JPH08138657A - Manufacturing method of electrode plate for lead-acid battery - Google Patents

Manufacturing method of electrode plate for lead-acid battery

Info

Publication number
JPH08138657A
JPH08138657A JP6279175A JP27917594A JPH08138657A JP H08138657 A JPH08138657 A JP H08138657A JP 6279175 A JP6279175 A JP 6279175A JP 27917594 A JP27917594 A JP 27917594A JP H08138657 A JPH08138657 A JP H08138657A
Authority
JP
Japan
Prior art keywords
lead
electrode plate
slurry
sulfuric acid
support
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
JP6279175A
Other languages
Japanese (ja)
Other versions
JP3267075B2 (en
Inventor
Katsuhiro Takahashi
勝弘 高橋
Takeshi Hatanaka
剛 畑中
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 JP27917594A priority Critical patent/JP3267075B2/en
Publication of JPH08138657A publication Critical patent/JPH08138657A/en
Application granted granted Critical
Publication of JP3267075B2 publication Critical patent/JP3267075B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

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  • Battery Electrode And Active Subsutance (AREA)

Abstract

(57)【要約】 【目的】 薄い支持体の表面に薄い活物質層を形成する
ことができるとともに、3PbO・PbSO4およびP
bO・H2Oなどの生成により反応性と結合性に優れた
鉛蓄電池用極板を提供するものである。 【構成】 硫酸を加えずに鉛粉と水とを主成分としてス
ラリーを作製する工程と、このスラリーを支持体に塗着
する工程と、スラリーを塗着した支持体を希硫酸に接触
させる工程と、希硫酸に接触させた後、スラリーを塗着
した支持体を空気中で熟成する工程とからなるものであ
る。
(57) [Abstract] [Purpose] A thin active material layer can be formed on the surface of a thin support, and 3PbO / PbSO 4 and P can be formed.
It is intended to provide an electrode plate for a lead storage battery which is excellent in reactivity and bondability due to generation of bO.H 2 O and the like. [Structure] A step of preparing a slurry containing lead powder and water as main components without adding sulfuric acid, a step of applying the slurry to a support, and a step of bringing the support applied with the slurry into contact with dilute sulfuric acid. And a step of aging the support coated with the slurry in air after being brought into contact with dilute sulfuric acid.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は鉛蓄電池のとくにその極
板に関し、活物質を支持体に薄く塗着することができる
極板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 lead acid battery, and more particularly to its electrode plate, and more particularly to a method of manufacturing an electrode plate capable of thinly coating an active material on a support.

【0002】[0002]

【従来の技術】近年、鉛蓄電池では高出力が可能な電池
の開発が進められており、極板を薄くして電池内に収納
する極板の枚数を増やしたり、集電体に設ける孔の径を
小さくして細孔分布を細かくして集電効率を高めたり、
また長尺状の極板を渦巻状にして極板間の接触面積を大
きくする検討が行われている。このような電池を実現す
るためには、500〜100μm以下の薄い活物質層を
極板に形成する必要がある。
2. Description of the Related Art In recent years, lead acid batteries have been under development for a high output battery, and the electrode plates are made thinner to increase the number of electrode plates to be housed in the battery, or the holes provided in the current collector are reduced. You can improve the current collection efficiency by reducing the diameter and fine pore distribution.
In addition, studies have been conducted to make the long electrode plates spiral to increase the contact area between the electrode plates. In order to realize such a battery, it is necessary to form a thin active material layer of 500 to 100 μm or less on the electrode plate.

【0003】従来、鉛蓄電池用極板は酸化鉛と鉛を主成
分とし活物質となる鉛粉と希硫酸および水などを混合
し、これらを練合して活物質ペーストを得た後、厚み
1.5〜2mmの鋳造格子体やエキスパンド格子体等の
支持体にペーストを充填し、ついでこれを適当な温度と
湿度の雰囲気下で熟成,乾燥させて、極板を得ていた。
Conventionally, an electrode plate for a lead storage battery is prepared by mixing lead oxide, lead powder containing lead as a main component and an active material, dilute sulfuric acid, water, etc., and kneading them to obtain an active material paste. A support such as a cast grid body or an expanded grid body having a thickness of 1.5 to 2 mm was filled with the paste, which was then aged and dried in an atmosphere of an appropriate temperature and humidity to obtain an electrode plate.

【0004】そして、この工程において酸化鉛(Pb
O)と希硫酸(H2SO4)の反応により3塩基性硫酸鉛
(3PbO・PbSO4)を生成しこれを元にして化成
し反応性の高い二酸化鉛(PbO2)を得るとともに、
鉛(Pb)を熟成中に酸素および水分と反応させてPb
O・H2Oを生成し活物質間の結合力を高め、さらにこ
れらの結晶の成長によって極板に適当な多孔度を得てい
た。
In this process, lead oxide (Pb
O) and dilute sulfuric acid (H 2 SO 4 ) react to produce tribasic lead sulfate (3PbO · PbSO 4 ) and form chemical compound based on this to obtain highly reactive lead dioxide (PbO 2 ).
Lead (Pb) reacts with oxygen and moisture during aging to produce Pb
Generate O · H 2 O to increase the binding force between active materials, had gained appropriate porosity electrode plate by further growth of these crystals.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、従来の
ような方法によって作製した活物質ペーストを薄い支持
体表面に塗着して薄形極板を得ようとした場合、硫酸の
添加による硫酸鉛の生成によって活物質ペースト粒子の
凝集が起こり、粗大な凝固塊が多数存在するために支持
体表面にペーストを薄く塗り込むことができなく塗着作
業が困難でなるという問題が生じていた。
However, when an active material paste prepared by a conventional method is applied to the surface of a thin support to obtain a thin electrode plate, the addition of sulfuric acid causes the formation of lead sulfate. The generation of the active material paste particles causes agglomeration, and since a large number of coarse coagulated masses are present, the paste cannot be thinly applied to the surface of the support, which causes a problem that the application work is difficult.

【0006】本発明はこのような課題を解決するもので
あり、薄い支持体の表面に薄い活物質層を形成すること
ができるとともに、3PbO・PbSO4およびPbO
・H2Oなどの生成により反応性と結合性に優れた鉛蓄
電池用極板を提供するものである。
The present invention is intended to solve such a problem, and it is possible to form a thin active material layer on the surface of a thin support and to obtain 3PbO.PbSO 4 and PbO.
-Provides an electrode plate for a lead storage battery, which is excellent in reactivity and bondability due to generation of H 2 O and the like.

【0007】[0007]

【課題を解決するための手段】上記の課題を解決するた
めに、本発明の鉛蓄電池用極板の製造法は、硫酸を加え
ずに鉛粉と水とを主成分とした鉛化合物のスラリーを作
製する工程と、このスラリーを支持体に塗着する工程
と、スラリーを塗着した支持体を希硫酸に浸漬する工程
と、希硫酸中からスラリーを塗着した支持体を取り出
し、これを空気中で熟成する工程とからなるものであ
る。
In order to solve the above-mentioned problems, a method of manufacturing an electrode plate for a lead storage battery according to the present invention is a slurry of a lead compound containing lead powder and water as main components without adding sulfuric acid. And a step of applying the slurry to a support, a step of immersing the support applied with the slurry in dilute sulfuric acid, and taking out the support applied with the slurry from dilute sulfuric acid. And aging in air.

【0008】[0008]

【作用】本発明では、活物質である鉛粉と水とを主成分
として硫酸を加えずに混合しているので、硫酸鉛の生成
による凝固塊の発生はなくこれらの混合状態は活物質粒
子が水中に懸濁しているスラリー状態になる。このた
め、活物質のスラリーを細孔を有する薄厚の多孔体から
なる支持体に塗着する際には、活物質の薄層を支持体上
に形成しやすくなり多孔度も適度に保つことができる。
In the present invention, since lead powder, which is an active material, and water are mixed as main components without adding sulfuric acid, solidified lumps are not generated due to the production of lead sulfate, and the mixed state of these is the active material particles. Is suspended in water and becomes a slurry state. Therefore, when the slurry of the active material is applied to the support made of a thin porous body having pores, it is easy to form a thin layer of the active material on the support, and the porosity can be appropriately maintained. it can.

【0009】ついで、スラリーを支持体に塗着した後、
この支持体を希硫酸中に浸漬しているので、鉛粉の酸化
鉛が硫酸鉛に変化し、活物質層は硬化し始め、活物質間
の結合力は高まる。
Then, after applying the slurry to the support,
Since this support is immersed in dilute sulfuric acid, the lead oxide in the lead powder changes to lead sulfate, the active material layer begins to harden, and the binding force between the active materials increases.

【0010】その後、この支持体を例えば温度40℃〜
80℃,湿度80%〜100%の空気中で熟成している
ので、酸化鉛と希硫酸との反応により三塩基性硫酸鉛を
生成することができ、電池充放時の二酸化鉛の反応性を
高めることができる。
Thereafter, the support is heated to, for example, a temperature of 40.degree.
Since it is aged in air at 80 ° C and humidity of 80% to 100%, tribasic lead sulfate can be produced by the reaction of lead oxide and dilute sulfuric acid, and the reactivity of lead dioxide during battery charge and discharge. Can be increased.

【0011】また、このとき、未酸化鉛の酸化によって
さらに活物質間の結合力を高めることができる。したが
って、本発明では活物質である鉛粉をスラリー状態で支
持体に薄く塗着することができるとともに、その後、こ
の支持体を希硫酸中に浸漬してさらに空気中で熟成して
いるので活物質間の結合力を高めるとともに三塩基性硫
酸鉛の生成によって反応性の高い二酸化鉛を得ることが
できる。
At this time, the bond strength between the active materials can be further increased by the oxidation of the unoxidized lead. Therefore, in the present invention, the lead powder, which is the active material, can be thinly applied to the support in a slurry state, and thereafter the support is immersed in dilute sulfuric acid and further aged in the air. It is possible to obtain highly reactive lead dioxide by increasing the bond strength between substances and forming tribasic lead sulfate.

【0012】[0012]

【実施例】以下、本発明の実施例を図面を参照にしなが
ら説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0013】図1に本発明の鉛蓄電池用極板の製造法を
示す。図1において、1は鉛粉、2は耐酸性導電材,糊
剤,樹脂のカット繊維等の添加物、3は水、4はこれら
を混合してスラリーを調整する工程、5は支持体にスラ
リーを塗着する工程、6は乾燥工程、7はスラリーを塗
着した支持体を希硫酸中に浸漬する工程、8は希硫酸中
から取り出した支持体を空気中で放置して熟成する工程
である。
FIG. 1 shows a method of manufacturing the lead-acid battery electrode plate of the present invention. In FIG. 1, 1 is lead powder, 2 is an additive such as acid-resistant conductive material, sizing agent, resin cut fiber, etc., 3 is water, 4 is a process of mixing these to prepare a slurry, and 5 is a support. Step of applying the slurry, 6 is a drying step, 7 is a step of immersing the support on which the slurry is applied in dilute sulfuric acid, and 8 is a step of aging the support taken out from the dilute sulfuric acid in the air. Is.

【0014】ここで、鉛粉には酸化度50%〜90%の
鉛粉を用いた。また、水分を鉛粉重量に対して10%〜
100%の割合で添加した。そして、鉛粉に対して40
重量%の水を加え、上記の工程によって得た正極板を正
極板A、極板の化成を促進するために有効な鉛丹(Pb
3O4)を鉛粉に対して20重量%混合したものに40重
量%の水を加え上記の工程によって得た正極板を正極板
B、耐酸性導電材として炭素粉末を鉛粉に対して5重量
%加えた正極板を正極板Cとした。
Here, as the lead powder, a lead powder having an oxidation degree of 50% to 90% was used. Also, the water content is 10% to the weight of the lead powder.
It was added at a rate of 100%. And 40 for lead powder
The positive electrode plate obtained by the above process is added to the positive electrode plate A, which is effective for promoting chemical conversion of the positive electrode plate (Pb).
3 O 4 ) was mixed with 20% by weight of lead powder, and 40% by weight of water was added, and the positive electrode plate obtained by the above process was used as the positive electrode plate B. The positive electrode plate added with 5% by weight was designated as positive electrode plate C.

【0015】また、支持体としては0.3mm×0.3
mmの菱形孔部を有し厚み0.2mmの鉛合金製のエキ
スパンド多孔体を用い、これに図3(A)に示したよう
にスラリーを100mg/cm2で厚み180μm塗着
した。
As a support, 0.3 mm × 0.3
An expanded porous body made of lead alloy and having a rhombic hole portion of 0.2 mm and a thickness of 0.2 mm was used, and the slurry was applied at a thickness of 100 mg / cm 2 and a thickness of 180 μm as shown in FIG. 3 (A).

【0016】このように、本発明の製造法では厚みの薄
い極板を作製することができた。ついで、スラリーを塗
着した支持体を比重1.4の希硫酸中に30秒間浸漬し
た。そして、希硫酸中から取り出した支持体を温度40
℃〜80℃,湿度80%〜100%の雰囲気中で数時間
〜数十時間放置して熟成した。
As described above, according to the manufacturing method of the present invention, a thin electrode plate can be manufactured. Then, the support coated with the slurry was immersed in dilute sulfuric acid having a specific gravity of 1.4 for 30 seconds. Then, the support taken out from the diluted sulfuric acid was heated to a temperature of 40
It was aged for several hours to several tens of hours in an atmosphere of 80 ° C to 80 ° C and humidity of 80% to 100%.

【0017】一方、負極板は、鉛粉に対して炭素粉末を
5重量%、リグニンスルホン酸塩を2〜4重量%、水を
40重量%加えたスラリーを用いて作製した。
On the other hand, the negative electrode plate was prepared by using a slurry in which 5% by weight of carbon powder, 2 to 4% by weight of lignin sulfonate and 40% by weight of water were added to lead powder.

【0018】そして、各正極板A,B,Cに前記負極板
を組み合わせて2V25mAhの鉛蓄電池を作製し、こ
れらを本発明の電池A,B,Cを作製した。
Then, each of the positive electrode plates A, B and C was combined with the negative electrode plate to prepare a lead storage battery of 2V25 mAh, and these were prepared into batteries A, B and C of the present invention.

【0019】そして、これらの電池を比重1.20の希
硫酸中で化成して電流密度25mA/cm2で放電した
際の放電電圧の変化を調べた。この結果を図4に示す。
Then, the change in discharge voltage when these batteries were formed in diluted sulfuric acid having a specific gravity of 1.20 and discharged at a current density of 25 mA / cm 2 was examined. The result is shown in FIG.

【0020】図4に示したように電池Aは良好な放電特
性を示したが、化成時の充電性の良い鉛丹を含む正極板
を用いた電池Bと、これに導電性粒子として炭素粉末を
加えた正極板を用いた電池Cがさらに電池Aより放電電
圧,放電時間ともに高くなった。
As shown in FIG. 4, the battery A showed good discharge characteristics, but the battery B using the positive electrode plate containing lead tin, which has good chargeability during formation, and the carbon powder as the conductive particles. The discharge voltage and the discharge time of the battery C using the positive electrode plate added with were higher than those of the battery A.

【0021】これに対して、図2に示したように鉛粉
1,添加物2,水3,希硫酸9を混合してペーストを練
合する工程10と、ペーストを支持体に塗着する工程1
1と、乾燥工程6と、熟成工程8とからなる従来の製造
法によって、厚み0.2mmの鉛合金製のエキスパンド
多孔体からなる支持体にペーストを塗着して極板を得よ
うと試みたが、硫酸鉛の生成によってペースト粒子の凝
集した粗大な塊が多数発生し、支持体上にペーストをう
まく塗り込むことができなかった。
On the other hand, as shown in FIG. 2, a step 10 of mixing lead powder 1, an additive 2, water 3, and dilute sulfuric acid 9 to knead the paste, and applying the paste to a support. Process 1
An attempt was made to obtain a polar plate by applying a paste to a support made of a lead alloy expanded porous body having a thickness of 0.2 mm by a conventional manufacturing method consisting of 1, a drying step 6, and an aging step 8. However, due to the formation of lead sulfate, a large number of coarse aggregates of paste particles were generated, and the paste could not be successfully applied onto the support.

【0022】ついで、前記正極板B中にさらにシリカ粉
末5重量%と澱粉性糊剤1重量%加えた正極板を用いて
電池Dを作製し、電池A,B,Dを用いて充放電サイク
ル寿命試験を行った。
Then, a battery D was prepared by using a positive electrode plate in which 5% by weight of silica powder and 1% by weight of a starch sizing agent were further added to the positive electrode plate B, and the batteries A, B and D were used for charge / discharge cycles. A life test was conducted.

【0023】この試験は、電流密度25mA/cm2で
前回放電量の125%の充電と完全放電量の20%の放
電により行った。
This test was carried out at a current density of 25 mA / cm 2 by charging 125% of the previous discharge amount and discharging 20% of the complete discharge amount.

【0024】この結果を図5に示す。図5に示したよう
に、電池Aは良好なサイクル特性を示したが、電池B,
Dではさらにサイクル経過時の容量が高かった。
The results are shown in FIG. As shown in FIG. 5, although the battery A showed good cycle characteristics, the battery B,
In D, the capacity after the lapse of cycles was higher.

【0025】次にスラリーを塗着した支持体の希硫酸中
での浸漬工程における希硫酸の比重と極板の浸漬時間と
の関係を調べた。
Next, the relationship between the specific gravity of dilute sulfuric acid in the dipping process of the support coated with the slurry in dilute sulfuric acid and the dipping time of the electrode plate was investigated.

【0026】この結果を図6に示す。ここで、T1,T
2,T3,T4,T5はそれぞれ希硫酸中での浸漬時間
を30秒,1分,5分,10分,60分としたものであ
る。
The results are shown in FIG. Where T1, T
Nos. 2, T3, T4, and T5 have immersion times in dilute sulfuric acid of 30 seconds, 1 minute, 5 minutes, 10 minutes, and 60 minutes, respectively.

【0027】図6からわかるように希硫酸の比重が高く
なるにともなって希硫酸中での浸漬時間を短くしても極
板の活物質利用率は向上した。
As can be seen from FIG. 6, as the specific gravity of dilute sulfuric acid increased, the active material utilization rate of the electrode plate improved even when the dipping time in dilute sulfuric acid was shortened.

【0028】なお、本実施例ではスラリーを塗着した支
持体を希硫酸中に浸漬したが、この支持体に希硫酸のシ
ャワーや噴霧を付与して希硫酸処理を行っても良い。
In this embodiment, the support coated with the slurry was immersed in dilute sulfuric acid, but a dilute sulfuric acid treatment may be performed by applying a shower or spray of dilute sulfuric acid to this support.

【0029】また、鉛粉に添加する添加物は本実施例以
外に極板の多孔度を良好に保つための酸化カルシウム粒
子や、負極に添加するリグニンとその誘導体および硫酸
バリウム等であっても良い。
Further, the additive added to the lead powder may be calcium oxide particles for maintaining good porosity of the electrode plate, lignin and its derivative, barium sulfate, etc. added to the negative electrode, in addition to the present embodiment. good.

【0030】さらに、本実施例では支持体としてエキス
パンド多孔体を用いたが、図3(B)に示したように薄
板に開孔部を設けたパンチングメタル等の他の支持体で
あっても良い。
Further, although the expanded porous body is used as the support in this embodiment, other supports such as punching metal having a thin plate provided with openings as shown in FIG. 3B may be used. good.

【0031】[0031]

【発明の効果】以上のように本発明では活物質である鉛
粉と水とを主成分としてスラリーを作製し、このスラリ
ーを支持体に塗着しているので、支持体上に活物質の薄
層を形成することができ、電池の高出力化を達成でき
る。
INDUSTRIAL APPLICABILITY As described above, in the present invention, a slurry is prepared by using lead powder which is an active material and water as main components, and this slurry is applied to a support. A thin layer can be formed, and high output of the battery can be achieved.

【0032】また、スラリーを塗着した支持体を希硫酸
中に浸漬し、ついで空気中でこの支持体を熟成すること
により、反応性の高い二酸化鉛を得るための三塩基性硫
酸鉛の生成や活物質間の結合力を高める酸化鉛の生成を
進めることができる。
Further, the support coated with the slurry is dipped in dilute sulfuric acid, and then the support is aged in air to form tribasic lead sulfate for obtaining highly reactive lead dioxide. It is possible to promote the production of lead oxide which enhances the bonding force between the active materials.

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

【図1】本発明の鉛蓄電池用極板の製造工程を示す図FIG. 1 is a diagram showing a manufacturing process of an electrode plate for a lead storage battery of the present invention.

【図2】従来の鉛蓄電池用極板の製造工程を示す図FIG. 2 is a diagram showing a manufacturing process of a conventional electrode plate for a lead storage battery.

【図3】(A) エキスパンド多孔体を用いた本発明の
極板の側面図 (B) パンチングメタルを用いた本発明の極板の側面
図
FIG. 3A is a side view of the electrode plate of the present invention using an expanded porous body. FIG. 3B is a side view of the electrode plate of the present invention using a punching metal.

【図4】本発明の鉛蓄電池の放電特性を示す図FIG. 4 is a diagram showing discharge characteristics of the lead acid battery of the present invention.

【図5】本発明の鉛蓄電池の充放電サイクル特性を示す
図
FIG. 5 is a diagram showing charge / discharge cycle characteristics of the lead acid battery of the present invention.

【図6】本発明の極板の希硫酸中での浸漬時間と希硫酸
の比重との関係を示す図
FIG. 6 is a graph showing the relationship between the immersion time of the electrode plate of the present invention in diluted sulfuric acid and the specific gravity of diluted sulfuric acid.

【符号の説明】[Explanation of symbols]

1 鉛粉 2 添加物 3 水 4 スラリー調整工程 5 スラリー塗着工程 6 乾燥工程 7 浸漬工程 8 熟成工程 9 希硫酸 10 ペースト練合工程 11 ペースト塗着工程 DESCRIPTION OF SYMBOLS 1 Lead powder 2 Additive 3 Water 4 Slurry adjusting step 5 Slurry applying step 6 Drying step 7 Immersion step 8 Aging step 9 Dilute sulfuric acid 10 Paste kneading step 11 Paste applying step

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】硫酸を加えずに鉛粉と水とを主成分とした
鉛化合物のスラリーを作製する工程と、このスラリーを
支持体に塗着する工程と、スラリーを塗着した支持体を
希硫酸に接触させる工程と、希硫酸に接触させた後、ス
ラリーを塗着した支持体を空気中で熟成する工程とから
なる鉛蓄電池用極板の製造法。
1. A step of preparing a slurry of a lead compound containing lead powder and water as main components without adding sulfuric acid, a step of applying the slurry to a support, and a step of applying the slurry to the support. A process for producing an electrode plate for a lead storage battery, which comprises a step of contacting with dilute sulfuric acid and a step of aging the support coated with the slurry in air after contacting with dilute sulfuric acid.
【請求項2】スラリーは鉛丹を含む請求項1記載の鉛蓄
電池用極板の製造法。
2. The method for producing an electrode plate for a lead storage battery according to claim 1, wherein the slurry contains red lead.
【請求項3】スラリーは耐酸性導電性粒子を含む請求項
1または2記載の鉛蓄電池用極板の製造法。
3. The method for producing an electrode plate for a lead storage battery according to claim 1, wherein the slurry contains acid resistant conductive particles.
【請求項4】希硫酸の濃度は比重1.20以上である請
求項1〜3のいずれかに記載の鉛蓄電池用極板の製造
法。
4. The method for producing a lead-acid battery electrode plate according to claim 1, wherein the concentration of the dilute sulfuric acid is 1.20 or more.
JP27917594A 1994-11-14 1994-11-14 Manufacturing method of electrode plate for lead-acid battery Expired - Fee Related JP3267075B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27917594A JP3267075B2 (en) 1994-11-14 1994-11-14 Manufacturing method of electrode plate for lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27917594A JP3267075B2 (en) 1994-11-14 1994-11-14 Manufacturing method of electrode plate for lead-acid battery

Publications (2)

Publication Number Publication Date
JPH08138657A true JPH08138657A (en) 1996-05-31
JP3267075B2 JP3267075B2 (en) 2002-03-18

Family

ID=17607495

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3267075B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006278000A (en) * 2005-03-28 2006-10-12 Furukawa Battery Co Ltd:The Method of manufacturing electrode plate for lead acid battery and lead acid battery
JP2010277807A (en) * 2009-05-28 2010-12-09 Furukawa Battery Co Ltd:The Lead-acid battery electrode and method for producing lead-acid battery electrode
CN114551815A (en) * 2022-02-16 2022-05-27 天能电池集团(马鞍山)新能源科技有限公司 Lead storage battery pole plate curing method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4523580B2 (en) * 2006-12-19 2010-08-11 エヌ・ティ・ティ・データ先端技術株式会社 Negative electrode active material for secondary battery and intermediate kneaded material for producing them

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006278000A (en) * 2005-03-28 2006-10-12 Furukawa Battery Co Ltd:The Method of manufacturing electrode plate for lead acid battery and lead acid battery
JP2010277807A (en) * 2009-05-28 2010-12-09 Furukawa Battery Co Ltd:The Lead-acid battery electrode and method for producing lead-acid battery electrode
CN114551815A (en) * 2022-02-16 2022-05-27 天能电池集团(马鞍山)新能源科技有限公司 Lead storage battery pole plate curing method
CN114551815B (en) * 2022-02-16 2023-09-22 天能电池集团(马鞍山)新能源科技有限公司 Lead storage battery polar plate curing method

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