JPH081801B2 - Method for manufacturing sheet electrode - Google Patents
Method for manufacturing sheet electrodeInfo
- Publication number
- JPH081801B2 JPH081801B2 JP6939791A JP6939791A JPH081801B2 JP H081801 B2 JPH081801 B2 JP H081801B2 JP 6939791 A JP6939791 A JP 6939791A JP 6939791 A JP6939791 A JP 6939791A JP H081801 B2 JPH081801 B2 JP H081801B2
- Authority
- JP
- Japan
- Prior art keywords
- sheet
- kneading
- extrusion
- electrode
- viscosity
- 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
-
- Y02E60/12—
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Description
【0001】[0001]
【産業上の利用分野】この発明は厚みのばらつきを小さ
く押さえるようにしたシート状電極の製造方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a sheet-shaped electrode which suppresses variations in thickness.
【0002】[0002]
【従来の技術】二酸化マンガンを主剤とする合剤からな
るシート状電極を製造するには、予め合剤を混練し、そ
の粘度を4000〜6000ポイズに調整し、金属集電
体を挟んでスクリュー押出成形機を通じて混練合剤を押
出成形することにより前記金属集電体を内部に一体化し
たシート状電極が得られるようにしている。2. Description of the Related Art In order to produce a sheet-like electrode composed of a mixture containing manganese dioxide as a main component, the mixture is kneaded in advance, its viscosity is adjusted to 4000 to 6000 poise, and a screw is sandwiched with a metal collector. By extruding the kneading mixture through an extruder, a sheet electrode having the metal current collector integrated therein can be obtained.
【0003】得られたシート状電極の厚みは、従来は押
出成形温度、スクリュー回転数、引取り速度などにより
変わってくるが、一般的にはヘッド温度を70℃、スク
リュー回転数を30rpmと一定値に設定し、押出成形
機から引き出されたシート状電極の厚みを計測し、この
厚みに応じて引取りロ―ラの速度を調整することによっ
て一定の範囲に押さえるようにしており、その押出速度
は5〜6m/分程度である。Although the thickness of the obtained sheet-like electrode conventionally varies depending on the extrusion molding temperature, the screw rotation speed, the take-up speed, etc., generally the head temperature is 70 ° C. and the screw rotation speed is constant at 30 rpm. It is set to a value, the thickness of the sheet-shaped electrode drawn out from the extruder is measured, and the speed of the take-up roller is adjusted according to this thickness to keep it within a certain range. The speed is about 5 to 6 m / min.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、この押
出速度調整のみによる厚み調整方法では、厚さの目標値
に対して±0.1〜0.2mm程度と大きくばらつき、
安定した品質が得難く、品質管理上から寸法公差を小さ
く設定すると、歩留まりが極端に低くなる欠点があっ
た。However, according to the thickness adjusting method by adjusting only the extrusion speed, there is a large variation of about ± 0.1 to 0.2 mm with respect to the target value of the thickness,
It is difficult to obtain stable quality, and if the dimensional tolerance is set to be small from the viewpoint of quality control, the yield becomes extremely low.
【0005】この発明は、以上の問題を解決するもので
あって、押出ヘッド付近での混練合剤の粘度を一定の範
囲とすることによって、厚みのばらつきを押さえ、品質
の向上を図り、歩留まりを向上できるようにしたシート
状電極の製造方法を提供することを目的とする。The present invention has been made to solve the above problems. By keeping the viscosity of the kneading agent near the extrusion head within a certain range, variations in thickness can be suppressed, quality can be improved, and yield can be improved. It is an object of the present invention to provide a method for manufacturing a sheet-shaped electrode that can improve
【0006】[0006]
【課題を解決するための手段】前記目的を達成するた
め、この発明は、多数のパンチング孔を開口した金属集
電体を挟んで混練合剤を押出成形して前記金属集電体と
一体化されたシート状電極を製造する方法において、前
記混練合剤は、押出成形機内に投入されたときに、その
ヘッド温度が40〜50℃において、粘度が600〜1
500ポイズであり、前記シート状電極の押出速度を7
〜12m/分とすることを特徴とするものである。In order to achieve the above-mentioned object, the present invention integrates with a metal current collector by extruding a kneading agent sandwiching a metal current collector having a large number of punching holes. In the method for producing a sheet-shaped electrode, the kneading mixture has a viscosity of 600 to 1 at a head temperature of 40 to 50 ° C. when put into an extruder.
It is 500 poise, and the extrusion speed of the sheet electrode is 7
It is characterized in that it is set to 12 m / min.
【0007】[0007]
【作用】以上の粘度範囲の混練合剤は、押出しによりシ
ート状電極に成形された状態での厚みのばらつきが従来
のばらつきに比べて極めて小さくなる。In the kneading agent having the above viscosity range, the thickness variation in the state of being formed into a sheet-like electrode by extrusion becomes extremely smaller than the conventional variation.
【0008】[0008]
【実施例】以下この発明方法の一実施例を詳細に説明す
る。 [混練合剤の組成] 二酸化マンガン 70(重量、以下同じ)% 導電剤 5 PVB 10 テフロンディスパージョン 5 アルコール 10 合計100% [混練工程]以上の組成のものを混練温度70℃でニー
ダにより70分程度混練すると、粘度800ポイズの混
練合剤ができあがる。なお、混練時間と合剤粘度および
合剤粘度と温度との関係を図1(a),(b)に示す。
混練時間が長すぎると粘度は低下するので、以上の組成
では70分程度で混練を停止することが望ましい。EXAMPLE An example of the method of the present invention will be described in detail below.
It [Composition of kneading agent] Manganese dioxide 70 (weight, the same applies hereinafter)% Conducting agent 5 PVB 10 Teflon dispersion 5Alcohol 10 100% in total [Kneading process] Kneading with a composition of at least 70% at a kneading temperature of 70 ° C
When kneading for about 70 minutes with a mixer, the viscosity is 800 poise.
The kneading agent is completed. In addition, kneading time and mixture viscosity and
The relationship between the mixture viscosity and the temperature is shown in FIGS. 1 (a) and 1 (b).
If the kneading time is too long, the viscosity will decrease.
Then, it is desirable to stop the kneading in about 70 minutes.
【0009】[押出工程]混練工程で得られた合剤を図
2に示す押出成形機1に投入し、押出作業を行う。この
押出成形機1は内部に押出用のスクリュー2を有すると
ともに、押出ヘッド1aには多数のパンチング孔を開口
した金属集電体3が供給され、集電体3は合剤に挾まれ
た状態で押出され、引取りロ―ラ4により引きとられ、
シート状電極5に形成される。また、押出ヘッド1aの
先端には厚み計6が配置され、常時厚みを監視してい
る。[Extrusion Step] The mixture obtained in the kneading step is put into the extrusion molding machine 1 shown in FIG. 2 to perform the extrusion operation. This extrusion molding machine 1 has a screw 2 for extrusion inside, and an extrusion head 1a is supplied with a metal current collector 3 having a large number of punched holes, and the current collector 3 is sandwiched by a mixture. It is extruded by and is taken by the take-off roller 4,
It is formed on the sheet electrode 5. A thickness meter 6 is arranged at the tip of the extrusion head 1a to constantly monitor the thickness.
【0010】図3は、ヘッド温度50℃、スクリュー回
転数30rpmで成形したときの合剤粘度と押出速度お
よびシート厚さのばらつきの関係を示すものである。図
において、合剤粘度が1500ポイズを越えると急速に
ばらつきが大きくなり、また、600ポイズを下回ると
軟らかすぎて押出しが困難となり、集電体3との間の剥
離も生じやすいものとなる。また、押出速度が7m/分
を下回るとシート状電極の表面に凹凸が生じやすくな
り、その逆に12m/分を越えると速すぎて集電体3に
合剤がうまく密着せず、集電体3が露出してしまう。し
たがって、この発明ではヘッド温度50℃において、混
練合剤の粘度は600〜1500ポイズに設定すること
が望ましく、また押出速度は7〜12m/分に設定する
ことが望ましい。FIG. 3 shows the relationship between the mixture viscosity, the extrusion speed, and the variation in sheet thickness when molded at a head temperature of 50 ° C. and a screw rotation speed of 30 rpm. In the figure, when the mixture viscosity exceeds 1500 poise, the dispersion rapidly increases, and when it is less than 600 poise, it is too soft and extrusion becomes difficult, and peeling from the current collector 3 easily occurs. On the other hand, if the extrusion speed is less than 7 m / min, irregularities are likely to occur on the surface of the sheet-shaped electrode, while if it exceeds 12 m / min, it is too fast and the mixture does not adhere well to the current collector 3, resulting in current collection. Body 3 is exposed. Therefore, in the present invention, at a head temperature of 50 ° C., the viscosity of the kneading agent is preferably set to 600 to 1500 poise, and the extrusion speed is preferably set to 7 to 12 m / min.
【0011】特に、ヘッド温度50℃、スクリュー回転
数30rpm、速度10m/分で前述の粘度800ポイ
ズの混練合剤を厚さ0.7mm,幅約25mmのシート
状電極を成形した場合、厚みのばらつきの度合いは0.
7mm±0.01mmとなり、従来のシート状電極の厚
みのばらつきより一桁低い値が得られることになる。In particular, when a sheet-like electrode having a thickness of 0.7 mm and a width of about 25 mm is formed by using the above kneading agent having a viscosity of 800 poise at a head temperature of 50 ° C., a screw rotation speed of 30 rpm and a speed of 10 m / min, The degree of variation is 0.
The value is 7 mm ± 0.01 mm, which is one digit lower than the variation in the thickness of the conventional sheet electrode.
【0012】[0012]
【発明の効果】以上実施例によって詳細に説明したよう
に、この発明によるシート状電極の製造方法にあって
は、押出しによりシート状電極に成形された状態での厚
みのばらつきが従来のばらつきに比べて極めて小さく、
安定した品質を得られ、またこれにより歩留まりを大巾
に向上でき、かつ生産性も向上するという利点がある。As described above in detail with reference to the embodiments, in the method for manufacturing a sheet electrode according to the present invention, the variation in thickness in the state of being formed into a sheet electrode by extrusion is different from the conventional variation. Very small compared to
There is an advantage that a stable quality can be obtained, the yield can be greatly improved, and the productivity can be improved.
【図1】(a)は混練時間と合剤粘度との関係を示すグ
ラフである。 (b)は合剤粘度と温度との関係を示すグラフである。FIG. 1A is a graph showing the relationship between kneading time and mixture viscosity. (B) is a graph showing the relationship between the mixture viscosity and the temperature.
【図2】この発明方法を適用した押出成形機を示す説明
図である。FIG. 2 is an explanatory view showing an extrusion molding machine to which the method of the present invention is applied.
【図3】成形時の合剤粘度と押出速度およびシート厚さ
のばらつきの関係を示すグラフである。FIG. 3 is a graph showing the relationship between the mixture viscosity at the time of molding, the extrusion rate, and the variation in sheet thickness.
1 押出成形機 1a ヘッド 2 スクリュー 3 金属集電体 4 引取りロ―ラ 5 シート状電極 6 厚み計 1 Extrusion Molding Machine 1a Head 2 Screw 3 Metal Current Collector 4 Pulling Roller 5 Sheet Electrode 6 Thickness Meter
───────────────────────────────────────────────────── フロントページの続き (72)発明者 鈴木 正章 東京都港区新橋5丁目36番11号 富士電気 化学株式会社内 (72)発明者 遠藤 幸郎 東京都港区新橋5丁目36番11号 富士電気 化学株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masaaki Suzuki 5-36-1 Shimbashi, Minato-ku, Tokyo Fuji Electric Chemical Co., Ltd. (72) Inventor Yukio Endo 5-36-11 Shinbashi, Minato-ku, Tokyo Fuji Electrochemical Co., Ltd.
Claims (1)
体を挟んで混練合剤を押出成形して前記金属集電体と一
体化されたシート状電極を製造する方法において、前記
混練合剤は、押出成形機内に投入されたときに、そのヘ
ッド温度が40〜50℃において、粘度が600〜15
00ポイズであり、前記シート状電極の押出し速度を7
〜12m/分とすることを特徴とするシート状電極の製
造方法。1. A method for producing a sheet-like electrode integrated with a metal current collector by extruding a kneading agent with a metal current collector having a large number of punched holes between the kneading agent. Has a viscosity of 600 to 15 at a head temperature of 40 to 50 ° C. when placed in an extruder.
00 poise, and the extrusion speed of the sheet electrode is 7
~ 12 m / min, the method for manufacturing a sheet electrode.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6939791A JPH081801B2 (en) | 1991-03-11 | 1991-03-11 | Method for manufacturing sheet electrode |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6939791A JPH081801B2 (en) | 1991-03-11 | 1991-03-11 | Method for manufacturing sheet electrode |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04282558A JPH04282558A (en) | 1992-10-07 |
JPH081801B2 true JPH081801B2 (en) | 1996-01-10 |
Family
ID=13401431
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6939791A Expired - Fee Related JPH081801B2 (en) | 1991-03-11 | 1991-03-11 | Method for manufacturing sheet electrode |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH081801B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20220165995A (en) * | 2021-06-09 | 2022-12-16 | 비나텍주식회사 | Electrode manufacturing method and electrode assembly manufactured using same |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0639865B1 (en) * | 1993-06-15 | 1998-03-11 | Fuji Photo Film Co., Ltd. | A method for producing a sheet-like plate |
CA2207801C (en) | 1996-06-19 | 2004-03-30 | Hideki Kaido | Nonaqueous electrolyte battery |
-
1991
- 1991-03-11 JP JP6939791A patent/JPH081801B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20220165995A (en) * | 2021-06-09 | 2022-12-16 | 비나텍주식회사 | Electrode manufacturing method and electrode assembly manufactured using same |
Also Published As
Publication number | Publication date |
---|---|
JPH04282558A (en) | 1992-10-07 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |