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    • 51. 发明授权
    • Full cells evaporative cooling and combined evaporative and sensible cooling
    • 全细胞蒸发冷却和组合蒸发和明智的冷却
    • US08182954B2
    • 2012-05-22
    • US12284904
    • 2008-09-26
    • Robert M. DarlingMichael L. Perry
    • Robert M. DarlingMichael L. Perry
    • H01M8/04
    • H01M8/04029H01M8/0258H01M8/0267H01M8/04089H01M8/241H01M8/2457H01M8/2484
    • Water passageways (67; 78, 85; 78a, 85a) that provide water through reactant gas flow field plates (74, 81) to cool the fuel cells (38) may be grooves (76, 77; 83, 84) or may comprise a plane of porous hydrophilic material (78a, 85a), may be vented to atmosphere (99) by a porous plug (69), or pumped (89, 146) with or without removing any water from the passageways. A condenser (59, 124) receives exhaust of reactant air that evaporatively cools the stack (37), and may have a contiguous reservoir (64, 128), be vertical (a vehicle radiator, FIG. 2), be horizontal across the top of the stack (37, FIG. 5), or below (124) the stack (120). Condenser air flow may be controlled by shutters (155), or by a controlled, freeze-proof heat exchanger (59a). A deionizer (175) may be used. Sensible heat transferred into the water is removed by a heat exchanger 182; a controller (185) controls water flow (180) and temperature as well as air flow to provide predetermined allocation of cooling between evaporative and sensible.
    • 通过用于冷却燃料电池(38)的反应气体流场板(74,81)提供水的水通道(67; 78,85; 78a,85a)可以是凹槽(76,77; 83,84),或者可以包括 多孔亲水材料(78a,85a)的平面可以通过多孔塞(69)排放到大气中(99),或者在有或没有从通道中去除任何水的情况下泵送(89,146)。 冷凝器(59,124)接收蒸发冷却堆(37)的反应物空气的排气,并且可以具有连续的储存器(64,128),垂直(图2的车辆散热器)横跨顶部 (37,图5)或下方(124)堆叠(120)。 冷凝器空气流可以由百叶窗(155)或受控的防冻热交换器(59a)控制。 可以使用去离子器(175)。 通过热交换器182除去传递到水中的明显的热量; 控制器(185)控制水流(180)和温度以及气流,从而在蒸发和显热之间提供预定的冷却分配。
    • 55. 发明申请
    • Oxygen-Consuming Zero-Gap Electrolysis Cells With Porous/Solid Plates
    • 使用多孔/固体板的氧消耗零缝隙电解电池
    • US20100314261A1
    • 2010-12-16
    • US12086374
    • 2005-12-14
    • Michael L. Perry
    • Michael L. Perry
    • C25B1/26C25B9/10
    • C25B1/26C25B9/206C25B15/08
    • An electrolysis stack (53) with oxygen-depolarized cathodes (31) employs solid-plate anodes (38) and porous-plate cathodes (42). The stack (53) of electrolysis cells (29) (e.g, hydrogen-chloride or chlor-allkali cells) each include an ion exchange membrane (32) sandwiched between an anode conductor (34) and a permeable cathode (35); an oxygen-consuming gas diffusion cathode (31) is adjacent the cathode conductor of each cell. Between the anode conductor of one cell and the gas diffusion cathode of an adjacent cell there is a composite bipolar plate (51) including a solid plate (38) having channels (39) for conducing salt solution and product of the process; the bipolar plates also include a porous plate (42) having channels (43) for conducting oxidant adjacent the gas diffusion cathode and channels (49) connected to a source of liquid (such as water or dilute sodium hydroxide).
    • 具有氧去极化阴极(31)的电解堆叠(53)采用固体阳极(38)和多孔板阴极(42)。 电解槽(29)的堆叠(53)(例如氯化氢或氯全质电池)各自包括夹在阳极导体(34)和可渗透阴极(35)之间的离子交换膜(32)。 耗氧气体扩散阴极(31)与每个电池的阴极导体相邻。 在一个电池的阳极导体和相邻电池的气体扩散阴极之间存在一个复合双极板(51),它包括固体板(38),该固体板具有用于引导盐溶液的通道(39)和该工艺的产物; 双极板还包括多孔板(42),其具有用于在气体扩散阴极附近传导氧化剂的通道(43)和连接到液体源(例如水或稀释氢氧化钠)的通道(49)。
    • 56. 发明申请
    • RAPID START-UP AND OPERATING SYSTEM FOR A FUEL CELL POWER PLANT UTILIZING A REFORMATE
    • 用于燃料电池的快速启动和操作系统利用改造
    • US20100304239A1
    • 2010-12-02
    • US12734862
    • 2007-12-20
    • Michael L. Perry
    • Michael L. Perry
    • H01M8/06H01M8/04
    • H01M8/04097H01M8/04201H01M8/04223H01M8/04225H01M8/04302
    • A fuel cell power plant (10) includes a power supply (58) that directs a direct current to catalysts (24), (26) of a fuel cell (22) after terminating flow of electricity to a primary load (52), and after flow of an oxidant adjacent the cathode catalyst (26) is terminated, and while a reformate fuel is directed adjacent the anode catalyst (24). Pure hydrogen fuel generated thereby at the cathode catalyst (26) is directed into a hydrogen storage tank (62). Upon start-up of the power plant (10), the stored hydrogen gas is directed from the tank (62) to flow adjacent the anode catalyst (24) while a reformer (12) is being warmed up for operation, to provide virtually instantaneous start-up of the plant (10). Optionally, the stored hydrogen may be used occasionally during operation with the reformate fuel to meet an increased demand for electricity.
    • 燃料电池发电厂(10)包括在终止电流到主负载(52)之后将直流引导到燃料电池(22)的催化剂(24),(26)的电源(58),以及 在邻近阴极催化剂(26)的氧化剂流动终止之后,并且当重整燃料被引导邻近阳极催化剂(24)时。 由此在阴极催化剂(26)产生的纯氢燃料被引导到储氢罐(62)中。 在发电厂(10)启动时,储存的氢气从储罐(62)引导到邻近阳极催化剂(24)流动,同时重整器(12)正在加热操作,以实质上提供 工厂的启动(10)。 任选地,储存的氢气可以在与重整燃料的操作期间偶尔使用以满足对电力的增加的需求。
    • 58. 发明申请
    • Full cells evaporative cooling and combined evaporative and sensible cooling
    • 全细胞蒸发冷却和组合蒸发和明智的冷却
    • US20090035616A1
    • 2009-02-05
    • US12284904
    • 2008-09-26
    • Robert M. DarlingMichael L. Perry
    • Robert M. DarlingMichael L. Perry
    • H01M8/04
    • H01M8/04029H01M8/0258H01M8/0267H01M8/04089H01M8/241H01M8/2457H01M8/2484
    • Water passageways (67; 78, 85; 78a, 85a) that provide water through reactant gas flow field plates (74, 81) to cool the fuel cells (38) may be grooves (76, 77; 83, 84) or may comprise a plane of porous hydrophilic material (78a, 85a), may be vented to atmosphere (99) by a porous plug (69), or pumped (89, 146) with or without removing any water from the passageways. A condenser (59, 124) receives exhaust of reactant air that evaporatively cools the stack (37), and may have a contiguous reservoir (64, 128), be vertical (a vehicle radiator, FIG. 2), be horizontal across the top of the stack (37, FIG. 5), or below (124) the stack (120). Condenser air flow may be controlled by shutters (155), or by a controlled, freeze-proof heat exchanger (59a). A deionizer (175) may be used. Sensible heat transferred into the water is removed by a heat exchanger 182; a controller (185) controls water flow (180) and temperature as well as air flow to provide predetermined allocation of cooling between evaporative and sensible.
    • 通过用于冷却燃料电池(38)的反应气体流场板(74,81)提供水的水通道(67; 78,85; 78a,85a)可以是凹槽(76,77; 83,84),或者可以包括 多孔亲水材料(78a,85a)的平面可以通过多孔塞(69)排放到大气中(99),或者在有或没有从通道中去除任何水的情况下泵送(89,146)。 冷凝器(59,124)接收蒸发冷却堆(37)的反应物空气的排气,并且可以具有连续的储存器(64,128),垂直(图2的车辆散热器)横跨顶部 (37,图5)或下方(124)堆叠(120)。 冷凝器空气流可以由百叶窗(155)或受控的防冻热交换器(59a)控制。 可以使用去离子器(175)。 通过热交换器182除去传递到水中的明显的热量; 控制器(185)控制水流(180)和温度以及气流,从而在蒸发和显热之间提供预定的冷却分配。
    • 59. 发明申请
    • Circulation of Gas-Entrained Fuel Cell Coolant
    • 气体驱动燃料电池冷却液循环
    • US20090011288A1
    • 2009-01-08
    • US12087088
    • 2005-12-29
    • Michael L. PerryRobert M. Darling
    • Michael L. PerryRobert M. Darling
    • H01M8/04H01M8/00
    • H01M8/04014H01M8/04029H01M8/04044H01M8/04074H01M8/04097H01M8/04164H01M8/04179H01M8/04253H01M8/04291H01M2008/1095H01M2250/20Y02T90/32
    • Coolant velocity greater than zero everywhere within the coolant channels (78, 85) of fuel cells (38) in a fuel cell stack (37) is assured by providing a flow of gas in the coolant channels, the flow being created by gas pressure from a source (92) of pressurized gas, an oxidant reactant air pump (52), a source (75) of hydrogen-containing fuel, or the fuel outlet (47), or the outflow of a condenser (59). Positive pressure may be applied to the coolant inlet (66) or negative pressure from an eductor (97) may be applied to a gas outlet (90) of the coolant channels, or both. Using gas to induce flow within the coolant channels eliminates the need for a bubble-clearing liquid pump and reduces liquid inventory and other plumbing; this makes the fuel cell power plant more freeze tolerant. Biphase flow from the condenser, which may be a vehicle radiator (120), renders the coolant return flow more freeze tolerant. Separate cooler plates (122) may be used with a coolant management system (125).
    • 在燃料电池堆(37)中的燃料电池(38)的冷却剂通道(78,85)内的任何地方的冷却剂速度大于零,通过在冷却剂通道中提供气体流来确保流动,气流由气体压力 加压气体源(92),氧化剂反应物气泵(52),含氢燃料源(75)或燃料出口(47)或冷凝器(59)的流出。 可以对冷却剂入口(66)施加正压力,或者可以将来自喷射器(97)的负压施加到冷却剂通道的气体出口(90)或两者。 使用气体在冷却剂通道内引起流动,消除了清除液体泵的需要,并减少液体库存和其他管道; 这使得燃料电池发电厂更具有耐冻性。 来自可以是车辆散热器(120)的冷凝器的双相流动使得冷却剂返回流更具有耐冻性。 分开的冷却器板(122)可以与冷却剂管理系统(125)一起使用。