JPH0619989B2 - Manufacturing method of nickel electrode for alkaline battery - Google Patents

Manufacturing method of nickel electrode for alkaline battery

Info

Publication number
JPH0619989B2
JPH0619989B2 JP58231738A JP23173883A JPH0619989B2 JP H0619989 B2 JPH0619989 B2 JP H0619989B2 JP 58231738 A JP58231738 A JP 58231738A JP 23173883 A JP23173883 A JP 23173883A JP H0619989 B2 JPH0619989 B2 JP H0619989B2
Authority
JP
Japan
Prior art keywords
electrode
nickel
active material
nickel electrode
alkaline 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.)
Expired - Lifetime
Application number
JP58231738A
Other languages
Japanese (ja)
Other versions
JPS60124353A (en
Inventor
良二 坪井
基秀 増井
正一 池山
功 松本
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 JP58231738A priority Critical patent/JPH0619989B2/en
Publication of JPS60124353A publication Critical patent/JPS60124353A/en
Publication of JPH0619989B2 publication Critical patent/JPH0619989B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M4/32Nickel oxide or hydroxide electrodes
    • 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)
  • 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、アルカリ電池用ニッケル極の製造法に関す
る。
TECHNICAL FIELD The present invention relates to a method for producing a nickel electrode for an alkaline battery.

従来例の構成とその問題点 非常灯用あるいは電子機器用の電源として、近年ニッケ
ル・カドミウム蓄電池(以下Ni−Cd電池という)の需要
が増大している。従来、Ni−Cd電池の正極には焼結式ニ
ッケル極とポケット式ニッケル極とが用いられているが
代表的なのは、焼結式である。焼結式ニッケル極は、ニ
ッケルあるいはニッケルメッキされた鉄の金属多孔板
に、カルボニルニッケル粉末を塗着し焼結させて基板を
作り、この焼結基板の活物質塩を含浸させ、加熱あるい
は化学反応により活物質に転化させて電極を得るもので
ある。この方法は、極板の性能がよく、長寿命で高率放
電特性に優れているが、焼結基板の多孔度が低く高容量
密度の電極が得られないとともに電極工程が煩雑である
といった問題があった。これに対し、高多孔度を有する
発泡状金属多孔体に活物質粉末を直接充填した非焼結式
電極は、簡単な工程で高い容量密度が得られる電極とし
て注目されている。しかし、この電極では比較的強度の
低い金属多孔体に活物質粉末を充填した後、高い圧力で
プレスする必要があるため、電極が亀裂、わん曲を発生
するという問題があった。
Configuration of Conventional Example and Its Problems In recent years, demand for nickel-cadmium storage batteries (hereinafter referred to as Ni-Cd batteries) has increased as a power source for emergency lights or electronic devices. Conventionally, a sintered nickel electrode and a pocket nickel electrode have been used for the positive electrode of a Ni-Cd battery, but a typical one is a sintered type. The sintered nickel electrode is a porous metal plate of nickel or nickel-plated iron, coated with carbonyl nickel powder and sintered to form a substrate, which is impregnated with the active material salt of the sintered substrate and heated or chemically treated. It is converted into an active material by a reaction to obtain an electrode. This method has good electrode plate performance, long life, and excellent high-rate discharge characteristics, but the problem is that the porosity of the sintered substrate is low and an electrode with high capacity density cannot be obtained, and the electrode process is complicated. was there. On the other hand, a non-sintered electrode in which a foamed metal porous body having a high porosity is directly filled with an active material powder has attracted attention as an electrode that can obtain a high capacity density in a simple process. However, in this electrode, since it is necessary to press the metal porous body having a relatively low strength with the active material powder and then pressing it at a high pressure, there is a problem that the electrode is cracked or bent.

発明の目的 本発明は、電池活物質を多孔体基板に直接充填するかあ
るいは塗着する非焼結式のニッケル極の製造法のうち、
特にプレス工程に関し、ニッケル極の高容量密度化及び
電極の亀裂、わん曲の発生防止を目的とする。
An object of the present invention is to provide a non-sintered nickel electrode, which comprises directly filling or coating a porous substrate with a battery active material,
Particularly in the pressing process, the purpose is to increase the capacity density of the nickel electrode and prevent cracks and bending of the electrode.

発明の構成 本発明は、非焼結式のニッケル極の製造法において、プ
レス工程時のニッケル極のペースト中の含水率を高湿度
雰囲気中で制御することを特徴とする。
Configuration of the Invention The present invention is characterized in that, in the method for producing a non-sintered nickel electrode, the water content of the nickel electrode paste during the pressing step is controlled in a high humidity atmosphere.

実施例の説明 以下、発明の詳細をNi−Cd電池を用いて説明する。Description of Examples Hereinafter, details of the present invention will be described using a Ni-Cd battery.

200メッシュのフルイを通過させた水酸化ニッケル,
カルボニルニッケル,金属コバルト粉末を、重量比で8
0:15:5の比率で混合したのち、0.5重量%のカ
ルボキシメチルセルロースを含む水を加えて含水率22
%のペーストを作成した。
Nickel hydroxide passed through a 200 mesh screen,
Carbonyl nickel and metallic cobalt powder in a weight ratio of 8
After mixing at a ratio of 0: 15: 5, water containing 0.5% by weight of carboxymethyl cellulose was added to obtain a water content of 22.
% Paste made.

つぎに、多孔度95%で厚さ0.13cmのニッケル金属
多孔体に、上記ペーストを充填し、1cm2あたり、0.
18gのペーストを含み、その寸法が、たて24cm、よ
こ8cm、厚さ0.13cmの充填極板を得た。充填極板を
プレスし高い充填密度を得るためには、活物質粉末は完
全乾燥状態よりも湿潤状態であるほうがよいことを種々
の検討から見い出した。これは活物質粉末の表面に存在
する水分が潤滑剤の作用をするためと考えられる。しか
し含水率が高すぎる場合は、プレス時に活物質粉末が流
出するため好ましくない。含水率の適正値は5〜10%
であったが、水分の分布が不均一である場合はわん曲の
発生が生じる。この極板中のペースト含水率が7〜8%
になる調整方法を4種類検討し、次表の如く分類した。
Next, a nickel metal porous body with a thickness of 0.13cm at a porosity of 95% was filled with the paste, per 1 cm 2, 0.
A filled electrode plate containing 18 g of paste and having dimensions of 24 cm in length, 8 cm in width and 0.13 cm in thickness was obtained. From various studies, it was found that the active material powder should be in a wet state rather than a completely dry state in order to press the filled electrode plate to obtain a high packing density. It is considered that this is because the water present on the surface of the active material powder acts as a lubricant. However, if the water content is too high, the active material powder flows out during pressing, which is not preferable. Proper value of water content is 5-10%
However, when the water distribution is non-uniform, bending occurs. The water content of the paste in this plate is 7-8%
4 adjustment methods were examined and classified as shown in the following table.

A〜Dの極板を、0.4mmの間隔のプレスロール間を通
過させて、平均厚さ0.60mmの極板を得た。しかしな
がら、AとBの処理を施した極板は、たわみ・歪み等が
発生し極板の切断・加工が困難であった。これは、極板
中の水分の分布が不均一であるからと考えられる。また
Aの方法においては極板の周辺部より乾燥がはじまるこ
とが確認され、水分不均一の原因となっている。またB
の方法においては、水を噴霧するなどの方法も検討した
が、極板の表面に多く分布し内部まで入らないといった
欠点が認められた。CとDの方法においては、雰囲気の
容積を大きく確保すれば、プレスに好ましい含水率7〜
8%の量に均一に保つことが可能であり、相対湿度が7
0〜100%の雰囲気であればプレスに適切な活物質の
含水率5〜10%が得られる。また、ロールプレス後の
たわみ・歪みもなく切断・加工も支障なく行なうことが
可能である。つぎにAとCの方法による極板を各150
枚ロールプレスしたときのプレス後の極板厚さのバラツ
キを、第1図と第2図に示す。この図に示されているよ
うに、含水率の調整方法の差により極板厚みのバラツキ
にも差が見られ、本発明の相対湿度70〜100%の高
湿度雰囲気中で調整する方法は、極板厚さのバラツキが
少ない点でもすぐれていることが確認された。
The electrode plates A to D were passed between press rolls having an interval of 0.4 mm to obtain an electrode plate having an average thickness of 0.60 mm. However, the electrode plates that have been subjected to the treatments A and B suffer from bending and distortion, which makes it difficult to cut and process the electrode plates. It is considered that this is because the distribution of water in the electrode plate is non-uniform. Further, in the method A, it was confirmed that the drying started from the peripheral portion of the electrode plate, which was the cause of nonuniform water content. Also B
In the above method, a method such as spraying water was also examined, but it was found that a large amount was distributed on the surface of the electrode plate and did not enter the inside. In the methods C and D, if a large volume of atmosphere is secured, the water content preferable for the press is 7 to 7.
It is possible to maintain a uniform amount of 8% and the relative humidity is 7
If the atmosphere is 0 to 100%, a water content of 5 to 10% of the active material suitable for pressing can be obtained. In addition, it is possible to perform cutting and processing without any trouble after the roll pressing without any bending or distortion. Next, each of the electrode plates according to the method of A and C is 150
FIG. 1 and FIG. 2 show the variation in the thickness of the electrode plate after pressing when the sheet is rolled. As shown in this figure, there is a difference in the variation of the electrode plate thickness due to the difference in the method of adjusting the water content, and the method of adjusting in the high humidity atmosphere of the relative humidity of 70 to 100% of the present invention is It was also confirmed that it was excellent in that there was little variation in electrode plate thickness.

発明の効果 以上述べたように本発明によれば、ロールプレス後の極
板厚さが均一で、たわみ・歪みとも少ない極板を得るこ
とが可能である。
EFFECTS OF THE INVENTION As described above, according to the present invention, it is possible to obtain an electrode plate having a uniform electrode plate thickness after roll pressing and less deflection and distortion.

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

第1図はペースト充填後、乾燥法により調整した極板の
ロールプレス後の厚さを示す度数分布図、第2図は本発
明の実施例による、ロールプレス後の極板厚さを示す度
数分布図である。
FIG. 1 is a frequency distribution diagram showing the thickness of the electrode plate after roll pressing after being filled with paste and adjusted by a drying method, and FIG. 2 is a frequency diagram showing the electrode plate thickness after roll pressing according to an embodiment of the present invention. It is a distribution map.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】少なくとも電池用活物質を含むペーストを
発泡状金属多孔体に直接充填するかあるいは金属多孔板
に塗着した後、これをプレスして電極とするニッケル極
の製造法であって、プレス時の電極の活物質ペースト含
水率を、相対湿度が70〜100%の雰囲気中で調整す
ることを特徴とするアルカリ電池用ニッケル極の製造
法。
1. A method for producing a nickel electrode in which a paste containing at least an active material for a battery is directly filled in a foamed metal porous body or coated on a metal porous plate and then pressed to form an electrode. A method for producing a nickel electrode for an alkaline battery, wherein the water content of the active material paste of the electrode during pressing is adjusted in an atmosphere having a relative humidity of 70 to 100%.
【請求項2】プレス時の電極中の活物質ペーストの含水
率が、5〜10%である特許請求の範囲第1項記載のア
ルカリ電池用ニッケル極の製造法。
2. The method for producing a nickel electrode for an alkaline battery according to claim 1, wherein the water content of the active material paste in the electrode during pressing is 5 to 10%.
JP58231738A 1983-12-08 1983-12-08 Manufacturing method of nickel electrode for alkaline battery Expired - Lifetime JPH0619989B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58231738A JPH0619989B2 (en) 1983-12-08 1983-12-08 Manufacturing method of nickel electrode for alkaline battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58231738A JPH0619989B2 (en) 1983-12-08 1983-12-08 Manufacturing method of nickel electrode for alkaline battery

Publications (2)

Publication Number Publication Date
JPS60124353A JPS60124353A (en) 1985-07-03
JPH0619989B2 true JPH0619989B2 (en) 1994-03-16

Family

ID=16928259

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58231738A Expired - Lifetime JPH0619989B2 (en) 1983-12-08 1983-12-08 Manufacturing method of nickel electrode for alkaline battery

Country Status (1)

Country Link
JP (1) JPH0619989B2 (en)

Also Published As

Publication number Publication date
JPS60124353A (en) 1985-07-03

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