JPS5833667B2 - Manufacturing method for battery electrodes - Google Patents
Manufacturing method for battery electrodesInfo
- Publication number
- JPS5833667B2 JPS5833667B2 JP52126561A JP12656177A JPS5833667B2 JP S5833667 B2 JPS5833667 B2 JP S5833667B2 JP 52126561 A JP52126561 A JP 52126561A JP 12656177 A JP12656177 A JP 12656177A JP S5833667 B2 JPS5833667 B2 JP S5833667B2
- Authority
- JP
- Japan
- Prior art keywords
- active material
- paste
- metal
- foamed metal
- porous body
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000011149 active material Substances 0.000 claims description 80
- 239000002184 metal Substances 0.000 claims description 68
- 229910052751 metal Inorganic materials 0.000 claims description 68
- 239000000126 substance Substances 0.000 claims description 2
- 239000006260 foam Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 12
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 8
- 238000003756 stirring Methods 0.000 description 7
- 239000007864 aqueous solution Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 229910052759 nickel Inorganic materials 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000006262 metallic foam Substances 0.000 description 2
- 238000007790 scraping Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- OJIJEKBXJYRIBZ-UHFFFAOYSA-N cadmium nickel Chemical compound [Ni].[Cd] OJIJEKBXJYRIBZ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 239000011162 core material Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Description
【発明の詳細な説明】
本発明は、連続的に連なった空隙部を有する三次元的構
造の金属多孔体(以下、これを発泡メタルという)を移
動させ、この発泡メタルの空隙部に連続的にペースト状
活物質を充填する電池用電極の製造法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention involves moving a metal porous body having a three-dimensional structure (hereinafter referred to as foamed metal) having continuously connected voids, and The present invention relates to a method for manufacturing a battery electrode in which a paste-like active material is filled in a battery electrode.
現在、良く知られているアルカリ蓄電池用陽極の代表的
なものは焼結式電極である。Currently, a typical well-known anode for alkaline storage batteries is a sintered electrode.
この電極は、ニッケル、ニッケルメッキ鉄等の金属ネッ
トや薄型多孔板とともにニッケル粉末を殆んどカロ圧す
ることなくカーボン型内に充填し、次に水素気流中にお
いて、例えば900℃程度の温度で焼結した多孔度70
〜so%の多孔性基板を用いるものである。This electrode is made by filling a carbon mold with nickel powder together with a metal net made of nickel, nickel-plated iron, etc. or a thin porous plate with almost no caloric pressure, and then baking it at a temperature of about 900°C in a hydrogen stream. Combined porosity 70
~so% porous substrate is used.
活物質を充填するには、前記の基板に高濃度の硝酸ニッ
ケル水溶液を含浸し、乾燥後高温の濃厚か性アルカリ水
溶液中で電解波水洗、乾燥するか、あるいは、単にアル
カリ水溶液中に浸漬後、乾燥加熱分解するなどの方法が
ある。To fill the active material, the above substrate is impregnated with a highly concentrated nickel nitrate aqueous solution, dried, washed with electrolytic waves in a concentrated caustic alkaline aqueous solution at high temperature, and dried, or simply immersed in an alkaline aqueous solution. There are methods such as drying and heating decomposition.
これらの製造法は、活物質の充填工程が煩雑で、しかも
繰り返し充填を行う必要があるので、製造工程の合理化
が要望されていた。These manufacturing methods require a complicated filling process of the active material and require repeated filling, so there has been a demand for rationalization of the manufacturing process.
この問題を改善する1つの方法として、無焼結電極が提
案されている。A non-sintered electrode has been proposed as one method to improve this problem.
この電極は、金属ネットの芯材に結着剤と混合した活物
質を塗り込み、加圧して製造されるが、活物質の脱落が
生じ易く、それによる容量低下が早いとともに、活物質
を多く充填することが困難であった。This electrode is manufactured by applying active material mixed with a binder to the core material of a metal net and applying pressure. It was difficult to fill.
これに対して、活物質保持体として、発泡メタルを使用
し、この発泡メタル内に、結着剤と混合したペースト状
活物質を充填し、加圧して得られる電極は、三次元的構
造の発泡状メタル内部に活物質を充填するため、活物質
の脱落による容量低下も少なく、また活物質を高密度に
充填できることから、高容量が期待できる。On the other hand, an electrode with a three-dimensional structure is obtained by using a foamed metal as an active material holder, filling the foamed metal with a paste-like active material mixed with a binder, and applying pressure. Since the active material is filled inside the foamed metal, there is little capacity loss due to active material falling off, and high capacity can be expected because the active material can be packed at a high density.
ところが、この発泡メタルの長尺物を用いて、これに連
続的に活物質を充填する場合、単に発泡メタルをペース
ト状の活物質中を通過させるだけでは、活物質が発泡メ
タルの内部まで均一に充填されないという問題点を生じ
た。However, when using a long piece of foamed metal to continuously fill it with active material, simply passing the foamed metal through the paste-like active material does not allow the active material to be uniformly distributed inside the foamed metal. This caused the problem that the liquid was not filled.
また、鉛電極の活物質練塗法のように、加圧ローラなど
により活物質を押し込み充填する方法は、発泡メタルの
開孔が小さいことと、耐圧縮強度が弱く容易に表面の開
孔が目つぶしされることなどにより採用することができ
ない。In addition, methods such as the active material kneading method for lead electrodes, in which the active material is pressed and filled using a pressure roller, etc., have small pores in the foamed metal, and the compressive strength is weak, so surface pores easily form. They cannot be hired because they are blinded.
本発明は、以上の点に鑑み、発泡メタルにペースト状活
物質を密にかつ円滑に充填する方法を提供するものであ
る。In view of the above points, the present invention provides a method for densely and smoothly filling a foamed metal with a paste-like active material.
すなわち、本発明は、長尺帯状の発泡メタルe上面にペ
ースト状活物質を供給し、この活物質を発泡メタルの上
面部を往復運動する擦り具により擦って発泡メタルの空
隙部に充填することを特徴とするものである。That is, the present invention supplies a paste-like active material to the top surface of a long strip-shaped foamed metal e, and rubs the active material with a rubbing tool that reciprocates on the top surface of the foamed metal to fill the voids in the foamed metal. It is characterized by:
この方法によれば、ペースト状活物質は擦り具により擦
られて少しずつ充填されるので、発泡メタルには大きな
圧縮力が加わらず二表面の開孔が目つぶしされることは
なく、次々と擦り込まれる活物質により空隙部は満たさ
れ、高密度に充填することができる。According to this method, the paste-like active material is rubbed with a rubbing tool and filled little by little, so a large compressive force is not applied to the foamed metal, the pores on the two surfaces are not closed, and the paste is rubbed one after another. The voids are filled with the active material contained in the active material, and can be filled with high density.
また、このような方法を採るとき、発泡メタルは、活物
質を収容したペースト槽C上部に配置し。Moreover, when adopting such a method, the foamed metal is placed above the paste tank C containing the active material.
発泡メタル下方のペースト槽内において活物質を攪拌し
ながら活物質を発泡メタルの周辺から上面部へ供給する
ようにするのが好都合である。It is convenient to supply the active material from the periphery of the foamed metal to the upper surface while stirring the active material in the paste tank below the foamed metal.
この方法によるときは、後述のように、発泡メタル上面
部における擦り込みによる加圧に対応して、下面部では
減圧作用が生じ、充填効率が一層向上する。When using this method, as will be described later, in response to the pressurization caused by rubbing on the upper surface of the foam metal, a depressurizing effect occurs on the lower surface, further improving the filling efficiency.
以下、本発明を実施例により説明する。The present invention will be explained below using examples.
まず、連続型の活物質充填装置の構成について説明する
。First, the configuration of a continuous active material filling device will be explained.
市販の水酸化ニッケル粉末に導電材料としてニッケル粉
末を10咎程加え、よく混合攪拌し、次に適量の水又は
カルボキシメチルセルロース水溶液を加え、更に良く攪
拌してペースト状の活物質とする。Approximately 10 tons of nickel powder as a conductive material is added to commercially available nickel hydroxide powder, mixed well and stirred. Next, an appropriate amount of water or carboxymethyl cellulose aqueous solution is added and further stirred to form a paste-like active material.
このペースト状活物質を活物質容器2の中に入れ、攪拌
機駆動モータ12を作動させ、回転式攪拌機11を回転
させて、更にペースト状活物質3をよく混練する。This paste-like active material is put into the active material container 2, the stirrer drive motor 12 is operated, the rotary stirrer 11 is rotated, and the paste-like active material 3 is further kneaded well.
なお、ペースト状活物質3の量は、容器2の上部に配し
た多孔板13より上部に来るように調節する。Note that the amount of paste-like active material 3 is adjusted so that it is above the porous plate 13 disposed at the top of the container 2.
長尺物の発泡メタル1は、主軸ローラ7から補助ローラ
9を通し、多孔板13と擦り具4に取り付けである刷毛
5との間から、補助ローラ10を通し、主軸ローラ8ま
で、まず手動させてから、自動的に主軸ローラ7.8を
回転させて長尺物の発泡メタルを移動させるようにする
。The elongated foamed metal 1 is first passed manually from the main shaft roller 7 to the auxiliary roller 9, from between the perforated plate 13 and the brush 5 attached to the scrubbing tool 4, through the auxiliary roller 10, and then to the main shaft roller 8. After that, the main shaft roller 7.8 is automatically rotated to move the long metal foam.
主軸ローラ7.8を作動させると同時に、擦り具4を擦
り具駆動モータ6で発泡メタルの移動方向に沿って摺動
動作させる。At the same time as the main shaft roller 7.8 is actuated, the rubbing tool 4 is caused to slide along the moving direction of the foamed metal by the rubbing tool drive motor 6.
このように、ペースト状活物質は連続的に移動する長尺
物の発泡メタルの中に、攪拌機11と擦り具4の発泡メ
タル上での摺動運動によって充填される構成になってい
る。In this way, the paste-like active material is filled into the continuously moving elongated foamed metal by the sliding movement of the stirrer 11 and the scraper 4 on the foamed metal.
その構成略図を第1図及び第2図に示した。A schematic diagram of its configuration is shown in FIGS. 1 and 2.
なお、発泡メタルは連続的に移動させても間けつ的に移
動させてもよい。Note that the foam metal may be moved continuously or intermittently.
次にペースト状活物質の充填機構について説明する。Next, the filling mechanism of the paste active material will be explained.
まず、攪拌機11、擦り具4を駆動させた後、主軸ロー
ラ7.8を駆動させ、長尺物の発泡メタル1を少しずつ
移動させる。First, after driving the agitator 11 and the scraping tool 4, the main shaft roller 7.8 is driven to move the elongated foamed metal 1 little by little.
攪拌機11は第2図に示す如く4枚羽根を持ったものを
2組使用し、容器2の中央部から周辺部に活物質が加圧
され盛り上がって移動するように回転させ、活物質が発
泡メタルの表面部に移動しつつ、同時に擦り具が発泡メ
タルの進行方向に対して、平行運動することによって、
発泡メタルの上面部の活物質をゴム製の刷毛で擦る操作
を行うことになる。The stirrer 11 uses two sets of four blades as shown in Fig. 2, and is rotated so that the active material is pressurized and moves from the center of the container 2 to the periphery, causing the active material to foam. While moving to the surface of the metal, at the same time the rubbing tool moves parallel to the direction of travel of the foam metal,
The active material on the top surface of the foam metal is rubbed with a rubber brush.
この擦り具の運動は上記方向に限らず、また往復運動し
てもよい。The movement of this rubbing tool is not limited to the above-mentioned direction, but may also be a reciprocating movement.
ただし、上記のように発泡メタルの移動方向に平行運動
する場合において、充填状態が最もよい。However, the filling state is best when the foam metal moves parallel to the moving direction as described above.
このような操作をすべて連続的に行い、発泡メタルの中
に活物質を連続的に充填する。All of these operations are performed continuously to continuously fill the active material into the foamed metal.
活物質の充填条件は次の通りである。The conditions for filling the active material are as follows.
使用した発泡メタルは幅15cnL、長さ5m、厚さ2
.5mm。The foam metal used is 15 cm wide, 5 m long, and 2 thick.
.. 5mm.
多孔度96±1%、活物質の充填部分の総容量は約50
1とし、充填装置内にはペースト状活物質を約80に2
収容させた。Porosity: 96±1%, total volume of active material filling area: approximately 50%
1, and the paste active material is placed in the filling device approximately 80% by 2.
It was accommodated.
ゴム刷毛をもつ擦り具は、幅16cm、厚さ3闘として
10枚を使い、擦り具の振幅は80mm、その速度は1
サイクル/秒である。The rubbing tool with a rubber brush has a width of 16 cm, a thickness of 3, and 10 sheets are used, the amplitude of the rubbing tool is 80 mm, and the speed is 1.
cycles/second.
攪拌機の回転速度は3〜5回転/秒、発泡メタルの移動
速度は0.5 mm 7秒、ペースト中の固形分濃度は
約70重量φとした。The rotational speed of the stirrer was 3 to 5 revolutions/second, the moving speed of the foamed metal was 0.5 mm 7 seconds, and the solid content concentration in the paste was about 70 weight φ.
これらの諸条件を基にして、更に詳細なペースト状活物
質の充填状況を第3図に示す。Based on these conditions, a more detailed filling situation of the paste active material is shown in FIG.
第3図のAは、攪拌機における活物質の移動状況を示し
、他の例として、第3図のB、第3図のCに示すように
、横型攪拌機14による活物質の移動状況を取りあげた
。A in FIG. 3 shows the movement of the active material in the stirrer, and as other examples, B in FIG. 3 and C in FIG. 3 show the movement of the active material in the horizontal stirrer 14. .
第3図のAにおいて、2個の攪拌機11は、各々中央部
から周辺部に活物質を移動するように回転している。In FIG. 3A, the two stirrers 11 are rotating so as to move the active material from the center to the periphery.
即ち、活物質を中央部から周辺部を通して、発泡メタル
の上面部まで盛り上げるように攪拌する。That is, the active material is stirred from the center, through the periphery, and up to the upper surface of the foam metal.
従って、中央部が減圧状態になり、発泡メタルの下面部
で減圧(吸引)現象が発生し、周辺から盛り上がって移
動して来た活物質が、発泡メタルの上面部で擦り具の刷
毛で擦られながら、発泡メタル中に移動して行く作用を
受けることになる。Therefore, the central part becomes depressurized, a depressurization (suction) phenomenon occurs at the lower surface of the foam metal, and the active material that has risen and moved from the periphery is rubbed by the brush of the rubbing tool on the upper surface of the foam metal. The foamed metal is moved into the foamed metal.
活物質は発泡メタルの上面部より、内部に入って、一部
分は下面部より通りぬけつつ、次第に発泡メタル全体に
均一に活物質が充填されるようになる一種の呼吸式攪拌
で、加圧部分(盛上げ部分)とそれに対応して減圧部分
を作って、効率良く活物質が充填される。The active material enters the inside of the foamed metal from the top surface, and a portion of it passes through the bottom surface, gradually filling the entire foamed metal with the active material uniformly. (a raised part) and a corresponding reduced pressure part are created to efficiently fill the active material.
これは単に攪拌による場合と比較しても充填効率が向上
する。This improves the filling efficiency compared to simply stirring.
従って、より効果的な充填法である。Therefore, it is a more effective filling method.
また、攪拌機が横型の場合でも、第3図のB。Also, even if the stirrer is horizontal, B in Figure 3.
Cに示すように、発泡メタルの進行方向に直角に板状の
攪拌機で横方向に移動させる(又は水平に移動させる)
と、活物質を押す方向に、活物質が一方の周辺に盛り上
がり、発泡メタルの上面部に押しやられる。As shown in C, move the foam metal horizontally (or move it horizontally) with a plate-shaped stirrer perpendicular to the direction of travel of the foam metal.
Then, in the direction of pushing the active material, the active material bulges around one side and is pushed to the upper surface of the foamed metal.
それに対応して、反対側方向は引張られる方向となるの
で、少し減圧方向となり、発泡メタルの下面部を吸引す
ることになる。Correspondingly, since the opposite direction is the direction of tension, the pressure is slightly reduced, and the lower surface of the foamed metal is sucked.
図中太い矢印が活物質を吸引している方向を示している
。In the figure, the thick arrow indicates the direction in which the active material is being sucked.
このように活物質が発泡メタルの上面部において擦り具
で加圧され、下面部で吸引されるので、一種の活物質の
循環が起こり、発泡メタルの内部まで十分に活物質が充
填されることになる。In this way, the active material is pressurized by the rubbing tool on the top surface of the foamed metal and sucked in on the bottom surface, so a kind of circulation of the active material occurs, and the active material is sufficiently filled to the inside of the foamed metal. become.
以上のように加圧作用(押し上げ、擦り込み)と減圧(
引張り)作用とを取り入れた攪拌充填方法により、より
効率よく、多くの活物質を均一に発泡メタル中に充填す
ることができ、量産性に優れたアルカリ蓄電池用電極の
製造法である。As mentioned above, pressure action (pushing up, rubbing) and depressurization (
This is a method for manufacturing electrodes for alkaline storage batteries that can be more efficiently and uniformly filled with a large amount of active material into a foamed metal using a stirring filling method that incorporates a tensile action.
ペースト状活物質の攪拌方向は、発泡メタルの進行方向
に対して直角方向になるようにすることが望ましい。It is desirable that the direction of stirring of the paste-like active material is perpendicular to the direction of movement of the foamed metal.
活物質の押し上げ、そして発泡メタル上への盛り上がり
が、周辺部より発生するようにしなければ、効率良く活
物質を充填することができない。The active material cannot be efficiently filled unless the active material is pushed up and bulges onto the foamed metal from the periphery.
発泡メタルの下面部のみの攪拌に終わってしまうと充填
量は低下する。If only the bottom surface of the foamed metal is stirred, the amount of filling will decrease.
従って、発泡メタルの進行方向と攪拌時の活物質の移動
方向とは直角方向が効果的である。Therefore, it is effective that the traveling direction of the foamed metal is perpendicular to the moving direction of the active material during stirring.
単に活物質を攪拌するだけでも充填されるが、充填量が
不均一になりやすい。Although the active material can be filled simply by stirring, the amount of filling tends to be uneven.
次に発泡メタルの表面を擦る方向であるが、発泡メタル
の進行方向に対して、平行となることが望ましい。Next, the direction in which the surface of the foamed metal is rubbed is preferably parallel to the direction in which the foamed metal travels.
例えば、移動する発泡メタルの進行方向と直角方向に擦
り具を動かせば、折角周辺部より盛り上がって来た活物
質を押し返して、元に戻すことになって、発泡メタルの
上面部で効率良く活物質を充填することができない。For example, if you move the scraping tool in a direction perpendicular to the direction of movement of the moving foam metal, the active material that has risen from the periphery will be pushed back and returned to its original state, allowing it to be efficiently activated on the top surface of the foam metal. Cannot be filled with substances.
すなわち、発泡メタル上面部の活物質を、発泡メタルを
通すことなく下に押しやってしまい、充填効率を非常に
悪くする。That is, the active material on the upper surface of the foamed metal is pushed downward without passing through the foamed metal, resulting in a very poor filling efficiency.
従って、移動する発泡メタルの進行方向に対して、平行
に活物質の擦り操作を行うことがより効果的である。Therefore, it is more effective to perform the rubbing operation of the active material parallel to the traveling direction of the moving metal foam.
なお、上記実施例においては、発泡メタルの下面側で活
物質を攪拌して供給するようにしたが、攪拌したペース
トを発泡メタルの上面から供給してもよい。In the above embodiment, the active material was stirred and supplied from the lower surface of the foam metal, but the stirred paste may be supplied from the upper surface of the foam metal.
しかし充填状態は実施例の場合の方が優れている。However, the filling condition in the example is better.
攪拌することによって活物質の沈降防止、濃度分布の不
均一を防止でき、多くの活物質を充填できる。By stirring, the active material can be prevented from settling and the concentration distribution can be prevented from becoming uneven, and a large amount of the active material can be filled.
次に第1図に示す装置で、活物質を充填した長尺物の発
泡メタルを適当な大きさに切断し、乾燥後、3重量φの
フッ素樹脂分散液中に浸漬して引き上げ、半乾燥の状態
で、400 Kp/mの圧力で厚さ方向に加圧し、完全
乾燥した後、50X55mmの大きさに切断し、リード
端子を取付けてニッケル電極とした。Next, using the apparatus shown in Figure 1, the long foamed metal filled with the active material is cut into appropriate sizes, dried, immersed in a 3 weight φ fluororesin dispersion, pulled out, and semi-dried. After applying pressure in the thickness direction at a pressure of 400 Kp/m and completely drying, it was cut into a size of 50 x 55 mm, and a lead terminal was attached to form a nickel electrode.
上記のようにして長尺物の発泡メタルの適当な位置から
10枚程無作意に選んだ電極について以下のような容量
の比較試験をした。As described above, about 10 electrodes were randomly selected from appropriate positions on a long piece of foamed metal, and the following capacity comparison test was conducted.
比較例の電極イとしては、一般に市販されているニッケ
ルーカドミウム電池に採用されている焼結式ニッケル陽
極を用いた。As the electrode in the comparative example, a sintered nickel anode, which is generally used in commercially available nickel-cadmium batteries, was used.
その容量は公称IAh、電極の大きさ50iiX55m
m、厚さ1.1mmである。Its capacity is nominal IAh, electrode size 50ii x 55m
m, and the thickness is 1.1 mm.
また、上記と同じ発泡メタルを単にペースト状の活物質
中を0.5 rnm 7秒の速さで通過させ、通過時間
10分間として、発泡メタルに活物質を充填させ、その
後は、上記の実施例と同様な方法で電極とした。In addition, the same foamed metal as above was simply passed through the paste-like active material at a speed of 0.5 rnm for 7 seconds, the passing time was 10 minutes, the foamed metal was filled with the active material, and then the above procedure was carried out. An electrode was prepared in the same manner as in the example.
これを口とし、上記実施例による電極をハとする。This will be referred to as a mouth, and the electrode according to the above embodiment will be referred to as C.
容量試験は、電極イは0.2A、電極口、ハは0.4A
のいずれも約5時間率(0,2C)で放電し、放電量の
130〜140饅程度充電する充放電サイクルを繰り返
し、容量が安定した10サイクル目の容量で比較した。For the capacitance test, electrode A is 0.2A, and electrode port C is 0.4A.
All of the batteries were discharged at a rate of about 5 hours (0.2C), and charge/discharge cycles were repeated in which the batteries were charged to about 130 to 140 of the discharge amount, and the capacity at the 10th cycle, when the capacity was stable, was compared.
その時の放電特性を第4図に示す。The discharge characteristics at that time are shown in FIG.
各電極の放電容量は、同一大きさの電極で比較した場合
、電極イは1.2±0. I A h%電極口は1.4
5±0.25Ahであり、本発明の電極ハは2.0±0
. I A hと電極イの1.8倍程度である。When comparing electrodes of the same size, the discharge capacity of each electrode is 1.2±0. I A h% electrode port is 1.4
5±0.25Ah, and the electrode C of the present invention is 2.0±0
.. I A h is about 1.8 times that of electrode A.
また、電極口は、同じ発泡メタルを用いているが、内蔵
する活物質の量が大きくバラツキ、しかも充填量も本発
明品よりも非常に少ない。In addition, although the same foamed metal is used for the electrode port, the amount of active material contained therein varies widely, and the filling amount is also much smaller than that of the product of the present invention.
電極口を切断すると活物質が内部まで均一に充填されて
いないことが確認された。When the electrode opening was cut, it was confirmed that the active material was not evenly filled inside.
容量バラツキも本発明品と比較して2倍以上も大きく、
実用上問題となる。The capacity variation is also more than twice as large compared to the product of the present invention.
This poses a practical problem.
以上のように、本発明は三次元的構造の金属多孔体に活
物質をペースト状にして擦り具で擦りながら充填してい
るので、活物質を密に、かつスムースに充填することが
できる。As described above, in the present invention, the three-dimensionally structured metal porous body is filled with the active material in the form of a paste while being rubbed with a rubbing tool, so that the active material can be filled densely and smoothly.
第1図は本発明の実施例で用いた連続型活物質充填装置
の構成略図、第2図は同装置の断面略図、第3図A、B
、Cはペー・スト状活物質の充填状況を示し、Aは回転
式攪拌機を用いた例、B、Cは横型攪拌機を用いた例で
あり、第4図は各種電極の放電容量特性の比較図である
。
1・・・・・・発泡メタル、2・・・・・・容器(ペー
スト槽)、3・・・・・・ペースト状活物質、4・・・
・・・擦り具、11゜14・・・・・・攪拌機、13・
・・・・・多孔板。Fig. 1 is a schematic diagram of the configuration of a continuous active material filling device used in an example of the present invention, Fig. 2 is a schematic cross-sectional diagram of the same device, and Figs. 3A and B
, C shows the filling status of paste-like active material, A shows an example using a rotary stirrer, B and C show an example using a horizontal stirrer, and Figure 4 shows a comparison of discharge capacity characteristics of various electrodes. It is a diagram. 1... Foamed metal, 2... Container (paste tank), 3... Paste active material, 4...
...Rubbing tool, 11゜14...Stirrer, 13.
...Perforated plate.
Claims (1)
状の金属多孔体の上面にペースト状活物質を供給し、こ
の活物質を前記多孔体の上面部を往復運動する擦り具に
より擦って前記多孔体の空隙部に充填することを特徴と
する電池用電極の製造法。 2 連続的に連なった空隙部を有する三次元的構造の帯
状の金属多孔体をペースト槽の上部に配し、ペースト槽
内のペースト状活物質を前記多孔体の下面において攪拌
するとともに、この活物質を前記多孔体に対してその周
辺から上面部へ供給し、前記多孔体C上面部を往復運動
する擦り具により前記活物質を擦って多孔体の空隙部へ
充填することを特徴とする電池用電極の製造法。[Scope of Claims] 1. A paste-like active material is supplied to the upper surface of a three-dimensionally structured band-shaped porous metal body having continuously connected voids, and the active material is reciprocated on the upper surface of the porous body. A method for producing a battery electrode, characterized in that the voids in the porous body are filled by rubbing with a rubbing tool. 2 A strip-shaped metal porous body having a three-dimensional structure having continuous voids is placed on the top of a paste tank, and the paste-like active material in the paste tank is stirred on the lower surface of the porous body, and the active material is stirred at the bottom of the porous body. A battery characterized in that a substance is supplied to the upper surface of the porous body from its periphery, and the active material is rubbed by a rubbing tool that reciprocates on the upper surface of the porous body C to fill the voids of the porous body. Method of manufacturing electrodes for use.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52126561A JPS5833667B2 (en) | 1977-10-20 | 1977-10-20 | Manufacturing method for battery electrodes |
| US05/952,542 US4217939A (en) | 1977-10-20 | 1978-10-18 | Method for manufacturing electrode for battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP52126561A JPS5833667B2 (en) | 1977-10-20 | 1977-10-20 | Manufacturing method for battery electrodes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5458835A JPS5458835A (en) | 1979-05-11 |
| JPS5833667B2 true JPS5833667B2 (en) | 1983-07-21 |
Family
ID=14938205
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP52126561A Expired JPS5833667B2 (en) | 1977-10-20 | 1977-10-20 | Manufacturing method for battery electrodes |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5833667B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63129784U (en) * | 1987-02-18 | 1988-08-24 | ||
| JPS63184288U (en) * | 1987-05-20 | 1988-11-28 | ||
| JPH0183984U (en) * | 1987-11-27 | 1989-06-05 |
-
1977
- 1977-10-20 JP JP52126561A patent/JPS5833667B2/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63129784U (en) * | 1987-02-18 | 1988-08-24 | ||
| JPS63184288U (en) * | 1987-05-20 | 1988-11-28 | ||
| JPH0183984U (en) * | 1987-11-27 | 1989-06-05 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5458835A (en) | 1979-05-11 |
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