JPS5931833B2 - Manufacturing method for battery electrodes - Google Patents
Manufacturing method for battery electrodesInfo
- Publication number
- JPS5931833B2 JPS5931833B2 JP53060125A JP6012578A JPS5931833B2 JP S5931833 B2 JPS5931833 B2 JP S5931833B2 JP 53060125 A JP53060125 A JP 53060125A JP 6012578 A JP6012578 A JP 6012578A JP S5931833 B2 JPS5931833 B2 JP S5931833B2
- Authority
- JP
- Japan
- Prior art keywords
- active material
- binder
- electrode
- manufacturing
- 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.)
- Expired
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 16
- 239000011149 active material Substances 0.000 claims description 52
- 239000011230 binding agent Substances 0.000 claims description 38
- 239000002184 metal Substances 0.000 claims description 22
- 229910052751 metal Inorganic materials 0.000 claims description 22
- 238000001035 drying Methods 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 12
- 239000011148 porous material Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 5
- 238000011049 filling Methods 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 4
- 239000006185 dispersion Substances 0.000 description 17
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 13
- 239000006260 foam Substances 0.000 description 6
- 229910052759 nickel Inorganic materials 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000005470 impregnation Methods 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 3
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 239000004020 conductor Substances 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000007865 diluting Methods 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000011550 stock solution Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 102100025490 Slit homolog 1 protein Human genes 0.000 description 1
- 101710123186 Slit homolog 1 protein Proteins 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000010981 methylcellulose Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- BFDHFSHZJLFAMC-UHFFFAOYSA-L nickel(ii) hydroxide Chemical compound [OH-].[OH-].[Ni+2] BFDHFSHZJLFAMC-UHFFFAOYSA-L 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000010287 polarization Effects 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 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】
本発明は三次元的構造を有し、連続的に連なつた空孔を
有するスポンジ状金属多孔体(以下発泡メタルと称す)
の空孔内に、ペースト状活物質を充填する工程を含む電
池用電極の製造法の改良に関する。Detailed Description of the Invention The present invention provides a sponge-like porous metal body (hereinafter referred to as foam metal) having a three-dimensional structure and continuously connected pores.
The present invention relates to an improvement in a method for manufacturing a battery electrode, which includes a step of filling the pores with a paste-like active material.
従来における電池用電極の代表的な製造法は、焼結多孔
体に活物質の塩溶液を含浸し、これを電解、加熱分解、
化学処理などにより活物質に転化する方法と、格子や穴
あき板などの導電性多孔体にペースト状にした活動性を
塗着する方法である。The typical manufacturing method for battery electrodes in the past involves impregnating a sintered porous body with a salt solution of an active material, which is then subjected to electrolysis, thermal decomposition,
There are two methods: one is to convert it into an active material through chemical treatment, and the other is to apply a paste-like active material to a conductive porous body such as a grid or perforated plate.
焼結体を用いる場合は、電極性能が優れているが、含浸
・転化を数回から10回以上繰り返す必要があり、工程
が煩雑である欠点を有する。一方、格子などの導電性多
孔体にペーストを塗着する方法は、焼結体の場合に比較
して製造は簡単であり、しかも導電性多孔体として、ス
クリーン、エキスパンデツドメタル、孔あき板等を用い
ると連続的な製法も可能である。When a sintered body is used, the electrode performance is excellent, but it has the disadvantage that impregnation and conversion must be repeated from several times to 10 or more times, making the process complicated. On the other hand, the method of applying paste to conductive porous bodies such as grids is easier to manufacture than sintered bodies, and can be used as conductive porous bodies such as screens, expanded metals, perforated plates, etc. Continuous manufacturing methods are also possible.
しかし、この場合は、活物質が結着剤等で導電体と結合
してしまい、その結果導電体との接触がはるかに少なく
なるため、電圧・寿命いずれの点でも焼結体を用いるも
のには及ばない。なお、焼結体を用いて塗着法が採用で
きると、両者の長所のみを生かすことができるが、従来
の焼結体では孔が小さく、したがつて活物質粉末を内部
まで均一に充填することは不可能である。ところが、最
近注目されている発泡メタルの場合は、多孔度をたとえ
90%以上としても、その孔径を活物質の粒径より大き
くすることは容易であり、したがつてこのような塗着法
を採用することができる。However, in this case, the active material is bound to the conductor using a binder, etc., and as a result, the contact with the conductor is much less, so it is not possible to use a sintered body in terms of both voltage and lifespan. It doesn't reach. Note that if the coating method can be adopted using a sintered body, the advantages of both methods can be utilized, but the pores of conventional sintered bodies are small, so it is difficult to uniformly fill the active material powder inside. That is impossible. However, in the case of foam metal, which has been attracting attention recently, even if the porosity is 90% or more, it is easy to make the pore size larger than the particle size of the active material, so this coating method is not suitable. Can be adopted.
すなわち、活物質粉末、必要に応じて加える導電性粉末
、それに結着剤とその溶媒を含むペースト状混合物を発
泡メタルに充填すれば活物質の塩溶液を加える場合のよ
うな転化処理を必要とせず、工程を簡略化できるととも
に、発泡メタルは三次元的構造を有するので導電性の点
でも優れた特性の電極が得られる。しかし、この発泡メ
タルは、一般の二次元的な広がりを持つたスクリーン・
穴あき板等と異なり三次元的な構造を有するので、その
空孔内へ活物質を充填するには工夫を要する。In other words, if a paste-like mixture containing an active material powder, an optional conductive powder, a binder and its solvent is filled into a foamed metal, no conversion process is required as in the case of adding a salt solution of the active material. First, the process can be simplified, and since the foamed metal has a three-dimensional structure, an electrode with excellent conductivity can be obtained. However, this foamed metal is not suitable for ordinary screens with two-dimensional expansion.
Unlike a perforated plate, etc., it has a three-dimensional structure, so it requires some ingenuity to fill the pores with active material.
すなわち、二次元的構造の多孔体に塗着する場合のよう
に、粘度の高いペーストを用いることはできず、含水率
が高く、流動性の大きいペーストを用いる必要がある。
この場合、ペーストに加えられる結着剤も水溶性のカル
ボキシメチルセルロースなどむしろペーストの練合剤と
して用いられ、恒久的な結着力を期待できるものでない
ものが好ましい。このようなペーストを充填した電極は
、その後の製造工程や電池組立後に活物質が脱落する不
都合がある。そこで、発泡メタルに活物質を充填した後
乾燥し、結着剤を含浸する方法が採られる。この方法に
よれば、乾燥後の活物質層に形成される細孔に結着剤が
浸透するので、少量の結着剤で活物質の脱落を有効に防
止することができる。この場合に用いる結着剤はフツ素
樹脂やポリエチレンなど耐電解液性のもので、細孔への
浸透性に優れる分散液が適している。しかしながら、乾
燥工程から結着剤の含浸工程において活物質の脱落を生
じる問題があつた。That is, it is not possible to use a paste with high viscosity, as in the case of coating a porous body with a two-dimensional structure, and it is necessary to use a paste with a high water content and high fluidity.
In this case, the binder added to the paste is preferably one that is used as a kneading agent for the paste, such as water-soluble carboxymethyl cellulose, and is not expected to have a permanent binding force. Electrodes filled with such a paste have the disadvantage that the active material may fall off during subsequent manufacturing processes or battery assembly. Therefore, a method is adopted in which a foamed metal is filled with an active material, dried, and then impregnated with a binder. According to this method, since the binder permeates into the pores formed in the active material layer after drying, it is possible to effectively prevent the active material from falling off with a small amount of binder. The binder used in this case is one that is resistant to electrolyte such as fluororesin or polyethylene, and a dispersion liquid that has excellent permeability into pores is suitable. However, there was a problem in that the active material fell off during the drying process to the binder impregnation process.
特に結着剤の分散液を用いる場合は、分散液中に発泡メ
タルを浸漬した際活物質中の細孔から逃げる空気が気泡
となるため、発泡メタル表面近傍の活物質が気泡により
脱落させられることになる。その結果品質の一定した電
極を得るのが困難であつた。本発明は、以上のような従
来の不都合を解消するもので、発泡メタルに充填したペ
ースト状活物質の湿潤状態において、表面に結着剤を含
む溶液または分散液を散布する工程を付加することを特
徴とする。Particularly when using a binder dispersion, when the foamed metal is immersed in the dispersion, the air that escapes from the pores in the active material becomes bubbles, causing the active material near the surface of the foamed metal to fall off due to the bubbles. It turns out. As a result, it has been difficult to obtain electrodes of consistent quality. The present invention solves the above-mentioned conventional inconveniences by adding a step of spraying a solution or dispersion containing a binder on the surface of a paste-like active material filled in a foamed metal in a wet state. It is characterized by
本発明によれば、活物質の湿潤状態で散布される結着剤
は活物質の内部まで浸透せず、次の乾燥工程から結着剤
の含浸工程において脱落しやすい表面部の活物質に結着
力を付与することができる。According to the present invention, the binder that is sprayed while the active material is wet does not penetrate into the active material and forms a bond on the surface of the active material that is likely to fall off during the subsequent drying process and binder impregnation process. It can impart adhesion.
そして乾燥後に含浸される結着剤によつて発泡メタル内
部の活物質に対しても十分な結着力が付与され、放電時
の膨張、収縮にも耐える強固な電極となる〇なお、活物
質の湿潤状態では結着剤は内部まで浸透しないので、最
初の結着剤液の散布のみによつて活物質全体に結着力を
付与することはできない。The binder impregnated after drying provides sufficient binding force to the active material inside the foam metal, resulting in a strong electrode that can withstand expansion and contraction during discharge. In a wet state, the binder does not penetrate into the interior, so it is not possible to impart binding force to the entire active material only by initially dispersing the binder liquid.
従つて、ここに用いる結着剤は乾燥後における結着剤の
含浸を阻害しないように低濃度のものを用いるのが好ま
しい。以下、本発明を実施例により説明する。Therefore, it is preferable that the binder used here has a low concentration so as not to inhibit the impregnation of the binder after drying. The present invention will be explained below using examples.
第1図はニツケル電極の製造工程を示す。FIG. 1 shows the manufacturing process of a nickel electrode.
1はペースト状の活物質、2はこれを充填した容器、3
はモータ4により駆動され活物質1を攪拌する攪拌機で
ある。1 is a paste-like active material, 2 is a container filled with this, 3
is a stirrer that is driven by a motor 4 and stirs the active material 1.
5はロール6,7により駆動される帯状の発泡メタルで
、まず容器2内の攪拌されているペースト状活物質中に
導人され、柔軟性を有する複数のゴム板8により表面部
から空孔内へ活物質が加圧充填される。Reference numeral 5 is a band-shaped foamed metal driven by rolls 6 and 7, which is first introduced into the paste-like active material being stirred in the container 2, and then pores are removed from the surface by a plurality of flexible rubber plates 8. The active material is pressurized and filled into the inside.
9はゴム板8の固定治具である。9 is a fixture for fixing the rubber plate 8.
こうして活物質が充填さわた発泡メタル5はスリツト1
0を通過する際に表面に余分に付着している活物質が除
去され、次に表面部の活物質がまだ湿潤状態にあるとき
、噴霧器11により結着剤を含む分散液が表面に薄く散
布される。12は乾燥機で、ここで活物質は十分乾燥さ
れまた表面に散布された結着剤の分散媒も除去され結着
剤の結着効果が表れる。In this way, the foamed metal 5 filled with active material is slit 1.
0, excess active material adhering to the surface is removed, and then, when the active material on the surface is still wet, a dispersion containing a binder is thinly sprayed onto the surface by a sprayer 11. be done. Reference numeral 12 denotes a dryer, in which the active material is sufficiently dried and the dispersion medium of the binder sprinkled on the surface is also removed, so that the binding effect of the binder is exhibited.
13は結着剤の分散液14を収容した結着剤含浸容器で
あり、ここに導人された発泡メタルはその内部の活物質
に結着剤が含浸される。Reference numeral 13 denotes a binder-impregnated container containing a binder dispersion 14, and the active material inside the foamed metal introduced therein is impregnated with the binder.
その後乾燥、加圧圧縮および切断工程を経た後、リード
線を取り付け電極として完成する。ここで実施した製造
条件は次のとおりである。After passing through drying, pressure compression and cutting steps, the lead wire is attached and completed as an electrode. The manufacturing conditions implemented here are as follows.
まず、発泡メタル5は幅10?、長さ200Cr1L1
厚さ2.5mrn1多孔度98%のニツケル製のものを
用い、移動速度は約0.5mm/秒とした。ペースト状
活物質は市販の水酸化ニツケル粉末に導電材料のニツケ
ル粉末を約20重量?程度加え、さらに適量の水とカル
ボキシメチルセルロースの水溶液を加えた含水率35重
量%のもの約70kgを用いた。噴霧器11から散布す
る結着剤分散液は市販の原液を水で40倍に希釈した樹
脂分1.5重量%のフツ素樹脂分散液、結着剤分散液1
4は市販の原液を水で10倍に希釈した樹脂分6.0重
量%のフツ素樹脂分散液をそれぞれ用いた。First, is the foam metal 5 width 10? , length 200Cr1L1
A piece made of nickel with a thickness of 2.5 mrn1 and a porosity of 98% was used, and the moving speed was about 0.5 mm/sec. The paste-like active material is commercially available nickel hydroxide powder and conductive material nickel powder about 20% by weight? Approximately 70 kg of water with a water content of 35% by weight, which was obtained by adding an appropriate amount of water and an aqueous solution of carboxymethyl cellulose, was used. The binder dispersion sprayed from the sprayer 11 is a fluororesin dispersion with a resin content of 1.5% by weight, which is obtained by diluting a commercially available stock solution 40 times with water, and a binder dispersion 1.
In No. 4, a fluororesin dispersion having a resin content of 6.0% by weight was used, which was obtained by diluting a commercially available stock solution 10 times with water.
また乾燥機12の温度は100〜150℃とし、10分
程度で乾燥できるようにした。以上のような製造方法に
よつて構成したニツケル正極と公知の鉄極を負極として
第2図に示すようなアルカリ蓄電池Aを構成した。Further, the temperature of the dryer 12 was set at 100 to 150°C, so that drying could be performed in about 10 minutes. An alkaline storage battery A as shown in FIG. 2 was constructed using the nickel positive electrode constructed by the above manufacturing method and a known iron electrode as a negative electrode.
第2図において、21は正極、22は負極、23はセパ
レータ、24は電槽、25は電解液、26はリード端子
、27は蓋、28は注液栓であり、電極の大きさは各々
50X60m77!とし、各々4枚構成とした。この電
池は正極律則で、負極の容量を正極容量より多くしてあ
る。また比較例として、噴霧器11による結着剤分散液
の散布工程を除いた他は上記と同様にして製造したニツ
ケル極を用いた電池をBとする。第3図はこれらの電池
を放電容量の150%相当以上の電気量で充電した後、
2Aの電流(放電率0.2C)で放電したときの放電特
性を示す。In Fig. 2, 21 is a positive electrode, 22 is a negative electrode, 23 is a separator, 24 is a battery container, 25 is an electrolytic solution, 26 is a lead terminal, 27 is a lid, and 28 is a liquid filling stopper, and the sizes of the electrodes are different from each other. 50x60m77! Each of them was made up of 4 sheets. This battery uses the positive electrode rule, and the capacity of the negative electrode is greater than the capacity of the positive electrode. As a comparative example, a battery using a nickel electrode manufactured in the same manner as described above except for the step of spraying the binder dispersion using the sprayer 11 was designated as B. Figure 3 shows that after charging these batteries with an amount of electricity equivalent to more than 150% of their discharge capacity,
The discharge characteristics when discharged with a current of 2A (discharge rate 0.2C) are shown.
第3図からも明らかなように、本発明による電極を採用
した電池Aの放電容量は、平均10Ahを示しているの
に対して、従来の電極を採用した電池Bの放電容量は平
均8Ahの容量しか示していない。このように本発明の
製造法による電極を採用した電池は従来の製造法による
電極を採用した電池と比較して平均1.25倍の容量向
上になつている。また本発明の電池は容量のバラツキが
5?以内であつたが、従来のものは10〜20%以上と
非常に大きい値を示しており、その原因は活物質の脱落
によりものであることを確認した。従つて、本発明の製
造法により、容量のバラツキが減少し、かつ均一な容量
の電極を製作することが可能となつた。これは、湿潤状
態にある表面部の活物質に結着剤分散液を散布し、表面
部およびその近傍の活物質同志の結着力を強くしたこと
によるものである。従来のものは、表面部またはその近
傍の活物質同志の結着力が弱く、また表面部では発泡メ
タルの格子によつて包囲されている部分が少ないので、
乾燥工程後に結着剤の分散液に含浸させると、表面部ま
たは近傍の活物質が分散液中へ脱落し、この結果、発泡
メタル内に実際に充填さわている活物質の量が減少し、
電極として放電容量試験をした場合、その脱容量に比例
して放電容量が減少している。それと同時にその脱落に
より、放電容量が大きなバラツキを生じている。本発明
において、ペースト状活物質を充填した発泡メタルの表
面部に散布する結着剤分散液の濃度は、後の乾燥および
結着剤の含浸工程中に活物質の脱落を防止できる程度の
低濃度が望ましい。As is clear from FIG. 3, the discharge capacity of battery A using the electrode according to the present invention is 10Ah on average, while the discharge capacity of battery B using the conventional electrode is 8Ah on average. It only shows capacity. As described above, the capacity of the battery employing the electrode manufactured by the manufacturing method of the present invention is increased by an average of 1.25 times compared to the battery employing the electrode manufactured by the conventional manufacturing method. Also, the battery of the present invention has a variation in capacity of 5? However, the conventional one showed a very large value of 10 to 20% or more, and it was confirmed that the cause of this was the dropout of the active material. Therefore, the manufacturing method of the present invention makes it possible to reduce variations in capacitance and to manufacture electrodes with uniform capacitance. This is due to the fact that a binder dispersion liquid is sprayed onto the active material on the surface in a wet state to strengthen the binding force between the active materials on the surface and in the vicinity thereof. In conventional products, the binding force between the active materials at or near the surface is weak, and there is only a small portion of the surface surrounded by the foam metal lattice.
When impregnated with a binder dispersion after the drying process, the active material on or near the surface falls into the dispersion, resulting in a decrease in the amount of active material actually filled into the foamed metal.
When conducting a discharge capacity test as an electrode, the discharge capacity decreases in proportion to the capacitance removed. At the same time, the dropout causes large variations in discharge capacity. In the present invention, the concentration of the binder dispersion sprayed on the surface of the foamed metal filled with a paste-like active material is set to a level low enough to prevent the active material from falling off during the subsequent drying and binder impregnation steps. Concentration is desirable.
濃度が高すぎると、活物質の脱落を防止できるが、逆に
電極自体の分極が大きくなつて、放電容量や高率放電特
性の減少につながり、また乾燥後の結着剤含浸工程にお
いて活物質内部への結着剤の浸透を阻害することになる
。活物質の湿潤状態で散布する結着剤の量は、乾燥後に
添加する結着剤の量の?〜履。程度で、濃度は0.5〜
5.0重量?の範囲が適当である。なお、実施例では、
活物質の湿潤状態および乾燥後に添加する結着剤として
フツ素樹脂分散液を用いたが、ポリエチレンやポリスチ
レンの分散液を用いることもできる。また、活物質の湿
潤状態で加える結着剤としては、上記の他カルボキシメ
チルセルロースやメチルセルロースの水溶液を用いるこ
とができる。また、ニツケル電極に適用した例を述べた
が、カドミウム極、鉄極、鉛極、炭素極にも適用できる
。If the concentration is too high, it is possible to prevent the active material from falling off, but on the other hand, the polarization of the electrode itself increases, leading to a decrease in discharge capacity and high rate discharge characteristics. This will inhibit the penetration of the binder into the interior. Is the amount of binder applied when the active material is wet compared to the amount of binder added after drying? ~wear. The concentration is about 0.5~
5.0 weight? A range of is appropriate. In addition, in the example,
Although a fluororesin dispersion was used as a binder to be added to the active material in a wet state and after drying, a dispersion of polyethylene or polystyrene may also be used. In addition to the above, an aqueous solution of carboxymethyl cellulose or methyl cellulose can be used as the binder added to the active material in a wet state. Further, although an example in which the present invention is applied to a nickel electrode has been described, it can also be applied to a cadmium electrode, an iron electrode, a lead electrode, or a carbon electrode.
以上のように本発明によれば、電極の製造工程中に発泡
メタルの表面部またはその近傍に充填された活物質が脱
落するということはなくなり、その結果ペースト状活物
質の充填量の均一化がはかれるとともに、放電容量の向
上もはかることができる。As described above, according to the present invention, the active material filled on or near the surface of the foam metal does not fall off during the electrode manufacturing process, and as a result, the filling amount of the paste-like active material becomes uniform. In addition to this, it is also possible to improve the discharge capacity.
第1図は本発明の実施例におけるニツケル極の製造工程
の概略図、第2図はアルカリ蓄電池の縦断面図、第3図
は放電特性の比較を示す。
1・・・・・ペースト状活物質、5・・・・・・発泡メ
タル、11・・・・・・結着剤を散布する噴霧器、12
・・・・・・乾燥機、13・・・・・・結着剤含浸容器
。FIG. 1 is a schematic diagram of the manufacturing process of a nickel electrode in an example of the present invention, FIG. 2 is a longitudinal cross-sectional view of an alkaline storage battery, and FIG. 3 is a comparison of discharge characteristics. 1... Paste active material, 5... Foamed metal, 11... Sprayer for spraying binder, 12
...Dryer, 13...Binder impregnated container.
Claims (1)
内へペースト状活物質を充填する工程と、前気多孔体表
面部の湿潤状態にある活物質に結着剤を含有する液体を
散布する工程と、次に乾燥した後結着剤を活物質に含浸
する工程とを有する電池用電極の製造法。1. Filling the pores of a sponge-like metal porous body with a three-dimensional structure with a paste-like active material, and spraying a liquid containing a binder onto the wet active material on the surface of the porous body. A method for manufacturing an electrode for a battery, comprising a step of drying the active material and then impregnating the active material with a binder after drying.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53060125A JPS5931833B2 (en) | 1978-05-19 | 1978-05-19 | Manufacturing method for battery electrodes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53060125A JPS5931833B2 (en) | 1978-05-19 | 1978-05-19 | Manufacturing method for battery electrodes |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54152133A JPS54152133A (en) | 1979-11-30 |
| JPS5931833B2 true JPS5931833B2 (en) | 1984-08-04 |
Family
ID=13133089
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53060125A Expired JPS5931833B2 (en) | 1978-05-19 | 1978-05-19 | Manufacturing method for battery electrodes |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5931833B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0693359B2 (en) * | 1982-08-24 | 1994-11-16 | 松下電器産業株式会社 | Method for producing paste type electrode for battery |
-
1978
- 1978-05-19 JP JP53060125A patent/JPS5931833B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54152133A (en) | 1979-11-30 |
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