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    • 3. 发明专利
    • FREE FLOW TYPE ELECTROPHORETIC APPARATUS
    • JPH028388A
    • 1990-01-11
    • JP15653488
    • 1988-06-24
    • MITSUBISHI HEAVY IND LTDNAT SPACE DEV AGENCY
    • SAKIMURA TORUMIYAMOTO HITOSHIMASUDA TSUYOSHIKOYAMA MASATOWATARIDO MITSURU
    • C25B7/00C25B9/00C25B9/08
    • PURPOSE:To balance the inflow and outflow of ions between electrode chambers and electrophoretic space and to suppress the rise of the electrical conductivity of a buffer soln. by spreading an electrode membrane obtd. by vertically joining an upper cation membrane and a lower anion membrane at the anode side of a free flow type electrophoretic apparatus and an electrode membrane obtd. by vertically joining an upper anion membrane and a lower cation membrane at the cathode side. CONSTITUTION:An electrode membrane 11 obtd. by vertically joining an upper cation permeable membrane (cation membrane) 11a and a lower anion permeable membrane (anion membrane) 11b of the same size is spread at the anode side of an electrophoretic apparatus. An electrode membrane 12 obtd. by vertically joining an upper anion membrane 12b and a lower cation membrane 12a of the same size is spread at the cathode side to form an electrophoretic chamber and electrode chambers. When voltage is impressed between both electrodes 4, 4, cations from the anode and anions from the cathode enter the electrophoretic chamber through the membranes 11, 12 in the upper part. In the lower part, anions enter the electrode chamber adjacent to the anode and cations enter the electrode chamber adjacent to the cathode because ion exchange membranes having opposite polarities are present and the concn. of ions in the electrophoretic chamber is kept nearly constant, so any electric current affects the concn. of ions in the electrophoretic chamber.
    • 4. 发明专利
    • Fuel cell system
    • 燃油电池系统
    • JP2006139984A
    • 2006-06-01
    • JP2004327485
    • 2004-11-11
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • MIYAMOTO HITOSHIKANEHIRA SHINGOTAKENOBU KOICHINISHIURA MASANORIKISHIZAWA HIROSHIWATABE MASAHARU
    • H01M8/06H01M8/04H01M8/12
    • Y02E60/525
    • PROBLEM TO BE SOLVED: To provide a fuel cell system that enhances efficiency, by removing moisture in exhausted fuel gas and carbon dioxide, and is capable of size reduction of the system, and setting moisture concentration suitable for enhancing efficiency.
      SOLUTION: In order to remove moisture and carbon dioxide at the same time, a gas controller 16 for example is installed in the fuel cell system. The gas controller 16 removes carbon dioxide from the exhausted fuel gas by the gas liquid contact of splay liquid sprayed from a spray header 25 and the exhausted fuel gas, and condenses and removes water vapor in the exhausted fuel gas, by cooling the exhausted fuel gas with a cooling pipe 26. An aqueous solution of calcium hydroxide or an aqueous solution of magnesium hydroxide is used as alkaline water. The gas controller 16 controls the moisture concentration in the exhausted fuel gas to be in the range of 25-40% and the carbon dioxide concentration to be in the range of 0-15%.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 解决的问题:提供一种通过去除排出的燃料气体和二氧化碳中的水分而提高效率的燃料电池系统,并且能够减小系统的尺寸,并且设定适合于提高效率的水分浓度。 解决方案:为了同时去除水分和二氧化碳,例如,燃料电池系统中安装有气体控制器16。 气体控制器16通过从喷射头25喷射的喷射液体与排出的燃料气体的气液接触而从排出的燃料气体中除去二氧化碳,并且通过冷却排出的燃料气体来冷凝和去除排出的燃料气体中的水蒸气 使用冷却管26.氢氧化钙水溶液或氢氧化镁水溶液用作碱性水。 气体控制器16将排出的燃料气体中的水分浓度控制在25-40%的范围内,并且二氧化碳浓度在0-15%的范围内。 版权所有(C)2006,JPO&NCIPI
    • 5. 发明专利
    • Solid oxide fuel cell
    • JP2004146193A
    • 2004-05-20
    • JP2002309738
    • 2002-10-24
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • BABA KINJIMIYAMOTO HITOSHIWATABE MASAHARUOTANI YUICHIONO KIMIOKI
    • H01M8/02H01M8/12
    • Y02E60/525
    • PROBLEM TO BE SOLVED: To prevent breakage of a power generating membrane by thermal stress caused by uneven temperature distribution on the inside of a solid oxide fuel cell. SOLUTION: This solid oxide fuel cell has the power generating membrane 11 and an interconnector 15, a recessed and projecting part is formed on the both sides of the power generating membrane, and the power generating membrane has a fuel electrode on one side and an oxygen electrode on the other side. The power generating membrane is interposed between the interconnectors, and the interconnector is joined with the power generating membrane in projecting parts of the recessed and projecting part. The interconnector has strength higher than that of the interconnector, coefficient of linear thermal expansion of the power generating membrane is made different from that of the interconnector, and in a part where tensile stress is applied, the coefficient of linear thermal expansion of the interconnector is made lower than that of the power generating membrane, and in a part where compression stress is applied, the coefficient of linear thermal expansion of the interconnector is made higher than that of the power generating membrane. COPYRIGHT: (C)2004,JPO
    • 6. 发明专利
    • Solid oxide fuel cell power generation system
    • 固体氧化物燃料电池发电系统
    • JP2004103282A
    • 2004-04-02
    • JP2002259936
    • 2002-09-05
    • Mitsubishi Heavy Ind Ltd三菱重工業株式会社
    • OTANI YUICHIWATABE MASAHARUMIYAMOTO HITOSHIKISHIZAWA HIROSHI
    • H01M8/12H01M8/04
    • Y02E60/525
    • PROBLEM TO BE SOLVED: To provide a solid oxide fuel cell power generation system, capable of enhancing system efficiency and reliability of various equipment.
      SOLUTION: This solid oxide fuel cell power generation system comprises a recirculation fan 17, by which the part of waste fuel exhausted by power-generating operations of a SOFC 10 is recirculated in the SOFC 10 as recirculation fuel, and a regenerative heat exchanger 15 for exchanging heat so as to decrease the temperature of the recirculation fuel, before passing the recirculation fan 17 and to raise the temperature of the recirculation fuel, after passing the recirculation fan 17. The regenerative heat exchanger 15 is composed of a high-temperature regenerative heat exchanger 15A for exchanging heat at a high-temperature region, and a low-temperature regenerative heat exchanger 15B for exchanging heat at a low-temperature region. In addition, the system comprises a condenser 16 for reducing the temperature of the recirculation fuel, before passing the recirculation fan 17 and removing the extra water.
      COPYRIGHT: (C)2004,JPO
    • 要解决的问题:提供一种能够提高各种设备的系统效率和可靠性的固体氧化物燃料电池发电系统。 解决方案:该固体氧化物燃料电池发电系统包括再循环风扇17,通过SOFC 10的发电操作排出的废燃料的一部分在SOFC 10中作为再循环燃料再循环,再生热 交换器15,用于在通过再循环风扇17之后交换热量以降低再循环燃料的温度,并在通过再循环风扇17之后提高再循环燃料的温度。再生热交换器15由高压 在高温区域进行热交换的高温蓄热式热交换器15A和在低温区域进行热交换的低温蓄热式热交换器15B。 此外,该系统包括用于在通过再循环风扇17并除去额外的水之前降低再循环燃料的温度的冷凝器16。 版权所有(C)2004,JPO
    • 9. 发明专利
    • FILLING MATERIAL FOR HIGH TEMPERATURE AND PRODUCTION THEREOF
    • JPH10316430A
    • 1998-12-02
    • JP12717197
    • 1997-05-16
    • MITSUBISHI HEAVY IND LTD
    • MORI KAZUTAKAMIYAMOTO HITOSHIMATSUDAIRA TSUNEAKITAKENOBU KOICHI
    • C01G25/00H01M8/02
    • PROBLEM TO BE SOLVED: To obtain a filler for a high temperature, having a low gas permeability by mixing a large-sized zirconia powder, a medium-sized zirconia powder each having a specified particle size and a zircon powder composed of fine particles having a specified particle diameter. SOLUTION: This filling material for a high temperature is obtained by preparing a large-sized zirconia powder having 10-40 μm particle diameter and a medium-sized zirconia powder having 1-10 μm particle diameter by crushing and classifying a raw powder of 3 mol.% yttria-stabilized zirconia, etc., having 10-80 μm particle diameter, 50 μm mean particle diameter and 10.9×10 deg.C expansion coefficient, using fine particles of zircon having 0.1-1.0 μm particle diameter, 0.3 μm mean particle diameter, 10 m /g specific surface area and 7.9×10 deg.C expansion coefficient, forming a slurry of the fine particle zircon powder, a dispersing medium such as water and a dispersing agent such as a polycarboxylic acid ammonium, etc., by a dispersing treatment with a ball mill, etc., then adding the zirconia powder consisting of approximately 80 wt.% medium-sized particles and approximately 20 wt.% large-sized particles in a weight ratio of the zirconia powder/the zircon powder = (75/25)-(85/15) for dispersing.