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JPH0815075B2 - Method for forming sealed lead-acid battery - Google Patents
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JPH0815075B2 - Method for forming sealed lead-acid battery - Google Patents

Method for forming sealed lead-acid battery

Info

Publication number
JPH0815075B2
JPH0815075B2 JP63005141A JP514188A JPH0815075B2 JP H0815075 B2 JPH0815075 B2 JP H0815075B2 JP 63005141 A JP63005141 A JP 63005141A JP 514188 A JP514188 A JP 514188A JP H0815075 B2 JPH0815075 B2 JP H0815075B2
Authority
JP
Japan
Prior art keywords
battery
amount
electrode plate
sealed lead
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
Application number
JP63005141A
Other languages
Japanese (ja)
Other versions
JPH01186559A (en
Inventor
健二 小林
洋一 菊地
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 Holdings Corp
Original Assignee
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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP63005141A priority Critical patent/JPH0815075B2/en
Publication of JPH01186559A publication Critical patent/JPH01186559A/en
Publication of JPH0815075B2 publication Critical patent/JPH0815075B2/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
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • H01M4/16Processes of manufacture
    • H01M4/22Forming of electrodes
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (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、電解液が少なく制限され、遊離したフリー
な電解液のない密閉形鉛蓄電池の電槽内化成方法に関す
るものである。
Description: FIELD OF THE INVENTION The present invention relates to a method for chemical conversion in a battery case of a sealed lead-acid battery in which the amount of electrolyte is limited and there is no free electrolyte.

従来の技術 密閉形鉛蓄電池は、充電時に正極より発生する酸素ガ
スを負極に吸収させることで電解液の減少を防いでい
る。そこで負極は酸素を吸収できる様に、気層(酸素)
および液層(電解液)が同時に接触しなければならな
い。この状態では負極は充電と同時に放電しているた
め、未化成極板を化成することはできない。そのため、
一般に密閉形鉛蓄電池は正極活物質を二酸化鉛に、負極
活物質を鉛にそれぞれ変化させる化成工程を電池組立以
前に電槽外で行なっている。
2. Description of the Related Art In a sealed lead-acid battery, the negative electrode absorbs oxygen gas generated from the positive electrode during charging to prevent the electrolyte from decreasing. Therefore, the negative electrode is a gas layer (oxygen) so that it can absorb oxygen.
And the liquid layer (electrolyte) must be in contact at the same time. In this state, the negative electrode is discharged at the same time as charging, and therefore the unformed electrode plate cannot be formed. for that reason,
Generally, in a sealed lead-acid battery, a chemical conversion process in which the positive electrode active material is changed to lead dioxide and the negative electrode active material is changed to lead is performed outside the battery case before the battery is assembled.

しかし、電槽外で化成をすることは、負極活物質の酸
化劣化を防止する即用乾燥処理をともなうこと、さらに
電池組立後に活性化のための充電を必要とするなど電池
製造工程が煩雑となり、コスト高となっていた。
However, chemical conversion outside the battery case complicates the battery manufacturing process, such as requiring immediate drying treatment to prevent oxidative deterioration of the negative electrode active material, and further requiring charging for activation after battery assembly. The cost was high.

これらの問題を解決する方法として電槽内で極板を化
成することが提案された。
As a method of solving these problems, it has been proposed to form an electrode plate in a battery case.

すなわち、未化成の正極板と負極板および電解液を保
持吸収できるガラスマットセパレータからなる極板群を
電槽内に収容するとともに、過剰の希硫酸を極板群が溢
液状態になる様に加えて、充電し化成完了時に電解液を
所定の濃度と液量にする方法である。
That is, an electrode plate group consisting of an unformed positive electrode plate, a negative electrode plate, and a glass mat separator capable of holding and absorbing an electrolytic solution is housed in a battery case, and excess dilute sulfuric acid is allowed to overflow into the electrode plate group. In addition, it is a method of charging the electrolytic solution to a predetermined concentration and liquid amount when the formation is completed.

発明が解決しようとする課題 この様な従来の構成は、電解液を多量に収容できる電
池は可能であるが、容積効率を高め、多量の希硫酸を加
えると溢れてしまう電池には適用できないものである。
Problems that the Invention is to Solve The conventional configuration as described above can be applied to a battery that can accommodate a large amount of electrolytic solution, but cannot be applied to a battery that increases volumetric efficiency and overflows when a large amount of dilute sulfuric acid is added. Is.

本発明は正極,負極とも未化成極板を用いて電槽化成
を行ない、過剰の電解液を加えることができない密閉形
鉛蓄電池の電槽化成を可能にしたものである。
The present invention makes it possible to perform battery case formation of a sealed lead-acid battery in which an excessive amount of electrolyte cannot be added by performing battery case formation by using unformed electrode plates for both the positive electrode and the negative electrode.

課題を解決するための手段 本発明は極板群を収容した電槽内に、化成終了後所定
量に満たない液量の希硫酸を加え、充電した後、所定の
電解液量と濃度になる様に補液をするか、又は補液した
後、さらに再充電して所定の液量と濃度となる様にした
化成方法である。
Means for Solving the Problem The present invention is to add a dilute sulfuric acid of a liquid amount which is less than a predetermined amount after completion of chemical conversion in a battery case accommodating an electrode plate group, and after charging, has a predetermined electrolytic liquid amount and concentration. In this way, the chemical conversion method is such that the liquid is replenished or the liquid is recharged after the liquid is replenished so as to obtain a predetermined liquid amount and concentration.

作用 このような本発明の化成方法では、大別して次の2通
りの作用がなされる。
Action In such a chemical conversion method of the present invention, the following two actions are roughly performed.

(A)液量が比較的多い場合 充電効率の良い負極板は正極板より早く化成が完了す
るため、希硫酸に囲まれて正極板よりの酸素ガス吸収が
少ない状態で化成が完了する。しかし正極板を化成する
めにさらに充電すると、電解液が分解減少し、所定の電
解液量に満たなくなるため電池としての容量が充分に得
られない。これを防ぐためには補液をなせばよく、補液
により所定の電解液量および濃度にすることにより解決
できる。
(A) When the amount of liquid is relatively large Since the formation of the negative electrode plate having good charging efficiency is completed earlier than that of the positive electrode plate, the formation is completed while being surrounded by dilute sulfuric acid and absorbing less oxygen gas than the positive electrode plate. However, if the battery is charged further to form the positive electrode plate, the electrolytic solution is decomposed and reduced, and the amount of the electrolytic solution becomes less than a predetermined value, so that the capacity as a battery cannot be sufficiently obtained. In order to prevent this, it is only necessary to use a replenishing solution, which can be solved by adjusting the replenishing solution to a predetermined amount and concentration of the electrolytic solution.

(B)液量が少ない場合 液量が少ない電池はガス吸収が良いため正極板から酸
素が発生し、それを負極板が吸収するため、負極板は充
電しながら放電するため、液量に見合った割合しか化成
しない。この場合補液しただけでは、負極板は化成が完
了していないために容量は充分でない。しかし所定の電
解液量よりも多く補液し、充電することにより、負極板
は希硫酸に囲まれて正極板よりの酸素ガス吸収がなくな
り放電状態が解消されて化成が完了できる。
(B) When the amount of liquid is small A battery with a small amount of liquid has good gas absorption, so oxygen is generated from the positive electrode plate and the negative electrode plate absorbs oxygen. Only formed in proportion. In this case, the capacity of the negative electrode plate is not sufficient because the formation of the negative electrode plate is not completed just by replenishing the liquid. However, by supplementing with more than the predetermined amount of electrolyte and charging, the negative electrode plate is surrounded by dilute sulfuric acid, oxygen gas absorption from the positive electrode plate disappears, and the discharge state is eliminated to complete the chemical conversion.

実施例 未化成の正極板と負極板および電解液を吸収保持する
ガラスマットセパレータからなる極板群を電槽内に収容
した10時間率容量3Ahの電池の電槽化成方法の具体例を
以下に述べる。この電池は前もって29ml以上注液をした
場合、充電中に液が電池外に排出されることが確認され
ている。
Example A specific example of a battery case formation method of a battery having a 10-hour rate capacity of 3 Ah in which an electrode plate group consisting of an unformed positive electrode plate, a negative electrode plate, and a glass mat separator that absorbs and holds an electrolytic solution is housed in a battery case is shown below. Describe. It has been confirmed that this battery discharges to the outside of the battery during charging if more than 29 ml of liquid is injected in advance.

濃度30重量%の希硫酸29mlを電槽内に注入し、電池内
に外部より酸素が入らないように弁をした後、0.3Aで40
時間充電をした後、濃度41.5重量%の希硫酸3mlを加
え、希硫酸電解液を濃度が41.5重量%、液量が27mlとな
るよう調整する。この本発明の化成方法によると電池
(A)と、補液をしない化成方法による電池(B)とす
る。
After injecting 29 ml of dilute sulfuric acid with a concentration of 30% by weight into the battery case and opening a valve to prevent oxygen from entering the battery from outside, 40 at 0.3A
After charging for 3 hours, add 3 ml of dilute sulfuric acid having a concentration of 41.5 wt% and adjust the dilute sulfuric acid electrolyte to have a concentration of 41.5 wt% and a liquid volume of 27 ml. According to the chemical conversion method of the present invention, there are a battery (A) and a battery (B) manufactured by a chemical conversion method without replacement liquid.

さらに注液量を多くでない電池を想定し、濃度28重量
%の希硫酸26mlを加え前記と同じく弁をした後、0.3Aで
40時間充電した後濃度41.5重量%の希硫酸4.5mlを加
え、さらに0.3Aで5時間充電することにより、前記と同
じ所定の濃度と液量となった。この本発明による電池
(C)と補液を行なわない電池(D)とする。
Furthermore, assuming a battery with a small injection volume, add 26 ml of dilute sulfuric acid with a concentration of 28% by weight, and after opening the valve in the same manner as above, at 0.3 A
After charging for 40 hours, 4.5 ml of dilute sulfuric acid having a concentration of 41.5% by weight was added and further charged at 0.3 A for 5 hours to obtain the same predetermined concentration and liquid amount as described above. The battery (C) according to the present invention and the battery (D) which does not perform replenishing solution.

次に本発明の化成方法による電池(A),(C)と従
来の化成方法による電池(B),(D)の放電容量結果
を次表に示す。
Next, the discharge capacity results of the batteries (A) and (C) by the chemical conversion method of the present invention and the batteries (B) and (D) by the conventional chemical conversion method are shown in the following table.

発明の効果 本発明の化成方法によれば、従来電槽内化成では不可
能であった、電解液を多量に収納できない電池にも適用
できるため、容量効率が非常に高い密閉形鉛蓄電池が製
造工程の簡素化により、低コスト化できるものである。
EFFECTS OF THE INVENTION According to the chemical conversion method of the present invention, a sealed lead-acid battery with extremely high capacity efficiency can be manufactured because it can be applied to a battery that cannot store a large amount of electrolyte, which was not possible by conventional chemical conversion in a battery case. The cost can be reduced by simplifying the process.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】電解液の吸収保持体をなすセパレータで正
負極板間を隔離し、かつ電解液量が少なく制限された密
閉形鉛蓄電池の化成方法であって、極板群を収納した電
槽内に、化成終了後所定量に満たない液量を注入する注
液工程と、充電電流を流して化成する工程と、次に所定
の電解液量および濃度とする補液工程を有し、補液後に
負極板の化成を完了するための充電を行う密閉形鉛蓄電
池の化成方法。
1. A method for forming a sealed lead-acid battery in which positive and negative electrode plates are separated by a separator that serves as an absorber for an electrolytic solution and the amount of the electrolytic solution is limited to a small amount. In the tank, there is a liquid injection step of injecting a liquid amount that is less than a predetermined amount after completion of formation, a step of forming an electric current by flowing a charging current, and a replenishment process of making a predetermined electrolyte amount and concentration next, A method for forming a sealed lead-acid battery, in which charging is performed later to complete formation of the negative electrode plate.
JP63005141A 1988-01-13 1988-01-13 Method for forming sealed lead-acid battery Expired - Lifetime JPH0815075B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63005141A JPH0815075B2 (en) 1988-01-13 1988-01-13 Method for forming sealed lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63005141A JPH0815075B2 (en) 1988-01-13 1988-01-13 Method for forming sealed lead-acid battery

Publications (2)

Publication Number Publication Date
JPH01186559A JPH01186559A (en) 1989-07-26
JPH0815075B2 true JPH0815075B2 (en) 1996-02-14

Family

ID=11603027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63005141A Expired - Lifetime JPH0815075B2 (en) 1988-01-13 1988-01-13 Method for forming sealed lead-acid battery

Country Status (1)

Country Link
JP (1) JPH0815075B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4601834B2 (en) * 2001-01-17 2010-12-22 古河電池株式会社 Battery case formation method for lead acid battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56153663A (en) * 1980-04-30 1981-11-27 Shin Kobe Electric Mach Co Ltd Formation of lead acid battery

Also Published As

Publication number Publication date
JPH01186559A (en) 1989-07-26

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