JPS63237366A - Manufacturing method of alkaline zinc storage battery - Google Patents

Manufacturing method of alkaline zinc storage battery

Info

Publication number
JPS63237366A
JPS63237366A JP62071027A JP7102787A JPS63237366A JP S63237366 A JPS63237366 A JP S63237366A JP 62071027 A JP62071027 A JP 62071027A JP 7102787 A JP7102787 A JP 7102787A JP S63237366 A JPS63237366 A JP S63237366A
Authority
JP
Japan
Prior art keywords
battery
electrolyte
zinc
storage battery
manufacturing
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.)
Granted
Application number
JP62071027A
Other languages
Japanese (ja)
Other versions
JPH0740491B2 (en
Inventor
Sanehiro Furukawa
古川 修弘
Kenji Inoue
健次 井上
Mitsuzo Nogami
光造 野上
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.)
Sanyo Electric Co Ltd
Original Assignee
Sanyo Electric 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 Sanyo Electric Co Ltd filed Critical Sanyo Electric Co Ltd
Priority to JP62071027A priority Critical patent/JPH0740491B2/en
Publication of JPS63237366A publication Critical patent/JPS63237366A/en
Publication of JPH0740491B2 publication Critical patent/JPH0740491B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/24Alkaline accumulators
    • H01M10/28Construction or manufacture
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Secondary Cells (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 に)産業上の利用分野 本発明はニッケルー亜鉛蓄電池、銀−亜鉛蓄電池などの
ように負極活物質として亜鉛を用いるアルカリ亜鉛蓄電
池の製造方法に関するものである。
D) Industrial Field of Application The present invention relates to a method for producing an alkaline zinc storage battery using zinc as a negative electrode active material, such as a nickel-zinc storage battery or a silver-zinc storage battery.

(ロ) 従来の技術 負極活物質に亜鉛を用いたアルカリM電池はエネルギー
゛d度が高く、高い作動電圧含有し、経済性に優れてい
るなどの利点含有するが、サイクル寿命が短いという欠
点がある。この原因は放電時に亜鉛がアルカリ電解液中
に亜鉛酸イオンとして溶出し、充電時にこの亜鉛酸イオ
ンが亜鉛負極表面に樹枝状に金属亜鉛として電析するた
め、充放11−繰り返すとこの樹枝状亜鉛が生長しセパ
レータを貫通して、正極と接し内部短絡を引き起すこと
に起因する。
(b) Conventional technologyAlkaline M batteries using zinc as the negative electrode active material have advantages such as high energy density, high operating voltage, and excellent economic efficiency, but have the disadvantage of short cycle life. There is. The reason for this is that during discharge, zinc is eluted into the alkaline electrolyte as zincate ions, and during charging, these zincate ions are deposited as metal zinc in a dendritic form on the surface of the zinc negative electrode. This is due to zinc growing and penetrating the separator and coming into contact with the positive electrode, causing an internal short circuit.

この樹枝状亜鉛の生長を抑制するため種々のセパレータ
材が検討されて−るが、セパレータが1枚よりなるもの
におiては抑制効果が十分でないので、セパレータを数
枚、数種類よりなるものより構成することが柚々提案さ
れてiる。
Various separator materials have been studied to suppress the growth of this dendritic zinc, but those made of one separator do not have a sufficient suppressive effect, so those made of several separators or several types have been studied. There have been many proposals to make the system more structured.

たとえば特開昭57−197757号公報には、遊離の
電解液を制限し、亜鉛負極に接するセパレータの含有す
る電解液量が、正極に接するセパレータの電解液量よシ
小となるように構成することが開示されている。この方
法によれは、亜鉛酸イオンの逸散が抑制され、樹枝状亜
鉛生長による正極との内部短絡を低減すると共に亜鉛負
極の変形を緩和しうる。
For example, Japanese Patent Application Laid-Open No. 57-197757 discloses that the amount of free electrolyte is limited so that the amount of electrolyte contained in the separator in contact with the zinc negative electrode is smaller than the amount of electrolyte in the separator in contact with the positive electrode. This is disclosed. This method can suppress the escape of zincate ions, reduce internal short circuits with the positive electrode due to dendritic zinc growth, and alleviate deformation of the zinc negative electrode.

(ハ)発明が解決しようとする問題点 しかしながら、特開昭57−197757号公報などに
記載された発明に用いられる多層セパレータを用い、か
つ電解液量を制限すると、正、負極間に電解液が均一に
分布しにくくなる。そして電解液が不均一に分布してφ
ると、充放電時に正、負極間の電流分布が不均一になシ
、充放電サイクルが進行するに従い、亜鉛負極の形状変
形が著しくなったQ、多層セパレータの一部が圧迫され
て部分的なドライアウトが生じる。その結果、形状変形
及び樹枝状亜鉛の生長が加速されて、急速に電池容量が
低下する。また、電池のサイクル寿命のバラツキも大き
くなり、安定した電池性能が得にくい。
(c) Problems to be solved by the invention However, if the multilayer separator used in the invention described in JP-A-57-197757 and the like is used and the amount of electrolyte is limited, the electrolyte will not be present between the positive and negative electrodes. becomes difficult to distribute uniformly. Then, the electrolyte is distributed unevenly and φ
As a result, the current distribution between the positive and negative electrodes becomes uneven during charging and discharging, and as the charging and discharging cycles progress, the shape of the zinc negative electrode becomes noticeably deformed. Dryout occurs. As a result, shape deformation and growth of dendritic zinc are accelerated, resulting in a rapid decrease in battery capacity. Furthermore, variations in battery cycle life also increase, making it difficult to obtain stable battery performance.

に)問題点を解決するための手段 本発明のアルカリ亜鉛蓄電池の製造方法は、正、負極間
に介在する多層セパレータに水を含浸させ念状態で、前
記正、負極及び多層セパレータよシなる電極体を構成し
、電槽に前dピ電極体金挿入した後、電解液の注液を行
うことを特徴とするものである。
B) Means for Solving the Problems The method for producing an alkaline zinc storage battery of the present invention involves impregnating a multilayer separator interposed between the positive and negative electrodes with water, and then removing the electrodes formed by the positive and negative electrodes and the multilayer separator in a predetermined state. After constructing the body and inserting the front d-pi electrode body into the battery case, the electrolyte is injected.

(ホ)作 用 あらかじめ多層セパレータを水でぬらしておいて、正、
負極及び多層セパレータよりなる電極体を構成しその後
電解液の注液を行なうと、電解液と水の接したところか
ら電解液中に溶解していた電解質が徐々に拡散していく
。電解液注液の直後には、多層セパレータの注液された
電解液と接した部分と、それ以外の部分で電解質の濃度
勾配が大きく生じて鱒るが、充分時間が経てば、この濃
度勾配は解消されて均一な濃度分布になるものと考えら
れる。この結果、あらかじめ水でぬらしておいた多層セ
パレータの部分は、充分な電解液を含液した状態となる
。このため、電極間における電解液の不均一分布が抑制
される。このように多層セパレータに水を含浸させた状
態に保っておかないと電解液自身の粘性が大きく、また
その注入量も制限しているために、電極間において電解
液が均一に分布しにくくなる。
(E) Function: Wet the multilayer separator with water beforehand, and
When an electrode body consisting of a negative electrode and a multilayer separator is constructed and then an electrolyte is injected, the electrolyte dissolved in the electrolyte gradually diffuses from the point where the electrolyte and water come into contact. Immediately after the electrolyte is injected, a large electrolyte concentration gradient occurs between the part of the multilayer separator that is in contact with the injected electrolyte and the other parts, and this concentration gradient disappears after enough time has passed. It is thought that this will be resolved and a uniform concentration distribution will result. As a result, the portion of the multilayer separator that has been pre-wetted with water becomes fully impregnated with electrolyte. Therefore, non-uniform distribution of the electrolyte between the electrodes is suppressed. If the multilayer separator is not kept impregnated with water, the viscosity of the electrolyte itself is high, and the amount of injection is limited, making it difficult to distribute the electrolyte uniformly between the electrodes. .

(へ)実施例 活物質として酸化亜鉛粉末85重量%及び、金属亜鉛粉
末10重量%、水素過電圧を上げるための酸化カドミウ
ム粉末5重f%t−加えてなる混合粉末に、水とポリテ
トラフルオロエチレンディスパージョンとを添加、混練
し、活物質ペーストを得た。この活物質ペーストをニッ
ケルメツシュよシなる導電芯体の両面に圧着して亜鉛負
極を得た。
(f) Example Active materials: 85% by weight of zinc oxide powder, 10% by weight of metallic zinc powder, and 5% by weight of cadmium oxide powder for increasing the hydrogen overvoltage were added to a mixed powder with water and polytetrafluorocarbon powder. Ethylene dispersion was added and kneaded to obtain an active material paste. This active material paste was pressed onto both sides of a conductive core made of nickel mesh to obtain a zinc negative electrode.

一方、ポリプロピレン製の微孔性フィルム(25μ)2
枚と、保液性が高いナイロン製の不織布(120μ)1
枚から構成された多層セパレータを、純水中に浸漬し余
分な水分全除去した後、前記亜鉛負極と、公知の焼結式
ニッケル正極とを組み曾せて、渦巻電極体t−構成し、
電槽である電池缶に前記電極体全挿入した。ここに、酸
化亜鉛を飽和させた36重量%KOH水溶液を注液し、
封口全行い、密閉し、公称容!2000mAHの電池を
得た。ここで、電解液であるKOH水溶液は多層セパレ
ータに水が含浸させであるので、通常、用いられる電解
液よりも少し濃度金高くしである。
On the other hand, polypropylene microporous film (25 μ) 2
1 piece of nylon non-woven fabric (120μ) with high liquid retention properties
After immersing a multilayer separator composed of a single sheet in pure water to remove all excess moisture, the zinc negative electrode and a known sintered nickel positive electrode are combined to form a spiral electrode body T-structure,
The entire electrode assembly was inserted into a battery case, which is a battery case. A 36% by weight KOH aqueous solution saturated with zinc oxide was poured into this,
Completely sealed, sealed, nominal capacity! A 2000 mAh battery was obtained. Here, since the KOH aqueous solution used as the electrolytic solution is a multilayer separator impregnated with water, it has a slightly higher gold concentration than the electrolytic solution normally used.

そしてこの電池を、本発明電池Aとした。This battery was designated as Invention Battery A.

比較例として、多層セパレータに水を含浸させず、酸化
亜鉛を飽和させた30重量%KOH水溶液を注液した以
外は電池Aと同一である、比較電池B1F!:得た。尚
、本発明電池Aと比較電池Bにおいて、各電池内におけ
る電解液濃度、電解液tは同一である。
As a comparative example, comparative battery B1F is the same as battery A except that the multilayer separator was not impregnated with water and a 30% by weight KOH aqueous solution saturated with zinc oxide was injected. :Obtained. Note that in the present invention battery A and the comparative battery B, the electrolyte concentration and the electrolyte t in each battery are the same.

これらの本発明電池A、比4[!2電池B全用いて4時
間率の電流で5時間充電した後に、1時間率の電流で電
池電圧がt3Vになるまで放電するという条件にて充放
電サイクル試験全行い、サイクル特性を比較した。ここ
で、放電時においてt3Vの電池電圧を42分間維持で
きなくなった時点、つまり電池放電容量が公称容量の7
0%以下となったところを電池のサイクル寿命とした。
These invention batteries A, ratio 4 [! A charge/discharge cycle test was performed under the condition that all two batteries B were charged at a current rate of 4 hours for 5 hours and then discharged at a current rate of 1 hour until the battery voltage reached t3V, and the cycle characteristics were compared. Here, when the battery voltage of t3V cannot be maintained for 42 minutes during discharging, that is, the battery discharge capacity is 7V of the nominal capacity.
The cycle life of the battery was defined as the point where it became 0% or less.

この結果を、図に示す。これ、CD本発明電池八へ比較
電池Bに比して、サイクル特性に優れ、またサイクル特
性のばらつきも小さいことが理解される。したがって、
本発明製造方法により得た電池Aは、サイクル寿命が長
く、品質の安定したものとなることが理解された。
The results are shown in the figure. It is understood that this CD battery according to the present invention has excellent cycle characteristics as compared to comparative battery B, and the variation in cycle characteristics is also small. therefore,
It was understood that the battery A obtained by the manufacturing method of the present invention has a long cycle life and stable quality.

更に、実施例において多層セパレータにろらかじめ含浸
させておくものが、通常用いられる従来の電解液よりも
腐食性の低いもの全使用しているので、電池の製造機器
を損傷させるという心配はない。つまり、本発明に用い
られる9水“とじては、腐食の程度が極めて低い低e4
反の電解液などtも用いることが可能でらる。
Furthermore, in the examples, the multilayer separator is pre-impregnated with a solution that is less corrosive than the conventional electrolyte that is commonly used, so there is no need to worry about damaging the battery manufacturing equipment. do not have. In other words, the 9-water used in the present invention is a low-e4, which has an extremely low degree of corrosion.
It is also possible to use a reverse electrolyte.

(ト)発明の効果 本発明の製造方法によれば1品質の安定したサイクル特
性に潰れるアルカリ亜鉛&IA池が得られるので、その
工業的価値はきわめて大きい。
(G) Effects of the Invention According to the production method of the present invention, an alkaline zinc & IA pond with stable cycle characteristics of one quality can be obtained, so its industrial value is extremely large.

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

図は、電池のサイクル特性比較図である。 A・・・本発明電池、 B・・・比較電池。 The figure is a comparison diagram of cycle characteristics of batteries. A: Battery of the present invention, B: Comparative battery.

Claims (1)

【特許請求の範囲】[Claims] (1)正、負極間に介在する多層セパレータに水を含浸
させた状態で、前記正、負極及び多層セパレータよりな
る電極体を構成し、電槽に前記電極体を挿入した後、電
解液の注液を行うことを特徴とするアルカリ亜鉛蓄電池
の製造方法。
(1) After impregnating the multilayer separator interposed between the positive and negative electrodes with water, construct an electrode body consisting of the positive and negative electrodes and the multilayer separator, and insert the electrode body into a battery container. A method for manufacturing an alkaline zinc storage battery, characterized by performing liquid injection.
JP62071027A 1987-03-25 1987-03-25 Method of manufacturing alkaline zinc storage battery Expired - Lifetime JPH0740491B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62071027A JPH0740491B2 (en) 1987-03-25 1987-03-25 Method of manufacturing alkaline zinc storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62071027A JPH0740491B2 (en) 1987-03-25 1987-03-25 Method of manufacturing alkaline zinc storage battery

Publications (2)

Publication Number Publication Date
JPS63237366A true JPS63237366A (en) 1988-10-03
JPH0740491B2 JPH0740491B2 (en) 1995-05-01

Family

ID=13448631

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62071027A Expired - Lifetime JPH0740491B2 (en) 1987-03-25 1987-03-25 Method of manufacturing alkaline zinc storage battery

Country Status (1)

Country Link
JP (1) JPH0740491B2 (en)

Also Published As

Publication number Publication date
JPH0740491B2 (en) 1995-05-01

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