JPS59205155A - Alkaline battery - Google Patents

Alkaline battery

Info

Publication number
JPS59205155A
JPS59205155A JP58079563A JP7956383A JPS59205155A JP S59205155 A JPS59205155 A JP S59205155A JP 58079563 A JP58079563 A JP 58079563A JP 7956383 A JP7956383 A JP 7956383A JP S59205155 A JPS59205155 A JP S59205155A
Authority
JP
Japan
Prior art keywords
zinc
mercury
current collector
negative electrode
battery
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.)
Pending
Application number
JP58079563A
Other languages
Japanese (ja)
Inventor
Ryoji Okazaki
良二 岡崎
Tomokazu Mitamura
知一 三田村
Shigeo Kobayashi
茂雄 小林
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP58079563A priority Critical patent/JPS59205155A/en
Publication of JPS59205155A publication Critical patent/JPS59205155A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Cell Electrode Carriers And Collectors (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は負極活物質VrC亜鉛、正極活物質に二酸化マ
ンガン、酸化銀、酸素、酸化水銀、水酸化ニッケルなど
各種の減極剤、電解液にアルカリ性水溶液をそれぞれ用
いる各種のアルカリ電池の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention uses VrC zinc as a negative electrode active material, manganese dioxide as a positive electrode active material, various depolarizers such as silver oxide, oxygen, mercury oxide, and nickel hydroxide, and an alkaline electrolyte as an electrolyte. The present invention relates to improvements in various alkaline batteries each using an aqueous solution.

従来例の構成とその問題点 一]二記の各神アルカリ電池の共通的な課題として、貯
蔵中の負極亜鉛の腐食による自己消耗と水素ガスの発生
とを効果的に抑止することがある。
A common problem of the conventional alkaline batteries described in [1] and [2] is to effectively suppress self-depletion due to corrosion of negative electrode zinc during storage and generation of hydrogen gas.

そのため、従来より粉体状の亜鉛を水化して加圧成型す
るか、ゲル中に分散させて、いわゆるゲル負極とし、こ
の負極と接触する負極集′屯体の少くとも表面を、氷化
され易くしかも電気化学的に責で安価な金属、例へは銅
、錫、1亘鍮から形成し、氷化により亜鉛自体の水素過
電圧を高めると共に、亜鉛から拡散して集電体の表面に
移行する水銀にまり集電体の水化を果し、集電面の水素
過電用倉高めることにより、防食する方法が一般的に採
用されている。
Therefore, conventionally powdered zinc is hydrated and pressure molded or dispersed in a gel to form a so-called gel negative electrode, and at least the surface of the negative electrode aggregate that comes into contact with this negative electrode is frozen. It is formed from metals that are easy to use and are electrochemically stable and inexpensive, such as copper, tin, and brass, and when it freezes, it increases the hydrogen overvoltage of the zinc itself, and it also diffuses from the zinc and migrates to the surface of the current collector. A commonly used method is to prevent corrosion by hydrating the current collector and increasing the hydrogen overcurrent capacity on the current collecting surface.

この場合、亜鉛と集電面との電位差により、亜鉛がアノ
ード、集電面がカノードとして作用する局部電池が形成
され、亜鉛の溶捏「と集電田]からの水素ガス発生の反
応が起こるか、集電面に「止鉛からの水銀が拡散して集
電面が氷化されると、水素過電圧が上昇し、水素発生反
応か抑制され、こf’Lに対応する亜鉛の溶解反応も必
然的に抑制されるととになル、亜鉛の腐食は事実上はぼ
満足すべき状態に抑制され、実用電池としての貯蔵性の
確保と電池膨張や漏液の促進を抑止する効果か認められ
ている。
In this case, due to the potential difference between the zinc and the current collecting surface, a local cell is formed in which the zinc acts as an anode and the current collecting surface acts as a cathode, and a reaction occurs that generates hydrogen gas from the zinc melting "and the current collecting field". Or, when the mercury from the lead stops diffuses into the current collecting surface and the current collecting surface becomes frozen, the hydrogen overvoltage increases and the hydrogen generation reaction is suppressed, causing the zinc dissolution reaction corresponding to f'L. However, if zinc corrosion is inevitably suppressed, zinc corrosion is effectively suppressed to a satisfactory state, and this has the effect of ensuring storability as a practical battery and suppressing the acceleration of battery expansion and leakage. It recognized.

しかし上記の方法の欠点として、通常亜鉛殴に対し、j
(<量比で6〜12%程度の水銀で水化する事が必要で
、水銀量が不足な場合、前記局部電池の水素過′1−シ
圧が十分に大きくできず、腐食反応を抑止できなく、貯
蔵性能の劣化、漏液、電池膨張の原因となるため、多量
の水銀を使用せざるを得ない点(/Cある。云う丑でも
なく、水銀の使用量を低減することは低公害化のための
社会的ニーズであり、コストダウンの上でも無視できな
い要素であるため、アルカリ電池中の水銀量を低減させ
る手段として、亜鉛の合金化、添加剤の検討などが行わ
れて来たか、未だ顕著な効果を期待できる方法が無いの
が現状である。
However, as a drawback of the above method, when compared to zinc punching,
(It is necessary to hydrate with about 6 to 12% mercury in terms of quantity ratio, and if the amount of mercury is insufficient, the hydrogen peroxide pressure in the local battery cannot be sufficiently increased, inhibiting the corrosion reaction. This means that a large amount of mercury must be used (/C) because it causes deterioration of storage performance, liquid leakage, and battery expansion. This is a social need due to pollution and is a factor that cannot be ignored in terms of cost reduction. Therefore, alloying of zinc and investigation of additives have been conducted as a means to reduce the amount of mercury in alkaline batteries. However, the current situation is that there is still no method that can be expected to have a significant effect.

発明の目的 公害化とコストダウンを果さんとするものである。purpose of invention The goal is to reduce pollution and reduce costs.

発明の構成 本発明(・」1、負極活物質として亜鉛 電解液にアル
カリ性水溶液を用い、負極集電体の少くとも表面が、銅
、錫、面端なと電気化学的に亜鉛より質で、アマルガム
され易い金属からなる各種のアルカリ電池において、負
極集電体の負極活物質と接する表面にカドミウムを存在
さぜたことtMj徴とするものである。カドミウムは水
素過電圧が大きく、水銀への溶解度も約4.9%と、亜
鉛の約2.2係、錫の約0.6%、銅の0.003係に
比較して極めて大きい性質を持っている。本発明は、こ
のカドミウムの性質に着目し、さらに亜鉛負極の腐食反
応は、亜鉛がアノードとして溶解し、カソードとして集
電体表面が作用して水素ガスが発生ずる局部電池反応が
支配的な要素を占めるため、亜鉛よりも集電体表面の水
銀濃度を高めて水素過電圧を犬きくすることが、亜鉛の
腐食防止の最重要課題であるとの認識のもとに、集電体
表面の水銀濃度を高め得るカドミウムを付着させたもの
である。
Composition of the Invention The present invention (・'1. Zinc as the negative electrode active material. An alkaline aqueous solution is used as the electrolyte, and at least the surface of the negative electrode current collector is electrochemically higher in quality than zinc, such as copper, tin, or surface edges. In various alkaline batteries made of metals that are easily amalgamated, tMj is characterized by the presence of cadmium on the surface of the negative electrode current collector in contact with the negative electrode active material.Cadmium has a large hydrogen overvoltage and has a low solubility in mercury. Cadmium has an extremely large property of about 4.9%, compared to about 2.2% of zinc, about 0.6% of tin, and 0.003% of copper. In addition, the corrosion reaction of zinc negative electrodes is dominated by a local battery reaction in which zinc dissolves as an anode and the surface of the current collector acts as a cathode, generating hydrogen gas. Recognizing that increasing the mercury concentration on the surface of the current collector to reduce hydrogen overvoltage is the most important issue in preventing corrosion of zinc, we decided to attach cadmium, which can increase the mercury concentration on the surface of the current collector. It is something that

この方法により亜鉛中の水銀濃度が極めて低い状態でも
十分に腐食が抑制できることを見出した。
It has been found that this method can sufficiently suppress corrosion even when the mercury concentration in zinc is extremely low.

水化亜鉛から集電体表面に水銀が拡散して移行する量は
、氷化亜鉛中の水銀含有率が大きいほど、多くなるが、
さらに本発明の作用機構を理解する上に重要なことは、
集電体表面の水銀との相溶性、ずなわち溶解度が大きい
程、集電体表面への水銀移行1i5すなわち、水銀の濃
度が犬となる点にある。従来、集電体の表面物質として
採用されている錫、銅、虹鍮なとは亜鉛に較べて水銀と
の相溶性に乏しいので、亜鉛中の水銀濃度より低濃度に
しか集電体表面の水銀濃度を維持し得す、負極亜鉛中の
水体濃度カバ5〜12wt係という高濃度の状態でない
と集市1体表面の水素過電圧を高めるに足る水Qk a
llとなし得ない。これに対し、集電体表面に水銀との
相票性が極めて大きい清ドミクムを存在させることによ
り、亜鉛中の水銀濃度よりはるかに高濃度の水銀をカド
ミウム中に含有し得るととになり、亜鉛中の水銀a度が
低い状態でも、集電体表面の水銀濃度を高めることがで
き、水素過71χ斤の−1−昇により、局部電池や作用
を事実上消極させることができる。
The amount of mercury that diffuses and transfers from zinc hydrate to the current collector surface increases as the mercury content in the zinc hydrate increases.
Furthermore, what is important in understanding the mechanism of action of the present invention is that
The higher the compatibility with mercury on the surface of the current collector, that is, the greater the solubility, the higher the mercury migration 1i5 to the surface of the current collector, that is, the higher the concentration of mercury. Conventionally, tin, copper, and brass, which have been used as surface materials for current collectors, have poor compatibility with mercury compared to zinc, so they can only be applied to the surface of current collectors at concentrations lower than the mercury concentration in zinc. Unless the water concentration in the negative electrode zinc is at a high concentration of 5 to 12 wt to maintain the mercury concentration, water Qk a is sufficient to increase the hydrogen overvoltage on the surface of the body.
I can't do it. On the other hand, by making clear domicum, which has extremely high affinity with mercury, exist on the surface of the current collector, it becomes possible to contain mercury in cadmium at a much higher concentration than that in zinc. Even when the degree of mercury in zinc is low, the mercury concentration on the surface of the current collector can be increased, and the local battery and action can be effectively made negative by increasing the hydrogen concentration by -1.

以にの説明は、氷化亜鉛から集電体表面に水銀全移行さ
せて局部作用を抑制する電池構成法を念頭において説明
したが、本発明の場合には以下に記述するように、電池
構成前に予め集電体表面を高濃度に水化し、無水化もし
くは低氷化率の一11j鉛を負極として用いる電池構成
法に適用しても効果的である。
The above explanation has been made with a battery configuration method in which all mercury is transferred from frozen zinc to the current collector surface to suppress local effects, but in the case of the present invention, the battery configuration is changed as described below. It is also effective to apply this method to a battery construction method in which the surface of the current collector is hydrated to a high concentration in advance, and 111j lead, which is anhydrous or has a low freezing rate, is used as the negative electrode.

すなわち、銅、面端、錫など水銀との相溶性か曲−鉛よ
り小さい金属のみで集電体表面が形成されている従来の
方法では、予め集電体表面を高濃度に水化しても、電池
構成後9、徐々に水銀が亜鉛仙jに移行し、集電体表面
の水銀濃度が減少するので、局部電池作用が活発化し、
亜鉛の腐食反応を抑制し得ないことになる。これに対し
、本発明で(は集電体表面のカドミウムと、亜鉛との水
銀相溶性の関係は全く逆となり、予め集電体表面を高濃
度にしておけば、これに近い状態が′電池構成後も縮性
でき、亜鉛中の水銀の濃度を極めて少なくシ/こ状態で
局部作用に基づく亜鉛の腐食反応を効果的に抑止できる
In other words, in the conventional method in which the current collector surface is formed only with metals such as copper, surface edge, and tin that are compatible with mercury or are smaller than lead, even if the current collector surface is hydrated to a high concentration in advance, , After battery construction 9, mercury gradually migrates to the zinc oxide, and the mercury concentration on the surface of the current collector decreases, so the local battery action becomes active.
This means that the corrosion reaction of zinc cannot be suppressed. In contrast, in the present invention, the relationship between mercury compatibility between cadmium on the surface of the current collector and zinc is completely opposite. Even after formation, the mercury concentration in the zinc is extremely low, and the corrosive reaction of zinc due to local action can be effectively suppressed in the sintered state.

前述のように、本発明は亜鉛中の水銀濃度の低い状態で
も集電体表面の水銀濃度を高い状態に維持して4卜鉛の
腐食反応を効果的に抑止でき、集電体表面の水銀にば、
高濃度の状態でも絶対和としてft:J:極くわつかな
ので、水銀使用量は大幅に減少させイ4Jる。
As mentioned above, the present invention can maintain the mercury concentration on the surface of the current collector in a high state even when the mercury concentration in zinc is low, effectively suppressing the corrosion reaction of 4 ml lead, and reducing the mercury concentration on the surface of the current collector. Niba,
Even at high concentrations, the absolute sum of mercury is extremely low (ft:J), so the amount of mercury used can be greatly reduced.

実施例の説明 本発明の効果を具体的に実証するためにボタン型のアル
カリマンガン電池により実験した内容について以下に記
述する。図はその実験に用いた電池の断面図である。図
中1は封口板で、Φ÷鉄を芯材としその外面1′がニッ
ケル、内面1″が面端のクラツド板からなり、内面1”
の構成は後述のよ2ば50〜100メツシユの亜鉛粉末
を後述の各4Φの比率で氷化した氷化粉末を含む亜鉛負
極で、これ―、力性カリの濃度40wt%水溶液に酸化
亜鉛′f:飽和させ、さらにカルボキシメチルセルロー
スをゲル化剤として分散させたゲル状電解液を使用して
いる。3はセルロース製の保液材、4は微多孔1η−の
ポリプロピレン製セパレータ、6は二酸化マンガンに人
造黒鉛を添加、混合して成型した正極、6はステンレス
スチール製の正極リング、7は鉄を芯材とし、外面、内
面ともニッケル7′のクラツド板からなる正極ケース、
8はポリプロピレン製ガスケットであり、正極ケース7
の開口部の折り曲げにより密封を果している。電解液は
負極2以外にも保液材3、セパレータ4、及び正極5に
含浸されており、その液組成は負極2中の電解液と同様
である。ここで、負極集電面として作用する個所は封口
板1の内面1” なので、す、下、封口板の内面の条件
と、亜鉛の水化率を種々変へて本発明の効果を検討する
ため試作した内容を第1表に示す。
DESCRIPTION OF EXAMPLES In order to specifically demonstrate the effects of the present invention, an experiment using a button-type alkaline manganese battery will be described below. The figure is a cross-sectional view of the battery used in the experiment. In the figure, 1 is a sealing plate, which has a core material of Φ÷iron, an outer surface 1' of which is nickel, and an inner surface 1" of which is a clad plate with an edge.
The composition is a zinc negative electrode containing frozen powder made by freezing 50 to 100 meshes of zinc powder at a ratio of 4Φ as described below. f: A gel electrolyte solution is used which is saturated and further has carboxymethylcellulose dispersed therein as a gelling agent. 3 is a liquid retaining material made of cellulose, 4 is a microporous 1η- polypropylene separator, 6 is a positive electrode made by adding and mixing manganese dioxide with artificial graphite, 6 is a positive electrode ring made of stainless steel, and 7 is made of iron. A positive electrode case consisting of a nickel 7' clad plate as the core material, both on the outer and inner surfaces.
8 is a polypropylene gasket, and the positive electrode case 7
Sealing is accomplished by bending the opening. In addition to the negative electrode 2, a liquid retaining material 3, a separator 4, and a positive electrode 5 are impregnated with the electrolytic solution, and the liquid composition is the same as that of the electrolytic solution in the negative electrode 2. Here, since the part that acts as the negative electrode current collecting surface is the inner surface 1'' of the sealing plate 1, the effects of the present invention will be examined by varying the conditions of the lower and inner surfaces of the sealing plate and the hydration rate of zinc. Table 1 shows the contents of the prototype.

以下余白 第1表 なお、亜鉛粉末の粒度ば50〜100メソ−/ユ、純度
は99.9係以上のものを用い、濃度約10wt係の力
性カリ溶液中に亜鉛粉末を入れ、攪拌しながら水銀を所
定量添加して水洗乾燥して氷化を行った。捷だ試作した
ボタン形電池の形状は、1t1径11.6mm、総高3
 、0腋に統一した。これらの各試作電池(a−q)に
ついて、放電性能、及び′I+i、/l!2の総高変化
、漏液の発生状況を調へた結果を第2表に示す。
Table 1 below: Use zinc powder with a particle size of 50 to 100 meso/yu and a purity of 99.9 or higher. Place the zinc powder in a potash solution with a concentration of about 10 wt and stir. While doing so, a predetermined amount of mercury was added, and the mixture was washed with water and dried to form ice. The shape of the prototype button battery is 1t1, 11.6mm in diameter, and 3 in total height.
, unified to 0 axilla. For each of these prototype batteries (a-q), the discharge performance and 'I+i,/l! Table 2 shows the results of investigating the total height change and occurrence of leakage.

以下余白 第2表に見られるように、封口板内面に無処理の真鍮を
用いた場合(a−e)には、亜鉛の水化率3wt%以下
(c、d、e)では電池の膨張、漏液とも著しく、貯蔵
中に発生した水素ガスのため、電池内の圧力が上昇した
ことを示している。
As shown in Table 2 below, when untreated brass is used for the inner surface of the sealing plate (a-e), the battery expands when the hydration rate of zinc is 3 wt% or less (c, d, e). Both the leakage and leakage were significant, indicating that the pressure inside the battery had increased due to hydrogen gas generated during storage.

はぼ完全に水素ガスの発生上抑止するには10wt係の
水化aを必要とする。5φ程度しでも実用上は大きな支
障がない程度にこれらの問題は良化するが、信頼性の点
で、今、−歩欠ける点がある。又、貯蔵後の放電性能の
劣化についても、水素ガスの発生が多い程、大きく、こ
れは、カス圧による化学的、物理的な接触不良と、亜鉛
の消耗に」=るものと考えられる。また、本発明の適用
例として、真鍮表面にカドミウムを被覆する方法(■〜
l)では、上記の貯蔵後の問題は唾鉛の水化率が6wt
%f1なら全く解消し、1〜Swt係g、hでも、カド
ミウムを被覆していない場合の5wt%bに相当する効
果が得られている。又、カドミウムを被覆しても、亜鉛
中に水銀が不足したり、含有しない場合にばi、Hには
、水素ガスの発生を抑止する効果(こ1乏しく、貯蔵性
能も劣化する。
To completely suppress the generation of hydrogen gas, 10 wt of hydration a is required. Although these problems can be solved to the extent that there is no major problem in practical use even if the diameter is about 5φ, there is still a shortcoming in terms of reliability. Furthermore, the deterioration of discharge performance after storage is greater as more hydrogen gas is generated, and this is thought to be due to poor chemical and physical contact due to gas pressure and consumption of zinc. In addition, as an application example of the present invention, a method of coating cadmium on the surface of brass (■ ~
In l), the problem after storage is that the hydration rate of salivary lead is 6wt.
%f1 completely eliminates the problem, and even with 1 to Swt ratios g and h, an effect equivalent to 5wt%b when not coated with cadmium is obtained. Further, even if cadmium is coated, if mercury is insufficient or not contained in zinc, B and H will have a poor effect in suppressing the generation of hydrogen gas, and storage performance will also deteriorate.

次Vこ、予め封口板内面を水化したのち電池構成しグζ
場合でも、封口板内面が真鍮の場合と、これにカドミウ
ム被覆したものを用いた場合とでは、効果が異り後者の
貯蔵後の緒特性は極めてずぐれており、亜鉛の氷化率、
Iwt以上n、oでは全く問題なく、0.5wt%以下
の場合p、qでも問題か少ない。
Next, after hydrating the inner surface of the sealing plate in advance, construct the battery.
However, the effects are different when the inner surface of the sealing plate is made of brass and when it is coated with cadmium, and the latter has extremely poor properties after storage.
There is no problem at all when n and o are more than Iwt, and there are few problems even when p and q are less than 0.5wt%.

これらの結果は、前述した本発明の作用効果を実i?+
I−するものである。
These results demonstrate that the effects of the present invention described above are actually realized. +
I-It is something to do.

発明の効果 以りのように、本発明は、アルカリ電解液中の亜鉛負極
の腐食金少敏の水銀の使用により効果的に抑:(ill
でき、電池の低公害化、コストダウンに極めて有効であ
る。
As described above, the present invention effectively suppresses corrosion of zinc negative electrode in alkaline electrolyte by using mercury.
This is extremely effective in reducing battery pollution and cost.

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

図に本発明の効果を実証する実験に用いたボタン形アル
カリ電池の断面図である。 1は封口板、1″ は負極集電面を兼ねた封口板内面、
2は1」l(鉛頁極、3は保液材、4はセパレータ、5
は正極、6は正極リング、7(/i、i]−極り一ス、
8はガスケット。
The figure is a sectional view of a button-shaped alkaline battery used in an experiment to demonstrate the effects of the present invention. 1 is the sealing plate, 1″ is the inner surface of the sealing plate that also serves as the negative electrode current collecting surface,
2 is 1''l (lead page electrode, 3 is liquid retaining material, 4 is separator, 5 is
is the positive electrode, 6 is the positive electrode ring, 7 (/i, i]-pole one step,
8 is a gasket.

Claims (1)

【特許請求の範囲】[Claims] 負極活物質として亜鉛、電解液としてアルカリ性水溶液
を用い、負極集電体の少なくとも負極活
Using zinc as the negative electrode active material and an alkaline aqueous solution as the electrolyte, at least the negative electrode active material of the negative electrode current collector is
JP58079563A 1983-05-06 1983-05-06 Alkaline battery Pending JPS59205155A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58079563A JPS59205155A (en) 1983-05-06 1983-05-06 Alkaline battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58079563A JPS59205155A (en) 1983-05-06 1983-05-06 Alkaline battery

Publications (1)

Publication Number Publication Date
JPS59205155A true JPS59205155A (en) 1984-11-20

Family

ID=13693473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58079563A Pending JPS59205155A (en) 1983-05-06 1983-05-06 Alkaline battery

Country Status (1)

Country Link
JP (1) JPS59205155A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10547046B2 (en) 2011-11-30 2020-01-28 Lawrence Livermore National Security, Llc High energy/power density nickel oxide/hydroxide materials and nickel cobalt oxide/hydroxide materials and production thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10547046B2 (en) 2011-11-30 2020-01-28 Lawrence Livermore National Security, Llc High energy/power density nickel oxide/hydroxide materials and nickel cobalt oxide/hydroxide materials and production thereof

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