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    • 5. 发明授权
    • Fuel cell system and fuel control method
    • 燃料电池系统和燃料电池控制方法
    • US08216731B2
    • 2012-07-10
    • US11702088
    • 2007-02-05
    • Shigeru InaiHiromichi YoshidaRyo Jinba
    • Shigeru InaiHiromichi YoshidaRyo Jinba
    • H01M8/04
    • H01M8/04089H01M8/04007H01M8/04253H01M8/04343H01M8/04589H01M8/04753H01M8/04761H01M2008/1095H01M2250/20Y02T90/32
    • A fuel cell system includes a fuel cell and a supplying unit, which supplies reactive gases to the fuel cell. A control unit includes a power production effective area calculator calculates the areas of the electrodes available for power production as a power production effective area. A current density calculator which calculates a current density of the power production effective area calculated by the power production effective area calculator based on the total amount of power required by the fuel cell. A gas supply amount determiner determines the amount of reactive gas to be supplied to the fuel cell depending on the current density. A gas supply controller controls the supplying unit so as to supply the amount of reactive gas determined by the gas supply amount determiner to the fuel cell.
    • 燃料电池系统包括燃料电池和供应单元,其向燃料电池供应反应性气体。 控制单元包括功率产生有效面积计算器计算可用于发电的电极的面积作为发电生产有效面积。 电流密度计算器,其基于由所述燃料电池所需的总功率计算由所述发电生产有效面积计算器计算出的发电有效面积的电流密度。 气体供给量确定器根据电流密度确定供给到燃料电池的反应气体的量。 气体供给控制器控制供给单元,以将由气体供给量确定器确定的反应气体的量供给到燃料电池。
    • 7. 发明申请
    • Fuel cell stack
    • 燃料电池堆
    • US20080187805A1
    • 2008-08-07
    • US12012322
    • 2008-02-01
    • Ryo JinbaShigeru Inai
    • Ryo JinbaShigeru Inai
    • H01M8/04
    • H01M8/04052H01M8/2415H01M8/2484H01M2008/1095
    • A fuel cell stack includes a first end power generation unit and a first dummy unit adjacent to a power generation unit at one end of a stack body in a stacking direction. In the first end power generation unit, a first separator is stacked on the power generation unit, a first membrane electrode assembly is stacked on the first separator, a second separator is stacked on the first membrane electrode assembly, an electrically conductive plate is stacked on the second separator, and a third separator is stacked on the electrically conductive plate. A coolant is supplied to a coolant flow field formed between the power generation unit and the first end power generation unit, for cooling a second membrane electrolyte assembly of the power generation unit and the first membrane electrode assembly of the first end power generation unit.
    • 燃料电池堆包括在层叠方向上的堆叠体的一端处的与发电单元相邻的第一端部发电单元和第一虚拟单元。 在第一端发电单元中,在发电单元上堆叠第一隔板,在第一隔板上层叠第一膜电极接合体,在第一膜电极接合体上层叠第二隔板,将导电性板堆叠在 第二分离器和第三分离器堆叠在导电板上。 冷却剂被供给到形成在发电单元和第一端部发电单元之间的冷却剂流场,用于冷却发电单元的第二膜式电解质组件和第一端部发电单元的第一膜电极组件。
    • 9. 发明申请
    • Electrode structure for solid polymer type fuel cell
    • 固体聚合物型燃料电池的电极结构
    • US20060068269A1
    • 2006-03-30
    • US10532963
    • 2003-10-21
    • Kaoru FukudaMasaki TaniHayato KajiShigeru InaiTakeshi MuroShinya Watanabe
    • Kaoru FukudaMasaki TaniHayato KajiShigeru InaiTakeshi MuroShinya Watanabe
    • H01M4/94H01M4/96H01M8/10H01M8/04
    • H01M8/1004H01M4/8605H01M4/8657H01M4/926
    • A water holding layer having a carbon-based material and a water holding material is arranged on an anode diffusion layer. The water holding material is contained at 5 to 20 wt % of total weight of the water holding material and an electron conductive material. Alternatively, carbon particles having water absorption amount at saturated water vapor pressure at 60° C. is not less than 150 cc/g are contained in the anode diffusion layer. Water absorption ratio of the anode diffusion layer at 60° C. is in a range of 40 to 85%, a differential pressure is in a range of 60 to 120 mmaq, and a ratio of quantity of electric charge of catalytic material of the cathode catalytic layer existing in proton conductive passage from the polymer electrolyte membrane is not less than 15% of the quantity of electric charge of all the catalytic material existing in the cathode catalytic layer. Furthermore, a layer including carbon particles having water absorption amount at saturated water vapor pressure at 60° C. of not less than 150 cc/g and fluorine resin, is arranged on a carbon-based material having a contact angle with water of not more than 90° by performing a hydrophilic treatment. The water absorption ratio at 60° C. is in a range of 40 to 85 wt %, and the penetration resistance is not more than 5 mΩ.
    • 具有碳基材料和保水材料的保水层设置在阳极扩散层上。 保水材料的含水量为水保持材料的总重量的5〜20重量%和电子传导性材料。 或者,阳极扩散层中含有在60℃的饱和水蒸气压下的吸水量为150cc / g以上的碳粒子。 阳极扩散层在60℃下的吸水率在40〜85%的范围内,差压在60〜120mm范围内,阴极的催化剂材料的电荷比例 存在于高分子电解质膜的质子传导路径中的催化剂层不低于存在于阴极催化剂层中的所有催化材料的电荷量的15%。 此外,将具有不低于150cc / g的饱和水蒸汽压在60℃以下的吸水量为150cc / g以上的碳粒子和氟树脂的层设置在与水不接触的接触角的碳系材料上 超过90°。 60℃下的吸水率为40〜85重量%,耐渗透性为5mOmega以下。