JPH02234355A - Manufacture of hydrogen absorbing electrode - Google Patents
Manufacture of hydrogen absorbing electrodeInfo
- Publication number
- JPH02234355A JPH02234355A JP1055448A JP5544889A JPH02234355A JP H02234355 A JPH02234355 A JP H02234355A JP 1055448 A JP1055448 A JP 1055448A JP 5544889 A JP5544889 A JP 5544889A JP H02234355 A JPH02234355 A JP H02234355A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- hydrogen storage
- alkali
- hydrogen
- paste
- 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.)
- Granted
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/24—Electrodes for alkaline accumulators
- H01M4/242—Hydrogen storage electrodes
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、アルカリ電池に用いる水索吸蔵電極のII!
遣方法に関するものである.
従来の技術とその課題
水素吸蔵電極は、水素を可逆的に吸蔵し放出する水素吸
蔵合金を電極に用いたものである.水素吸蔵電極は、そ
の作動電位がカドミウム電極とほぼ等しく、しかも単位
体積当りの放電容量がカドミウム電極よりも著しく大き
い.したがって、この電極をアルカリ蓄電池の負極に用
いる場合には、カドミウムを負極に用いる場合とほぼ同
じ電圧で作動し、しかも放電容量がカドミウムを負極に
用いる場合よりも著しく大きいアルカリ蓄電池が得られ
ることが知られている.
この水素吸蔵電極は、従来は主として水素吸蔵合金と金
属とを焼結する方法および水素吸蔵合金と高分子結着剤
とを含むペーストを用いる方法で製作されていた.前者
の方法で製作された電極は、水素吸蔵合金と金属とが強
固に結合しているので、電極の強度が高いという点で有
利であるが、電極を製作する際に高温で長時間の焼結を
必要とする欠点がある.一方、ペーストを用いる後者の
方法《以下では、この方法を「ペースト式」と呼ぶ》は
、前者の方法と比較して短時間で電極を製作できる点で
有利である.
ペースト式の水素吸蔵電極の製造方法には次のものがあ
る.
すなわち、実公昭57−34678号公報に記載される
ように、水素吸蔵合金の粉末と耐アルカリ性の高分子結
着剤とを含むペースト状混合物を発泡メタルに充填する
方法である.この方法では、高分子結着剤として分散液
の状態のフッ素樹脂や溶液の状態のメチルセルロースを
用いている.そして、ペーストを乾燥させて、これらの
高分子の結着力を発現させている.
発明者は、この方法で水素吸蔵合金の製作を試みた結果
、次のような欠点を見出だした.すなわち、フッ素樹脂
を結着剤に用いる場合には、このフッ素樹脂が混練によ
って繊維状に変形しやすいので、ペーストを混練してい
る間にこのm維がからみあってペースト全体の粘度が高
くなり、ペーストの粘度を調節することが困難になって
ペーストの塗着量が不均一になるという不都合がある.
さらにフッ素樹脂の繊維は、ペーストを発泡ニッケルに
充填する際に、発泡ニッケルの多孔体を形成している骨
格にからみつくので、発泡ニッケルにペーストを充填す
ることが困難になるという不都合も生ずる.
また、メチルセルロースなどの水溶性高分子を結着剤に
用いる場合には、ペーストを乾燥する際に、この高分子
の被膜が水素吸蔵合金の表面に形成されて、水素吸蔵合
金とアルカリ電解液との接触が阻害される.その結果、
t極の充放電反応に関与しない水素吸蔵合金の量が増加
し、水素吸蔵電極の放電容量が減少するという不都合が
ある.さらにこの方法では、ペースト状混合物を発泡メ
タルに充填する際に、ペーストをゴムベラで練り込む必
要があるので、電極の製作に煩雑な操作を必要とすると
いう欠点もある.
課題を解決するための手段
本発明は、従来のペースト式水素吸蔵電極よりも簡単な
操作で製作できて、しかも水素吸蔵合金の重量の分布が
均一であり、さらに合金中の水素の放電が容易で放電容
量が大きいペースト式の水素吸蔵電極を得て、上述の課
題を解決しようとするものである.
具体的には本発明は、水素吸蔵合金の粉末と、混練時に
繊維化することなく球状を保つ耐アルカリ性高分子の粒
子を分散した高分子ラテックスと、金属または炭素質の
耐アルカリ性導電性粉末とを含むペースト状混合物を導
電性芯体に塗布した後に、塗布されたペースト状混合物
をラテックスに含まれる耐アルカリ性高分子の融点より
も低い温度で乾燥して、水素吸蔵極板を得るものである
。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a water cable storage electrode used in alkaline batteries.
This is related to the method of delivery. Conventional technologies and their problems Hydrogen storage electrodes use hydrogen storage alloys that reversibly store and release hydrogen. The operating potential of a hydrogen storage electrode is almost the same as that of a cadmium electrode, and its discharge capacity per unit volume is significantly larger than that of a cadmium electrode. Therefore, when this electrode is used as the negative electrode of an alkaline storage battery, it is possible to obtain an alkaline storage battery that operates at approximately the same voltage as when cadmium is used as the negative electrode, and has a discharge capacity that is significantly larger than when cadmium is used as the negative electrode. Are known. Conventionally, hydrogen storage electrodes have been manufactured mainly by sintering a hydrogen storage alloy and metal, or by using a paste containing a hydrogen storage alloy and a polymer binder. Electrodes manufactured using the former method are advantageous in that they have high strength because the hydrogen storage alloy and metal are strongly bonded, but they require long-term baking at high temperatures when manufacturing the electrodes. It has the disadvantage of requiring a connection. On the other hand, the latter method using paste (hereinafter referred to as the "paste method") is advantageous in that electrodes can be manufactured in a shorter time than the former method. The following methods are available for manufacturing paste-type hydrogen storage electrodes. That is, as described in Japanese Utility Model Publication No. 57-34678, there is a method in which a foamed metal is filled with a paste-like mixture containing hydrogen storage alloy powder and an alkali-resistant polymer binder. In this method, a fluororesin in the form of a dispersion or methylcellulose in the form of a solution is used as a polymeric binder. The paste is then dried to develop the binding strength of these polymers. The inventor attempted to produce a hydrogen storage alloy using this method and discovered the following drawbacks. That is, when a fluororesin is used as a binder, the fluororesin is easily deformed into fibers by kneading, so the m-fibers become entangled with each other while the paste is kneaded, increasing the viscosity of the paste as a whole. This has the disadvantage that it becomes difficult to control the viscosity of the paste, resulting in uneven application of the paste.
Furthermore, when the fluororesin fibers are filled with the paste into the nickel foam, they become entangled with the framework that forms the porous nickel foam, making it difficult to fill the nickel foam with the paste. Additionally, when a water-soluble polymer such as methylcellulose is used as a binder, a film of this polymer is formed on the surface of the hydrogen storage alloy when the paste is dried, and the hydrogen storage alloy and alkaline electrolyte are bonded together. contact is inhibited. the result,
There is a disadvantage that the amount of hydrogen storage alloy that does not participate in the charge/discharge reaction of the t-electrode increases, and the discharge capacity of the hydrogen storage electrode decreases. Furthermore, this method has the disadvantage that when filling the foamed metal with a paste-like mixture, the paste must be kneaded with a rubber spatula, which requires complicated operations to manufacture the electrodes. Means for Solving the Problems The present invention can be manufactured with simpler operations than conventional paste-type hydrogen storage electrodes, and the weight distribution of the hydrogen storage alloy is uniform, and hydrogen in the alloy can be easily discharged. The aim is to solve the above-mentioned problems by obtaining a paste-type hydrogen storage electrode with a large discharge capacity. Specifically, the present invention comprises a hydrogen storage alloy powder, a polymer latex in which particles of an alkali-resistant polymer that maintain a spherical shape without becoming fibrous during kneading are dispersed, and a metal or carbonaceous alkali-resistant conductive powder. After applying a paste-like mixture containing the above to a conductive core, the applied paste-like mixture is dried at a temperature lower than the melting point of the alkali-resistant polymer contained in the latex to obtain a hydrogen storage electrode plate. .
作用
高分子ラテックスとは、界面活性剤等を作用させてモノ
マを水中に分散させ、このモノマを重合させて《この反
応は乳化重合と呼ばれる》得たもので、高分子の微粒子
が水に分散しているものである.乳化重合で得られる高
分子には、ポリエチレン.ポリ塩化ビニリデン,ポリ塩
化ビニル.ポリ酢酸ビニル,ポリエチレン,ボリプロビ
レン.ポリメチルメタクリレート,ポリウレタン.クロ
ロブレン,ポリテトラフ口口エチレン等のボリマや、ズ
チ゛レンーブタジエン共重合体.塩化ビニリデンー塩化
ビニル共重合体,アクリルニトリルーブタジエン共重合
体.アクリロニトリルースチレン共重合体,塩化ビニル
ー酢酸ビニル共重合体等のコボリマ等、きわめて多くの
種類がある.そして、これらの高分子ラテックスを構成
する粒子は、その粒径がサブミクロンというきわめて小
さいものである.本発明は、以下に述べるように、この
高分子ラテックスの特徴を利用するものである.発明者
は、この高分子ラテックスについて次のことを見出した
.すなわち、この高分子ラテックスを水素吸蔵合金の粉
末と混合してペースト状混合物を作り、これを乾燥する
と、乾燥の進行にともなって、水素吸蔵合金とラテック
ス粒子との間隙の水が失われていく.この乾燥過程の途
中でラテックスを楕成する粒子や水素吸蔵合金の粒子の
間隙に水が残留している状態では゜、この水の大きい毛
管力が作用する.したがって、水素吸蔵合金の粒子間に
介在するラテックス粒子は、乾燥温度がラテックスの高
分子の融点よりもはるかに低い場合にも著しく圧縮され
て変形する.その結果、ラテックス粒子は、水素吸蔵合
金粒子間の強固な結着剤としての作用が発現する.
本発明では、この現象を利用して水素吸蔵合金を得てい
る.すなわち、水素吸蔵合金の粉末と、耐アルカリ性高
分子の微粒子を分散した高分子ラテックスと、金属ニッ
ケル,黒鉛.アセチレンブラック等のような金属または
炭素質の耐アルカリ性導電性粉末とを含むペースト状混
合物を、ニッケルメッキを施した穿孔を有する鋼板や、
金属ニッゲル製のエクスパンデッドメタル等のような耐
アルカリ性導電性芯体に塗着し、その塗着物を耐アルカ
リ性高分子の融点よりも低い温度で乾燥する.このよう
にすると、単にペースト状混合物を導電性芯体に塗着し
て乾燥するというきわめて簡単な操作で、強度が高い水
素吸蔵1極が得られるのである.したがって、本発明に
よれば、従来のペースト式の電極のように発泡ニッケル
の三次元的な骨格によって活物質を支持することもなく
、強度が高い電極が得られる.
本発明では、ペースト状混合物を高分子の融点よりも低
い温度で乾燥する.その理由は次の通りである.すなわ
ち、温度が高分子の融点よりも高くなると、高分子が流
動して、高分子の被膜が水素吸蔵合金の表面に形成され
、水素吸蔵合金とアルカリ電解液との接触が阻害されて
、充放電に関与する水素吸蔵合金の量が減少し、t極の
放電容量が現象するという不都合J生ずる。Active polymer latex is obtained by dispersing monomers in water using a surfactant, etc., and polymerizing the monomers (this reaction is called emulsion polymerization), in which fine particles of polymers are dispersed in water. This is what we are doing. Polymers obtained by emulsion polymerization include polyethylene. Polyvinylidene chloride, polyvinyl chloride. Polyvinyl acetate, polyethylene, polypropylene. Polymethyl methacrylate, polyurethane. Polymers such as chloroprene, polytetrafluoroethylene, and diethylene-butadiene copolymers. Vinylidene chloride-vinyl chloride copolymer, acrylonitrile-butadiene copolymer. There are many types of cobolima such as acrylonitrile-styrene copolymer and vinyl chloride-vinyl acetate copolymer. The particles that make up these polymer latexes are extremely small, submicron in size. The present invention utilizes the characteristics of this polymer latex, as described below. The inventor discovered the following about this polymer latex. In other words, when this polymer latex is mixed with hydrogen storage alloy powder to create a paste-like mixture and this is dried, water in the gaps between the hydrogen storage alloy and latex particles is lost as the drying progresses. .. During this drying process, if water remains in the gaps between the latex oval particles and the hydrogen storage alloy particles, a large capillary force acts on this water. Therefore, the latex particles interposed between the particles of the hydrogen storage alloy are significantly compressed and deformed even when the drying temperature is much lower than the melting point of the latex polymer. As a result, the latex particles act as a strong binder between the hydrogen storage alloy particles. In the present invention, this phenomenon is utilized to obtain a hydrogen storage alloy. That is, hydrogen storage alloy powder, polymer latex in which fine particles of alkali-resistant polymer are dispersed, metallic nickel, and graphite. A paste mixture containing a metal or carbonaceous alkali-resistant conductive powder such as acetylene black is applied to a nickel-plated steel plate with perforations,
It is applied to an alkali-resistant conductive core such as Expanded Metal made by Metal Nigel, and the applied material is dried at a temperature lower than the melting point of the alkali-resistant polymer. In this way, a highly strong hydrogen storage single pole can be obtained by simply applying a paste-like mixture to a conductive core and drying it. Therefore, according to the present invention, an electrode with high strength can be obtained without supporting the active material by a three-dimensional skeleton of foamed nickel unlike conventional paste-type electrodes. In the present invention, the paste-like mixture is dried at a temperature lower than the melting point of the polymer. The reason is as follows. In other words, when the temperature becomes higher than the melting point of the polymer, the polymer flows and a polymer film is formed on the surface of the hydrogen storage alloy, inhibiting the contact between the hydrogen storage alloy and the alkaline electrolyte, resulting in charging. The amount of hydrogen storage alloy involved in discharge decreases, resulting in the disadvantage that the discharge capacity of the t-electrode decreases.
また、本発明では、高分子ラテックスとしてポリエチレ
ン,ポリ塩化ビニリデン,ポリ塩化ビニル,ポリ酢酸ビ
ニル,ポリエチレン,ボリプロビレン.ポリメチルメタ
クリレート.夕ロロプレン等のボリマや、スチレンーブ
タジエン共重合体,塩化とニリデンー塩化ビニル共重合
体,アクリルニトリルーブタジエン共重合体,アクリロ
ニトリルースチレン共重合体等のコボリマのように、べ
−ストを混練してこれを調製する際に、球状を保って繊
維化しにくい耐アルカリ性高分子を分散したものを用い
る.そして、ポリテトラフ口口エチレン等のフッ素樹脂
のように混線によって容易に繊維化する高分子を分散し
たラテックスを用いない.したがって、本発明では、ペ
ーストを混練する際にラテックス粒子が繊維化すること
がなく、安定したペーストの粘度が得られるので、前述
の不都合が生ずることがなくなり、安定した作業条ft
−が得られる点で有利である.
さらに本発明では、ペースト状混合物に金属または炭素
質の耐アルカリ性導電性粉末を添加する.その目的は、
f4極の丞素吸蔵合金粉末と導電性芯体との導電性を良
好にして、水素吸蔵合金の水素化物の放電を容易にする
ことにある.すなわち、発明者は、−{アルカリ性の導
電性粉末の添加量を変えて、水素吸R電極を本発明の方
法で製作し、この電極をアルカリ電解液中で充放電した
結果、導電性粉末を添加しない場合には、この電極を充
電することは容易であるが、放電することはきわめて困
難であることを見出した.
このような現象が生ずる理由は定かではないが、次のよ
うに考えられる。すなわち、水素吸蔵合金は放電状態で
は金属であるので、電子伝導性がきわめて良好であるか
ら、導電性の粉末を用いなくとも容易に充電できる.し
かし充電が進行すると、電子伝導性に劣る金属水素化物
が生成する.次に、放電する場合には、導電性粉末を用
いない場合には、充電生成物である金属水素化物の電気
抵抗が大きいので、導電性芯体から遠い位置にある金属
水素化物の集電が困難になって、電極の放電が困龍にな
る.一方、導電性粉末を用いる場合には、金属水素化物
の集電性が良好になって、電極の放電が容易になる.本
発明の方法では、3次元のネットワークを形成しないパ
ンチングメタルやエキスパンデッドメタルを導電性芯体
に用いるので、耐アルカリ性の導電性粉末を用いること
によって、電極の放電が可能になる.なお、発泡ニッケ
ルに水素吸蔵合金を充填する従来の電極の場合には、そ
の骨格は3次元の集電体ネットワークとして作用するの
で、導電性粉末は必ずしも用いる必要はないが、前述の
ような電極の制作に煩雑な操作を必要とするという問題
が解決しない.
実施例
以下、本発明を好適な実膣例を用いて詳細に説明する.
く実験1〉
まず、ペーストを混練する際に球状を保つ耐アルカリ性
高分子の粒子を分散した高分子ラテックスを用いる本発
明の水素吸蔵電極と、混練時に球状を保つことなく繊維
化する高分子の粒子を分散した高分子ラテックスを用い
る比較例の水素吸蔵電極および水溶性高分子を結着剤に
用いる比教例の水素吸蔵電極を製作した例を示して、本
発明による水素吸蔵電極の優位性を具体的に説明する.
[水素吸蔵電極Al (本発明実施例)本発明による水
素吸蔵t[+Aを次のようにしてー作した.
水素吸蔵合金は、金属チタン粉末および金属ニッケル粉
末を原子比で2:1の割合で混合し、アルゴン雰囲気の
アーク溶解炉を用いてこの混合物を溶解して製作した.
溶解して得た台金塊は、その組成を均一にずるために、
冷却した後に裏返して再度溶解するというう操作を3回
繰り返した.次に、このようにして得られた金属間化合
物Ti2旧の合金塊を、超硬合金製の乳鉢で粉砕した.
そして、100メッシュの篩を通過したこの水素吸蔵合
金粉末100重量部と人造黒船粉末( LON7A社製
,商品名: [850−200) 20重量部とを混合
し、この混合物に水を加えてよく混練した.そレて混練
時に球状を保つ耐アルカリ性高分子の粉末を分散した高
分子ラテックスとしてポリエチレン樹脂(融点110″
C)の微粒子が分散した高分子ラテックス(三洋化成(
株)製,商品名:パーマリンPI{)を用い、このラテ
ックス20重量部を加えて混練し、ペースト状の混練物
を得た.そして、この混合物を、穿孔を有する厚さ0.
09nusの鋼板に厚さ20ミクロンのニッケルメッ
キを施した導電性芯体に塗着し、ドクターブレードで塗
着物の厚さを調節した。In addition, in the present invention, polyethylene, polyvinylidene chloride, polyvinyl chloride, polyvinyl acetate, polyethylene, polypropylene can be used as the polymer latex. Polymethyl methacrylate. The base is kneaded, such as polymers such as roloprene, copolymer such as styrene-butadiene copolymer, chloride and nylidene-vinyl chloride copolymer, acrylonitrile-butadiene copolymer, and acrylonitrile-styrene copolymer. When preparing this, we use a dispersion of an alkali-resistant polymer that maintains its spherical shape and does not easily form into fibers. Also, latex containing dispersed polymers, such as fluorocarbon resins such as polytetrafluoroethylene, which easily become fibers due to cross-wires, is not used. Therefore, in the present invention, the latex particles do not become fibrous when the paste is kneaded, and a stable viscosity of the paste is obtained, so that the above-mentioned disadvantages do not occur and stable working conditions can be achieved.
This is advantageous in that it allows you to obtain -. Furthermore, in the present invention, a metal or carbonaceous alkali-resistant conductive powder is added to the paste mixture. Its purpose is
The objective is to improve the conductivity between the f4 pole boron storage alloy powder and the conductive core to facilitate the discharge of hydride from the hydrogen storage alloy. That is, the inventor manufactured a hydrogen absorbing R electrode by the method of the present invention by changing the amount of alkaline conductive powder added, and as a result of charging and discharging this electrode in an alkaline electrolyte, the conductive powder was It has been found that in the absence of additives, it is easy to charge this electrode, but it is extremely difficult to discharge it. The reason why such a phenomenon occurs is not clear, but it is thought to be as follows. In other words, since the hydrogen storage alloy is a metal in the discharged state, it has extremely good electronic conductivity, so it can be easily charged without using conductive powder. However, as charging progresses, metal hydrides with poor electronic conductivity are formed. Next, when discharging, if conductive powder is not used, the electrical resistance of the metal hydride, which is the charge product, is large, so the metal hydride located far from the conductive core will collect current. It becomes difficult and the electrode discharge becomes difficult. On the other hand, when a conductive powder is used, the metal hydride has good current collection properties, making it easier to discharge the electrode. In the method of the present invention, a punched metal or an expanded metal that does not form a three-dimensional network is used for the conductive core, so the use of an alkali-resistant conductive powder makes it possible to discharge the electrode. In the case of conventional electrodes in which foamed nickel is filled with a hydrogen storage alloy, the skeleton acts as a three-dimensional current collector network, so it is not necessarily necessary to use conductive powder, but in the case of electrodes such as those described above, The problem of requiring complicated operations for production remains unsolved. EXAMPLE Hereinafter, the present invention will be explained in detail using a preferred example of a real vagina. Experiment 1 First, we used the hydrogen storage electrode of the present invention, which uses a polymer latex in which alkali-resistant polymer particles that maintain a spherical shape when kneading the paste are dispersed, and the hydrogen storage electrode of the present invention, which uses a polymer latex in which particles of an alkali-resistant polymer that maintain a spherical shape when kneaded, and a polymer latex that does not maintain a spherical shape during kneading but turn into fibers. The superiority of the hydrogen storage electrode according to the present invention will be explained by showing an example of manufacturing a comparative hydrogen storage electrode using a polymer latex with particles dispersed therein and a comparison hydrogen storage electrode using a water-soluble polymer as a binder. I will explain specifically.
[Hydrogen storage electrode Al (Example of the present invention)] A hydrogen storage electrode Al according to the present invention was prepared as follows. The hydrogen storage alloy was manufactured by mixing metallic titanium powder and metallic nickel powder at an atomic ratio of 2:1 and melting this mixture using an arc melting furnace in an argon atmosphere.
In order to make the composition of the base metal ingot obtained by melting uniform,
After cooling, the mixture was turned over and redissolved, which was repeated three times. Next, the thus obtained intermetallic compound Ti2 old alloy ingot was crushed in a mortar made of cemented carbide.
Then, 100 parts by weight of this hydrogen storage alloy powder that has passed through a 100 mesh sieve is mixed with 20 parts by weight of artificial Kurofune powder (manufactured by LON7A, trade name: [850-200), and water is added to this mixture. Kneaded. Polyethylene resin (melting point 110''
C) Polymer latex in which fine particles are dispersed (Sanyo Chemical Co., Ltd.)
20 parts by weight of this latex was added and kneaded using Permarin PI {), manufactured by Co., Ltd., to obtain a paste-like kneaded product. This mixture is then applied to a thickness of 0.5 mm with perforations.
The coating was applied to a conductive core made of a 20 micron thick nickel plated steel plate of 0.09 nus, and the thickness of the coating was adjusted using a doctor blade.
次に、75゜Cの熱風を用いてこの塗着物を乾燥した。Next, this coating was dried using hot air at 75°C.
そして、室温でロールでプレスして電極の厚さを約0.
71HIに調節し、aonnx 401111の大き
さに切断して水素吸蔵電極を得た。Then, press the electrode with a roll at room temperature to make the electrode thickness about 0.
71HI and cut into a size of aonnx 401111 to obtain a hydrogen storage electrode.
[水索吸蔵電iFi!B] (比較例)本発明による
水素吸蔵電[!Aにおけるポリエチレン樹脂の微粒子が
分散している高分子ラテックスの変りに、混練時に繊維
化する高分子であるボ・リテトラフ口口エチレンの微粒
子が分散している高分子ラテックス《ダイキン(株)製
,商品名:ボリフロンディスバージョンD−1》を用い
たほかは、本発明による水素吸蔵電極Aと同様の条件で
比較例の水素吸蔵電極Bを製作した.
[水素吸蔵電極C] (比教例》
本発明による水素吸蔵tiAにおいてポリエチレン樹脂
の微粒子が分散している高分子ラテックス20重量部を
加えて混練する代りに、水溶性高分子であるメチルセル
ロース(信越化学《株》製.商品名二メトロース3M−
4000 ) 10重量部を加え、これを混合して分散
させてから、70℃に昇渇してメチルセルロースを溶解
させた後に室温に冷却して、ペースト状混合物を得た.
そして、そのほかQgkPI−を本発明による水素吸蔵
1極Aと同様にして比較例の水素吸蔵電fiCを製作し
た.これらの電極1枚に含まれる水索吸蔵合金の平均値
および標準偏差を第1表に示す.
第1表から、本発明による水素吸R電4ffiAおよび
比較例の水素吸′R電極Cに含まれる水素吸蔵合弟IA
金の重量の標準偏差は、比較例の水素吸蔵電iBよりも
著しく小さいので、これらの電極AおよびCに含まれる
水素吸蔵合金の重1の分布は、電極Bよりも均一である
ことがわかる.
次に、上述の水素吸蔵電iA,BおよびCのそれぞれ1
枚を負極に用い、焼結式の水酸化ニッケル電極・2枚を
正極に用いて、電池の放電が負極の容量で制限される3
種類のアルカリ蓄電池を製作した.そして、水素吸蔵電
極に用いる結着剤の種類が、電池を構成した状態におけ
る負極の放電性能に及ぼす影響を調べた.
負極には、上述の3種類のどの電極の場合にも、約5.
2gの水素吸蔵合金を含む電極を選んだ.正極の水酸化
ニッケル電極は、次のようにして製作した.
すなわち、多孔度が約85%の焼結ニッケル基板を用い
、通常の減圧含漫法で減圧含浸を6回繰り返して、水酸
化ニッケルと水酸化コバルトとをこの焼結基板の細孔中
に共沈させて、焼結式水酸化ニッケル電極を製作した。[Water cable storage electric iFi! B] (Comparative example) Hydrogen storage battery according to the present invention [! Instead of the polymer latex in A in which fine particles of polyethylene resin are dispersed, there is a polymer latex in which fine particles of ethylene trough, which is a polymer that turns into fibers during kneading, are dispersed (manufactured by Daikin Corporation). A hydrogen storage electrode B of a comparative example was manufactured under the same conditions as the hydrogen storage electrode A according to the present invention, except that a product named: Boliflon Disversion D-1 was used. [Hydrogen storage electrode C] (Educational example) In the hydrogen storage tiA according to the present invention, instead of adding and kneading 20 parts by weight of polymer latex in which fine particles of polyethylene resin are dispersed, methylcellulose (Shin-Etsu), which is a water-soluble polymer, is used. Manufactured by Kagaku Co., Ltd. Product name Nimetrose 3M-
4000) was added, mixed and dispersed, heated to 70°C to dissolve the methylcellulose, and then cooled to room temperature to obtain a paste-like mixture.
In addition, a hydrogen storage electric fiC as a comparative example was fabricated using QgkPI- in the same manner as the hydrogen storage monopole A according to the present invention. Table 1 shows the average value and standard deviation of the water cord storage alloy contained in each of these electrodes. From Table 1, it can be seen that the standard deviation of the weight of the hydrogen-absorbing brother IA gold contained in the hydrogen-absorbing electrode 4ffiA according to the present invention and the hydrogen-absorbing electrode C of the comparative example is significantly smaller than that of the hydrogen-absorbing electrode iB of the comparative example. Therefore, it can be seen that the distribution of hydrogen storage alloy weight 1 contained in these electrodes A and C is more uniform than in electrode B. Next, 1 each of the above-mentioned hydrogen storage batteries iA, B and C
By using one sheet as the negative electrode and two sintered nickel hydroxide electrodes as the positive electrode, the discharge of the battery is limited by the capacity of the negative electrode.
We manufactured different types of alkaline storage batteries. We then investigated the effect of the type of binder used in the hydrogen storage electrode on the discharge performance of the negative electrode in the battery configuration. For the negative electrode, for any of the three types of electrodes mentioned above, approximately 5.
An electrode containing 2 g of hydrogen storage alloy was chosen. The positive nickel hydroxide electrode was manufactured as follows. That is, using a sintered nickel substrate with a porosity of approximately 85%, vacuum impregnation was repeated six times using the usual vacuum impregnation method to co-inject nickel hydroxide and cobalt hydroxide into the pores of this sintered substrate. Then, a sintered nickel hydroxide electrode was manufactured.
この電極の大きさは、40偽vlx 40Ix 0.
85nnでありり、この電[!1枚に充填されている水
酸化ニッケルおよび水酸化コバルトの合計の量は、2、
4gであった.!Lた水酸化コバルトの含有量は、水酸
化ニッケルと水酸化コバルトとの合計の量に対するモル
比で約95%であった.次に、水素吸蔵電!f!1枚を
負極とし、水酸化ニッケル電極2枚を正極とし、ナイロ
ン製の不織布をセパレー夕として、5.8Hκ011電
解液を大量に用゛いて開放形に横成したいゆるフラッデ
ッドタイプの試験用電池を製作した.この電池に用いて
いる正極の放電容量は、放電が1電子反応過程に従う場
合に、1 . 39nAhである.電槽は、寸法が45
X45x 3nmのアクリル樹脂製のものを用いた.こ
のようにして本発明による水素吸蔵電!Ii!A,比較
例の水素吸蔵電極BおよびCを用いて製作した電池を、
それぞれ電池A,B,Cと呼ぶこれらの電池を25゜C
において、0. 085八の電流で20時間充電し、0
. 085Aの電流で1.OVまで放電するという条件
で充放電試験を行なった場合の3サイクル目の放電容量
を第2表に示す.
第2表
第2表から、電池Aおよび電池Bの放電容量は、電池C
よりも著しく大きいことがわかる.これらの試験結果か
ら、混練時に球状を保つ耐アルカリ性高分子の粒子を分
散した高分子ラテックスを用いる本発明の場合には、混
線時に繊維化する高分子の粒子を分散した高分子ラテッ
クスを用いる場合や水溶性高分子を用いる場合と比較し
て、電極に含まれる水素吸蔵合金の重量分布が均一で、
しかも放電容量が大きいという 2つの特徴を兼ね備え
る水素吸蔵電極が得られることが明らかである。The size of this electrode is 40 false vlx 40Ix 0.
It is 85nn, and this electric [! The total amount of nickel hydroxide and cobalt hydroxide filled in one sheet is 2,
It was 4g. ! The content of cobalt hydroxide was approximately 95% in molar ratio to the total amount of nickel hydroxide and cobalt hydroxide. Next, hydrogen storage electricity! f! A flooded type test battery made in an open type using a large amount of 5.8Hκ011 electrolyte, with one electrode as a negative electrode, two nickel hydroxide electrodes as a positive electrode, and a nylon nonwoven fabric as a separator. was produced. The discharge capacity of the positive electrode used in this battery is 1. It is 39nAh. The size of the battery case is 45
A piece made of acrylic resin with a size of 45 x 3 nm was used. In this way, the hydrogen storage battery according to the present invention! Ii! A, a battery manufactured using hydrogen storage electrodes B and C of comparative example,
These batteries, referred to as batteries A, B, and C, respectively, were heated at 25°C.
In, 0. Charged for 20 hours with a current of 0858,
.. 1 with a current of 085A. Table 2 shows the discharge capacity at the third cycle when a charge/discharge test was conducted under the condition of discharging to OV. Table 2 From Table 2, the discharge capacity of battery A and battery B is
It can be seen that it is significantly larger than . From these test results, it was found that in the case of the present invention, which uses a polymer latex in which particles of an alkali-resistant polymer are dispersed, which maintain a spherical shape during kneading, when using a polymer latex in which particles of alkali-resistant polymer, which form into fibers when mixed, are dispersed. The weight distribution of the hydrogen-absorbing alloy contained in the electrode is uniform compared to the case where a water-soluble polymer is used.
Moreover, it is clear that a hydrogen storage electrode that has two characteristics of large discharge capacity can be obtained.
く実験2〉
次に、金属または炭素質の耐アルカリ性の導電性粉末の
添加量を変えて試験した結果を示して、これらの導電性
粉末を添加することが本発明の必須の楕成要件′である
ことを説明する.水素吸蔵な極は次のようにして製作し
な。すなわち、水素吸蔵合金として、実験lにおける■
12Niの代りにLaNl*.s CO2.sを用いた
。そして、耐アルカリ性の導電性粉末として、カーボニ
ルニッケル粉末( INCO社製,商品名: Type
255 )よタC,t人造黒鉛粉末(LONZA社製,
WfJ晶名: LN50−200) f用い、水素吸
蔵合金と耐アルカリ性の導電性粉末との合計を110重
量部の一定値にしながら、水素吸蔵合金粉末と導電性粉
末との混合比を広い範囲で変えた.そして、混練時に球
状を保つ耐アルカリ性高分子の粒子を分散した高分子ラ
テックスとして、アクリルニトリルースチレン共重合体
の微粒子が分散している高分子ラテックス《旭化成(株
)性,商品名:ボリトロンA−65 )を用いた.その
ほかの条件は、実験1における本発明の水素吸蔵電極A
と同じにした.ここで、導電性粉末としてカーボニルニ
ッケル粉末および人造黒鈴扮末を用いる電極をそれぞれ
電極Dおよび電極Eと呼ぶ.
そして、これらの電極を負極として用いる曲は、実験1
における電池Aと同じ構成にして、試験用の電池を製作
した.電極Dを用いた電池を電池D、電fl!Eを用い
た電池を電池Eと呼ぶ.これらの電池を用いて、実験1
と同じ通電条『トの充放電サイクル試験を行ない、10
サイクル目の放電容量を測定した.また、10サイクル
目に放電されることなく水索吸蔵合金に残留している水
素の量を測定した.その結果を第1図に示す。Experiment 2 Next, we will show the results of tests with varying amounts of metal or carbonaceous alkali-resistant conductive powders, and show that the addition of these conductive powders is an essential elliptical requirement of the present invention. Explain that. Produce a hydrogen-absorbing pole as follows. That is, as a hydrogen storage alloy, ■
12Ni instead of LaNl*. s CO2. s was used. Carbonyl nickel powder (manufactured by INCO, trade name: Type) is used as an alkali-resistant conductive powder.
255) Yota C, t Artificial graphite powder (manufactured by LONZA,
WfJ crystal name: LN50-200) f was used, and the mixing ratio of the hydrogen storage alloy powder and the conductive powder was varied over a wide range while keeping the total of the hydrogen storage alloy and the alkali-resistant conductive powder at a constant value of 110 parts by weight. changed. Then, as a polymer latex in which particles of an alkali-resistant polymer that maintain a spherical shape during kneading are dispersed, a polymer latex in which fine particles of an acrylonitrile-styrene copolymer are dispersed (manufactured by Asahi Kasei Co., Ltd., product name: Bolitron A) is used. -65) was used. Other conditions were as follows: Hydrogen storage electrode A of the present invention in Experiment 1
I made it the same as Here, electrodes using carbonyl nickel powder and artificial black bell pepper powder as conductive powders are referred to as electrode D and electrode E, respectively. The songs using these electrodes as negative electrodes were created in Experiment 1.
A test battery was manufactured with the same configuration as battery A in . A battery using electrode D is called battery D, electric fl! A battery using E is called battery E. Experiment 1 using these batteries
A charge/discharge cycle test was conducted under the same energizing conditions, and
The discharge capacity at the 1st cycle was measured. In addition, the amount of hydrogen remaining in the water cable storage alloy without being discharged at the 10th cycle was measured. The results are shown in FIG.
第1図において、曲線(ア)および(イ)は、それぞれ
水素吸蔵合金粉末と導電性粉末との混合比を変えた場合
の電池DおよびEの放電容量と負極の水素吸蔵合金の重
量との比と、水素吸蔵合金と導電性粉末との合計に対す
る導電性粉末の重量比との関係を表す。そして曲線(ウ
)および(工)は、それぞれ電池DおよびEの負極の水
索吸蔵合金に含まれる未放電の水素の量を放電容量に換
算した値と負極の水素吸蔵合金の重量との比と、水素吸
蔵合金と導電性粉末との合計に対する導電性粉末の重量
比との関係を表す.
第1図の曲線(ア)および(イ)から、電池DおよびE
のいずれにおいても、導電性粉末を添加しない場合には
、電池がほとんど放電できないことがわかる.そして、
電池の放電容量と水累吸蔵合金の重量との比は、導電性
粉末の添加量が少ない場合には、添加量の増加にともな
って大きくなり、導電性粉末の添加量が水素吸蔵合金の
量と同程度よりも大きくなると、ほぼ一定になることが
わかる.
そして曲線(ア),《イ》,(ウ》および《工》を合わ
せて考えると、導電性粉末を添加しない場合に水素吸蔵
合金が放電できない現象および導電性粉末の添加量が少
ない場合に水素吸蔵合金の放電容量が小さい現象の主た
る原因は、放電が困雑な水素が水素吸蔵合金に残留して
いることにあることがわかる。In Figure 1, curves (A) and (B) show the relationship between the discharge capacity of batteries D and E and the weight of the hydrogen storage alloy of the negative electrode when the mixing ratio of hydrogen storage alloy powder and conductive powder is changed, respectively. It represents the relationship between the ratio and the weight ratio of the conductive powder to the total of the hydrogen storage alloy and the conductive powder. Curves (c) and (d) are the ratio of the amount of undischarged hydrogen contained in the negative electrode water storage alloy of batteries D and E, respectively, converted into discharge capacity and the weight of the negative electrode hydrogen storage alloy. represents the relationship between the weight ratio of the conductive powder to the total of the hydrogen storage alloy and the conductive powder. From the curves (A) and (B) in Figure 1, batteries D and E
In both cases, it can be seen that if no conductive powder is added, the battery can hardly be discharged. and,
When the amount of conductive powder added is small, the ratio between the discharge capacity of the battery and the weight of the water storage alloy increases as the amount of added conductive powder increases. It can be seen that when it becomes larger than the same level as , it becomes almost constant. Considering curves (A), (B), (C), and (C) together, we can see that the hydrogen storage alloy cannot discharge when no conductive powder is added, and when the amount of conductive powder added is small, hydrogen It can be seen that the main cause of the phenomenon in which the discharge capacity of the storage alloy is small is that hydrogen, which is difficult to discharge, remains in the hydrogen storage alloy.
したがって、本発明においては、ニッケルや黒鉛のよう
に金属または炭素質の耐アルカリ性導電性粉末を添加す
ると、高い放電容量が得られることが明らかである。Therefore, in the present invention, it is clear that a high discharge capacity can be obtained by adding metal or carbonaceous alkali-resistant conductive powder such as nickel or graphite.
〈実験3〉
最後に、ペースト状混合物の乾燥温度を変えた場合の水
素吸蔵電極の放電性能を示して、ペースト状混合物の乾
燥温度を耐アルカリ性高分子の融点よりも低くすること
が、本発明の必須要件であることを説明する.
負極板は、実験2における電[zDにおいて、混合時に
球状を保つ耐アルカリ性高分子としてポリエチレン(融
点110℃)の粒子を分散した前述の高分子ラテックス
(三洋化成《株》性,商品名:パーマリンPM)を用い
、水素吸蔵合金100重量部を用い、カーボニルニッケ
ル粉末40重量部を用いて、乾燥の温度を60゜Cから
160℃の範囲で変えたほかは、条件を電極Dと同様に
した水索吸蔵電検Fを製作した。<Experiment 3> Finally, we will show the discharge performance of the hydrogen storage electrode when the drying temperature of the paste-like mixture is changed, and show that the present invention can make the drying temperature of the paste-like mixture lower than the melting point of the alkali-resistant polymer. Explain that this is an essential requirement. The negative electrode plate was made of the aforementioned polymer latex (manufactured by Sanyo Kasei Co., Ltd., trade name: Permarin) in which particles of polyethylene (melting point 110°C) were dispersed as an alkali-resistant polymer that maintained a spherical shape during mixing in the electrolyte [zD in Experiment 2]. PM), 100 parts by weight of hydrogen storage alloy, 40 parts by weight of carbonyl nickel powder, and the conditions were the same as for electrode D, except that the drying temperature was varied from 60°C to 160°C. We created the water cable occlusion electric test F.
次に、電極Fを用いるほかは、条件を実In!lの電池
Aと同じにした電池Fを製作した。そして、実@1と同
じ通電条件で充放電サイクル試験を行ない、10サイク
ル目の放電容量を調べた.この場合の放電容量とペース
ト状混合物の乾燥温度との関係を第2図に示す.第2図
から、乾燥温度がラテックスに含まれる高分子の融点1
10゜Cよりも低い場合に放電容量が低下しないという
特徴があることがわかる.
なお、融点が異なるそのほかの高分子を用いる場合にも
、同様にその高分子の融点よりも低い温度で乾燥するこ
とが適していることがわかった。Next, except for using electrode F, the conditions were set to In! A battery F, which was the same as battery A, was manufactured. Then, a charge/discharge cycle test was conducted under the same current conditions as in Actual @1, and the discharge capacity at the 10th cycle was investigated. Figure 2 shows the relationship between the discharge capacity and the drying temperature of the paste mixture in this case. From Figure 2, the drying temperature is the melting point of the polymer contained in the latex.
It can be seen that the discharge capacity does not decrease when the temperature is lower than 10°C. It has been found that when using other polymers with different melting points, it is also suitable to dry at a temperature lower than the melting point of the polymer.
発明の効果
以上述べたように、本発明により、従来のペースト式水
素吸蔵電極よりも簡単な操作で製造でき、しかも水素吸
蔵合金の重量の分布が均一であり、さらに合金中の水素
の放電が容易で放電容量が大きいという効果を兼ね備え
た水素吸蔵電極を得ることができる.Effects of the Invention As described above, the present invention enables manufacturing with simpler operations than conventional paste-type hydrogen storage electrodes, has a uniform weight distribution of the hydrogen storage alloy, and furthermore, the hydrogen storage electrode in the alloy can be easily discharged. It is possible to obtain a hydrogen storage electrode that is easy to use and has a large discharge capacity.
第1図は、水索吸蔵電極を負極に用いるアルカリ電池の
放電容量および未放電の水素に対する容量と水素吸蔵合
金の重量との比と、水索吸蔵合金と導電性粉末との合計
に対する導電性粉末の重量比との関係を表す図である.
同図中(ア)および(イ)は、実際に放電した容量を表
し、(ウ)および(工)は、未放電の水素の容量を表す
.第2図は、水素吸蔵電極を負極に用いるアルカリ蓄電
池の放電容量と水素吸蔵合金の重量との比と、ペースト
状混合物の乾燥温度との関係を示した図である.Figure 1 shows the discharge capacity of an alkaline battery using a water cable storage electrode as the negative electrode, the ratio of the capacity for undischarged hydrogen to the weight of the hydrogen storage alloy, and the electrical conductivity relative to the sum of the water cable storage alloy and conductive powder. It is a diagram showing the relationship with the weight ratio of powder.
In the figure, (a) and (b) represent the actual discharged capacity, and (c) and (d) represent the undischarged hydrogen capacity. FIG. 2 is a diagram showing the relationship between the ratio of the discharge capacity of an alkaline storage battery using a hydrogen storage electrode as the negative electrode and the weight of the hydrogen storage alloy, and the drying temperature of the paste mixture.
Claims (1)
カリ性高分子の粒子を分散した高分子ラテックスと、金
属または炭素質の耐アルカリ性導電性粉末とを含むペー
スト状混合物を、導電性芯体に塗布してから、塗布され
たペースト状混合物を、ラテックスに含まれる耐アルカ
リ性高分子の融点よりも低い温度で乾燥することを特徴
とする水素吸蔵電極の製造方法。1. A paste-like mixture containing a hydrogen storage alloy powder, a polymer latex in which particles of an alkali-resistant polymer that maintain a spherical shape during kneading are dispersed, and a metal or carbonaceous alkali-resistant conductive powder is mixed into a conductive core. A method for producing a hydrogen storage electrode, which comprises applying the paste mixture to the latex and then drying the applied paste mixture at a temperature lower than the melting point of the alkali-resistant polymer contained in the latex.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP05544889A JP3177653B2 (en) | 1989-03-08 | 1989-03-08 | Method for producing hydrogen storage electrode |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP05544889A JP3177653B2 (en) | 1989-03-08 | 1989-03-08 | Method for producing hydrogen storage electrode |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02234355A true JPH02234355A (en) | 1990-09-17 |
| JP3177653B2 JP3177653B2 (en) | 2001-06-18 |
Family
ID=12998884
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP05544889A Expired - Lifetime JP3177653B2 (en) | 1989-03-08 | 1989-03-08 | Method for producing hydrogen storage electrode |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3177653B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0629018A (en) * | 1992-04-23 | 1994-02-04 | Furukawa Battery Co Ltd:The | Hydrogen storage electrode |
| EP0602768A3 (en) * | 1992-12-17 | 1995-05-17 | Sanyo Electric Co | Hydrogen-absorbing alloy electrode and manufacturing method therefor. |
| US6242133B1 (en) | 1998-06-17 | 2001-06-05 | Sanyo Electric Co., Ltd. | Hydrogen-absorbing alloy electrode for alkaline secondary battery and method of manufacture thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4859354B2 (en) * | 2004-08-05 | 2012-01-25 | 三洋電機株式会社 | A hydrogen storage alloy electrode for an alkaline storage battery, an alkaline storage battery using the electrode, and a method for producing the electrode. |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5223636A (en) * | 1975-08-19 | 1977-02-22 | Tokyo Shibaura Electric Co | Secondary alkaline battery |
| JPS5271643A (en) * | 1975-12-11 | 1977-06-15 | Matsushita Electric Industrial Co Ltd | Nickel electrode |
| JPS62264557A (en) * | 1986-05-13 | 1987-11-17 | Toshiba Corp | Metal oxide-hydrogen battery |
-
1989
- 1989-03-08 JP JP05544889A patent/JP3177653B2/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5223636A (en) * | 1975-08-19 | 1977-02-22 | Tokyo Shibaura Electric Co | Secondary alkaline battery |
| JPS5271643A (en) * | 1975-12-11 | 1977-06-15 | Matsushita Electric Industrial Co Ltd | Nickel electrode |
| JPS62264557A (en) * | 1986-05-13 | 1987-11-17 | Toshiba Corp | Metal oxide-hydrogen battery |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0629018A (en) * | 1992-04-23 | 1994-02-04 | Furukawa Battery Co Ltd:The | Hydrogen storage electrode |
| EP0602768A3 (en) * | 1992-12-17 | 1995-05-17 | Sanyo Electric Co | Hydrogen-absorbing alloy electrode and manufacturing method therefor. |
| US6242133B1 (en) | 1998-06-17 | 2001-06-05 | Sanyo Electric Co., Ltd. | Hydrogen-absorbing alloy electrode for alkaline secondary battery and method of manufacture thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3177653B2 (en) | 2001-06-18 |
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