JPH1012245A - Manufacture of alkaline dry battery - Google Patents

Manufacture of alkaline dry battery

Info

Publication number
JPH1012245A
JPH1012245A JP15967296A JP15967296A JPH1012245A JP H1012245 A JPH1012245 A JP H1012245A JP 15967296 A JP15967296 A JP 15967296A JP 15967296 A JP15967296 A JP 15967296A JP H1012245 A JPH1012245 A JP H1012245A
Authority
JP
Japan
Prior art keywords
positive electrode
electrode mixture
weight
alkaline dry
dry battery
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.)
Pending
Application number
JP15967296A
Other languages
Japanese (ja)
Inventor
Hideaki Tokugawa
秀昭 徳川
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.)
Sony Corp
Original Assignee
Sony Corp
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 Sony Corp filed Critical Sony Corp
Priority to JP15967296A priority Critical patent/JPH1012245A/en
Publication of JPH1012245A publication Critical patent/JPH1012245A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02E60/12

Landscapes

  • Primary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a highly efficient manufacturing method of a high capacity alkaline dry battery. SOLUTION: After pressurizing molding is performed on a positive electrode mix 2 composed of a manganese dioxide, carbon and a pottasium hydroxide aqueous solution of 39wt.% to 48wt.%, a potassium hydroxide aqueous solution of 30wt.% to 38wt.% is injected into a separator 4 and the positive electrode mix 2, and the concentration of the potassium hydroxide aqueous solution in the whole battery is set to 35wt.% to 45wt.%. Density after pressurizing molding of the positive electrode mix 2 is set not less than 3.4g/cm<3> . By being constituted in this way, the occurrence of a crack and a fragment of the positive electrode mix 2 is reduced, and since impregnating time of an electrolyte can be shortened, a high capacity alkaline dry battery can be manufactured with an excellent yield.

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】本発明は粉状正極合剤を用い
るアルカリ乾電池の高容量化と製造の高効率化に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to increasing the capacity and manufacturing efficiency of an alkaline dry battery using a powdered positive electrode mixture.

【0002】[0002]

【従来の技術】近年、携帯用電子機器やコードレス電子
機器等の電源として、電池の高容量化への要求が高まっ
てきている。この電池の高容量化には、従来より電池の
体積的な制約があるなかで、正極、負極の活物質の充填
量を多くすることが考えられてきた。例えば正極合剤に
ついては結着剤を用いずにリング状に成形し、高密度化
することが一般的になっている。しかしながら、結着剤
を用いていないため、正極合剤の成形性、形状安定性を
確保することは困難であり、また、高密度化された正極
合剤に短時間で高粘度の電解液を含浸させることも困難
であった。
2. Description of the Related Art In recent years, there has been an increasing demand for higher capacity batteries as power supplies for portable electronic devices and cordless electronic devices. In order to increase the capacity of this battery, it has been conventionally considered to increase the filling amount of the active material of the positive electrode and the negative electrode in view of the volume limitation of the battery. For example, it is common to form a positive electrode mixture into a ring shape without using a binder to increase the density. However, since a binder is not used, it is difficult to secure the moldability and shape stability of the positive electrode mixture, and a high-viscosity electrolytic solution is applied to the densified positive electrode mixture in a short time. It was also difficult to impregnate.

【0003】正極合剤の成形性を良くするためには正極
合剤のバインダーとして架橋型ポリアクリル酸ソーダを
用い、正極合剤を筒形に成形するときに割れや欠けが発
生するのを防止する技術がある。これに関しては、例え
ば特開昭57−152674号の明細書中に述べられて
いる。しかしながら、この方法では、限られた電池内容
積の一部を電池反応に関与しないバインダーに費やすこ
とになり、高容量化を行う上で問題となるだけでなく、
電池に使用する材料の種類を増やすことにもなり、製造
コストの増加要因にもなるものである。
In order to improve the moldability of the positive electrode mixture, a crosslinked type sodium polyacrylate is used as a binder of the positive electrode mixture to prevent cracking and chipping when the positive electrode mixture is formed into a cylindrical shape. There is technology to do. This is described, for example, in the specification of JP-A-57-152677. However, in this method, a part of the limited battery internal volume is used for a binder not involved in the battery reaction, which is not only a problem in increasing the capacity, but also a problem.
This also increases the types of materials used for the battery, and also increases the manufacturing cost.

【0004】また、加圧成形した正極合剤への電解液の
含浸は、従来より、電解液を添加したあと長時間放置す
ることにより行われていた。この電解液の含浸を促進さ
せるために、正極缶に正極合剤を収納した後、過剰な電
解液を注入し、それら全体を加熱して電解液を正極合剤
に含浸させた後、余剰の電解液を取り除くこと等の技術
がある。これに関しては、例えば特開昭57−1488
79号の明細書中に述べられている。しかしながらこの
含浸方法では、加熱と電解液の除去工程が増え、また、
余剰の電解液の処理工程も必要となり、製造工程が煩雑
になる問題点があった。
In addition, the impregnation of the pressure-molded positive electrode mixture with the electrolytic solution has been conventionally performed by adding the electrolytic solution and allowing the mixture to stand for a long time. In order to accelerate the impregnation of the electrolyte, after storing the positive electrode mixture in the positive electrode can, an excessive amount of the electrolyte is injected, and the entire mixture is heated to impregnate the electrolyte with the positive electrode mixture. There are techniques such as removing the electrolyte. Regarding this, for example, Japanese Patent Laid-Open No. 57-1488
No. 79 is mentioned in the specification. However, in this impregnation method, the steps of heating and removing the electrolytic solution are increased, and
There is also a problem that a process for treating an excessive electrolyte is required, and the manufacturing process is complicated.

【0005】[0005]

【発明が解決しようとする課題】従って本発明の課題
は、正極合剤を筒形に成形するときに割れや欠けが発生
することを防止し、また、正極合剤に電解液を短時間で
含浸することができるようにして、歩留りが良く、生産
性の高いアルカリ乾電池の製造方法を提供しようとする
ものである。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to prevent cracks and chipping from occurring when a positive electrode mixture is formed into a cylindrical shape, and to apply an electrolyte to the positive electrode mixture in a short time. An object of the present invention is to provide a method of manufacturing an alkaline dry battery which can be impregnated, has a good yield, and has high productivity.

【0006】[0006]

【課題を解決するための手段】本発明は上記課題に鑑み
なされたものであり、粉状正極合剤を有するアルカリ乾
電池の製造工程において、二酸化マンガン、カーボンお
よび39重量%以上、48重量%以下の水酸化カリウム
水溶液からなる正極合剤を加圧成形後、セパレータおよ
び正極合剤に30重量%以上、38重量%以下の水酸化
カリウム水溶液を注入し、全電池内水酸化カリウム水溶
液濃度を35重量%以上、45重量%以下とする。ま
た、上述した正極合剤の加圧成形後の密度が3.4g/
cm3 以上となるアルカリ乾電池の製造方法を用いて上
記課題を解決する。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned problems, and it is an object of the present invention to provide a process for manufacturing an alkaline dry battery having a powdered positive electrode mixture, in which manganese dioxide, carbon and 39% by weight or more and 48% by weight or less are used. After press-molding a positive electrode mixture composed of an aqueous solution of potassium hydroxide, 30% by weight or more and 38% by weight or less of an aqueous potassium hydroxide solution are injected into the separator and the positive electrode mixture, and the concentration of the aqueous potassium hydroxide solution in all the batteries is reduced to 35%. % By weight and 45% by weight or less. Further, the density of the above-mentioned positive electrode mixture after pressure molding was 3.4 g /
The above problem is solved by using a method for manufacturing an alkaline dry battery having a capacity of 3 cm 3 or more.

【0007】本発明の製造方法によると、結着剤の添加
なしで正極合剤の割れや欠けが防止され、また、電解液
の含浸時間の短縮が図れる。
According to the production method of the present invention, cracking and chipping of the positive electrode mixture can be prevented without adding a binder, and the time for impregnation with the electrolyte can be shortened.

【0008】[0008]

【発明の実施の形態】本発明の実施の形態例について図
1および図2を参照して説明する。図1は本発明の一例
である筒形アルカリ乾電池の断面図であり、図2は電解
液注入について説明するためのフローチャートである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described with reference to FIGS. FIG. 1 is a cross-sectional view of a cylindrical alkaline dry battery as an example of the present invention, and FIG. 2 is a flowchart for explaining electrolyte injection.

【0009】筒形アルカリ乾電池は図1に示すように、
電池ケースを兼ねる、上端部が閉塞されて下端部が開口
された円筒形の正極ケース1内に二酸化マンガンとカー
ボンおよび水酸化カリウム水溶液からなる正極合剤2を
外側に、また、粒状亜鉛と水酸化カリウム水溶液および
増粘剤等からなるゲル状の負極合剤3を内側にして、不
織布からなるセパレータ4により分離されて設けられて
いる。
[0009] As shown in FIG.
A positive electrode mixture 2 composed of manganese dioxide, carbon and an aqueous solution of potassium hydroxide is placed outside in a cylindrical positive electrode case 1 which also serves as a battery case and has a closed upper end and an open lower end. It is provided separated by a separator 4 made of a non-woven fabric with the gelled negative electrode mixture 3 made of an aqueous solution of potassium oxide, a thickener and the like inside.

【0010】また、正極ケース1の円筒外周面は外装ラ
ベル5によって覆われており、正極ケース1の上部に正
極端子6が設けられている。正極ケース1の開口部に
は、封口部材7が嵌合されていて、この開口部を封口し
ている。封口部材7はナイロンやポリプロピレン等のプ
ラスチック材で作られ、この封口部材7を補強するため
に補強部材8が設けられ、更に、補強部材8を覆うよう
にスプリング9と、負極端子10を兼ねる円盤状の金属
カバーが取り付けられている。また、前記補強部材8が
嵌合された封口部材7の貫通孔を通して黄銅性の集電ピ
ン11が負極合剤3の中に挿入されている。
A cylindrical outer peripheral surface of the positive electrode case 1 is covered with an outer label 5, and a positive electrode terminal 6 is provided on the upper part of the positive electrode case 1. A sealing member 7 is fitted into the opening of the positive electrode case 1 and seals this opening. The sealing member 7 is made of a plastic material such as nylon or polypropylene. A reinforcing member 8 is provided to reinforce the sealing member 7. -Shaped metal cover is attached. In addition, a brass collector pin 11 is inserted into the negative electrode mixture 3 through a through hole of the sealing member 7 in which the reinforcing member 8 is fitted.

【0011】つぎに、図2を参照し、電解液注入につい
て説明する。まず、二酸化マンガン(符号20)を90
重量%計量し(符号23)、また、カーボン(符号2
1)を4重量%計量して(符号24)、両者を乾式混合
する(符号26)。一方、39〜48重量%の電解液
(符号22)を6重量%計量して(符号25)、乾式混
合したものとこの電解液を湿式混合する(符号27)。
つぎにこの混合物を造粒し(符号28)、加圧成形して
(符号29)正極合剤のペレットとし、このペレットを
正極ケースに挿入する(符号30)。その後、シール剤
(図示せず)を塗布し、ペレットの内側にセパレータを
挿入して(符号31)、そのセパレータ内部に30〜3
8重量%の電解液を注入する(符号32)。その後に続
く工程については図示および説明を省略する。
Next, the injection of the electrolyte will be described with reference to FIG. First, manganese dioxide (symbol 20) was converted to 90
Weight% (reference number 23) and carbon (reference number 2).
1) is weighed at 4% by weight (reference numeral 24) and both are dry-mixed (reference numeral 26). On the other hand, 39% to 48% by weight of the electrolytic solution (reference numeral 22) is measured at 6% by weight (reference numeral 25), and the dry-mixed electrolyte is wet-mixed (reference numeral 27).
Next, this mixture is granulated (reference numeral 28), pressed and molded (reference numeral 29) to form a pellet of the positive electrode mixture, and inserted into a positive electrode case (reference numeral 30). Thereafter, a sealant (not shown) is applied, and a separator is inserted inside the pellet (reference numeral 31).
An electrolyte of 8% by weight is injected (reference numeral 32). Illustration and description of subsequent steps are omitted.

【0012】実施例 上述した製造方法に則り、次に示す種類の筒形アルカリ
乾電池を作製した。まず、表1に示すA〜Hの正極合剤
を作成する。表の値はA〜Hの正極合剤を構成する水酸
化カリウム水溶液の濃度である。この正極合剤は二酸化
マンガンとカーボン(グラファイト)と表1に示す濃度
の水酸化カリウム水溶液を90:4:6の重量%で混合
し、外形13.2mm、内径9mm、高さ14mm、質
量3.5g、密度3.4g/cm3 のリング状としたも
のである。
EXAMPLES In accordance with the above-described production method, the following types of cylindrical alkaline dry batteries were produced. First, the positive electrode mixtures A to H shown in Table 1 are prepared. The values in the table are the concentrations of the aqueous potassium hydroxide solutions constituting the positive electrode mixtures A to H. This positive electrode mixture was prepared by mixing manganese dioxide, carbon (graphite), and an aqueous potassium hydroxide solution having the concentrations shown in Table 1 at a weight ratio of 90: 4: 6, and was 13.2 mm in outer diameter, 9 mm in inner diameter, 14 mm in height, and 3 in mass. This was a ring having a density of 0.5 g and a density of 3.4 g / cm 3 .

【0013】[0013]

【表1】 [Table 1]

【0014】上述した正極合剤A〜Hの成形体をそれぞ
れ1万個製造し、正極合剤成形工程における割れ欠けの
発生率を調べた。その結果を表2に示す。
[0014] Each of the above-mentioned molded articles of the positive electrode mixtures A to H was manufactured in 10,000 pieces, and the occurrence rate of cracks and chips in the positive electrode mixture molding step was examined. Table 2 shows the results.

【0015】[0015]

【表2】 [Table 2]

【0016】表2に示すように正極合剤成形体の割れ欠
けの発生は水酸化カリウム水溶液の濃度と関係している
ことが分かる。特に38%以下の濃度で割れ欠けの発生
率が急増している。
As shown in Table 2, it can be seen that the occurrence of cracks in the molded article of the positive electrode mixture is related to the concentration of the aqueous potassium hydroxide solution. In particular, at a concentration of 38% or less, the incidence of cracks and chips is rapidly increasing.

【0017】また、正極合剤成形体Aを3個を正極ケー
ス1に充填し、セパレータ4を挿入した後、表3に示す
ようなa〜hの濃度の水酸化カリウム水溶液を1g注入
して含浸時間を測定した。
Further, after three positive electrode mixture molded articles A were filled in the positive electrode case 1 and the separator 4 was inserted, 1 g of an aqueous potassium hydroxide solution having a concentration of a to h as shown in Table 3 was injected. The impregnation time was measured.

【0018】[0018]

【表3】 [Table 3]

【0019】含浸時間は正極ケース1の底に水酸化カリ
ウム水溶液の液溜まりが見られなくなり、正極ケース1
を反転しても液こぼれがなくなる時間を含浸時間とし、
その結果を表4に示す。
During the impregnation time, no liquid pool of the aqueous potassium hydroxide solution was observed at the bottom of the positive electrode case 1 and the positive electrode case 1
The time when the liquid does not spill even if it is reversed is the impregnation time,
Table 4 shows the results.

【0020】[0020]

【表4】 [Table 4]

【0021】表4に示すように、正極合剤成形体Aに対
する水酸化カリウム水溶液の含浸時間はその水酸化カリ
ウム水溶液の濃度と関係していることが分かる。特に3
9%以上の濃度で含浸時間が急増している。
As shown in Table 4, it can be seen that the impregnation time of the aqueous potassium hydroxide solution with respect to the positive electrode mixture molded product A is related to the concentration of the aqueous potassium hydroxide solution. Especially 3
Above 9%, the impregnation time increases rapidly.

【0022】以上の結果から、39重量%以上、48重
量%以下の水酸化カリウム水溶液からなる電解液を正極
合剤の成形前に添加することにより、成形体の割れ欠け
の発生率を大幅に抑制することが可能となり、また、そ
の後のセパレータおよび正極合剤に電解液を注入する工
程において30重量%以上、38重量%以下の水酸化カ
リウム水溶液からなる電解液を注入することにより、電
解液の含浸時間を大幅に短縮することが可能となること
が認められる。
From the above results, by adding an electrolyte comprising an aqueous solution of potassium hydroxide of 39% by weight or more and 48% by weight or less before forming the positive electrode mixture, the occurrence rate of cracking and chipping of the formed body can be greatly reduced In addition, by injecting an electrolyte composed of an aqueous solution of potassium hydroxide of 30% by weight or more and 38% by weight or less in the subsequent step of injecting the electrolyte into the separator and the positive electrode mixture, It can be seen that the impregnation time of the.

【0023】[0023]

【発明の効果】以上の説明からも明らかなように、本発
明による製造方法、即ち、39重量%以上、48重量%
以下の水酸化カリウム水溶液からなる電解液を正極合剤
の成形前に添加し、また、その後のセパレータおよび正
極合剤に電解液を注入する工程において30重量%以
上、38重量%以下の水酸化カリウム水溶液からなる電
解液を注入することにより、正極合剤成形体の割れ欠け
の発生を低減し、電解液の含浸時間が短縮される。従っ
て、高容量のアルカリ乾電池を効率よく製造することが
可能となる。
As is clear from the above description, the production method according to the present invention, that is, at least 39% by weight and 48% by weight
The following electrolytic solution consisting of an aqueous potassium hydroxide solution is added before forming the positive electrode mixture, and in the subsequent step of injecting the electrolytic solution into the separator and the positive electrode mixture, 30% by weight or more and 38% by weight or less of hydroxide are added. By injecting the electrolytic solution composed of the aqueous potassium solution, the occurrence of cracks and chips in the positive electrode mixture molded article is reduced, and the impregnation time of the electrolytic solution is shortened. Therefore, a high-capacity alkaline dry battery can be efficiently manufactured.

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

【図1】 本発明の一例である筒形アルカリ乾電池の断
面図である。
FIG. 1 is a sectional view of a cylindrical alkaline dry battery which is an example of the present invention.

【図2】 電解液注入について説明するためのフローチ
ャートである。
FIG. 2 is a flowchart for explaining electrolyte injection.

【符号の説明】 1…正極ケース、2…正極合剤、3…負極合剤、4…セ
パレータ、5…外装ラベル、6…正極端子、7…封口部
材、8…補強部材、9…スプリング、10…負極端子、
11…集電ピン
[Description of References] 1 ... Positive electrode case, 2 ... Positive electrode mixture, 3 ... Negative electrode mixture, 4 ... Separator, 5 ... Outer label, 6 ... Positive electrode terminal, 7 ... Sealing member, 8 ... Reinforcement member, 9 ... Spring, 10 ... negative electrode terminal,
11 ... current collecting pin

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 粉状正極合剤を有するアルカリ乾電池の
製造工程において、 二酸化マンガンと、カーボンと、39重量%以上、48
重量%以下の水酸化カリウム水溶液とからなる正極合剤
を加圧成形後、 セパレータおよび正極合剤に30重量%以上、38重量
%以下の水酸化カリウム水溶液を注入し、 全電池内水酸化カリウム水溶液濃度を35重量%以上、
45重量%以下とすることを特徴とするアルカリ乾電池
の製造方法。
In a manufacturing process of an alkaline dry battery having a powdered positive electrode mixture, manganese dioxide, carbon, and at least 39% by weight
After press-molding a positive electrode mixture comprising an aqueous solution of potassium hydroxide of not more than 30% by weight, an aqueous solution of potassium hydroxide of not less than 30% by weight and not more than 38% by weight is poured into the separator and the positive electrode mixture. Aqueous solution concentration of 35% by weight or more,
A method for producing an alkaline dry battery, wherein the content is 45% by weight or less.
【請求項2】 前記正極合剤の加圧成形後の密度を3.
4g/cm3 以上とすることを特徴とする、請求項1に
記載のアルカリ乾電池の製造方法。
2. The density of the positive electrode mixture after pressure molding is set to 3.
Characterized by a 4g / cm 3 or more, a manufacturing method of an alkaline dry battery according to claim 1.
JP15967296A 1996-06-20 1996-06-20 Manufacture of alkaline dry battery Pending JPH1012245A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15967296A JPH1012245A (en) 1996-06-20 1996-06-20 Manufacture of alkaline dry battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15967296A JPH1012245A (en) 1996-06-20 1996-06-20 Manufacture of alkaline dry battery

Publications (1)

Publication Number Publication Date
JPH1012245A true JPH1012245A (en) 1998-01-16

Family

ID=15698819

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15967296A Pending JPH1012245A (en) 1996-06-20 1996-06-20 Manufacture of alkaline dry battery

Country Status (1)

Country Link
JP (1) JPH1012245A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003536230A (en) * 2000-06-19 2003-12-02 エヴァレディー バッテリー カンパニー インコーポレイテッド Alkaline electrochemical battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003536230A (en) * 2000-06-19 2003-12-02 エヴァレディー バッテリー カンパニー インコーポレイテッド Alkaline electrochemical battery

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