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JPH0756799B2 - Method for producing hydrogen storage alloy negative electrode - Google Patents
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JPH0756799B2 - Method for producing hydrogen storage alloy negative electrode - Google Patents

Method for producing hydrogen storage alloy negative electrode

Info

Publication number
JPH0756799B2
JPH0756799B2 JP61287903A JP28790386A JPH0756799B2 JP H0756799 B2 JPH0756799 B2 JP H0756799B2 JP 61287903 A JP61287903 A JP 61287903A JP 28790386 A JP28790386 A JP 28790386A JP H0756799 B2 JPH0756799 B2 JP H0756799B2
Authority
JP
Japan
Prior art keywords
hydrogen storage
storage alloy
negative electrode
battery
aqueous solution
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
JP61287903A
Other languages
Japanese (ja)
Other versions
JPS63141258A (en
Inventor
良夫 森脇
明美 新谷
孝治 蒲生
勉 岩城
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 JP61287903A priority Critical patent/JPH0756799B2/en
Publication of JPS63141258A publication Critical patent/JPS63141258A/en
Publication of JPH0756799B2 publication Critical patent/JPH0756799B2/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
    • H01M4/242Hydrogen storage electrodes
    • 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
    • H01M4/36Selection of substances as active materials, active masses, active liquids
    • H01M4/38Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/383Hydrogen absorbing alloys
    • 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、水素を可逆的に吸蔵・放出する水素吸蔵合金
を用いる水素吸蔵合金負極の製造方法に関するもので、
無公害で高エネルギー密度のアルカリ蓄電池を提供でき
るものである。
Description: TECHNICAL FIELD The present invention relates to a method for producing a hydrogen storage alloy negative electrode using a hydrogen storage alloy that reversibly stores and releases hydrogen.
It is possible to provide a pollution-free and high energy density alkaline storage battery.

従来の技術 各種の電源のうち二次電池としては、鉛蓄電池とアルカ
リ蓄電池とが広く使われている。
2. Description of the Related Art Lead storage batteries and alkaline storage batteries are widely used as secondary batteries among various power sources.

アルカリ蓄電池のうち、最も広く使われているのは、ニ
ッケル−カドミウム蓄電池である。この電池は性能的に
かなり優れているが、依然として高エネルギー密度や無
公害への期待が高く新しい電池系が検討されている。
The most widely used alkaline storage battery is the nickel-cadmium storage battery. Although this battery is considerably superior in performance, there are still high expectations for high energy density and pollution-free, and new battery systems are being investigated.

例えばこの中で負極をカドミウムに代わって亜鉛が取り
上げられてきたが、よく知られているように寿命に問題
があるので広い実用化には至っていない。最近注目され
てきたのは水素を可逆的に吸蔵・放出する水素吸蔵合金
を負極に用いるアルカリ蓄電池である。この場合は、カ
ドミウムや亜鉛などと同じ取扱いで電池を構成でき、実
際の放電可能な容量密度をカドミウムより大きくできる
ことや亜鉛のようなデンドライトの形成などがないこと
などから、高エネルギー密度で長寿命、無公害のアルカ
リ蓄電池として有望である。
For example, zinc has been taken up in place of cadmium as the negative electrode, but it is not widely used because it has a problem in life as well known. Recently, attention has been paid to alkaline storage batteries that use a hydrogen storage alloy that reversibly stores and releases hydrogen as the negative electrode. In this case, a battery can be constructed in the same way as cadmium and zinc, and the actual dischargeable capacity density can be made larger than that of cadmium, and there is no formation of dendrite such as zinc. Promising as a pollution-free alkaline storage battery.

ところが、水素吸蔵合金は水素の吸蔵・放出を繰り返す
ことにより微粉化が一層進み、これを電池用電極の構成
材料とした場合に、電極の変形や脱落をもたらす。ま
た、アルカリ蓄電池、特に密閉形アルカリ蓄電池でノイ
マン方式でガスの吸収を行なう系では、正極から発生す
る酸素ガスによって表面が酸化を受けて水素の吸蔵・放
出能力の低下を生ずる。
However, the hydrogen storage alloy is further pulverized by repeating storage and release of hydrogen, and when this is used as a constituent material of a battery electrode, the electrode is deformed or comes off. Further, in a system that absorbs gas by the Neumann method in an alkaline storage battery, particularly a sealed alkaline storage battery, the surface is oxidized by oxygen gas generated from the positive electrode, and the hydrogen storage / release capacity is reduced.

従って、水素吸蔵合金を負極に使用する場合には電極に
する前に微粉化を進めておき、電池内で充放電をしても
それ以上微粉化しないようにすることや、酸素ガスによ
って性能が低下しないように耐酸化性の改善が重要であ
る。これらの解決のため従来から、出来るだけ細かく水
素吸蔵合金を粉砕することや水素吸蔵合金の表面を耐酸
化性の被膜で被覆することなどが検討されている。ま
た、粉砕した水素吸蔵合金をアルカリ水溶液で表面処理
することにより長寿命化を図ることも検討されていた。
Therefore, when using a hydrogen storage alloy for the negative electrode, advance the pulverization before making it into an electrode so that it will not be pulverized further even if charged and discharged in the battery, and the performance will be improved by oxygen gas. It is important to improve the oxidation resistance so as not to decrease. In order to solve these problems, it has been studied to pulverize the hydrogen storage alloy as finely as possible and to coat the surface of the hydrogen storage alloy with an oxidation resistant coating. Further, it has been considered to extend the life of the crushed hydrogen storage alloy by surface-treating it with an alkaline aqueous solution.

発明が解決しようとする問題点 水素吸蔵合金を負極に用いるアルカリ蓄電池は、このよ
うに高エネルギー密度の向上には有効であるが微粉化や
酸化に問題があった。
Problems to be Solved by the Invention An alkaline storage battery using a hydrogen storage alloy for a negative electrode is effective in improving high energy density as described above, but has problems in pulverization and oxidation.

本発明はこの水素吸蔵合金をアルカリ蓄電池の水素吸蔵
合金負極に使用するとき、これまで問題であった微粉化
や酸化を解決すると同時に簡易な水素吸蔵合金の製造方
法を提供することを目的とする。
It is an object of the present invention to provide a simple method for producing a hydrogen storage alloy while using the hydrogen storage alloy for a hydrogen storage alloy negative electrode of an alkaline storage battery to solve the problems such as pulverization and oxidation which have been problems so far. .

問題点を解決するための手段 本発明は水素吸蔵合金を機械的に粉砕する工程をアルカ
リ水溶液中で行なった後、少なくとも水洗と乾燥を施し
その後水素吸蔵合金負極にすることを特徴とする水素吸
蔵合金負極の製造方法である。そして、好ましくはアル
カリ水溶液が比重1.05〜1.50の苛性アルカリであり、か
つそのアルカリ水溶液を30〜80℃に加温したものであ
り、水素吸蔵合金を機械的に粉砕する工程が特にボール
ミル法であることが良い。
Means for Solving the Problems The present invention is characterized in that the step of mechanically crushing a hydrogen storage alloy is carried out in an alkaline aqueous solution, and then at least washing and drying are performed to obtain a hydrogen storage alloy negative electrode. It is a manufacturing method of an alloy negative electrode. And, preferably the alkaline aqueous solution is a caustic alkali having a specific gravity of 1.05 to 1.50, and the alkaline aqueous solution is heated to 30 to 80 ° C., and the step of mechanically pulverizing the hydrogen storage alloy is particularly a ball mill method. Is good.

作用 粉砕はアルカリ水溶液中で行なうことによって、比較的
粉砕され難い不純物相がアルカリ水溶液に溶解されるこ
とにより、より微細な粉砕が短時間に可能である。
By carrying out the grinding in an alkaline aqueous solution, the impurity phase, which is relatively hard to grind, is dissolved in the alkaline aqueous solution, so that finer grinding can be performed in a short time.

実施例 まず、本発明の構成について概念的にのべる。水素吸蔵
合金をアルカリ蓄電池の負極として使用する場合、これ
までから合金溶解によって得た水素吸蔵合金を予め水素
化や機械的な手段で粉砕することが行なわれている。
Example First, the structure of the present invention will be described conceptually. When a hydrogen storage alloy is used as a negative electrode of an alkaline storage battery, the hydrogen storage alloy obtained by melting the alloy has been previously pulverized by hydrogenation or mechanical means.

本発明は、この粉砕工程を湿式の機械的粉砕法を採用す
るものであり、この場合アルカリ水溶液中で行なうとこ
ろに特徴がある。
The present invention employs a wet mechanical pulverization method for this pulverization step, and is characterized in that it is carried out in an alkaline aqueous solution.

これまで水素吸蔵合金を製造後、微粉末に粉砕した後ア
ルカリ水溶液中で水素吸蔵合金粉末もしくは水素吸蔵合
金負極をアルカリ処理することが行なわれていた。この
アルカリ処理は、アルカリ蓄電池の電解液である苛性ア
ルカリに溶解し易い成分を予めこの処理によって除去し
たり、水素吸蔵合金粉末表面をアルカリに馴染ますこと
によって密閉電池にしたとき、長寿命化が可能になるな
どの効果がある。
Up to now, it has been practiced to manufacture a hydrogen storage alloy, pulverize it into fine powder, and then subject the hydrogen storage alloy powder or the hydrogen storage alloy negative electrode to alkali treatment in an alkaline aqueous solution. This alkaline treatment will prolong the life of sealed batteries by removing components that are easily dissolved in caustic alkali, which is the electrolyte of alkaline storage batteries, or by accommodating the surface of the hydrogen-absorbing alloy powder into alkalis to make sealed batteries. It has the effect of being possible.

すなわち、これまでそれぞれ別々に行なっていた粉砕工
程とアルカリ処理工程を同時に行なうことにより工程を
簡易にするとともに、二つの工程を同時に行なうことに
よってこれまでの粉砕をより効果的に行なおうとするも
のである。ここで重要なことは、単に別々に粉砕とアル
カリ処理を行なって得られる水素吸蔵合金負極よりも本
発明のように苛性アルカり中で粉砕して得られた水素吸
蔵合金負極は、より優れた寿命特性を発揮することであ
る。その理由としては、水素吸蔵合金粉砕時に新しい合
金の粉砕面が直ちに苛性アルカリに触れることによるも
のと推定される。粉砕はアルカリ水溶液中で行なうこと
によって、比較的粉砕されにくい不純物相がアルカリ水
溶液に溶解されることにより、より微細な粉砕が短時間
に可能である。
That is, the crushing step and the alkali treatment step, which have been performed separately respectively, are simplified at the same time, and at the same time, the two steps are simultaneously performed so that the crushing up to now can be performed more effectively. Is. What is important here is that the hydrogen storage alloy negative electrode obtained by crushing in a caustic alkali as in the present invention is superior to the hydrogen storage alloy negative electrode obtained by simply performing pulverization and alkali treatment separately. It is to exhibit life characteristics. It is presumed that the reason is that the crushed surface of the new alloy immediately comes into contact with caustic when crushing the hydrogen storage alloy. By performing the pulverization in the alkaline aqueous solution, the impurity phase which is relatively difficult to be pulverized is dissolved in the alkaline aqueous solution, so that finer pulverization can be performed in a short time.

さらに粉砕時での発熱もよい影響を与えている。つま
り、特別な加熱を行なわなくてもアルカリ中粉砕は加熱
を促進している。
Furthermore, the heat generated during crushing also has a positive effect. That is, crushing in alkali promotes heating without special heating.

以下、本発明の具体的実施例について説明する。Hereinafter, specific examples of the present invention will be described.

市販のMn(ミッシュメタル),Ni,Co,Mn,Alの各原材料を
一定の組成比に秤量してアルゴンアーク溶解炉によって
MmNi3.8Co0.5Mn0.4Al0.3合金を製造した。ついでこの合
金を公知の方法に従って真空熱処理炉で熱処理した。
Commercially available raw materials such as Mn (Misch metal), Ni, Co, Mn, and Al are weighed to a certain composition ratio, and are measured by an argon arc melting furnace.
An MmNi 3.8 Co 0.5 Mn 0.4 Al 0.3 alloy was produced. The alloy was then heat treated in a vacuum heat treatment furnace according to known methods.

この合金試料をアルミナ製のポットとボールからなるボ
ールミルに入れ、さらに比重1.30の水酸化カリウム水溶
液を合金100gに対し50mlの割合で加えた。この状態でボ
ールミル粉砕を10時間室温下で行なった。なおこの粉砕
終了時のボールミル内の温度は約40℃であった。粉砕し
た水素吸蔵合金粉末を水洗し、その後乾燥した。このア
ルカリ水溶液中で粉砕した合金試料の粒度分布測定をし
たところ全て50ミクロン以下の微粉末になっていた。
The alloy sample was placed in a ball mill consisting of an alumina pot and balls, and an aqueous potassium hydroxide solution having a specific gravity of 1.30 was added at a ratio of 50 ml to 100 g of the alloy. In this state, ball milling was performed for 10 hours at room temperature. The temperature in the ball mill at the end of this pulverization was about 40 ° C. The crushed hydrogen storage alloy powder was washed with water and then dried. When the particle size distribution of the alloy sample crushed in this alkaline aqueous solution was measured, it was found to be a fine powder of 50 microns or less.

このようなアルカリ水溶液中で粉砕した水素吸蔵合金試
料をその後、ポリビニルアルコールなどの結着剤ととも
にペーストにし、ニッケルメッキを施したパンチングメ
タル板に塗着して乾燥を行い負極板Aを得た。
The hydrogen storage alloy sample crushed in such an alkaline aqueous solution was then made into a paste together with a binder such as polyvinyl alcohol, and the paste was applied to a nickel-plated punching metal plate and dried to obtain a negative electrode plate A.

このようにして得られた負極板Aを電池に組み込んだ。
電池としては、単2形の円筒密閉形ニッケル−水素蓄電
池を例にした。したがって、このようにして得られた負
極板Aを幅3.9cm、長さ26cmに裁断し、リード板を所定
の2カ所にスポット溶接により取り付けた。相手極とし
ては、公知の焼結式ニッケル極を選び、同じく幅3.9c
m、長さ22cmとして用いた。この場合もリード板を2カ
所取り付けた。
The negative electrode plate A thus obtained was incorporated into a battery.
As the battery, a C1-type cylindrical sealed nickel-hydrogen storage battery was taken as an example. Therefore, the negative electrode plate A thus obtained was cut into a width of 3.9 cm and a length of 26 cm, and the lead plates were attached by spot welding to two predetermined places. A well-known sintered nickel electrode was selected as the counter electrode and the width was 3.9c.
It was used as m and 22 cm in length. Also in this case, the lead plates were attached at two places.

セパレータとしては、ポリアミド不織布、電解液として
は、比重1.20の苛性カリ水溶液に水素化リチウムを20g/
L溶解して用いた。公称容量は3.0Ahである。この電池を
Aとする。
As the separator, a polyamide nonwoven fabric, and as the electrolytic solution, 20 g of lithium hydride in a caustic potash aqueous solution having a specific gravity of 1.20.
L was used after dissolving. The nominal capacity is 3.0 Ah. This battery is designated as A.

つぎに比較のために、従来の方法として先と同じMmNi
3.8Co0.5Mn0.4Al0.3合金を選びその水素吸蔵合金を機械
的に50ミクロン以下の粒径に粉砕した。所要時間は24時
間であった。その後40℃の比重1.30の水酸化カリウム水
溶液中に10時間浸漬しアルカリ処理を行なったものを同
様な方法で負極板Bとし、電池Bを得た。正極の容量律
則にしているのでこの電池の公称容量も3.0Ahである。
Next, for comparison, the same MmNi
3.8 Co 0.5 Mn 0.4 Al 0.3 alloy was selected and the hydrogen storage alloy was mechanically pulverized to a particle size of 50 microns or less. It took 24 hours. After that, a negative electrode plate B was obtained by immersing in an aqueous potassium hydroxide solution having a specific gravity of 1.30 at 40 ° C. for 10 hours and using the same method as a negative electrode plate B to obtain a battery B. Because of the capacity regulation of the positive electrode, the nominal capacity of this battery is 3.0 Ah.

さらに比較のために、先と同じ水素吸蔵合金で同じく24
時間機械的粉砕して50ミクロン以下にし、アルカリ処理
をしないで負極板Cを得、同様に公称容量3.0Ahの電池
Cを得た。
For further comparison, the same hydrogen storage alloy as before was also used for 24
Negative electrode plate C was obtained by mechanically pulverizing for 50 hours or less without alkaline treatment, and similarly, battery C having a nominal capacity of 3.0 Ah was obtained.

これらの電池を通常の充放電サイクル試験によって評価
した結果を説明する。
The results of evaluating these batteries by a normal charge / discharge cycle test will be described.

充電は、0.2C(5時間率)で130%まで、放電は0.5C
(2時間率)で終止電圧1.0Vとし充放電サイクルを繰り
返した。その結果A、B、Cの3種の電池とも100サイ
クル程度までは放電容量がほぼ3.0Ahであり、Cの電池
がA、Bの電池に比べてやや放電の端子電圧が低いこと
以外には大きな差異が見当らなかった。しかし、この充
放電サイクルをさらに繰り返して行くと電池Cは142サ
イクル目より急激に放電容量が低下した。また電池Bは
356サイクル目から低下が始まった。これに対して本発
明の電池Aは500サイクルまで異常が認められなかっ
た。
Charge up to 130% at 0.2C (5-hour rate), discharge at 0.5C
The charging / discharging cycle was repeated at a final voltage of 1.0 V (at a rate of 2 hours). As a result, the discharge capacities of the three types of batteries A, B, and C were approximately 3.0 Ah up to about 100 cycles, except that the C battery had a slightly lower discharge terminal voltage than the A and B batteries. No big difference was found. However, when this charging / discharging cycle was further repeated, the discharge capacity of Battery C dropped sharply from the 142nd cycle. Battery B is
The decrease started at the 356th cycle. On the other hand, in Battery A of the present invention, no abnormality was observed up to 500 cycles.

このことから本発明の電池Aは、最も寿命特性に優れて
いることが明らかになった。
From this, it was revealed that the battery A of the present invention has the most excellent life characteristics.

発明の効果 以上のように本発明の水素吸蔵合金負極の製造方法は、
これまでの水素吸蔵合金の粉砕工程とアルカリ処理工程
を同時に行なうものであり、製造工程の簡易化は当然で
あるが、特に電池の充放電寿命を改善する効果がある。
As described above, the method for producing the hydrogen storage alloy negative electrode of the present invention is
Since the pulverization step and the alkali treatment step of the hydrogen storage alloy that have been performed so far are performed at the same time, it is natural to simplify the manufacturing process, but it is particularly effective in improving the charge / discharge life of the battery.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】水素吸蔵合金を機械的に粉砕する工程をア
ルカリ水溶液中で行なった後、少なくとも水洗と乾燥を
施しその後水素吸蔵合金負極にすることを特徴とする水
素吸蔵合金負極の製造方法。
1. A method for producing a hydrogen storage alloy negative electrode, which comprises performing a step of mechanically pulverizing a hydrogen storage alloy in an alkaline aqueous solution, followed by at least washing and drying to obtain a hydrogen storage alloy negative electrode.
【請求項2】アルカリ水溶液が比重1.05〜1.50の苛性ア
ルカリであり、かつそのアルカリ水溶液を30〜80℃に加
温したことを特徴とする特許請求の範囲第1項記載の水
素吸蔵合金負極の製造方法。
2. The hydrogen storage alloy negative electrode according to claim 1, wherein the alkaline aqueous solution is a caustic alkali having a specific gravity of 1.05 to 1.50, and the alkaline aqueous solution is heated to 30 to 80 ° C. Production method.
【請求項3】水素吸蔵合金を機械的に粉砕する工程が特
にボールミル法である特許請求の範囲第1項または第2
項記載の水素吸蔵合金負極の製造方法。
3. The method according to claim 1, wherein the step of mechanically pulverizing the hydrogen storage alloy is a ball mill method.
Item 6. A method for producing a hydrogen storage alloy negative electrode according to the item.
【請求項4】水素吸蔵合金をアルカリ水溶液中で機械的
に粉砕する工程で100ミクロン以下の粒子径にすること
を特徴とする特許請求の範囲第1項、第2項または第3
項記載の水素吸蔵合金負極の製造方法。
4. A particle size of 100 μm or less in the step of mechanically grinding the hydrogen storage alloy in an alkaline aqueous solution, wherein the particle size is 100 μm or less.
Item 6. A method for producing a hydrogen storage alloy negative electrode according to the item.
JP61287903A 1986-12-03 1986-12-03 Method for producing hydrogen storage alloy negative electrode Expired - Lifetime JPH0756799B2 (en)

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JP61287903A JPH0756799B2 (en) 1986-12-03 1986-12-03 Method for producing hydrogen storage alloy negative electrode

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JP61287903A JPH0756799B2 (en) 1986-12-03 1986-12-03 Method for producing hydrogen storage alloy negative electrode

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JPS63141258A JPS63141258A (en) 1988-06-13
JPH0756799B2 true JPH0756799B2 (en) 1995-06-14

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JP2975625B2 (en) * 1989-02-16 1999-11-10 三洋電機株式会社 Hydrogen storage alloy electrode and method for producing the same
USRE34471E (en) * 1989-03-10 1993-12-07 Sanyo Electric Co., Ltd. Hydrogen-absorbing alloy electrode for use in an alkaline storage cell and its manufacturing method
JP2680669B2 (en) * 1989-03-10 1997-11-19 三洋電機株式会社 Hydrogen storage alloy electrode for alkaline storage battery
JP2572337B2 (en) * 1993-02-09 1997-01-16 古河電池株式会社 Nickel-hydrogen secondary battery
JP3016064B2 (en) * 1995-09-27 2000-03-06 古河電池株式会社 Method for producing hydrogen storage alloy powder for battery

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