JPH024990B2 - - Google Patents
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- Publication number
- JPH024990B2 JPH024990B2 JP57190713A JP19071382A JPH024990B2 JP H024990 B2 JPH024990 B2 JP H024990B2 JP 57190713 A JP57190713 A JP 57190713A JP 19071382 A JP19071382 A JP 19071382A JP H024990 B2 JPH024990 B2 JP H024990B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- negative electrode
- bromine
- mol
- bromide
- 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.)
- Expired - Lifetime
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Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/36—Accumulators not provided for in groups H01M10/05-H01M10/34
- H01M10/365—Zinc-halogen accumulators
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy 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)
Description
本発明は電解液循環型、亜鉛−臭素二次電池用
の電解液、さらに詳しくは亜鉛デンドライトの発
生を抑制する負極液の組成に関するものである。
近時エネルギー有効利用の観点から亜鉛−臭素
二次電池が著目され開発されている。例えば第1
図に示す如き電解液循環型の亜鉛−臭素二次電池
が利用されている。第1図はその基本的構成を示
すもので、図中1は単一セル、2は正極室、3は
負極室、4は隔膜(イオン交換膜または多孔質薄
膜のセパレータ)、5は正極、6は負極、7は正
極液、8は負極液、9は正極液貯槽、10は負極
液貯槽、11および12はポンプである。
これら電解液循環型の亜鉛−臭素二次電池に和
いては、充電時に、図中で示した負極6面上に
析出する亜鉛は負極面近傍の電界分布の不均一、
負極液の流れの乱れなどから平滑となりにくて樹
枝状晶の所謂デンドライトを形成することが多
く、特に充放電サイクルが増してくると次の問題
が生ずる。即ちこのデンドライト状析出亜鉛は非
常に脆いため、電極から脱落しやすく、電池のエ
ネルギー効率を低下せしめる。また電極から脱落
しなくても、そのまゝデンドライトが樹枝状に成
長し、隔膜4を貫通破壊し、正極5との短絡を起
し最終的に電池の破壊を惹起する原因となる。以
上の欠点を防止するために、ある種の添加剤を負
極液中に添加することによつてデンドライトの発
生及び長を防止する必要があつた。
従来上述のデンドライトの抑制剤としては、非
イオン系界面活性剤、亜鉛メツキ光沢剤等が使用
されていたが、充放電サイクル数が多くかつ長期
間に亘ると安定性に欠ける問題が生じた。特に隔
膜に安価な多孔質薄膜を用いると正極室から臭素
分子が微量ずつ負極室に滲透拡散するため、デン
ドライト抑制剤に対し耐臭素性の問題を生じ易
く、長期間に亘る多数回の充放電サイクル使用に
対して安定した性能を維持することが出来なかつ
た。また耐臭素性のあるものでも第2図に示す如
く負極面に析出した亜鉛表面に不均一な亜鉛の酸
化皮膜の形成によつて、デンドライトの発生を起
こすことが多かつた。
第2図は酸化皮膜の上にデンドライトが発生す
る機構を示す模式図である。第2−イ図は充放電
サイクルの少い間の充電末期における電極表面を
示し、負極6上に金属亜鉛Znが析出する。第2
−ロ図は放電初期における電極表面を示し、電極
6の表面より亜鉛イオンZn++が溶出する。第2
−ハ図は多数回の充放電サイクル後の放電末期の
状況を示し、金属亜鉛Zn上に不均一な酸化皮膜
ZnOを形成する。第2−ニ図は酸化皮膜形成後の
充電再開時の状況を示し不均一な酸化皮膜ZnO上
に選択的に金属亜鉛が析出する。第2−ホ図は充
電中期の状況を示し酸化皮膜上に選択的に析出し
た金属亜鉛上にデンドライトの樹枝状晶が発生す
る。即ち耐臭素性のある添加剤を使用した場合、
充放電サイクルが少ない間はデンドライトを形成
しなくても、サイクルを多数重ねるに従つて、放
電時生成された酸化皮膜によつてデンドライトが
形成され、これを防止する必要があつた。
本発明の目的は、前述の如く電解液循環型亜鉛
−臭素二次電池において、デンドライトの発生及
び成長を防止するための電解液の組成を提供する
にある。
本発明者らは、電解液循環型の亜鉛−臭素二次
電池のデンドライトの生成要因を究明し、これに
基いて、ある種の添加剤を負極電解液に添加する
ことによつて、上記発明の目的を達することを見
出し発明に至つたものである。
本発明の亜鉛−臭素電池の電解液は、活物質と
しての臭素と亜鉛を含む臭素亜鉛(ZnBr2)水溶
液中に2価の錫イオン(Sn++)を含有するとと
もに、メチル・エチル・モルホリニウム・ブロマ
イド及びメチル・エチル・ピロリジニウム・ブロ
マイドをそれぞれ0.5mol/含有したことを特
徴とした電解液である。
電解液中に含有される2価の錫イオンは放電時
に形成される亜鉛酸化皮膜の発生を防止し、その
形成に起因するデンドライトの発生を抑止する。
更に、2価の錫イオンとともに電解液中に特定
量含有される特定の複素環式第4級アンモニウム
塩からなる臭素錯化剤、即ちメチル・エチル・モ
ルホリニウム及びメチル・エチル・ピロジニウ
ム・ブロマイドは、隔膜(例えば多孔質膜)を介
し負極室に拡散した臭素(充電時に正極室で発
生)を捕獲するとともに、デンドライトの発生を
抑止するように働く。即ち、本発明では2価の錫
イオンと耐臭素性の臭素錯化剤であるメチル・エ
チル・モルホリニウム及びメチル・エチル・ピロ
リジニウム・ブロマイドを併用することによつて
デンドライトの発生及び成長を防止している。
亜鉛−臭素二次電池の負極電解液組成を、臭化
亜鉛(ZnBr2)をベースとし、これに2価の錫イ
オン(Sn++)を種々添加したもの、ならび、2
価の錫イオン(Sn++)の添加量を種々変えたも
のと、デンドライト抑制効果の大きい臭素錯体形
成剤として
A メチル、エチル、モルホリニウム、
The present invention relates to an electrolytic solution for a circulating electrolyte type zinc-bromine secondary battery, and more particularly to a composition of a negative electrode solution that suppresses the formation of zinc dendrites. Recently, zinc-bromine secondary batteries have been attracting attention and being developed from the viewpoint of effective energy utilization. For example, the first
An electrolyte circulation type zinc-bromine secondary battery as shown in the figure is used. Figure 1 shows its basic configuration, in which 1 is a single cell, 2 is a positive electrode chamber, 3 is a negative electrode chamber, 4 is a diaphragm (ion exchange membrane or porous thin film separator), 5 is a positive electrode, 6 is a negative electrode, 7 is a positive electrode liquid, 8 is a negative electrode liquid, 9 is a positive electrode liquid storage tank, 10 is a negative electrode liquid storage tank, and 11 and 12 are pumps. In terms of these electrolyte circulation type zinc-bromine secondary batteries, the zinc deposited on the negative electrode 6 surface shown in the figure during charging is caused by uneven electric field distribution near the negative electrode surface.
Due to disturbances in the flow of the negative electrode liquid, it is difficult to smooth the surface, and dendrites, which are dendrites, are often formed. Especially as the number of charge/discharge cycles increases, the following problem occurs. That is, since this dendrite-like precipitated zinc is very brittle, it easily falls off from the electrode, reducing the energy efficiency of the battery. Further, even if the dendrite does not fall off from the electrode, it continues to grow in a dendritic shape, penetrating and breaking the diaphragm 4, causing a short circuit with the positive electrode 5, and ultimately causing destruction of the battery. In order to prevent the above-mentioned drawbacks, it has been necessary to prevent the generation and length of dendrites by adding certain additives to the negative electrode liquid. Conventionally, nonionic surfactants, galvanizing brighteners, and the like have been used as dendrite inhibitors, but these have the problem of lack of stability when the number of charge/discharge cycles is large and over a long period of time. In particular, if an inexpensive porous thin film is used as the diaphragm, bromine molecules percolate and diffuse from the positive electrode chamber into the negative electrode chamber little by little, which tends to cause problems with bromine resistance to dendrite inhibitors, and it is difficult to charge and discharge many times over a long period of time. It was not possible to maintain stable performance over cycle use. Furthermore, even with bromine-resistant materials, as shown in FIG. 2, dendrites often occurred due to the formation of a non-uniform zinc oxide film on the surface of the zinc deposited on the negative electrode surface. FIG. 2 is a schematic diagram showing the mechanism by which dendrites are generated on an oxide film. FIG. 2-A shows the electrode surface at the end of charging during a short period of charging and discharging cycles, and metallic zinc Zn is deposited on the negative electrode 6. Second
- Figure 6 shows the electrode surface at the initial stage of discharge, and zinc ions Zn ++ are eluted from the surface of the electrode 6. Second
-Figure C shows the situation at the end of discharge after many charge-discharge cycles, with a non-uniform oxide film on metallic zinc Zn.
Forms ZnO. Figure 2-D shows the situation when charging is restarted after the oxide film is formed, and metal zinc is selectively deposited on the non-uniform oxide film ZnO. Figure 2-E shows the situation in the middle stage of charging, and dendrite dendrites are generated on metallic zinc selectively deposited on the oxide film. In other words, when using bromine-resistant additives,
Even if dendrites are not formed while the number of charge/discharge cycles is small, as the number of cycles increases, dendrites are formed due to the oxide film generated during discharge, and it is necessary to prevent this. An object of the present invention is to provide an electrolyte composition for preventing the generation and growth of dendrites in an electrolyte circulation type zinc-bromine secondary battery as described above. The present inventors have investigated the factors behind the formation of dendrites in electrolyte circulation type zinc-bromine secondary batteries, and based on this, the above invention has been achieved by adding certain additives to the negative electrode electrolyte. This invention was discovered by discovering that this object could be achieved. The electrolytic solution of the zinc-bromine battery of the present invention contains divalent tin ions (Sn ++ ) in a zinc bromine (ZnBr 2 ) aqueous solution containing bromine and zinc as active materials, and also contains methyl, ethyl, and morpholinium. - An electrolytic solution characterized by containing 0.5 mol/bromide and methyl ethyl pyrrolidinium bromide each. Divalent tin ions contained in the electrolytic solution prevent the formation of a zinc oxide film formed during discharge, and suppress the generation of dendrites due to the formation. Furthermore, bromine complexing agents consisting of specific heterocyclic quaternary ammonium salts, namely methyl ethyl morpholinium and methyl ethyl pyrodinium bromide, which are contained in a specific amount in the electrolyte together with divalent tin ions, It works to capture bromine (generated in the positive electrode chamber during charging) diffused into the negative electrode chamber through the diaphragm (for example, a porous membrane) and to suppress the generation of dendrites. That is, in the present invention, the generation and growth of dendrites are prevented by using divalent tin ions and bromine-resistant bromine complexing agents methyl ethyl morpholinium and methyl ethyl pyrrolidinium bromide. There is. The negative electrode electrolyte composition of the zinc-bromine secondary battery is based on zinc bromide (ZnBr 2 ), to which various divalent tin ions (Sn ++ ) are added, and
Those with various added amounts of valent tin ions (Sn ++ ), and A bromine complex forming agent with a large dendrite suppressing effect, methyl, ethyl, morpholinium,
【式】およびブロマイド
B メチル、エチル、ピロジニウム、
[Formula] and bromide B methyl, ethyl, pyrodinium,
【式】ブロマイド
を夫々0.5モル/、添加した負極電解液を調整
し、これらの電解液を用い充電、ならびに充放電
試験を行ない、更にサイクル試験を行ない電極状
況の評価をした結果、Sn++のみを負極電解液に
添加した場合、充放電、サイクル数の少い初期充
電時のデンドライト発生を抑制する点については
Sn++濃度1×10-5モル/〜5×10-4モル/
(ほぼ飽和量)においてある程度の効果があるが、
5×10-6モル/では効果がなかつた。更に5×
10-6モル/〜1×10-5モル/のSn++添加と、
前述のメチル、エチル、モルホリニウム、ブロマ
イド及びメチル、エチル、ピロリジニウム、ブロ
マイドの錯体形成剤を夫々0.5モル宛一定量混合
した場合は、夫々Sn++イオンまたは錯体形成剤
単独の場合に比べて効果がみられた。更にSn++
イオンとメチル、エチル、モルホリニウム、ブロ
マイドを1モル、またはSn++イオンとメチル、
エチル、ピロリジニウム、ブロマイドを1モル加
えた負極電解液でも上記と同様かまたは多少劣る
結果が得られた。次に充電−放電−充電のサイク
ル試験を行なつた結果、錯体形成剤のみを添加し
た負極電解液を用いた電極状況に比して、5×
10-6モル/〜5×10-4モル/のSn++および
夫々0.5モル/を混合した錯体形成剤を加えた
負極電解液を用いた電極状況は格段と良好であ
り、また、初回充電時の電着状況を次回以降の充
電時も維持し得て、錫の2価イオンが効果がある
ことを示した。またその添加量は1×10-5モル/
〜飽和量が望ましく、Sn++としてはSnCl2、
SnBr2、SnSO4などを用いることが出来る。
また前述のA、B錯体形成剤夫々を0.5モル/
およびSn++濃度1×10-5モル/〜飽和量を
添加した電解液を用いて充放電(6時間)サイク
ルを20サイクル重ねても初期と同様の電着状況を
示し、2価の錫イオンと臭化錯化剤であるメチ
ル、エチル、モルホリニウム、及びメチル、エチ
ル、ピロリジニウム、ブロマイドを添加すること
の効果が立証された。
次に本発明の実施例を以下に述べる。
実施例 1
第1図に示す如き液循環型亜鉛−臭素二次電池
を用い負極電解液として臭化亜鉛3モル/をベ
ースとして酸化抑止剤としてSn++を5×10-6モ
ル/から5×10-4モル/と変え、これにデン
ドライト抑制効果の大きい臭素錯体形成剤とし
て、メチル、エチル、モルホリニウム、ブロマイ
ド、およびメチル、エチル、ピロジニウム、ブロ
マイドを所定量(夫々0.5モル/宛)を配合調
製したものを用い、電流密度40mA/cm2で6時間
充電しカーボンプラスチツク電極に亜鉛を電着さ
せ、その電着面の状況により次の基準により評価
を行なつた。
評価基準A:優れている平滑面をもつ。B:少
量の凹凸あり、C:デンドライトが多量ある。な
おAおよびBは実用出来Aが最適である。
この結果を第1表に示す。[Formula] We prepared a negative electrode electrolyte containing 0.5 mole of each bromide, performed charging and charge/discharge tests using these electrolytes, and then performed a cycle test to evaluate the electrode condition. As a result, Sn ++ Regarding the point of suppressing the generation of dendrites during initial charging with a small number of charging/discharging cycles when only 100% is added to the negative electrolyte,
Sn ++ concentration 1×10 -5 mol/~5×10 -4 mol/
Although it has some effect at (nearly saturation amount),
There was no effect at 5×10 -6 mol/. 5 more
Addition of Sn ++ of 10 -6 mol/~1×10 -5 mol/,
When the above-mentioned methyl, ethyl, morpholinium, bromide and methyl, ethyl, pyrrolidinium, bromide complex forming agents are mixed in a fixed amount of 0.5 mol each, they are more effective than when Sn ++ ion or the complex forming agent is used alone. It was seen. Furthermore, Sn ++
ion and methyl, ethyl, morpholinium, 1 mole of bromide, or Sn ++ ion and methyl,
A negative electrode electrolyte solution containing 1 mole of ethyl, pyrrolidinium, and bromide also gave similar or slightly inferior results to those described above. Next, we performed a charge-discharge-charge cycle test and found that compared to the electrode situation using a negative electrode electrolyte containing only a complexing agent, the
The electrode condition using a negative electrode electrolyte containing a complex forming agent mixed with 10 -6 mol/~5×10 -4 mol/Sn ++ and 0.5 mol/each was much better, and the initial charge The current electrodeposition condition could be maintained during subsequent charging, demonstrating that divalent tin ions are effective. The amount added is 1×10 -5 mol/
~ Saturation amount is desirable, SnCl 2 as Sn ++ ,
SnBr 2 , SnSO 4 , etc. can be used. In addition, each of the above-mentioned A and B complex forming agents was added at 0.5 mol/
Even after repeating 20 charge/discharge cycles (6 hours) using an electrolytic solution with a Sn ++ concentration of 1 × 10 -5 mol/~saturation amount, the same electrodeposition situation as in the initial stage was observed, indicating that divalent tin The effectiveness of adding the ion and bromide complexing agents methyl, ethyl, morpholinium, and methyl, ethyl, pyrrolidinium, bromide was demonstrated. Next, examples of the present invention will be described below. Example 1 A liquid circulating zinc-bromine secondary battery as shown in Fig. 1 was used, and the negative electrode electrolyte was based on 3 mol of zinc bromide and 5 x 10 -6 mol/ to 5 of Sn ++ as an oxidation inhibitor. ×10 -4 mol/, and add methyl, ethyl, morpholinium, bromide, and predetermined amounts (0.5 mol/each) of methyl, ethyl, morpholinium, and bromide as bromine complex forming agents with a large dendrite suppressing effect. Using the prepared material, it was charged at a current density of 40 mA/cm 2 for 6 hours to electrodeposit zinc on a carbon plastic electrode, and the condition of the electrodeposited surface was evaluated according to the following criteria. Evaluation Criteria A: Excellent smooth surface. B: A small amount of unevenness is present, C: A large amount of dendrites are present. Note that for A and B, A is optimal for practical use. The results are shown in Table 1.
【表】
3−1、2は比較例
上表に示すようにSn++のみではデンドライト
の抑制の点からはそれほど効果が期待できない、
なお少量即ち5×10-6モル/(実験番号1−
5)の添加では比較例(実験番号3−1)と同じ
ようにデンドライトが大量発生する結果となつて
いる。
実施例 2
実施例1に引続きさらに同じ組成の電解液を用
い40mA/cm2の電流密度で3時間初回充電の後、
2時間放電し、その後2時間充電するという放充
電の3サイクル試験を行ない、電着面の状況を観
察し評価基準により評価を行なつた。
第2表にこの結果を示す。[Table] 3-1 and 2 are comparative examples. As shown in the table above, Sn ++ alone cannot be expected to be very effective in suppressing dendrites.
In addition, a small amount, that is, 5 × 10 -6 mol/(Experiment number 1-
The addition of 5) resulted in the generation of a large amount of dendrites as in the comparative example (experiment number 3-1). Example 2 Continuing from Example 1, after initial charging for 3 hours at a current density of 40 mA/cm 2 using an electrolytic solution with the same composition,
A 3-cycle test of discharging and charging, in which the battery was discharged for 2 hours and then charged for 2 hours, was conducted, and the condition of the electrodeposited surface was observed and evaluated based on evaluation criteria. Table 2 shows the results.
【表】
上表に示す如く錯体形成剤A、Bを夫々0.5モ
ル/を添加し更にSn++濃度1×10-5〜5×10-4
モル/を添加した臭化亜鉛電解液を用いると初
回の電着状態を維持させる能力をSn++が有して
いることが判る。
実施例 3
実施例2でAおよびB評価を得た電解液組成
(実験番号1−1c〜4cと2−1c〜4c)にて、電流
密度30mA/cm2で6時間充電その後6時間放電の
サイクルテストを行なつた結果上記組成のもの
は、20サイクルを経過した後も初期と同様の電着
面を保持した。
本発明においては、亜鉛−臭素電池の電解液中
に2価の錫イオンと臭素錯化剤であるメチル・エ
チル・モルホリニウム及びメチル・エチル・ピロ
リジニウム・ブロマイドを含有させたことによつ
て、放電時に負極において亜鉛の酸化皮膜が形成
されるのを防止し、亜鉛−臭素電池におけるデン
ドライトの発生成長をほぼ完全に防止することが
できる。
本発明の電解液を用いれば、充放電サイクルを
多数重ねる場合でも、デンドライトの発生成長を
抑止することができるので、電解液循環型亜鉛−
臭素二次電池の充放電寿命を延長せしめることが
できる。[Table] As shown in the above table, 0.5 mol/each of complex forming agents A and B were added, and further Sn ++ concentration was 1×10 -5 to 5×10 -4
It can be seen that Sn ++ has the ability to maintain the initial electrodeposition state when using a zinc bromide electrolyte containing mol. Example 3 Using the electrolyte compositions that obtained A and B ratings in Example 2 (experiment numbers 1-1c to 4c and 2-1c to 4c), the batteries were charged for 6 hours at a current density of 30 mA/cm 2 and then discharged for 6 hours. As a result of a cycle test, the electrodeposited surface with the above composition maintained the same electrodeposited surface even after 20 cycles. In the present invention, by containing divalent tin ions and bromine complexing agents methyl ethyl morpholinium and methyl ethyl pyrrolidinium bromide in the electrolyte solution of the zinc-bromine battery, during discharge, It is possible to prevent the formation of a zinc oxide film on the negative electrode, and almost completely prevent the generation and growth of dendrites in zinc-bromine batteries. By using the electrolyte of the present invention, it is possible to suppress the generation and growth of dendrites even when repeated charge/discharge cycles.
The charge/discharge life of a bromine secondary battery can be extended.
第1図は電解液循環型の亜鉛−臭素二次電池の
基本構成を示す模式図、第2図は酸化皮膜の上に
デンドライトが発生する機構を示す模式図であ
る。
1:単一セル、2:正極室、3:負極室、4:
隔膜、5:正極、6:負極、7:正極電解液、
8:負極電解液、9:正極液貯槽、10:負極液
貯槽、11,12:ポンプ、Zn:析出亜鉛、
ZnO:酸化皮膜、ZnD:デンドライト。
FIG. 1 is a schematic diagram showing the basic structure of an electrolyte circulation type zinc-bromine secondary battery, and FIG. 2 is a schematic diagram showing the mechanism by which dendrites are generated on an oxide film. 1: Single cell, 2: Positive electrode chamber, 3: Negative electrode chamber, 4:
Diaphragm, 5: positive electrode, 6: negative electrode, 7: positive electrode electrolyte,
8: negative electrode electrolyte, 9: positive electrode liquid storage tank, 10: negative electrode liquid storage tank, 11, 12: pump, Zn: precipitated zinc,
ZnO: oxide film, ZnD: dendrite.
Claims (1)
される電解液において、2価の錫イオンを含有す
るとともに、メチル・エチル・モルホリニウム・
ブロマイド及びメチル・エチル・ピロリジニウ
ム・ブロマイドをそれぞれ0.5mol/含有した
ことを特徴とする亜鉛−臭素電池の電解液。1 The electrolyte circulated to the negative electrode side of a circulating electrolyte zinc-bromine battery contains divalent tin ions and contains methyl, ethyl, morpholinium,
An electrolytic solution for a zinc-bromine battery, characterized in that it contains 0.5 mol/each of bromide and methyl ethyl pyrrolidinium bromide.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57190713A JPS5981875A (en) | 1982-11-01 | 1982-11-01 | Electrolyte for zinc-bromine battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57190713A JPS5981875A (en) | 1982-11-01 | 1982-11-01 | Electrolyte for zinc-bromine battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5981875A JPS5981875A (en) | 1984-05-11 |
| JPH024990B2 true JPH024990B2 (en) | 1990-01-31 |
Family
ID=16262586
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57190713A Granted JPS5981875A (en) | 1982-11-01 | 1982-11-01 | Electrolyte for zinc-bromine battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5981875A (en) |
-
1982
- 1982-11-01 JP JP57190713A patent/JPS5981875A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5981875A (en) | 1984-05-11 |
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