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    • 92. 发明公开
    • Power generation system using molten carbonate fuel cells
    • 系统使用的燃料电池用熔融碳酸盐产生能量。
    • EP0496011A1
    • 1992-07-29
    • EP91100702.9
    • 1991-01-21
    • Ishikawajima-Harima Heavy Industries Co., Ltd.
    • Uematsu, HiroyoshiHatori, Satoshi
    • H01M8/06
    • H01M8/0612H01M8/145Y02E60/526
    • A reformer (45) includes a reforming chamber (46) for reforming raw material and a heating chamber (47) for heating the reforming chamber. Exhaust gas from a cathode chamber (42) of a fuel cell (40) is directly introduced to the heating chamber (47) such that the exhaust gas is combusted, or the exhaust gas from the cathode chamber (42) is introduced to a catalyst comubstor (44) together with exhaust gas discharged from the anode chamber (43) such that these gases undergo combustion. Combustion exhaust gas is introduced to the heating chamber (47) and sensible heat of the cathode exhaust gas is effectively used as heat source for a reforming reaction in the reforming chamber (46).
    • 的重整器(45)包括用于重整原料和用于加热重整室的加热室(47)的重整室(46)。 从燃料电池(40)的阴极室(42)的废气被直接引入到加热腔室(47)检测并排出气体燃烧,或从阴极室排出气体(42)被引入到催化剂 comubstor(44)与从所述阳极室(43)排出的废气一起测试所做的合成气进行燃烧。 燃烧废气被引入到加热腔室(47)和热敏感的阴极废气被有效地用作用于在重整室(46)的重整反应热源。
    • 93. 发明公开
    • Electric power producing system using molten carbonate type fuel cell
    • 一种用于通过利用燃料电池和熔融碳酸盐产生电能。
    • EP0456848A1
    • 1991-11-21
    • EP90109042.3
    • 1990-05-14
    • Ishikawajima-Harima Heavy Industries Co., Ltd.
    • Kobayashi, KazunoriYoshida, Toshiaki
    • H01M8/06
    • H01M8/0612H01M2008/147H01M2300/0051Y02E60/526
    • An electric power producing system using a molten carbonate type fuel cell (25) comprises a fuel cell (25) whose anode chamber (27) is fed with hydrogen gas and whose cathode chamber (28) is fed with air (43) and carbon dioxide and a reformer (26) including a reforming chamber (29) for reforming fuel gas (31) into anode gas and a combustion chamber (30) for maintaining the reforming chamber temperature. In the reformer (26) fuel gas (31) and steam (36) are fed into the reforming chamber (29), the gases discharged from the anode chamber (27) are introduced into the combustion chamber (30) and non-reacted gases in the anode exhaust gas are burned with air (43), and heat produced by the combustion is utilized to heat the reforming chamber (29). Hydrogen-rich gas produced in the reforming chamber (29) is fed into the anode chamber (27), air (43) is introduced into the cathode chamber (28), the cathode exhaust gas is partially fed into the combustion chamber (30) whereas the remainder is discharged from the system (48), and the combustion gas from the combustion chamber (30) is separated from water and then recirculated into the cathode chamber (28). The anode exhaust gas and the cathode exhaust gas are directly introduced into the combustion chamber (30) so that the pressure in the anode and cathode chambers (27,28) is equalized.
    • 使用熔融碳酸盐型燃料电池(25)的电力产生系统包括燃料电池(25),其阳极室(27)被供给氢气和其阴极室(28)被供给空气(43)和二氧化碳 和一个重整器(26)包括用于燃料气体(31)重整到阳极气体以及用于维持重整室温度的燃烧室(30)的重整室(29)。 在重整器(26)的燃料气体(31)和蒸汽(36)被送入重整室(29)中,从阳极室(27)排出的气体引入所述燃烧室(30)和未反应的气体 阳极废气中的燃烧用空气(43),和由燃烧产生的热量被用来加热重整室(29)。 在改质室(29)中产生富含氢的气体供入阳极室(27),空气(43)被引入到阴极室(28),阴极废气被部分地供给到所述燃烧室(30) 而其余从系统(48),和燃烧气体从燃烧室排出(30)从水分离,然后再循环到阴极室(28)。 阳极废气和阴极废气被直接引入所述燃烧室(30),所以没有在阳极和阴极室(27,28)中的压力相等。
    • 95. 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.
    • 97. 发明公开
    • Electrode for use in a gas fuel cell which contains a set of electrodes
    • ElektrodefürAnwendung在einer Gas-Brennstoffzelle,enthaltend einen Satz von Elektroden。
    • EP0408103A1
    • 1991-01-16
    • EP90201721.9
    • 1990-06-28
    • Stichting Energieonderzoek Centrum Nederland(ECN)
    • Quaadvliet, Henricus Johannes Adrianus
    • H01M8/02H01M4/86
    • H01M8/0254H01M4/8631H01M8/0206H01M8/0208H01M8/0228H01M2008/147H01M2300/0051Y02E60/526
    • Electrode for use in a gas fuel cell into which a reactant gas is passed in order to generate electrical energy, the electrode being provided with a virtually flat catalyst for ionizing the gas, a current collector which is arranged in direct contact with, and in electrical contact with, a flat surface of said catalyst in order to convey the current which is produced by the ionization of the reactant gas, said current collector (8) being provided with a number of linear ribs which form alternatingly open and closed channels along the flat surface of the catalyst through which the reactant gas can be passed wherein in the sections of the supporting plate (8) are offset with respect to one another by half a pitch length in the transverse direction, and which electrode is provided with inlets and outlets (13, 14) for reactant gas and oxidizing gas.
    • 用于气体燃料电池的电极,其中通过反应气体以产生电能,该电极设置有用于电离气体的实质上平坦的催化剂,与电极直接接触并且在电气中布置的集电器 与所述催化剂的平坦表面接触以便传送由反应物气体的电离产生的电流,所述集流器(8)设置有多个线性肋,所述线形肋沿着平坦形成交替打开和闭合的通道 催化剂的表面可以通过反应气体通过,其中在支撑板(8)的部分中相对于彼此相对于横向方向偏移半个节距长度,并且哪个电极设置有入口和出口( 13,14),用于反应气体和氧化气体。
    • 99. 发明公开
    • Fuel cell
    • Brennstoffzelle。
    • EP0399077A1
    • 1990-11-28
    • EP89109427.8
    • 1989-05-24
    • Ishikawajima-Harima Heavy Industries Co., Ltd.
    • Shiozawa, ShojiShimizu, Toru
    • H01M8/24
    • F28F3/042H01M8/0273H01M8/04007H01M8/04014H01M8/04089H01M8/2415H01M8/244H01M8/2484H01M2008/147H01M2300/0051Y02E60/526
    • A conventional fuel cell comprises a plurality of cell elements stacked via separator plates (4), each cell element comprising an electrolyte plate (1), a cathode (2) and an anode (3) which sandwich the electrolyte plate (1). A power generation part of the fuel cell is defined by the electrolyte plate (1), cathode (2) and anode (3). Oxidizing gas (OG) and fuel gas (FG) are supplied to each cell element in the same direction but the direction is opposite to the gas flow of an adjacent cell element. In the improvement, preheating devices (II) are provided next to the power generation part (I) as a part of the fuel cell in the direction gases flow in a manner such that both incoming and outgoing gases pass through the preheating device (II). The preheating device (II) includes a plurality of heat exchange promoting elements (12) in the form of projections provided on both faces of the separator plate (4).
    • 传统的燃料电池包括通过隔板(4)堆叠的多个电池元件,每个电池单元包括夹着电解质板(1)的电解质板(1),阴极(2)和阳极(3)。 燃料电池的发电部分由电解质板(1),阴极(2)和阳极(3)限定。 氧化气体(OG)和燃料气体(FG)以相同的方向被提供给每个电池元件,但是该方向与相邻电池元件的气流相反。 在改进中,预热装置(II)作为燃料电池的一部分沿着气体的流动方式设置在发电部分(I)旁边,使得进入和排出的气体都通过预热装置(II) 。 预热装置(II)包括设置在隔板(4)的两个表面上的突起形式的多个热交换促进元件(12)。