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    • 4. 发明申请
    • INTERNAL CONVECTION CELL
    • 内部对流电池
    • WO2013066829A2
    • 2013-05-10
    • PCT/US2012/062503
    • 2012-10-30
    • FLUIDIC, INC.
    • FRIESEN, Cody A.KRISHNAN, RamkumarFRIESEN, GrantHAYES, Joel
    • H01M8/22
    • H01M12/08H01M2/385H01M4/8605Y02E60/128
    • An electrochemical cell includes a permeable fuel electrode configured to support a metal fuel thereon, and an oxidant reduction electrode spaced from the fuel electrode. An ionically conductive medium is provided for conducting ions between the fuel and oxidant reduction electrodes, to support electrochemical reactions at the fuel and oxidant reduction electrodes. A charging electrode is also included, selected from the group consisting of (a) the oxidant reduction electrode, (b) a separate charging electrode spaced from the fuel and oxidant reduction electrodes, and (c) a portion of the permeable fuel electrode. The charging electrode is configured to evolve gaseous oxygen bubbles that generate a flow of the ionically conductive medium. One or more flow diverters are also provided in the electrochemical cell, and configured to direct the flow of the ionically conductive medium at least partially through the permeable fuel electrode.
    • 电化学电池包括被配置为在其上支撑金属燃料的可渗透燃料电极和与燃料电极间隔开的氧化剂还原电极。 提供离子导电介质用于在燃料和氧化剂还原电极之间传导离子,以支持燃料和氧化剂还原电极处的电化学反应。 还包括充电电极,选自(a)氧化剂还原电极,(b)与燃料和氧化剂还原电极隔开的分开的充电电极,和(c)可渗透燃料电极的一部分。 充电电极被配置为产生产生离子导电介质流的气态氧气泡。 还在电化学电池中提供一个或多个流量分流器,并且被配置为引导离子导电介质的流动至少部分地通过可渗透的燃料电极。
    • 5. 发明申请
    • IMMERSIBLE GASEOUS OXIDANT CATHODE FOR ELECTROCHEMICAL CELL SYSTEM
    • 电化学电池系统不可或缺的氧化物阴极
    • WO2013066828A2
    • 2013-05-10
    • PCT/US2012/062502
    • 2012-10-30
    • FLUIDIC, INC.
    • FRIESEN, Cody A.KRISHNAN, RamkumarMIHALKA, MichaelFRIESEN, GrantGOODFELLOW, Andrew
    • H01M8/22H01M4/88H01M4/86
    • H01M12/065H01M4/86H01M12/08Y02E60/128Y02E60/50
    • An electrochemical cell system is configured to utilize an oxidant reduction electrode module containing an oxidant reduction electrode mounted to a housing to form a gaseous oxidant space therein that is immersed into the ionically conductive medium. A fuel electrode is spaced from the oxidant reduction electrode, such that the ionically conductive medium may conduct ions between the fuel and oxidant reduction electrodes to support electrochemical reactions at the fuel and oxidant reduction electrodes. A gaseous oxidant channel extending through the gaseous oxidant space provides a supply of oxidant to the oxidant reduction electrode, such that the fuel electrode and the oxidant reduction electrode are configured to, during discharge, oxidize the metal fuel at the fuel electrode and reduce the oxidant at the oxidant reduction electrode, to generate a discharge potential difference therebetween for application to a load.
    • 电化学电池系统被配置为利用氧化剂还原电极模块,其包含安装到壳体上的氧化剂还原电极,以在其中形成浸入离子导电介质中的气态氧化剂空间。 燃料电极与氧化剂还原电极间隔开,使得离子导电介质可以在燃料和氧化剂还原电极之间传导离子,以支持在燃料和氧化剂还原电极处的电化学反应。 延伸穿过气态氧化剂空间的气态氧化剂通道提供氧化剂还原电极的氧化剂供应,使得燃料电极和氧化剂还原电极被配置成在放电期间氧化燃料电极处的金属燃料并减少氧化剂 在氧化剂还原电极处产生用于负载的放电电位差。
    • 6. 发明申请
    • WATER MANAGEMENT SYSTEM IN ELECTROCHEMICAL CELLS WITH VAPOR RETURN COMPRISING AIR ELECTRODES
    • 具有包含空气电极的蒸汽返回的电化学电池中的水管理系统
    • WO2016160418A1
    • 2016-10-06
    • PCT/US2016/023564
    • 2016-03-22
    • FLUIDIC, INC.
    • KRISHNAN, RamkumarHAYES, JoelFRIESEN, GrantFINK, Shawn
    • H01M12/08
    • H01M8/0485C25B15/08H01M8/04126H01M8/04171H01M10/42H01M12/08Y02E60/128
    • A system and methods for managing water content in one or more electrochemical cell is disclosed. The system includes a gas-phase conduit for receiving humid gas-phase associated with the electrochemical cell, a desiccator unit connected to each electrochemical cell and configured for extracting water from the humid gas-phase, a heater for selectively heating the desiccator unit, and a carbon dioxide (CO2) scrubber connected to the desiccator unit. The system may capture water vapor at the desiccator unit from a humid gas-phase exiting electrochemical cell, or release water vapor in desiccator unit, via actuation of heater, that is transported into the electrochemical cell depending on the mode of operation. The CO2 scrubber may also be used to capture water vapor, based on the mode of operation.
    • 公开了一种或多种电化学电池中用于管理含水量的系统和方法。 该系统包括用于接收与电化学电池相关联的湿气相的气相管道,连接到每个电化学电池并被构造用于从湿气相中提取水的干燥器单元,用于选择性加热干燥器单元的加热器,以及 连接到干燥器单元的二氧化碳(CO 2)洗涤器。 该系统可以从干燥器单元捕获来自离开电化学电池的潮湿气相中的水蒸汽,或者通过致动加热器释放干燥器单元中的水蒸汽,根据操作模式将其传输到电化学电池中。 CO2洗涤器也可用于捕获水蒸气,基于操作模式。
    • 10. 发明申请
    • SYSTEMS AND METHODS FOR MANAGEMENT OF ADDITIVES IN ELECTROCHEMICAL CELLS
    • 用于管理电化学细胞中添加剂的系统和方法
    • WO2016123113A1
    • 2016-08-04
    • PCT/US2016/014936
    • 2016-01-26
    • FLUIDIC, INC.
    • TRIMBLE, ToddKRISHNAN, RamkumarPUZHAEV, SergeyFRIESEN, Grant
    • H01M12/02H01M12/04H01M12/06H01M12/08H01M8/22H01M8/02
    • H01M8/0482H01M8/02H01M8/188H01M8/22H01M12/02H01M12/04H01M12/06H01M12/08Y02E60/128
    • The present disclosure relates to an electrochemical cell comprising a fuel electrode for oxidizing a fuel, an oxidant electrode for reducing an oxidant, and an ionically conductive medium for conducting ions between the fuel and oxidant electrodes to support electrochemical reactions at the fuel and oxidant electrodes. The ionically conductive medium comprises at least one active additive for enhancing (controlling the rate, overpotential and/or the reaction sites for) at least one electrochemical reaction within the cell. The cell further comprises an additive medium in contact with the ionically conductive medium and containing the at least one active additive capable of corroding or dissolving in the ionically conductive medium. The additive medium and/or casing is configured to release the active additive to the ionically conductive medium as a concentration of the active additive in the ionically conductive medium is depleted during operation of the cell.
    • 本公开涉及一种电化学电池,其包括用于氧化燃料的燃料电极,用于还原氧化剂的氧化剂电极和用于在燃料和氧化剂电极之间导电离子的离子导电介质,以支持燃料和氧化剂电极处的电化学反应。 离子导电介质包含用于增强(控制速率,超电势和/或反应位点)至少一个电池内的电化学反应的活性添加剂。 细胞还包含与离子导电介质接触并含有能够腐蚀或溶解在离子导电介质中的至少一种活性添加剂的添加剂介质。 添加剂介质和/或壳体被配置为当活性添加剂在离子导电介质中的浓度在电池操作期间耗尽时将活性添加剂释放到离子导电介质中。