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JP3272009B2 - Method for producing nickel electrode for alkaline storage battery - Google Patents
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JP3272009B2 - Method for producing nickel electrode for alkaline storage battery - Google Patents

Method for producing nickel electrode for alkaline storage battery

Info

Publication number
JP3272009B2
JP3272009B2 JP34307791A JP34307791A JP3272009B2 JP 3272009 B2 JP3272009 B2 JP 3272009B2 JP 34307791 A JP34307791 A JP 34307791A JP 34307791 A JP34307791 A JP 34307791A JP 3272009 B2 JP3272009 B2 JP 3272009B2
Authority
JP
Japan
Prior art keywords
active material
nickel
electrode
substrate
material filling
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 - Fee Related
Application number
JP34307791A
Other languages
Japanese (ja)
Other versions
JPH05174815A (en
Inventor
浩三 大槻
憲俊 池田
和昭 尾崎
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP34307791A priority Critical patent/JP3272009B2/en
Publication of JPH05174815A publication Critical patent/JPH05174815A/en
Application granted granted Critical
Publication of JP3272009B2 publication Critical patent/JP3272009B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • 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】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、ニッケルーカドミウム
電池等のアルカリ蓄電池に用いられるニッケル電極の製
造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a nickel electrode used in an alkaline storage battery such as a nickel-cadmium battery.

【0002】[0002]

【従来の技術】従来、アルカリ蓄電池用ニッケル電極の
製造方法としては、活物質保持体としての多孔性ニッケ
ル焼結基板を硝酸ニッケル等の酸性ニッケル塩含浸溶液
に浸漬して基板の孔中にニッケル塩含浸させた後、アル
カリ溶液中で酸性ニッケル塩を活物質である水酸化ニッ
ケルに変化させるという活物質充填操作が一般に知られ
ている。しかしながら、このような活物質充填操作で
は、1回当たりの活物質充填量が少なく、1回の操作で
は十分な充填量が得られないため、上記の操作を複数回
繰り返して、所望量の活物質を充填する必要がある。し
たがって、ニッケル電極の作製に多大な時間を要し、製
造コストが高騰するという課題を有していた。
2. Description of the Related Art Conventionally, as a method of manufacturing a nickel electrode for an alkaline storage battery, a porous nickel sintered substrate as an active material holder is immersed in an acidic nickel salt impregnating solution such as nickel nitrate to form nickel in a hole of the substrate. It is generally known to perform an active material filling operation in which an acidic nickel salt is converted into nickel hydroxide as an active material in an alkaline solution after salt impregnation. However, in such an active material filling operation, the amount of active material charged per operation is small, and a sufficient amount of active material cannot be obtained by one operation. Therefore, the above operation is repeated a plurality of times to obtain a desired amount of active material. The substance needs to be filled. Therefore, there has been a problem that a large amount of time is required for manufacturing the nickel electrode, and the manufacturing cost increases.

【0003】そこで、特開昭62−58566号公報等
に示されるように、含浸溶液として高温且つ高濃度の硝
酸ニッケル水溶液等の溶融塩含浸液を用いて、活物質充
填効率を向上させて、製造工程を簡略化させるような方
法が提案されている。
[0003] Therefore, as disclosed in Japanese Patent Application Laid-Open No. 62-58566, a high-temperature and high-concentration molten salt impregnating solution such as nickel nitrate aqueous solution is used as an impregnating solution to improve the active material filling efficiency. A method for simplifying the manufacturing process has been proposed.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、このよ
うな方法では、含浸溶液の腐食性が強くなるため、基板
が浸食される(即ち、基板を構成するニッケルが溶解す
る)。この結果、基板が脆弱化して、このような極板を
用いた電池のサイクル特性が低下するという課題を有し
ていた。
However, in such a method, the substrate is eroded (that is, the nickel constituting the substrate is dissolved) because the impregnating solution becomes more corrosive. As a result, there has been a problem that the substrate becomes brittle and the cycle characteristics of a battery using such an electrode plate deteriorate.

【0005】本発明は上記課題を考慮してなされたもの
であり、活物質充填操作の回数を低減することにより、
焼結式ニッケル電極を用いた電池のサイクル特性を向上
させ且つ焼結式ニッケル電極の生産性を向上させて製造
コストの低減を図り得るアルカリ蓄電池用ニッケル電極
の製造方法の提供を目的としている。
[0005] The present invention has been made in view of the above problems, and by reducing the number of active material filling operations,
It is an object of the present invention to provide a method of manufacturing a nickel electrode for an alkaline storage battery, which can improve the cycle characteristics of a battery using a sintered nickel electrode and improve the productivity of the sintered nickel electrode to reduce the manufacturing cost.

【0006】[0006]

【課題を解決するための手段】本発明は上記目的を達成
するために、多孔性ニッケル基板を酸性ニッケル塩含浸
水溶液に浸漬する第1工程と、上記基板をアルカリ水溶
液に浸漬して前記酸性ニッケル塩を活物質化させる第2
工程と、第2工程で基板に保持されたアルカリ水溶液を
そのまま保持させつつ乾燥を行う第3工程とから成る活
物質充填操作を、複数回行うことを特徴とする。
In order to achieve the above object, the present invention provides a first step in which a porous nickel substrate is immersed in an acidic nickel salt impregnated aqueous solution; The second to make salt active material
And the alkaline aqueous solution held on the substrate in the second step.
The active material filling operation including the third step of drying while holding the material as it is is performed a plurality of times.

【0007】[0007]

【作用】一般に、ニッケル焼結基板の孔中で、酸性ニッ
ケル塩とアルカリ水溶液との中和反応によって水酸化ニ
ッケルを生成させる活物質充填操作を繰り返していく
と、徐々に活物質充填量の伸びが減少してゆくことを実
験により確認した。これは、ニッケル焼結基板の孔の体
積に占める活物質の体積の割合が、活物質充填操作と共
に増加するという理由によるものと考えられる。
Generally, when the active material filling operation for generating nickel hydroxide by the neutralization reaction between an acidic nickel salt and an aqueous alkali solution in the pores of a nickel sintered substrate is repeated, the active material filling amount gradually increases. It was confirmed by experiments that the concentration decreased. This is considered to be because the ratio of the volume of the active material to the volume of the pores of the nickel sintered substrate increases with the active material filling operation.

【0008】このようなことを考慮すると、ニッケル焼
結基板に活物質を効率良く充填させるには、ニッケル焼
結基板の孔の深部から水酸化ニッケルを生成させ、且つ
この生成したニッケルの嵩密度が大きいことが必要とな
る。そこで、上記方法の如く、酸性ニッケル塩を活物質
化させるために用いるアルカリ水溶液を除去することな
く乾燥させると、2回目以降の活物質充填操作におい
て、基板を酸性ニッケル塩水溶液に浸漬した場合には、
酸性ニッケル塩水溶液と固体状態のアルカリとが反応し
て水酸化ニッケルが生成する。このように、固体状態の
アルカリとの反応による水酸化ニッケルは、本発明者ら
の実験によると、液体状態のアルカリとの反応による水
酸化ニッケルに比べて嵩密度が大きくなるということが
確認された。このように、嵩密度の大きな水酸化ニッケ
ルが生成されると、ニッケル焼結基板に活物質を効率良
く充填することができるので、生産性が向上する。尚、
別の実験により、上記のような水酸化ニッケルの嵩密度
の増大は、水酸化ニッケルの真密度が大きくなるという
ことに起因していることを確認した。
In view of the above, in order to efficiently fill the nickel sintered substrate with the active material, nickel hydroxide is generated from the deep part of the hole of the nickel sintered substrate, and the volume density of the generated nickel is increased. Must be large. Therefore, as in the above method, when the substrate is dried without removing the alkaline aqueous solution used to make the acidic nickel salt an active material, the substrate is immersed in the acidic nickel salt aqueous solution in the second and subsequent active material filling operations. Is
The acidic nickel salt aqueous solution reacts with the solid alkali to form nickel hydroxide. Thus, according to experiments performed by the present inventors, it has been confirmed that nickel hydroxide produced by reaction with solid-state alkali has a higher bulk density than nickel hydroxide produced by reaction with liquid-state alkali. Was. As described above, when nickel hydroxide having a large bulk density is generated, the nickel sintered substrate can be efficiently filled with the active material, so that productivity is improved. still,
According to another experiment, it was confirmed that the increase in the bulk density of nickel hydroxide as described above was caused by an increase in the true density of nickel hydroxide.

【0009】加えて、上記方法であれば、2回目以降の
活物質充填操作において、酸性ニッケル塩水溶液に浸漬
した場合とアルカリ水溶液に浸漬した場合とに活物質生
成反応が生じる。即ち、1回の活物質充填操作で2回の
活物質生成反応が生じることになる。したがって、活物
質充填作業の作業回数を減らすことができるので、生産
性を向上させることができると共に、酸性ニッケル塩含
浸液にニッケル焼結基板を浸漬する回数を減らすことが
できるので、ニッケル焼結基板の腐食が抑制され、この
結果、本発明の製造方法による電極を用いた電池のサイ
クル特性を向上させることが可能となる。
In addition, with the above method, in the second and subsequent active material filling operations, an active material generation reaction occurs when immersed in an acidic nickel salt aqueous solution and when immersed in an alkaline aqueous solution. That is, two active material generation reactions occur in one active material filling operation. Therefore, the number of times of the active material filling operation can be reduced, so that the productivity can be improved, and the number of times of immersing the nickel sintered substrate in the acidic nickel salt impregnating liquid can be reduced. Corrosion of the substrate is suppressed, and as a result, it is possible to improve the cycle characteristics of the battery using the electrode according to the manufacturing method of the present invention.

【0010】更に、本発明の方法であれば、ニッケル焼
結基板の孔の深部から水酸化ニッケルを生成させること
ができるので、この点からも効率良く活物質充填操作を
行うことができる。
Further, according to the method of the present invention, nickel hydroxide can be generated from the deep portion of the hole of the nickel sintered substrate, and the active material filling operation can be performed efficiently from this point as well.

【0011】[0011]

【実施例】本発明の一実施例を、図1に基づいて、以下
に説明する。 〔実施例〕先ず初めに、還元性雰囲気中で乾燥すること
により得た多孔度80%のニッケル焼結基板を、硝酸ニ
ッケル溶融塩(温度80℃、比重1.75)に浸漬す
る。次に、上記ニッケル焼結基板を25%の苛性ソーダ
水溶液に浸漬することにより、上記硝酸ニッケルを活物
質である水酸化ニッケルに変化させる。次いで、アルカ
リを上記ニッケル焼結基板に保持させた状態で基板を乾
燥させる。このような一連の活物質充填操作を5回繰り
返すことにより、ニッケル電極を作製した。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to FIG. EXAMPLE First, a nickel sintered substrate having a porosity of 80% obtained by drying in a reducing atmosphere is immersed in a molten salt of nickel nitrate (temperature: 80 ° C., specific gravity: 1.75). Next, the nickel nitrate is converted into nickel hydroxide, which is an active material, by immersing the nickel sintered substrate in a 25% aqueous solution of caustic soda. Next, the substrate is dried while the alkali is held on the nickel sintered substrate. By repeating such a series of active material filling operations five times, a nickel electrode was produced.

【0012】このようにして作製した電極を、以下
(A)電極と称する。 〔比較例1〕アルカリを保持させた状態でニッケル焼結
基板を乾燥させる工程の代わりに、活物質である水酸化
ニッケルを生成させた後水洗によってアルカリを除去す
るという工程を実施する他は、上記実施例と同様にして
電極を作製した。尚、このような活物質充填操作は、上
記実施例と同様、5回繰り返している。
The electrode fabricated in this manner is hereinafter referred to as (A) electrode. [Comparative Example 1] Instead of a step of drying a nickel sintered substrate while holding an alkali, a step of generating nickel hydroxide as an active material and then removing the alkali by washing with water was performed. An electrode was produced in the same manner as in the above example. Note that such an active material filling operation is repeated five times as in the above-described embodiment.

【0013】このようにして作製した電極を、以下(X
1 )電極と称する。 〔比較例2〕アルカリを保持させた状態でニッケル焼結
基板を乾燥させる工程を実施しない(即ち、基板にアル
カリを液体状態で保持させたまま、次回の活物質充填操
作を行う)他は、上記実施例と同様にして電極を作製し
た。尚、このような活物質充填操作は、上記実施例と同
様、5回繰り返している。
The electrode fabricated in this manner is referred to as (X
1 ) Called electrodes. [Comparative Example 2] Except for not performing the step of drying the nickel sintered substrate while holding the alkali (that is, performing the next active material filling operation while holding the alkali in the liquid state on the substrate), An electrode was produced in the same manner as in the above example. Note that such an active material filling operation is repeated five times as in the above-described embodiment.

【0014】このようにして作製した電極を、以下(X
2 )電極と称する。 〔実験1〕上記本発明の製造方法にて作製した(A)電
極と比較例の製造方法にて作製した(X1 )電極,(X
2 )電極とにおいて、1〜5回目の活物質充填操作にお
ける活物質充填量を調べたので、その結果を図1に示
す。尚、図1においては、比較例の(X1 )電池におけ
る5回目の活物質充填操作終了後の活物質充填量を10
0として表している。また、各回の活物質充填量は、ア
ルカリにニッケル基板を浸漬して活物質化する操作を終
了した後、水洗、乾燥を行い、この後に計量したもので
ある。
The electrode fabricated in this manner is referred to as (X
2 ) Called electrodes. [Experiment 1] The electrode (A) produced by the production method of the present invention and the electrode (X 1 ) produced by the production method of the comparative example, (X)
2 ) As to the electrodes, the active material filling amounts in the first to fifth active material filling operations were examined, and the results are shown in FIG. In FIG. 1, the active material filling amount after the fifth active material filling operation in the (X 1 ) battery of the comparative example was 10
It is represented as 0. Further, the active material filling amount at each time is obtained by immersing the nickel substrate in an alkali to convert the active material into an active material, rinsing with water, drying, and then measuring.

【0015】図1から明らかなように、本発明の製造方
法にて作製した(A)電極は比較例の製造方法にて作製
した(X1 )電極,(X2 )電極に比べて、2回目以降
の活物質充填量が飛躍的に多くなっていることが認めら
れる。これは、以下に示す理由によるものと考えられ
る。即ち、本発明の(A)電極では、2回目以降の活物
質充填操作において、硝酸ニッケル溶融塩と固体状態の
苛性ソーダとが反応して水酸化ニッケルが生成する。こ
のように、固体状態のアルカリとの反応による水酸化ニ
ッケルは、液体状態のアルカリとの反応による水酸化ニ
ッケルに比べて嵩密度が大きくなる。この結果、活物質
充填操作を円滑に進行させることができる。加えて、2
回目以降の活物質充填操作においては、硝酸ニッケル溶
融塩に浸漬した場合と苛性ソーダに浸漬した場合とに活
物質生成反応が生じる。即ち、1回の活物質充填操作で
2回の活物質生成反応が生じることになる。これらのこ
とから、上記の如く2回目以降の活物質充填量が飛躍的
に多くなったものと考えられる。
As is apparent from FIG. 1, the electrode (A) manufactured by the manufacturing method of the present invention is 2 times smaller than the electrodes (X 1 ) and (X 2 ) manufactured by the manufacturing method of the comparative example. It is recognized that the active material filling amount after the first time has increased dramatically. This is considered to be due to the following reason. That is, in the (A) electrode of the present invention, in the second and subsequent active material filling operations, the nickel nitrate molten salt reacts with solid caustic soda to produce nickel hydroxide. As described above, nickel hydroxide produced by the reaction with the alkali in the solid state has a larger bulk density than nickel hydroxide produced by the reaction with the alkali in the liquid state. As a result, the active material filling operation can proceed smoothly. In addition, 2
In the active material filling operation after the first time, an active material generation reaction occurs when immersed in molten nickel nitrate and when immersed in caustic soda. That is, two active material generation reactions occur in one active material filling operation. From these facts, it is considered that the filling amount of the active material after the second time has increased dramatically as described above.

【0016】これに対して、比較例の(X1 )電極で
は、活物質化した後にアルカリを除去しているので、各
回の活物質充填操作において生成する活物質は、液体状
のアルカリとの反応によって生成するもののみであるた
め、活物質の嵩密度が小さくなる。加えて、1回の活物
質充填操作においては、1回しか活物質生成反応が生じ
ない。また、比較例の(X2 )電極では、2回目以降の
活物質充填操作では2回の活物質生成反応が生じるが、
生成する活物質は共に液体状のアルカリとの反応による
嵩密度の小さい活物質となる。加えて、基板の深部では
なく表面で活物質生成反応が生じる。これらのことか
ら、上記の如く2回目以降の活物質充填量が少なくなっ
たものと考えられる。 〔実験2〕本発明の製造方法にて作製した(A)電極と
比較例の製造方法にて作製した(X1 )電極,(X2
電極とにおいて、活物質の利用率を測定した。尚、実験
に当り、全ての極板の活物質充填量を同一に設定してい
る。また、実験条件は、水酸化カリウム水溶液中で、理
論容量の5時間率で充電した後、3時間率で放電すると
いう条件である。
On the other hand, in the (X 1 ) electrode of the comparative example, the alkali was removed after the active material was turned into an active material. Since only active substances are generated by the reaction, the bulk density of the active material is reduced. In addition, in one active material filling operation, only one active material generation reaction occurs. Further, in the (X 2 ) electrode of the comparative example, the active material generation reaction occurs twice in the second and subsequent active material filling operations.
The generated active material is an active material having a small bulk density due to the reaction with the liquid alkali. In addition, an active material generation reaction occurs on the surface, not on the deep part of the substrate. From these facts, it is considered that the amount of the active material charged after the second time is reduced as described above. [Experiment 2] The electrode (A) produced by the production method of the present invention and the electrode (X 1 ) and (X 2 ) produced by the production method of the comparative example
The utilization rate of the active material was measured for the electrodes. In the experiment, the active material filling amounts of all the electrode plates were set to be the same. The experimental conditions are such that the battery is charged in an aqueous solution of potassium hydroxide at a theoretical capacity of 5 hours and then discharged at a rate of 3 hours.

【0017】この結果、図示はしないが、(A)電極及
び(X1 )電極,(X2 )電極共に、同一の活物質利用
率であることを確認した。したがって、嵩密度の大小に
関わらず、活物質の利用率は同一であることがわかる。
As a result, although not shown, it was confirmed that the (A) electrode, the (X 1 ) electrode, and the (X 2 ) electrode had the same active material utilization rate. Therefore, it is understood that the utilization rate of the active material is the same regardless of the magnitude of the bulk density.

【0018】[0018]

【発明の効果】以上説明したように本発明によれば、固
体状態のアルカリと酸性ニッケル塩水溶液との反応によ
り活物質である水酸化ニッケルが生成するので、水酸化
ニッケルの嵩密度が大きくなる。加えて、ニッケル焼結
基板の孔の深部から水酸化ニッケルを生成させることが
できる。これらのことから、効率良く活物質充填操作を
行うことができる。
As described above, according to the present invention, the reaction between the solid-state alkali and the aqueous acidic nickel salt solution produces nickel hydroxide, which is an active material, so that the bulk density of nickel hydroxide increases. . In addition, nickel hydroxide can be generated from the deep part of the hole of the nickel sintered substrate. From these, the active material filling operation can be performed efficiently.

【0019】更に、2回目以降の活物質充填操作におい
ては、1回の活物質充填操作で2回の活物質生成反応が
生じることになるので、活物質充填作業の作業回数を減
らすことができ、この結果生産性を向上させることがで
きる。加えて、酸性ニッケル塩含浸液にニッケル焼結基
板を浸漬する回数を減らすことができるので、ニッケル
焼結基板の腐食が抑制され、この結果、本発明の製造方
法による電極を用いた電池のサイクル特性を向上させる
ことができるといった優れた効果を奏する。
Further, in the second and subsequent active material filling operations, two active material generation reactions occur in one active material filling operation, so that the number of active material filling operations can be reduced. As a result, productivity can be improved. In addition, since the number of times the nickel sintered substrate is immersed in the acidic nickel salt impregnation liquid can be reduced, the corrosion of the nickel sintered substrate is suppressed, and as a result, the cycle of the battery using the electrode according to the manufacturing method of the present invention is reduced. Excellent effects such as improvement of characteristics can be obtained.

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

【図1】本発明の製造方法にて作製した(A)電極と比
較例の製造方法にて作製した(X1 )電極,(X2 )電
極とにおいて、1〜5回目の活物質充填操作における活
物質充填量を示すグラフである。
FIG. 1 shows the first to fifth active material filling operations for the (A) electrode manufactured by the manufacturing method of the present invention and the (X 1 ) electrode and (X 2 ) electrode manufactured by the manufacturing method of the comparative example. 4 is a graph showing the amount of active material charged in FIG.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭64−648(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 4/24 - 4/26 H01M 4/32 ────────────────────────────────────────────────── (5) References JP-A-64-648 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) H01M 4/24-4/26 H01M 4 / 32

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 多孔性ニッケル基板を酸性ニッケル塩含
浸水溶液に浸漬する第1工程と、上記基板をアルカリ水
溶液に浸漬して前記酸性ニッケル塩を活物質化させる第
2工程と、前記第2工程で基板に保持されたアルカリ水
溶液をそのまま保持させつつ乾燥を行う第3工程とから
成る活物質充填操作を、複数回行うことを特徴とするア
ルカリ蓄電池用ニッケル電極の製造方法。
1. A first step in which a porous nickel substrate is immersed in an acidic nickel salt impregnated aqueous solution, a second step in which the substrate is immersed in an alkaline aqueous solution to convert the acidic nickel salt into an active material, and the second step. Alkaline water held on substrate by
3. A method for producing a nickel electrode for an alkaline storage battery, comprising performing a plurality of times of an active material filling operation including a third step of drying while keeping the solution as it is.
JP34307791A 1991-12-25 1991-12-25 Method for producing nickel electrode for alkaline storage battery Expired - Fee Related JP3272009B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34307791A JP3272009B2 (en) 1991-12-25 1991-12-25 Method for producing nickel electrode for alkaline storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34307791A JP3272009B2 (en) 1991-12-25 1991-12-25 Method for producing nickel electrode for alkaline storage battery

Publications (2)

Publication Number Publication Date
JPH05174815A JPH05174815A (en) 1993-07-13
JP3272009B2 true JP3272009B2 (en) 2002-04-08

Family

ID=18358767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34307791A Expired - Fee Related JP3272009B2 (en) 1991-12-25 1991-12-25 Method for producing nickel electrode for alkaline storage battery

Country Status (1)

Country Link
JP (1) JP3272009B2 (en)

Also Published As

Publication number Publication date
JPH05174815A (en) 1993-07-13

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