JPS62126565A - Manufacture of sealed lead-acid battery - Google Patents

Manufacture of sealed lead-acid battery

Info

Publication number
JPS62126565A
JPS62126565A JP60265249A JP26524985A JPS62126565A JP S62126565 A JPS62126565 A JP S62126565A JP 60265249 A JP60265249 A JP 60265249A JP 26524985 A JP26524985 A JP 26524985A JP S62126565 A JPS62126565 A JP S62126565A
Authority
JP
Japan
Prior art keywords
retainer
plates
formation
sulfuric acid
amount
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
JP60265249A
Other languages
Japanese (ja)
Other versions
JPH0624139B2 (en
Inventor
Shinji Saito
慎治 斉藤
Yuzaburo Ishikawa
石川 雄三郎
Takumi Hayakawa
早川 他く美
Yasushi Matsumura
松村 康司
Akio Komaki
小牧 昭夫
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.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery 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 Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP60265249A priority Critical patent/JPH0624139B2/en
Publication of JPS62126565A publication Critical patent/JPS62126565A/en
Publication of JPH0624139B2 publication Critical patent/JPH0624139B2/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
    • H01M10/06Lead-acid accumulators
    • H01M10/12Construction or manufacture
    • H01M10/128Processes for forming or storing electrodes in the battery container
    • 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 uniformly distribute an adequate amount of electrolyte in plates and retainers by pouring a sulfuric acid containing gel mainly comprising silica into retainers, and performing formation in a container with step constant current. CONSTITUTION:Conventional production and assembly processes are omitted, and non-formed plates are assembled and put into a container. An adequate amount of dilute sulfuric acid is impregnated into plates and retainers, then, a sulfuric acid containing gel mainly comprising silica is poured into the retainers. Formation is performed in the container with step constant current, and controlled in the potential at which closed reaction is undergone in the final stage of the formation. thereby, the electrolyte is uniformly distributed into the plates, and in addition the process is simplified.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、密閉型鉛電池の製造法に関するものである。[Detailed description of the invention] Industrial applications The present invention relates to a method for manufacturing a sealed lead-acid battery.

従来の技術 密閉型鉛電池の充放電性能を向上名せるには、正・負極
板とリテーナ中に希硫酸をできる限り多くしかも均一に
保持することが重要でちる。
Conventional Technology In order to improve the charging and discharging performance of sealed lead-acid batteries, it is important to retain as much dilute sulfuric acid as possible and uniformly in the positive and negative electrode plates and the retainer.

しかし多すぎると遊離液か出C漏液の原因になるし、少
ないと内部抵抗が増加して性能が低下する。そこでリテ
ーナからの遊離液をすべて何らかの手段で吸収する必要
がある。一方リテーナが均一な状態で電解液を含浸して
いる場合には、充放電反応が極板の一部に集中し、残り
の極板部分はサルフエーション化また反応部ハ活物質の
泥状化につながる。
However, if it is too large, it will cause free liquid or C leakage, and if it is too small, internal resistance will increase and performance will deteriorate. Therefore, it is necessary to absorb all the free liquid from the retainer by some means. On the other hand, if the retainer is uniformly impregnated with electrolyte, the charge/discharge reaction will concentrate on a part of the plate, and the remaining plate will become sulfated, and the active material in the reaction area will become muddy. Leads to.

したがって、従来の密閉型鉛電池は、既化板を使っ°C
電池を組み立てて、これに所定量の電解液を注入するか
、または未化板を使っ”C組立てたリテーナ式電池でリ
テーナに過剰に電解液を注入して、電槽化成によるガツ
シングに伴なう減液により電解液の含浸量を適正量にし
Cいた。
Therefore, conventional sealed lead-acid batteries use prefabricated plates at °C.
Either assemble the battery and inject a predetermined amount of electrolyte into it, or inject an excessive amount of electrolyte into the retainer of a cage-type battery assembled using unconverted plates to prevent gassing caused by cell formation. The amount of electrolyte impregnated was adjusted to an appropriate amount by thinning.

発明が解決しようとする問題点 上記製造法による密閉型鉛電池では、前者は既化板の多
孔度あるいは表面積、電槽寸法、リテーナ寸法が個々に
異なるために電解液を所内量注入し゛〔もセル間でバラ
ツキを生じ液が不均一となり、密閉反応効率も1セル毎
で違っ′Cいた。また、後者は過剰量の液をリテーナに
含浸させ°C電槽化成を行う場合も、密閉反応効率とは
無関係に、定常流化成を行い、残った遊離液がなくなる
まで過充電しCいた。このような電池では、密閉反応を
無視しており、過充電となり、リテーナや極板中Iこ均
一な電解液の分散が困難であると考えられる。
Problems to be Solved by the Invention In the sealed lead-acid batteries manufactured by the above-mentioned manufacturing method, the porosity or surface area of the pre-treated plates, the dimensions of the battery case, and the dimensions of the retainer are different, so it is difficult to inject a specified amount of electrolyte. Fluctuations occurred between the cells, resulting in non-uniformity of the liquid, and the sealing reaction efficiency also varied from cell to cell. In addition, in the case of the latter, when carrying out cell formation at °C by impregnating the retainer with an excessive amount of liquid, constant flow formation was carried out regardless of the sealed reaction efficiency, and overcharging was performed until the remaining free liquid disappeared. In such a battery, the sealing reaction is ignored, resulting in overcharging, and it is thought that it is difficult to uniformly disperse the electrolyte in the retainer and electrode plates.

問題点を解決するための手段 本発明は、リテーナ式密閉型鉛電池のもつ上記欠点を改
良し、極板・リテーナ中に適正含浸量の電解液を均一に
分散させたすぐれた密閉型鉛電池の製造法を提供するも
のである。
Means for Solving the Problems The present invention improves the above-mentioned drawbacks of the cage-type sealed lead-acid battery, and provides an excellent sealed lead-acid battery in which an appropriate amount of electrolyte is uniformly dispersed in the electrode plates and the retainer. The present invention provides a method for manufacturing.

手段としては、atに既化板の製造および組立工程をす
べて省略し、極板を未化板の状態で組み立−rt槽内に
挿入し、極板およびリテーナに希硫酸を適正含浸量含浸
させ、次いでシリ力位に制御せしめるものである。
The method is to omit all the manufacturing and assembly processes of the pre-treated plates in the AT, insert the electrode plates in an uncured state into the assembly-RT tank, and impregnate the electrode plates and retainer with an appropriate amount of dilute sulfuric acid. Then, the force position is controlled.

作用 本発明は、電解液を適正含浸量だけ極板とりげろと端子
電圧か下がるために、密閉反応効率か良くなり、電槽化
成における過充電を極め〔少なくし°C終了させること
ができ、たとえ、過充電になったとしてもゲル中の電解
液をリテーナに供給できるため1こ、液が不均一に減少
したり、極板と接するリテーナ中での減液は少なくCす
む。また、電槽化成であるために、組立工程が極めて簡
単である。
Function The present invention improves the efficiency of the sealing reaction because the terminal voltage decreases when the electrode plate is impregnated with an appropriate amount of electrolyte, and overcharging in the cell forming process can be minimized and the battery can be terminated at °C. Even if overcharging occurs, the electrolytic solution in the gel can be supplied to the retainer, so that uneven reduction of the electrolyte and less loss of liquid in the retainer in contact with the electrode plates can be avoided. Furthermore, since the container is made of chemical material, the assembly process is extremely simple.

実施例 一例として、正極板理論容ヱを13Ah、公称容114
Ahの電池の場合、希硫酸の適正含浸量は32ゴである
。今、正極東活物質の化成上がりの状態を良好なものに
するために化成課電量を理論容量の200優とする。従
って過充電量は1004となりLaAh’9である。一
般に過剰液量を入れて電槽化成を行った場合に、電解液
がH,ガスとO,ガスに電気分解されて減液し、ついで
負極でO,ガスが効率よく吸収されはじめるのは、全化
成工程の1704化成量になった段階からである。しか
し、本発明のようにリテーナにゲルを保持したものでは
、0゜ガスか上方に散逸しにくいため、ゲル中を通Q負
極板と接触しやすくなるので1504化成量で密閉反応
となる。従って減液に費P!れる電気量はl 3AhX
0.5=6.5Ahで水量にすると2.24となる。つ
まり電槽化成前に注液する所定の液量は32a/+ 2
.2rttl= 34.2ゴとなる。
As an example, the theoretical capacity of the positive electrode plate is 13Ah, and the nominal capacity is 114.
In the case of an Ah battery, the appropriate amount of dilute sulfuric acid to be impregnated is 32g. Now, in order to make the formation condition of the positive far east active material good, the formation charge amount is set to 200 yen of the theoretical capacity. Therefore, the overcharge amount is 1004, which is LaAh'9. Generally, when carrying out battery cell formation with an excess amount of liquid, the electrolyte is electrolyzed into H, gas and O, gas, and the liquid decreases, and then O and gas begin to be efficiently absorbed at the negative electrode. This is from the stage when the total chemical conversion amount reaches 1704. However, in the case where the gel is held in a retainer as in the present invention, the 0° gas is difficult to dissipate upward, so that it easily passes through the gel and comes into contact with the Q negative electrode plate, resulting in a sealed reaction at a conversion amount of 1504. Therefore, it costs P to reduce the liquid! The amount of electricity generated is l 3AhX
If the amount of water is 0.5=6.5Ah, it will be 2.24. In other words, the predetermined amount of liquid to be injected before forming the battery is 32a/+2
.. 2rttl=34.2go.

従来法では、上記2.24の水を別に注入して過剰液と
していたか、本発明法ではゲルでリテーナ部分を満たす
tこめ、ケイ酸塩:希硫酸−6:4の場合には、5 m
lのゲルを注入すると2−以上の水分を含んでいるので
十分に過充電量をゲルからの供給で補なえる。従って、
全く過剰の液が不必要で、しかも、1501化成量で低
い定電流にするとますます密閉反応がtoo4に近くな
る。第1図に本発明法の化成電圧と電流および電池液量
の関係を示す。図面より明らかなように減液は少なく、
82図に示すようにゲル・リテーナ併用による全体保液
量か従来より多いために放電特性もよい。
In the conventional method, the above 2.24 water was separately injected to make an excess liquid, or in the method of the present invention, the retainer part was filled with gel. m
When 1 liter of gel is injected, since it contains 2 or more of water, the overcharge amount can be sufficiently compensated for by the supply from the gel. Therefore,
There is no need for any excess liquid, and if the amount of 1501 is used and the constant current is low, the hermetic reaction will become closer to that of too4. FIG. 1 shows the relationship between the chemical formation voltage, current, and battery liquid amount according to the present invention. As is clear from the drawing, there is little liquid loss;
As shown in Fig. 82, the total amount of liquid retained due to the combined use of a gel retainer is larger than that of the conventional system, so the discharge characteristics are also good.

また、化成工程と組立工程か簡単になる。Also, the chemical conversion process and assembly process are simplified.

発明の効果 第1に減液量を考慮することなく電槽化成かできる。′
@2に、段別定電流化成により少ない課電量でよい。第
3に極板に対して均一な電解液分散ができる。第4に放
電特性が全体保液量アップによりよくなった。第5に工
程が簡略化することができる。
The first effect of the invention is that it is possible to form a battery case without considering the amount of liquid to be reduced. ′
In @2, a small amount of current can be applied due to the step-by-step constant current formation. Thirdly, the electrolyte can be uniformly dispersed over the electrode plate. Fourthly, the discharge characteristics were improved due to the increase in the total amount of liquid retained. Fifth, the process can be simplified.

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

第1図は本発明による電槽化成の特性図、哨2図は本発
明による電池(本発明品)と従来の電池(従来品)との
高率放電特性図である。
FIG. 1 is a characteristic diagram of a battery case formed according to the present invention, and FIG. 2 is a high rate discharge characteristic diagram of a battery according to the present invention (product of the present invention) and a conventional battery (conventional product).

Claims (1)

【特許請求の範囲】[Claims] 正極と負極とガラス繊維を主成分とするリテーナとから
なる密閉型鉛電池において、極板を未化板の状態で組み
立て電槽内に挿入し、極板およびリテーナに希硫酸を適
正含浸量含浸させ、次いでシリカを主成分とせる硫酸保
有ゲルをリテーナに注入した後、段別定電流による電槽
化成を行い、化成末期で密閉反応を生ずる電位に制御せ
しめることを特徴とする密閉型鉛電池の製造法。
In a sealed lead-acid battery consisting of a positive electrode, a negative electrode, and a retainer whose main components are glass fiber, the electrode plates are assembled in an unprocessed state and inserted into a battery case, and the electrode plates and retainer are impregnated with the appropriate amount of dilute sulfuric acid. Then, after injecting a sulfuric acid-containing gel containing silica as a main component into the retainer, cell formation is carried out using a constant current in stages, and the potential is controlled to a potential that causes a sealing reaction at the final stage of formation. manufacturing method.
JP60265249A 1985-11-26 1985-11-26 Manufacturing method of sealed lead battery Expired - Lifetime JPH0624139B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60265249A JPH0624139B2 (en) 1985-11-26 1985-11-26 Manufacturing method of sealed lead battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60265249A JPH0624139B2 (en) 1985-11-26 1985-11-26 Manufacturing method of sealed lead battery

Publications (2)

Publication Number Publication Date
JPS62126565A true JPS62126565A (en) 1987-06-08
JPH0624139B2 JPH0624139B2 (en) 1994-03-30

Family

ID=17414600

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60265249A Expired - Lifetime JPH0624139B2 (en) 1985-11-26 1985-11-26 Manufacturing method of sealed lead battery

Country Status (1)

Country Link
JP (1) JPH0624139B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004193097A (en) * 2002-10-17 2004-07-08 Furukawa Battery Co Ltd:The Method for formation of lead storage battery
JP2008204638A (en) * 2007-02-16 2008-09-04 Gs Yuasa Corporation:Kk Control valve type lead-acid battery, and manufacturing method thereof
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 (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54153240A (en) * 1978-05-24 1979-12-03 Japan Storage Battery Co Ltd Method of producing closed lead storage battery
JPS56123675A (en) * 1980-03-04 1981-09-28 Matsushita Electric Ind Co Ltd Manufacture of closed type lead-acid battery
JPS57107575A (en) * 1980-11-06 1982-07-05 Sonnenschein Accumulatoren Lead storage battery and method of producing same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54153240A (en) * 1978-05-24 1979-12-03 Japan Storage Battery Co Ltd Method of producing closed lead storage battery
JPS56123675A (en) * 1980-03-04 1981-09-28 Matsushita Electric Ind Co Ltd Manufacture of closed type lead-acid battery
JPS57107575A (en) * 1980-11-06 1982-07-05 Sonnenschein Accumulatoren Lead storage battery and method of producing same

Cited By (4)

* 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
JP2004193097A (en) * 2002-10-17 2004-07-08 Furukawa Battery Co Ltd:The Method for formation of lead storage battery
JP2008204638A (en) * 2007-02-16 2008-09-04 Gs Yuasa Corporation:Kk Control valve type lead-acid battery, and manufacturing method thereof
US8257856B2 (en) 2007-02-16 2012-09-04 Gs Yuasa International Ltd. Valve-regulated lead-acid battery and production method thereof

Also Published As

Publication number Publication date
JPH0624139B2 (en) 1994-03-30

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