JPH0680585B2 - Method for producing paste type cadmium negative electrode - Google Patents

Method for producing paste type cadmium negative electrode

Info

Publication number
JPH0680585B2
JPH0680585B2 JP59245065A JP24506584A JPH0680585B2 JP H0680585 B2 JPH0680585 B2 JP H0680585B2 JP 59245065 A JP59245065 A JP 59245065A JP 24506584 A JP24506584 A JP 24506584A JP H0680585 B2 JPH0680585 B2 JP H0680585B2
Authority
JP
Japan
Prior art keywords
cadmium
negative electrode
metal
powder
nickel
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
Application number
JP59245065A
Other languages
Japanese (ja)
Other versions
JPS61124057A (en
Inventor
英男 海谷
収 高橋
信吾 津田
実 山賀
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 JP59245065A priority Critical patent/JPH0680585B2/en
Publication of JPS61124057A publication Critical patent/JPS61124057A/en
Publication of JPH0680585B2 publication Critical patent/JPH0680585B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • 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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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、アルカリ蓄電池に使用するペースト式カドミ
ウム負極に関するものである。
TECHNICAL FIELD The present invention relates to a paste type cadmium negative electrode used in an alkaline storage battery.

従来の技術 一般に、アルカリ蓄電池用ペースト式カドミウム負極の
製造法は、酸化カドミウムあるいは水酸化カドミウムを
主体とするカドミウム活物質粉末,カーボニルニッケル
やブラファイト等の導電性粉末,ポリビニルアルコール
やカルボキシメチルセルロース等の結着剤と水やユチレ
ングリコール等の溶媒を混練してペーストとしたものを
ニッケルメッキした開孔鋼板等の導電性芯体に塗着し乾
燥したものをアルカリ溶液中で化成している。化成工程
の目的は、放電状態のカドミウム化合物(酸化カドミウ
ム,水酸化カドミウム)の一物を充電状態の金属カドミ
ウムに変換し、負極内に予備充電部分を付与することに
ある。負極内に予備充電部分が存在しない場合は、負極
の利用率が正極に比べ低いために、放電が負極支配とな
り、電池の高率放電特性が悪く、また、負極が完全放電
を受けるため、電池の特性劣化が著しい。以上のような
理由で化成を行なう。
2. Description of the Related Art Generally, a method for producing a paste-type cadmium negative electrode for an alkaline storage battery includes a cadmium active material powder mainly composed of cadmium oxide or cadmium hydroxide, a conductive powder such as carbonyl nickel or braphite, polyvinyl alcohol or carboxymethyl cellulose, etc. A paste prepared by kneading a binder and a solvent such as water or utylene glycol is applied to a conductive core body such as a nickel-plated perforated steel sheet and dried, and then formed into an alkaline solution. The purpose of the chemical conversion step is to convert one of the cadmium compounds in the discharged state (cadmium oxide, cadmium hydroxide) into metallic cadmium in the charged state to provide a precharged portion in the negative electrode. When there is no pre-charged part in the negative electrode, the negative electrode utilization rate is lower than that of the positive electrode, so the discharge is dominant in the negative electrode, the high rate discharge characteristics of the battery are poor, and the negative electrode receives a complete discharge. Markedly deteriorated. The formation is performed for the above reasons.

発明が解決しようとする問題点 しかし化成工程では、負極容量の20−50%の充電を行な
うため使用する電力は膨大である。また、化成工程で、
充電状態の金属カドミウムを極板内に均一に分布させる
ことは容易でなく、極板特性のバラツキを生じやすい。
特にペースト式カドミウム負極の場合は、シンター式の
ものに比べ、その傾向が大きい。このような問題点を解
決するために、近年では、例えば特公昭57-37986号,あ
るいは特開昭58-32744号に見られるように、活性な金属
カドミウム粉末を予備充電量として活物質混合時に添加
することにより化成工程を不要とするペースト式カドミ
ウム負極板が提案されている。予備充電量として添加す
る金属カドミウム粉末は、電池充放電反応に効率よく寄
与するためには、活性度の高いもの、すなわち活物質利
用率の高いものが良好である。
Problems to be Solved by the Invention However, in the chemical conversion process, a large amount of electric power is used to charge 20-50% of the negative electrode capacity. Also, in the chemical conversion process,
It is not easy to evenly distribute the charged metal cadmium in the electrode plate, and variations in the electrode plate characteristics are likely to occur.
Particularly in the case of the paste type cadmium negative electrode, the tendency is larger than that in the sinter type. In order to solve such a problem, in recent years, for example, as shown in JP-B-57-37986 or JP-A-58-32744, an active metal cadmium powder is used as a precharge amount when an active material is mixed. A paste-type cadmium negative electrode plate has been proposed which does not require a chemical conversion step by adding. The metal cadmium powder added as a precharge amount is preferably one having a high activity, that is, one having a high utilization rate of the active material, in order to efficiently contribute to the battery charge / discharge reaction.

しかし、特公昭57-37986号で提案されているような乾式
法により製造される金属カドミウム粉末は粒形が球状の
ため、表面積が小さく、活物質利用率の低いものであ
る。また、特公昭58-32744号で提案されているように金
属ニッケル粉末を含むカドミウム塩中で、亜鉛を化学置
換させ、金属カドミウムと金属ニッケルとの混合物を使
用するものでも、カドミウムの凝集防止と導電性向上の
目的であらかじめ添加された金属ニッケル粉末は、生成
した金属カドミウムに覆われる形となり、金属カドミウ
ムの放電状態である絶縁性の水酸化カドミウムに変化し
た場合、金属ニッケルが十分に機能しなくなるなど改善
の必要があった。
However, since the metal cadmium powder produced by the dry method as proposed in Japanese Patent Publication No. 57-37986 has a spherical particle shape, it has a small surface area and a low utilization rate of the active material. In addition, even if a mixture of metal cadmium and metal nickel is used to chemically substitute zinc in a cadmium salt containing metal nickel powder as proposed in Japanese Patent Publication No. 58-32744, it is possible to prevent cadmium from aggregating. The metallic nickel powder added in advance for the purpose of improving conductivity becomes a form covered with the generated metallic cadmium, and when it changes to insulating cadmium hydroxide, which is the discharge state of metallic cadmium, metallic nickel functions sufficiently. There was a need for improvement such as disappearance.

本発明は、以上の問題点を解決し、高性能の金属カドミ
ウム粉末を製造する方法と、これを適用した、化成工程
を必要としない、高性能のペースト式カドミウム負極の
製造法を提供するものである。
The present invention solves the above problems and provides a method for producing a high-performance metal cadmium powder, and a method for producing a high-performance paste-type cadmium negative electrode to which this is applied, which does not require a chemical conversion step. Is.

問題点を解決するための手段 本発明は化成工程を必要としないペースト式カドミウム
負極に関するものであり、酸化カドミウム粉末と、予備
充電量としての金属カドミウム粉末を主体とする活物質
と、結着剤と、その溶媒を混練してなるペーストを、開
孔ニッケル板等の導電性芯体に練塗,乾燥する方法にお
いて、予備充電量としての金属カドミウム粉末が、湿式
または乾式等の一般的な手法によって製造された金属カ
ドミウム粉末をニッケルイオンを含む溶液中に浸漬し、
置換反応により、カドミウム金属の一部をニッケル金属
に変換し、カドミウム金属上に析出させたものであるこ
とを特徴とするものである。
Means for Solving the Problems The present invention relates to a paste type cadmium negative electrode that does not require a chemical conversion step, and contains cadmium oxide powder, an active material mainly composed of metal cadmium powder as a precharge amount, and a binder. In a method of kneading and drying a paste obtained by kneading the solvent with a conductive core body such as an open-hole nickel plate, the metal cadmium powder as a precharge amount is a general method such as a wet type or a dry type. Immersing the metal cadmium powder produced by in a solution containing nickel ions,
It is characterized in that a part of cadmium metal is converted into nickel metal by a substitution reaction and deposited on the cadmium metal.

作用 以下、本発明の原理を説明する。Operation The principle of the present invention will be described below.

金属カドミウム単体の利用率、あるいは金属カドミウム
と、主体となる活物質の酸化カドミウムの混合物の利用
率に影響するものには、以下のような項目がある。
There are the following items that affect the utilization rate of metallic cadmium alone or the utilization rate of a mixture of metallic cadmium and cadmium oxide as the main active material.

1 表面積 表面積は、活物質同志の接触及び電解液との接触が多い
ほうが利用率が高いため、大きいほうが望ましい。
1 Surface area The larger the surface area, the higher the contact rate between the active materials and the contact with the electrolytic solution.

2 形状 表面積が大きいこと、あるいは活物質同志のからまりに
よる接触が多く導電性が高いほうが利用率が高くなる。
従ってその形状は、球状のようなものよりも凸凹の多い
不定形が望ましい。
2 Shape The utilization rate is higher when the surface area is large or there are many contacts due to the entanglement of the active materials and the conductivity is high.
Therefore, the shape is preferably an irregular shape having more irregularities than a spherical shape.

3 導電性 金属カドミウムは、空気中の酸素、水分と反応しやす
く、その表面に酸化物、あるいは水酸化物の被膜を形成
しやすい。これらの被膜は、化学的,電気化学的に安定
であるため、このような被膜を形成した金属カドミウム
粉末を電極に使用すると、活物質間の導電性が低下し、
活物質利用率は低下する。従って、金属カドミウム粉末
は、金属ニッケル等、電池電解液中あるいは空気中で安
定な金属で被覆されているのが望ましい。
3 Conductive metal cadmium easily reacts with oxygen and moisture in the air, and easily forms an oxide or hydroxide film on the surface thereof. Since these coatings are chemically and electrochemically stable, when the metal cadmium powder having such coatings is used for the electrodes, the conductivity between the active materials is lowered,
The active material utilization rate decreases. Therefore, it is desirable that the metal cadmium powder be coated with a metal that is stable in the battery electrolyte or in the air, such as metal nickel.

本発明は以上のような項目を、金属カドミウム粉末を、
ニッケルイオンを含む溶液中に浸漬処理することによ
り、置換反応で、金属カドミウムの表面の一部に金属ニ
ッケルを析出させる方法により、満足させたものであ
る。
The present invention has the above items, metal cadmium powder,
This is satisfied by a method of precipitating metallic nickel on a part of the surface of metallic cadmium by a substitution reaction by immersion treatment in a solution containing nickel ions.

金属カドミウム粉末を硫酸ニッケル水溶液等のニッケル
塩溶液に浸漬すると、置換反応により金属カドミウムが
溶解し、ニッケル金属が析出する。この反応を適度に進
行させ、後に水洗等により反応を停止させると、金属カ
ドミウム粉末の表面層が金属ニッケルで被覆された状態
となる。
When the metal cadmium powder is immersed in a nickel salt solution such as an aqueous solution of nickel sulfate, the substitution reaction dissolves the metal cadmium and deposits nickel metal. When this reaction is allowed to proceed appropriately and then stopped by washing with water or the like, the surface layer of the metal cadmium powder is in a state of being coated with metal nickel.

金属カドミウム粉末は、溶解によりその表面が荒れた状
態となり、その上に微細な金属ニッケルが存在するた
め、表面積が非常に大きくなり、活性度の高い金属カド
ミウム活物質となる。この場合原料としての金属カドミ
ウム粉末は、湿式法により得られるものでも、また、乾
式法により得られる表面積の小さいものでもよい。湿式
法によるものを用いた場合さらに高活性度のものが得ら
れる。また粉末としては取り扱いやすいが活性度の低い
乾式法によるものを用いても、十分に活性化される。
The surface of the metal cadmium powder becomes rough due to melting, and since fine metal nickel is present thereon, the surface area becomes very large, and the metal cadmium active material has high activity. In this case, the metal cadmium powder as a raw material may be one obtained by a wet method or one having a small surface area obtained by a dry method. When the wet method is used, a higher activity is obtained. Moreover, even if a powder produced by a dry method which is easy to handle but has low activity is used, it is sufficiently activated.

表面積が大きく活性度の高いカドミウム粉末は、先に述
べたように空気中、あるいは水中において酸化されやす
く、極板製造時の取り扱い、あるいは乾燥工程等の処理
により、不活性化しやすく、性能の低下を招きやすい。
Cadmium powder, which has a large surface area and high activity, is easily oxidized in air or water as described above, and is easily inactivated by handling during electrode plate manufacturing or treatment such as the drying process, resulting in poor performance. Easy to invite.

しかし、本発明によるように、金属カドミウム粉末の表
面が金属ニッケルで覆われているようなものでは、酸化
を受けにくく、また、金属カドミウム上に部分的に酸化
被膜が形成されても、電池活物質として使用した場合、
金属カドミウム上に存在する金属ニッケルを通して電流
が流れ、活物質の充放電反応が進行するため、特性の劣
化は招きにくい。
However, according to the present invention, when the surface of the metal cadmium powder is covered with metal nickel, it is less susceptible to oxidation, and even if a partially oxidized film is formed on the metal cadmium, the battery activity is reduced. When used as a substance,
An electric current flows through the metallic nickel existing on the metallic cadmium, and the charging / discharging reaction of the active material proceeds, so that the deterioration of the characteristics is less likely to occur.

実施例 以下本発明の実施例を詳述する。Examples Examples of the present invention will be described in detail below.

原料としての金属カドミウム粉末は、湿式法により製造
された平均粒径約2μmのものを使用した。この金属カ
ドミウム粉末を0.5モル濃度の20℃の硫酸ニッケル水溶
液中に約10秒浸漬した後、これを取り出し、水洗,乾燥
した。これを極板の予備電量としての活物質として使用
した。
The metal cadmium powder used as a raw material had a mean particle size of about 2 μm manufactured by a wet method. This metal cadmium powder was immersed in a 0.5 molar aqueous solution of nickel sulfate at 20 ° C. for about 10 seconds, then taken out, washed with water and dried. This was used as an active material as a preliminary charge of the electrode plate.

主活物質としての酸化カドミウム粉末100重量部に対
し、前記の予備充電量としての金属カドミウム粉末20重
量部を加えて混合し、これにポリビニルアルコールのエ
チレングリコール溶液を加え、混練してペースト状にす
る。このペーストを厚さ0.1mmのニッケルメッキした開
孔鉄板に塗着,乾燥し、厚さ約0.5mmの極板を得た。上
記カドミウム負極、及びニッケル塩液溶に浸漬処理をし
ない金属カドミウム粉末を使用したカドミウム負極を焼
結式ニッケル正極と組み合せて密閉形蓄電池を試作し、
その放電率特性と、過充電時の電池内圧試験とを行っ
た。放電率特性は電池を20℃において0.1C相当の電流で
15時間充電し、1〜3C相当の電流で放電したときの放電
容量と、0.2C相当の電流で放電したときの放電容量との
比率で評価した。また過充電時の内圧特性は、20℃で1/
3〜3C相当の電流で過充電したときの電池内圧のピーク
値で評価した。
To 100 parts by weight of the cadmium oxide powder as the main active material, 20 parts by weight of the metal cadmium powder as the above-mentioned precharge amount was added and mixed, and an ethylene glycol solution of polyvinyl alcohol was added thereto, and kneaded into a paste form. To do. This paste was applied on a nickel-plated iron plate having a thickness of 0.1 mm and dried to obtain an electrode plate having a thickness of about 0.5 mm. The above cadmium negative electrode, and a cadmium negative electrode using a metal cadmium powder that is not subjected to immersion treatment in a nickel salt solution are combined with a sintered nickel positive electrode to prototype a sealed storage battery,
The discharge rate characteristics and the battery internal pressure test at the time of overcharging were performed. The discharge rate characteristic is that the battery is at a current equivalent to 0.1C at 20 ° C.
It was evaluated by the ratio of the discharge capacity when it was charged for 15 hours and discharged at a current equivalent to 1 to 3 C and the discharge capacity when discharged at a current equivalent to 0.2 C. Also, the internal pressure characteristics during overcharging are 1 / at 20 ° C.
The peak value of the battery internal pressure when overcharged with a current equivalent to 3 to 3 C was evaluated.

第1図は放電レートと放電容量比率との関係を示す。a
は本発明による負極を用いた電池、bは比較例の負極を
用いた電池を示す。一般に放電率特性は、予備充電量と
しての金属カドミウム量の増加とともに向上するが、金
属カドミウム量を同一とした上記の負極を用いた場合の
特性の差は、充放電の電気化学反応に寄与する金属カド
ミウムの割合、すなわち利用率の差によるものと考えら
れる。本発明による負極では、金属カドミウムの活性度
が高いために、利用率が向上し、放電率特性が向上した
ものと考えられる。第2図は、充電レートと電池内圧と
の関係を示す。電池内圧においても本発明の効果が表わ
れている。
FIG. 1 shows the relationship between the discharge rate and the discharge capacity ratio. a
Indicates a battery using the negative electrode according to the present invention, and b indicates a battery using the negative electrode of the comparative example. Generally, the discharge rate characteristic improves with an increase in the amount of metal cadmium as a precharge amount, but the difference in the characteristic when the above negative electrode having the same amount of metal cadmium is used contributes to the electrochemical reaction of charge and discharge. It is considered that this is due to the difference in the rate of metal cadmium, that is, the utilization rate. In the negative electrode according to the present invention, it is considered that the utilization rate is improved and the discharge rate characteristics are improved because the activity of metal cadmium is high. FIG. 2 shows the relationship between the charging rate and the battery internal pressure. The effect of the present invention is exhibited even in the battery internal pressure.

電池過充電時には、正極から酸素が発生するが、この酸
素は負極の金属カドミウムで吸収される。この場合、負
極の金属カドミウムが活性であれば、酸素ガスの吸収能
力が高くなり電池の内圧は低くなる。密閉形蓄電池で
は、この酸素ガスの吸収能力が重要となる。通常、酸素
ガス吸収能力を向上させるためには、金属カドミウム量
を多くするような方法が用いられるが、同一金属カドミ
ウム量で、その活性度を上げることにより酸素ガス吸収
能力を向上させるほうが利点が多い。本発明による負極
は、予備充電量として添加した金属カドミウムの活性度
が高く、またその表面に存在する金属ニッケルが、酸素
ガス吸収の触媒として作用するので、酸素ガス吸収能力
が高く、電池の内圧が低いと考えられる。
When the battery is overcharged, oxygen is generated from the positive electrode, and this oxygen is absorbed by the metal cadmium of the negative electrode. In this case, if the negative electrode metal cadmium is active, the oxygen gas absorption capacity becomes high and the internal pressure of the battery becomes low. In a sealed storage battery, this oxygen gas absorption capacity is important. Usually, in order to improve the oxygen gas absorption capacity, a method of increasing the amount of metal cadmium is used, but it is more advantageous to improve the oxygen gas absorption capacity by increasing the activity with the same amount of metal cadmium. Many. The negative electrode according to the present invention has a high activity of metal cadmium added as a precharge amount, and the metal nickel present on the surface thereof acts as a catalyst for absorbing oxygen gas, so that the oxygen gas absorption capacity is high and the internal pressure of the battery is high. Is considered to be low.

発明の効果 以上のように本発明によれば、活性度の高い予備充電量
としての金属カドミウムが得られ、優れた特性で、かつ
化成不要のペースト式カドミウム負極が得られる。
EFFECTS OF THE INVENTION As described above, according to the present invention, a highly active pre-charged amount of metal cadmium can be obtained, and a paste type cadmium negative electrode having excellent characteristics and requiring no chemical conversion can be obtained.

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

第1図は密閉形ニッケルカドミウム蓄電池の放電レート
と放電容量比率との関係を示す図、第2図は充電レート
と電池内圧のピーク値との関係を示す図である。
FIG. 1 is a diagram showing the relationship between the discharge rate and the discharge capacity ratio of a sealed nickel-cadmium storage battery, and FIG. 2 is a diagram showing the relationship between the charge rate and the peak value of the battery internal pressure.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】酸化カドミウム粉末と、予備充電量として
の金属カドミウム粉末を主体とする活物質と、結着剤
と、その溶媒を混練してなるペーストを、導電性芯体に
練塗,乾燥するカドミウム負極の製造法であって、前記
予備充電量としての金属カドミウム粉末が、原料のカド
ミウム粉末をニッケルイオンを含む溶液に浸漬し、置換
反応により、ニッケル金属を部分的にカドミウム粉末上
に析出させたものであることを特徴とするペースト式カ
ドミウム負極の製造法。
1. A conductive core is kneaded and dried with a paste obtained by kneading cadmium oxide powder, an active material mainly composed of metal cadmium powder as a precharge amount, a binder, and a solvent thereof. A method for producing a cadmium negative electrode, wherein the metal cadmium powder as the precharge amount is obtained by immersing a raw material cadmium powder in a solution containing nickel ions, and by a substitution reaction, nickel metal is partially deposited on the cadmium powder. A method for producing a paste-type cadmium negative electrode, characterized in that
JP59245065A 1984-11-20 1984-11-20 Method for producing paste type cadmium negative electrode Expired - Lifetime JPH0680585B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59245065A JPH0680585B2 (en) 1984-11-20 1984-11-20 Method for producing paste type cadmium negative electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59245065A JPH0680585B2 (en) 1984-11-20 1984-11-20 Method for producing paste type cadmium negative electrode

Publications (2)

Publication Number Publication Date
JPS61124057A JPS61124057A (en) 1986-06-11
JPH0680585B2 true JPH0680585B2 (en) 1994-10-12

Family

ID=17128065

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59245065A Expired - Lifetime JPH0680585B2 (en) 1984-11-20 1984-11-20 Method for producing paste type cadmium negative electrode

Country Status (1)

Country Link
JP (1) JPH0680585B2 (en)

Also Published As

Publication number Publication date
JPS61124057A (en) 1986-06-11

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