electrodes that face one another, and a quantity of liquid electrolyte present at least between the electrodes. A separator plate is interposed between each two successive electrodes of adjacent ones of the fuel cells and is unified therewith into an integral separator plate. Each integral separator plate is provided with a circumferentially complete barrier that prevents flow of shunt currents onto and on an outer peripheral surface of the separator plate. This barrier consists of electrolyte-nonwettable barrier members that are accommodated, prior to the formation of the integral separator plate, in corresponding edge recesses situated at the interfaces between the electrodes and the separator plate proper. Each barrier member extends over the entire length of the associated marginal portion and is flush with the outer periphery of the integral separator plate. This barrier also prevents cell-to-cell migration of any electrolyte that may be present at the outer periphery of the integral separator plate while the latter is incorporated in the fuel cell stack.
    • 燃料电池堆包括在堆叠中彼此并置的多个燃料电池,并且每个燃料电池包括彼此面对的一对板状阳极和阴极电极,以及至少存在于电极之间的液体电解质的量。 隔板相邻的燃料电池的两个连续的电极之间插入隔板,并将其与其一体分隔板一体化。 每个整体分离板设置有周向完整的屏障,其防止分流电流流到隔板的外周表面上和外侧。 该阻挡层由电解质不可润湿的阻挡构件组成,在形成整体隔板之前,在位于电极和隔板本体之间的界面处的相应的边缘凹槽中容纳电解质不可润湿的阻挡构件。 每个阻挡构件在相关边缘部分的整个长度上延伸并且与整体隔离板的外周齐平。 该阻挡层也可防止可能存在于整体隔离板的外周边的任何电解质的细胞间迁移,同时将其结合到燃料电池堆中。
    • 10. 发明授权
    • Fuel mixing control for fuel cell power plants operating on multiple fuels
    • 用于燃料电池发电厂的燃料混合控制,用于多种燃料
    • US06890671B2
    • 2005-05-10
    • US10324454
    • 2002-12-19
    • Robert P. RochePaul R. MargiottJohn C. Trocciola
    • Robert P. RochePaul R. MargiottJohn C. Trocciola
    • C01B3/02H01M8/04H01M8/06H02J20060101
    • H01M8/04089H01M8/0612Y02E70/20
    • Fuel mixing control arrangements are provided for fuel cell power plants (10) operating on multiple fuels (22, 24, 26). A fuel delivery system (16) supplies hydrogen-rich fuel (20) to the cell stack assembly (CSA) (12) after controlled mixing of a primary fuel (22) and at least a secondary fuel (24), each having a respective “equivalent hydrogen (H2) content”. The relative amounts of the primary fuel (22) and secondary fuel (24) mixed are regulated (18, 34, 36) to provide at least a minimum level (LL) of hydrogen-rich fuel having an equivalent hydrogen content sufficient for normal operation of the CSA (12). The primary fuel (22) is a bio-gas or the like having a limited, possibly variable, equivalent H2 content, and the secondary fuel (22) has a greater and relatively constant equivalent H2 content and is mixed with the primary fuel in an economic, constant relationship that assures adequate performance of the CSA (12). One or more parameters (IDC, P, V, E. C.) of the operating power plant (10) related to the equivalent H2 content of at least the primary fuel may be sensed (72, 26, 78, 84, 176) and used to control (18, 36) the relative amounts of secondary and primary fuels (22, 24) mixed in response thereto.
    • 为燃料电池发电厂(10)提供燃料混合控制装置,燃料电池发电厂(10)在多种燃料(22,24,26)上运行。 燃料输送系统(16)在主燃料(22)和至少二级燃料(24)的受控混合之后,向细胞堆叠组件(CSA)(12)供应富氢燃料(20) “等同氢(H 2 N 2)含量”。 调节混合的主燃料(22)和二次燃料(24)的相对量(18,34,36)以提供具有足够正常操作的等效氢含量的至少最低水平(LL)的富氢燃料 的CSA(12)。 主要燃料(22)是具有有限的,可能变化的等同H 2 O 2含量的生物气体等,并且二次燃料(22)具有更大且相对恒定的等效H 2含量, 与主要燃料混合,经济,不断的关系,确保CSA的充分表现(12)。 可以感测与至少主要燃料的等效H 2 N 2含量有关的工作电厂(10)的一个或多个参数(IDC,P,V,EC)(72,26,78 ,84,176),并且用于控制(18,36)响应于此混合的二级和一级燃料(22,24)的相对量。