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JP2832018B2 - Method for producing negative electrode for alkaline battery - Google Patents
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JP2832018B2 - Method for producing negative electrode for alkaline battery - Google Patents

Method for producing negative electrode for alkaline battery

Info

Publication number
JP2832018B2
JP2832018B2 JP63259501A JP25950188A JP2832018B2 JP 2832018 B2 JP2832018 B2 JP 2832018B2 JP 63259501 A JP63259501 A JP 63259501A JP 25950188 A JP25950188 A JP 25950188A JP 2832018 B2 JP2832018 B2 JP 2832018B2
Authority
JP
Japan
Prior art keywords
added
gelling agent
negative electrode
mixing
fluorocarbon
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
Application number
JP63259501A
Other languages
Japanese (ja)
Other versions
JPH02106872A (en
Inventor
健一 篠田
廣彦 太田
隆 松尾
清英 筒井
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.)
FDK Corp
Original Assignee
FDK 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 FDK Corp filed Critical FDK Corp
Priority to JP63259501A priority Critical patent/JP2832018B2/en
Publication of JPH02106872A publication Critical patent/JPH02106872A/en
Application granted granted Critical
Publication of JP2832018B2 publication Critical patent/JP2832018B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/06Electrodes for primary cells
    • H01M4/08Processes of manufacture
    • H01M4/12Processes of manufacture of consumable metal or alloy electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M6/00Primary cells; Manufacture thereof
    • H01M6/22Immobilising of electrolyte
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Primary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 《産業上の利用分野》 この発明は、亜鉛粉末をアルカリ電解液に分散させた
アルカリ電池用負極の製造方法の改良に関する。
The present invention relates to an improvement in a method for manufacturing a negative electrode for an alkaline battery in which zinc powder is dispersed in an alkaline electrolyte.

《従来の技術》 アルカリ電池に用いられているゲル状負極は、水酸化
カリウム水溶液などのアルカリ電解液を亜鉛粉末ととも
にゲル化剤を用いてゲル状にしたものである。ゲル化剤
としてはカルボキシメチルセルローズ(CMC)、ポリア
クリル酸ソーダ、ポリアクリル酸などを単独あるいは2
種以上混合して用いている。また、ゲル状負極を得る具
体的な手順としては湿式混合と乾式混合とがある。
<< Conventional Technology >> A gelled negative electrode used in an alkaline battery is obtained by gelling an alkaline electrolyte such as an aqueous potassium hydroxide solution with a zinc powder and a gelling agent. As a gelling agent, carboxymethyl cellulose (CMC), sodium polyacrylate, polyacrylic acid, etc., alone or
More than one species are mixed and used. Specific procedures for obtaining a gelled negative electrode include wet mixing and dry mixing.

湿式混合では、ゲル化剤の微粉末を所定濃度のアルカ
リ電解液に直接添加し、撹拌混合してゲル状電解液を
得、これに亜鉛粉末を混合して分散させる。
In the wet mixing, a fine powder of a gelling agent is directly added to an alkaline electrolyte having a predetermined concentration, and the mixture is stirred and mixed to obtain a gel electrolyte, and zinc powder is mixed and dispersed therein.

乾式混合では、粉末のゲル化剤と粒状亜鉛とを予め混
合した後、これにアルカリ電解液を加えて撹拌混合す
る。
In dry mixing, after a powdery gelling agent and granular zinc are mixed in advance, an alkaline electrolyte is added thereto, followed by stirring and mixing.

《発明が解決しようとする課題》 前述の湿式混合によると、粉末のゲル化剤をアルカリ
電解液に添加・混合する際、無秩序に分散するとゲル化
剤粒子の塊ができやすく(この塊を一般にママコと称し
ている)、その表面は溶媒和をおこし、均一なゲル状電
解液を得るのには長時間撹拌する必要があり、この撹拌
工程が負極製造時間の短縮化を阻害する大きな要因にな
っていた。
<< Problems to be Solved by the Invention >> According to the above-mentioned wet mixing, when the powdery gelling agent is added to and mixed with the alkaline electrolyte, the gelling agent particles are likely to be formed if they are dispersed in a random manner. It is necessary to stir the surface for solvation and obtain a uniform gel electrolyte for a long time, and this stirring process is a major factor that hinders shortening of the negative electrode manufacturing time. Had become.

前述の乾式混合では、粉末のゲル化剤と粒状亜鉛とを
混合してからアルカリ電解液に添加するので、湿式混合
のような極端なママコにはなりにくく、湿式混合の1/2
〜1/3の撹拌時間でゲル状負極を製造することができ
る。しかし、乾式混合では、亜鉛粒子の表面が十分にア
ルカリ電解液の浸透していないゲル化剤で覆われやすく
(アルカリ電解液が亜鉛粒子の表面に付着したゲル化剤
に浸透しにくい)、そのため電池の内部抵抗が増加し、
放電性能が低下するという欠点があった。
In the above-mentioned dry mixing, since the powdered gelling agent and the particulate zinc are mixed and then added to the alkaline electrolyte, it is difficult to become an extreme mamako like a wet mixing, and it is 1/2 of the wet mixing.
A gel negative electrode can be manufactured with a stirring time of about 1/3. However, in dry mixing, the surface of zinc particles is likely to be covered with a gelling agent that has not sufficiently penetrated the alkaline electrolyte (the alkaline electrolyte does not easily penetrate the gelling agent attached to the surface of the zinc particles). The internal resistance of the battery increases,
There is a disadvantage that the discharge performance is reduced.

この発明は上述した従来の問題点に鑑みなされたもの
で、その目的は、撹拌時間が短くてすみ、しかも亜鉛粉
末を良好な状態でゲル状電解液に分散させることができ
るようにした製造方法を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned conventional problems, and has as its object to provide a manufacturing method capable of shortening the stirring time and dispersing zinc powder in a gel electrolyte in a favorable state. Is to provide.

《課題を解決するための手段》 そこでこの発明では、エーテル結合を有するフルオロ
カーボンを添加した水にゲル化剤を加えて混合した後、
これにアルカリ電解液を加えて撹拌混合してゲル状電解
液を得、これに亜鉛粉末を分散させるようにした。
<< Means for Solving the Problems >> Therefore, in the present invention, after adding a gelling agent to water to which a fluorocarbon having an ether bond is added and mixing,
An alkaline electrolyte was added thereto, followed by stirring and mixing to obtain a gel electrolyte, in which zinc powder was dispersed.

《作 用》 エーテル結合を有するフルオロカーボンは一種の界面
活性剤であり、これを含んだ水に微粉末のゲル化剤を加
えて混合し、さらにアルカリ電解液を加えて撹拌混合す
る際に、界面活性剤の働きによってアルカリ電解液中に
ゲル化剤が分散されやすくなり、前述のママコを発生せ
ずに短い撹拌工程で均一なゲル状電解液を得ることがで
きる。この後は従来の湿式混合と同じで、このゲル状電
解液に亜鉛粉末を加えて混合・分散させる。
<Action> Fluorocarbon having an ether bond is a kind of surfactant, and when a fine powder gelling agent is added to water containing the same and mixed, and then an alkaline electrolyte is added and mixed with stirring, the surfactant is used. The action of the activator makes it easier for the gelling agent to be dispersed in the alkaline electrolyte, so that a uniform gel electrolyte can be obtained in a short stirring step without generating the above-mentioned mamako. Thereafter, zinc powder is added to the gel electrolyte and mixed and dispersed in the same manner as in conventional wet mixing.

《実施例》 エーテル結合を有するフルオロカーボンとしてはデュ
ポン社製の商品名ゾニールを用いる。またゲル化剤とし
てポリアクリル酸(日本紙薬製の商品名ジュンロンPW−
150)を用いる。混合手順は次の通りである。
<< Example >> As a fluorocarbon having an ether bond, Zonyl (trade name, manufactured by DuPont) is used. As a gelling agent, polyacrylic acid (trade name: Junron PW-
150). The mixing procedure is as follows.

水21重量%に前記ゾニールを添加する。なおゾニール
の添加量については後述する。
The zonil is added to 21% by weight of water. The amount of zonyl added will be described later.

前記ゾニールを含んだ水に微粉末のゲル化剤2重量%
を添加して混合する。
2% by weight of a fine powder gelling agent in water containing the zonil
Add and mix.

前記の水+ゾニール+ゲル化剤に水酸化カリウムの47
%水溶液を77重量%の割合で加えて、よく撹拌混合す
る。これでゲル状の電解液が得られる。
The above water + zonil + gelling agent
% Aqueous solution at a ratio of 77% by weight, and well mixed with stirring. Thus, a gel electrolyte solution is obtained.

前記のゲル状電解液に亜鉛粉末を所定量加えて混合・
分散させる。
A predetermined amount of zinc powder is added to the gel electrolyte and mixed.
Disperse.

前記のようにフルオロカーボン(商品名ゾニール)を
添加した湿式混合による本発明の製造方法によれば、従
来の乾式混合の場合と同様に、従来の湿式混合の場合の
1/2〜1/3の撹拌時間でママコのない均一なゲル状負極を
得ることができる。また従来の湿式混合と同様に予めゲ
ル状になった電解液が亜鉛粉末の表面に付着することに
なるので、従来の乾式混合のようにアルカリ電解液が浸
透していないゲル化剤で亜鉛粉末の表面が覆われるとい
うことは全くない。
According to the production method of the present invention by wet mixing to which a fluorocarbon (trade name: Zonyl) is added, as in the case of the conventional wet mixing, as in the case of the conventional dry mixing.
It is possible to obtain a uniform gelled negative electrode with no agitation with a stirring time of 1/2 to 1/3. Also, as in the case of the conventional wet mixing, the pre-gelled electrolytic solution will adhere to the surface of the zinc powder. The surface is never covered.

なお、前記フルオロカーボンの添加量は前記ゲル化剤
に対して1.0重量%以下が望ましい。これより多くのフ
ルオロカーボンを添加しても撹拌時間の短縮効果はそれ
ほど大きくならず、必要以上のフルオロカーボンを添加
することで放電容量が低下する傾向が確かめられた。従
って、撹拌混合時間を十分に短縮できる範囲内でフルオ
ロカーボンの添加量は少ない程よい。
In addition, the addition amount of the fluorocarbon is desirably 1.0% by weight or less based on the gelling agent. Even if more fluorocarbon was added, the effect of shortening the stirring time was not so large, and it was confirmed that the discharge capacity tended to decrease by adding more fluorocarbon than necessary. Therefore, the smaller the amount of fluorocarbon added, the better the stirring and mixing time can be sufficiently reduced.

《発明の効果》 以上詳細に説明したように、この発明に係るアルカリ
電池用負極の製造方法によれば、従来の乾式混合のよう
に亜鉛粒子の表面が十分にアルカリ電解液の浸透してい
ないゲル化剤で覆われるという不都合(その結果電池の
放電性能が低下する)がなく、しかも従来の湿式混合よ
りも格段に短い撹拌工程でママコのない均一なゲルを得
ることができる。したがって、この方法を採用すること
によって性能のよいアルカリ電池を能率よく生産するこ
とができるようになる。
<< Effects of the Invention >> As described in detail above, according to the method for manufacturing a negative electrode for an alkaline battery according to the present invention, the surface of the zinc particles does not sufficiently penetrate the alkaline electrolyte as in conventional dry mixing. There is no inconvenience of being covered with the gelling agent (as a result, the discharge performance of the battery is reduced), and a uniform gel without lumps can be obtained in a stirring step much shorter than the conventional wet mixing. Therefore, by adopting this method, an alkaline battery having good performance can be efficiently produced.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 筒井 清英 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 (56)参考文献 特開 昭49−4131(JP,A) (58)調査した分野(Int.Cl.6,DB名) H01M 4/06 - 4/12 H01M 6/22──────────────────────────────────────────────────続 き Continuation of front page (72) Inventor Kiyohide Tsutsui 5-36-11 Shimbashi, Minato-ku, Tokyo Inside Fuji Electric Chemical Co., Ltd. (56) References JP-A-49-4131 (JP, A) ( 58) Surveyed field (Int.Cl. 6 , DB name) H01M 4/06-4/12 H01M 6/22

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】エーテル結合を有するフルオロカーボンを
添加した水にゲル化剤を加えて混合した後、これにアル
カリ電解液を加えて撹拌混合してゲル状電解液を得、こ
れに亜鉛粉末を分散させるようにしたアルカリ電池用負
極の製造方法。
1. A gelling agent is added to and mixed with water to which a fluorocarbon having an ether bond is added, and then an alkaline electrolyte is added thereto, followed by stirring and mixing to obtain a gel electrolyte, and zinc powder is dispersed therein. A method for producing a negative electrode for an alkaline battery.
【請求項2】前記フルオロカーボンの添加量は前記ゲル
化剤に対して1.0重量%以下である請求項1記載のアル
カリ電池用負極の製造方法。
2. The method according to claim 1, wherein the amount of the fluorocarbon added is 1.0% by weight or less based on the gelling agent.
JP63259501A 1988-10-17 1988-10-17 Method for producing negative electrode for alkaline battery Expired - Fee Related JP2832018B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63259501A JP2832018B2 (en) 1988-10-17 1988-10-17 Method for producing negative electrode for alkaline battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63259501A JP2832018B2 (en) 1988-10-17 1988-10-17 Method for producing negative electrode for alkaline battery

Publications (2)

Publication Number Publication Date
JPH02106872A JPH02106872A (en) 1990-04-18
JP2832018B2 true JP2832018B2 (en) 1998-12-02

Family

ID=17334975

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63259501A Expired - Fee Related JP2832018B2 (en) 1988-10-17 1988-10-17 Method for producing negative electrode for alkaline battery

Country Status (1)

Country Link
JP (1) JP2832018B2 (en)

Also Published As

Publication number Publication date
JPH02106872A (en) 1990-04-18

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