JPH0752644B2 - Method for manufacturing negative electrode zinc plate for dry battery - Google Patents
Method for manufacturing negative electrode zinc plate for dry batteryInfo
- Publication number
- JPH0752644B2 JPH0752644B2 JP60121852A JP12185285A JPH0752644B2 JP H0752644 B2 JPH0752644 B2 JP H0752644B2 JP 60121852 A JP60121852 A JP 60121852A JP 12185285 A JP12185285 A JP 12185285A JP H0752644 B2 JPH0752644 B2 JP H0752644B2
- Authority
- JP
- Japan
- Prior art keywords
- zinc plate
- mol
- dry battery
- copolymer
- negative electrode
- 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 - Lifetime
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M6/00—Primary cells; Manufacture thereof
- H01M6/04—Cells with aqueous electrolyte
- H01M6/06—Dry cells, i.e. cells wherein the electrolyte is rendered non-fluid
- H01M6/08—Dry cells, i.e. cells wherein the electrolyte is rendered non-fluid with cup-shaped electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/46—Separators, membranes or diaphragms characterised by their combination with electrodes
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- 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、乾電池の負極に用いられる亜鉛板を製造する
方法に関する。TECHNICAL FIELD The present invention relates to a method for producing a zinc plate used for a negative electrode of a dry battery.
[従来の技術] 乾電池の負極としている亜鉛板は通常アマルガム化する
ことにより均質化され局部電流の発生の防止や放電によ
る均一溶解が促進されている。[Prior Art] A zinc plate used as a negative electrode of a dry battery is generally homogenized by forming an amalgam to prevent generation of a local current and promote uniform dissolution by discharging.
[発明が解決しようとする問題点] しかしながら、かなりの量の水銀が用いられていること
は廃電池の処理に当って公害防止のために多大の労力と
経費が必要とされることから、かかるアマルガム化を特
に処こさなくても実用に充分耐え得る乾電池用の亜鉛板
が製造出来れば、その産業上の意義は極めて大きいもの
である。[Problems to be Solved by the Invention] However, the fact that a considerable amount of mercury is used requires a great deal of labor and cost to prevent pollution when treating a waste battery. If a zinc plate for a dry battery that can withstand practical use without particularly undergoing amalgamation can be manufactured, its industrial significance will be extremely great.
[問題点を解決するための手段] 本発明者はかかる問題点を改善するため鋭意研究を重ね
た結果、酢酸ビニル50〜99.8モル%、不飽和ジカルボン
酸50〜0.2モル%の割合の共重合体であり、かつその酢
酸ビニル成分の70モル%以上がケン化された共重合体ケ
ン化物の層を亜鉛板表面に設ける場合、その目的が達成
出来ることを見出し、本発明を完成するに到った。[Means for Solving Problems] The inventors of the present invention have conducted extensive studies to improve such problems, and as a result, vinyl acetate 50 to 99.8 mol% and unsaturated dicarboxylic acid 50 to 0.2 mol% It was found that the object can be achieved when a layer of a saponified copolymer in which 70 mol% or more of its vinyl acetate component is saponified is provided on the surface of a zinc plate, and the present invention has been completed. It was.
該共重合体ケン化物の層は負極と合剤との物理的接触を
防止出来るだけの充分な強度をもち、更に保水性、イオ
ン透過性に優れ、pHが酸性サイドでも安定し、亜鉛層と
共重合体ケン化物層との密着が強固であって、層間部に
気泡等の異物を全く含む恐れがない等の特性を有するた
めにアマルガム化の省略という前記顕著な効果が得られ
るのである。The layer of the saponified copolymer has sufficient strength to prevent physical contact between the negative electrode and the mixture, and further has excellent water retention and ion permeability, stable pH even on the acidic side, and a zinc layer. Since the adhesiveness to the saponified copolymer layer is strong and there is no possibility that foreign matters such as bubbles are contained in the interlayer portion, the above-mentioned remarkable effect of omitting amalgamation can be obtained.
従来、合剤と負極の接触を防止するために各種のプラス
チックフィルムをセパレーターとして用いることが提案
されているが、従来品では前記した如き特性を有してい
ないため、フィルムと亜鉛板との密着が不充分で、気泡
の混入等が発生し、電池の寿命を縮める恐れがあり、本
発明の如き効果は全く得られない。Conventionally, it has been proposed to use various plastic films as a separator in order to prevent contact between the mixture and the negative electrode, but since the conventional product does not have the above-mentioned characteristics, the adhesion between the film and the zinc plate Is insufficient, bubbles may be mixed in, and the battery life may be shortened, and the effects of the present invention cannot be obtained.
本発明で用いる共重合体ケン化物は上記した如く酢酸ビ
ニルが50〜99.8モル%、不飽和ジカルボン酸50〜0.2モ
ル%の割合で共重合されており、かつその酢酸ビニル成
分の70モル%以上がケン化されていることが必要であ
る。As described above, the saponified copolymer used in the present invention contains 50 to 99.8 mol% of vinyl acetate and 50 to 0.2 mol% of unsaturated dicarboxylic acid as a copolymer, and 70 mol% or more of the vinyl acetate component. Must be saponified.
かかる範囲外では本発明の効果は得られない。The effect of the present invention cannot be obtained outside this range.
これらの条件の中でもさらに好ましくは酢酸ビニル80〜
99.8モル%、不飽和ジカルボン酸20〜0.2モル%、ケン
化度70モル%以上の範囲の共重合体ケン化物が一段と優
れた性能を有する。Among these conditions, vinyl acetate 80-
A saponified copolymer having a content of 99.8 mol%, an unsaturated dicarboxylic acid of 20 to 0.2 mol% and a saponification degree of 70 mol% or more has further excellent performance.
不飽和ジカルボン酸としては、(無水)マレイン酸、フ
マール酸、イタコン酸、グルタコン酸、アリルマロン酸
などおよびメチル、エチル、プロピルエステルなどのモ
ノエステル類、ジエステル類などが挙げられる。Examples of unsaturated dicarboxylic acids include (anhydrous) maleic acid, fumaric acid, itaconic acid, glutaconic acid, allylmalonic acid and the like, and monoesters and diesters such as methyl, ethyl and propyl esters.
さらに少量であれば他の共重合可能な単量体を共重合さ
せても差し支えない。かかる共重合体ケン化物は、酢酸
ビニルと不飽和ジカルボン酸とを前記比率の共重合体と
なるように通常の溶液重合を行い、得られた共重合体を
苛性ソーダ、ナトリウムメチラートなどのアルカリ触媒
を用いて所定の割合にケン化することによって製造され
る。Further, if it is a small amount, another copolymerizable monomer may be copolymerized. Such a saponified copolymer is a solution of vinyl acetate and an unsaturated dicarboxylic acid which are subjected to ordinary solution polymerization so as to form a copolymer having the above ratio, and the resulting copolymer is then subjected to an alkali catalyst such as caustic soda or sodium methylate. It is produced by saponifying to a predetermined ratio with.
共重合体ケン化物の層を亜鉛板表面に成形させるには、
共重合体ケン化物の水溶液、有機溶剤溶液、水−有機溶
剤混合液を亜鉛板上に流涎するのが普通である。勿論、
かる手段のみに限らず、一旦共重合体ケン化物のフィル
ムを作成し、これを亜鉛板上にラミネートする等の方法
も任意に実施可能である。To form a layer of saponified copolymer on the surface of a zinc plate,
It is common to sprinkle an aqueous solution of saponified copolymer, an organic solvent solution, or a water-organic solvent mixture on a zinc plate. Of course,
The method is not limited to such a method, and a method such as once forming a saponified film of a copolymer and laminating the film on a zinc plate can also be arbitrarily performed.
亜鉛板等は平板に限らず、缶状に成型されたものであっ
ても差し支えない。缶状の場合、この中に共重合体ケン
化物の溶液を供給し、続いてそれを除去することによっ
て壁面に共重合体ケン化物の層を成形させることも出来
る。The zinc plate or the like is not limited to a flat plate, and may be formed in a can shape. In the case of a can, it is also possible to form a saponified copolymer layer on the wall surface by supplying a solution of the saponified copolymer and then removing it.
形成された共重合体ケン化物の層は続いて乾燥される。
乾燥温度は40〜90℃程度、乾燥時間は5〜120分が適当
である。The saponified copolymer layer formed is subsequently dried.
It is suitable that the drying temperature is about 40 to 90 ° C and the drying time is 5 to 120 minutes.
かかる共重合体ケン化物層はさらに加熱処理をすること
によって一段と優れた性能が付与される。一般に空気ま
たは不活性ガス雰囲気下温度110〜200℃で1〜360分加
熱処理する。層の厚みは5〜100μ程度が適当であり、
1回の塗工操作、ラミネート操作で均一な膜が得難い時
は二回以上の塗工操作、ラミネート操作を行ってよい。By further heat-treating such a saponified copolymer layer, more excellent performance is imparted. Generally, heat treatment is performed at a temperature of 110 to 200 ° C. for 1 to 360 minutes in an air or inert gas atmosphere. A layer thickness of 5 to 100μ is appropriate,
When it is difficult to obtain a uniform film by one coating operation or laminating operation, two or more coating operations or laminating operations may be performed.
かくして製造された亜鉛板を用いて乾電池を製造するに
は、従来公知の手段が任意に実施される。In order to manufacture a dry battery using the zinc plate thus manufactured, any conventionally known means may be optionally carried out.
即ち、例えば共重合体ケン化物を設けた亜鉛缶に塩化亜
鉛、塩化アンモン、水等から構成される電解液で充分湿
潤した二酸化マンガンとアセチレンブラックからなる減
極合剤を充填し、更にこの減極合剤の中心に集電体とし
ての炭素棒を挿入し、亜鉛缶の開口部を封口する等の任
意の方法が実施出来る。That is, for example, a zinc can provided with a saponified copolymer is filled with a depolarizing agent composed of manganese dioxide and acetylene black sufficiently moistened with an electrolytic solution composed of zinc chloride, ammonium chloride, water, etc. Any method such as inserting a carbon rod as a current collector into the center of the electrode mixture and sealing the opening of the zinc can can be carried out.
[作用] 本発明においては、特定の酢酸ビニル−不飽和ジカルボ
ン酸共重合体ケン化物の層を設けた亜鉛板を用いること
によって、公害の恐れのない、かつ実用的寿命をもつ乾
電池が容易に製造出来る。[Operation] In the present invention, by using a zinc plate provided with a layer of a specific saponified product of vinyl acetate-unsaturated dicarboxylic acid copolymer, a dry battery without fear of pollution and having a practical life can be easily formed. Can be manufactured.
[実施例] 実例を挙げて本発明の方法を具体的に説明する。[Examples] The method of the present invention will be specifically described with reference to examples.
実例1 酢酸ビニル含量96.1モル%、マレイン酸モノメチル含量
3.9モル%、酢酸ビニル成分のケン化度98.1モル%のマ
レイン酸モノメチル−酢酸ビニル共重合体ケン化物粉末
(295μ以下)を水に溶解し、10重量%水溶液を調整し
た。この溶液を単3型亜鉛缶1の内壁に一様に塗布して
75℃で1時間乾燥した。Example 1 Vinyl acetate content 96.1 mol%, monomethyl maleate content
A saponified powder of monomethyl maleate-vinyl acetate copolymer having a saponification degree of 3.9 mol% and a vinyl acetate component of 98.1 mol% (295 μm or less) was dissolved in water to prepare a 10 wt% aqueous solution. Apply this solution evenly on the inner wall of AA zinc can 1.
It was dried at 75 ° C for 1 hour.
この操作を2回繰り返し平均膜厚31μの共重合体ケン化
物層を形成させた。続いて140℃で3時間熱処理を行っ
た。This operation was repeated twice to form a saponified copolymer layer having an average film thickness of 31μ. Then, heat treatment was performed at 140 ° C. for 3 hours.
この層を形成させた亜鉛缶に塩化亜鉛5部、塩化アンモ
ン25部、水70部からなる電解液で充分湿潤した二酸化マ
ンガン80部、アセチレンブラック20部の組成の減極合剤
を充填した。更にこの減極合剤の中心に集電体としての
炭素棒を挿入し、亜鉛缶の開口部をミクロクリスタリン
ワックスで封口し、電池を完成した。The zinc can in which this layer was formed was filled with a depolarizing agent having a composition of 5 parts of zinc chloride, 25 parts of ammonium chloride, 80 parts of manganese dioxide sufficiently moistened with an electrolytic solution consisting of 70 parts of water, and 20 parts of acetylene black. Furthermore, a carbon rod as a current collector was inserted into the center of this depolarizing mixture, and the opening of the zinc can was sealed with microcrystalline wax to complete the battery.
この様にして得られた単3型電池の製造直後及び45℃保
存後の10Ω連続放電の放電容量を従来型乾電池の製造直
後の放電容量を100として指数表示にて示すと製造直後
が130、2ケ月後110、3ケ月後100であり、優れた性能
であることが判った。The discharge capacity of 10 Ω continuous discharge immediately after the production of the thus obtained AA battery and after storage at 45 ° C. is shown as an index with the discharge capacity immediately after the production of the conventional dry battery as 100, and the discharge capacity immediately after the production is 130, It was 110 after two months and 100 after three months, which proved to be excellent performance.
実例2〜4 マレイン酸モノメチルの含量を8モル%に変更した以外
は実例1と同じ方法を行った。(実例2) 熱処理条件を180℃,0.25時間に変更した以外は実例1と
同じ実験を行った。(実例3) マレイン酸モノメチルに代えてイタコン酸を用いた以外
は実例1と同様の実験を行った。(実例4) いずれの場合も実例1と同じ結果が得られた。Examples 2 to 4 The same method as in Example 1 was performed except that the content of monomethyl maleate was changed to 8 mol%. (Example 2) The same experiment as in Example 1 was performed except that the heat treatment condition was changed to 180 ° C for 0.25 hours. Example 3 The same experiment as in Example 1 was conducted except that itaconic acid was used instead of monomethyl maleate. (Example 4) In all cases, the same result as Example 1 was obtained.
比較例1 マレイン酸モノメチル−酢酸ビニル共重合体ケン化物に
かえてケン化度98.1モル%のポリビニルアルコールを用
いた以外は実例1と同様の実験を行った結果、放電容量
指数として製造直後が128、2ケ月後98、3ケ月後85と
いう結果が得られた。Comparative Example 1 The same experiment as in Example 1 was carried out except that a saponified product of a monomethyl maleic acid-vinyl acetate copolymer was replaced with a polyvinyl alcohol having a saponification degree of 98.1 mol%. The results were 98 after 2 months and 85 after 3 months.
第1図は本発明の方法で得られる亜鉛板を用いて製造し
た乾電池の断面図である。 1は亜鉛缶 2は共重合体ケン化物層 3は減極合剤 4は炭素棒 5はミクロクリスタリンワックス をそれぞれ示す。FIG. 1 is a sectional view of a dry battery manufactured using a zinc plate obtained by the method of the present invention. 1 is a zinc can 2 is a saponified copolymer layer 3 is a depolarizing agent 4 is a carbon rod 5 is a microcrystalline wax.
Claims (1)
ボン酸50〜0.2モル%の割合の共重合体であり、かつそ
の酢酸ビニル成分の70モル%以上がケン化された共重合
体ケン化物の層を亜鉛板表面に設け、温度110〜200℃で
1〜360分加熱処理することを特徴とする乾電池用負極
亜鉛板の製造方法。1. A copolymer ken which is a copolymer having a proportion of vinyl acetate of 50 to 99.8 mol% and an unsaturated dicarboxylic acid of 50 to 0.2 mol% and in which 70 mol% or more of the vinyl acetate component is saponified. A method for producing a negative electrode zinc plate for a dry battery, comprising providing a compound layer on the surface of a zinc plate and performing heat treatment at a temperature of 110 to 200 ° C for 1 to 360 minutes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60121852A JPH0752644B2 (en) | 1985-06-05 | 1985-06-05 | Method for manufacturing negative electrode zinc plate for dry battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60121852A JPH0752644B2 (en) | 1985-06-05 | 1985-06-05 | Method for manufacturing negative electrode zinc plate for dry battery |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61281459A JPS61281459A (en) | 1986-12-11 |
JPH0752644B2 true JPH0752644B2 (en) | 1995-06-05 |
Family
ID=14821523
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60121852A Expired - Lifetime JPH0752644B2 (en) | 1985-06-05 | 1985-06-05 | Method for manufacturing negative electrode zinc plate for dry battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0752644B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2000059052A2 (en) * | 1999-03-29 | 2000-10-05 | The Gillette Company | Alkaline cell separator |
CN118176600A (en) * | 2021-11-01 | 2024-06-11 | 株式会社可乐丽 | Binder for electricity storage device, binder solution for electricity storage device, electricity storage device electrode slurry, electricity storage device electrode, and electricity storage device |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS518168A (en) * | 1974-07-12 | 1976-01-22 | Hitachi Chemical Co Ltd |
-
1985
- 1985-06-05 JP JP60121852A patent/JPH0752644B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS61281459A (en) | 1986-12-11 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |