JPS60258854A - Method of manufacturing paste type cadmium negative pole - Google Patents

Method of manufacturing paste type cadmium negative pole

Info

Publication number
JPS60258854A
JPS60258854A JP59115942A JP11594284A JPS60258854A JP S60258854 A JPS60258854 A JP S60258854A JP 59115942 A JP59115942 A JP 59115942A JP 11594284 A JP11594284 A JP 11594284A JP S60258854 A JPS60258854 A JP S60258854A
Authority
JP
Japan
Prior art keywords
plate
cadmium
nickel
paste
electrode plate
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
JP59115942A
Other languages
Japanese (ja)
Other versions
JPH03745B2 (en
Inventor
Hideo Kaiya
英男 海谷
Shingo Tsuda
津田 信吾
Osamu Takahashi
収 高橋
Motohide Masui
増井 基秀
Minoru Yamaga
山賀 実
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 JP59115942A priority Critical patent/JPS60258854A/en
Publication of JPS60258854A publication Critical patent/JPS60258854A/en
Publication of JPH03745B2 publication Critical patent/JPH03745B2/ja
Granted 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
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/26Processes of manufacture
    • 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

Abstract

PURPOSE:To manufacture a paste type cadmium negative pole with high performance by immersing a plate into solution containing nickel oil after giving metal cadmium as a preliminary charging volume to the plate in the formation process, and permitting the nickel to deposit on the plate. CONSTITUTION:When a plate, in which paste of active material mainly composed by cadmium oxide etc. is applied to the core, is negatively electrolyzed in alkaline solution, metal cadmium is electrochemically generated in the plate. This process is carried out so as to give a preliminary charging volume. When the plate, in which the formation has been completed, is immersed into solution containing nickel ions, the cadmium is dissolved and the substitution reaction which deposits the nickel in the plate is generated, because the metal cadmium in the plate has lower potential than that of the nickel. The metal nickel is deposited in surface layers of the plate and in holes within the plate to form a conductive matrix. Whereby, it is possible to manufacture a paste type cadmium negative pole with high performance which can be charged in a short time.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、アルカリ蓄電池用ペースト式カドミウム負極
の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for producing a paste-type cadmium negative electrode for alkaline storage batteries.

従来例の構成とその問題点 アルカリ蓄電池用ペースト式カドミウム負極は、一般に
酸化カドミウムあるいは水酸化カドミウムを主体とし、
これにカーボニルニッケル、グラファイト等の導電性粉
末、ポリビニルアルコール。
Structure of conventional examples and their problems Paste-type cadmium negative electrodes for alkaline storage batteries generally consist of cadmium oxide or cadmium hydroxide,
In addition, carbonyl nickel, conductive powder such as graphite, and polyvinyl alcohol.

カルボキシメチルセルロース等の結着剤及び水やエチレ
ングリコール等の溶媒を加え、混練してペーストとし、
これをニッケルメッキした開孔鋼板等の導電性芯材に塗
着し、乾燥した後、アルカリ溶液中で化成することによ
って製造される。
Add a binder such as carboxymethyl cellulose and a solvent such as water or ethylene glycol, knead to make a paste,
It is manufactured by applying this to a conductive core material such as a nickel-plated perforated steel plate, drying it, and then chemically converting it in an alkaline solution.

前記の化成工程の目的は、活物質相別に用いる酸化カド
ミウム、水酸化カドミウム々との放電状態のカドミウム
化合物の一部または全部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。
The purpose of the above chemical conversion process is to convert part or all of the cadmium compound in the discharged state with cadmium oxide and cadmium hydroxide used for each active material phase into metallic cadmium in the charged state, and to provide a pre-charged portion in the negative electrode. It's about doing.

ペースト式カドミウム負極は、焼結式に比べて製造が容
易で、高い容量密度が得られる利点を有するが、焼結式
のような導電性マトリクスが存在しないため、電池充電
時に生成する金属カドミウムの成長が芯材近傍で起とり
、極板表面層まで達しにくい。このため過充電時に正極
から発生する酸素ガスとの反応が効率的に行われず、密
閉形電池に使用すると、電池の内圧が高くなるという欠
点がある。また、電池を高温雰囲気で放置したり、充放
電を繰り返したりすると、負極表面の活物質粒子の粗大
化を招き、3 ・ 充放電特性の劣化を招く。このような活物質粒子の粗大
化は、活物質を保持する骨格を有する焼結式では起こり
にくい現象である。
Paste-type cadmium negative electrodes have the advantage of being easier to manufacture and providing higher capacity density than sintered-type ones, but because they do not have a conductive matrix like sintered-type cadmium negative electrodes, metal cadmium produced during battery charging is Growth occurs near the core material and is difficult to reach the surface layer of the electrode plate. For this reason, the reaction with oxygen gas generated from the positive electrode during overcharging does not occur efficiently, and when used in a sealed battery, there is a drawback that the internal pressure of the battery increases. Furthermore, if the battery is left in a high-temperature atmosphere or repeatedly charged and discharged, the active material particles on the surface of the negative electrode will become coarser, resulting in the deterioration of charge-discharge characteristics. Such coarsening of active material particles is a phenomenon that is unlikely to occur in a sintered type having a skeleton that holds the active material.

このような問題を解決するため、化成前の極板をニッケ
ルイオンを含む溶液中で陰電解し、極板表面にニッケル
層を付与する方法も提案されている(特開昭58−32
363)が、工程が煩雑となる欠点を有する。
In order to solve these problems, a method has been proposed in which the electrode plate before chemical formation is subjected to negative electrolysis in a solution containing nickel ions to form a nickel layer on the electrode plate surface (Japanese Patent Laid-Open No. 58-32).
363) has the disadvantage that the process is complicated.

発明の目的 本発明は、以上のような従来の不都合をなくし、高性能
のペースト式カドミウム負極を提供することを目的とす
る。
OBJECTS OF THE INVENTION It is an object of the present invention to eliminate the above-mentioned conventional disadvantages and provide a high-performance paste-type cadmium negative electrode.

発明の構成 本発明は、酸化カドミウム粉末もしくは水酸化カドミウ
ム粉末を主とする活物質ペーストを導電性芯材に塗着し
た後、化成工程で予備充電量としての金属カドミウムを
付与した後、ニッケルイオl ンを含む溶液中に浸漬し
、カドミウムとの置換度1′ 応によりニッケルを極板へ析出させるペースト式カドミ
ウム負極の製造法である。
Structure of the Invention The present invention involves applying an active material paste mainly composed of cadmium oxide powder or cadmium hydroxide powder to a conductive core material, and then adding metallic cadmium as a precharge amount in a chemical formation process. This is a method for producing a paste-type cadmium negative electrode in which nickel is immersed in a solution containing nickel and nickel is deposited on the electrode plate by reaction with cadmium at a degree of substitution of 1'.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

酸化カドミウムあるいは水酸化カドミウムを主とする活
物質ペーストを芯材に塗着した極板を、アルカリ溶液中
で陰電解すると、電気化学的に金属カドミウムが極板中
に生成する。この工程は、予備充電量を付与するだめに
一般的に行われる化成工程である。この化成済み極板を
、ニッケルイオンを含む溶液中に浸漬すると、極板中の
金属カドミウムがニッケルより卑々電位をもつため、カ
ドミウムが溶解し、極板にニッケルが析出する置換反応
が起こる。金属ニッケルは、極板表面層と極板中の空孔
内に析出し、導電性のマトリクスを形成する。
When an electrode plate whose core material is coated with an active material paste containing cadmium oxide or cadmium hydroxide is subjected to negative electrolysis in an alkaline solution, metallic cadmium is electrochemically generated in the electrode plate. This process is a chemical conversion process that is generally performed to provide a preliminary charge amount. When this chemically formed electrode plate is immersed in a solution containing nickel ions, the metal cadmium in the electrode plate has a lower potential than nickel, so a substitution reaction occurs in which the cadmium dissolves and nickel is deposited on the electrode plate. Metallic nickel is deposited in the plate surface layer and in the pores in the plate to form a conductive matrix.

上記の極板を密閉形蓄電池に用いると、電池充電時に負
極内に生成する金属カドミウムは、付力された金属ニッ
ケルの導電性マトリクスに沿って極板表面層1で均一に
成長する。一方、化成工程のみ行い、本発明のような導
電性マトリクスを有しない極板では、充電時の金属カド
ミウムの生成が芯材付近に集中し、表面層まで達する割
合が少ない。密閉形電池では、過充電時に正極より発生
する酸素ガスの負極での吸収反応が重要である。
When the above electrode plate is used in a sealed storage battery, the metal cadmium generated in the negative electrode during battery charging grows uniformly on the electrode plate surface layer 1 along the conductive matrix of applied metal nickel. On the other hand, in an electrode plate that undergoes only a chemical conversion process and does not have a conductive matrix like the one of the present invention, the generation of metallic cadmium during charging is concentrated near the core material, and the proportion of metal cadmium reaching the surface layer is small. In sealed batteries, the absorption reaction at the negative electrode of oxygen gas generated from the positive electrode during overcharging is important.

この酸素吸収が悪いと、過充電時に電池内圧が上昇する
ので、大電流での充電ができない。言い換えると、短時
間充電ができない。酸素ガスは、負極の金属カドミウム
により吸収されるものであるから、本発明によるものの
ように金属カドミウムが極板表面に多く分布している方
が有利である。
If this oxygen absorption is poor, the internal pressure of the battery will rise during overcharging, making it impossible to charge with a large current. In other words, it cannot be charged for a short period of time. Since oxygen gas is absorbed by the metal cadmium of the negative electrode, it is advantageous for the metal cadmium to be distributed in large amounts on the electrode plate surface, as in the case of the present invention.

また、ペースト式カドミウム負極は、前述のように、高
温で活物質粒子の粗大化を招く欠点を有している。粗大
化した活物質粒子は、電気化学的に不活性であるため、
充放電特性が劣化するという結果となる。また、この現
象がさらに進行すると、デンドライト状に成長したカド
ミウム化合物がセパレータを貫通して正極に達し、内部
短絡の原因となる。このような活物質粗大化の現象は、
焼結式のように、活物質を物理的に保持する骨格をもだ
ないペースト式で著しく、またその位置は極板表面で起
こりやすい。本発明によると、極板に金属ニッケルのマ
トリクスができ、これが極板6 ・・− 表面での活物質の粗大化を物理的におさえるだめ、前記
のような特性劣化の防止に有効である。
Further, as described above, the paste-type cadmium negative electrode has the drawback that the active material particles become coarse at high temperatures. Since the coarse active material particles are electrochemically inactive,
This results in deterioration of charge/discharge characteristics. Further, as this phenomenon progresses further, the cadmium compound that has grown in the form of a dendrite penetrates the separator and reaches the positive electrode, causing an internal short circuit. This phenomenon of active material coarsening is
This is particularly noticeable in paste types that do not have a skeleton that physically holds the active material, such as the sintered type, and is more likely to occur on the surface of the electrode plate. According to the present invention, a matrix of metallic nickel is formed on the electrode plate, which physically suppresses the coarsening of the active material on the surface of the electrode plate 6, and is effective in preventing the above-mentioned characteristic deterioration.

実施例の説明 平均粒径約1μmの酸化カドミウム粉末をポリビニルア
ルコールのエチレングリコール溶液で練合してペースト
とし、これをニッケルメッキした開孔鉄板に塗着し、乾
燥して約0,25朋厚の極板とした。次に、この極板を
比重1.20の水酸化ナトリウム水溶液中で陰電解し、
金属カドミウムを付与する化成を行い、水洗、乾燥した
。その後pH3,6,液温50’Cに調整した硫酸ニッ
ケルの1モル/l水溶液に約20秒間浸漬し、金属カド
ミウムの一部とニッケルイオンの置換反応を行わせた。
Description of Examples Cadmium oxide powder with an average particle size of about 1 μm is kneaded with a polyvinyl alcohol ethylene glycol solution to make a paste, which is applied to a nickel-plated perforated iron plate and dried to a thickness of about 0.25 mm. It was used as a pole plate. Next, this electrode plate was subjected to negative electrolysis in a sodium hydroxide aqueous solution with a specific gravity of 1.20,
Chemical conversion was performed to add metal cadmium, followed by washing with water and drying. Thereafter, it was immersed for about 20 seconds in a 1 mol/l aqueous solution of nickel sulfate adjusted to a pH of 3.6 and a liquid temperature of 50'C to cause a substitution reaction between part of the metal cadmium and nickel ions.

この処理により生成した金属ニッケルは、極板表面に被
膜を形成するとともに、極板内の空孔部に析出し、導電
性のマ) IJクスを形成する。実施例の場合、分析結
果によれば、金属カドミウムの約6〜10%が金属ニッ
ケルに置換された。
The metallic nickel produced by this treatment forms a film on the surface of the electrode plate, and also precipitates in the pores within the electrode plate, forming a conductive matrix. In the case of the example, the analytical results showed that about 6-10% of the metallic cadmium was replaced by metallic nickel.

この極板を水洗、乾燥した後、所定の寸法に切り断し、
焼結式ニッケル正極と組み合わせて1200mAh相当
の密閉形蓄電池を構成し、電池特性を試験した。
After washing and drying this electrode plate, cut it to the specified size,
In combination with a sintered nickel positive electrode, a sealed storage battery equivalent to 1200 mAh was constructed and the battery characteristics were tested.

試験は、負極の酸素ガス吸収性を評価するための過充電
時の電池内圧試験と、高温特性を評価するための高温で
の充放電サイクル試験をした。電池内圧試験は、20′
Cにおいて1〜3C相当の電流で充電したときの電池内
圧のピークで評価し、充放電ザイクル試験は、46°C
において10相当の電流で充放電を繰り返したときの放
電時間で評価した。
The tests included a battery internal pressure test during overcharging to evaluate the oxygen gas absorption of the negative electrode, and a high-temperature charge-discharge cycle test to evaluate the high-temperature characteristics. Battery internal pressure test is 20'
Evaluation was made at the peak of the battery internal pressure when charged at a current equivalent to 1 to 3C at 46°C.
Evaluation was made based on the discharge time when charging and discharging were repeated at a current equivalent to 10%.

第1図は充電レートと電池内圧力のピークとの関係を示
す。aは上記実施例の負極を用いた電池、bは実施例の
化成工程までを行った比較例の負極を用いた電池を示す
。本発明による負極は、充電時に金属カドミウムが極板
表面に分布しやすく、酸素ガス吸収能力が高く、従って
電池aは電池内圧が低く、高率で充電が可能である。
FIG. 1 shows the relationship between the charging rate and the peak of the battery internal pressure. A shows a battery using the negative electrode of the above example, and b shows a battery using a negative electrode of a comparative example in which the chemical conversion process of the example was performed. In the negative electrode according to the present invention, metal cadmium is easily distributed on the electrode plate surface during charging, and the oxygen gas absorption capacity is high. Therefore, battery a has a low internal pressure and can be charged at a high rate.

! 1 第2図は充放電サイクルに伴う放電時間の変化シl 平板状に成長した和犬結晶が多数存在したが、電池aで
は少なかった。このように本発明の負極では結晶の粗大
化が起こりにくいため、電池aでは高温での充放電サイ
クルによる特性の劣化が少ない。
! 1 Figure 2 shows the change in discharge time associated with the charge/discharge cycle.There were many Japanese dog crystals that grew in a flat plate shape, but there were fewer of them in battery a. As described above, in the negative electrode of the present invention, coarsening of the crystals is less likely to occur, so that in battery a, there is little deterioration in characteristics due to charging/discharging cycles at high temperatures.

発明の効果 以上のように、本発明によれば、簡単な処理で、ペース
ト式カドミウム負極の特性を大幅に改良することができ
る。
Effects of the Invention As described above, according to the present invention, the characteristics of a paste-type cadmium negative electrode can be significantly improved with simple processing.

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

第1図はニッケルーカドミウム蓄電池の充電レートと電
池内のピーク圧力との関係を示す図、第2図は充放電回
数と放電時間との関係を示す図である。
FIG. 1 is a diagram showing the relationship between the charging rate of a nickel-cadmium storage battery and the peak pressure inside the battery, and FIG. 2 is a diagram showing the relationship between the number of times of charging and discharging and the discharge time.

Claims (1)

【特許請求の範囲】[Claims] 酸化カドミウムもしくは水酸化カドミウムを主とするペ
ーストを導電性芯材に塗着する工程と、前記の塗着極板
をアルカリ電解液中で陰電解して予備充電量を付与する
化成工程と、化成後の極板をニッケルイオンを含む溶液
中に浸漬して極板にニッケルを析出させる工程を有する
ペースト式カドミウム負極の製造法。
A process of applying a paste mainly containing cadmium oxide or cadmium hydroxide to a conductive core material, a chemical conversion process of applying a preliminary charge amount by electrolyzing the applied electrode plate in an alkaline electrolyte, and a process of applying a pre-charge amount to the conductive core material. A method for producing a paste-type cadmium negative electrode, which includes the step of immersing the subsequent electrode plate in a solution containing nickel ions to deposit nickel on the electrode plate.
JP59115942A 1984-06-06 1984-06-06 Method of manufacturing paste type cadmium negative pole Granted JPS60258854A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59115942A JPS60258854A (en) 1984-06-06 1984-06-06 Method of manufacturing paste type cadmium negative pole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59115942A JPS60258854A (en) 1984-06-06 1984-06-06 Method of manufacturing paste type cadmium negative pole

Publications (2)

Publication Number Publication Date
JPS60258854A true JPS60258854A (en) 1985-12-20
JPH03745B2 JPH03745B2 (en) 1991-01-08

Family

ID=14674986

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59115942A Granted JPS60258854A (en) 1984-06-06 1984-06-06 Method of manufacturing paste type cadmium negative pole

Country Status (1)

Country Link
JP (1) JPS60258854A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63310565A (en) * 1987-06-12 1988-12-19 Matsushita Electric Ind Co Ltd Manufacture of paste type cadmium negative electrode
US5264309A (en) * 1991-01-10 1993-11-23 Sorapec S.A. Cadmium electrodes for alkaline batteries

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63310565A (en) * 1987-06-12 1988-12-19 Matsushita Electric Ind Co Ltd Manufacture of paste type cadmium negative electrode
JPH0831316B2 (en) * 1987-06-12 1996-03-27 松下電器産業株式会社 Method for producing paste type cadmium negative electrode
US5264309A (en) * 1991-01-10 1993-11-23 Sorapec S.A. Cadmium electrodes for alkaline batteries
US5334465A (en) * 1991-01-10 1994-08-02 Sorapec S.A. Method of making cadmium electrodes for alkaline batteries

Also Published As

Publication number Publication date
JPH03745B2 (en) 1991-01-08

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