JPH0795444B2 - Alkaline battery negative electrode manufacturing method - Google Patents
Alkaline battery negative electrode manufacturing methodInfo
- Publication number
- JPH0795444B2 JPH0795444B2 JP2088520A JP8852090A JPH0795444B2 JP H0795444 B2 JPH0795444 B2 JP H0795444B2 JP 2088520 A JP2088520 A JP 2088520A JP 8852090 A JP8852090 A JP 8852090A JP H0795444 B2 JPH0795444 B2 JP H0795444B2
- Authority
- JP
- Japan
- Prior art keywords
- negative electrode
- alkaline battery
- battery negative
- sheet
- binder
- 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 - Fee Related
Links
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】 産業上の利用分野 本発明はニッケル−カドミウム蓄電池、ニッケル−水素
蓄電池などのアルカリ電池の負極の製造法に関する。TECHNICAL FIELD The present invention relates to a method for producing a negative electrode of an alkaline battery such as a nickel-cadmium storage battery or a nickel-hydrogen storage battery.
従来の技術 各種の電源として使われる蓄電池として鉛電池とアルカ
リ電池がある。このうちアルカリ蓄電池は高信頼性が期
待でき、小形軽量化も可能などの理由で小型は各種ポー
タブル機器用に、大型は産業として広く使われてきた。2. Description of the Related Art Lead-acid batteries and alkaline batteries are used as storage batteries for various power sources. Among them, the alkaline storage battery is expected to have high reliability and can be made compact and lightweight. For this reason, the small size has been widely used for various portable devices, and the large size has been widely used as an industry.
このアルカリ蓄電池において、正極としては一部空気極
なども取り上げられているが、ほとんどの場合ニッケル
極である。ポケット式から焼結式に代わって特性が向上
し、さらに密閉化が可能になるととともに用途も広がっ
た。In this alkaline storage battery, an air electrode or the like is also taken up as a positive electrode, but in most cases, it is a nickel electrode. The characteristics have been improved from the pocket type to the sintered type, and it has become possible to further seal and expand the applications.
一方負極としてはカドミウムの他に亜鉛、鉄、水素など
が使われている。現在のところカドミウム極が主体であ
るが、水素吸蔵合金を用いた水素極が注目されている。On the other hand, as the negative electrode, zinc, iron, hydrogen, etc. are used in addition to cadmium. At present, the cadmium electrode is mainly used, but a hydrogen electrode using a hydrogen storage alloy is drawing attention.
負極の場合も低廉化を目指して負極材料に結着剤を加え
てシート状に加工して得られる非焼結式が研究されカド
ミウム極はすでに実用化され多くの製造法の改良提案も
なされている。In the case of negative electrodes, non-sintering type, which is obtained by adding a binder to the negative electrode material and processing it into a sheet, has been studied for the purpose of cost reduction. There is.
発明が解決しようとする課題 充電状態のカドミウム極あるいは水素吸蔵合金を用いた
水素極はいずれも金属なので電子伝導性の点で比較的優
れているため、すでにカドミウム極は非焼結式が実用化
している。すなわちこれら負極材料粉末を結着剤ととも
にペースト状としこれを多孔性導電板に塗着し平滑化し
ている。この場合結着剤としてポリビニルアルコールや
カルボキシメチルセルロースそれに絶縁性のポリエチレ
ン、ポリ塩化ビニル、スチレン系ゴムなどの熱可塑性樹
脂が用いられる。Problems to be Solved by the Invention Since both the cadmium electrode in the charged state and the hydrogen electrode using a hydrogen storage alloy are metals, they are relatively excellent in terms of electron conductivity. ing. That is, these negative electrode material powders are made into a paste together with a binder, and the paste is applied to the porous conductive plate for smoothing. In this case, as a binder, polyvinyl alcohol, carboxymethyl cellulose, or a thermoplastic resin such as insulating polyethylene, polyvinyl chloride, or styrene rubber is used.
その他強度保持のために耐アルカリ性の金属や合成樹脂
の単繊維が加えられていて、これが逆に電極の均一性や
製法上の複雑さをもたらしているという課題があった。In addition, alkali-resistant metal or synthetic resin monofilaments are added to maintain the strength, which, on the contrary, has a problem in that the uniformity of the electrode and the complexity of the manufacturing method are brought about.
本発明はこのような課題を解決するものでこれらの背景
から一層均一性を有する非焼結式電極の製造法を提供す
ることを目的とする。The present invention solves such a problem, and an object of the present invention is to provide a method for manufacturing a non-sintered electrode having more uniformity from these backgrounds.
課題を解決するための手段 本発明は結着剤として熱可塑性樹脂を用いてアルカリ電
池負極材料をシート状とし、その後エキスパンドメタ
ル、スクリーン、パンチングメタルなど多孔性導電体と
を積層し、結着剤の軟化点以上の温度で両者を加圧一体
化するものである。Means for Solving the Problems The present invention is a sheet of alkaline battery negative electrode material using a thermoplastic resin as a binder, and then laminated with a porous conductor such as expanded metal, screen, punching metal, the binder Both are pressure-integrated at a temperature equal to or higher than the softening point of.
作用 以上の様に、本発明はまず負極材料粉末と結着剤からな
るペーストのみでシートを製作するので、多孔性芯材に
塗着する従来の方法よりも均一なシートができ、その
後、導電性多孔体とシートとを結着剤の軟化点以上の温
度で加圧するのでシートと導電性多孔体が容易に一体化
できる。Action As described above, according to the present invention, since the sheet is first produced only by the paste composed of the negative electrode material powder and the binder, a more uniform sheet can be formed than the conventional method of coating the porous core material, and then the conductive core Since the porous porous body and the sheet are pressed at a temperature equal to or higher than the softening point of the binder, the sheet and the conductive porous body can be easily integrated.
実 施 例 以下負極に酸化カドミウムを用いた場合の本発明の一実
施例について述べる。Example An example of the present invention in which cadmium oxide is used for the negative electrode will be described below.
市販の酸化カドミウム粉末93部、ニッケル粉末5部これ
にスチレン−ブチレン共重合体の3(重量)%のトルエ
ン溶液をこの樹脂が水酸化カドミウムに対して2部にな
るように加えてペーストとする。公知のドクターブレー
ド法によりこのペーストからシートを製作し100℃で乾
燥した。厚さ0.3mmにした。Commercially available cadmium oxide powder 93 parts, nickel powder 5 parts To this, a 3% (by weight) toluene solution of a styrene-butylene copolymer is added so that this resin becomes 2 parts with respect to cadmium hydroxide to form a paste. . A sheet was produced from this paste by a known doctor blade method and dried at 100 ° C. The thickness is 0.3mm.
このシート2枚間に厚さ0.17mm、孔径1.8mm、開口度53
%の鉄製でニッケルメッキを施したパンチングメタル板
を重ね、150℃に加熱したエンボス加工を施したローラ
プレス機を通して一体化した。平均の厚さは0.55mmであ
った。この後さらにワット浴を用いて表面に電解でニッ
ケルメッキを施した後0.3%フッソ樹脂ディスパージョ
ンに浸漬し、120℃で1時間乾燥した。このようにして
得られたペースト式カドミウム極を幅39mm、長さ370mm
に裁断し、リード板をスポット溶接により取り付けた。
部分充電を行ってカドミウム極とし、このカドミウム極
をAとする。The thickness between these two sheets is 0.17 mm, the hole diameter is 1.8 mm, and the opening degree is 53.
% Of iron and nickel-plated punching metal plates were stacked and integrated through a roller press machine with embossing heated to 150 ° C. The average thickness was 0.55 mm. After that, the surface of the plate was electrolytically nickel-plated using a Watt bath, immersed in a 0.3% fluorine resin dispersion, and dried at 120 ° C. for 1 hour. The paste-type cadmium electrode thus obtained was 39 mm wide and 370 mm long.
Then, the lead plate was attached by spot welding.
Partial charge is performed to make a cadmium electrode, and this cadmium electrode is set to A.
つぎに、比較のためにAと同じパンチングメタルとペー
ストを用い、パンチングメタルの両面にペーストを塗着
しスリット間を通す従来の方法でやはり平均厚さ0.55mm
のカドミウム極とし、以下Aと同じ工程で得られたカド
ミウム極をBとして加える。Next, for comparison, using the same punching metal and paste as in A, the average thickness of 0.55 mm was also obtained by the conventional method of applying the paste on both sides of the punching metal and passing it between the slits.
Then, the cadmium electrode obtained in the same step as A is added as B.
両電極20枚を用いてその重量から計算容量を求めたとこ
ろA群は5.9Ahを最大に最小は5.6Ahであったのに対して
B群では最大は同じ5.9Ahであったが最小は5.2Ahであ
り、Aのバラツキが小さいことがわかった。When the calculated capacity was calculated from the weight using 20 electrodes, the maximum value was 5.9Ah in group A and the minimum value was 5.6Ah, while the maximum value was 5.9Ah in group B but the minimum value was 5.2. It was Ah, and it was found that the variation of A was small.
したがって、たとえばニッケル正極を用いて電池を構成
する場合、正極の容量を2.8Ahとしその2倍の計算容量
を持つ負極を設計の基準とした場合、Bでは最小を5.6A
hにひきあげると最大が6.35Ahになるように電極をつく
る必要があるが、Aでは最小5.6Ahが保証できるのでそ
のまま実施例の電極が使える。それだけコストダウンが
可能になり容量も若干ではあるが大きくなる。なお具体
的にAおよびBを用い相手極として公知の長寿命の焼結
式ニッケル極、それに親水処理ポリプロピレン不織布セ
パレータを用いて単2形密閉形ニッケル−カドミウム蓄
電池を構成した。電解液として比重1.22の苛性カリ水溶
液に20g/1の水酸化リチウムを溶解して用いた。Therefore, for example, when constructing a battery using a nickel positive electrode, if the capacity of the positive electrode is set to 2.8 Ah and the negative electrode having twice the calculated capacity is used as the design reference, the minimum for B is 5.6 Ah.
It is necessary to make the electrode so that the maximum becomes 6.35 Ah when pulled up to h, but in A, the minimum of 5.6 Ah can be guaranteed, so the electrode of the embodiment can be used as it is. The cost can be reduced by that much, and the capacity also increases slightly. In addition, a A2 sealed nickel-cadmium storage battery was constructed by specifically using A and B and using a known long-life sintered nickel electrode as a counter electrode and a hydrophilically treated polypropylene nonwoven fabric separator. As an electrolytic solution, 20 g / 1 of lithium hydroxide was dissolved in a caustic potash aqueous solution having a specific gravity of 1.22 and used.
まず初期の放電電圧と容量を比較した。5時間率で容量
の130%定電流充電−1.0Aで0.9Vまでの定電流放電を行
ったところ、A,Bとも平均電圧は1.22Vであり、放電容量
はAは2.8Ahで、Bは2.6Ahであった。First, the initial discharge voltage and capacity were compared. When the constant current charge of 130% of the capacity at a rate of 5 hours and constant current discharge of up to 0.9V was performed at 1.0A, the average voltage of both A and B was 1.22V, and the discharge capacity A was 2.8Ah and B was It was 2.6 Ah.
つぎに両電池それぞれ10セル用い、この充放電の条件で
寿命特性を比較した。その結果、放電容量が初期の65%
にまで劣化するサイクル数が、A,Bとも1050〜1100サイ
クルであった。Next, 10 cells were used for each battery, and the life characteristics were compared under the conditions of this charge / discharge. As a result, the discharge capacity is 65% of the initial value.
The number of cycles that deteriorated to 10 was 1,050 to 1,100 cycles for both A and B.
以上が負極に酸化カドミウムを用いた場合の一実施例で
あるが、本発明は負極に水素吸蔵合金を用いた場合でも
先と同様の結果が得ることができた。The above is one example of the case where cadmium oxide is used for the negative electrode, but in the present invention, the same result as above can be obtained even when the hydrogen storage alloy is used for the negative electrode.
発明の効果 本発明のアルカリ電池負極の製造法は、電極の厚さの均
一性が向上し容量のバラツキが減少する優れたアルカリ
電池負極の製造方法を提供できる。Effect of the Invention The method for producing an alkaline battery negative electrode of the present invention can provide an excellent method for producing an alkaline battery negative electrode in which the uniformity of the electrode thickness is improved and the variation in capacity is reduced.
Claims (4)
リ電池負極材料をシート状とし、このシートに多孔性導
電体膜を積層し、上記結着剤の軟化点以上の温度で上記
シートと導電体膜とを加圧し一体化するアルカリ電池負
極の製造法。1. An alkaline battery negative electrode material is formed into a sheet using a thermoplastic resin as a binder, a porous conductor film is laminated on the sheet, and the sheet is formed at a temperature equal to or higher than the softening point of the binder. A method for manufacturing an alkaline battery negative electrode in which a conductor film is pressed and integrated.
又は水素吸蔵合金の粉末を主成分とする請求項1記載の
アルカリ電池負極の製造法。2. The method for producing an alkaline battery negative electrode according to claim 1, wherein the alkaline battery negative electrode material contains a powder of cadmium oxide or a hydrogen storage alloy as a main component.
載のアルカリ電池負極の製造法。3. The method for producing an alkaline battery negative electrode according to claim 1, wherein the binder is styrene rubber.
リ電池負極材料をシート状としたシートに多孔性導電体
膜を積層し、上記結着剤の軟化点以上の温度で上記シー
トと導電体膜とを加圧し一体化し、フッ素樹脂ディスパ
ーションを添加するアルカリ電池負極の製造法。4. A porous conductor film is laminated on a sheet of a sheet of an alkaline battery negative electrode material using a thermoplastic resin as a binder, and the sheet is electrically conductive with the sheet at a temperature higher than the softening point of the binder. A method for producing an alkaline battery negative electrode in which a body membrane is pressed and integrated to add a fluororesin dispersion.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2088520A JPH0795444B2 (en) | 1990-04-03 | 1990-04-03 | Alkaline battery negative electrode manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2088520A JPH0795444B2 (en) | 1990-04-03 | 1990-04-03 | Alkaline battery negative electrode manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03289045A JPH03289045A (en) | 1991-12-19 |
| JPH0795444B2 true JPH0795444B2 (en) | 1995-10-11 |
Family
ID=13945108
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2088520A Expired - Fee Related JPH0795444B2 (en) | 1990-04-03 | 1990-04-03 | Alkaline battery negative electrode manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0795444B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0812778B2 (en) * | 1989-09-11 | 1996-02-07 | 工業技術院長 | Method for manufacturing hydrogen storage electrode |
-
1990
- 1990-04-03 JP JP2088520A patent/JPH0795444B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03289045A (en) | 1991-12-19 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |