JP3099527B2 - Manufacturing method of sealed lead-acid battery - Google Patents

Manufacturing method of sealed lead-acid battery

Info

Publication number
JP3099527B2
JP3099527B2 JP04179589A JP17958992A JP3099527B2 JP 3099527 B2 JP3099527 B2 JP 3099527B2 JP 04179589 A JP04179589 A JP 04179589A JP 17958992 A JP17958992 A JP 17958992A JP 3099527 B2 JP3099527 B2 JP 3099527B2
Authority
JP
Japan
Prior art keywords
battery
sulfuric acid
sol
electrode group
sealed lead
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
JP04179589A
Other languages
Japanese (ja)
Other versions
JPH0620715A (en
Inventor
安平 坂田
隆生 尾崎
恒典 吉村
正治 府川
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.)
Panasonic Corp
Panasonic Holdings Corp
Original Assignee
Panasonic Corp
Matsushita Electric Industrial 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 Panasonic Corp, Matsushita Electric Industrial Co Ltd filed Critical Panasonic Corp
Priority to JP04179589A priority Critical patent/JP3099527B2/en
Publication of JPH0620715A publication Critical patent/JPH0620715A/en
Application granted granted Critical
Publication of JP3099527B2 publication Critical patent/JP3099527B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • 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

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  • Secondary Cells (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、密閉型鉛蓄電池の製造
法に関するもので、特に多量に電解液を保持する密閉型
鉛蓄電池の製造法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of manufacturing a sealed lead-acid battery, and more particularly to a method of manufacturing a sealed lead-acid battery holding a large amount of electrolyte.

【0002】[0002]

【従来の技術】密閉型鉛蓄電池は、正極活物質および負
極活物質を理論量よりかなり多量に使用する設計が多
く、大半の電池では硫酸量で容量が決められる。また、
使用途中で充放電を繰り返すものでは、電池内に硫酸の
濃度差を生じるいわゆる成層化現象が発生し、また、長
時間使用する電池では、電槽等の樹脂より水分が透過し
減液現象を生じ容量低下を起こすなどの点から電池内に
できるだけ多くの電解液を確保するとともに表面積の大
きい電解液保持材が要望されている。この電解液の確保
と成層化防止対策として電池内の空間スペースにゲル材
を充填する方法がとられている。
2. Description of the Related Art In many cases, sealed lead-acid batteries are designed to use a positive electrode active material and a negative electrode active material in a considerably larger amount than the theoretical amount, and the capacity of most batteries is determined by the amount of sulfuric acid. Also,
If the battery is repeatedly charged and discharged during use, a so-called stratification phenomenon occurs, which causes a difference in the concentration of sulfuric acid in the battery.In a battery that is used for a long time, moisture permeates from the resin in the battery case, etc. There is a demand for an electrolyte holding material that secures as much electrolyte solution as possible in a battery and has a large surface area in view of the resulting capacity reduction. As a method for securing the electrolyte and preventing stratification, a method of filling a space in the battery with a gel material has been adopted.

【0003】一つの方法として化成正極板、化成負極板
をガラス繊維製セパレータを介し集合し、さらに集電体
を正、負極別にストラップに溶接して一体化して極板群
を構成し、電槽に収納し、顆粒状シリカ粉末を電槽と極
板の間に充填し、相隣り合うセル間の接合や蓋と電槽と
の接着を行い電池を組み立てて、その後希硫酸を注液し
て電池とする方法がとられている。
As one method, a formed positive electrode plate and a formed negative electrode plate are assembled via a glass fiber separator, and a current collector is welded to a strap for each of a positive electrode and a negative electrode to be integrated to form an electrode plate group. And filling the granular silica powder between the battery case and the electrode plate, bonding the cells adjacent to each other and bonding the lid to the battery case, and assembling the battery. The way to do it is taken.

【0004】しかしながら、この方法では極板が顆粒状
シリカ粉末で覆われているので、電解液の極板群への吸
収が遅く時間がかかるとともにケイ酸粉末が均一になる
ように希硫酸を浸透させることが難しく、ケイ酸粉末が
ままこ状に残る場合があり、極板群へ電解液が多く含ま
れるなどして電解液が不均一になり、また、この方法で
は電槽化成方式の採用が難しいなどの欠点があった。
However, in this method, since the electrode plate is covered with the granular silica powder, absorption of the electrolytic solution into the electrode plate group is slow, it takes time, and dilute sulfuric acid is impregnated so that the silicic acid powder becomes uniform. It is difficult to do so, and the silicic acid powder may remain in the shape of a cage, and the electrolyte may become uneven due to the large amount of electrolyte contained in the electrode plate group. There were drawbacks such as difficulty.

【0005】[0005]

【発明が解決しようとする課題】そこで、顆粒状シリカ
粉末を電池内に充填する方式に代え、予めシリカ粉末を
希硫酸に均一に分散させたゾル溶液を用意して、これを
組み立てられた電池に注液して電池を構成することが考
えられる。
Therefore, instead of the method of filling granular silica powder in a battery, a sol solution in which silica powder is uniformly dispersed in dilute sulfuric acid is prepared in advance, and the battery is assembled with the sol solution. To form a battery.

【0006】しかしながら、シリカ粉末の溶液はシリカ
粉末が高濃度になると電池内への充填が難しく、攪拌等
によって流動化はできるが、ある限度を超えると取り扱
えるゲル濃度に限界がある。
However, when the silica powder solution has a high silica powder concentration, it is difficult to fill the solution into the battery, and the solution can be fluidized by stirring or the like. However, when the silica powder solution exceeds a certain limit, the gel concentration that can be handled is limited.

【0007】また、電槽化成を行った場合は化成によっ
て液が減少するにつれて下部の濃度が濃くなり容量にバ
ラツキを生ずるという不都合を有している。
[0007] In addition, when the battery formation is performed, there is an inconvenience that the concentration of the lower part increases as the liquid decreases due to the formation, and the capacity varies.

【0008】[0008]

【課題を解決するための手段】本発明は極板群中の液状
態を適当量より少ない不足状態にしたいわゆる乾いた状
態にして、ゾル溶液を充填してゾル中の硫酸水を極板群
側へ移行させ、ゾルを非流動化させ、ポジションフリー
の電池を提供しようとするものである。
SUMMARY OF THE INVENTION The present invention is directed to a so-called dry state in which the liquid state in an electrode group is reduced to a shortage less than an appropriate amount, and a sol solution is filled to remove sulfuric acid water in the sol. Side to de-fluidize the sol and provide a position-free battery.

【0009】即ち、本発明の密閉型鉛蓄電池の製造法
は、リテナー式セパレータを用いた極板群で組み立てた
電池に、適当量に満たない希硫酸電解液を注液し、極板
群を電解液の不足状態とし、その後、ケイ酸ソーダある
いはシリカ粉末を含んだ希硫酸ゾルを電池内の電槽と極
板群間に充填し、ゾル中の硫酸水を極板群側に吸収させ
て、ゾルを非流動化することを特徴とする。
That is, in the method for manufacturing a sealed lead-acid battery of the present invention, a dilute sulfuric acid electrolyte solution, which is less than an appropriate amount, is injected into a battery assembled from a group of electrodes using a retainer type separator. After the electrolyte was in a shortage state, dilute sulfuric acid sol containing sodium silicate or silica powder was filled between the battery case and the electrode group in the battery, and the sulfuric acid solution in the sol was absorbed by the electrode group side. , Making the sol non-fluidized.

【0010】また、電槽化成を行う場合の本発明の密閉
型鉛蓄電池の製造法は、リテナー式セパレータを用いた
極板群で組み立てた電池に、極板群に含浸する適当量よ
りも過剰の希硫酸電解液を注液し、電槽化成を行い極板
群中の電解液を減液させ、極板群を電解液の不足状態と
し、その後、ケイ酸ソーダあるいはシリカ粉末を含んだ
希硫酸ゾルを電池内の電槽と極板群間に充填し、ゾル中
の硫酸水を極板群側に吸収させて、ゾルを非流動化する
ことを特徴とする。
Further, the method for producing a sealed lead-acid battery according to the present invention in the case of carrying out battery case formation requires that a battery assembled with an electrode group using a retainer type separator has an excess of an appropriate amount impregnated into the electrode group. The electrolyte solution in the electrode group was reduced by injecting a diluted sulfuric acid electrolyte solution of the electrode plate, and the electrode group in the electrode group was reduced, and the electrode group was brought into an insufficient state of the electrolyte solution, and then diluted with sodium silicate or silica powder. It is characterized in that a sulfuric acid sol is filled between a battery case and an electrode group in a battery, and a sulfuric acid solution in the sol is absorbed on the electrode group side to make the sol non-fluidized.

【0011】上記何れの場合も、希硫酸ゾルは、シリカ
粉末濃度30〜60g/リットルの希硫酸ゾルを極板群
に吸収させて、ゾル中のシリカ粉末濃度を100g/リ
ットル以上にするのが好ましい。
In any of the above cases, the diluted sulfuric acid sol should be made such that the diluted sulfuric acid sol having a silica powder concentration of 30 to 60 g / l is absorbed by the electrode plate group so that the concentration of the silica powder in the sol is 100 g / l or more. preferable.

【0012】また、電槽化成の場合、比重1.15〜
1.25の希硫酸電解液を注液し、その比重が1.25
〜1.35になるまで電槽化成して過充電を行い、電解
液を減液するのが好ましい。
In the case of battery case formation, the specific gravity is 1.15 to 15.
A 1.25 diluted sulfuric acid electrolyte was injected, and the specific gravity was 1.25.
It is preferable that the battery case is formed and overcharged to reduce the electrolyte solution to 1.35.

【0013】また、電槽化成完了後の電池内電解液の平
均濃度より高濃度の硫酸ゾルを充填することにより硫酸
濃度を均一にするのが好ましい。
It is preferable that the sulfuric acid concentration is made uniform by filling a sulfuric acid sol having a higher concentration than the average concentration of the electrolytic solution in the battery after the formation of the battery container.

【0014】[0014]

【作用】本発明では、流動化状態でゾルを電池内に充填
し、いわゆる乾いた極板群にゾル中の硫酸水を吸い取ら
せることによりゾルの濃度を上げ、ゾルを非流動化しよ
うとするものである。
According to the present invention, the sol is filled in a battery in a fluidized state, and the concentration of the sol is increased by causing a so-called dry electrode group to absorb the sulfuric acid aqueous solution in the sol, thereby making the sol non-fluidized. Things.

【0015】[0015]

【実施例】以下、実施例によって本発明を詳述する。The present invention will be described below in detail with reference to examples.

【0016】図1は本発明を適用した密閉型鉛蓄電池の
構成例を示す。図中、1はABS樹脂製の電槽を示し、
該電槽1内に未化成活物質を充填した正極板2、負極板
3およびガラス繊維製セパレータ4で構成される極板群
5を挿入し、蓋6を電槽1に接着固定して電池を組み立
てたものである。尚、図中7は集電体、8は注液孔を示
す。
FIG. 1 shows an example of the configuration of a sealed lead-acid battery to which the present invention is applied. In the figure, 1 indicates a battery case made of ABS resin,
The battery case 1 is filled with an electrode plate group 5 composed of a positive electrode plate 2, a negative electrode plate 3, and a glass fiber separator 4 filled with an unactivated material, and a lid 6 is bonded and fixed to the battery case 1. Is assembled. In the figure, 7 indicates a current collector, and 8 indicates a liquid injection hole.

【0017】このように組み立てられた電池の注液孔8
から、極板群5に含浸する適当量よりも過剰の希硫酸電
解液を注液し、次いで通電して正、負極板2,3を化成
し、正、負極活物質量の理論容量以上に過充電すること
により過剰の水素ガスと酸素ガスに電気分解して電池外
へ放出し、さらに極板群5に含浸する適当量よりさらに
過充電により減液させる。
The battery injection hole 8 of the battery thus assembled.
Then, an excessive amount of dilute sulfuric acid electrolyte is injected into the electrode group 5 in excess of an appropriate amount to be impregnated, and then energized to form the positive and negative electrode plates 2 and 3 so that the positive and negative electrode active materials have a theoretical capacity or more. By overcharging, excess hydrogen gas and oxygen gas are electrolyzed and released out of the battery, and the liquid is further reduced by overcharging from an appropriate amount impregnated in the electrode plate group 5.

【0018】その後、乾式シリカ微粉末(通称アエロジ
ル)を希硫酸電解液に攪拌機で分散させた流動状態にあ
るゾルを電槽1と極板群5の間および極板群5上部まで
注液孔8から充填し、このゾルから極板群5へ希硫酸電
解液を一部吸い取らせ極板2,3中の電解液量が適当量
になるように移動させ、流動状態にあったゾルを非流動
化したゾル9にした。
Thereafter, a flowing sol obtained by dispersing dry silica fine powder (commonly known as Aerosil) in a dilute sulfuric acid electrolytic solution with a stirrer is injected into the space between the battery case 1 and the electrode group 5 and up to the upper part of the electrode group 5. 8, and a part of the diluted sulfuric acid electrolyte solution is sucked from the sol to the electrode group 5 and moved so that the amount of the electrolyte solution in the electrode plates 2 and 3 becomes an appropriate amount. The fluidized sol 9 was obtained.

【0019】次に15Ahの電池を例に、より具体的な
実施例を比較例とともに説明する。 実施例1 比重1.25の電解液を電池容量Ah当たり8cc/A
h注液し、理論化成電気量の250%で電槽化成した。
さらに理論容量の100%で過充電して、硫酸比重1.
30、シリカ微粉末濃度60g/リットルのゾル溶液を
2cc/Ah相当、電槽と極板群間に充填し電池を試作
した。シリカ微粉末ゾルは90g/リットルを越えると
急激に非流動化しゲル状の堅いケーキ状となった。 実施例2 次に、比重1.25の電解液を電池容量Ah当たり8c
c/Ah注液し、理論化成電気量の250%で電槽化成
して、電池内の上下の平均電解液比重を1.30にし、
さらに理論容量の100%で過充電して、硫酸比重1.
32、シリカ微粉濃度60g/リットルのゾル溶液を2
cc/Ah相当、電槽と極板群間に充填し電池を試作し
た。 比較例 比較例として、比重1.25の電解液を電池容量Ah当
たり8cc/Ah注液し、理論化成電気量の250%で
電槽化成した従来電池を試作した。
Next, a more specific example will be described together with a comparative example, taking a 15 Ah battery as an example. Example 1 An electrolytic solution having a specific gravity of 1.25 was subjected to 8 cc / A per battery capacity Ah.
h, and the battery was formed at 250% of the theoretical formation electricity amount.
Further, the battery was overcharged at 100% of the theoretical capacity to obtain a sulfuric acid specific gravity of 1.
30, a sol solution having a silica fine powder concentration of 60 g / liter was filled between the battery case and the electrode plate in an amount corresponding to 2 cc / Ah to produce a prototype battery. When the silica fine powder sol exceeded 90 g / liter, it rapidly non-fluidized and became a gel-like hard cake. Example 2 Next, an electrolyte having a specific gravity of 1.25 was applied at a rate of 8 c per battery capacity Ah.
c / Ah, and the cell was formed at 250% of the theoretical formation electricity amount, and the average specific gravity of the upper and lower electrolytes in the battery was 1.30.
Further, the battery was overcharged at 100% of the theoretical capacity to obtain a sulfuric acid specific gravity of 1.
32, a sol solution having a silica fine powder concentration of 60 g / liter
A battery equivalent to cc / Ah was filled between the battery case and the electrode plate group to produce a prototype. Comparative Example As a comparative example, a conventional battery in which an electrolytic solution having a specific gravity of 1.25 was injected at a rate of 8 cc / Ah per battery capacity Ah and a battery case was formed at 250% of the theoretical formation electricity amount was prototyped.

【0020】上記、各実施例並びに比較例により試作さ
れた電池の初期容量とトリクル寿命を測定し、その結果
を下記表1に示す。
The initial capacity and the trickle life of the batteries experimentally produced in the above Examples and Comparative Examples were measured, and the results are shown in Table 1 below.

【0021】[0021]

【表1】 [Table 1]

【0022】表1から明らかなように、比較例に比し、
実施例1,2の場合、共に初期容量、トリクル寿命とも
向上し、特に、実施例2の場合、トリクル寿命の向上が
6年と著しかった。
As is clear from Table 1, compared with the comparative example,
In the case of Examples 1 and 2, both the initial capacity and the trickle life were improved, and particularly in the case of Example 2, the life of the trickle was remarkably improved to 6 years.

【0023】尚、前記実施例では電槽化成の例のみ示し
たが、予め化成した極板を用いた場合にも本発明密閉型
鉛蓄電池の製造法を適用できることは言うまでもない。
In the above embodiment, only the case of battery case formation is shown, but it goes without saying that the method of manufacturing a sealed lead-acid battery of the present invention can also be applied to the case where a previously formed electrode plate is used.

【0024】[0024]

【発明の効果】以上の説明で明らかなように、本発明の
密閉型鉛蓄電池の製造法によれば、電解液量を多く確保
できるとともに、電槽化成で生じる上下の濃度差を硫酸
濃度の濃いゾルを電池内に充填することにより緩和でき
る。
As is apparent from the above description, according to the method for producing a sealed lead-acid battery of the present invention, a large amount of electrolyte can be ensured, and the difference between the upper and lower concentrations caused by battery formation can be reduced by the sulfuric acid concentration. This can be alleviated by filling the battery with a dense sol.

【0025】また、シリカ粉末により表面積を増し、表
面張力によって充放電中に生じる成層化を防止でき、製
品の品質を向上できる。
Further, the surface area is increased by the silica powder, stratification occurring during charging and discharging due to surface tension can be prevented, and the quality of the product can be improved.

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

【図1】本発明の実施例による密閉型鉛蓄電池の断面図FIG. 1 is a sectional view of a sealed lead-acid battery according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 電槽 2 正極板 3 負極板 4 セパレータ 5 極板群 6 蓋 7 集電体 8 注液孔 9 非流動化したゾル DESCRIPTION OF SYMBOLS 1 Battery case 2 Positive electrode plate 3 Negative electrode plate 4 Separator 5 Electrode plate group 6 Lid 7 Current collector 8 Injection hole 9 Non-fluidized sol

───────────────────────────────────────────────────── フロントページの続き (72)発明者 府川 正治 大阪府門真市大字門真1006番地 松下電 器産業株式会社内 (56)参考文献 特開 昭63−221565(JP,A) 特開 平3−145067(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 10/10 - 10/12 ────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Masaharu Fukawa 1006 Kazuma Kadoma, Kadoma City, Osaka Inside Matsushita Electric Industrial Co., Ltd. (56) References JP-A-63-221565 (JP, A) JP-A-3-3 145067 (JP, A) (58) Field surveyed (Int. Cl. 7 , DB name) H01M 10/10-10/12

Claims (5)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 リテナー式セパレータを用いた極板群で
組み立てた電池に、適当量に満たない希硫酸電解液を注
液し、極板群を電解液の不足状態とし、その後、ケイ酸
ソーダあるいはシリカ粉末を含んだ希硫酸ゾルを電池内
の電槽と極板群間に充填し、ゾル中の硫酸水を極板群側
に吸収させて、ゾルを非流動化することを特徴とする密
閉型鉛蓄電池の製造法。
An insufficiency of a dilute sulfuric acid electrolytic solution is injected into a battery assembled with an electrode group using a retainer type separator, and the electrode group is brought into a state of insufficient electrolyte. Alternatively, a dilute sulfuric acid sol containing silica powder is filled between the battery case and the electrode group in the battery, and the sulfuric acid solution in the sol is absorbed to the electrode group side, thereby making the sol non-fluidized. Manufacturing method for sealed lead-acid batteries.
【請求項2】 リテナー式セパレータを用いた極板群で
組み立てた電池に、極板群に含浸する適当量よりも過剰
の希硫酸電解液を注液し、電槽化成を行い極板群中の電
解液を減液させ、極板群を電解液の不足状態とし、その
後、ケイ酸ソーダあるいはシリカ粉末を含んだ希硫酸ゾ
ルを電池内の電槽と極板群間に充填し、ゾル中の硫酸水
を極板群側に吸収させて、ゾルを非流動化することを特
徴とする密閉型鉛蓄電池の製造法。
2. A battery assembled with an electrode group using a retainer-type separator is poured with a dilute sulfuric acid electrolyte in excess of an appropriate amount for impregnating the electrode group. The electrode group is brought into a state of lack of electrolyte solution, and then dilute sulfuric acid sol containing sodium silicate or silica powder is filled between the battery case and the electrode group in the battery. A method for producing a sealed lead-acid battery, characterized in that the sol is made non-fluid by absorbing the sulfuric acid solution into the electrode plate group side.
【請求項3】 シリカ粉末濃度30〜60g/リットル
の希硫酸ゾルを極板群に吸収させて、ゾル中のシリカ粉
末濃度を100g/リットル以上にすることを特徴とす
る請求項1または2に記載の密閉型鉛蓄電池の製造法。
3. The method according to claim 1, wherein a diluted sulfuric acid sol having a silica powder concentration of 30 to 60 g / l is absorbed by the electrode group so that the silica powder concentration in the sol is 100 g / l or more. A method for producing a sealed lead-acid battery as described in the above.
【請求項4】 比重1.15〜1.25の希硫酸電解液
を注液し、その比重が1.25〜1.35になるまで電
槽化成して過充電を行い、電解液を減液することを特徴
とする請求項2または3に記載の密閉型鉛蓄電池の製造
法。
4. A dilute sulfuric acid electrolytic solution having a specific gravity of 1.15 to 1.25 is injected, and a battery case is formed until the specific gravity becomes 1.25 to 1.35 to perform overcharging to reduce the electrolytic solution. 4. The method for producing a sealed lead-acid battery according to claim 2, wherein the battery is liquid.
【請求項5】 電槽化成完了後の電池内電解液の平均濃
度より高濃度の硫酸ゾルを充填することにより硫酸濃度
を均一にすることを特徴とする請求項2乃至4の何れか
に記載の密閉型鉛蓄電池の製造法。
5. The method according to claim 2, wherein the sulfuric acid concentration is made uniform by filling a sulfuric acid sol having a higher concentration than the average concentration of the electrolytic solution in the battery after the battery case formation is completed. For manufacturing sealed lead-acid batteries.
JP04179589A 1992-07-07 1992-07-07 Manufacturing method of sealed lead-acid battery Expired - Fee Related JP3099527B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04179589A JP3099527B2 (en) 1992-07-07 1992-07-07 Manufacturing method of sealed lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04179589A JP3099527B2 (en) 1992-07-07 1992-07-07 Manufacturing method of sealed lead-acid battery

Publications (2)

Publication Number Publication Date
JPH0620715A JPH0620715A (en) 1994-01-28
JP3099527B2 true JP3099527B2 (en) 2000-10-16

Family

ID=16068375

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Link
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Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19513343C1 (en) * 1995-04-08 1996-10-10 Europ Accumulateurs Process for the production of a lead accumulator

Also Published As

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JPH0620715A (en) 1994-01-28

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