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    • 66. 发明专利
    • COOLING TYPE FUEL REFORMING DEVICE
    • JPS6393343A
    • 1988-04-23
    • JP23796386
    • 1986-10-08
    • HITACHI LTD
    • SUGITA NARIHISAKOYAMA KAZUHITOSEIKI NOBUHIROSAKAGUCHI HARUICHIROHANZAWA AKIO
    • B01J8/06C01B3/38H01M8/06
    • PURPOSE:To prevent the dissipation of heat to the open air and to reduce the thickness of a heat insulating layer, by providing a combustion gas flow passage and an air flow passage between the flow passage of combustion gas generated and the open air and providing a flow passage between the air flow passage and a combustion apparatus. CONSTITUTION:Raw fuel to be reformed such as methane and steam are mixed to be supplied from a supply pipe 4 and introduced into a reaction tube. The raw fuel passes through the reforming catalyst 3 provided in the inner cylinder 1 and outer cylinder 2 of the reaction tube and, at the same time, receives heat from the combustion gas flowing outside the outer cylinder of the reaction tube to generate reforming reaction being endothermic reaction. The raw fuel passing through the reforming catalyst 3 flows through the inner cylinder 1 of the reaction tube to be discharged out of the reforming device from a discharge pipe 5. Air flows through a flow passage 15 and, at the same time, cools a flow passage guide 11 to rise in its temp. The air leaving the flow passage 15 flows through the space between the flow passage guide 11 and the container 10 in the reforming device to also cool said container 10.
    • 68. 发明专利
    • METHOD FOR CLEANING FUEL-REFORMING DEVICE
    • JPS61253772A
    • 1986-11-11
    • JP9369485
    • 1985-05-02
    • HITACHI LTD
    • KOYAMA KAZUHITOSUGITA NARIHISASAKAGUCHI HARUICHIROSHIINA KOJINOGUCHI YOSHIKI
    • H01M8/04B01J8/00B01J8/02C10L3/10H01M8/06
    • PURPOSE:To constitute a highly reliable fuel cell generation system by making a reformed gas supplied to the anode of the fuel cell free from minute catalyst particles contained in the fuel-reforming device. CONSTITUTION:The temperature of the fuel and steam is increased by feeding a high temperature fluid through a heating medium pipe 13 which passes through a heat exchanger 14 and by feeding the fuel and steam respectively through a fuel pipe 12 and a steam pipe 13 introduced into the heat exchanger 14. In the heat exchanger 14, the temperature of the fuel and steam is increased while they are mixed together. During this process, the flow rate of steam is higher than (for example 1.5-2 times) that during the rated operation of the fuel- reforming device. When the temperature of the catalyst in the reaction tube 4 is increased by the heat supplied to the reaction tube 4, the reaction gas composed of the fuel and steam flowing through the reaction tube 4 is reformed to produce a reformed gas. The reformed gas is separated into a gas 27 and a liquid 28 in a steam separator 26 and the gas 27 is discharged through an exhaust tube 29. Cleaning of the fuel-reforming device is completed when it is determined by macroscopic observation that the amount of minute catalyst particles in the liquid 28 is below the maximum allowable level.