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1.发明申请System and Method for Returning Material from the BR2 Side of an H2/BR2 Flow Battery Back after Crossover 审中-公开H2 / BR2流量电池BR2侧回流材料的分离系统和方法公开(公告)号：US20160322653A1
公开(公告)日：2016-11-03
申请号：US15105874
申请日：2014-12-22
IPC分类号： H01M8/04089 , H01M8/04007 , H01M8/04082 , H01M8/04276 , H01M8/20 , H01M8/18
CPC分类号： H01M8/04097 , H01M8/04007 , H01M8/04197 , H01M8/04216 , H01M8/04283 , H01M8/188 , H01M8/20 , Y02E60/528
摘要： A flow battery system includes a first tank having a hydrogen reactant, a second tank having a bromine electrolyte, at least one cell including a hydrogen reactant side operably connected to the first tank through an ¾ feed and return system and a bromine electrolyte side operably connected to the second tank, and a crossover return system. The crossover return system includes a vessel operably connected to the ¾ feed and return system and configured to receive an effluent containing a first portion of the hydrogen reactant and a second portion of the bromine electrolyte, the vessel configured to separate the first portion from the second portion. A first return line returns the first portion of the hydrogen reactant to the first tank and a second return line returns the bromine electrolyte to the second tank.
摘要翻译： 流动电池系统包括具有氢反应物的第一罐，具有溴电解质的第二罐，至少一个包含氢反应物侧的电池，其通过¾进料和返回系统可操作地连接到第一罐，并且溴电解质侧可操作地连接 到第二个坦克，和一个交叉回报系统。 交叉返回系统包括可操作地连接到¾进料和返回系统并构造成接收含有氢反应物的第一部分和溴电解质的第二部分的流出物的容器，该容器被配置为将第一部分与第二部分 一部分。 第一返回线将氢反应物的第一部分返回到第一罐，第二回流管线将溴电解液返回到第二罐。
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2.发明申请Hydrogen/Bromine Flow Battery in which Hydrogen is Freely Exchanged between Two Cell Compartments 审中-公开在两个电池室之间自由交换氢气的氢/溴流量电池公开(公告)号：US20160308237A1
公开(公告)日：2016-10-20
申请号：US15104161
申请日：2014-12-18
IPC分类号： H01M8/18 , H01M8/20 , H01M8/22 , H01M8/04082
CPC分类号： H01M8/188 , H01M8/04201 , H01M8/04208 , H01M8/184 , H01M8/20 , H01M8/22 , H01M2250/10 , Y02B90/14 , Y02E60/528
摘要： A flow battery system includes a first tank including a hydrogen reactant, a second tank including a bromine electrolyte, and at least one cell including a first electrolyte side operably connected to the first tank and a second electrolyte side operably connected to the second tank. The battery system further includes a direct connection line directly connecting the first tank and the second tank and configured such that the hydrogen reactant passes between the first tank and the second tank.
摘要翻译： 流动电池系统包括包括氢反应物的第一罐，包括溴电解质的第二罐和至少一个包含可操作地连接到第一罐的第一电解质侧和与第二罐可操作地连接的第二电解质侧的电池。 电池系统还包括直接连接第一罐和第二罐的直接连接管，并且构造成使得氢反应物在第一罐和第二罐之间通过。
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3.发明授权公开(公告)号：US11594749B2
公开(公告)日：2023-02-28
申请号：US15104161
申请日：2014-12-18
IPC分类号： H01M4/36 , H01M6/24 , H01M4/58 , H01M6/04 , H01M6/20 , H01M8/18 , H01M8/04082 , H01M8/20 , H01M8/22
摘要： A flow battery system includes a first tank including a hydrogen reactant, a second tank including a bromine electrolyte, and at least one cell including a first electrolyte side operably connected to the first tank and a second electrolyte side operably connected to the second tank. The battery system further includes a direct connection line directly connecting the first tank and the second tank and configured such that the hydrogen reactant passes between the first tank and the second tank.
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公开(公告)号：US10326153B2
公开(公告)日：2019-06-18
申请号：US15105874
申请日：2014-12-22
IPC分类号： H01M8/04007 , H01M8/20 , H01M8/04089 , H01M8/18 , H01M8/04082 , H01M8/04276
摘要： A flow battery system includes a first tank having a hydrogen reactant, a second tank having a bromine electrolyte, at least one cell including a hydrogen reactant side operably connected to the first tank through an ¾ feed and return system and a bromine electrolyte side operably connected to the second tank, and a crossover return system. The crossover return system includes a vessel operably connected to the ¾ feed and return system and configured to receive an effluent containing a first portion of the hydrogen reactant and a second portion of the bromine electrolyte, the vessel configured to separate the first portion from the second portion. A first return line returns the first portion of the hydrogen reactant to the first tank and a second return line returns the bromine electrolyte to the second tank.
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公开(公告)号：US11881604B2
公开(公告)日：2024-01-23
申请号：US17488408
申请日：2021-09-29
发明人： Masaki Ando , Toshihiko Yoshida , Adam Z. Weber
IPC分类号： H01M8/00 , H01M8/04828 , H01M8/04492 , H01M8/04119
CPC分类号： H01M8/04835 , H01M8/045 , H01M8/04119 , H01M8/04507
摘要： A fuel cell system comprising: a fuel cell, a fuel gas supplier configured to supply fuel gas to an anode of the fuel cell, an oxidant gas supplier configured to supply oxidant gas to a cathode of the fuel cell, a humidity adjuster configured to adjust a relative humidity of the fuel gas and a relative humidity of the oxidant gas, and a controller, wherein the controller detects the relative humidity of the fuel gas at an anode inlet of the fuel cell, and the controller detects the relative humidity of the oxidant gas at a cathode outlet of the fuel cell, and wherein, based on detection results, the controller controls the humidity adjuster so that the relative humidity of the fuel gas at the anode inlet is higher than the relative humidity of the oxidant gas at the cathode outlet.
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公开(公告)号：US11843146B2
公开(公告)日：2023-12-12
申请号：US17488408
申请日：2021-09-29
发明人： Masaki Ando , Toshihiko Yoshida , Adam Z. Weber
IPC分类号： H01M8/00 , H01M8/04828 , H01M8/04492 , H01M8/04119
CPC分类号： H01M8/04835 , H01M8/045 , H01M8/04119 , H01M8/04507
摘要： A fuel cell system comprising: a fuel cell, a fuel gas supplier configured to supply fuel gas to an anode of the fuel cell, an oxidant gas supplier configured to supply oxidant gas to a cathode of the fuel cell, a humidity adjuster configured to adjust a relative humidity of the fuel gas and a relative humidity of the oxidant gas, and a controller, wherein the controller detects the relative humidity of the fuel gas at an anode inlet of the fuel cell, and the controller detects the relative humidity of the oxidant gas at a cathode outlet of the fuel cell, and wherein, based on detection results, the controller controls the humidity adjuster so that the relative humidity of the fuel gas at the anode inlet is higher than the relative humidity of the oxidant gas at the cathode outlet.
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