JP2925591B2 - Method for producing hydrogen storage electrode - Google Patents
Method for producing hydrogen storage electrodeInfo
- Publication number
- JP2925591B2 JP2925591B2 JP1220831A JP22083189A JP2925591B2 JP 2925591 B2 JP2925591 B2 JP 2925591B2 JP 1220831 A JP1220831 A JP 1220831A JP 22083189 A JP22083189 A JP 22083189A JP 2925591 B2 JP2925591 B2 JP 2925591B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen storage
- electrode
- battery
- polyethylene oxide
- weight
- 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
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Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】 (イ) 産業上の利用分野 本発明は、アルカリ蓄電池の負極として用いられ、水
素を可逆的に吸蔵及び放出することのできる水素吸蔵電
極の製造方法に関するものである。The present invention relates to a method for producing a hydrogen storage electrode used as a negative electrode of an alkaline storage battery and capable of reversibly storing and releasing hydrogen.
(ロ) 従来の技術 従来から良く用いられている蓄電池としては、ニッケ
ルーカドミウム蓄電池、あるいは鉛蓄電池などがある
が、近年、これらの電池より軽量且つ高容量で高エネル
ギー密度となる可能性があるということで、水素吸蔵合
金を用いてなる水素吸蔵電極を負極に備えた金属−水素
アルカリ蓄電池が注目されている。(B) Conventional technology Conventionally used storage batteries include nickel-cadmium storage batteries and lead storage batteries. In recent years, there is a possibility that these batteries are lighter, have higher capacity and higher energy density than these batteries. Therefore, a metal-hydrogen alkaline storage battery having a negative electrode provided with a hydrogen storage electrode using a hydrogen storage alloy has attracted attention.
ところで、この種水素吸蔵電極は、充放電サイクルを
繰り返すことにより、水素吸蔵合金が微粉化し電極から
脱落して容量低下を招くと共に、電極の機械的強度の低
下を起こし、長期にわたって極板容量を維持することが
困難であるという問題点があった。このため、特開昭61
−66366号公報では、極板の機械的強度を高め、上記問
題点を解決する方法が提案されている。即ち、ポリテト
ラフルオロエチレンやポリエチレンオキサイドなどの複
数の結着剤を併用して用い、これらと水素吸蔵合金粉末
とを混練したペーストを、パンチングメタル等の導電性
支持体に塗着して電極を作製することにより、前記結着
剤により水素吸蔵合金を強固に保持することを可能とし
ている。By the way, in this kind of hydrogen storage electrode, by repeating the charge and discharge cycle, the hydrogen storage alloy is pulverized and drops from the electrode to cause a decrease in capacity, and also causes a decrease in the mechanical strength of the electrode, and the electrode capacity is reduced for a long time. There was a problem that it was difficult to maintain. For this reason, JP
Japanese Patent Application Publication No. 66366/1999 proposes a method for increasing the mechanical strength of the electrode plate and solving the above-mentioned problems. That is, a plurality of binders such as polytetrafluoroethylene and polyethylene oxide are used in combination, and a paste obtained by kneading these with a hydrogen storage alloy powder is applied to a conductive support such as a punching metal to form an electrode. By manufacturing, the hydrogen storage alloy can be held firmly by the binder.
しかしながら、電極の容量を大きくするためには、結
着剤のような絶縁性の不純物の添加剤は少ない程良く、
上記公報の実施例で示されるように結着剤の添加量の合
計を6%にもすると、どうしても電極の容量を充分に大
きくすることができない。However, in order to increase the capacity of the electrode, the smaller the additive of the insulating impurity such as the binder, the better,
If the total amount of the binder added is 6% as shown in the examples of the above publication, the capacity of the electrode cannot be sufficiently increased.
他方、水素吸蔵電極における導電性支持体に合金を保
持させる結着効果をみると、ポリテトラフルオロエチレ
ン等のフッ素樹脂結着剤に比べて、ヒドロキシプロピル
セルロースやポリエチレンオキサイド等の水溶性高分子
結着剤の方が少量の添加で効果を得ることができる。と
ころが、アルカリ蓄電池用のペースト式電極として従来
から結着剤を用いて作製されているペースト式カドミウ
ム極では、前記水溶性高分子結着剤としてポリエチレン
オキサイドを添加すると、水素発生の過電圧を低くし、
水素ガスが発生し易くなり、カドミウム極の充電効率を
低下させる。このようにペースト式カドミウム極では、
結着剤の種類により電池性能を左右されることがあり、
一般にヒドロキシプロピルセルロース等を結着剤として
使用することが多く、ポリエチレンオキサイドは使用さ
れていなかった。On the other hand, regarding the binding effect of holding the alloy on the conductive support in the hydrogen storage electrode, a water-soluble polymer binding agent such as hydroxypropylcellulose and polyethylene oxide is compared with a fluorine resin binding agent such as polytetrafluoroethylene. The effect of the adhesive can be obtained with a small amount of addition. However, in the past-type cadmium electrode conventionally manufactured using a binder as a paste-type electrode for an alkaline storage battery, the addition of polyethylene oxide as the water-soluble polymer binder reduces the overvoltage of hydrogen generation. ,
Hydrogen gas is easily generated, which lowers the charging efficiency of the cadmium electrode. In this way, the paste-type cadmium electrode
Battery performance may be affected by the type of binder,
Generally, hydroxypropyl cellulose or the like is often used as a binder, and polyethylene oxide has not been used.
(ハ) 発明が解決しようとする課題 本発明は、電極容量が大きく、しかも機械的強度を十
分に保つことができる水素吸蔵電極の製造方法を提供し
ようとするものである。(C) Problems to be Solved by the Invention The present invention aims to provide a method for producing a hydrogen storage electrode that has a large electrode capacity and can maintain sufficient mechanical strength.
(ニ) 課題を解決するための手段 本発明の水素吸蔵電極の製造方法は、水素吸蔵合金粉
末と、少なくともポリエチレンオキサイドを含む結着剤
と、分散媒とを混練したスラリーを作製し、このスラリ
ーを平面的な導電性支持体上に塗着し、保持させる電極
の製造方法であって、前記結着剤の総量は前記合金に対
して2重量%以下の量であり、且つ、前記ポリエチレン
オキサイドを前記合金に対して少なくとも0.5重量%以
上を含むとともに、前記スラリーの粘度を10,000〜100,
000mPa・sに規制することを特徴とするものである。(D) Means for Solving the Problems The method for producing a hydrogen storage electrode according to the present invention comprises preparing a slurry in which a hydrogen storage alloy powder, a binder containing at least polyethylene oxide, and a dispersion medium are kneaded, and Is applied onto a planar conductive support and held, wherein the total amount of the binder is 2% by weight or less based on the alloy, and the polyethylene oxide is used. At least 0.5% by weight or more based on the alloy, and the viscosity of the slurry is 10,000 to 100,
It is characterized in that it is regulated to 000 mPa · s.
(ホ) 作用 水素吸蔵電極では、充電の際に水素吸蔵合金上に吸着
した水素原子は水素分子としてガス発生をする前に、速
やかに水素吸蔵合金内部に拡散し吸蔵されるため、電極
の結着剤としてポリエチレンオキサイドを用いた場合に
おいても、他の粘性剤を用いた場合に比べて水素ガス発
生量が多くなるということはなく、したがって、充電電
流が水素ガス発生に用いられることによる充電効率の低
下は生じ難い。(E) Function In the hydrogen storage electrode, the hydrogen atoms adsorbed on the hydrogen storage alloy during charging are diffused and absorbed into the hydrogen storage alloy immediately before generating gas as hydrogen molecules, so that the electrode connection Even when polyethylene oxide is used as the adhesive, the amount of hydrogen gas generated does not increase as compared with the case where other viscous agents are used, and therefore, the charging efficiency due to the charging current being used for hydrogen gas generation Is unlikely to decrease.
また、ポリエチレンオキサイドはヒトロキシプロピル
セルロース等に比べて、粘性が高く、結着効果も高いの
で、少量の添加で十分なスラリー粘度と結着力を得るこ
とができ、更にポリエチレンオキサイドは直鎖状高分子
であるため、活性基が高分子の末端に存在するだけとな
り、化学的にも非常に安定で有利である。In addition, polyethylene oxide has a higher viscosity and a higher binding effect than human hydroxypropylcellulose and the like, so that it is possible to obtain a sufficient slurry viscosity and binding power with a small amount of addition. Since it is a molecule, the active group only exists at the terminal of the polymer, and it is chemically very stable and advantageous.
このポリエチレンオキサイドを電極の結着剤として用
い、水素吸蔵合金に対する添加量を0.5重量%以上にす
ると、電極強度を充分に維持することができる。また、
結着剤としてはポリエチレンオキサイド単独またはポリ
エチレンオキサイドと他の結着剤との組み合わせで用い
ても良いが、結着剤の総量が水素吸蔵合金に対して2重
量%を超えると、電極の導電性が低下すると同時に結着
剤が水素吸蔵合金表面を被覆して水素の吸蔵効率を低下
させるため、2重量%以下にする必要がある。また、ス
ラリーの粘度は10,000〜100,000mPa・sの範囲にするこ
とで、導電性支持体にスラリーを均一に保持させること
ができる。When this polyethylene oxide is used as a binder for the electrode and the amount added to the hydrogen storage alloy is 0.5% by weight or more, the electrode strength can be sufficiently maintained. Also,
As the binder, polyethylene oxide alone or a combination of polyethylene oxide and another binder may be used. However, when the total amount of the binder exceeds 2% by weight with respect to the hydrogen storage alloy, the conductivity of the electrode is reduced. At the same time, the binder needs to be 2% by weight or less because the binder covers the surface of the hydrogen storage alloy to lower the hydrogen storage efficiency. Further, by setting the viscosity of the slurry in the range of 10,000 to 100,000 mPa · s, the slurry can be uniformly held on the conductive support.
(ヘ) 実施例 本発明の実施例を以下に説明し、比較例との対比に言
及する。(F) Examples Examples of the present invention will be described below, and reference will be made to comparisons with comparative examples.
[実施例1] 市販されているミッシュメタル(Mm)、ニッケル、コ
バルト、マンガンの原料を一定の組成比に秤量し、アー
ク溶解炉を用いて組成式MmNi3Co1.4Mn0.6で表わされる
合金を作製した後、機械的に粉砕して平均粒径50μmの
水素吸蔵合金粉末を得た。次いで、この水素吸蔵合金に
対し1重量%のポリエチレンオキサイドと、分散媒とし
ての水を前記合金に加えて混練し、30,000mPa・sの粘
度のスラリーを作製した。尚、ここにおいて、スラリー
の粘度は、東京計器(株)製B型粘度計B8U型を使用
し、スピンドルT−B、回転速度20r.p.mで測定した値
である。[Example 1] misch commercially available metal (Mm), nickel, cobalt, manganese raw material was weighed into a predetermined composition ratio, the alloy represented by the composition formula MmNi 3 Co 1.4 Mn 0.6 using an arc melting furnace After the preparation, it was pulverized mechanically to obtain a hydrogen storage alloy powder having an average particle diameter of 50 μm. Next, 1% by weight of polyethylene oxide and water as a dispersion medium were added to the hydrogen-absorbing alloy and kneaded, and a slurry having a viscosity of 30,000 mPa · s was produced. Here, the viscosity of the slurry is a value measured using a B-type viscometer B8U manufactured by Tokyo Keiki Co., Ltd. at a spindle TB and a rotation speed of 20 rpm.
このようにして作製したスラリーを容器内に入れ、こ
の容器内にニッケルメッキを施したパンチングメタルか
らなる導電性支持体を通過させ引き上げることにより、
支持体表面に前記スラリーを塗着し、乾燥及び加圧を行
ない本発明による水素吸蔵電極を得た。The slurry thus prepared is put in a container, and the container is passed through a conductive support made of punched metal plated with nickel and pulled up.
The slurry was applied to the surface of a support, dried and pressed to obtain a hydrogen storage electrode according to the present invention.
この電極を負極とし、正極として焼結式ニッケル極を
使用して、これら正、負極の間に不織布からなるセパレ
ータを介して捲回するとにより渦巻電極体を得た。そし
て、この渦巻電極体を電池外装缶に挿入し、30重量%の
水酸化カリウム水溶液を電解液として注液した後、封口
して公称容量1200mAHの密閉型ニッケル−水素アルカリ
蓄電池を組み立てた。こうして作製した電池を本発明電
池Aとする。This electrode was used as a negative electrode, a sintered nickel electrode was used as a positive electrode, and a spiral electrode body was obtained by winding the positive electrode and the negative electrode with a separator made of a nonwoven fabric interposed therebetween. Then, the spiral electrode body was inserted into a battery outer can, a 30% by weight aqueous solution of potassium hydroxide was injected as an electrolytic solution, and then sealed to assemble a sealed nickel-hydrogen alkaline storage battery having a nominal capacity of 1200 mAH. The battery thus manufactured is referred to as Battery A of the present invention.
また、上記実施例において、ポリエチレンオキサイド
の量を0.5重量%とし、その他は全く同一の条件で電池
を作製し、本発明電池Bとすると共に、同様にポリエチ
レンオキサイドの量を2重量%として電池を作製し、本
発明電池Cとする。In the above example, a battery was prepared under the same conditions except that the amount of polyethylene oxide was 0.5% by weight, and the other conditions were exactly the same as the battery B of the present invention. The battery was manufactured to be Battery C of the present invention.
[実施例2] 上記実施例1において、ポリエチレンオキサイドの量
を1重量%とし、更にポリテトラフルオロエチレンを1
重量%添加して同様にスラリーを得、その他は全く同一
の条件で電池を作製し、この電池を本発明電池Dとす
る。Example 2 In Example 1 described above, the amount of polyethylene oxide was set to 1% by weight, and
In the same manner as above, a slurry was obtained by adding the same by weight, and a battery was prepared under the same conditions as the other conditions, and this battery was designated as Battery D of the present invention.
[比較例1] 上記実施例1において、ポリエチレンオキサイドの量
を0.3重量%とし、その他は全く同一の条件で電池を作
製して比較電池Eとし、また、同様にポリエチレンオキ
サイドの量を3重量%として電池を作製して比較電池F
とする。Comparative Example 1 A battery was prepared under the same conditions as in Example 1 except that the amount of polyethylene oxide was 0.3% by weight, and the other conditions were exactly the same as Comparative Battery E. Similarly, the amount of polyethylene oxide was 3% by weight. As a comparative battery F
And
[比較例2] 上記実施例において、ポリエチレンオキサイドの量を
1重量%とし、更にポリテトラフルオロエチレンを5重
量%添加して同様にスラリーを得、その他は全く同一の
条件で電池を作製し、この電池を比較電池Gとする。[Comparative Example 2] In the above example, the amount of polyethylene oxide was set to 1% by weight, polytetrafluoroethylene was further added by 5% by weight, and a slurry was obtained in the same manner. This battery is referred to as Comparative Battery G.
こうして作製した電池を夫々120mAの電流で16時間充
電した後、240mAの電流で放電し、電池電圧が1.0Vにな
った時点で放電を停止するサイクル条件で、充放電サイ
クル試験を行なった。この結果を第1図に示す。尚、図
中、電池容量は電池Aの初期容量を100%として示して
いる。Each of the batteries thus produced was charged at a current of 120 mA for 16 hours, then discharged at a current of 240 mA, and a charge / discharge cycle test was performed under a cycle condition in which the discharge was stopped when the battery voltage reached 1.0 V. The result is shown in FIG. In the drawing, the battery capacity is shown assuming that the initial capacity of the battery A is 100%.
第1図から明らかなように、本発明電池A〜Dは、比
較電池E〜Gより、サイクル特性が優れることがわか
る。As is clear from FIG. 1, the batteries A to D of the present invention have better cycle characteristics than the comparative batteries EG.
このように本発明電池の特性が優れたのは、結着剤と
してのポリエチレンオキサイドの添加量が、水素吸蔵合
金に対して0.5重量%以上添加しており、且つ結着剤を
総量が2重量%以下となっているため、水素吸蔵電極の
強度を維持しつつ、電極の導電性の低下及び水素吸蔵効
率の低下を最小限に抑制することができたからと考えら
れる。Thus, the battery of the present invention was excellent in characteristics because the amount of polyethylene oxide added as a binder was 0.5% by weight or more based on the hydrogen storage alloy, and the total amount of the binder was 2% by weight. %, The decrease in the conductivity of the electrode and the decrease in the hydrogen storage efficiency can be suppressed to a minimum while maintaining the strength of the hydrogen storage electrode.
これに対し、比較電池Eでは、ポリエチレンオキサイ
ドを0.3重量%しか添加しておらず、水素吸蔵電極の強
度を充分に維持することができなかったため、サイクル
の進行に伴って水素吸蔵合金の電極からの脱落が生じ、
電池容量が低下している。比較電池Fでは、ポリエチレ
ンオキサイドを3重量%添加しており、水素吸蔵電極の
強度は充分となるが、ポリエチレンオキサイドの添加量
が多いため、電極の導電性が低下すると同時に、ポリエ
チレンオキサイドが水素吸蔵合金表面を被覆し、水素の
吸蔵効率を低下させる。したがって、サイクルの初期よ
り電池容量が低くなり、また、サイクルの進行に伴って
負極から発生する水素ガスにより電池内部ガス圧が増加
して行き、電池の安全弁が作動することによって電解液
の漏液が起こり電池容量が低下する。また、比較電池G
では、ポリエチレンオキサイドは1重量%しか添加して
いないものの、ポリテトラフルオロエチレンを5重量%
添加しているため、比較電池Eと同様に水素吸蔵電極の
導電性か低下して、充分に性能を得ることができない。On the other hand, in the comparative battery E, only 0.3% by weight of polyethylene oxide was added, and the strength of the hydrogen storage electrode could not be sufficiently maintained. Fall off,
Battery capacity is low. In Comparative Battery F, polyethylene oxide was added in an amount of 3% by weight, and the strength of the hydrogen storage electrode was sufficient. However, since the amount of polyethylene oxide added was large, the conductivity of the electrode was lowered, and at the same time, the polyethylene oxide stored hydrogen. Covers the alloy surface and reduces hydrogen storage efficiency. Therefore, the battery capacity becomes lower than at the beginning of the cycle, and the internal gas pressure of the battery increases due to the hydrogen gas generated from the negative electrode as the cycle progresses, and the electrolyte leaks due to the operation of the battery safety valve. Occurs and the battery capacity decreases. In addition, the comparative battery G
Although only 1% by weight of polyethylene oxide is added, 5% by weight of polytetrafluoroethylene is added.
Since it is added, the conductivity of the hydrogen storage electrode is reduced similarly to the comparative battery E, so that sufficient performance cannot be obtained.
また、スラリーの粘度については上記実施例では30,0
00mPa・sとして使用したが、本発明者らの詳細な試験
の結果、粘度が100,000mPa・sを超えた場合、及び10,0
00mPa・sより低くなった場合には、スラリーをパンチ
ングメタルからなる導電性支持体に均一に塗着し保持さ
せることができなかった。これは、水素吸蔵合金粉末の
粒子形状がくさび形であるため、非常にすべりが悪いこ
と、また、真比重が8.0g/cc以上と非常に重い事に起因
するものである。以上の結果より、スラリーの粘度は1
0,000mPa・s以上で100,000mPa・s以上であることが望
ましい。The viscosity of the slurry was 30,0 in the above example.
It was used as 00 mPas, but as a result of detailed tests by the present inventors, when the viscosity exceeded 100,000 mPas,
When it was lower than 00 mPa · s, the slurry could not be uniformly applied to and held on the conductive support made of punched metal. This is due to the fact that the hydrogen storage alloy powder has a wedge shape, so that the slip is very poor and the true specific gravity is 8.0 g / cc or more, which is very heavy. From the above results, the viscosity of the slurry is 1
Desirably, it is not less than 0,000 mPa · s and not less than 100,000 mPa · s.
(ト) 発明の効果 本発明の水素吸蔵電極の製造方法は、ポリエチレンオ
キサイドを水素吸蔵合金に対して少なくとも0.5重量%
以上含んだ結着剤を用い、且つ、結着剤の総量は前記合
金に対して2重量%以下にするとともに、活物質スラリ
ーの粘度を10,000〜100,000mPa・sに規制して平面的な
導電性支持体上に前記スラリー塗着しているため、電極
強度を維持しつつ、電極の導電性の低下及び水素吸蔵効
率の低下を抑制でき、高容量で且つ長寿命の水素吸蔵電
極が得られる,また、導電性支持体に活物質スラリーを
均一に保持させることができるため、水素吸蔵電極の生
産性を向上させることが可能である,(G) Effect of the Invention The method for producing a hydrogen storage electrode of the present invention is characterized in that polyethylene oxide is used in an amount of at least 0.5% by weight based on the hydrogen storage alloy.
The binder contained above is used, and the total amount of the binder is set to 2% by weight or less based on the alloy, and the viscosity of the active material slurry is regulated to 10,000 to 100,000 mPa · s, so that the planar conductive property is controlled. Since the slurry is coated on the porous support, it is possible to suppress a decrease in the conductivity of the electrode and a decrease in the hydrogen storage efficiency while maintaining the electrode strength, and to obtain a high-capacity and long-life hydrogen storage electrode. Further, since the active material slurry can be uniformly held on the conductive support, the productivity of the hydrogen storage electrode can be improved.
第1図は本発明による電極を備えた電池と比較電池のサ
イクル特性比較図である。FIG. 1 is a cycle characteristic comparison diagram of a battery having an electrode according to the present invention and a comparative battery.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) H01M 4/24 - 4/26 H01M 4/62 ──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) H01M 4/24-4/26 H01M 4/62
Claims (1)
レンオキサイドを含む結着剤と、分散媒とを混練したス
ラリーを作製し、このスラリーを平面的な導電性支持体
上に塗着し、保持させる電極の製造方法であって、前記
結着剤の総量は前記合金に対して2重量%以下の量であ
り、且つ、前記ポリエチレンオキサイドを前記合金に対
して少なくとも0.5重量%以上含むとともに、前記スラ
リーの粘度を10,000〜100,000mPa・sに規制することを
特徴とする水素吸蔵電極の製造方法。1. A slurry is prepared by kneading a hydrogen storage alloy powder, a binder containing at least polyethylene oxide, and a dispersion medium, and the slurry is applied on a planar conductive support and held. A method for manufacturing an electrode, wherein the total amount of the binder is 2% by weight or less based on the alloy, and the polyethylene oxide contains at least 0.5% by weight or more based on the alloy, and the slurry A method for producing a hydrogen storage electrode, wherein the viscosity of the hydrogen storage electrode is regulated to 10,000 to 100,000 mPa · s.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1220831A JP2925591B2 (en) | 1989-08-28 | 1989-08-28 | Method for producing hydrogen storage electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1220831A JP2925591B2 (en) | 1989-08-28 | 1989-08-28 | Method for producing hydrogen storage electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0384857A JPH0384857A (en) | 1991-04-10 |
| JP2925591B2 true JP2925591B2 (en) | 1999-07-28 |
Family
ID=16757229
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1220831A Expired - Lifetime JP2925591B2 (en) | 1989-08-28 | 1989-08-28 | Method for producing hydrogen storage electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2925591B2 (en) |
-
1989
- 1989-08-28 JP JP1220831A patent/JP2925591B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0384857A (en) | 1991-04-10 |
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