JP2002015748A - Manufacturing method of cylindrical alkaline battery - Google Patents

Manufacturing method of cylindrical alkaline battery

Info

Publication number
JP2002015748A
JP2002015748A JP2000196182A JP2000196182A JP2002015748A JP 2002015748 A JP2002015748 A JP 2002015748A JP 2000196182 A JP2000196182 A JP 2000196182A JP 2000196182 A JP2000196182 A JP 2000196182A JP 2002015748 A JP2002015748 A JP 2002015748A
Authority
JP
Japan
Prior art keywords
positive electrode
concentration
electrolyte
electrode mixture
separator
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.)
Withdrawn
Application number
JP2000196182A
Other languages
Japanese (ja)
Inventor
Yasuo Mukai
保雄 向井
Seiji Wada
誠司 和田
Yuji Mototani
祐司 元谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
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 by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP2000196182A priority Critical patent/JP2002015748A/en
Publication of JP2002015748A publication Critical patent/JP2002015748A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • Y02E60/12

Abstract

PROBLEM TO BE SOLVED: To improve the yield of a cylindrical alkaline battery by maintaining the discharge performance without adding a special binder and by improving the strength of the positive electrode pellet. SOLUTION: In the manufacturing method in which after a plastic positive mixture and a separator are inserted in the battery case, an electrolyte is filled and made to be absorbed, and then the gel form negative electrode is filled, the concentration of the alkaline electrolyte for the positive mixture is made higher concentration than the alkaline electrolyte for the filling use. Preferably, the concentration of the electrolyte for the positive mixture is made 45-50 wt.% and the concentration of the electrolyte for the filling use is made 35-40 wt.% and the former is made higher concentration than the latter by 5 wt.% or more.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、電池ケース内へ正
極合剤成形体、セパレータおよびゲル状負極を順次挿入
した構成の円筒形アルカリ電池の製造方法の改良に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a method for manufacturing a cylindrical alkaline battery having a structure in which a positive electrode material mixture, a separator and a gelled negative electrode are sequentially inserted into a battery case.

【0002】[0002]

【従来の技術】近年、ビデオカメラや小型液晶テレビ等
の電子機器の高性能化および小型化は目ざましく、これ
ら電子機器の電源となる電池への高容量化の要求も強ま
ってきている。こうした用途の電池として、マンガン乾
電池に代わって、より大きな容量が得られるものとし
て、水酸化カリウム等のアルカリ電解液を用いたアルカ
リ乾電池が多用されるようになってきている。アルカリ
乾電池の代表的な製造方法は、二酸化マンガンと黒鉛お
よびアルカリ電解液を含有する正極合剤粉末を円筒形に
成形する工程、得られた正極合剤成形体を金属製電池ケ
ースに挿入し、再加圧して正極合剤成形体を電池ケース
へ密着させる工程、前記正極合剤成形体の内側に筒状セ
パレータを配置する工程、前記筒状セパレータの内部へ
アルカリ電解液を注入し、電解液を正極合剤成形体およ
びセパレータへ吸収させる工程、および前記筒状セパレ
ータ内へゲル状負極を充填する工程を有する。
2. Description of the Related Art In recent years, the performance and miniaturization of electronic devices such as video cameras and small liquid crystal televisions have been remarkable, and the demand for higher capacity of batteries serving as power supplies for these electronic devices has been increasing. As a battery for such an application, an alkaline dry battery using an alkaline electrolyte such as potassium hydroxide has been increasingly used in place of a manganese dry battery as a battery capable of obtaining a larger capacity. A typical method of manufacturing an alkaline dry battery is a step of forming a positive electrode mixture powder containing manganese dioxide, graphite and an alkaline electrolyte into a cylindrical shape, inserting the obtained positive electrode mixture molded body into a metal battery case, Re-pressurizing the positive electrode mixture molded body to adhere to the battery case, arranging a cylindrical separator inside the positive electrode mixture molded body, injecting an alkaline electrolyte into the cylindrical separator, And a step of filling the cylindrical negative electrode with a gelled negative electrode.

【0003】ここに用いられる電解液は、水酸化カリウ
ムの35〜45wt%水溶液で、正極合剤と混合する電
解液、筒状セパレータの内部へ注入する電解液およびゲ
ル状負極に含める電解液として、一般的には同一のもの
が共用されていた。そして、正極合剤に添加される電解
液量は1〜5wt%であり、合剤粉末の結着性をよくし
て成形性を向上し、正極合剤成形体(以下正極ペレット
という)の強度を高めることが主目的である。正極ペレ
ットは、中空円筒形に成形されているため、電池を製造
ラインで組み立てる工程において、特に、正極ペレット
の搬送工程において、割れや欠けが発生しやすく、製品
化への歩留まりが悪く、品質上においても種々の特性値
のばらつきの要因となっていた。
The electrolyte used here is a 35 to 45 wt% aqueous solution of potassium hydroxide, which is mixed with the positive electrode mixture, injected into the cylindrical separator, and included in the gelled negative electrode. In general, the same thing was shared. The amount of the electrolytic solution added to the positive electrode mixture is 1 to 5 wt%, and the binding property of the mixture powder is improved to improve the moldability, and the strength of the positive electrode mixture molded product (hereinafter referred to as positive electrode pellet) is improved. Is the main purpose. Since the positive electrode pellet is formed into a hollow cylindrical shape, cracks and chips are likely to occur in the process of assembling the battery on the production line, especially in the transporting process of the positive electrode pellet, resulting in poor product yield and poor quality. Also causes various variations in characteristic values.

【0004】そこで、正極合剤粉末の結着性をよくして
成形性を向上させるために、ポリエチレン、ポリテトラ
フルオロエチレン、ポリアクリル酸ソーダ等の微粉末を
バインダーとして添加する提案もなされている。しか
し、このようなバインダーの添加は、活物質の充填量を
減少させたり電気抵抗を増大させたりして放電性能を低
下させるという問題がある。
Therefore, it has been proposed to add a fine powder of polyethylene, polytetrafluoroethylene, sodium polyacrylate or the like as a binder in order to improve the binding property of the positive electrode mixture powder and improve the moldability. . However, the addition of such a binder has a problem that the discharge performance is deteriorated by decreasing the filling amount of the active material or increasing the electric resistance.

【0005】[0005]

【発明が解決しようとする課題】本発明は、以上の点に
鑑み、特別なバインダーは添加せずに放電性能を維持
し、なおかつ正極ペレットの強度を向上させて歩留まり
を向上することを目的とする。本発明は、また、電池ケ
ース内のセパレータへ注入した電解液の吸液時間を短縮
できる円筒形アルカリ電池の製造方法を提供することを
も目的とする。
SUMMARY OF THE INVENTION In view of the above, it is an object of the present invention to maintain the discharge performance without adding a special binder, and to improve the yield by improving the strength of the positive electrode pellet. I do. Another object of the present invention is to provide a method of manufacturing a cylindrical alkaline battery capable of shortening a time required for absorbing an electrolytic solution injected into a separator in a battery case.

【0006】[0006]

【課題を解決するための手段】本発明の円筒形電池の製
造方法は、二酸化マンガンと黒鉛およびアルカリ電解液
を含有する正極合剤粉末を中空円筒形に成形する工程、
得られた正極合剤成形体を金属製電池ケースに挿入し、
再加圧して正極合剤成形体を電池ケースへ密着させる工
程、前記正極合剤成形体の内側に筒状セパレータを配置
する工程、前記筒状セパレータの内部へアルカリ電解液
を注入し、電解液を正極合剤成形体およびセパレータへ
吸収させる工程、および前記筒状セパレータ内へゲル状
負極を充填する工程を有し、前記正極合剤の含有するア
ルカリ電解液の濃度を前記セパレータの内部へ注入する
アルカリ電解液のそれより高濃度としたことを特徴とす
る。
The method of manufacturing a cylindrical battery according to the present invention comprises the steps of: forming a positive electrode mixture powder containing manganese dioxide, graphite and an alkaline electrolyte into a hollow cylindrical shape;
Insert the obtained positive electrode mixture molded body into a metal battery case,
Re-pressurizing the positive electrode mixture molded body to adhere to the battery case, arranging a cylindrical separator inside the positive electrode mixture molded body, injecting an alkaline electrolyte into the cylindrical separator, And a step of filling the gelled negative electrode into the cylindrical separator, and injecting the concentration of the alkaline electrolyte contained in the positive electrode mixture into the separator. The concentration of the alkaline electrolyte is higher than that of the alkaline electrolyte.

【0007】ここに用いるアルカリ電解液は、水酸化カ
リウム水溶液であり、前記正極合剤の含有する電解液の
水酸化カリウム濃度が40〜50wt%、前記セパレー
タの内部へ注入する電解液の水酸化カリウム濃度が35
〜45wt%であり、前者の濃度が後者のそれより5w
t%以上高濃度であることが好ましい。正極合剤の含有
する電解液の水酸化カリウム濃度が40wt%未満であ
ると、重負荷放電性能および正極ペレットの強度が低下
する。また、50wt%を越える濃度の電解液を調製す
るのは量産上不利である。一方、セパレータの内部へ注
入する電解液の水酸化カリウム濃度が35wt%未満で
あると、重負荷放電性能が低下する。また、45wt%
を越えると、セパレータへの吸収に時間を要し、生産性
が低下する。正極合剤の含有する電解液の水酸化カリウ
ム濃度は45〜50wt%であるのがより好ましい。
The alkaline electrolyte used here is an aqueous solution of potassium hydroxide. The electrolyte contained in the positive electrode mixture has a potassium hydroxide concentration of 40 to 50% by weight. Potassium concentration 35
4545 wt%, and the concentration of the former is 5 watts higher than that of the latter.
It is preferable that the concentration is at least t% or higher. When the potassium hydroxide concentration of the electrolyte solution contained in the positive electrode mixture is less than 40% by weight, the heavy load discharge performance and the strength of the positive electrode pellet decrease. Also, preparing an electrolytic solution having a concentration exceeding 50 wt% is disadvantageous in mass production. On the other hand, if the concentration of potassium hydroxide in the electrolyte injected into the separator is less than 35% by weight, the heavy-load discharge performance decreases. In addition, 45wt%
If it exceeds, it takes time for absorption into the separator, and the productivity is reduced. More preferably, the concentration of potassium hydroxide in the electrolyte solution contained in the positive electrode mixture is 45 to 50 wt%.

【0008】[0008]

【発明の実施の形態】本発明は、正極合剤粉末に添加す
る電解液の水酸化カリウム濃度を高濃度にすると、正極
ペレットの強度が向上することに着目してなされたもの
である。この効果の理由の詳細は定かではないが、アル
カリ電解液の濃度が高いほど電解液の粘性が高く、また
界面張力等が作用して正極合剤粉末の結着性が増すこと
によるものと思われる。一方、前記のような正極ペレッ
トの強度を向上する効果を有する高濃度のアルカリ電解
液は、セパレータへの吸収速度が遅く、生産性が低下す
る。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention has been made by paying attention to the fact that the strength of a positive electrode pellet is improved by increasing the concentration of potassium hydroxide in an electrolytic solution added to a positive electrode mixture powder. Although the details of the reason for this effect are not clear, it is thought that the higher the concentration of the alkaline electrolyte, the higher the viscosity of the electrolyte, and the more the interfacial tension acts to increase the binding property of the positive electrode mixture powder. It is. On the other hand, a high-concentration alkaline electrolyte having the effect of improving the strength of the positive electrode pellet as described above has a low absorption rate to the separator, and the productivity is reduced.

【0009】そこで、本発明では、正極合剤用の電解液
に高濃度のものを用い、注液用の電解液にそれより低濃
度のものを用いる。これによって、正極ペレットの強度
の増加と、セパレータへの吸液時間の短縮化とを同時に
達成することができる。また、正極合剤用の電解液と、
注液用の電解液の濃度とを異ならせても、両者の電解液
の濃度を適度に調整することにより、放電性能を維持す
ることができる。本発明は、上記のように、正極合剤へ
特別なバインダーを添加するものではないから、従来の
放電性能を維持することができる。また、正極ペレット
の強度の向上のために、成形圧力を特別に高くするもの
ではないから、成形金型の摩耗や成形ピンの折れなどの
不都合が増加するという問題もない。
Therefore, in the present invention, a high concentration electrolyte is used for the positive electrode mixture, and a lower concentration electrolyte is used for the injection solution. As a result, it is possible to simultaneously increase the strength of the positive electrode pellet and shorten the liquid absorption time to the separator. Also, an electrolyte for a positive electrode mixture,
Even if the concentration of the electrolyte for injection is made different, the discharge performance can be maintained by appropriately adjusting the concentrations of both electrolytes. Since the present invention does not add a special binder to the positive electrode mixture as described above, the conventional discharge performance can be maintained. In addition, since the molding pressure is not particularly increased in order to improve the strength of the positive electrode pellet, there is no problem that inconveniences such as abrasion of the molding die and breakage of the molding pin increase.

【0010】以下に、本発明の実施例を説明する。図1
は、本実施例に係るアルカリ乾電池LR6の要部を断面
にした正面図である。1は鋼製の電池ケースである。電
池ケース1内には、正極合剤2が収容されている。この
正極合剤は、次のようにして作製された。まず、二酸化
マンガンと黒鉛とアルカリ電解液とを重量比95:5:
2の割合で混合し、十分攪拌した後、フレーク状に圧縮
成形した。このフレーク状に成形した正極合剤を粉砕し
て顆粒状とし、これを篩により分級し、14〜80メッ
シュのものを中空円筒形に加圧成形して正極ペレットを
得た。この正極ペレット4個を電池ケース1内へ挿入
し、加圧治具により正極ペレットを再成形して電池ケー
ス1の内壁に密着させた。
An embodiment of the present invention will be described below. Figure 1
FIG. 5 is a front view of a cross section of a main part of the alkaline dry battery LR6 according to the present embodiment. Reference numeral 1 denotes a battery case made of steel. A positive electrode mixture 2 is accommodated in the battery case 1. This positive electrode mixture was produced as follows. First, manganese dioxide, graphite, and an alkaline electrolyte were mixed in a weight ratio of 95: 5:
After mixing at a ratio of 2 and sufficiently stirring, the mixture was compression-molded into flakes. The flake-shaped positive electrode mixture was pulverized into granules, which were classified by a sieve, and 14-80 mesh powder was pressed into a hollow cylindrical shape to obtain positive electrode pellets. Four of these positive electrode pellets were inserted into the battery case 1, and the positive electrode pellets were re-formed by a pressing jig and brought into close contact with the inner wall of the battery case 1.

【0011】上記のようにして電池ケース内に配置され
た正極合剤2の中央に有底円筒形のセパレータ4を配置
し、セパレータ内へアルカリ電解液の所定量を注入し
た。所定時間経過後、アルカリ電解液とゲル化剤と亜鉛
合金粉末からなるゲル状負極3をセパレータ4内へ充填
した。
A bottomed cylindrical separator 4 was placed at the center of the positive electrode mixture 2 placed in the battery case as described above, and a predetermined amount of an alkaline electrolyte was injected into the separator. After a lapse of a predetermined time, the separator 4 was filled with the gelled negative electrode 3 composed of an alkaline electrolyte, a gelling agent, and a zinc alloy powder.

【0012】次に、常法により電池ケース1の開口部近
傍に段部を形成した後、負極集電子6、座金7および負
極端子板8を組み合わせた樹脂製封口体5を電池ケース
の開口部に填め、電池ケース1の開口端を内方へ折曲す
ることにより封口工程を完了した。この後、熱収縮性樹
脂チューブからなる外装ラベルを被着した。
Next, after a step is formed in the vicinity of the opening of the battery case 1 by a conventional method, a resin sealing body 5 in which the negative electrode current collector 6, the washer 7 and the negative electrode terminal plate 8 are combined is attached to the opening of the battery case. And the opening end of the battery case 1 was bent inward to complete the sealing step. Thereafter, an outer label made of a heat-shrinkable resin tube was attached.

【0013】以上のアルカリ乾電池の製造工程におい
て、表1に示すように、正極合剤用、注液用、およびゲ
ル状負極用の水酸化カリウム電解液の濃度を各種変えて
電池を製造した。それらの電池の正極ペレットの強度、
注入した電解液の吸収時間、および放電容量の比較を表
1に示す。正極ペレットの強度は、円筒形のペレットを
台上に横向きにのせ、上からペレットの胴部にゲージ付
きの治具を押しつけ、ペレットが破壊したときの押圧力
で表した。放電容量は、20℃において、500mAの
電流で連続放電したときの終止電圧0.9Vまでの放電
時間を比較例1の値を基準値100とした指数で表し
た。比較例1は、従来の代表的な処方によるものであ
る。
In the above alkaline dry battery manufacturing process, as shown in Table 1, various concentrations of potassium hydroxide electrolytes for the positive electrode mixture, the liquid injection, and the gelled negative electrode were manufactured. The strength of the positive electrode pellets of those batteries,
Table 1 shows the comparison between the absorption time of the injected electrolyte and the discharge capacity. The strength of the positive electrode pellet was represented by a pressing force when a cylindrical pellet was placed sideways on a table, a jig with a gauge was pressed against the body of the pellet from above, and the pellet was broken. The discharge capacity was represented by an index using the value of Comparative Example 1 as a reference value of 100 as the discharge time up to a final voltage of 0.9 V when the battery was continuously discharged at a current of 500 mA at 20 ° C. Comparative Example 1 is based on a conventional typical formulation.

【0014】[0014]

【表1】 [Table 1]

【0015】図2は正極合剤に含有させた電解液の濃度
と正極ペレットの強度との関係を表したグラフである。
また、図3は注液用電解液の濃度と吸液時間との関係を
表したグラフである。図2から、電解液の水酸化カリウ
ム濃度が40wt%以上において従来の正極ペレットの
強度を保持することができ、従来の強度を上回るには4
5wt%以上50wt%とするのが好ましいことがわか
る。一方、注液した電解液の吸液時間は、電解液の水酸
化カリウム濃度が45wt%程度までなら従来に比べて
さほど長くはならないが、吸液時間だけに限れば40w
t%あるいはそれ以下が好ましい。また、放電性能を考
慮に入れると、正極合剤用電解液の濃度を高くして正極
ペレットの強度を上げるとともに吸液時間を延ばさず、
放電性能を維持するには、正極合剤用電解液濃度を45
〜50wt%、注液用電解液濃度を35〜40wt%と
し、前者の濃度が後者のそれより5wt%以上高くする
のが最も好ましい。
FIG. 2 is a graph showing the relationship between the concentration of the electrolyte contained in the positive electrode mixture and the strength of the positive electrode pellet.
FIG. 3 is a graph showing the relationship between the concentration of the electrolyte for injection and the liquid absorption time. From FIG. 2, it can be seen that the strength of the conventional positive electrode pellet can be maintained when the concentration of potassium hydroxide in the electrolytic solution is 40 wt% or more.
It is understood that the content is preferably set to 5 wt% or more and 50 wt%. On the other hand, the absorption time of the injected electrolyte solution is not so long as compared with the conventional one if the potassium hydroxide concentration of the electrolyte solution is up to about 45 wt%.
t% or less is preferred. In addition, taking into account the discharge performance, the concentration of the electrolyte for the positive electrode mixture is increased to increase the strength of the positive electrode pellet, and the liquid absorption time is not extended,
In order to maintain the discharge performance, the concentration of the electrolyte for the positive electrode mixture should be 45
It is most preferable that the concentration of the electrolyte for injection is 35 to 40 wt%, and the concentration of the former is 5 wt% or more higher than that of the latter.

【0016】[0016]

【発明の効果】以上のように本発明によれば、従来の放
電性能を維持し、なおかつ正極ペレットの強度を向上さ
せて円筒形アルカリ電池の歩留まりを向上することがで
きる。
As described above, according to the present invention, it is possible to improve the yield of a cylindrical alkaline battery by maintaining the conventional discharge performance and improving the strength of the positive electrode pellet.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の一実施例に係るアルカリ乾電池の要部
を切欠した正面図である。
FIG. 1 is a front view of an alkaline dry battery according to one embodiment of the present invention, in which main parts are cut away.

【図2】正極合剤用電解液の濃度と正極ペレットの強度
との関係を示すグラフである。
FIG. 2 is a graph showing the relationship between the concentration of an electrolyte for a positive electrode mixture and the strength of a positive electrode pellet.

【図3】注液用電解液の濃度と吸液時間との関係を示す
グラフである。
FIG. 3 is a graph showing a relationship between a concentration of an electrolyte for injection and a liquid absorption time.

【符号の説明】[Explanation of symbols]

1 電池ケース 2 正極合剤 3 ゲル状負極 4 セパレータ 5 封口体 6 負極集電体 7 座金 8 負極端子板 9 外装ラベル DESCRIPTION OF SYMBOLS 1 Battery case 2 Positive electrode mixture 3 Gelled negative electrode 4 Separator 5 Sealing body 6 Negative current collector 7 Washer 8 Negative terminal plate 9 Exterior label

───────────────────────────────────────────────────── フロントページの続き (72)発明者 元谷 祐司 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 Fターム(参考) 5H024 AA02 AA14 BB05 BB07 BB08 CC02 CC14 DD09 DD14 FF09 HH08 5H050 AA14 AA19 BA04 CA02 CB13 DA02 DA09 EA12 FA08 GA03 GA10 GA23 HA10  ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Yuji Motoya 1006 Kazuma Kadoma, Kadoma-shi, Osaka Matsushita Electric Industrial Co., Ltd. F term (reference) 5H024 AA02 AA14 BB05 BB07 BB08 CC02 CC14 DD09 DD14 FF09 HH08 5H050 AA14 AA19 BA04 CA02 CB13 DA02 DA09 EA12 FA08 GA03 GA10 GA23 HA10

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 二酸化マンガンと黒鉛およびアルカリ電
解液を含有する正極合剤粉末を中空円筒形に成形する工
程、得られた正極合剤成形体を金属製電池ケースに挿入
し、再加圧して正極合剤成形体を電池ケースへ密着させ
る工程、前記正極合剤成形体の内側に筒状セパレータを
配置する工程、前記筒状セパレータの内部へアルカリ電
解液を注入し、電解液を正極合剤成形体およびセパレー
タへ吸収させる工程、および前記筒状セパレータ内へゲ
ル状負極を充填する工程を有し、前記正極合剤の含有す
るアルカリ電解液の濃度を前記セパレータの内部へ注入
するアルカリ電解液のそれより高濃度としたことを特徴
とする円筒形アルカリ電池の製造方法。
1. A step of forming a positive electrode mixture powder containing manganese dioxide, graphite and an alkaline electrolyte into a hollow cylindrical shape, inserting the obtained positive electrode mixture molded body into a metal battery case, and pressurizing again. A step of bringing the positive electrode mixture molded body into close contact with the battery case, a step of arranging a cylindrical separator inside the positive electrode mixture molded body, injecting an alkaline electrolyte into the cylindrical separator, and dissolving the electrolytic solution in the positive electrode mixture. An alkaline electrolyte solution comprising a step of absorbing the molded body and the separator, and a step of filling the cylindrical separator with a gelled negative electrode, and injecting the concentration of the alkaline electrolyte contained in the positive electrode mixture into the interior of the separator A method for producing a cylindrical alkaline battery, wherein the concentration is higher than that of the above.
【請求項2】 前記アルカリ電解液が、水酸化カリウム
水溶液であり、前記正極合剤の含有する電解液の水酸化
カリウム濃度が40〜50wt%、前記セパレータの内
部へ注入する電解液の水酸化カリウム濃度が35〜45
wt%であり、前者の濃度が後者のそれより5wt%以
上高濃度である請求項1記載の円筒形アルカリ電池の製
造方法。
2. The method according to claim 1, wherein the alkaline electrolyte is an aqueous solution of potassium hydroxide, the concentration of potassium hydroxide in the electrolyte contained in the positive electrode mixture is 40 to 50 wt%, and the concentration of hydroxide in the electrolyte to be injected into the separator is increased. Potassium concentration 35-45
The method for producing a cylindrical alkaline battery according to claim 1, wherein the concentration is 5 wt% or more, and the concentration of the former is 5 wt% or more higher than that of the latter.
【請求項3】 前記正極合剤の含有する電解液の水酸化
カリウム濃度が45〜50wt%である請求項2記載の
円筒形アルカリ電池の製造方法。
3. The method for producing a cylindrical alkaline battery according to claim 2, wherein the concentration of potassium hydroxide in the electrolyte solution contained in the positive electrode mixture is 45 to 50 wt%.
JP2000196182A 2000-06-29 2000-06-29 Manufacturing method of cylindrical alkaline battery Withdrawn JP2002015748A (en)

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100413133C (en) * 2002-07-12 2008-08-20 日立万胜株式会社 Alkaline battery and method for producing the same
US7510801B2 (en) 2002-07-12 2009-03-31 Hitachi Maxell, Ltd. Alkaline battery and method for producing the same

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100413133C (en) * 2002-07-12 2008-08-20 日立万胜株式会社 Alkaline battery and method for producing the same
US7510801B2 (en) 2002-07-12 2009-03-31 Hitachi Maxell, Ltd. Alkaline battery and method for producing the same
US7767336B2 (en) 2002-07-12 2010-08-03 Hitachi Maxell, Ltd. Alkaline battery and method for producing the same

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