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    • 1. 发明专利
    • WATER RECOVERY PROCESSING DEVICE FOR FUEL CELL GENERATING EQUIPMENT
    • JPH07220748A
    • 1995-08-18
    • JP1253494
    • 1994-02-04
    • ISHIKAWAJIMA HARIMA HEAVY IND
    • SAITO HAJIMEHATORI SATOSHI
    • H01M8/04H01M8/06
    • PURPOSE:To provide a water recovery processing device simple in small size at a low cost by providing a condensation separator, comprising a condensing heat exchanger, mist separator, carbon dioxide take out port, wire mesh and an air blow nozzle, in an exhaust gas flow path of a reformer. CONSTITUTION:Exhaust gas 10a generated in a combustion side of a reformer 10, when advanced into a condensation separator 33, is cooled by a condensing heat exchange part 35 in the upper part of a vessel main unit 34, to store water as the condensed water 23 in a bottom part. The rest of carbon dioxide 24, after a mist is separated in a mist separator 36 by compressed air 7 from an air blow nozzle 39, is supplied with the air 7 to a cathode electrode 5 of a fuel cell 1 through a low temperature blower 25 from a carbon dioxide take out port 37. The water 23, accumulated in the bottom part of the main unit 34, is processed by alkaline water in a water purifying device 26, thereafter guided to a boiler 27 and presented to serve as generating reforming steam. Since water condensation and steam separation are performed by the single separator 33, a device can be simply miniaturized.
    • 5. 发明专利
    • MOLTEN CARBONATE TYPE FUEL CELL GENERATING DEVICE
    • JPH03245471A
    • 1991-11-01
    • JP4119490
    • 1990-02-23
    • ISHIKAWAJIMA HARIMA HEAVY IND
    • UEMATSU KOKICHIHATORI SATOSHI
    • H01M8/14H01M8/04H01M8/06
    • PURPOSE:To enhance generating efficiency by connecting a vapor line to the inlet side of the reforming section of a reformer, and thereby mixing a part of gas from the outlet of an anode, and vapor generated owing to thermal recovery within a system with reforming gas so as to be forwarded to the reformer. CONSTITUTION:Combustion exhaust gas exhausted out of the combustion chamber 4b of a reformer 4 is led to a gas-liquid separator 15 by way of an evaporator 13 and a heat exchanger 14, gas separated by the separator 15 is mixed with air within an air supply line 16, is pressurized by a blower 17 thereafter, and is then supplied to a cathode 2 through an air preheater 18. In the second place, liquid (water) separated by the separator 15 is pressurized by a pump 19, and is then forwarded to the evaporator 13 from a liquid-pool container 20. A part of vapor when the liquid is evaporated, is supplied to the inlet side of the reforming section 4a of the reformer for reforming natural gas from the liquid-pool container 20 through a vapor line 21. A device is provided with a cathode outlet gas line 12b which discharges remaining gas for preheating air to atmosphere from a cathode outlet through the air preheater 18, a butterfly valve 22 adjusting the flow rate of gas from an anode outlet, and with a butterfly valve 23 adjusting the flow rate of gas from a cathode outlet.
    • 10. 发明专利
    • MOLTEN CARBONATE FUEL CELL POWER GENERATING UNIT
    • JPH0419965A
    • 1992-01-23
    • JP12297190
    • 1990-05-15
    • ISHIKAWAJIMA HARIMA HEAVY IND
    • HATORI SATOSHI
    • H01M8/06
    • PURPOSE:To shorten the distance of piping from a cathode blower to each of numerous reformers and each of numerous fuel cells by separating piping on the inlet and outlet sides of a cathode blower into two parts, and connecting the two parts to the reformer and fuel cell of each cell module, respectively. CONSTITUTION:Gas discharged from the combustion chamber of the reformer 4 of each of numerous cell modules A is centralized into one cathode blower 17 through piping 14a on the inlet side of the cathode blower 17 and is supplied from the cathode blower 17 to the cathode of the fuel cell I of each of the numerous cell modules A through piping 14b on the outlet side of the blower. In this case, the piping 14a and 14b connecting each reformer 4 and each fuel cell 1 to one cathode blower 17 can be relatively shortened because the cathode blower 17 is located at the center of the numerous cell modules A, and in addition, a symmetrical piping layout can be offered so gas is distributed well from each reformer 4 to each fuel cell I.