JPH01294369A - Sealed clad type lead battery - Google Patents

Sealed clad type lead battery

Info

Publication number
JPH01294369A
JPH01294369A JP63124662A JP12466288A JPH01294369A JP H01294369 A JPH01294369 A JP H01294369A JP 63124662 A JP63124662 A JP 63124662A JP 12466288 A JP12466288 A JP 12466288A JP H01294369 A JPH01294369 A JP H01294369A
Authority
JP
Japan
Prior art keywords
separator
electrode plate
battery
electrolyte
electrolytic cell
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
JP63124662A
Other languages
Japanese (ja)
Inventor
Masaaki Shiomi
塩見 正昭
Katsuto Takahashi
克仁 高橋
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.)
Japan Storage Battery Co Ltd
Original Assignee
Japan Storage Battery 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 Japan Storage Battery Co Ltd filed Critical Japan Storage Battery Co Ltd
Priority to JP63124662A priority Critical patent/JPH01294369A/en
Publication of JPH01294369A publication Critical patent/JPH01294369A/en
Pending 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
    • H01M10/06Lead-acid accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/34Gastight accumulators
    • H01M10/342Gastight lead accumulators
    • 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

Abstract

PURPOSE:To obtain a sealed clad type lead battery with excellent discharging capacity and cycle lifetime by installing a group of electrode plates composed of specified separators, positive and negative plates into an electrolytic cell with pressure more than a specified value under the state of being dry before putting electrolyte into the electrolytic cell. CONSTITUTION:Glass fiber formed into sheet with uniform fiber diameter of less than 10mum is used for a separator 3 and gelled dilute sulfuric acid for electrolyte. A group of electrode plates composed of separators, positive and negative plates 2 with pressure more than 20kg/dm<2> per apparent surface are (longitudinal and transverse dimensions of a plate) of the positive plate is accommodated in an electrolytic cell under the state of being dry before putting electrolyte into the electrolytic cell. The glass separator 3 extremely increase its surface contacting with the positive plate 1 by strong pressing and has the construction in which the separator easily absorbs H2SO4 formed at charging. Thus, the gap of the clad type positive plate and the separator becomes about half compared with a conventional battery not being pressed. Therefore, discharging capacity and cycle lifetime are extremely improved.

Description

【発明の詳細な説明】 産業上の利用分野 本発明はクラッド式正極板を用いた密閉形鉛電池に関す
るもので、特に放電容量およびサイクル寿命性能に優れ
た密閉形鉛電池を提供することを目自勺とするものであ
る。
[Detailed Description of the Invention] Industrial Application Field The present invention relates to a sealed lead-acid battery using a clad positive electrode plate, and particularly aims to provide a sealed lead-acid battery with excellent discharge capacity and cycle life performance. It is something to be done on your own.

従来の技術 一般に正極板にクラッド式極板を用いた電池は正極活物
質をチューブで包み、圧迫しているため、充放電を繰り
返しても活物質の脱落がなく、ペースト式極板を用いた
電池に比べ寿命性能がすぐれていることが知られている
。従来このクラッド式鉛電池を密閉化する場合、以下の
3つの方法A。
Conventional technology In general, batteries that use a clad type positive electrode plate wrap the positive electrode active material in a tube and compress it, so the active material does not fall off even after repeated charging and discharging. It is known that they have a superior lifespan compared to batteries. Conventionally, when sealing this clad lead-acid battery, there are three methods A:

B、Cが行われてきた。B and C have been carried out.

1つ目Aは平均繊維径が10μm以上のガラス繊維や、
パルプ、合成樹脂などの非吸液性のセパレータを用いた
電池にSi O2やAl2O3などの無殿酸化物を含む
ゾル状希硫酸を注探し、電池内でゲル化させて密閉化す
る方法。2つ目Bは繊維径がもっと細い吸液性のガラス
@維セパレータを極板群内でほとんど圧迫しない状態で
使用した電池に、上記方法と同様にゾル状希硫酸を注液
して電池内でゲル化させる方法。3つ目Cは2つ目と同
じく吸液性のセパレータを極板群内で圧迫して使用し、
このセパレータと極板群内だけに希VA酸を含浸させた
いわゆるリテーナクラッド式電池である。
The first type A is glass fiber with an average fiber diameter of 10 μm or more,
A method in which a sol-like dilute sulfuric acid containing non-precipitating oxides such as SiO2 and Al2O3 is added to a battery using a non-liquid-absorbing separator such as pulp or synthetic resin, and the battery is gelled and sealed inside the battery. The second method B is to use a liquid-absorbing glass@fiber separator with a thinner fiber diameter in a state where it is hardly compressed within the electrode plate group, and inject sol-form dilute sulfuric acid into the battery using the same method as above. How to make it gel. The third C, like the second one, uses a liquid-absorbing separator compressed within the electrode group,
This is a so-called retainer clad type battery in which only the separator and the electrode plate group are impregnated with dilute VA acid.

発明が解決しようとする課題 Aの方法による電池ではセパレータが吸液性に乏しいた
め、充放電を繰り返すような使い方をすると、充電時に
正極板で生成しなH2SO,がゲル電解液のボアを通じ
て容易に電池下部に蓄積して、電池の上下部でのH2S
O4濃度に大きな差が生じるいわゆる電解液の成層化現
象を生じる。その結果、極板下部にpbso、が多量に
蓄積し、電池性能が著しく劣化する欠点を有していた。
Problem to be Solved by the Invention In the battery according to method A, the separator has poor liquid absorption properties, so if the battery is repeatedly charged and discharged, H2SO, which is generated on the positive electrode plate during charging, easily passes through the bore of the gel electrolyte. H2S accumulates at the bottom of the battery and
This causes a so-called electrolyte stratification phenomenon in which a large difference in O4 concentration occurs. As a result, a large amount of PBSO accumulates at the bottom of the electrode plate, resulting in a disadvantage that the battery performance is significantly degraded.

Bの方式による電池では、セパレータが吸液性であるの
で上記欠点による電池の劣化程度は小さくすることがで
きる。しかし、この電池において、極板群は第2図の横
断面図に示すごとくほとんど圧迫をかけないで構成して
いるため、クラッド式正極板とセパレータとの間に大き
な隙間が生じる。
In the battery according to method B, since the separator is liquid-absorbing, the degree of deterioration of the battery due to the above-mentioned drawbacks can be reduced. However, in this battery, since the electrode plate group is constructed with almost no pressure applied as shown in the cross-sectional view of FIG. 2, a large gap is created between the clad type positive electrode plate and the separator.

この部分はゲル状電解液が充填されているので放電容量
にはそれほど影響しないが、深い放電を行って電解液比
重が低下するとゲル電解液が著しく軟化するため、この
ときに生成したH2Oが容易に上部に進み、いわゆる電
解液の成層化現象を生じ、電池が劣化する。これはAの
方法でも同様の現象が生じる。
Since this part is filled with gel electrolyte, it does not affect the discharge capacity much, but when deep discharge is performed and the specific gravity of the electrolyte decreases, the gel electrolyte softens significantly, so the H2O generated at this time is easily removed. The electrolyte then progresses to the top, causing what is called a stratification phenomenon of the electrolyte and deteriorating the battery. A similar phenomenon occurs with method A.

またCの方法よる電池では極板群をいかに圧迫しても、
またクラッド式正極板として偏平形チューブを用いても
、クラッド式正極板とセパレータとの間には必ず隙間が
生じるため、その隙間をゲル状電解液で埋める前者の電
池に比べて放電容量が著しく低下するとという欠点を有
していた。
In addition, in the battery using method C, no matter how much pressure is applied to the electrode plate group,
Furthermore, even if a flat tube is used as the cladding type positive electrode plate, there will always be a gap between the cladding type positive electrode plate and the separator, so the discharge capacity will be significantly lower than in the former battery where the gap is filled with gel electrolyte. It had the disadvantage that it deteriorated.

課題を解決するための手段 本発明は密閉形のクラッド式!9電池において放電容量
およびサイクル寿命性能を向上させることを目的とする
もので、その要旨はセパレータに平均繊維径が10μm
以下のガラス繊維をシート状にしたものを、また電解液
にはゲル状の希硫酸を使用すると共に、該セパレータ、
正極板および負極板で構成される極板群を電解液注入前
の乾燥状態で正極板のみかけ表面積(極板のタテ寸法×
ヨコ寸法)当たり20kg/di2以上の圧迫力で電槽
内に収納したことを特徴とするものである。
Means for Solving the Problems The present invention is a closed clad type! The purpose is to improve the discharge capacity and cycle life performance of 9 batteries, and the gist is that the separator has an average fiber diameter of 10 μm.
The following glass fibers were made into a sheet, and gel-like dilute sulfuric acid was used as the electrolyte, and the separator,
The apparent surface area of the positive electrode plate (vertical dimension of the electrode plate x
It is characterized by being housed in a battery case with a compression force of 20 kg/di2 or more per horizontal dimension).

実施例 以下、本発明による密閉形クラッド弐B池を図面を用い
て説明する。
EXAMPLE Hereinafter, a closed type clad 2B pond according to the present invention will be explained with reference to the drawings.

電池は容量が約35Ahで、クラッド式正極板3枚とペ
ースト式負極板4枚とで構成し、セパレータには平均繊
維径が1μm、10μm、そして比較のために従来の2
0μmのガラス繊維をシート状にした3種類のセパレー
タ イ22ロ、ハ使用した。
The battery has a capacity of approximately 35 Ah, and is composed of three clad positive plates and four paste negative plates.The separator has average fiber diameters of 1 μm and 10 μm, and for comparison, conventional 2
Three types of separators made of 0 μm glass fiber sheets were used.

これらを圧迫力が0 、10.20.30.40.50
および60 k(1/dl12  (正極板のみかけ表
面積当たり)になるようにして電池を製作した。電解液
はs; 02が約7%含まれた比重1.24(20℃)
の希硫酸を注液し、充電後には比重が1.30(20℃
)になるようにした。これらの電池を放電深さが75%
、充電量が110%の条件でサイクル寿命試験に供した
The compression force for these is 0, 10.20.30.40.50
and 60 k (1/dl12 (per apparent surface area of the positive electrode plate)).The electrolyte had a specific gravity of 1.24 (at 20°C) and contained about 7% S;02.
of dilute sulfuric acid, and after charging, the specific gravity was 1.30 (at 20℃).
). These batteries have a discharge depth of 75%
A cycle life test was conducted under the condition that the charge amount was 110%.

第3図にガラスセパレータの平均繊維径を変えた電池の
圧迫力と寿命サイクル数との関係を示す。
FIG. 3 shows the relationship between the compressive force and the number of life cycles of batteries with different average fiber diameters of the glass separators.

平均@維径が10μm以下のセパレータを用いた電池(
曲線イおよび口)で圧迫力を20 kg/di2  (
正極板のみかけ表面積当たり)以上(本発明品)にする
と著しく寿命性能が向上することがわかる。
A battery using a separator with an average fiber diameter of 10 μm or less (
The compression force is 20 kg/di2 (curve A and mouth).
(per apparent surface area of the positive electrode plate) or more (product of the present invention), it can be seen that the life performance is significantly improved.

つまり圧迫力をかけない従来品では本発明による電池と
同等の寿命性能を得ることは出来ないことがわかる。
In other words, it can be seen that it is not possible to obtain the same life performance as the battery according to the present invention with conventional products that do not apply compressive force.

第1図に本発明による極板群の横断面図を示す。FIG. 1 shows a cross-sectional view of an electrode plate group according to the present invention.

図から明らかなようにガラスセパレータは圧迫を強くか
けることにより正極板と接触する面積が著しく増加して
おり、充電時に生成されるH2SO。
As is clear from the figure, by applying strong pressure to the glass separator, the area in contact with the positive electrode plate increases significantly, and H2SO generated during charging increases.

を吸収しやすい構造で、かつ、第2図の圧迫をかけない
従来品の場合と比較して、クラッド式正極板とセパレー
タとの隙間部が約172になっていることがわかる。
It can be seen that the gap between the clad positive electrode plate and the separator is approximately 172 mm compared to the conventional product that does not apply pressure as shown in Figure 2.

平均繊維径が20μmのセパレータを使用した電池(曲
線ハ)では、圧迫力をいくらかけても本発明品以上の寿
命性能は得られなかった。
In a battery using a separator with an average fiber diameter of 20 μm (curve C), no matter how much pressure was applied, no longer life performance than the product of the present invention could be obtained.

このように、セパレータによる電解液の吸収能力を向上
させることによって電解液の成層化を防止し、電池の寿
命を伸ばすことができる。
In this way, by improving the electrolyte absorption capacity of the separator, stratification of the electrolyte can be prevented and the life of the battery can be extended.

また、平均繊維径が1μmのガラス繊維セパレータを用
いた電池に、5102を含まない希硫酸を注液し、セパ
レータに保持させたリテーナタイプの密閉形クラッド式
電池(従来品)も製作し、本発明品のようにゲル電解液
を用いた場合と放電容量の比較を行った。第4図にゲル
クラッド式電池A(本発明品を含む)と従来のリテーナ
タイプのクラッド式電池Bの放電容量を圧迫力を変えて
測定した結果を示す。
We also manufactured a cage-type sealed clad battery (conventional product) in which dilute sulfuric acid not containing 5102 was injected into a battery using a glass fiber separator with an average fiber diameter of 1 μm and held in the separator. The discharge capacity was compared with the case where a gel electrolyte was used like the invented product. FIG. 4 shows the results of measuring the discharge capacity of gel clad battery A (including the product of the present invention) and conventional retainer type clad battery B by varying the compressive force.

ゲルクラッド式電池Aもリテーナタイプのクラッド式電
池Bも圧迫力が大きくなるにつれ放電容量が増大してい
る。しかしリテーナタイプの電池Bはどんなに圧迫をか
けても本発明品に比べると放電容量は低くなっている。
In both the gel clad battery A and the retainer type clad battery B, the discharge capacity increases as the compressive force increases. However, no matter how much pressure is applied to the retainer type battery B, the discharge capacity is lower than that of the product of the present invention.

これはいくら圧迫力を大きくしてもクラッド式正極板と
セパレータとの間の隙間をなくすることができないため
で、その隙間をゲルで埋めているゲル式のクラッド式電
池の方が放電容量が大きいのは当然であろう。
This is because no matter how much pressure is applied, the gap between the clad positive electrode plate and the separator cannot be eliminated, and gel-type clad batteries, which fill the gap with gel, have a higher discharge capacity. Of course it's big.

なお、本発明ではセパレータとしてガラス繊維セパレー
タのみを使用して説明したが、正極板と接するセパレー
タの吸水能力を高めることが目的であるので、例えば正
極板側のみに本発明による平均繊維径が10μm以下の
ガラス繊維セパレータを当接し、負極板側にはポリエチ
レンなど、合成樹脂製セパレータを当接するという二種
類以上のセパレータを組み合わせて使用し7てもその効
果は同じである。
Although the present invention has been described using only a glass fiber separator as a separator, since the purpose is to increase the water absorption capacity of the separator in contact with the positive electrode plate, for example, the average fiber diameter according to the present invention is 10 μm only on the positive electrode plate side. The same effect can be obtained even if two or more types of separators are used in combination, such as a glass fiber separator shown below is brought into contact with the negative electrode plate, and a synthetic resin separator such as polyethylene is brought into contact with the negative electrode plate.

また、本発明による電池においても、極板内部とセパレ
ータ内部にはSi O□やAl2O,を含まず、正極板
とセパレータの隙間のみに、S;02やAt 20、を
多く含むゲル状電解液が入るようにすると、H2SO4
の移動速度が著しく大きくなるため放電容量がさらに改
善されると考えられる。
Furthermore, in the battery according to the present invention, the inside of the electrode plate and the separator do not contain SiO□ or Al2O, and only the gap between the positive electrode plate and the separator contains a gel electrolyte containing a large amount of S;02 and At20. If it is allowed to enter, H2SO4
It is thought that the discharge capacity is further improved because the moving speed of

発明の効果 以上のべたように本発明による密閉形クラッド式鉛電池
は従来の密閉形クラッド式鉛電池に比べ、放電容量およ
びサイクル寿命性能を著しく改善することができ、その
工業的価値は極めて大きいといえる。
Effects of the Invention As described above, the sealed clad lead-acid battery according to the present invention can significantly improve discharge capacity and cycle life performance compared to conventional sealed clad lead-acid batteries, and its industrial value is extremely large. It can be said.

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

第1図は本発明電池の極板群の横断面図、第2図は従来
電池の極板群の横断面図、第3図はガラスセパレータの
平均繊維径および圧迫力と電池寿命性能との関係を示し
た図、第4図はゲルクラッド式電池における電解液の違
い(ゲルまたはりチーす)および圧迫力と放電容量との
関係を示した図である。 1・・・クラッド式正極板、2ペ一スト式負極板、3・
・・ガラスセパレータ 坪 1 回 亨 −5囚 ayθ    2θ   3θ   〃   倣   
W反復77(脣/dン)
Fig. 1 is a cross-sectional view of the electrode plate group of the battery of the present invention, Fig. 2 is a cross-sectional view of the electrode plate group of the conventional battery, and Fig. 3 is the relationship between the average fiber diameter and compression force of the glass separator and battery life performance. FIG. 4 is a diagram showing the relationship between the difference in electrolyte (gel or liquid) and the relationship between compression force and discharge capacity in gel-clad batteries. 1... Clad type positive electrode plate, 2 paste type negative electrode plate, 3.
...Glass separator tsubo 1 times -5 ayθ 2θ 3θ 〃 Copying
W repetition 77 (脣/dn)

Claims (1)

【特許請求の範囲】[Claims] 1、ゲル状電解液を用いたクラッド式鉛電池において、
平均繊維径が10μm以下のガラス繊維をシート状にし
たセパレータを正極板と負極板との間に介在させると共
に、該セパレータ、正極板および負極板で構成される極
板群を電解液注入前の乾燥状態において正極板のみかけ
表面積当たり20kg/dm^2以上の圧迫力で電槽内
に収納したことを特徴とする密閉形クラッド式鉛電池。
1. In a clad lead-acid battery using a gel electrolyte,
A separator made of a sheet of glass fiber with an average fiber diameter of 10 μm or less is interposed between the positive electrode plate and the negative electrode plate, and the electrode plate group consisting of the separator, the positive electrode plate, and the negative electrode plate is placed in a A sealed clad lead-acid battery, characterized in that it is housed in a battery case with a compression force of 20 kg/dm^2 or more per apparent surface area of the positive electrode plate in a dry state.
JP63124662A 1988-05-20 1988-05-20 Sealed clad type lead battery Pending JPH01294369A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63124662A JPH01294369A (en) 1988-05-20 1988-05-20 Sealed clad type lead battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63124662A JPH01294369A (en) 1988-05-20 1988-05-20 Sealed clad type lead battery

Publications (1)

Publication Number Publication Date
JPH01294369A true JPH01294369A (en) 1989-11-28

Family

ID=14890950

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63124662A Pending JPH01294369A (en) 1988-05-20 1988-05-20 Sealed clad type lead battery

Country Status (1)

Country Link
JP (1) JPH01294369A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7682738B2 (en) 2002-02-07 2010-03-23 Kvg Technologies, Inc. Lead acid battery with gelled electrolyte formed by filtration action of absorbent separators and method for producing it

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5835877A (en) * 1981-08-26 1983-03-02 Yuasa Battery Co Ltd Closed type lead battery and its production method
JPS60119082A (en) * 1983-11-30 1985-06-26 Yuasa Battery Co Ltd Sealed lead-acid battery

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5835877A (en) * 1981-08-26 1983-03-02 Yuasa Battery Co Ltd Closed type lead battery and its production method
JPS60119082A (en) * 1983-11-30 1985-06-26 Yuasa Battery Co Ltd Sealed lead-acid battery

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7682738B2 (en) 2002-02-07 2010-03-23 Kvg Technologies, Inc. Lead acid battery with gelled electrolyte formed by filtration action of absorbent separators and method for producing it

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