JPS609059A - Manufacture of positive pole plate for alkaline storage battery - Google Patents

Manufacture of positive pole plate for alkaline storage battery

Info

Publication number
JPS609059A
JPS609059A JP58116758A JP11675883A JPS609059A JP S609059 A JPS609059 A JP S609059A JP 58116758 A JP58116758 A JP 58116758A JP 11675883 A JP11675883 A JP 11675883A JP S609059 A JPS609059 A JP S609059A
Authority
JP
Japan
Prior art keywords
cadmium
nickel
salt
impregnating
positive electrode
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
JP58116758A
Other languages
Japanese (ja)
Inventor
Tetsuzo Kojima
哲三 小島
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.)
Japan Storage Battery Co Ltd
Nihon Denchi KK
Original Assignee
Japan Storage Battery Co Ltd
Nihon Denchi KK
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 Japan Storage Battery Co Ltd, Nihon Denchi KK filed Critical Japan Storage Battery Co Ltd
Priority to JP58116758A priority Critical patent/JPS609059A/en
Publication of JPS609059A publication Critical patent/JPS609059A/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
    • H01M4/24Electrodes for alkaline accumulators
    • H01M4/26Processes of manufacture
    • H01M4/28Precipitating active material on the carrier
    • 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 generate efficiently the reducing reaction of cadmium for checking the generation of hydrogen even when a battery reaches an overdischarge state by impregnating independently cadmium salt in addition to the impregnation of nickel salt. CONSTITUTION:The impregnating operation of nickel salt to become a positive pole active substance and the impregnation of cadmium salt as the overdischarge countermeasures are independently performed. For instance, a cadmium nitrate water solution is firstly impregnated into a sintering type substrate having a porosity degree of about 80% when sintering nickel powder while being neutralized in a sodium hydroxide water solution after being dried for performing the impregnating operation to be dried again and secondly for being impregnated in the water solution mainly composed of nickel nitrate followed by being neutralized in the sodium hydroxide water solution after being dried for being dried again, that is to say that the impregnating operation of nickel salt is repeated five times.

Description

【発明の詳細な説明】 本発明は、ニッケルわ)末を焼結したいわゆる焼結式基
板にニッケル塩を含浸してなるアルカリ蓄電池用正極板
の製造力肱に関するものであり、その目的どづるところ
は、ニッケル」為の含浸に加えてカドミウム塩を単独に
含浸ザることによって、電池が過放電状態に至っても、
カドミウムの37元反応が効率よく生じて、水素の発生
を阻止する事を可0ヒならしめることにある。アルカリ
蓄電池の中でも、密閉式アルカリ蓄電池は、過充電にお
(プる電池内圧上T等の弊害防止のため、正極に対して
負(折の活物質量を過剰にして、正極の充電が終了後に
発生ずる酸素を負極で吸収せしめ、電池内圧の上y7を
防止し、しかも電解液の消耗をなくづるという対策をと
っている。一方電池が過放電状態に至った場合、正極か
らtま水素が、負極からは酸素が発生りる。特に正極か
ら水素が発生すると、電池内で吸収される事がぼとんど
ないために、過放電が進むにつれて電池の内圧が異常に
上昇し電池1(l能を害づることが知られている。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a positive electrode plate for an alkaline storage battery, which is made by impregnating a nickel salt into a so-called sintered substrate made of sintered nickel powder. However, by impregnating cadmium salt alone in addition to impregnating nickel, even if the battery reaches an overdischarge state,
The purpose is to make it possible for the 37-element reaction of cadmium to occur efficiently and to prevent the generation of hydrogen. Among alkaline storage batteries, sealed alkaline storage batteries are designed to prevent negative effects such as overcharging (such as an increase in battery internal pressure) by using an excessive amount of active material on the positive electrode to terminate charging of the positive electrode. The negative electrode absorbs the oxygen generated later, preventing the internal pressure of the battery from rising, and also eliminating the consumption of the electrolyte.On the other hand, when the battery reaches an overdischarge state, hydrogen is removed from the positive electrode. However, oxygen is generated from the negative electrode.In particular, when hydrogen is generated from the positive electrode, it is hardly absorbed within the battery, so as over-discharge progresses, the internal pressure of the battery rises abnormally and battery 1 (It is known to impair one's ability.

有害な過放電を防止するために、従来は放電電圧が一定
の電圧にまで低下した時に、その電圧を検出して自動的
に放電を中止する方法が通常採用されてさた。しかしこ
の様な方法は、装置が複雑。
In order to prevent harmful overdischarge, a method has conventionally been adopted in which when the discharge voltage drops to a certain level, the voltage is detected and the discharge is automatically stopped. However, this method requires complicated equipment.

高価になるどともに、多数の単電池を直列に接続して使
用する場合、単電池ごとの容量差は必然的に存在し、容
量の相対的に小さい電池が、過放電になる危険性はどの
様な方法をとろうとも避り難いもの、であった。
In addition to being expensive, when a large number of cells are connected in series, there is inevitably a difference in capacity between the cells, and there is a risk that batteries with relatively small capacities will over-discharge. No matter what methods we tried, it was unavoidable.

以上の点から、密閉形アルカリ蓄電池の理想としては、
過放電に至っても異常な(しかも再度充電ずれば正常に
復帰する拝な電池をつくればよいわけである。方法とし
て(,1幾種類かあるが、実現させるには、次に説明す
る様に困ガであった。
From the above points, the ideal sealed alkaline storage battery is:
All you have to do is create a battery that will not malfunction even if it is over-discharged (and will return to normal after being recharged again.There are several ways to do this, but to make it happen, please use the following method). I was in trouble.

1つは電池内にガス吸収用の電極を設け、過放°市時に
発生ずる酸素や水素を回収ザる方法がある。
One method is to provide a gas absorption electrode inside the battery and recover oxygen and hydrogen generated during over-release.

しかしこの方法は、触媒として高価な貴金属を使用し、
(苦造的にも複雑で、無駄が多く、一般的ではない。
However, this method uses expensive precious metals as catalysts,
(It is complicated, wasteful, and not common.

もう 1つは正極活物質中に水酸化カドミウムを混合し
、電池が過放電状態になっても、正極活物質中の水酸化
カドミウムが、金属カドミウムとなる反応を国光的に生
じさせ、水素発生を防ぐ方法である。この方式で使用す
る正極は、正極活物質となるニッケル塩水溶液中にカド
ミウム塩を混合し、これを焼結式基板に含浸、乾燥、中
和する含浸操作を繰り返−ツガ法で作られるが、この方
法では過放電時にお(プるカドミウム利用率が非常に悪
く、有効に作用させるには、多用のカドミウムを混入さ
せる必要があった。この為ニッケル塩の含有量を少くせ
ざるをえなくなり、正極としての放電容■が若しく低下
し、実用的ではなかった。
The other method is to mix cadmium hydroxide into the positive electrode active material, so that even if the battery is over-discharged, the cadmium hydroxide in the positive electrode active material undergoes a reaction to become metallic cadmium, and hydrogen is generated. This is a way to prevent this. The positive electrode used in this method is made using the hemlock method, which involves repeating an impregnation process in which cadmium salt is mixed into an aqueous nickel salt solution that serves as the positive electrode active material, impregnated into a sintered substrate, dried, and neutralized. However, in this method, the utilization rate of cadmium was very poor during overdischarge, and it was necessary to mix a large amount of cadmium in order to make it work effectively.For this reason, the content of nickel salt had to be reduced. As a result, the discharge capacity (2) as a positive electrode slightly decreased, making it impractical.

本発明は、上記に説明した、過放電対策・として正極中
に水素発生を防ぐカドミウムの含浸方法に関し、従来]
)法による欠点を除去し、過放電対策としての惧れた性
能を右するアルカリ蓄電池用正極板を得るための製造方
法に関づるものである。
The present invention relates to a cadmium impregnation method for preventing hydrogen generation in a positive electrode as a countermeasure against overdischarge, as explained above.
This invention relates to a manufacturing method for obtaining a positive electrode plate for an alkaline storage battery that eliminates the drawbacks caused by the above method and has the desired performance as a countermeasure against overdischarge.

即ら含浸液としてのニッケル塩水溶液中にカドミウム塩
を添加して、同時に正極基板中に含浸を行う従来の方法
に変えて、正極活物質となるニッケル膓の含浸操作と、
過放電対策としてのカドミウム塩の含浸を別個に行うこ
とを特徴とするものである。以下に実施例に基づいて詳
細な31明を行う。
That is, instead of the conventional method of adding cadmium salt to an aqueous nickel salt solution as an impregnation liquid and impregnating it into the positive electrode substrate at the same time, an operation of impregnating nickel salt, which will become the positive electrode active material, is performed.
It is characterized by separately impregnating with cadmium salt as a countermeasure against overdischarge. A detailed explanation will be given below based on the examples.

ニッケルわ)末を焼結した多孔度約80%、厚み0.7
mn+の焼結式Jユ仮に、まず硝酸カドミウム水溶液を
含浸し、乾燥後水酸化す1−リウム水溶液中にて中和し
、再度乾燥する含浸操作を行い、次には硝酸ニッケルを
主成分とする水溶液に含浸し、乾燥後水酸化ナトリウム
水溶液中で中和し、再度乾燥するというニッケル塩の含
浸操作を5回繰り返し行い、本発明による正極板Aを得
た。次にAと同じ基板に硝酸ニッケルに対して20%の
硝酸カドミウムを含む硝酸ニッケルと硝酸カドミウムの
混合水78液を含浸し、乾1g/、後水酸化ナトリウム
水溶液中で中和、再度乾燥するという含浸操作を6回繰
り返して得た従)Kの製造方d1による正極板Bを製作
し、A、8両11々板をつぎの条件で試験を行い、その
性能を比較した。これらA、B極板の中の水酸化ニッケ
ルど水酸化カドミウムの聞は同一どなる様に調整した。
Sintered nickel powder, porosity approximately 80%, thickness 0.7
For the sintering type J of mn+, an impregnation operation is performed in which the material is first impregnated with a cadmium nitrate aqueous solution, dried, neutralized in a 1-lium hydroxide aqueous solution, and dried again, and then nickel nitrate is used as the main component. The positive electrode plate A according to the present invention was obtained by repeating the nickel salt impregnation operation five times, in which the positive electrode plate A was impregnated with a nickel salt aqueous solution, dried, neutralized in a sodium hydroxide aqueous solution, and dried again. Next, the same substrate as A was impregnated with 78 liquid mixed water of nickel nitrate and cadmium nitrate containing 20% of cadmium nitrate to nickel nitrate, dried at 1 g/water, then neutralized in an aqueous sodium hydroxide solution, and dried again. A positive electrode plate B was produced by the manufacturing method d1 of sub)K obtained by repeating the impregnation operation 6 times, and the positive electrode plate B was tested under the following conditions and the performance was compared. The content of nickel hydroxide and cadmium hydroxide in these A and B electrode plates was adjusted to be the same.

まず6moj水酸化カリウム水溶液中で充分な容量を右
づ゛るノJドミウム極を相手極どじて2 lit A/
 cut XlGll間の充電を行った後、4m△/c
IITで放電したどころ、表1に示す結果を得た。
First, in a 6moj potassium hydroxide aqueous solution, add a 2 liter domium electrode to the other electrode to a sufficient capacity.
After charging between cut XlGll, 4m△/c
When discharging at IIT, the results shown in Table 1 were obtained.

過放電領域でのカドミウムの反応による過放電可能量(
01(01−1)2 ’αの反応によってH2発生時J
ulを遅延さUうる容量)は本発明の製造法による正極
板では6mΔ11/ cot bあるが、従来の製造方
法による正(らLではわずか1.5m A h / a
n?と非常に少く、カドミウムの利用率でも非常に小さ
い事がわかる。なお正極どしての容量は本発明あるいは
従来法による正極とも(よぼ同じであった。
Possible overdischarge amount due to the reaction of cadmium in the overdischarge area (
01 (01-1) 2 'When H2 is generated by the reaction of α, J
The positive electrode plate manufactured by the manufacturing method of the present invention has a positive capacity of 6 mΔ11/cot b, but the positive electrode plate manufactured by the conventional manufacturing method has a positive capacity of only 1.5 mA h/a.
n? It can be seen that the utilization rate of cadmium is very small. Note that the capacity of the positive electrode was almost the same as that of the positive electrode according to the present invention or the conventional method.

表1.放電試M結果 次に本発明になる正極Aと従来法による正極Bをイれぞ
れ使用し円筒形の1.8At+の電池を作り過放電時の
性能を比較した。試験は0.IOAの電流で1G時間充
電した後0.2CAの電流で放電し、過放電特性を比較
した結果を第1図に示す。OVまでの通常の放電領域に
おいては△、B共にほぼ同じ特性であるが、転極(OV
以下)しだ後過放電状態になると、Bは多少のカドミウ
ムの効果はあるものの、す”ぐに電圧は水素発生を示す
−0,2Vl→近まで低下づ−ると同時に内圧が異常に
上昇する。−力木発明の製造法による正極を使った電池
八は転極後も1簡間以上カドミウムが有効に作用し、過
放電領域での水素発生を遅延させる事が明らかである。
Table 1. Results of Discharge Test M Next, cylindrical 1.8 At+ batteries were made using positive electrode A according to the present invention and positive electrode B according to the conventional method, and their performance during overdischarge was compared. The test is 0. FIG. 1 shows the results of comparing overdischarge characteristics obtained by charging with a current of IOA for 1 G hours and then discharging with a current of 0.2 CA. In the normal discharge region up to OV, both △ and B have almost the same characteristics, but the polarity reversal (OV
(Below) When the overdischarge condition begins, B has some cadmium effect, but the voltage immediately drops to -0.2 Vl, which indicates hydrogen generation, and at the same time the internal pressure rises abnormally. - It is clear that in Battery No. 8 using the positive electrode manufactured by Rikiki's invention, cadmium acts effectively for more than one minute after polarity reversal, delaying hydrogen generation in the overdischarge region.

尚、先の実施例ではカドミウム塩を初回に含浸し以後ニ
ッケル塩の含浸を繰り返すという方法について述べたが
、ノJドミウム塩の含浸は初回に限らず、ニッケル塩を
含浸した後であっても、又はニッケル塩の含浸を数回課
り返J“その途中であっても、何らさしつかえf1同様
の効果が得られた。
In the previous example, the method of impregnating with cadmium salt for the first time and then repeating the impregnation with nickel salt was described, but impregnation with domium salt is not limited to the first time, and even after impregnating with nickel salt. , or impregnated with nickel salt several times, even in the middle of the process, the same effect as f1 was obtained.

正極にカドミウムを添加する方法どして、従来の含浸液
のニッケル塩中にカドミウムを添加してニッケルとカド
ミウムを同時に含浸する方法に比べ、ニッケル塩とは別
にカドミウムJuを含浸づるという本発明による正極の
方がはるかに過放電時にJ3けるノJドミウムの効果が
大きい原因は詳細にはわからないが、基板中にJj4ノ
ろ水酸化ニッケルと水酸化カドミウムの配列の近いにあ
るものと考えられる。
Compared to the conventional method of adding cadmium to the nickel salt of the impregnating solution to impregnate nickel and cadmium at the same time, the method of adding cadmium to the positive electrode is based on the present invention, in which cadmium Ju is impregnated separately from the nickel salt. The reason why the positive electrode has a much greater effect on J3 during overdischarge is not known, but it is thought to be due to the close arrangement of Jj4 nickel hydroxide and cadmium hydroxide in the substrate.

以上説明した様に、本発明によるアルノJり蓄電池用正
極板は、ニッケル塩の含浸とは別個に過放電対U↓とし
Cのカドミウム塩の含浸を独立して行う事にJ、って、
過放電条件下で、添加したカドミウムが有効に作用して
水素の発生を遅延さμる事が可能どなるものでその工業
的価値は大である。
As explained above, in the positive electrode plate for an Alno J storage battery according to the present invention, impregnation with cadmium salt for overdischarge protection U↓ and C is performed independently from impregnation with nickel salt.
Under overdischarge conditions, the added cadmium can effectively act to delay the generation of hydrogen, which is of great industrial value.

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

第1図は本発明による電池△と従来法による電池Bの放
電時の端子電圧63 J:び電池内圧゛比較した図であ
る。
FIG. 1 is a diagram comparing the terminal voltage 63 J: and battery internal pressure during discharging of the battery Δ according to the present invention and the battery B according to the conventional method.

Claims (1)

【特許請求の範囲】[Claims] 1、焼結式基板の多孔部にニッケル塩を主体とづろ水溶
液を含浸し、乾燥、−中和する含浸操作を繰り返し行う
工程に加えて、カドミウム塩水溶液を含浸し、乾燥、中
和する工程を含む事を特徴4するアルカリ蓄電池用正極
板の製造方法。
1. In addition to the process of repeatedly impregnating the porous parts of the sintered substrate with an aqueous solution mainly composed of nickel salts, drying, and neutralizing, impregnating with an aqueous cadmium salt solution, drying, and neutralizing. 4. A method for producing a positive electrode plate for an alkaline storage battery, characterized in that it includes a step.
JP58116758A 1983-06-27 1983-06-27 Manufacture of positive pole plate for alkaline storage battery Pending JPS609059A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58116758A JPS609059A (en) 1983-06-27 1983-06-27 Manufacture of positive pole plate for alkaline storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58116758A JPS609059A (en) 1983-06-27 1983-06-27 Manufacture of positive pole plate for alkaline storage battery

Publications (1)

Publication Number Publication Date
JPS609059A true JPS609059A (en) 1985-01-18

Family

ID=14695009

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58116758A Pending JPS609059A (en) 1983-06-27 1983-06-27 Manufacture of positive pole plate for alkaline storage battery

Country Status (1)

Country Link
JP (1) JPS609059A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5121450A (en) * 1974-08-15 1976-02-20 Nippon Electric Co
JPS53126131A (en) * 1977-04-12 1978-11-04 Matsushita Electric Ind Co Ltd Method of manufacturing positive electrode for alkaline battery
JPS56143669A (en) * 1980-04-10 1981-11-09 Sanyo Electric Co Ltd Positive plate for alkaline storage battery
JPS575018A (en) * 1980-06-13 1982-01-11 Olympus Optical Co Ltd Focus controller
JPS57205968A (en) * 1981-06-10 1982-12-17 Sanyo Electric Co Ltd Manufacture of anode plate for alkali cell

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5121450A (en) * 1974-08-15 1976-02-20 Nippon Electric Co
JPS53126131A (en) * 1977-04-12 1978-11-04 Matsushita Electric Ind Co Ltd Method of manufacturing positive electrode for alkaline battery
JPS56143669A (en) * 1980-04-10 1981-11-09 Sanyo Electric Co Ltd Positive plate for alkaline storage battery
JPS575018A (en) * 1980-06-13 1982-01-11 Olympus Optical Co Ltd Focus controller
JPS57205968A (en) * 1981-06-10 1982-12-17 Sanyo Electric Co Ltd Manufacture of anode plate for alkali cell

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