JPH0927341A - Electrolyte for alkaline zinc storage battery and alkaline zinc storage battery - Google Patents
Electrolyte for alkaline zinc storage battery and alkaline zinc storage batteryInfo
- Publication number
- JPH0927341A JPH0927341A JP7177432A JP17743295A JPH0927341A JP H0927341 A JPH0927341 A JP H0927341A JP 7177432 A JP7177432 A JP 7177432A JP 17743295 A JP17743295 A JP 17743295A JP H0927341 A JPH0927341 A JP H0927341A
- Authority
- JP
- Japan
- Prior art keywords
- zinc
- storage battery
- alkaline
- alkaline zinc
- electrolytic solution
- 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.)
- Withdrawn
Links
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 229910052725 zinc Inorganic materials 0.000 title claims abstract description 63
- 239000011701 zinc Substances 0.000 title claims abstract description 63
- 239000003792 electrolyte Substances 0.000 title abstract description 8
- NROKBHXJSPEDAR-UHFFFAOYSA-M potassium fluoride Chemical compound [F-].[K+] NROKBHXJSPEDAR-UHFFFAOYSA-M 0.000 claims abstract description 15
- 229910001515 alkali metal fluoride Inorganic materials 0.000 claims abstract description 8
- 239000011698 potassium fluoride Substances 0.000 claims abstract description 6
- 235000003270 potassium fluoride Nutrition 0.000 claims abstract description 6
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims abstract description 5
- 239000012670 alkaline solution Substances 0.000 claims abstract description 5
- 239000008151 electrolyte solution Substances 0.000 claims description 35
- 239000007864 aqueous solution Substances 0.000 claims description 11
- 238000005192 partition Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 2
- 238000010828 elution Methods 0.000 abstract description 4
- 239000000243 solution Substances 0.000 abstract description 4
- 210000001787 dendrite Anatomy 0.000 abstract description 3
- 238000007599 discharging Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract 1
- 230000000979 retarding effect Effects 0.000 abstract 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 33
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 27
- 229910052759 nickel Inorganic materials 0.000 description 13
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 11
- 230000000052 comparative effect Effects 0.000 description 8
- -1 zincate ions Chemical class 0.000 description 6
- 239000011787 zinc oxide Substances 0.000 description 5
- QELJHCBNGDEXLD-UHFFFAOYSA-N nickel zinc Chemical class [Ni].[Zn] QELJHCBNGDEXLD-UHFFFAOYSA-N 0.000 description 4
- 229940021013 electrolyte solution Drugs 0.000 description 3
- 239000012212 insulator Substances 0.000 description 3
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 2
- 239000007773 negative electrode material Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 239000007774 positive electrode material Substances 0.000 description 2
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000003411 electrode reaction Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910000474 mercury oxide Inorganic materials 0.000 description 1
- UKWHYYKOEPRTIC-UHFFFAOYSA-N mercury(ii) oxide Chemical compound [Hg]=O UKWHYYKOEPRTIC-UHFFFAOYSA-N 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229910001923 silver oxide Inorganic materials 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
Classifications
-
- 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
Landscapes
- Secondary Cells (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は,アルカリ亜鉛蓄電
池及びそれに用いる電解液に関し,詳しくは,負極活物
質として亜鉛,正極活物質として水酸化ニッケル,酸化
銀,二酸化マンガン等を用い,電解液としてアルカリ溶
液を用いるアルカリ亜鉛蓄電池とそれに用いる電解液に
関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an alkaline zinc storage battery and an electrolytic solution used for the same, and more specifically, it uses zinc as a negative electrode active material, nickel hydroxide, silver oxide, manganese dioxide as a positive electrode active material, and the like as an electrolytic solution. The present invention relates to an alkaline zinc storage battery using an alkaline solution and an electrolytic solution used therefor.
【0002】[0002]
【従来の技術】近年,携帯機器の小型軽量化が進む中
で,高エネルギー密度蓄電池の需要が増々高まってい
る。このような蓄電池の負極活物質としての亜鉛は,単
位重量当りのエネルギー密度や出力密度が高く,安価で
安全性が優れているという利点がある。2. Description of the Related Art In recent years, the demand for high energy density storage batteries has been increasing as mobile devices have become smaller and lighter. Zinc as the negative electrode active material of such a storage battery has the advantages of high energy density and output density per unit weight, low cost, and excellent safety.
【0003】[0003]
【発明が解決しようとする課題】しかしながら,亜鉛は
充放電の繰り返しに伴う劣化が早いために,サイクル寿
命が短いという欠点がある。これは亜鉛の放電生成物で
ある亜鉛酸イオンが電解液である濃いアルカリ金属水酸
化物の水溶液に溶解し易い性質を有することに起因す
る。このため蓄電池の放電時において,負極では亜鉛の
溶出が起こり易いが,充電時の亜鉛析出の際に元の形状
が復元されず,亜鉛極の多孔性は徐々に失われ,亜鉛の
利用効率が著しく低下する。また充電時に亜鉛酸イオン
が亜鉛に還元される際,析出する亜鉛がデンドライト成
長して正負極間でショートが起こるという問題もある。However, zinc has a drawback that its cycle life is short because it deteriorates rapidly with repeated charging and discharging. This is because zincate, which is a discharge product of zinc, has a property of being easily dissolved in an aqueous solution of a concentrated alkali metal hydroxide which is an electrolytic solution. Therefore, when the storage battery is discharged, zinc is likely to be eluted at the negative electrode, but the original shape is not restored during zinc deposition during charging, the porosity of the zinc electrode is gradually lost, and zinc utilization efficiency is reduced. Markedly reduced. Another problem is that when zincate ions are reduced to zinc during charging, the deposited zinc grows as dendrites, causing a short circuit between the positive and negative electrodes.
【0004】従って,亜鉛の溶出を抑えるため電解液の
量を極力少なくしたり,種々の金属や金属酸化物を亜鉛
極や電解液中に添加して電極反応を制御しようという試
みがなされているが十分な成果は上げていない。Therefore, attempts have been made to reduce the amount of the electrolytic solution as much as possible in order to suppress the elution of zinc and to control the electrode reaction by adding various metals and metal oxides to the zinc electrode and the electrolytic solution. Has not achieved sufficient results.
【0005】そこで,本発明の技術的課題は,放電時の
亜鉛の溶出を抑えることにより,電極形状の変化やデン
ドライト成長の問題のない,サイクル寿命の長いアルカ
リ亜鉛蓄電池とそれに用いる電解液とを提供することに
ある。Therefore, a technical problem of the present invention is to provide an alkaline zinc storage battery having a long cycle life and an electrolytic solution used therefor, which is free from the problem of electrode shape change and dendrite growth by suppressing the elution of zinc during discharge. To provide.
【0006】[0006]
【課題を解決するための手段】本発明は,前記課題を解
決すべくなされたものであり,従来の電解液であるアル
カリ金属水酸化物水溶液に代わって,アルカリ金属フッ
化物水溶液,例えば,フッ化カリウム(KF)水溶液を
用いることにより,亜鉛の充放電サイクル特性に優れた
蓄電池を提供するものである。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and instead of an aqueous solution of an alkali metal hydroxide, which is a conventional electrolytic solution, an aqueous solution of an alkali metal fluoride, such as a fluorine solution, is used. A storage battery having excellent charge-discharge cycle characteristics of zinc is provided by using an aqueous solution of potassium fluoride (KF).
【0007】すなわち本発明によれば,アルカリ金属フ
ッ化物を含有する水溶液であることを特徴とするアルカ
リ亜鉛蓄電池用電解液が得られる。That is, according to the present invention, there is obtained an electrolytic solution for an alkaline zinc storage battery, which is an aqueous solution containing an alkali metal fluoride.
【0008】また,本発明によれば,前記電解液におい
て,前記アルカリ金属フッ化物はフッ化カリウムである
ことを特徴とするアルカリ亜鉛蓄電池用電解液が得られ
る。Further, according to the present invention, in the electrolytic solution, there is obtained an electrolytic solution for an alkaline zinc storage battery, wherein the alkali metal fluoride is potassium fluoride.
【0009】また,本発明によれば,前記電解液にアル
カリ金属水酸化物を添加することを特徴とするアルカリ
亜鉛蓄電池用電解液が得られる。Further, according to the present invention, there is obtained an electrolytic solution for an alkaline zinc storage battery, which is characterized in that an alkaline metal hydroxide is added to the electrolytic solution.
【0010】さらに,本発明によれば,亜鉛を含む亜鉛
負極と,アルカリ溶液中で亜鉛よりも貴な電極電位を有
する物質からなる正極とを隔壁部を介して対向させて,
前記亜鉛負極,前記正極,及び前記隔壁部を前記アルカ
リ亜鉛蓄電池用電解液を介して電気的に接触させたこと
を特徴とするアルカリ亜鉛蓄電池が得られる。Further, according to the present invention, a zinc negative electrode containing zinc and a positive electrode made of a substance having an electrode potential nobler than zinc in an alkaline solution are opposed to each other via a partition wall,
An alkaline zinc storage battery is obtained in which the zinc negative electrode, the positive electrode, and the partition wall are electrically contacted via the electrolytic solution for the alkaline zinc storage battery.
【0011】[0011]
【作用】本発明においては,アルカリ金属フッ化物,例
えば,フッ化カリウムの水溶液を電解液として用いるこ
とにより,亜鉛の放電生成物はアルカリ溶液に可溶な亜
鉛酸イオンではなく,不溶性の水酸化亜鉛,酸化亜鉛あ
るいはフッ素を含む化合物になる。従って電極形態の変
化はなくなり,亜鉛のサイクル寿命は向上すると考えら
れる。In the present invention, by using an aqueous solution of an alkali metal fluoride such as potassium fluoride as the electrolytic solution, the zinc discharge product is not a zincate ion soluble in the alkaline solution but an insoluble hydroxide. It becomes a compound containing zinc, zinc oxide or fluorine. Therefore, it is considered that the electrode morphology does not change and the cycle life of zinc is improved.
【0012】また本発明においては,フッ化カリウムの
みでは正極の利用効率が低いため,アルカリ金属水酸化
物,例えば,水酸化カリウムを1から10g/1添加し
た。水酸化カリウムの添加量が多いほど,可溶な亜鉛酸
イオンの生成量が多くなるので,水酸化カリウムはニッ
ケルの利用効率を低下させないための必要最低限の量を
用いるのが望ましい。Further, in the present invention, since the utilization efficiency of the positive electrode is low only with potassium fluoride, an alkali metal hydroxide such as potassium hydroxide is added in an amount of 1 to 10 g / 1. As the amount of potassium hydroxide added increases, the amount of soluble zincate ions produced increases. Therefore, it is desirable to use the minimum amount of potassium hydroxide necessary for not lowering the utilization efficiency of nickel.
【0013】[0013]
【発明の実施の形態】以下,本発明の実施の形態につい
て説明する。Embodiments of the present invention will be described below.
【0014】図1は本発明の実施の一形態におけるニッ
ケル亜鉛蓄電池の概略的な構成を示す断面図である。図
1を参照して,ニッケル亜鉛蓄電池10は亜鉛負極1と
正極をなす焼結式ニッケル極2とを,セパレーター3を
介して対向させ容器状の負極端子4内に挿入して,焼結
式ニッケル極2側に正極端子5を設けて,負極端子4の
内壁と焼結式ニッケル極2との間に絶縁体6を設けて構
成されている。FIG. 1 is a sectional view showing a schematic structure of a nickel-zinc storage battery according to an embodiment of the present invention. Referring to FIG. 1, a nickel-zinc storage battery 10 includes a zinc negative electrode 1 and a sintered nickel electrode 2 forming a positive electrode, which are opposed to each other through a separator 3 and inserted into a negative electrode terminal 4 in a container shape. A positive electrode terminal 5 is provided on the nickel electrode 2 side, and an insulator 6 is provided between the inner wall of the negative electrode terminal 4 and the sintered nickel electrode 2.
【0015】本発明の実施の一形態による亜鉛蓄電池の
電解液として,フッ化カリウム(KF)水溶液に水酸化
カリウム(KOH)添加した溶液を用いた。これらの電
解液に対する酸化亜鉛の溶解度を調査した結果,酸化亜
鉛は,ほとんど溶解しないことが判明した。また,サイ
クル特性も良好で,水酸化カリウム濃度が低いほど,サ
イクル特性は,良好であった。さらに,水酸化カリウム
濃度が高いほど,焼結式ニッケル極の利用効率は高い。As the electrolytic solution of the zinc storage battery according to the embodiment of the present invention, a solution obtained by adding potassium hydroxide (KOH) to an aqueous solution of potassium fluoride (KF) was used. As a result of investigating the solubility of zinc oxide in these electrolytes, it was found that zinc oxide was hardly dissolved. The cycle characteristics were also good, and the lower the potassium hydroxide concentration, the better the cycle characteristics. Furthermore, the higher the potassium hydroxide concentration, the higher the utilization efficiency of the sintered nickel electrode.
【0016】[0016]
【実施例】以下,本発明の実施例について説明する。Embodiments of the present invention will be described below.
【0017】図1に示すものと同様の構成のニッケル亜
鉛蓄電池を構成した。ここで,亜鉛負極1は,酸化亜鉛
粉末90重量%,酸化水銀粉末5重量%,結着剤として
ポリテトラフルオロエチレン分散液5重量%の混合粉末
を水で希釈して混練したのちシート状にしたものを銅か
らなる集電体の両面に圧着して作製した。また,焼結式
ニッケル極2は,公知の基板用ニッケルグリッドの上
に,ニッケル粉末を焼結し,正極活物質を含浸したもの
を用いた。また,セパレーター3は,ポリプロピレンか
らなる耐アルカリ性多孔板を用いた。電解液は正負極
1,2とセパレーター3にそれぞれ含浸させて用いられ
ている。また,絶縁体6として,ポリテトラフルオロエ
チレンを用いた。A nickel-zinc storage battery having the same structure as that shown in FIG. 1 was constructed. Here, the zinc negative electrode 1 was formed into a sheet after diluting a mixed powder of 90% by weight of zinc oxide powder, 5% by weight of mercury oxide powder and 5% by weight of polytetrafluoroethylene dispersion liquid as a binder with water and kneading. The obtained product was pressed onto both sides of a current collector made of copper. As the sintered nickel electrode 2, a known nickel grid for a substrate was used, in which nickel powder was sintered and impregnated with a positive electrode active material. As the separator 3, an alkali resistant porous plate made of polypropylene was used. The electrolytic solution is used by impregnating the positive and negative electrodes 1 and 2 and the separator 3 respectively. Moreover, polytetrafluoroethylene was used as the insulator 6.
【0018】次に,本発明の実施例に係るニッケル亜鉛
蓄電池の電解液として,下記表1に示すように350g
/1フッ化カリウム(KF)水溶液に水酸化カリウム
(KOH)を0から10g/1添加した溶液(試料N
o.1〜5)を用いた。なお,比較例として400g/
1水酸化カリウム水溶液を電解液(試料No.6)とし
て用いた。Next, as an electrolytic solution for a nickel-zinc storage battery according to an embodiment of the present invention, as shown in Table 1 below, 350 g was used.
Solution of potassium hydroxide (KOH) added to an aqueous solution of potassium fluoride (KF) in an amount of 0 to 10 g / 1 (Sample N
o. 1 to 5) were used. As a comparative example, 400 g /
An aqueous solution of potassium monohydroxide was used as an electrolytic solution (Sample No. 6).
【0019】[0019]
【表1】 [Table 1]
【0020】上記表1に示すように,これらの電解液に
対する酸化亜鉛の溶解度は,比較例の試料No.6の場
合,加熱によって30g/1の溶解がみられたのに対し
て,実施例の試料No.1の場合はほとんど溶解しなか
った。As shown in Table 1 above, the solubility of zinc oxide in these electrolytes was determined by the comparative sample No. In the case of Sample No. 6, dissolution of 30 g / 1 was observed by heating, whereas Sample No. In the case of 1, it hardly dissolved.
【0021】これらの電解液の特性を確かめるために,
金属亜鉛を作用極とし,対極に白金を用いて実施例の試
料1と比較例の試料No.6の電解液中で各々定電流酸
化を行ったところ,実施例1の電解液中では亜鉛極の重
量が増えたのに対し,比較例1の電解液中では,通電量
から計算される分だけ亜鉛の酸化溶解反応が起こってい
た。In order to confirm the characteristics of these electrolytic solutions,
Using metallic zinc as the working electrode and platinum as the counter electrode, the sample No. 1 of the example and the sample no. When constant current oxidation was performed in each of the electrolyte solutions of Example 6, the weight of the zinc electrode increased in the electrolyte solution of Example 1, while in the electrolyte solution of Comparative Example 1, the amount calculated from the energization amount. Only the oxidative dissolution reaction of zinc was occurring.
【0022】図2は電解液の試料No.1〜6を用い
て,図1の電池を構成したときのサイクル特性の比較図
である。サイクル条件は100mAで4時間充電したの
ち,終止電圧1.2Vまで150mAで放電するもので
ある。FIG. 2 shows the sample No. of the electrolytic solution. It is a comparison figure of the cycle characteristic when the battery of FIG. 1 is comprised using 1-6. The cycle condition is that the battery is charged at 100 mA for 4 hours and then discharged at a final voltage of 1.2 V at 150 mA.
【0023】図2から明らかなように,本発明の実施例
に係る電解液の試料No.1〜5を用いることにより,
比較例の試料No.6に対しサイクル特性が著しく改善
されており,水酸化カリウムの濃度が低いほどサイクル
特性は良いことがわかる。As is apparent from FIG. 2, the sample No. of the electrolytic solution according to the embodiment of the present invention was used. By using 1-5,
Sample No. of Comparative Example 6 that the cycle characteristics are remarkably improved, and it is understood that the cycle characteristics are better as the concentration of potassium hydroxide is lower.
【0024】図3は本発明の実施例に係わる電解液試料
No.1〜5を用いたときの水酸化カリウムの濃度に対
する正極の焼結式ニッケル極の利用効率の変化図であ
る。図3に示すように,水酸化カリウムの濃度が高いほ
ど,ニッケルの利用効率は高いことがわかり,利用効率
の低下を防ぐためには,ある程度水酸化カリウムを添加
することが望ましいことがわかる。なお,比較例1の電
解液のニッケルの利用効率は100%であった。しか
し,比較例1においては,KOH濃度が高く,酸化亜鉛
の溶解度が大きく適当ではない。FIG. 3 shows the electrolyte sample No. 1 according to the embodiment of the present invention. It is a change figure of the utilization efficiency of the sintering type nickel electrode of a positive electrode with respect to the density | concentration of potassium hydroxide when 1-5 is used. As shown in FIG. 3, it can be seen that the higher the concentration of potassium hydroxide, the higher the utilization efficiency of nickel, and that it is desirable to add potassium hydroxide to some extent in order to prevent the reduction in utilization efficiency. The use efficiency of nickel in the electrolytic solution of Comparative Example 1 was 100%. However, in Comparative Example 1, the KOH concentration is high and the solubility of zinc oxide is large, which is not suitable.
【0025】[0025]
【発明の効果】以上,述べたように,本発明では,亜鉛
の溶出を抑えるアルカリ金属フッ化物,例えば,フッ化
カリウムを含むアルカリ水溶液を電解液としてアルカリ
亜鉛電池に用いることにより,サイクル特性に優れたア
ルカリ亜鉛蓄電池とそれに用いる電解液とを提供するこ
とができる。As described above, according to the present invention, by using an alkali metal fluoride that suppresses elution of zinc, for example, an alkaline aqueous solution containing potassium fluoride as an electrolytic solution in an alkaline zinc battery, cycle characteristics are improved. It is possible to provide an excellent alkaline zinc storage battery and an electrolytic solution used therein.
【図1】本発明の実施の一形態による電解液を用いたア
ルカリ亜鉛蓄電池の断面図である。FIG. 1 is a cross-sectional view of an alkaline zinc storage battery using an electrolytic solution according to an embodiment of the present invention.
【図2】本発明の実施例による電解液を用いたアルカリ
亜鉛蓄電池と比較例のサイクル特性図である。FIG. 2 is a cycle characteristic diagram of an alkaline zinc storage battery using an electrolytic solution according to an example of the present invention and a comparative example.
【図3】本発明の実施例によるアルカリ亜鉛蓄電池のニ
ッケル正極の利用効率を示す図である。併せて,比較例
電解液のニッケル正極の利用効率を示している。FIG. 3 is a diagram showing utilization efficiency of a nickel positive electrode of an alkaline zinc storage battery according to an embodiment of the present invention. In addition, the utilization efficiency of the nickel positive electrode of the comparative electrolyte is also shown.
1 亜鉛負極 2 ニッケル極 3 セパレーター 4 負極端子 5 正極端子 6 絶縁体 1 Zinc negative electrode 2 Nickel electrode 3 Separator 4 Negative electrode terminal 5 Positive electrode terminal 6 Insulator
Claims (4)
いられ,アルカリ金属フッ化物を含有する水溶液である
ことを特徴とするアルカリ亜鉛蓄電池用電解液。1. An electrolytic solution for an alkaline zinc storage battery, which is used as an electrolytic solution for an alkaline zinc storage battery and is an aqueous solution containing an alkali metal fluoride.
電解液において,前記アルカリ金属フッ化物はフッ化カ
リウムであることを特徴とするアルカリ亜鉛蓄電池用電
解液。2. The electrolytic solution for an alkaline zinc storage battery according to claim 1, wherein the alkali metal fluoride is potassium fluoride.
電解液において,更にアルカリ金属水酸化物を含有する
ことを特徴とするアルカリ亜鉛蓄電池用電解液。3. The electrolyte solution for an alkaline zinc storage battery according to claim 1, further comprising an alkali metal hydroxide.
中で亜鉛よりも貴な電極電位を有する物質からなる正極
とを隔壁部を介して対向させて,前記亜鉛負極,前記正
極,及び前記隔壁部を請求項1乃至3のうちのいずれか
に記載のアルカリ亜鉛蓄電池用電解液を介して電気的に
接触させたことを特徴とするアルカリ亜鉛蓄電池。4. A zinc negative electrode containing zinc and a positive electrode made of a substance having an electrode potential nobler than zinc in an alkaline solution are opposed to each other via a partition wall portion to form the zinc negative electrode, the positive electrode, and the partition wall. An alkaline zinc storage battery, characterized in that the parts are brought into electrical contact with each other through the electrolytic solution for an alkaline zinc storage battery according to any one of claims 1 to 3.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7177432A JPH0927341A (en) | 1995-07-13 | 1995-07-13 | Electrolyte for alkaline zinc storage battery and alkaline zinc storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7177432A JPH0927341A (en) | 1995-07-13 | 1995-07-13 | Electrolyte for alkaline zinc storage battery and alkaline zinc storage battery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0927341A true JPH0927341A (en) | 1997-01-28 |
Family
ID=16030846
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7177432A Withdrawn JPH0927341A (en) | 1995-07-13 | 1995-07-13 | Electrolyte for alkaline zinc storage battery and alkaline zinc storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0927341A (en) |
-
1995
- 1995-07-13 JP JP7177432A patent/JPH0927341A/en not_active Withdrawn
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