JPH02242570A - Storage of zinc-bromine battery - Google Patents

Storage of zinc-bromine battery

Info

Publication number
JPH02242570A
JPH02242570A JP1062590A JP6259089A JPH02242570A JP H02242570 A JPH02242570 A JP H02242570A JP 1062590 A JP1062590 A JP 1062590A JP 6259089 A JP6259089 A JP 6259089A JP H02242570 A JPH02242570 A JP H02242570A
Authority
JP
Japan
Prior art keywords
bromine
battery
zinc
anode
stored
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP1062590A
Other languages
Japanese (ja)
Other versions
JP2526659B2 (en
Inventor
Takashi Hashimoto
敬史 橋本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Original Assignee
Meidensha Corp
Meidensha Electric Manufacturing Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Meidensha Corp, Meidensha Electric Manufacturing Co Ltd filed Critical Meidensha Corp
Priority to JP1062590A priority Critical patent/JP2526659B2/en
Publication of JPH02242570A publication Critical patent/JPH02242570A/en
Application granted granted Critical
Publication of JP2526659B2 publication Critical patent/JP2526659B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M12/00Hybrid cells; Manufacture thereof
    • H01M12/08Hybrid cells; Manufacture thereof composed of a half-cell of a fuel-cell type and a half-cell of the secondary-cell type
    • H01M12/085Zinc-halogen cells or batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Hybrid Cells (AREA)

Abstract

PURPOSE:To prevent the lowering of battery efficiency even for long time storage by removing bromine with zinc electrodeposited to a cathode and anode through a process of forcing an electric current to flow in a discharge direction under a condition where the supply of bromine is stopped after a battery is charged. CONSTITUTION:A zinc-bromine battery 1 to be transported or stored for a long time is charged, the bromine having large specific gravity generated and collected in the bottom part of an anode tank is removed and then the battery is discharged. Then after battery voltage becomes 0V, electric current is forced to flow continuously in a discharge direction, and after the zinc is sufficiently electrically deposited on an anode 11, electrolytic solution is circulated, the bromine is removed in such a way that the zinc and bromine on the anode 11 are made to make direct mutual reaction, and the battery 1 from which the bromine is removed is transported or stored for a long time. This enables the bromine to be unresidual in the battery 1, the deterioration of an electrode or separator due to a bromine attack to be prevented, and the battery to be stored for a long time in its good condition.

Description

【発明の詳細な説明】 A 産業上の利用分野 この発明は、亜鉛−臭素電池を、効率低下させることな
く、長期に亘って保管しうろ方法に関−4ろ。
DETAILED DESCRIPTION OF THE INVENTION A. Industrial Field of Application The present invention relates to a method for storing zinc-bromine batteries over long periods of time without reducing efficiency.

L3  発明の概要 本発明は、電解液を循環させて使用する亜鉛臭素電池に
おいて、 電池充電後、臭素の供給を断った状態で、放電方向に電
流を流し、臭素を除去してから保管することにより、 臭素アタックによる電極のワーページ、劣化を防止し、
良好に長期保管可能とするものである。
L3 Summary of the Invention The present invention provides a method for storing a zinc bromine battery using a circulating electrolyte by passing a current in the discharge direction with the supply of bromine cut off after charging the battery to remove bromine. This prevents electrode warpage and deterioration caused by bromine attack,
It allows for good long-term storage.

C0従来の技術 近時、電池電力貯蔵システ18の開発が促進されており
、その−環として第2図乃至第4図に例示する如く電解
液循環型亜鉛−臭素積層二次電池が開発されている。
BACKGROUND OF THE INVENTION Recently, the development of battery power storage systems 18 has been promoted, and electrolyte circulation type zinc-bromine laminated secondary batteries have been developed as a part of this system, as illustrated in FIGS. 2 to 4. There is.

これは、第2図の構成原理図に示すように、電池本体1
をイオン交換膜または多孔質膜からなるセパレータ2で
陽極室3と陰極室4とに区画17、この両極室にそれぞ
れ電解液を循環させるための送液管5.6と返液管7,
8とにより電解液タンク9.IOを接続して設け、臭化
亜鉛(7,n f’、 r 2)の電解液をそれぞれの
゛屯極室に循環させるようにしたものである。尚、11
は陽極、I2は陰極、13.14は共に送液ポンプ、1
5は弁である。
As shown in the structural principle diagram in Fig. 2, this
is divided into an anode chamber 3 and a cathode chamber 4 by a separator 2 made of an ion exchange membrane or a porous membrane, and a liquid sending tube 5.6 and a liquid return tube 7 for circulating the electrolyte in these two electrode chambers, respectively.
8 and electrolyte tank 9. IO is connected and provided, and an electrolytic solution of zinc bromide (7, n f', r 2) is circulated to each electrode chamber. In addition, 11
is an anode, I2 is a cathode, 13.14 are both liquid pumps, 1
5 is a valve.

しかして、充電時には、電解液が図の矢印の方向に循環
し、陰極12てはZ n ”+ 2 e−> Z n、
陽極IIでは2Br−→Br2+2eの反応を生じ、陽
極11で生成された臭素は分子となり、電解液中に混じ
り、一部溶解し、大部分は陽極液中の錯化剤によって錯
化物となり、陽極室側の電解液タンク■0内に沈澱して
蓄積される。又、放電時には、電解液が循環した状態で
各電極11,12ではそれぞれ前記反応式と逆の反応を
生じ、析出物(Zn、Br、)  か各電極I+、12
上て消費(酸化、還元)され、上気エネルギーが放出さ
れるようにしたものである。
Therefore, during charging, the electrolyte circulates in the direction of the arrow in the figure, and the cathode 12 has Zn''+2e->Zn,
At the anode II, a reaction of 2Br-→Br2+2e occurs, and the bromine generated at the anode 11 becomes a molecule, mixes in the electrolyte, partially dissolves, and mostly becomes a complex with the complexing agent in the anolyte, and the bromine produced at the anode 11 becomes a molecule. Precipitates and accumulates in the electrolyte tank ① on the room side. Further, during discharge, a reaction opposite to the above reaction formula occurs at each electrode 11 and 12 with the electrolyte circulating, and precipitates (Zn, Br,) or each electrode I+, 12
It is designed so that the upper air energy is consumed (oxidized, reduced) and released.

また、」−述のような構成原理の亜鉛−臭素電池には、
第3図に例示するような実用積層電池本体として多数の
セル積層構造のスタックが用いられている。にれは、ス
タック全体を、−側面から他側面にかけて貫挿する複数
のボルト28に、各々ナツト29を嵌合して、セル積層
体全体を挟むように押さえるための一対の締付端板16
との間に、例えば30セル積層1.て構成する。
In addition, the zinc-bromine battery with the construction principle as described above has
A stack of a large number of cell laminated structures is used as a practical laminated battery body as illustrated in FIG. A pair of tightening end plates 16 are used to sandwich and hold the entire cell stack by fitting nuts 29 into a plurality of bolts 28 that penetrate the entire stack from one side to the other.
For example, 30 cells are stacked 1. Configure.

このように積層構成したスタックには、第3図に示すよ
うに、その四隅角部に流液孔である正極マニホールド2
4と負極マニホールド25とを穿設する。
As shown in Fig. 3, this stack has positive electrode manifolds 2, which are liquid flow holes, at its four corners.
4 and the negative electrode manifold 25 are bored.

また、各セパレータ板2Iは、ぞの周囲にパラキンとし
ても機能する枠体21aの両車面部1−下にそれぞれ表
裏対称形状にマイクロチャンネル26を設置して成り、
その−側面の実線で示すマイクロチャンネル26は、そ
れぞれ対角線上の正極マニホールド24から導入した電
解液を均一・に広げてセパレータ2の全面に流し、又は
これより液を回収する。また、他側面の破線で示すマイ
ク[Jチャンネル26は、負極マニホールド25からの
電解液を導入1回収するものである。
Further, each separator plate 2I is formed by installing microchannels 26 in a symmetrical shape on the front and back under both vehicle surface portions 1 of a frame body 21a that also functions as a parakin around the separator plate 2I,
The microchannels 26 shown by solid lines on the negative side of the microchannels 26 uniformly spread the electrolytic solution introduced from the positive electrode manifold 24 on the diagonal line and flow it over the entire surface of the separator 2, or collect the solution therefrom. In addition, the microphone [J channel 26 shown by the broken line on the other side is for introducing and recovering the electrolyte from the negative electrode manifold 25.

このようにして、各セパレータ板21の両側面部にそれ
ぞれ配置された電極との間において、第2図に例示した
単位電池となるセルを構成し、スタックとしては、この
セルか30個直列接続されるよう構成するものである。
In this way, between the electrodes arranged on both side surfaces of each separator plate 21, cells that become the unit battery illustrated in FIG. 2 are constructed, and 30 of these cells are connected in series to form a stack. It is configured so that

このような、亜鉛−臭素電池を保管するには、従来、電
池を充電後又は、完全放電後の場合に応して、次のよう
に行っていた。
Conventionally, such a zinc-bromine battery has been stored as follows, depending on whether the battery has been charged or completely discharged.

まず、電池を充電後に保管するときに、保管時間が10
時間を越える場合には、スタック内の電解液を全て、電
解液タンク9.10内に戻した状態で保管する。
First, when storing the battery after charging, the storage time is 10
If the time is exceeded, all the electrolyte in the stack is returned to the electrolyte tank 9.10 and stored.

これは、電池を充電した状態では、陰極12面」−に亜
鉛が電析しており、陽極11面」二には、臭素が付着し
た状態にある。このため、電解液をスタックに充填した
状態で電池を保管すると、陽極液中の臭素が陰極12上
の亜鉛と自己放電を起こし、さらに、保管時、この臭素
が電極とセパレータを腐食して、電池効率が低下するの
を防止するためである。
This means that when the battery is charged, zinc is electrodeposited on the cathode 12 surface, and bromine is deposited on the anode 11 surface. Therefore, if the battery is stored with the electrolyte filled in the stack, bromine in the anolyte will cause self-discharge with the zinc on the cathode 12, and furthermore, during storage, this bromine will corrode the electrodes and separators. This is to prevent battery efficiency from decreasing.

また、電池を完全放電後に保管するには、第4図に示4
−ように、スタック内に電解液を充填したままの状態で
保管していた。これは、電池の完全放電後は、陰極12
上の亜鉛が完全に溶解し、陰極12の表面が露出してい
る状態にあるので、自己放電の心配がないからである。
In addition, to store the battery after it has been completely discharged, please use the
- The stack was stored with the electrolyte still filled. This means that after the battery is fully discharged, the cathode 12
This is because the upper zinc is completely dissolved and the surface of the cathode 12 is exposed, so there is no fear of self-discharge.

なお、陽極11面上には、臭素が付層した状態となって
いる。
Note that bromine is layered on the surface of the anode 11.

■) 発明が解決しようとする課題 前述したような、電池の充電後又は完全放電後のそれぞ
れの保管方法においても第4図に例示ずろ如く、陽極l
l上に臭素が111着しているため、保管期間中に、カ
ーボンプラスチック電極及びセパレータを腐食し、これ
を劣化させ電池効率を低下させることがあるという問題
がある。
■) Problems to be Solved by the Invention In each of the storage methods described above after charging or completely discharging a battery, as shown in FIG.
Since 111 bromine is attached to L, there is a problem in that during storage, the carbon plastic electrode and separator may corrode, deteriorate them, and reduce battery efficiency.

さらに、カーボンプラスチック電極は、臭素による膨潤
により、ワーページ(撓み)を生じ、その平滑性が損な
われる。
Furthermore, the carbon plastic electrode undergoes warpage (deflection) due to swelling due to bromine, and its smoothness is impaired.

このように、電極にワーベージを生ずると、スタック内
における電解液の流れ分布か乱れ、亜鉛のデンドライト
発生(亜鉛がひげ状に電析する現象)ににる効率低下の
原因となるという問題があった。
As described above, when worming occurs in the electrodes, the flow distribution of the electrolyte within the stack is disturbed, which causes a decrease in efficiency due to the formation of zinc dendrites (a phenomenon in which zinc is deposited in the form of whiskers). Ta.

また、このような電極に対する臭素アタックを防lトす
るため、スタック内を、イオン交換水によって洗浄する
手段も試みられたが、電池本体内の臭素を除去するのは
困難であった。
Furthermore, in order to prevent such bromine attack on the electrodes, attempts have been made to clean the inside of the stack with ion-exchanged water, but it has been difficult to remove bromine from within the battery body.

特に、陽極11の素材として、炭素繊維を使用している
電池では、臭素の吸着が起こっているため、イオン交換
水で数日間洗浄しても、はとんど臭素を除去できず、こ
の問題を解決する手段がなか っ ノこ。
In particular, in batteries that use carbon fiber as the material for the anode 11, bromine is adsorbed, so even if washed with ion-exchanged water for several days, bromine cannot be removed, causing this problem. There is no way to solve this problem.

本発明は、上述の点に鑑み、亜鉛 臭素電池を長期に亘
って保管しても、電池効率が低電しないようにできる保
管方法を新たに提供することを「1的とする。
In view of the above points, it is an object of the present invention to provide a new storage method that can prevent the battery efficiency from decreasing even if a zinc bromine battery is stored for a long period of time.

D〕 課題を解決するための手段 本発明の亜鉛−臭素電池の保管方法は、電池を充電後、
臭素の供給を断った状態で、放電方向に電流を流し、陰
極及び陽極に亜鉛を電着させるようにして臭素を除去す
るようにしたことを特徴とする。
D] Means for Solving the Problems The method for storing a zinc-bromine battery of the present invention includes: after charging the battery,
The present invention is characterized in that, while the supply of bromine is cut off, current is passed in the direction of discharge to cause zinc to be electrodeposited on the cathode and anode, thereby removing bromine.

F9作用 」二連のような方法を施すことにより、電池内に臭素が
残留しないよう除去して、臭素アタックによる電極やセ
パレータの劣化を防止し、電極のワーページ発生を防止
し、良好な状態で電池を長期に亘って保管できるように
するという作用を奏する。
By applying a method such as "F9 action" in two series, bromine is removed so that it does not remain in the battery, preventing deterioration of the electrodes and separators due to bromine attack, preventing warpage of the electrodes, and keeping the battery in good condition. This has the effect of allowing batteries to be stored for a long period of time.

G、実施例 以下、本発明の亜鉛−臭素電池の保管方法の実施例を、
第1図によって説明する。なお、この第1図において、
第2図乃至第4図に示す従来例に対応する部分には同一
符号を付すこととし、説明の便に供する。
G. Examples Hereinafter, examples of the method for storing zinc-bromine batteries of the present invention will be described.
This will be explained with reference to FIG. In addition, in this Figure 1,
The same reference numerals are given to the parts corresponding to the conventional example shown in FIGS. 2 to 4 for convenience of explanation.

本例の手段は、電池のスタック内の臭素を完全に除去す
るたぬの、電気化学的処理方法であって、特に、亜鉛−
臭素電池を運搬する場合や、長期保管する場合に適する
ものである。
The means of the present example is an electrochemical treatment method for completely removing bromine in a battery stack, in particular zinc-
This is suitable for transporting bromine batteries and storing them for long periods of time.

まず、第1に、運搬又は長期保管する亜鉛−臭素電池を
充電する。
First, a zinc-bromine battery to be transported or stored for a long time is charged.

この充電電気量は、充電時の電解液中の臭素量や、スタ
ック内に何着している臭素量を十分に越える蛍で、陽極
11上に亜鉛電析が始まったときても陰極I2上に十分
に亜鉛が残っているような適正量を確保できるものとす
る。なお、この充電電気量は、個々の電池の構造に依存
するが、陰極12上の亜鉛が不足すると、陽極lI上で
は亜鉛の電析が行われるが、陰極上では臭素が発生ずる
ことになり、スタック内から臭素を除去するこきができ
なくなるので十分な量が必要である。
This charging amount of electricity sufficiently exceeds the amount of bromine in the electrolyte during charging and the amount of bromine deposited in the stack, and even when zinc electrodeposition begins on the anode 11, the amount of electricity on the cathode I2 is It shall be possible to secure an appropriate amount of zinc so that there is enough remaining in the zinc. The amount of charged electricity depends on the structure of each individual battery, but if there is a shortage of zinc on the cathode 12, zinc will be deposited on the anode II, but bromine will be generated on the cathode. A sufficient amount is necessary because it will not be possible to remove bromine from the stack.

本例では、電極面積1600c1N2.30セルのバイ
ポーラ電池を用い、2OAで5時間充電するものとした
In this example, a bipolar battery with an electrode area of 1600 c1N2.30 cells was used and was charged at 2OA for 5 hours.

第2に、第1工程の充電時に発生した比重の大きい臭素
が陽極タンクの底部に溜まっているので、これを除去す
る。
Second, since bromine with a high specific gravity generated during charging in the first step is accumulated at the bottom of the anode tank, this is removed.

第3にこの電池を放電する。本例では20Δで、1時間
放電したところで電池電圧が0■に達した。
Third, discharge the battery. In this example, the battery voltage reached 0■ after discharging for 1 hour at 20Δ.

この放電は、電解液中に溶(Jている臭素や、陽極上に
耐着している臭素が消費されながら行なわれるものであ
る。
This discharge occurs while bromine dissolved in the electrolyte and bromine adhered to the anode are consumed.

第4に、電池電圧がOVになった以後、放電方向に1ト
流を流し続ける。
Fourth, after the battery voltage reaches OV, the current continues to flow in the discharge direction.

これにより、陽極11上には、亜鉛の電析(Z n”−
7,n+ 2 e)と、臭素の還元(B r、−Br 
+ 2 e)の反応が同時に起こり、このまま通電する
ことにより、電解液中の臭素を除去する3、本例では、
放電と同じ方向に2時間通電し、陽極液が無色透明とな
って、臭素が除去さ石たのを確認した。
As a result, zinc electrodeposition (Z n”-
7, n+ 2 e) and the reduction of bromine (Br, -Br
+ 2 e) reaction occurs at the same time, and by applying current as it is, bromine in the electrolyte is removed 3. In this example,
Electricity was applied in the same direction as the discharge for 2 hours, and the anolyte became colorless and transparent, confirming that bromine had been removed.

第5に、上述の方法で、陽極11F〕に十分亜鉛が電析
した後、電解液を循環し、陽極11上の亜鉛と臭素とを
直接反応させるようにし、(Z n +B r、+ Z
 n”÷2Br−)臭素を除去する。
Fifth, after sufficiently depositing zinc on the anode 11F] using the above method, the electrolytic solution is circulated to cause the zinc on the anode 11 to react directly with bromine, so that (Z n +B r, + Z
n''÷2Br-) Remove bromine.

上述のように、臭素を除去した電池を、運搬又は長期保
管するものである。
As mentioned above, the battery from which bromine has been removed is transported or stored for a long period of time.

本例では、3ケ月放置した。In this example, it was left for three months.

そして、この後、電池の長期保管法の効果を見るため、
充電側に通電し、陽極液に臭素が発生したのを確認して
から、第2工程で除去した臭素をタンクに戻し、完全放
電を行った。この後、この電池のスタックを解体して調
査したところ、電極には全くワーページや劣化が見られ
ず、十分に効果があることが確認された。
After this, in order to see the effects of long-term battery storage methods,
After applying electricity to the charging side and confirming that bromine was generated in the anolyte, the bromine removed in the second step was returned to the tank, and complete discharge was performed. After this, the battery stack was disassembled and investigated, and the electrodes showed no warpage or deterioration, confirming that they were sufficiently effective.

なお、比較の為、前述した従来の完全放電をしただ11
.lで放置した電池を解体したところ、電極には、臭素
劣化によるツーページCl0m屑程度のそり)が生じて
いた。これと比較しても、本例の方法が実効あることが
理解される。
For comparison, the conventional complete discharge described above was performed.
.. When the battery that had been left unattended was dismantled, the electrodes were found to have warpage (about the size of two-page Cl0m scraps) due to bromine deterioration. Even when compared with this, it can be seen that the method of this example is effective.

tr  発明の効果 以上詳述したように、本発明の亜鉛−臭素電池の保管方
法によれば、亜鉛−臭素電池を充電後、電池内への臭素
の供給を断った状態で、放電方向に電流を流し、臭素を
除去するため陰極及び陽極に亜鉛を電着させる処理をし
た後、運搬や長期保管をするようにしたので、電池内に
臭素が残留しない。従って、臭素アタックによる電極や
セパレータの劣化を防1トシ、電極のワーページ発生を
防止し、良好な状態で電池を長期に亘って保管できると
いう効果がある。
tr Effects of the Invention As detailed above, according to the method for storing a zinc-bromine battery of the present invention, after charging a zinc-bromine battery, a current is applied in the discharge direction while the supply of bromine to the battery is cut off. Since the batteries are transported and stored for long periods of time after being subjected to a treatment in which zinc is electrodeposited on the cathode and anode to remove bromine, no bromine remains inside the batteries. Therefore, it is possible to prevent deterioration of the electrodes and separators due to bromine attack, prevent warpage of the electrodes, and enable the battery to be stored in good condition for a long period of time.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の亜鉛−臭素電池の保管方法の実施例を
説明4−る単電池モデルを示す要部説明線図、第2図は
従来の亜鉛−臭素電池の原理の概略説明線図、第3図は
その要部である電池本体部分の拡大分解斜視図、第4図
はその単電池モデルを示す要部説明線図である。 1−・電池本体、11・陽極、12・・陰極、18端板
電極、23・・・中間電極。 妊
Fig. 1 is a diagram illustrating the main parts of a unit cell model explaining an embodiment of the method for storing zinc-bromine batteries according to the present invention, and Fig. 2 is a diagram schematically explaining the principle of a conventional zinc-bromine battery. , FIG. 3 is an enlarged exploded perspective view of the main part of the battery, and FIG. 4 is an explanatory diagram of the main parts showing the unit cell model. 1- Battery body, 11 Anode, 12 Cathode, 18 End plate electrode, 23 Intermediate electrode. pregnancy

Claims (1)

【特許請求の範囲】[Claims] (1)電池を所要量充電し、この後、当該電池を、臭素
の供給を断った状態で放電方向に通電して臭素を除去し
てから保管するようにしたことを特徴とする亜鉛−臭素
電池の保管方法。
(1) Zinc-bromine, characterized in that the battery is charged to a required amount, and then the battery is stored after being energized in the discharge direction with bromine supply cut off to remove bromine. How to store batteries.
JP1062590A 1989-03-15 1989-03-15 How to store zinc-bromine batteries Expired - Fee Related JP2526659B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1062590A JP2526659B2 (en) 1989-03-15 1989-03-15 How to store zinc-bromine batteries

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1062590A JP2526659B2 (en) 1989-03-15 1989-03-15 How to store zinc-bromine batteries

Publications (2)

Publication Number Publication Date
JPH02242570A true JPH02242570A (en) 1990-09-26
JP2526659B2 JP2526659B2 (en) 1996-08-21

Family

ID=13204690

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1062590A Expired - Fee Related JP2526659B2 (en) 1989-03-15 1989-03-15 How to store zinc-bromine batteries

Country Status (1)

Country Link
JP (1) JP2526659B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0177270U (en) * 1987-11-12 1989-05-24

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0177270U (en) * 1987-11-12 1989-05-24

Also Published As

Publication number Publication date
JP2526659B2 (en) 1996-08-21

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