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    • 91. 发明专利
    • Removal of oxygen from coke oven gas
    • 从焦炭烤箱中去除氧气
    • JPS5763388A
    • 1982-04-16
    • JP13860580
    • 1980-10-02
    • Osaka Gas Co Ltd
    • YAMAUCHI SHIGEAKIMORIMOTO MASAHIKOOKADA OSAMU
    • C10K3/02
    • PURPOSE: To prevent the sintering of the catalyst metal and the deposition of a large quantity of carbon, and to elongate the catalytic life remarkably, by contacting oxygen-containing coke oven gas with a catalyst in the presence of steam, thereby removing the oxygen.
      CONSTITUTION: Coke oven gas containing pref. ≤30vol% of oxygen is mixed with steam. The molar ratio of H
      2 O/O
      2 in the mixture is usually 0.1W100. The mixture is catalytically reacted with a deoxygenation catalyst (e.g. Ni-Mo, Co-Mo, Ni-S, etc.) pref. under normal pressure W50kg/cm
      2 at 100W500°C to effect the oxygen removal.
      EFFECT: The temperature increase of the catalyst layer is also suppressed.
      COPYRIGHT: (C)1982,JPO&Japio
    • 目的:为了防止催化剂金属的烧结和沉积大量的碳,并显着延长催化寿命,通过在蒸汽存在下使含氧焦炉气与催化剂接触,从而除去氧气。 构成:焦炉煤气含有 <= 30vol%的氧气与蒸汽混合。 混合物中H 2 O / O 2的摩尔比通常为0.1-100。 混合物与脱氧催化剂(例如Ni-Mo,Co-Mo,Ni-S等)催化反应。 在100-500摄氏度的常压-50kg / cm 2下进行除氧。 效果:也抑制催化剂层的升温。
    • 93. 发明专利
    • Operation method of fuel cell
    • 燃料电池操作方法
    • JP2008300368A
    • 2008-12-11
    • JP2008234912
    • 2008-09-12
    • Osaka Gas Co Ltd大阪瓦斯株式会社
    • SUZUKI MINORUECHIGO MITSUAKIYAMAZAKI OSAMUOKADA OSAMU
    • H01M8/04H01M8/10H01M8/24
    • Y02E60/521
    • PROBLEM TO BE SOLVED: To provide an operation method of a fuel cell capable of recovering deterioration due to a deterioration causing gas in order to reduce the cost and size of the fuel cell by obviating the need of installation of a gas processing device.
      SOLUTION: In this operation method of a fuel cell wherein a plurality of cells C each having an oxygen electrode 2 on one surface of an electrolyte layer 1 and a fuel electrode 3 on the other surface thereof are arranged in a state electrically connected in series to one another, and power is generated by supplying an oxygen-containing gas to the oxygen electrodes 2, and supplying a hydrogen-containing gas to the fuel electrodes 3, a deterioration recovery process of recovering the deterioration of the oxygen electrodes 2 by stopping supply of the oxygen-containing gas to the oxygen electrodes 2 and making hydrogen exist in the oxygen electrodes 2 is executed by hydrogen permeating from the fuel electrode 3 side to the oxygen electrode 2 side by forming a state where current is not carried to the cells C, supplying the hydrogen-containing gas to the fuel electrodes 3, and stopping the supply of the oxygen-containing gas to the oxygen electrodes 2.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 解决方案:提供一种燃料电池的操作方法,该燃料电池能够回收由于导致气体的劣化引起的劣化,以便通过避免安装气体处理装置的需要来降低燃料电池的成本和尺寸 。 解决方案:在这种燃料电池的操作方法中,其中在电解质层1的一个表面上具有氧电极2的多个电池单元C和其另一个表面上的燃料电极3布置成电连接的状态 彼此串联,通过向氧电极2供给含氧气体,向燃料电极3供给含氢气体而产生电力,通过以下方式回收氧电极2的劣化的劣化恢复处理 停止向氧电极2供应氧气并使氧气存在于氧气电极2中的氢是通过从不从燃料电极3侧向氧电极2侧渗透的氢进行的, 电池C,将含氢气体供应到燃料电极3,并停止向氧电极2供应含氧气体。版权所有(C)2009,JPO&INPIT
    • 94. 发明专利
    • Fuel cell system using dimethyl ether as fuel
    • 使用二甲醚燃料的燃料电池系统
    • JP2005108792A
    • 2005-04-21
    • JP2003344509
    • 2003-10-02
    • Osaka Gas Co Ltd大阪瓦斯株式会社
    • SUZUKI MINORUTAKEMOTO TETSUYAOKADA OSAMUINOUE NAOKI
    • C01B3/32C01B3/38C01B3/48H01M8/06
    • Y02E60/50
    • PROBLEM TO BE SOLVED: To provide a fuel cell system using dimethyl ether as fuel which uses fuel having dimethyl ether as a main component and in which down-sizing and high power generation efficiency can be attained compatibly. SOLUTION: The fuel cell system using dimethyl ether as fuel comprises a reforming reactor 6 for reforming the fuel having dimethyl ether as a main component, a carbon monoxide conversion reactor 10 for reducing the concentration of a carbon monoxide gas, and a solid polymer type fuel cell 14 for carrying out the power generation reaction of a fuel cell. In the reforming reactor 6, the fuel reacts with water vapor and is reformed into a reformed fuel gas with the high concentration of a hydrogen gas, and the reformed gas is introduced into the carbon monoxide conversion reactor 10 and the concentration of a carbon monoxide contained in the reformed fuel gas is reduced; and in a range from the exit of the reforming reactor 6 to the inside of the carbon monoxide conversion reactor 10, water is added into the reformed fuel gas, and by the amount of water added, the carbon monoxide conversion reaction in the carbon monoxide conversion reactor 10 is controlled. COPYRIGHT: (C)2005,JPO&NCIPI
    • 解决的问题:提供一种使用二甲醚作为燃料的燃料电池系统,该燃料电池系统采用以二甲醚为主要成分的燃料,并能兼容地获得降低尺寸和高发电效率。 解决方案:使用二甲醚作为燃料的燃料电池系统包括用于重整具有二甲醚作为主要成分的燃料的重整反应器6,用于降低一氧化碳气体浓度的一氧化碳转化反应器10和固体 聚合型燃料电池14,用于进行燃料电池的发电反应。 在重整反应器6中,燃料与水蒸汽反应并重整成具有高浓度氢气的重整燃料气体,重整气体被引入一氧化碳转化反应器10中,并且含有一氧化碳的浓度 在改造后的燃气中减少; 并且在从重整反应器6的出口到一氧化碳转化反应器10的内部的范围内,向重整燃料气体中加入水,通过加入的水量,一氧化碳转化反应中的一氧化碳转化反应 反应器10被控制。 版权所有(C)2005,JPO&NCIPI
    • 97. 发明专利
    • MANUFACTURE OF METHANOL REFORMING CATALYST
    • JP2000117107A
    • 2000-04-25
    • JP29780798
    • 1998-10-20
    • OSAKA GAS CO LTD
    • ECHIGO MITSUAKISUZUKI MINORUOKADA OSAMU
    • C01B3/40B01J23/80B01J37/03B01J37/16B01J38/02
    • PROBLEM TO BE SOLVED: To achieve a long life and high activity and raise heat resistance by a method wherein when a methanol reforming catalyst is manufactured, a copper compound, a zinc compound, and an aluminum hydroxide are used, a precipitate is generated by mixing with alkali substance, and the generated precipitate is separated and burnt. SOLUTION: When a catalyst to be used in the case of manufacturing a reformed gas having hydrogen as a main constituent by allowing methanol to react on water vapor, aluminum hydroxide is firstly added to aqueous liquid containing a copper compound and a zinc compound, this mixed liquid is dropped into alkali substance aqueous liquid kept at about 800 deg.C while stirring, and a precipitate is generated. Then, after washing the generated precipitate by water, it is filtered, dried, and burnt with in a temperature range of 300 to 650 deg.C to obtain a sinter compact. Thereby, even at a high reacting temperature and in a high methanol feed speed condition, a catalyst having high activity and a long life is obtained. Further, as occasion dempands, a burning treating material is treated by hydrogen reduction at 150 deg.C or higher and not higher than 300 deg.C.