JPS6023961A - Manufacture of paste type negative electrode plate for alkaline storage battery - Google Patents

Manufacture of paste type negative electrode plate for alkaline storage battery

Info

Publication number
JPS6023961A
JPS6023961A JP58131157A JP13115783A JPS6023961A JP S6023961 A JPS6023961 A JP S6023961A JP 58131157 A JP58131157 A JP 58131157A JP 13115783 A JP13115783 A JP 13115783A JP S6023961 A JPS6023961 A JP S6023961A
Authority
JP
Japan
Prior art keywords
cadmium
plate
nickel
negative electrode
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
JP58131157A
Other languages
Japanese (ja)
Other versions
JPH0318304B2 (en
Inventor
Masahiko Oshitani
政彦 押谷
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.)
Yuasa Corp
Original Assignee
Yuasa Corp
Yuasa Battery Corp
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 Yuasa Corp, Yuasa Battery Corp filed Critical Yuasa Corp
Priority to JP58131157A priority Critical patent/JPS6023961A/en
Publication of JPS6023961A publication Critical patent/JPS6023961A/en
Publication of JPH0318304B2 publication Critical patent/JPH0318304B2/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 fully remove an organic solvent that deteriorates the charge efficiency of a positive electrode by filling a nickel fiber sintering body with active material in which cadmium oxide and metallic cadmium are formed into a slurry shape by an ethylene glycol solvent and drying it above the melting point temperature of the solvent. CONSTITUTION:While 60-80% cadmium oxide and 20-40% metallic cadmium are being well mixed, they are formed into a slurry shape by adding 5-9% ethylne glycol to them. Then a high porosity sintering body made of nickel fiber with fiber diameter 4-5mu is filled with active material by continuously passing though and penetrating into this slurry solution. Subsequently, a plate it is partially dried in a drying machine consisting of an infrared lamp that is adjusted so that the vicinity of the plate surface can approach to 60-80 deg.C and is set in a specified thickness by a roller press. After the thickness of the plate is adjusted, the plate passed through a hot air drying machine with 250 deg.C and fully removes ethylene glycol. Finally, the plate is cut in dimensions conforming to the desired battery size. A sealed type nicke cadmium battery with high capacity and life can be obtained by using this negative electrode plate.

Description

【発明の詳細な説明】 本発明は、密閉型ニッケルカドミウム二次電池用カドミ
ウム電極の製造法に関するもので。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a cadmium electrode for a sealed nickel-cadmium secondary battery.

線径4μ〜50μの二・7ケル繊維焼結体に酸化カドミ
ウムと金属カドミウムをエチレングリコール溶剤によっ
てスラリー状とした活物質を充填した後、溶媒の沸点温
度の200 ’C以上で、乾燥させ、完全に溶剤を除去
したことを特徴とする。
After filling a 2.7 Kel fiber sintered body with a wire diameter of 4μ to 50μ with an active material made of a slurry of cadmium oxide and metal cadmium in an ethylene glycol solvent, it is dried at a temperature of 200°C or higher, which is the boiling point temperature of the solvent, Characterized by complete removal of solvent.

これまで、耐アルカリニッケル繊維のもつとも安価な製
造方法は、二・7ケルに少量の異種金属を添加したもの
を切削することによって製造されていた。しかしながら
、切削のさいに用いるナイフの消耗が激しく、常に均一
な線径の繊維を作成することが困難であった。本発明に
用いているニッケル繊維焼結体は、ニッケル粉末あるい
は酸化ニッケル粉末に有機バインダー。
Up until now, the most inexpensive method of manufacturing alkali-resistant nickel fibers has been to cut 2.7 Kel with a small amount of different metals added. However, the knives used during cutting are subject to significant wear and tear, making it difficult to always produce fibers with a uniform diameter. The nickel fiber sintered body used in the present invention is made of nickel powder or nickel oxide powder and an organic binder.

水等を加えてペースト状にし、しかる後微孔ノズルから
押し出して繊維状にしたのち、このものを約500’C
に加熱することにより、有機バインダー、水等を除去す
る。その後約1000°Cの高温還元性雰囲気下で充分
に焼結すると第1図a、b (bはaの拡大図である。
Add water, etc. to make a paste, then extrude it through a micro-hole nozzle to make it into a fiber, and heat it to about 50'C.
The organic binder, water, etc. are removed by heating to . After that, it is sufficiently sintered in a high-temperature reducing atmosphere at about 1000°C, as shown in Figures 1a and 1b (b is an enlarged view of a).

)の形状を有するものである。).

従来、酸化カドミウム、水酸化カドミウム等の活物質、
ニッケル粉末等の電導利、および有機溶剤等を電導性基
体に塗着乾燥されたペースト式カドミウム電極は、ア/
14カリ電解液中で化成と呼ばれる充放電処理をほどこ
した。化成によって、一部カドミウムを残存させた状態
で取り出し、水洗、乾燥を行なった。このカドミウム極
と放電末のニッケル電極並びにセパレータ等と共に電槽
に巻込まれ、電解液を注液後封口されて、密閉型ニッケ
ルカドミウム電池として製造されている。公知のごとく
、一部カドミウムを残存させる目的は、放電時ニッケル
極側で電池容量を制限させるためである。
Conventionally, active materials such as cadmium oxide and cadmium hydroxide,
Paste-type cadmium electrodes are made by applying conductive materials such as nickel powder and organic solvents to conductive substrates and drying them.
A charging/discharging process called chemical conversion was performed in a 14-potassium electrolyte. After chemical conversion, some of the cadmium was removed, washed with water, and dried. This cadmium electrode, the nickel electrode at the end of discharge, a separator, etc. are rolled up into a battery case, and after pouring an electrolyte solution, the container is sealed to produce a sealed nickel-cadmium battery. As is well known, the purpose of leaving some cadmium behind is to limit the battery capacity on the nickel electrode side during discharge.

もしカドミウムの残存がなく封口時すべて水酸化カドミ
ウムの場合、ニッケル電極に比較し。
If there is no residual cadmium and all cadmium hydroxide is used during sealing, compared to a nickel electrode.

カドミウム電極の方が利用率が悪いため、カドミウム極
側で容量制限をうける。又、ニッケル極側は、充放電サ
イクルの進行に伴ない容量劣化がほとんどない特性をも
っているのに対し。
Since the cadmium electrode has a lower utilization rate, the capacity is limited on the cadmium electrode side. In addition, the nickel electrode side has the characteristic that there is almost no capacity deterioration as the charge/discharge cycle progresses.

カドミウム極側は徐々に劣化を示す特性を有するため、
これを補なうためにカドミウムを残存させるのである。
Since the cadmium electrode side has the characteristic of gradually deteriorating,
Cadmium is left to compensate for this.

このカドミウム極の劣化は。The deterioration of this cadmium pole.

活物質の電気化学的理論容量の約60〜80%程度で停
止し、それ以後は劣化が極端に遅くなる。すなわち、活
物質の利用率はニッケル極側がほぼ100%近くである
のに対し、カドミウム極側は60〜80%程度であり、
この両者の容量の均衡を保たせるために、上記化成処理
をイテなうのである。この工程は複雑なたけでなく。
It stops at about 60 to 80% of the theoretical electrochemical capacity of the active material, and thereafter deterioration becomes extremely slow. In other words, the utilization rate of the active material is nearly 100% on the nickel electrode side, while it is around 60 to 80% on the cadmium electrode side.
In order to maintain a balance between these two capacities, the chemical conversion treatment described above is repeated. This process is not only complicated.

ペースト式カドミウム極は焼結式カドミウム極と異なり
、化成中に発生するガスによって活物質の脱落がしばし
ば発生ずる。そのため粘性の少ない低濃度アルカリ電解
液でかつ低電流密度で長時間充電を行ない5発生するガ
スがすみやかに極板外にのがれるようにするといった処
決を用いたりしなければならない。ニッケル繊維焼結体
を用い従来法によってペースト式負極板を作成すること
も可能であるが2本発明の方法は活物質と有機溶剤から
なるスラリーをニソうル繊維焼結体に充填後、活物質以
外の不純物である7有機溶剤を完全に除去し、化成処理
をうけることなく、ニッケル極、セパレータ等と共に巻
き込み、電解液を注液したのち封口することによって密
閉型ニッケルカドミウム電池とする。電解液を注液する
工程にいたるまで、アルカリを使用しないために電池に
とって有害な炭酸根の混入がきわめて少ない。又有機溶
剤は正極の充電効率を悪化させるといった欠点があるが
、沸点以」二の温度で乾燥することによって完全に除去
することが出来る2本発明はこれらの種々の点で多くの
長所を有するものである。
Unlike sintered cadmium electrodes, paste-type cadmium electrodes often suffer from active material falling off due to gases generated during formation. Therefore, it is necessary to use a solution such as charging with a low concentration alkaline electrolyte with low viscosity and a low current density for a long time so that the generated gas can quickly escape from the electrode plate. Although it is possible to create a paste-type negative electrode plate using a conventional method using a nickel fiber sintered body, the method of the present invention involves filling a nickel fiber sintered body with a slurry consisting of an active material and an organic solvent, and then applying an active material to the nickel fiber sintered body. A sealed nickel-cadmium battery is obtained by completely removing the organic solvent, which is an impurity other than the substance, and rolling it in with nickel electrodes, separators, etc. without undergoing chemical conversion treatment, and sealing the battery after pouring an electrolyte. Since no alkali is used in the process of injecting the electrolyte, there is very little chance of contamination with carbonate radicals, which are harmful to the battery. Furthermore, organic solvents have the disadvantage of deteriorating the charging efficiency of the positive electrode, but can be completely removed by drying at a temperature above the boiling point.The present invention has many advantages in these various points. It is something.

またこのニッケル繊維焼結体は繊維を焼結させたもので
あるため、多孔度が90%と高く。
Furthermore, since this nickel fiber sintered body is made by sintering fibers, it has a high porosity of 90%.

また強度の点でも優れている。It also has excellent strength.

公知のごとく今日、金属カドミウムは数μ〜士数μの微
細な粒子の製造が可能であり、かつ安価で市販されてい
る。また酸化カドミウムは。
As is well known, today metal cadmium can be produced into fine particles of several microns to several microns and is commercially available at low cost. Also, cadmium oxide.

水もしくはアルカリ電解液と接触すると、CaO十H2
O−>C(1(OH) 2 、と水酸化カドミウムに変
化し、一方金属カドミウムのCa (OH)2への変化
は少ない。
When in contact with water or alkaline electrolyte, CaO+H2
O−>C(1(OH) 2 ) and changes to cadmium hydroxide, while the change of metal cadmium to Ca (OH) 2 is small.

以下本発明の一実施例に基づき説明する。An explanation will be given below based on one embodiment of the present invention.

酸化カドミウム60〜8D%、金属カドミウム20〜4
0%をよく混合しながらこのものに5〜9%のエチレン
グリコールを加えてスラリー状とする。しかる後数士米
の前記高多孔度焼結体をこのスラリー液中に連続的に通
過させ。
Cadmium oxide 60-8D%, metal cadmium 20-4
Add 5 to 9% ethylene glycol to this mixture while mixing well to form a slurry. After that, several pieces of the highly porous sintered body were continuously passed through the slurry liquid.

浸透さゼることによって活物質を充填させる。The active material is filled by osmosis.

その後60〜80°Cに極板表面付近がなるように調整
された赤外線ランプよりなる乾燥機中で部分的に乾燥さ
tl、ついでローラープレスによって所定の厚みにされ
る。厚味調整後の極板は。
Thereafter, it is partially dried in a dryer equipped with an infrared lamp adjusted so that the temperature near the surface of the electrode plate is 60 to 80°C, and then it is made to a predetermined thickness using a roller press. The electrode plate after thickness adjustment.

温度250 ’Cの熱風乾燥機を通りエチレングリコー
ルは完全に除去される。最後に極板は、希望する電池サ
イズに見合った寸法に切断される。
Ethylene glycol is completely removed by passing through a hot air dryer at a temperature of 250'C. Finally, the plates are cut to size commensurate with the desired battery size.

この負極板と、従来の化成処理によって完全放電された
シンタ一式正極板、並びにポリプロピレン不織布よりな
るセパレータ等を用いて自動的に書きこまれた後、電槽
に挿入される。その後、水酸化カリウム、水酸化ナトリ
ウム、水酸化リチウム中から1種もしくは2種以上のア
ルカリ性水溶液を注液し封口する。封口後電池は一昼夜
放置することによって、電解液との親和性をもたした後
、充放電を行ない完成電池となる。
This negative electrode plate, a sintered positive electrode plate completely discharged by conventional chemical conversion treatment, a separator made of polypropylene nonwoven fabric, etc. are used to automatically write information, and then the information is inserted into the battery case. Thereafter, one or more alkaline aqueous solutions selected from potassium hydroxide, sodium hydroxide, and lithium hydroxide are injected and sealed. After sealing, the battery is left for a day and night to become compatible with the electrolyte, and then charged and discharged to become a completed battery.

このように完成されたC型サイズの密閉型ニッケルカド
ミウム電池(1)と、従来の化成処理工程に」、って作
成された負極板からなる同−一−・Jイズの密12J 
5ニッケル力ドミウノ・電池(1)の常h1□)におけ
る寿命を1週へたと(−ろ、第2図に示すごとく、不発
明による電池の方か容量、並びに寿6θ共優ねているこ
とか判明した。
The C-sized sealed nickel-cadmium battery (1) completed in this way and the negative electrode plate made using the conventional chemical conversion treatment process are used to produce a compact 12J battery of the same J size.
When the lifespan of the 5-nickel power domiuno battery (1) (h1□) was reduced to one week (-ro), as shown in Figure 2, the uninvented battery was superior in both capacity and lifespan 6θ. It turned out.

以りのごとく1本発明は製造工程が従来法よりきわめて
簡1iiであり、かつ有害ろ′エチレングIJ H)−
ルか完全除去されているため、容量、寿命切においても
優れた特徴をもっており工業的価(+f目ははなはだ大
なるものである。
As described above, the manufacturing process of the present invention is much simpler than the conventional method, and the manufacturing process of the present invention is much simpler than that of the conventional method.
Since the metal is completely removed, it has excellent characteristics in terms of capacity and lifespan, and its industrial value (+f is extremely large).

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

第1 II″Aのa、bは本発明(・5−用いている二
・ノケル繊&ft焼結体の顕i大鏡写真である。第2図
は本7、明電池と従来電池のAf命比較特性曲@]4で
ある。 (1) 本発明電池 (11)従来Ei、池出願出願人
浅電池株式会社 第1図 α 第1図 す 第 2 図 100 200 300 充放γaサイクル数(へ)
1 II''A, a and b are microscopic photographs of the Nokel fiber & ft sintered body used in the present invention (・5-). (1) Battery of the present invention (11) Conventional Ei, Ike Applicant Asa Battery Co., Ltd. Figure 1 α Figure 1 Figure 2 Figure 100 200 300 Number of charging/discharging γa cycles ( fart)

Claims (1)

【特許請求の範囲】[Claims] ニッケル粉末あるいは酸化ニッケル粉末より作tした4
μ〜50μのニッケル繊維を焼結した焼結体に、酸化カ
ドミウムおよび金属カドミウムの混合活物質を充填して
なるアルカリ蓄電池用ベース1式負極板の製造法。
4 made from nickel powder or nickel oxide powder
A method for producing a base 1 negative electrode plate for an alkaline storage battery, in which a sintered body made by sintering nickel fibers of μ to 50 μ is filled with a mixed active material of cadmium oxide and metal cadmium.
JP58131157A 1983-07-18 1983-07-18 Manufacture of paste type negative electrode plate for alkaline storage battery Granted JPS6023961A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58131157A JPS6023961A (en) 1983-07-18 1983-07-18 Manufacture of paste type negative electrode plate for alkaline storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58131157A JPS6023961A (en) 1983-07-18 1983-07-18 Manufacture of paste type negative electrode plate for alkaline storage battery

Publications (2)

Publication Number Publication Date
JPS6023961A true JPS6023961A (en) 1985-02-06
JPH0318304B2 JPH0318304B2 (en) 1991-03-12

Family

ID=15051327

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58131157A Granted JPS6023961A (en) 1983-07-18 1983-07-18 Manufacture of paste type negative electrode plate for alkaline storage battery

Country Status (1)

Country Link
JP (1) JPS6023961A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61264670A (en) * 1985-05-20 1986-11-22 Matsushita Electric Ind Co Ltd Manufacture of cadmium negative electrode for alkaline storage battery
US5248571A (en) * 1990-09-27 1993-09-28 Gates Energy Products, Inc. Cadmium electrode and cell having anti-agglomeration characteristics

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61264670A (en) * 1985-05-20 1986-11-22 Matsushita Electric Ind Co Ltd Manufacture of cadmium negative electrode for alkaline storage battery
US5248571A (en) * 1990-09-27 1993-09-28 Gates Energy Products, Inc. Cadmium electrode and cell having anti-agglomeration characteristics

Also Published As

Publication number Publication date
JPH0318304B2 (en) 1991-03-12

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