JP3427402B2 - Method for manufacturing electrode plate for lead-acid battery - Google Patents

Method for manufacturing electrode plate for lead-acid battery

Info

Publication number
JP3427402B2
JP3427402B2 JP34374392A JP34374392A JP3427402B2 JP 3427402 B2 JP3427402 B2 JP 3427402B2 JP 34374392 A JP34374392 A JP 34374392A JP 34374392 A JP34374392 A JP 34374392A JP 3427402 B2 JP3427402 B2 JP 3427402B2
Authority
JP
Japan
Prior art keywords
lead
electrode plate
current collector
active material
lead oxide
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
JP34374392A
Other languages
Japanese (ja)
Other versions
JPH05242893A (en
Inventor
一郎 向谷
康司 松村
健介 弘中
仁彦 乾
朝比古 三浦
慎治 斉藤
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.)
Shin Kobe Electric Machinery Co Ltd
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 JP34374392A priority Critical patent/JP3427402B2/en
Publication of JPH05242893A publication Critical patent/JPH05242893A/en
Application granted granted Critical
Publication of JP3427402B2 publication Critical patent/JP3427402B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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

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、ペースト式の鉛蓄電池
極板の製造方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 paste type electrode plate for a lead storage battery.

【0002】[0002]

【従来の技術】従来の鉛蓄電池用極板は次のようにして
製造する。まず酸化鉛、水及び希硫酸を混練して活物質
ペーストを作り、この活物質ペーストを鉛または鉛合金
からなる格子体等の集電体に充填して未乾燥極板を作
る。次に、この未乾燥極板を熟成、乾燥して集電体と活
物質とを一体化した後に化成を行って完成する。
2. Description of the Related Art A conventional lead-acid battery electrode plate is manufactured as follows. First, lead oxide, water, and dilute sulfuric acid are kneaded to form an active material paste, and the active material paste is filled in a current collector such as a grid body made of lead or a lead alloy to form an undried electrode plate. Next, this undried electrode plate is aged and dried to integrate the current collector and the active material, and then chemical conversion is performed to complete the process.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、酸化
鉛、水及び希硫酸を混練した活物質ペーストは粘性が高
いため、未乾燥極板を熟成、乾燥しても活物質と集電体
とが十分に密着しないという問題がある。特に近年では
集電体として表面が平坦な圧延シートをエキスパンド加
工して形成するエキスパンド集電体が用いられているた
め、活物質ペーストと集電体の表面との密着はより一層
難くなっている。そのため、従来の極板を用いた電池に
充放電が繰り返されると、活物質が軟化して集電体表面
から脱落し易くなり、電池の充放電サイクル寿命が短く
なるという問題があった。
However, since the active material paste prepared by kneading lead oxide, water and dilute sulfuric acid has a high viscosity, the active material and the current collector will be sufficient even if the undried electrode plate is aged and dried. There is a problem of not sticking to. Particularly in recent years, since an expanded current collector formed by expanding a rolled sheet having a flat surface is used as the current collector, it is even more difficult to adhere the active material paste to the surface of the current collector. . Therefore, when the battery using the conventional electrode plate is repeatedly charged and discharged, the active material is softened and easily falls off from the surface of the current collector, which causes a problem that the charge and discharge cycle life of the battery is shortened.

【0004】尚、集電体表面の活物質の脱落を防止する
ために、極板間に介在させるセパレータとして、ガラス
繊維を主体とする弾力性に富むマット状セパレータを使
用して極板群の加圧力を高めて、活物質と集電体との密
着性を高めることにより充放電サイクルの性能の向上を
図ることが提案されている。しかしながら、この場合に
は、組立時に加圧力を高める構成とすることに多大な困
難を伴う上、工業的に量産する場合には更に改良が必要
になる。
In order to prevent the active material on the surface of the current collector from falling off, a highly elastic mat-like separator mainly made of glass fiber is used as a separator interposed between the electrode plates. It has been proposed to improve the performance of the charge / discharge cycle by increasing the applied pressure to improve the adhesion between the active material and the current collector. However, in this case, it is extremely difficult to increase the pressing force at the time of assembly, and further improvement is required in the case of industrial mass production.

【0005】また、従来の製造方法では未乾燥極板を熟
成する際に集電体の表面部ではPb+HO+1/2
→Pb(OH)→PbO+HOの反応が
起きるため、未乾燥極板を熟成させるためには多くの酸
素が必要となり、熟成に多大な時間がかかるという問題
があった。
Further, in the conventional manufacturing method, when the undried electrode plate is aged, Pb + H 2 O + 1/2 is formed on the surface of the current collector.
Since the reaction of O 2 → Pb (OH) 2 → PbO + H 2 O occurs, a large amount of oxygen is required for aging the undried electrode plate, and there is a problem that aging takes a long time.

【0006】本発明の目的は、集電体表面からの活物質
の脱落を防止でき、しかも熟成時間を短くできる鉛蓄電
池用極板の製造方法を提供することにある。
An object of the present invention is to provide a method for manufacturing a lead storage battery electrode plate which can prevent the active material from falling off from the surface of the current collector and can shorten the aging time.

【0007】[0007]

【課題を解決するための手段】請求項1の発明は、鉛ま
たは鉛合金からなる集電体の表面に、高位の鉛酸化物
(PbOx:1.13≦X≦2.0 )を水で混練したスラリと
して塗布して接触させ、前記集電体の表面部に正方晶系
鉛酸化物層を形成した後に、前記集電体に鉛酸化物を主
成分とする活物質ペーストを充填する鉛蓄電池用極板の
製造方法において、 前記高位の鉛酸化物として鉛丹を用
いることを特徴とする
According to a first aspect of the present invention , a high level lead oxide is formed on the surface of a current collector made of lead or a lead alloy .
(PbOx: 1.13 ≤ X ≤ 2.0) and a slurry kneaded with water
Then, apply and contact the surface of the current collector with a tetragonal system.
After forming the lead oxide layer, lead oxide is mainly added to the current collector.
Of a lead-acid battery electrode plate filled with an active material paste as a component
In the manufacturing method, red lead is used as the high order lead oxide.
It is characterized by being

【0008】請求項2の発明は、鉛または鉛合金からな
る集電体に、鉛丹、PbO 1.37 及びPbO から
選択した少なくとも1種の高位の鉛酸化物(PbOx:
1.13≦X≦2.0 )を主成分とし水で混練した活物質ペー
ストを充填して未乾燥極板を作った後に、前記未乾燥極
板を乾燥、熟成して前記集電体の表面部に正方晶系鉛酸
化物層を形成する鉛蓄電池用極板の製造方法において、
前記活物質ペーストにアニオン系界面活性剤を添加する
ことを特徴とする
The invention of claim 2 is made of lead or lead alloy.
In that current collector, lead, from PbO 1.37 and PbO 2
At least one selected higher lead oxide (PbOx:
1.13 ≦ X ≦ 2.0) as the main component and kneaded with water
After making the wet electrode plate by filling the strike,
The plate is dried and aged to form tetragonal lead acid on the surface of the current collector.
In the method of manufacturing a lead storage battery electrode plate for forming a compound layer,
Anionic surfactant is added to the active material paste
It is characterized by

【0009】[0009]

【作用】正方晶系鉛酸化物層は結晶構造が緻密な酸化鉛
(t−PbO、ここでtはtetoragonal のtである。)
から形成された酸化腐食層である。そのため、請求項1
の発明のように集電体の表面部に正方晶系鉛酸化物層を
形成すると集電体と活物質との密着性を高めることがで
きる。本発明の極板が正極板であれば、化成を行うと、
固相反応により集電体の表面部の正方晶系鉛酸化物層は
α−PbOを含んだ酸化鉛層となる。この酸化鉛層
は活物質と集電体との密着性を向上させる。
The tetragonal lead oxide layer has a dense crystal structure of lead oxide (t-PbO, where t is tetoragonal t).
Is an oxidative corrosion layer formed from. Therefore, claim 1
When a tetragonal lead oxide layer is formed on the surface portion of the current collector as in the invention of No. 1, the adhesion between the current collector and the active material can be enhanced. When the electrode plate of the present invention is a positive electrode plate, when chemical conversion is performed,
By the solid phase reaction, the tetragonal lead oxide layer on the surface of the current collector becomes a lead oxide layer containing α-PbO 2 . This lead oxide layer improves the adhesion between the active material and the current collector.

【0010】また、本発明の極板が負極板であれば、化
成により、集電体の表面部の正方晶系鉛酸化物層は多孔
質な海綿状の金属鉛層になる。この海面状の金属鉛層も
活物質と集電体との密着性を向上させる。
If the electrode plate of the present invention is a negative electrode plate, the tetragonal lead oxide layer on the surface of the current collector becomes a porous sponge-like metallic lead layer by chemical conversion. This sea-surface-like metallic lead layer also improves the adhesion between the active material and the current collector.

【0011】集電体の表面に高位の鉛酸化物(PbO
x:1.13≦X≦2.0 )を接触させることにより、集電体
との電気化学的な作用(局部電池)により、集電体の表
面に正方晶系鉛酸化物層を形成することができる。即ち
集電体の腐食反応はOHの拡散により進行する。イ
オンの移動、生成は水の存在下において高温ほど促進さ
れるので、高位の鉛酸化物を接触させる場合には、高温
(集電体の軟化点以下)で且つ水が存在するの条件で行
うことが好ましい。このため、結果的に電槽内のように
酸素拡散が阻害される条件においても、短時間で腐食反
応(熟成)が進む。尚、PbOxのXの範囲を1.13≦X
≦2.0 とすることにより、表1及び図1に示すように集
電体の表面部を腐食(熟成)する反応式の起電力を高く
できるので、Xをこの範囲にすると腐食を効果的に促進
することができる。
High-level lead oxide (PbO ) is formed on the surface of the current collector.
x: by contacting a 1.13 ≦ X ≦ 2.0), the electrochemical action of the current collector (local battery), it is possible to form the tetragonal lead oxide layer on the surface of the current collector. That is, the corrosion reaction of the current collector proceeds due to the diffusion of OH . The movement and generation of ions are accelerated in the presence of water at higher temperatures, so contact with high-level lead oxides should be performed at high temperatures (below the softening point of the current collector) and in the presence of water. It is preferable. Therefore, the corrosion reaction (aging) proceeds in a short time even under the condition that oxygen diffusion is hindered as in the battery case. In addition, the range of X of PbOx is 1.13 ≦ X
By setting ≦ 2.0, the electromotive force of the reaction formula that corrodes (ages) the surface part of the current collector can be increased as shown in Table 1 and FIG. 1, so if X is in this range, corrosion is effectively promoted. can do.

【0012】[0012]

【表1】 また、高位の鉛酸化物を水で混練したスラリを作り、こ
のスラリを集電体の表面に塗布することにより、高位の
酸化物を集電体の表面に容易に接触させることができ
る。
[Table 1] Further, the high lead oxide to make a slurry obtained by kneading with water, by applying this slurry on the surface of the current collector, can be easily brought into contact with high-order oxide on the surface of the current collector.

【0013】特に本発明のように、高位の鉛酸化物とし
て鉛丹を用いることにより、鉛丹は比較的容易に入手で
きるので、本発明の製造方法を簡単に実施することがで
きる。
[0013] Especially as in the present invention, by using the red lead as high lead oxide, red lead, since relatively readily available, can be easily carried out the production method of the present invention.

【0014】請求項2の発明のように、集電体に高位の
鉛酸化物(PbOx:1.13≦X≦2.0 )を主成分とし水
で混練した活物質ペーストを塗布して未乾燥極板を作る
ことにより、集電体と鉛酸化物との電気化学的な作用
(局部電池)により、未乾燥極板を熟成乾燥する際に集
電体の表面部に正方晶系鉛酸化物層が形成される。その
ため、活物質ペーストを単に塗布するという単純な作業
で集電体と活物質との間の密着性が高い極板を短時間の
熟成で製造することができる。
According to a second aspect of the present invention, the current collector is coated with an active material paste containing high-grade lead oxide (PbOx: 1.13≤X≤2.0) as a main component and kneaded with water to form a undried electrode plate. create
As a result, due to the electrochemical action of the current collector and lead oxide (local battery), a tetragonal lead oxide layer is formed on the surface of the current collector when the undried electrode plate is aged and dried. It Therefore, an electrode plate having high adhesion between the current collector and the active material can be produced in a short time by a simple operation of simply applying the active material paste.

【0015】前述したように従来では、未乾燥極板を熟
成する際に集電体の表面部はPb+HO+1/2O
→Pb(OH)→PbO+HOの反応式で
酸化し、その起電力はペースト中のHOに溶解しう
る酸素濃度等を考慮すると0.8V前後になる。これに
して、高位の鉛酸化物として鉛丹、PbO1.37
びPbOから選択した少なくとも1種を用いること
により、それぞれの高位の鉛酸化物が集電体の表面部の
鉛と反応し、PbOを生成する起電力を0.8Vより高
くすることができる。そのため従来に比べて集電体の熟
成を大きく促進することができる。例えば高位の鉛酸化
物として鉛丹(Pb)を用いると、集電体の
表面部はPb+Pb→4PbO(Pb
+4HO+2e−→3Pb(OH)+2O
H−、Pb+2OH−→PbO+HO)の反応式で
熟成し、その起電力は0.835Vとなる。また、高位
の鉛酸化物としてPbOを用いると、集電体の表面
部はPbO+Pb→2PbO(PbO+2e−
→PbO+O−、Pb+O−→PbO+2e
−)の反応式で熟成し、その起電力はでは0.834V
となる。尚、高位の鉛酸化物としてPbO1.37を用
いると希硫酸との反応でPbO1.37はα−PbO
になり、鉛丹(Pb)を用いた場合より
緻密な腐食層が集電体と活物質との界面にできる。
As described above, in the conventional case, the surface portion of the current collector is Pb + H 2 O + 1 / 2O when the undried electrode plate is aged.
It is oxidized by the reaction formula of 2 → Pb (OH) 2 → PbO + H 2 O, and its electromotive force is about 0.8 V in consideration of the oxygen concentration which can be dissolved in H 2 O in the paste. And <br/> pairs thereto, minium as high lead oxide, to use at least one selected from PbO 1.37 and PbO 2
As a result , each high-ranking lead oxide reacts with lead on the surface portion of the current collector, and the electromotive force for generating PbO can be made higher than 0.8V. Therefore, aging of the current collector can be greatly promoted as compared with the conventional case. For example, when lead oxide (Pb 3 O 4 ) is used as the high-order lead oxide, the surface portion of the current collector is Pb 3 O 4 + Pb → 4PbO (Pb 3 O).
4 + 4H 2 O + 2e- → 3Pb (OH) 2 + 2O
H−, Pb + 2OH− → PbO + H 2 O), and the electromotive force is 0.835V. When PbO 2 is used as the high-order lead oxide, the surface portion of the current collector is PbO 2 + Pb → 2PbO (PbO 2 + 2e−
→ PbO + O 2 −, Pb + O 2 − → PbO + 2e
Aged with the reaction formula of −), and its electromotive force is 0.834V
Becomes When PbO 1.37 is used as the high-ranking lead oxide, PbO 1.37 becomes α-PbO by the reaction with dilute sulfuric acid.
2 , and a denser corrosion layer than the case where lead oxide (Pb 3 O 4 ) is used is formed at the interface between the current collector and the active material.

【0016】特に本発明のように、活物質ペーストにア
ニオン系界面活性剤を添加することにより、OH−が表
面に出ているペーストの粒子がアニオン(マイナス帯電
粒子)により互いに反発し合うため粒子同志が転がり合
う様になる。そのため、活物質ペーストの集電体へのぬ
れ性が向上して、活物質ペーストがレベリング(平坦に
なる)しやすくなる。したがって本発明によれば活物質
の集電体に対する密着を極板全体に亘って略均一にする
ことができる。
[0016] Especially as in the present invention, active in material paste by adding an anionic surfactant, because the particles of the paste OH- is exposed on the surface repel each other by anionic (negatively charged particles) particles Comrades will roll each other. Therefore, the wettability of the active material paste to the current collector is improved, and the active material paste is easily leveled (flattened). Therefore, according to the present invention, the adhesion of the active material to the current collector can be made substantially uniform over the entire electrode plate.

【0017】[0017]

【実施例】以下、本発明をより具体的に説明するために
実施例を示すが、本発明はこれらの実施例によって限定
されるものではない。
EXAMPLES Examples will be shown below to more specifically describe the present invention, but the present invention is not limited to these examples.

【0018】[実施例1] 鉛−錫−カルシウム合金からなるエキスパンド格子を集
電体として用いて本発明の実施例を含む各種の正極板
(寸法86×56×2.4 mm)a〜iを作り、各極板の特性を
調べた。正極板aは集電体に一酸化鉛からなら酸化鉛8
0重量%と30%の硫酸13重量%と水7重量%とから
作成した従来の活物質ペーストを充填して作った従来の
極板である。正極板bは集電体に鉛丹80重量%と30
%の硫酸13重量%と水7重量%を混練して作成した活
物質ペーストを充填して作った従来の極板である。
Example 1 Various positive electrode plates (size 86 × 56 × 2.4 mm) a to i including the examples of the present invention were prepared by using an expanded grid made of a lead-tin-calcium alloy as a current collector. The characteristics of each electrode plate were examined. If the positive electrode plate a is made of lead monoxide for the current collector, lead oxide 8
It is a conventional electrode plate made by filling a conventional active material paste prepared from 0% by weight, 30% by weight sulfuric acid 13% by weight, and water 7% by weight. The positive electrode plate b has a collector of 80% by weight of lead tin and 30
% Of sulfuric acid and 7% by weight of water are kneaded, and the conventional electrode plate is made by filling the active material paste.

【0019】正極板cは集電体に鉛丹70重量%と水3
0重量%とを混練してなるスラリを塗布して16時間放
置して集電体の表面部に正方晶系鉛酸化物層を形成した
後に、正極板aで用いた従来の活物質ペーストを充填し
て作った本発明の実施例の極板である。正極板dは集電
体に50wt%のα−PbOと鉛丹15重量%と水35
重量%と混練してなるスラリを塗布して16時間放置し
た後に、鉛丹89重量%と水11重量%とを混練して作
成した活物質ペーストを充填して作った本発明の実施例
の極板である。正極板eは集電体に正極板cを作る際に
用いたスラリを塗布してから180℃で5分間熱処理し
た後に、鉛丹80重量%と硫酸13重量%と水7重量%
とを混練して作成した活物質ペーストを充填して作った
本発明の実施例の極板である。
The positive electrode plate c has a collector of 70% by weight of lead tin and 3 parts of water.
After applying a slurry prepared by kneading 0% by weight and standing for 16 hours to form a tetragonal lead oxide layer on the surface of the current collector, the conventional active material paste used in the positive electrode plate a was applied. It is the electrode plate of the Example of this invention produced by filling. The positive electrode plate d has a current collector of 50 wt% α-PbO 2 , 15 wt% of red lead and 35 wt.
After applying a slurry prepared by kneading with the composition of the present invention and leaving it for 16 hours, the active material paste prepared by kneading 89% by weight of red lead and 11% by weight of water was filled. It is a polar plate. The positive electrode plate e was applied with the slurry used for forming the positive electrode plate c on the current collector and then heat-treated at 180 ° C. for 5 minutes, and then 80% by weight of lead tin, 13% by weight of sulfuric acid and 7% by weight of water.
It is an electrode plate of an embodiment of the present invention, which is prepared by filling an active material paste prepared by kneading and.

【0020】正極板fは集電体に鉛丹89重量%と水1
1重量%とを混練して作成した活物質ペーストを充填し
て作った本発明の実施例の極板である。正極板gは集電
体にPbO89重量%と水11重量%とから作成し
た活物質ペーストを充填して作った本発明の実施例の極
板である。正極板hは集電体にPbO1.3789重量
%と水11重量%とを混練して作成した活物質ペースト
を充填して作った本発明の実施例の極板である。正極板
iは集電体にPbO1.3789重量%と水11重量%
とベンゼンスルホン酸塩からなるアニオン系界面活性剤
0.05重量%とを混練して作成した活物質ペーストを
充填して作った本発明の実施例の極板である。
The positive electrode plate f has a collector of 89% by weight of lead tin and 1 part of water.
1 is an electrode plate of an example of the present invention, which is prepared by filling an active material paste prepared by kneading 1% by weight. The positive electrode plate g is an electrode plate of an embodiment of the present invention, which is made by filling a current collector with an active material paste made of 89% by weight of PbO 2 and 11% by weight of water. The positive electrode plate h is an electrode plate of an embodiment of the present invention made by filling an active material paste prepared by kneading 89% by weight of PbO 1.37 and 11% by weight of water in a current collector. The positive electrode plate i has a collector of PbO 1.37 89% by weight and water 11% by weight.
It is an electrode plate of an example of the present invention made by filling an active material paste prepared by kneading and 0.05% by weight of an anionic surfactant composed of benzene sulfonate.

【0021】尚、各正極板a〜iで充填した活物質ペー
ストの量はいずれも30gであり、各正極板はいずれも
40℃で16時間放置して熟成を行った後に同一条件で
化成を行った。そして各正極板a〜iをガラス繊維の不
織布からなる電解液保持体を介してそれぞれ同種の負極
板(寸法86×56×1.6 mm)と積層してシール形鉛蓄電池
A〜Iを作り、各電池の容量試験及びサイクル試験を行
った。容量試験の試験条件は1A放電(終止電圧1.75
V)で行い、サイクル試験の試験条件は1A放電(終止
電圧1.75V)←→2.45V定電圧充電3時間(制限電流1.
4 A)とした。
The amount of the active material paste filled in each of the positive electrode plates a to i was 30 g, and each of the positive electrode plates was left to stand at 40 ° C. for 16 hours to be aged and then formed under the same conditions. went. Then, each positive electrode plate a to i is laminated with the same type of negative electrode plate (dimensions 86 × 56 × 1.6 mm) via the electrolytic solution holder made of a non-woven fabric of glass fiber to make sealed lead acid batteries A to I. A battery capacity test and a cycle test were performed. The test condition of the capacity test is 1A discharge (cutoff voltage 1.75
V), and the test condition of the cycle test is 1A discharge (end voltage 1.75V) ← → 2.45V constant voltage charge 3 hours (limit current 1.
4 A).

【0022】容量試験の結果を図2に、サイクル試験の
結果を図3に示した。図2に示すように本実施例の極板
を用いた電池C〜Iでは初期容量は5〜15%増加した。
また図3に示すようにサイクル特性も本実施例の極板を
用いた電池C〜Iは従来の極板を用いた電池A,Bに比
べ長くなる傾向にある。
The result of the capacity test is shown in FIG. 2, and the result of the cycle test is shown in FIG. As shown in FIG. 2, in the batteries C to I using the electrode plate of this example, the initial capacity increased by 5 to 15%.
Further, as shown in FIG. 3, the cycle characteristics of the batteries C to I using the electrode plate of this embodiment tend to be longer than those of the batteries A and B using the conventional electrode plate.

【0023】[実施例2] 次に本発明により負極板を製造する実施例について説明
する。負極板(寸法86×56×1.6 mm)は、鉛−錫−カル
シウム合金からなるエキスパンド格子を集電体として用
いて作成した。負極板jは酸化鉛85重量%と希硫酸9
重量%と水6重量%とを混練して作成した従来の活物質
ペーストを用いて作った従来の極板である。負極板kは
β−PbO40重量%と水60重量%とを混練して
作成したをスラリを集電体に塗布して16時間放置した
後、負極板jに用いた従来の活物質ペーストを充填して
得た本発明の実施例の極板である。そして、各負極板
j,kをガラス繊維の不織布からなる電解液保持体を介
してそれぞれ前述の試験に用いた本実施例の正極板dと
積層してシール形鉛蓄電池J,Kを作り、各電池のサイ
クル試験及びトリクル試験を行った。サイクル試験の試
験条件は、1A放電(終止電圧1.75V)←→2.45V定電
圧充電3時間(制限電流1.4 A)で行い、トリクル試験
は2.27Vの定電圧充電方式で行った。
Example 2 Next, an example of manufacturing a negative electrode plate according to the present invention will be described. The negative electrode plate (size 86 × 56 × 1.6 mm) was prepared by using an expanded grid made of a lead-tin-calcium alloy as a current collector. The negative electrode plate j was 85% by weight of lead oxide and 9% of dilute sulfuric acid.
It is a conventional electrode plate prepared by using a conventional active material paste prepared by kneading 1% by weight and 6% by weight of water. The negative electrode plate k was prepared by kneading 40% by weight of β-PbO 2 and 60% by weight of water. The slurry was applied to the current collector and left for 16 hours, and then the conventional active material paste used for the negative electrode plate j was used. 2 is an electrode plate of an example of the present invention obtained by filling Then, each of the negative electrode plates j and k is laminated with the positive electrode plate d of this embodiment used in the above-mentioned test through the electrolytic solution holder made of a non-woven fabric of glass fiber to form sealed lead-acid batteries J and K, A cycle test and a trickle test of each battery were performed. The test conditions of the cycle test were 1 A discharge (final voltage 1.75 V) ← → 2.45 V constant voltage charging for 3 hours (limit current 1.4 A), and the trickle test was 2.27 V constant voltage charging method.

【0024】図4に、サイクル試験の結果を示した。図
示のように正極板と負極板に本発明の極板を適用する
と、正極板に本発明の極板を用いた場合と比べて電池の
サイクル寿命を更に改善することができる。
FIG. 4 shows the result of the cycle test. When the electrode plate of the present invention is applied to the positive electrode plate and the negative electrode plate as shown in the figure, the cycle life of the battery can be further improved as compared with the case where the electrode plate of the present invention is used for the positive electrode plate.

【0025】図5に、従来の負極板と本実施例の負極板
のトリクル電流の比較結果を示す。図から、本実施例の
極板を用いれば電池のトリクル電流を低減できるのが判
る。次に集電体に鉛丹と水とを混練してなるスラリを塗
布した後に施す温度と、熟成時における集電体の表面に
形成される一酸化鉛層の厚みの経時変化との関係を調べ
た。極板lは集電体に鉛丹50重量%と水50重量%と
を混練してなるスラリを塗布した後に180℃で3分間
の熱処理を施した極板である。極板mは熱処理を施さな
い極板であり、熱処理以外は極板lと同様にして作っ
た。そして、各極板l,mに酸化鉛80重量%と30%
の硫酸13重量%と水7重量%とから作成した従来の活
物質ペーストを充填し、熟成時における一酸化鉛層の厚
みの経時変化を測定した。図6はその測定結果を示して
いる。尚、本図には前述の試験に用いた従来の正極板a
の測定結果も合わせて示している。本図より集電体にス
ラリを塗布した後に熱処理を施すと短時間で一酸化鉛層
の厚みを厚くできるのが判る。
FIG. 5 shows the results of comparison of the trickle currents of the conventional negative electrode plate and the negative electrode plate of this embodiment. From the figure, it can be seen that the trickle current of the battery can be reduced by using the electrode plate of this embodiment. Next, the relationship between the temperature applied after applying the slurry prepared by kneading lead tin and water to the current collector and the change with time in the thickness of the lead monoxide layer formed on the surface of the current collector during aging Examined. The electrode plate 1 is an electrode plate obtained by applying a slurry prepared by kneading 50% by weight of lead tin and 50% by weight of water to a current collector and then performing heat treatment at 180 ° C. for 3 minutes. The electrode plate m is an electrode plate that is not heat-treated, and was made in the same manner as the electrode plate 1 except for the heat treatment. And, 80% by weight and 30% by weight of lead oxide are applied to each electrode plate 1 and m.
A conventional active material paste prepared from 13% by weight of sulfuric acid and 7% by weight of water was filled, and the change in thickness of the lead monoxide layer during aging was measured. FIG. 6 shows the measurement result. In this figure, the conventional positive electrode plate a used in the above-mentioned test is shown.
The measurement results of are also shown. From this figure, it can be seen that the thickness of the lead monoxide layer can be increased in a short time by applying heat treatment after applying the slurry to the current collector.

【0026】次に、従来の活物質ペーストを用いて作っ
た前述の従来の正極板aと、集電体に鉛丹と水とを混練
してなるスラリを塗布してから熱処理した後に鉛丹を含
む活物質ペーストを充填して作った前述の実施例の正極
板eと、正極板eに充填する活物質ペーストを酸化鉛8
0重量%と30%の硫酸13重量%と水7重量%とから
作成した従来の活物質ペーストに変えて充填して作った
正極板nとからそれぞれ電池A,E,Nを作り、各電池
の容量回復性を調べた。試験条件は各電池を0.5オー
ム定抵抗で24時間放置した後に25±2℃雰囲気中で
3ケ月回路状態で放置し、その後に2.45V(制限電
流1.2A)で4時間充電してから、0.25CAで放
電して測定した。図7はその測定結果を示している。本
図より実施例の極板e,nを用いると回復性能の優れた
電池を得ることができるのが判る。
Next, the above-mentioned conventional positive electrode plate a prepared by using the conventional active material paste, and a slurry prepared by kneading lead tin and water on the current collector are applied and heat-treated, and then lead tin The positive electrode plate e of the above-described embodiment made by filling the active material paste containing
Batteries A, E, and N were made from the positive electrode plates n prepared by replacing the conventional active material paste prepared from 13% by weight of sulfuric acid (0% by weight and 30% by weight) and 7% by weight of water. Was investigated for capacity recovery. The test conditions were that each battery was left for 24 hours at a constant resistance of 0.5 ohm, then left in a circuit condition for 3 months in an atmosphere of 25 ± 2 ° C., and then charged at 2.45 V (limit current 1.2 A) for 4 hours. Then, it was discharged at 0.25 CA and measured. FIG. 7 shows the measurement result. From this figure, it can be seen that a battery having excellent recovery performance can be obtained by using the electrode plates e and n of the embodiment.

【0027】[0027]

【発明の効果】請求項1の発明によれば、集電体の表面
部に結晶構造が緻密な酸化鉛(t−PbO)から形成さ
れている正方晶系鉛酸化物層を形成するため、集電体と
活物質との密着性を高めることができる。したがって本
発明によれば電池のサイクル特性及びトリクル特性を向
上できる極板を得ることができる。
According to the invention of claim 1, since a tetragonal lead oxide layer having a dense crystal structure made of lead oxide (t-PbO) is formed on the surface of the current collector, Adhesion between the current collector and the active material can be improved. Therefore, according to the present invention, it is possible to obtain an electrode plate that can improve the cycle characteristics and trickle characteristics of the battery.

【0028】また、集電体の表面に高位の酸化物(Pb
Ox:1.13≦X≦2.0 )を接触させるため、集電体との
電気化学的な作用(局部電池)により、集電体の表面部
に正方晶系鉛酸化物層を形成することができる。
[0028] In addition, oxide of high-level on the surface of the current collector (Pb
Ox: 1.13 ≦ X ≦ 2.0), so that a tetragonal lead oxide layer can be formed on the surface portion of the current collector by an electrochemical action (local battery) with the current collector.

【0029】また、高位の鉛酸化物のスラリを作り、こ
れを集電体の表面に塗布するので集電体の表面に高位の
酸化物を容易に接触させることができる。
Further , since a high-level lead oxide slurry is prepared and applied to the surface of the current collector, the high-level oxide can be easily brought into contact with the surface of the current collector.

【0030】特に本発明では、高位の鉛酸化物として鉛
丹を用いるので、本発明の製造方法を簡単に実施するこ
とができる。
Particularly, in the present invention, since lead oxide is used as the high-ranking lead oxide, the production method of the present invention can be easily carried out.

【0031】請求項2の発明によれば、集電体に高位の
鉛酸化物(PbOx:1.13≦X≦2.0 )を主成分とし水
で混練した活物質ペーストを塗布して未乾燥極板を作る
ので集電体と鉛酸化物との電気化学的な作用(局部電
池)により、未乾燥極板を熟成乾燥する際に集電体の表
面部に正方晶系鉛酸化物層が形成される。そのため、活
物質ペーストを単に塗布するだけで集電体と活物質との
密着性の高い極板を短時間の熟成で製造することができ
る。
According to the second aspect of the present invention, the current collector is coated with an active material paste containing high-grade lead oxide (PbOx: 1.13≤X≤2.0) as a main component and kneaded with water to form a undried electrode plate. Because of the electrochemical action of the current collector and lead oxide (local battery), a tetragonal lead oxide layer is formed on the surface of the current collector when the undried electrode plate is aged and dried. . Therefore, an electrode plate having high adhesion between the current collector and the active material can be manufactured in a short time by simply applying the active material paste.

【0032】また、高位の鉛酸化物として鉛丹、PbO
1.37及びPbOから選択した少なくとも1種を
用いるので、それぞれの高位の鉛酸化物が集電体の表面
部の鉛と反応し、PbOを生成する起電力を高くするこ
とができる。そのため従来に比べて集電体の熟成を大き
く促進することができる。
Further , as high-ranking lead oxide, red lead and PbO
Since at least one selected from 1.37 and PbO 2 is used, each high-order lead oxide can react with lead on the surface portion of the current collector to increase the electromotive force that produces PbO. Therefore, aging of the current collector can be greatly promoted as compared with the conventional case.

【0033】特に本発明では、活物質ペーストにアニオ
ン系界面活性剤を添加するので、活物質の集電体に対す
る密着を極板全体に亘って略均一にすることができる。
Particularly in the present invention, since the anionic surfactant is added to the active material paste, the adhesion of the active material to the current collector can be made substantially uniform over the entire electrode plate.

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

【図1】本発明の極板に用いる高位の酸化物PbOxの
Xの限定範囲を示す線図である。
FIG. 1 is a diagram showing a limited range of X in a high-order oxide PbOx used for an electrode plate of the present invention.

【図2】本発明の実施例の正極板を用いた電池と従来の
正極板を用いた電池の初期容量比較図である。
FIG. 2 is a comparison diagram of initial capacities of a battery using a positive electrode plate of an example of the present invention and a battery using a conventional positive electrode plate.

【図3】本発明の実施例の正極板を用いた電池と従来の
正極板を用いた電池の放電サイクル試験比較図である。
FIG. 3 is a comparison diagram of discharge cycle tests of a battery using a positive electrode plate of an example of the present invention and a battery using a conventional positive electrode plate.

【図4】本発明の実施例の負極板を用いた電池と従来の
負極板を用いた電池のサイクル試験比較図である。
FIG. 4 is a cycle test comparison diagram of a battery using the negative electrode plate of the example of the present invention and a battery using the conventional negative electrode plate.

【図5】本発明の実施例の負極板を用いた電池と従来の
負極板を用いた電池のトリクル電流比較図である。
FIG. 5 is a trickle current comparison diagram of a battery using the negative electrode plate of the example of the present invention and a battery using the conventional negative electrode plate.

【図6】集電体に鉛丹スラリ層をプレコーティングした
後に加熱する温度と、熟成時における集電体の表面に形
成される一酸化鉛層の厚みの経時変化との関係を示す図
である。
FIG. 6 is a diagram showing a relationship between a temperature at which a current collector is pre-coated with a red lead slurry layer and heating, and a change with time in the thickness of a lead monoxide layer formed on the surface of the current collector during aging. is there.

【図7】本発明の実施例の正極板を用いた電池と従来の
正極板を用いた電池の容量回復性を示す図である。
FIG. 7 is a diagram showing capacity recoverability of a battery using a positive electrode plate of an example of the present invention and a battery using a conventional positive electrode plate.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 乾 仁彦 東京都新宿区西新宿二丁目1番1号 新 神戸電機株式会社内 (72)発明者 三浦 朝比古 東京都新宿区西新宿二丁目1番1号 新 神戸電機株式会社内 (72)発明者 斉藤 慎治 東京都新宿区西新宿二丁目1番1号 新 神戸電機株式会社内 (56)参考文献 特開 昭53−3631(JP,A) 特開 昭60−86757(JP,A) 特開 昭63−66852(JP,A) 特開 昭55−163769(JP,A) (58)調査した分野(Int.Cl.7,DB名) H01M 4/64 - 4/84 H01M 4/14 - 4/23 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshihiko Inui 1-1-1, Nishi-Shinjuku, Shinjuku-ku, Tokyo Within Kobe Electric Co., Ltd. (72) Inventor Miura Asahiko 2-chome, Nishi-Shinjuku, Shinjuku-ku, Tokyo No. 1 in Shin-Kobe Electric Co., Ltd. (72) Inventor Shinji Saito No. 1-1-1, Nishi-Shinjuku, Shinjuku-ku, Tokyo Inside Shin-Kobe Electric Co., Ltd. (56) Reference JP-A-53-3631 (JP, A) JP-A-60-86757 (JP, A) JP-A-63-66852 (JP, A) JP-A-55-163769 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) H01M 4/64-4/84 H01M 4/14-4/23

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 鉛または鉛合金からなる集電体の表面
に、高位の鉛酸化物(PbOx:1.13≦X≦2.0 )を水
で混練したスラリとして塗布して接触させ、前記集電体
の表面部に正方晶系鉛酸化物層を形成した後に、前記集
電体に鉛酸化物を主成分とする活物質ペーストを充填す
る鉛蓄電池用極板の製造方法において、 前記高位の鉛酸化物として鉛丹を用いることを特徴とす
る鉛蓄電池用極板の製造方法
1. A surface of a current collector made of lead or a lead alloy.
High lead oxide (PbOx: 1.13 ≦ X ≦ 2.0) in water
Is applied as a slurry kneaded with and brought into contact with the current collector.
After forming a tetragonal lead oxide layer on the surface of the
Fill an electric conductor with an active material paste containing lead oxide as the main component
A method of manufacturing a lead-acid battery electrode plate according to claim 1, wherein lead oxide is used as the high-order lead oxide.
A method for manufacturing a lead-acid battery electrode plate .
【請求項2】 鉛または鉛合金からなる集電体に、鉛
丹、PbO 1.37 及びPbO から選択した少なく
とも1種の高位の鉛酸化物(PbOx:1.13≦X≦2.0
)を主成分とし水で混練した活物質ペーストを充填し
て未乾燥極板を作った後に、前記未乾燥極板を乾燥、熟
成して前記集電体の表面部に正方晶系鉛酸化物層を形成
する鉛蓄電池用極板の製造方法において、 前記活物質ペーストにアニオン系界面活性剤を添加する
ことを特徴とする鉛蓄電池用極板の製造方法。
2. A current collector comprising lead or lead alloy, lead
Tan, PbO 1.37 and PbO 2 selected less
Both are high-grade lead oxides (PbOx: 1.13 ≦ X ≦ 2.0
) As the main component and filled with an active material paste kneaded with water.
After making the undried electrode plate, dry and ripen the undried electrode plate.
Forming a tetragonal lead oxide layer on the surface of the current collector
In the method for producing a lead-acid battery electrode plate, a method for producing a lead-acid battery electrode plate, characterized in that an anionic surfactant is added to the active material paste .
JP34374392A 1991-12-26 1992-12-24 Method for manufacturing electrode plate for lead-acid battery Expired - Fee Related JP3427402B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34374392A JP3427402B2 (en) 1991-12-26 1992-12-24 Method for manufacturing electrode plate for lead-acid battery

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP3-344468 1991-12-26
JP34446891 1991-12-26
JP34374392A JP3427402B2 (en) 1991-12-26 1992-12-24 Method for manufacturing electrode plate for lead-acid battery

Publications (2)

Publication Number Publication Date
JPH05242893A JPH05242893A (en) 1993-09-21
JP3427402B2 true JP3427402B2 (en) 2003-07-14

Family

ID=27624579

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34374392A Expired - Fee Related JP3427402B2 (en) 1991-12-26 1992-12-24 Method for manufacturing electrode plate for lead-acid battery

Country Status (1)

Country Link
JP (1) JP3427402B2 (en)

Also Published As

Publication number Publication date
JPH05242893A (en) 1993-09-21

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