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    • 7. 发明公开
    • Power generation system using molten carbonate fuel cell
    • 采用熔融碳酸盐燃料电池的发电系统
    • EP0429958A2
    • 1991-06-05
    • EP90121804.0
    • 1990-11-14
    • Ishikawajima-Harima Heavy Industries Co., Ltd.
    • Koga, MinoruWatanabe, TakenoriKamata, ToshioMorishima, SatoshiMizusawa, MinoruKobayashi, Kazunori
    • H01M8/06
    • H01M8/0612H01M8/0625H01M8/145Y02E60/526
    • A power generation system uses fuel cells (C, S) stacked via separators (31). Cooling plates (33) are provided in the fuel cell stack (S). Passages (34) are formed in each cooling plate (33) for allowing raw-­material-gas-for-reformation (which also serves as stack-cooling-gas) to flow therethrough and the passages (34) are filled with reforming catalyst (61). An external reformer (37) which includes a combustion section (39) and a reforming section (38) is provided outside of the fuel cell stack (5). A stack-cooling-­gas-line (45) is connected to the passages (34) of the cooling plates (33) for introducing the raw-material­gas-for-the-reformation (the stack-cooling-gas) into the passages (33). A line (50) for gas-for-processing is connected to the reforming section (38) of the external reformer (37) for feeding raw-material -gas-for-­processing to the reforming section (38). An anode gas feed line (52) is provided for feeding to the anode (3) the reformed gas which has been reformed through the passages (34) of the cooling plates (33) and the reformed gas which has been reformed by the reforming section (38) of the external reformer (37). An anode exit gas line (53) is provided for feeding the anode exit gas to the combustion section (39) of the external reformer (37). A cathode gas feed line (55) is provided for feeding the combustion exhaust gas discharged from the combustion section (39) to the cathode (2) with air (A). A cathode exit gas line (56) is provided for discharging the cathode exit gas.
    • 发电系统使用经由分离器(31)堆叠的燃料电池(C,S)。 在燃料电池堆(S)中设有冷却板(33)。 在各冷却板33上形成用于使重整用原料气体(也兼作叠层冷却用气体)流通的通路34,在通路34中填充改性催化剂( 61)。 在燃料电池组(5)的外部设有具有燃烧部(39)和改性部(38)的外部改性器(37)。 在冷却板(33)的通路(34)上连接有用于将重整用原料气体(电池组冷却用气体)导入到通路(34)内的电池组冷却气体管线(45) 33)。 加工用气体管线(50)与外部改性器(37)的改性部(38)连接,向改性部(38)供给原料气体。 设置阳极气体供给管线(52),用于将通过冷却板(33)的通路(34)重整的重整气体和通过重整部分重整的重整气体供给到阳极(3) (37)的外部重整器(38)。 提供阳极出口气体管线(53),用于将阳极出口气体供给外部重整器(37)的燃烧部分(39)。 设置阴极气体供给管线(55),用于将从燃烧部分(39)排出的燃烧废气与空气(A)一起供给到阴极(2)。 提供阴极排出气体管线(56)用于排出阴极排出气体。
    • 8. 发明公开
    • Plate reformer
    • Platten重整
    • EP0691701A1
    • 1996-01-10
    • EP95110504.8
    • 1995-07-05
    • Ishikawajima-Harima Heavy Industries Co., Ltd.
    • Hamada, KoukiMizusawa, MinoruKoga, Minoru
    • H01M8/06B01J8/02
    • H01M8/0631B01J8/0207B01J19/249B01J2208/022B01J2219/2453B01J2219/2462B01J2219/247B01J2219/2481B01J2219/2497C01B3/384H01M8/0625H01M2008/147H01M2300/0051Y02E60/526
    • In the plate reformer, a reforming chamber (2) is sandwiched by combustion chambers (4) so that heat transfer plates (5) also be sandwiched between the reforming chamber and the combustion chambers, and these three plate-shaped components are again sandwiched with fuel introducing chambers (7) with a number of dispersion holes (6a), forming a unit a plurality of which is then vertically stacked up to form the reformer. The plate reformer includes:
      entrance and exit of the reforming chamber (2) and entrance and exit of the combustion chamber (4), wherein the gas flows in the reforming chamber and in the combustion chamber are opposite to each other; and
      a gas permeable partition wall for partitioning each of the reforming and the combustion chambers into entrance-side section and exit-side section according to the gas flow, as well as for passing gases through during reaction;
      wherein the reforming chamber (2) includes:
      a reforming reaction section (2a) which is the entrance-side section of the reforming chamber partitioned by the partition wall (8) filled with reforming catalyst (1); and
      a heat exchange section (2b) which is the exit-side section of the partitioned reformer and filled with heat transfer component (10);
      while the combustion chamber (4) includes:
      a combustion reaction section (4a) which is the entrance-side section of the combustion chamber partitioned by the partition wall (9) and filled with combustion catalyst (3); and a heat exchange section (4b) which is the exit-side of the partitioned combustion chamber and filled with heat transfer component (10).
      The invention allows the peak locations of temperature distribution profiles of reformed and combusted gases to coincide, achieving an adequate temperature of the reformed gas at the exit.
    • 在板式重整器中,重整室(2)被燃烧室(4)夹持,使得传热板(5)也夹在重整室和燃烧室之间,并且这三个板状部件再次夹在 具有多个分散孔(6a)的燃料引入室(7),形成多个单元,然后将其垂直堆叠形成重整器。 板式重整器包括:重整室(2)的入口和出口以及燃烧室(4)的入口和出口,其中在重整室和燃烧室中流动的气体彼此相对; 以及气体分离壁,用于根据气体流将每个重整燃烧室和燃烧室分隔成入口侧部分和出口侧部分,以及在反应期间使气体通过; 其特征在于,所述重整室包括:重整反应部(2a),其由被填充有重整催化剂(1)的分隔壁(8)分隔的重整室的入口侧部分; 和作为分隔重整器的出口侧部分并填充有传热部件(10)的热交换部分(2b)。 而燃烧室(4)包括:燃烧反应部分(4a),其是由分隔壁(9)分隔并填充有燃烧催化剂(3)的燃烧室的入口侧部分; 和作为分隔燃烧室的出口侧并填充有传热部件(10)的热交换部(4b)。 本发明允许重整和燃烧的气体的温度分布曲线的峰值位置重合,实现出口处重整气体的适当温度。
    • 10. 发明公开
    • Power generation system using molten carbonate fuel cell
    • 使用碳酸氢盐燃料电池的发电系统
    • EP0429958A3
    • 1991-07-24
    • EP90121804.0
    • 1990-11-14
    • Ishikawajima-Harima Heavy Industries Co., Ltd.
    • Koga, MinoruWatanabe, TakenoriKamata, ToshioMorishima, SatoshiMizusawa, MinoruKobayashi, Kazunori
    • H01M8/06
    • H01M8/0612H01M8/0625H01M8/145Y02E60/526
    • A power generation system uses fuel cells (C, S) stacked via separators (31). Cooling plates (33) are provided in the fuel cell stack (S). Passages (34) are formed in each cooling plate (33) for allowing raw-­material-gas-for-reformation (which also serves as stack-cooling-gas) to flow therethrough and the passages (34) are filled with reforming catalyst (61). An external reformer (37) which includes a combustion section (39) and a reforming section (38) is provided outside of the fuel cell stack (5). A stack-cooling-­gas-line (45) is connected to the passages (34) of the cooling plates (33) for introducing the raw-material­gas-for-the-reformation (the stack-cooling-gas) into the passages (33). A line (50) for gas-for-processing is connected to the reforming section (38) of the external reformer (37) for feeding raw-material -gas-for-­processing to the reforming section (38). An anode gas feed line (52) is provided for feeding to the anode (3) the reformed gas which has been reformed through the passages (34) of the cooling plates (33) and the reformed gas which has been reformed by the reforming section (38) of the external reformer (37). An anode exit gas line (53) is provided for feeding the anode exit gas to the combustion section (39) of the external reformer (37). A cathode gas feed line (55) is provided for feeding the combustion exhaust gas discharged from the combustion section (39) to the cathode (2) with air (A). A cathode exit gas line (56) is provided for discharging the cathode exit gas.