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    • 4. 发明授权
    • Fuel cell stack cooling system
    • 燃料电池堆冷却系统
    • US4824740A
    • 1989-04-25
    • US198604
    • 1988-05-09
    • Martin L. AbramsDaniel L. D'AquilaGlenn W. Scheffler
    • Martin L. AbramsDaniel L. D'AquilaGlenn W. Scheffler
    • H01M8/04H01M2/00
    • H01M8/04029H01M8/04119
    • Fuel Cell stack coolant water is processed by moving the two-phase water/steam coolant exhaust through a steam separator wherein the water phase is separated from the steam phase. The water phase is then moved through a heat exchanger where its temperature is lowered to a subcooled level which is below the coolant operating temperature in the stack. A flow control valve is associated with the coolant heat exchanger to regulate water flow through and/or around the heat exchanger depending on the temperature of the water which leaves the steam separator. By subcooling the coolant before it reenters the stack, a lessening of electrolyte loss through evaporation is achieved. By eliminating steam condensation as a form of system heat rejection, system engineering is simplified and construction costs are lowered.
    • 燃料电池堆冷却水通过将两相水/蒸汽冷却剂排气通过蒸汽分离器移动来处理,其中水相与蒸汽相分离。 然后将水相移动通过热交换器,其中其温度降低到低于堆中的冷却剂操作温度的过冷水平。 流量控制阀与冷却剂热交换器相关联,以根据离开蒸汽分离器的水的温度调节通过热交换器和/或周围的水流。 通过在冷却剂重新进入堆叠之前过冷却,实现通过蒸发减少电解质损失。 通过消除蒸汽冷凝作为系统排热的一种形式,简化了系统工程,降低了施工成本。
    • 6. 发明授权
    • Water management system for solid polymer electrolyte fuel cell power
plants
    • 固体聚合物电解质燃料电池发电厂水管理系统
    • US5503944A
    • 1996-04-02
    • US497674
    • 1995-06-30
    • Alfred P. MeyerGlenn W. SchefflerPaul R. Margiott
    • Alfred P. MeyerGlenn W. SchefflerPaul R. Margiott
    • H01M8/10H01M8/04H01M8/06
    • H01M8/04119H01M8/04029H01M2300/0082H01M8/04291
    • A simplified solid polymer electrolyte fuel cell power plant utilizes porous conductive separator plates having central passages which are filled with circulating coolant water. The coolant water passes through a heat exchanger which rejects heat generated in the power plant. Water appearing on the cathode side of each cell membrane is pumped into the water circulation passages through the porous oxidant reactant flow field plates by a positive .DELTA.P created between the cathode reactant flow field of each cell and the coolant water circulation passages between each cell. In order to create the desired .DELTA.P, at least one of the reactant gas streams will be referenced to the coolant water loop so as to create a coolant loop pressure which is less than the referenced reactant gas stream pressure. Excess water is removed from the coolant water stream. The system can operate at ambient or at elevated pressures. Each cell in the power plant is individually cooled on demand, and the power plant does not require a separate cooling section or reactant stream humidifying devices.
    • 简化的固体聚合物电解质燃料电池发电厂利用具有填充有循环冷却水的中心通道的多孔导电隔板。 冷却水通过热交换器,排除发电厂产生的热量。 出现在每个电池膜的阴极侧的水通过多孔氧化剂反应物流场板通过在每个电池的阴极反应物流场和每个电池之间的冷却水循环通道之间产生的正的DELTA P泵送到水循环通道中。 为了产生所需的DELTA P,反应物气流中的至少一个将以冷却水回路为参考,以产生小于参考反应物气流压力的冷却剂回路压力。 从冷却水流中除去过量的水。 该系统可以在环境温度或高压下工作。 电厂中的每个电池都需要单独冷却,发电厂不需要单独的冷却段或反应物流加湿装置。
    • 9. 发明授权
    • Passive water management fuel cell
    • 被动水管理燃料电池
    • US06794077B2
    • 2004-09-21
    • US10036181
    • 2001-12-28
    • Jung S. YiDeliang YangRichard D. BreaultAlbert P. GrassoGlenn W. Scheffler
    • Jung S. YiDeliang YangRichard D. BreaultAlbert P. GrassoGlenn W. Scheffler
    • H01M202
    • H01M8/04291H01M8/0247H01M8/0267H01M8/04104H01M8/04134H01M8/241H01M8/2457H01M8/2484
    • A proton exchange membrane (PEM) fuel cell includes fuel and oxidant flow field plates (26, 40) having fuel and oxidant channels (27, 28; 41, 44), and water channels, the ends (29, 48) of which that are adjacent to the corresponding reactant gas inlet manifold (34, 42) are dead ended, the other ends (31, 50) draining excess water into the corresponding reactant gas exhaust manifold (36, 45). Flow restrictors (39, 47) maintain reactant gas pressure above exit manifold pressure, and may comprise interdigitated channels (65, 66; 76, 78). Solid reactant gas flow field plates have small holes (85, 88) between reactant gas channels (27, 28; 41) and water drain channels (29, 30; 49, 50). In one embodiment, the fuel cells of a stack may be separated by either coolant plates (51) or solid plates (55) or both. In a second embodiment, coolant plates (51a) have weep holes (57) that inject water into the ends (29) of the reactant gas water channels which are in the region of the inlet manifold (34), thereby assuring humidification of the reactants.
    • 质子交换膜(PEM)燃料电池包括具有燃料和氧化剂通道(27,28,41,44)和水通道的燃料和氧化剂流场板(26,40),其中所述端部(29,48) 邻近相应的反应气体入口歧管(34,42)是死端的,另一端(31,50)将多余的水排放到相应的反应气体排气歧管(36,45)中。 流量限制器(39,47)将反应气体压力保持在出口歧管压力以上,并且可以包括交错的通道(65,66; 76,78)。 固体反应物气体流场板在反应气体通道(27,28; 41)和排水通道(29,30; 49,50)之间具有小孔(85,88)。 在一个实施例中,堆叠的燃料电池可以由冷却板(51)或固体板(55)或两者分开。 在第二实施例中,冷却剂板(51a)具有将水注入位于入口歧管(34)的区域中的反应物气体水通道的端部(29)的排水孔(57),从而确保反应物的加湿 。
    • 10. 发明授权
    • Predictive control arrangement for load-following fuel cell-powered applications
    • 负载跟随燃料电池供电应用的预测控制装置
    • US06393354B1
    • 2002-05-21
    • US09736098
    • 2000-12-13
    • Glenn W. SchefflerPaul R. MargiottZakiul Kabir
    • Glenn W. SchefflerPaul R. MargiottZakiul Kabir
    • G06G770
    • H01M16/003B60L11/1881B60L11/1892B60L11/1894H01M8/04223H01M8/043H01M8/04559H01M8/04589H01M8/04753H01M8/04768H01M8/04992H01M8/24Y02T90/34Y10T477/45
    • A method and system are provided for controlling a fuel cell power plant (10). A demand signal (Mld) representing the anticipated current/power required by the electrical load(s) is provided. A current signal (Iap) representative of the actual current drawn by the load(s) (20) is provided. The greater of the demand signal (Mld) and the current signal (Iap) is selected (46) and utilized to provide a control signal (Mx, Mx′, Mx″) for regulating one or more of the reactants and coolant (24). One or more status signals (Xp, Xp′, Xp″, Vap) indicative of the status of a regulated one of more of the reactant/coolant and/or a respective operating process effected, is provided. Each status signal is transformed to a respective load capability signal (61, 61′, 61″). The lesser of the demand signal (Mld) and each of the load capability signals (61, 61′, 61 ″) is selected (62) to provide an output signal (Mi) for commensurately controlling a system load (20, 32).
    • 提供了一种用于控制燃料电池发电厂(10)的方法和系统。 提供表示电负载所需的预期电流/功率的需求信号(Mld)。 提供代表由负载(20)提取的实际电流的电流信号(Iap)。 选择需求信号(Mld)和电流信号(Iap)中的较大者(46)并用于提供用于调节一个或多个反应物和冷却剂(24)的控制信号(Mx,Mx',Mx“) )。 提供了指示反应物/冷却剂中的更多的一种或多种反应物/冷却剂的状态的一个或多个状态信号(Xp,Xp',Xp“,Vap)。 每个状态信号被变换为相应的负载能力信号(61,61',61“)。 选择要求信号(Mld)中的较小者和每个负载能力信号(61,61',61“)(62)以提供用于相应地控制系统负载(20,32)的输出信号(Mi) 。