Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6359228B2 - - Google Patents
[go: Go Back, main page]

JPS6359228B2 - - Google Patents

Info

Publication number
JPS6359228B2
JPS6359228B2 JP57052477A JP5247782A JPS6359228B2 JP S6359228 B2 JPS6359228 B2 JP S6359228B2 JP 57052477 A JP57052477 A JP 57052477A JP 5247782 A JP5247782 A JP 5247782A JP S6359228 B2 JPS6359228 B2 JP S6359228B2
Authority
JP
Japan
Prior art keywords
substrate
sintered
microcapsules
slurry
nickel
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
Application number
JP57052477A
Other languages
Japanese (ja)
Other versions
JPS58169773A (en
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 filed Critical
Priority to JP57052477A priority Critical patent/JPS58169773A/en
Publication of JPS58169773A publication Critical patent/JPS58169773A/en
Publication of JPS6359228B2 publication Critical patent/JPS6359228B2/ja
Granted 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
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/80Porous plates, e.g. sintered carriers
    • 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)
  • Powder Metallurgy (AREA)
  • Cell Electrode Carriers And Collectors (AREA)

Description

【発明の詳細な説明】 本発明は、アルカリ蓄電池用焼結基板の製造法
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a sintered substrate for an alkaline storage battery.

従来、アルカリ蓄電池用の焼結基板の製造法に
は、乾式法を湿式法とがある。乾式法は炭素の枠
型内に芯材となるニツケル、鉄などの金網や開孔
板と焼結用のニツケル等の粉末とを配し、還元雰
囲気中で焼結したものである。湿式法は焼結用金
属粉とCMCなどの粘着剤と混合した水性スラリ
ーを芯材に塗着した後乾燥し、700〜900℃の還元
雰囲気中で焼結したものである。乾燥法は湿式法
に比べて焼結基板の多孔度がやや大きくなるが、
製造時の作業性が悪く、特に連続生産できないた
め、生産性に乏しい。一方湿式法は生産性の面で
優れているが、多孔度が低くなる欠点がある。特
にスラリーをスリツトによつて塗着する場合に、
ニツケル微粉末がスリツト近傍に集まる現像があ
るため、基板表面付近の多孔度が小さくなる欠点
を有していた。焼結基板はその中に電極活性質を
充填して電極として使用するため、その多孔度が
大きい程容量密度が大となり、また充填しやすく
なるために、基板多孔度を大きくする方法が種々
検対されてきた。
Conventionally, methods for producing sintered substrates for alkaline storage batteries include a dry method and a wet method. In the dry method, a wire mesh or perforated plate made of nickel or iron as a core material and a powder of nickel or the like for sintering are arranged in a carbon frame and sintered in a reducing atmosphere. In the wet method, an aqueous slurry of sintering metal powder and an adhesive such as CMC is applied to the core material, dried, and sintered in a reducing atmosphere at 700 to 900°C. The dry method results in a slightly larger porosity of the sintered substrate than the wet method, but
Workability during manufacturing is poor, especially since continuous production is not possible, resulting in poor productivity. On the other hand, the wet method is superior in terms of productivity, but has the disadvantage of low porosity. Especially when applying slurry through a slit,
Since the fine nickel powder gathers near the slit during development, it has the disadvantage that the porosity near the substrate surface becomes small. Since a sintered substrate is used as an electrode by filling it with an electrode active material, the larger the porosity, the higher the capacity density, and the easier it is to fill, so various methods have been investigated to increase the porosity of the substrate. has been faced.

例えば特公昭52−15774号では、湿式法で得た
スラリー表面層内に可燃性粉末を付着させ、焼結
時に燃焼焼失させることにより表面多孔度の増加
を図つている。同様に特公昭53−47492号では焼
結用金属粉末をスラリー表面に付着させ、湿式法
と乾式法の混合使用的方法により多孔度の増加を
図つている。しかし、一般に湿式法によつて得ら
れる焼結基板の多孔度は70〜78%程度で表面多孔
度度の増加による多少の多孔度増加はあるが、よ
り高多孔度の基板を作ることは不可能あるし、工
程上粉末付着工程が伴うために生産性の低下が生
じる。
For example, in Japanese Patent Publication No. 52-15774, an attempt is made to increase the surface porosity by attaching combustible powder to the surface layer of a slurry obtained by a wet method and burning it off during sintering. Similarly, in Japanese Patent Publication No. 53-47492, sintering metal powder is attached to the slurry surface, and the porosity is increased by a mixed method of wet and dry methods. However, the porosity of the sintered substrate obtained by the wet method is generally around 70 to 78%, and although there is a slight increase in porosity due to an increase in surface porosity, it is difficult to create a substrate with higher porosity. Although it is possible, the process involves a powder adhesion step, which causes a decrease in productivity.

一方、非常に高多孔度の電極基板を得る方法と
して特公昭37−8331号に示されるように、無水マ
グネシウム塩、ニツケル塩等の焼結温度付近にお
いて分解膨張する膨張材を混合して焼結基板を製
造する方法があるが、これは分解が急激に起こる
ためにスラリーに適用した場合、芯材から焼結層
が脱落したり、金属粉末間距離が大きすぎて焼結
強度が低くなつたりするために好ましいものでは
ない。
On the other hand, as shown in Japanese Patent Publication No. 37-8331, a method for obtaining an electrode substrate with extremely high porosity is to mix and sinter an expanding material that decomposes and expands near the sintering temperature, such as anhydrous magnesium salt or nickel salt. There is a method for manufacturing the substrate, but this method causes rapid decomposition, so when applied to slurry, the sintered layer may fall off from the core material, or the distance between the metal powders may be too large, resulting in low sintering strength. It's not a good thing to do.

また高多孔度の電極基板を得る方法として発泡
高分子体を所定の厚さにスライスし、これに導電
性塗膜を塗布した後電解メツキを行ない、その後
高分子体を燃焼焼失させて高多孔度の海綿状多孔
基板を得るものがある。また同様に、高分子発泡
体に、ニツケル粉末を振動充填した後、焼結する
ことにより海綿状高多孔体を得る方法も提案され
ている。この方法は、Guy Grespy等により
Power Sources 7(Research and
Development in Non Mechanical Electrical
Power Sources1979)に発表されたものである
が、いずれの方法にせよ、電極用基体内に芯材を
配置できないため、基体そのものの強度が弱く、
また電極として使用する場合のリード端子の取り
出しがきわめて困難であるなど、電極製造時の制
約が大きいため好ましくない。
In addition, as a method of obtaining a highly porous electrode substrate, a foamed polymer is sliced to a predetermined thickness, a conductive coating is applied to this, electrolytic plating is performed, and the polymer is then burned out to create a highly porous electrode substrate. There are some that yield a spongy porous substrate with a degree of pores. Similarly, a method of obtaining a spongy highly porous body by vibrationally filling a polymer foam with nickel powder and then sintering the same has been proposed. This method was developed by Guy Grespy et al.
Power Sources 7 (Research and
Development in Non-Mechanical Electrical
Power Sources (1979), but either method does not allow the core material to be placed inside the electrode substrate, so the strength of the substrate itself is weak.
Further, when used as an electrode, it is extremely difficult to take out the lead terminal, which is undesirable because there are many restrictions when manufacturing the electrode.

さらに特公昭53−8895号に示されるように、ニ
ツケル粉と樹脂球とを混練したペースト物を成形
し有機物を燃焼除去した後焼結して高多孔度の海
綿状ニツケル多孔体を得るものもある。この方法
で高多孔度の焼結基板を作るためには、体積的に
はニツケル粉は少なく、ペースト状物のほとんど
が樹脂球と粘着剤である。このため見掛密度の小
さいニツケル粉を使用したとしても樹脂球をニツ
ケルの数倍の体積混入しないと高多孔度の焼結体
る作ることはできない。また、活物質充填方法に
は種々あるが、活物質ペーストを多孔基板に直接
充填していく方法などにおいては、多孔体の孔経
が、数十〜数百ミクロン必要であるが、このよう
な大きな孔径を得るには、必要孔径相当の樹脂球
を混入する必要があるが、球径があまり大きくな
るとペースト中で、ニツケル粉と球とが分離した
り、スリツトにひつかかつたりするため樹脂球の
大きさにおのずと制限が生じる。このように本来
の目的とする焼結基板を得るために多くの焼失材
量が必要であつたり、焼結基板孔径に制限があつ
たりするため、生産性の良い方法とは言えない。
Furthermore, as shown in Japanese Patent Publication No. 53-8895, a highly porous spongy nickel porous body is obtained by molding a paste made by kneading nickel powder and resin balls, burning off organic matter, and then sintering it. be. In order to make a highly porous sintered substrate using this method, the volume of nickel powder is small, and most of the paste-like material is resin balls and adhesive. For this reason, even if nickel powder with a low apparent density is used, a highly porous sintered body cannot be produced unless resin spheres are mixed in at several times the volume of nickel. In addition, there are various active material filling methods, but in methods such as directly filling an active material paste into a porous substrate, the pore size of the porous body needs to be several tens to hundreds of microns; In order to obtain a large pore size, it is necessary to mix resin spheres with the required pore size, but if the sphere diameter becomes too large, the nickel powder and spheres will separate in the paste or get stuck in the slit, so the resin There is a natural limit to the size of the ball. In this way, a large amount of burnt material is required to obtain the intended sintered substrate, and there are restrictions on the hole diameter of the sintered substrate, so it cannot be said to be a method with good productivity.

また、ニツケルスラリー中で気泡を混入させる
手法が特公昭54−14737号で示されているが、気
泡を経時的に均一に保つことが困難であつたり、
スラリー粘度の違い等により気泡径がバラツクな
どの問題があり、好ましくない。
In addition, a method of mixing air bubbles into a nickel slurry was shown in Japanese Patent Publication No. 14737/1982, but it was difficult to keep the air bubbles uniform over time.
This is not preferable since there are problems such as variations in bubble diameter due to differences in slurry viscosity.

本発明は、上記基板製造法の持つ欠点を解消す
るもので、従来の湿式法による焼結基板製造法と
ほぼ同一の工程で、高多孔度で海綿状の焼結基板
を安価に提供すると同時に高容量密度の極板を提
供することを目的とするものである。
The present invention eliminates the drawbacks of the above-mentioned substrate manufacturing method, and provides a highly porous and spongy sintered substrate at a low cost using almost the same process as the conventional wet method sintered substrate manufacturing method. The purpose is to provide an electrode plate with high capacity density.

本発明は、低沸点炭化水素を内包する熱膨張性
マイクロカプセルとニツケル粉末及び、CMC等
の粘着剤を混合して得られたスラリーを、スリツ
トを通して開孔鉄板等の多孔金属芯材に塗着後、
発泡倍率等を考慮した所定温度で乾燥させ、同時
にマイクロカプセルを発泡させた後に焼結するこ
とによつて芯材を有する3次元的海綿状多孔体が
得られるものである。この方法において熱膨張性
マイクロカプセルは、内包剤の炭化水素により沸
点が異なるのと同時に外皮に用いる樹脂によつて
も軟化点が異なるため、乾燥時の温度によつて発
泡倍率が異なる。このため条件を種々コントロー
ルすることにより種々の大きさの独立気泡性の骨
格を形成し、その気泡間に取り込まれたニツケル
粉が、焼結時に海綿状に融着し同時に膨張したマ
イクロカプセルとCMC等の粘着剤とが焼失され、
結果として高多孔度の焼結基板ができる。この発
泡性のマイクロカプセルは大気圧下では、20〜70
倍の発泡倍率を有するが、乾燥時の粘着剤、例え
ばCMCなどの乾燥が優先すると発泡倍率が低下
し、140℃程度で発泡するものを用い、赤外線ヒ
ータ等で乾燥すれば、CMC水溶液が乾燥した後
に昇温されるため、発泡圧がCMC膜圧を下まわ
るために、事実上発泡させないこともできる。
The present invention involves applying a slurry obtained by mixing thermally expandable microcapsules containing low-boiling hydrocarbons, nickel powder, and an adhesive such as CMC to a porous metal core material such as a perforated iron plate through a slit. rear,
A three-dimensional spongy porous body having a core material is obtained by drying at a predetermined temperature taking into consideration the expansion ratio, etc., and simultaneously foaming the microcapsules and then sintering them. In this method, the thermally expandable microcapsules have different boiling points depending on the hydrocarbon in the encapsulating agent and different softening points depending on the resin used for the outer shell, so the expansion ratio varies depending on the temperature during drying. Therefore, by controlling various conditions, closed-cell skeletons of various sizes are formed, and the nickel powder trapped between the cells fuses into a spongy shape during sintering, simultaneously expanding the microcapsules and CMC. and other adhesives are burned out,
The result is a highly porous sintered substrate. This effervescent microcapsule has a resistance of 20 to 70% under atmospheric pressure.
It has a foaming ratio of twice as much, but if drying of the adhesive, such as CMC, takes priority, the foaming ratio decreases. Since the temperature is raised after the process, the foaming pressure is lower than the CMC membrane pressure, so foaming can be virtually prevented.

以下、本発明の実施例を説明する。 Examples of the present invention will be described below.

実施例 1 焼結用金属粉として、カーボニルニツケル粉末
(比重0.8〜1.0g/c.c.)100重量部、粘着剤として
濃度3%のCMC水溶液100重量部、発泡性マイク
ロカプセルとして、塩化ビニリデン−アクリロニ
トリル主体の共重合体シエルにイソブタンを内包
した8〜10μの粒径のものを5重量部、10重量
部、15重量部各々混練したスラリーを3種作り、
これを開孔鉄板(開孔率54%)に塗着後120℃で
20分乾燥し、引き続いて920℃で30分焼結し、
各々0.7mm厚さの多孔性基板A,B,Cを得た。
これらの焼結基板において発泡倍率は約20倍とな
り、25〜50μ程度の孔径のものであつた。また多
孔度は各々92.5%、95%、96.5%であつた。この
ようにして得られた多孔基板の顕微鏡写真をトレ
ースして図に示した。図において斜線部1は、ニ
ツケル粉末の焼結部分で数ミクロンの小さな孔が
多数存在する。また、白くぬけた部分2は、発泡
性マイクロカプセルにより生成した孔径数十ミク
ロンの孔である。
Example 1 100 parts by weight of carbonyl nickel powder (specific gravity 0.8 to 1.0 g/cc) as metal powder for sintering, 100 parts by weight of CMC aqueous solution with a concentration of 3% as adhesive, and mainly vinylidene chloride-acrylonitrile as foamable microcapsules. Three types of slurry were prepared by kneading 5 parts by weight, 10 parts by weight, and 15 parts by weight of particles with a particle size of 8 to 10 μ containing isobutane in the copolymer shell.
After applying this to a perforated steel plate (porosity 54%), it was heated at 120℃.
Dry for 20 minutes, followed by sintering at 920°C for 30 minutes,
Porous substrates A, B, and C each having a thickness of 0.7 mm were obtained.
In these sintered substrates, the foaming ratio was approximately 20 times, and the pore diameter was approximately 25 to 50 μm. The porosity was 92.5%, 95%, and 96.5%, respectively. A traced micrograph of the porous substrate thus obtained is shown in the figure. In the figure, the shaded area 1 is the sintered part of the nickel powder, and there are many small pores of several microns. In addition, the white areas 2 are pores with a pore size of several tens of microns generated by the foamable microcapsules.

またこのようにして得られた基板A,B,C
と、従来の焼結基板とを通常用いられる化学含浸
法により4モル/の硝酸ニツケル水溶液を用い
て活物質を充填し、ニツケル正極を作成した結
果、従来の基板の活物質充填容量は360mAh/c.c.
であるのに対し、本発明による基板A,B,Cを
用いたものは各々420mAh/c.c.、450mAh/c.c.、
460mAh/c.c.の容量の極板が得られた。
Also, the substrates A, B, and C obtained in this way
and a conventional sintered substrate were filled with an active material using a 4 mol/a nickel nitrate aqueous solution using a commonly used chemical impregnation method to create a nickel positive electrode.As a result, the active material filling capacity of the conventional substrate was 360mAh/ cc
On the other hand, those using substrates A, B, and C according to the present invention have 420 mAh/cc, 450 mAh/cc, and 450 mAh/cc, respectively.
A plate with a capacity of 460 mAh/cc was obtained.

さらに実施例1で使用したマイクロカプセルは
大気圧下では120℃で、50倍程度に膨張するもの
であるが、実際には、20倍程度の発泡倍率しか得
られなかつた。これは120℃で乾燥したために
CMC水溶液中の水分が、沸点(100℃)で先に蒸
発したため、マイクロカプセルの発泡が十分起こ
る前にスラリーが乾燥してしまつたからである。
マイクロカプセルの発泡能力を十分引き出すため
に、次の実験を行なつた。
Further, although the microcapsules used in Example 1 are expected to expand approximately 50 times at 120° C. under atmospheric pressure, in reality, only an expansion ratio of approximately 20 times could be obtained. This is because it was dried at 120℃.
This is because the water in the CMC aqueous solution evaporated first at the boiling point (100°C), so the slurry dried before the microcapsules were sufficiently foamed.
In order to fully utilize the foaming ability of microcapsules, the following experiment was conducted.

実施例 2 実施例1と同一条件であるが、発泡性マイクロ
カプセルのシエル表面を黒色に着色したものを用
い、マイクロカプセル5重量部、15重量部添加し
たスラリーの各々を芯材に塗着し、赤外ヒータで
乾燥後870℃で焼結し、海綿状多孔基板を作つた。
このようにして出きた多孔板の多孔度は、各々
96.5%と98%で、5重量部添加したものは実施例
1におけるマイクロカプセル15重量部添加したも
のと同じとなつた。また、孔径は50〜100ミクロ
ン程度であつた。なお、遠赤外ヒータによる加熱
も同等の効果があつた。
Example 2 The conditions were the same as in Example 1, but using foamable microcapsules whose shell surfaces were colored black, slurries containing 5 parts by weight and 15 parts by weight of microcapsules were applied to the core material. After drying with an infrared heater, the material was sintered at 870°C to create a spongy porous substrate.
The porosity of the perforated plate produced in this way is
At 96.5% and 98%, the addition of 5 parts by weight was the same as the addition of 15 parts by weight of microcapsules in Example 1. Moreover, the pore diameter was about 50 to 100 microns. Note that heating with a far-infrared heater had the same effect.

実施例2で作られた多孔基板に、水酸化ニツケ
ル粉とCMC水溶液とニツケル粉とからなるペー
ストをヘラ状物の往復運動により摺り込む方法に
より活物質を充填しニツケル正極を作成したとこ
ろ、450mAh/c.c.の容量密度の極板を得た。しか
し、多孔度が98%になつたものは活物質充填時
に、基板表面の破壊が正じ充分な充填量は得られ
なかつた。本実施例において、マイクロカプセル
は8〜10μのものを用いたが、百数十ミクロンの
ものの使用においても焼結基板が得られた。また
マイクロカプセルの内包剤はイソブタンで行なつ
たが、製造上常温以上で粘着剤が焼けない程度の
範囲の温度に沸点を有するものと、シエルの軟化
点が接近するものの組合せならば何んでも良い。
A nickel positive electrode was prepared by filling the active material into the porous substrate prepared in Example 2 by sliding a paste consisting of nickel hydroxide powder, CMC aqueous solution, and nickel powder using the reciprocating motion of a spatula-like object. A plate with a capacity density of /cc was obtained. However, when the porosity was 98%, the substrate surface was destroyed when the active material was filled, and a sufficient amount of filling could not be obtained. In this example, microcapsules of 8 to 10 microns were used, but sintered substrates were obtained even when microcapsules of 100-odd microns were used. In addition, the encapsulating agent for the microcapsules was made with isobutane, but any combination of materials with a boiling point above room temperature that does not burn the adhesive and a material with a softening point close to that of the shell can be used. good.

このように本発明による焼結基板の製造法は、
従来の湿式法による焼結基板の製造工程を何ら変
更することなく、単に低沸点炭化水素を内包する
マイクロカプセルをスラリーに少量混入するだけ
で、高多孔度の焼結基板が容易に作れ、またマイ
クロカプセルの材質、内包剤、又は乾燥温度を変
えるだけで、種々の多孔度、孔径を有する多孔基
板が得られる。さらに本発明では従来多く用いら
れている発泡高分子体にメツキ又は金属粉を振動
により充填して得られる海綿状多孔基板では、得
られなかつた芯材を有するため、強度的にも強く
また極板リードの取り出しが容易であるため極板
としての使用が格段に便利なものである。また本
発明によれば使用発泡体量が少ないため、焼結時
に使用する還元ガス量も少なくてすむという利点
がある。
As described above, the method for manufacturing a sintered substrate according to the present invention is as follows:
Highly porous sintered substrates can be easily produced by simply mixing a small amount of microcapsules containing low-boiling hydrocarbons into the slurry, without any changes to the conventional wet method sintered substrate manufacturing process. Porous substrates having various porosity and pore diameter can be obtained by simply changing the material of the microcapsules, the encapsulating agent, or the drying temperature. Furthermore, the present invention has a core material that cannot be obtained with the spongy porous substrate obtained by filling a foamed polymer with plating or metal powder by vibration, which has been widely used in the past, so it is strong and extremely strong. Since the plate lead can be easily taken out, it is extremely convenient to use it as an electrode plate. Further, according to the present invention, since the amount of foam used is small, there is an advantage that the amount of reducing gas used during sintering can also be reduced.

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

図は本発明の実施例による海綿状多孔基板の顕
微鏡写真をトレースしたものである。 1……ニツケル粉末焼結部分、2……空孔部。
The figure is a traced micrograph of a cavernous porous substrate according to an example of the present invention. 1... Nickel powder sintered part, 2... Hole part.

Claims (1)

【特許請求の範囲】 1 スラリーが炭化水素を樹脂製シエルに内包し
たマイクロカプセルと、ニツケル粉末と、粘着剤
との混合物からなり、このスラリーを多孔性金属
芯材に塗着する工程と、 スラリーを塗着した多孔性金属芯材を加熱乾燥
して前記マイクロカプセルを膨張させる工程と、 その後還元雰囲気中で焼結して、ニツケル焼結
部1とマイクロカプセルの離脱により生じた気孔
2とを設ける工程とからなるアルカリ蓄電池用焼
結基板の製造法。 2 スラリー中に混合するマイクロカプセルのシ
エル表面が黒色であり、スラリーを塗着した多孔
性金属芯材の加熱乾燥を赤外線又は遠赤外線で行
なう特許請求の範囲第1項記載のアルカリ蓄電池
用焼結基板の製造法。
[Scope of Claims] 1. A step in which the slurry is made of a mixture of microcapsules containing hydrocarbons in a resin shell, nickel powder, and an adhesive, and the slurry is applied to a porous metal core material; The microcapsules are expanded by heating and drying the porous metal core coated with nickel, and then sintered in a reducing atmosphere to remove the nickel sintered part 1 and the pores 2 generated by the separation of the microcapsules. A method for manufacturing a sintered substrate for an alkaline storage battery, which comprises a step of providing a sintered substrate for an alkaline storage battery. 2. Sintering for an alkaline storage battery according to claim 1, wherein the shell surface of the microcapsules mixed in the slurry is black, and the porous metal core material coated with the slurry is heated and dried using infrared rays or far infrared rays. Substrate manufacturing method.
JP57052477A 1982-03-30 1982-03-30 Manufacturing method of sintered base plate for alkaline storage battery Granted JPS58169773A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57052477A JPS58169773A (en) 1982-03-30 1982-03-30 Manufacturing method of sintered base plate for alkaline storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57052477A JPS58169773A (en) 1982-03-30 1982-03-30 Manufacturing method of sintered base plate for alkaline storage battery

Publications (2)

Publication Number Publication Date
JPS58169773A JPS58169773A (en) 1983-10-06
JPS6359228B2 true JPS6359228B2 (en) 1988-11-18

Family

ID=12915798

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57052477A Granted JPS58169773A (en) 1982-03-30 1982-03-30 Manufacturing method of sintered base plate for alkaline storage battery

Country Status (1)

Country Link
JP (1) JPS58169773A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0229333U (en) * 1988-08-12 1990-02-26

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60205967A (en) * 1984-03-29 1985-10-17 Shin Kobe Electric Mach Co Ltd Manufacture of porous sintered substrate for sealed alkaline battery
JPH02205602A (en) * 1989-02-03 1990-08-15 Nippon Steel Corp Composition for light discontinuous porous metal sintered body and manufacture of sintered body
JPH02277704A (en) * 1989-04-19 1990-11-14 Nippon Steel Corp Closed-cell foamed iron base porous body and manufacture thereof
JP4588288B2 (en) * 2001-07-10 2010-11-24 パナソニック株式会社 Method for manufacturing substrate for electrode plate, method for manufacturing positive electrode plate, and alkaline storage battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5866267A (en) * 1981-10-16 1983-04-20 Yuasa Battery Co Ltd Manufacture of substrate for alkaline storage battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0229333U (en) * 1988-08-12 1990-02-26

Also Published As

Publication number Publication date
JPS58169773A (en) 1983-10-06

Similar Documents

Publication Publication Date Title
JPS58171469A (en) Hollow spherical body free fluidity assembly
JPS6359228B2 (en)
JPS60131765A (en) Nickel positive electrode for batteries and its manufacturing method
JP4079667B2 (en) Sintered substrate for alkaline storage battery and manufacturing method thereof
JPS5956361A (en) Manufacture of substrate for alkaline storage battery
JPH04248269A (en) Manufacture of sintered substrate for alkaline storage battery
JPS6255870A (en) Manufacture of sintered substrate for cell
JP2615538B2 (en) Nickel positive electrode for alkaline storage batteries
JPS60131766A (en) Positive plate for alkaline battery
JPH0734366B2 (en) Battery electrode manufacturing method
JPS5866267A (en) Manufacture of substrate for alkaline storage battery
US3356537A (en) Foamed silver electrode and a method for preparing it
JPS63105469A (en) Manufacture of nickel substrate for alkaline battery
JP3783457B2 (en) Method for producing sintered substrate for alkaline storage battery
JP2798700B2 (en) Method for producing sintered substrate for alkaline storage battery
JPS59195544A (en) Hollow and cellular vitreous granule and its manufacture
JPH11329450A (en) Method for producing sintered substrate for alkaline storage battery
JPS6065464A (en) Manufacture of sintered substrate for battery
JP2680609B2 (en) Method for manufacturing electrode for alkaline storage battery
Choi et al. Microstructure of PTFE and acid absorption behavior in PTFE-bonded carbon electrodes
JP2870125B2 (en) Manufacturing method of non-woven metal sintered sheet
JPS6114636B2 (en)
JP2004183055A (en) Porous liquid absorbing-holding member, and alcohol absorbing-holding member
JPS62154568A (en) Manufacture of plate alkaline storage battery
JP3032421B2 (en) Manufacturing method of nickel positive electrode for batteries