JPH03203158A - Lead-acid battery - Google Patents

Lead-acid battery

Info

Publication number
JPH03203158A
JPH03203158A JP1340448A JP34044889A JPH03203158A JP H03203158 A JPH03203158 A JP H03203158A JP 1340448 A JP1340448 A JP 1340448A JP 34044889 A JP34044889 A JP 34044889A JP H03203158 A JPH03203158 A JP H03203158A
Authority
JP
Japan
Prior art keywords
lead
formation
mat
carbon
conductive
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.)
Pending
Application number
JP1340448A
Other languages
Japanese (ja)
Inventor
Takeshi Hirakawa
平川 武
Imakichi Hirasawa
今吉 平沢
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 JP1340448A priority Critical patent/JPH03203158A/en
Publication of JPH03203158A publication Critical patent/JPH03203158A/en
Pending 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

Landscapes

  • Cell Separators (AREA)

Abstract

PURPOSE:To enhance formation efficiency and to lengthen life by using a positive plate containing conductive fibers made of lead or carbon and also using a conductive mat on the surface in contact with the positive plate. CONSTITUTION:A carbon fiber layer 3 is positioned on the side in contact with a positive plate of a glass mat 2 and a separator 1 is attached to the glass mat 2. Carbon fibers each having a specified diameter are entangled and stacked on a 0.8mm thick glass mat, for example, and they are compressed so as to have the total thickness of 1.0mm, then the separator 1 made of reinforced fibers is sticked thereon. A positive plate is formed in such a way that carbon fibers are added to lead powder, and they are kneaded with dilute sulfuric acid to prepare active material paste, then the paste is filled in a lead alloy grid. Part of formation current is used for the formation of an active material near the grid and the residual current reaches the surface of the positive plate from the grid through the carbon fibers 3 and is used for the formation of the positive through the mat or a conductive porous sheet. Formation is advanced through the both passages and its efficiency is enhanced. The formation is conducted by small amount of electricity in a short time and the life of a battery is equal to or longer than ordinary batteries.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は鉛蓄電池に関する。[Detailed description of the invention] Industrial applications The present invention relates to lead acid batteries.

従来技術 鉛電池の未化成極板は、一般には鉛合金から成る格子体
に鉛ペースト(鉛粉を希硫酸で練ったもの)を塗布した
後、熟成、乾燥の各工程を経て作られる。このとき、陰
極用鉛ペースト中には防縮剤としてリグニン、硫酸バリ
ウムが添加される。リグニンは、陰極の性能を長期間維
持するための重要な添加剤であるが、化成がされにくく
なるため、これらに加えてアセチレンブラックなどのカ
ーボンブラックも同時に添加されるのが一般的である。
Conventional unformed electrode plates for lead batteries are generally made by applying lead paste (lead powder kneaded with dilute sulfuric acid) to a lattice made of lead alloy, followed by aging and drying steps. At this time, lignin and barium sulfate are added to the cathode lead paste as an antishrink agent. Lignin is an important additive for maintaining the performance of the cathode for a long period of time, but since it is difficult to undergo chemical conversion, carbon black such as acetylene black is also generally added at the same time.

これに対して、陽極用鉛ペースト中には活物質の脱落防
止用の繊維以外、特に何も添加しないことが多い。
On the other hand, in most cases, nothing is added to the lead paste for anode except for fibers to prevent the active material from falling off.

上記未化成極板は、一般に1日あるいは2日間かけて、
十分な電気量を用いて化成される。
The above-mentioned unformed electrode plate is generally processed for one or two days.
It is chemically formed using a sufficient amount of electricity.

ここで、原価低減などを目的に短時間で化成しようとす
ると、陽極の化成が不十分となり、活物質中に未化成の
硫酸鉛が残留したり、陽極板の表面に硫酸鉛が白色状態
で多量に残留したりする。特に、後者の現象は、著しい
外観不良に発展する。これらの現象を防止する手段とし
て、従来、陽極用鉛ペースト中へのアセチレンブラック
などのカーボンブラック、カーボン繊維、あるいは鉛丹
などの添加が検討されている。これらの添加物はいずれ
も、ペースト中に格子体以外の電子伝導性のネットワー
クを形成し、化成効率を上げてやろうというものである
。カーボンブラックどカーボン繊維は、耐酸、耐酸化性
の電子伝導性材料として選定されたものであり、鉛丹は
化成液である希硫酸との化学反応によって二酸化鉛を生
成し、これがペースト中に電子伝導性を与えることにな
る。たとえば、カーボン繊維の添加については、特公昭
38−14425号公報などに記載されている。
If an attempt is made to chemically form the anode in a short period of time for the purpose of reducing costs, the chemical formation of the anode will be insufficient, and unformed lead sulfate may remain in the active material, or white lead sulfate may appear on the surface of the anode plate. A large amount remains. In particular, the latter phenomenon develops into a significant appearance defect. As a means to prevent these phenomena, the addition of carbon black such as acetylene black, carbon fiber, or red lead to the lead paste for an anode has been considered. All of these additives are intended to form an electronically conductive network other than the lattice in the paste, thereby increasing the chemical conversion efficiency. Carbon black and other carbon fibers are selected as acid- and oxidation-resistant, electronically conductive materials, and red lead produces lead dioxide through a chemical reaction with dilute sulfuric acid, which is a chemical liquid, and this creates electrons in the paste. It will give conductivity. For example, the addition of carbon fiber is described in Japanese Patent Publication No. 38-14425.

発明が解決しようとする課題 カーボンや鉛丹等の粉末を陽極活物質中に添加する方法
は、添加物が陽極活物質中に均一に分散することによっ
て、活物質すなわち二酸化鉛の結晶の結合力を弱め、充
放電による結晶粒子の脱落を促進してしまうために寿命
性能が低下する欠点を有する。
Problems to be Solved by the Invention The method of adding powder such as carbon or red lead to the anode active material is such that the additive is uniformly dispersed in the anode active material, thereby increasing the bonding strength of the active material, that is, lead dioxide crystals. This has the disadvantage that the life performance is reduced because it weakens the crystal particles and promotes the shedding of crystal particles due to charging and discharging.

一方、カーボン繊維を添加する方法は、繊維径が数μm
から数十μmとカーボン粉末例えばアセチレンブラック
の粒径の数百Aより極めて大きいために、化成効率をカ
ーボン添加電池差にするためには添加量を多くしなげれ
ばならず、格子に活物質を充填する工程でトラブルが多
発するとともに寿命性能が低下する欠点を有する。
On the other hand, in the method of adding carbon fiber, the fiber diameter is several μm.
The particle size of carbon powder, for example, acetylene black, is several hundreds of micrometers, which is much larger than the several hundred amps. Therefore, in order to make the chemical conversion efficiency the same as that of carbon-added batteries, the amount of addition must be increased, and the active material in the lattice must be increased. The disadvantage is that troubles occur frequently in the filling process and the life performance is reduced.

本発明は、このような電池の寿命性能の低下を招くこと
なく、極板、特に、陽極の化成効率の向上を図ろうとい
うものである。
The present invention aims to improve the chemical formation efficiency of the electrode plate, particularly the anode, without causing such a decrease in battery life performance.

課題を解決するための手段 寿命性能に影響しない程度の少量の鉛、鉛合金、カーボ
ン等の繊維状物質を添加した陽極板に、陽極板に接する
面に導電性を付与したマントを接するか、あるいはこの
陽極板とガラスマットまたは隔離板との間に主として鉛
、鉛合金、カーボン等の導電性物質より成る多孔性シー
トを配置するものである。
Means to solve the problem: Either attach a conductive mantle to the anode plate to which a small amount of fibrous material such as lead, lead alloy, carbon, etc. is added so as not to affect the life performance of the anode plate, or Alternatively, a porous sheet mainly made of a conductive material such as lead, lead alloy, carbon, etc. is arranged between the anode plate and the glass mat or separator.

作用 本発明によれば、陽極活物質中に鉛または鉛合金あるい
はカーボンより成る導電性繊維状物質が含まれているの
で、化成電流の一部は格子近傍の活物質の化成に消費さ
れるが、残りは格子から導電性繊維状物質を通って陽極
板表面に至り、さらにこれに接しているマットの導電性
を付与した部分、あるいは導電性多孔シートを通って、
陽極板表面を化成する。すなわち格子近傍と極板表面か
ら同時に化成が進行するので化成効率が向上する。
According to the present invention, since the anode active material contains a conductive fibrous material made of lead, lead alloy, or carbon, a part of the formation current is consumed for formation of the active material near the lattice. The rest passes from the lattice through the conductive fibrous material to the anode plate surface, and then through the conductive part of the mat that is in contact with it, or the conductive porous sheet.
Chemically convert the surface of the anode plate. That is, since chemical formation proceeds simultaneously from the vicinity of the lattice and the surface of the electrode plate, the chemical formation efficiency is improved.

上記の様に陽極活物質中に含まれているカーボン等の導
電性繊維状物質は格子と極板表面との電気的導通な確保
するものであるから寿命性能に悪影響を及ぼさブよい程
度の少量であっても十分効果がある。
As mentioned above, the conductive fibrous material such as carbon contained in the anode active material ensures electrical continuity between the grid and the surface of the electrode plate, so it is contained in a small amount that does not adversely affect the life performance. Even so, it is quite effective.

実施例 実施例1 5 − 第1図は本発明の構成要素であるガラスマットの陽極板
に接する側にカーボン繊維層3を設げたガラスマット2
の付いた隔離板の断面図である。カーボン繊維1i3は
例えば、カーボン繊維を通常のガラスマットの製造方法
と同様に交錯させて積み重ねることにより製造すること
ができる。また抄紙法等により製造することもできる。
Examples Example 1 5 - Figure 1 shows a glass mat 2 in which a carbon fiber layer 3 is provided on the side of the glass mat that is in contact with the anode plate, which is a component of the present invention.
FIG. The carbon fibers 1i3 can be manufactured, for example, by interlacing and stacking carbon fibers in the same manner as in the manufacturing method of ordinary glass mats. It can also be manufactured by a papermaking method or the like.

本実施例の場合、0.8mm厚のガラスマット2上に繊
維径10〜20μmのカーボン繊維を交錯さセテ積ミ重
ね、10に9./dr7!′の荷重下(以下カーボン繊
維層およびガラスマットの厚さはすべて1o19/di
の荷重下の値とする)で総厚1.On+n+のものにし
、これに0.25 mmの主として強化繊維よりなる隔
離板1を貼り合わせた。
In the case of this example, carbon fibers with a fiber diameter of 10 to 20 μm are stacked and stacked on a glass mat 2 with a thickness of 0.8 mm. /dr7! (The thickness of the carbon fiber layer and glass mat are all 1o19/di.
The total thickness is 1. On+n+, and a 0.25 mm separator 1 mainly made of reinforcing fibers was bonded thereto.

一方、陽極板は、鉛粉に対して直径約10μm1長さ約
1 mmのカーボン繊維を0.05%添加シ、これを希
硫酸とともに通常の方法で混練し、得られたペーストを
鉛合金格子に充填した後、通常の極板製造工程をへて作
製する。
On the other hand, the anode plate is made by adding 0.05% carbon fiber with a diameter of about 10 μm and a length of about 1 mm to the lead powder, kneading this with dilute sulfuric acid in the usual manner, and using the resulting paste with a lead alloy grid. After filling the plate, the electrode plate is manufactured through the normal electrode plate manufacturing process.

なお、ガラスマット表面に設けるカーボン繊 6− 離層3の厚さと、陽極活物質中に添加するカーボン繊維
の添加量について種々検討した結果、カーボン繊維層3
の厚さは0.1mm以上、陽極活物質中のカーボン繊維
添加量は直径が約10μm、長さが約IMのもので0.
05%以上で陽極板の化成効率向上に有効であることが
明らかに九った。
In addition, as a result of various studies on the thickness of the carbon fiber layer 3 provided on the surface of the glass mat and the amount of carbon fiber added to the anode active material, it was found that the carbon fiber layer 3
The thickness of the anode active material is 0.1 mm or more, and the amount of carbon fiber added in the anode active material is about 10 μm in diameter and about IM in length.
It was clearly found that 0.05% or more is effective in improving the chemical formation efficiency of the anode plate.

カーボン繊維層を設けないガラスマット付隔離板を用い
る場合には、陽極活物質中のカーボン繊維添加量を0.
5%以上にすることにまり化成効率は向上するが、0.
2%以上添加すると、ペーストを鉛合金格子に充填した
後に、これを充填ベルトから剥ぐ工程で、剥ぐための刃
にカーボン繊維が付着して充填不良が生じやすい。さら
に0.4%以上添加すると、JISの鍔命試験のような
深い充放電を繰り返す試験では性能低下が早いことが認
められた。
When using a glass mat separator without a carbon fiber layer, the amount of carbon fiber added in the anode active material should be 0.
If it is set to 5% or more, the chemical conversion efficiency will improve, but if it is set to 0.
If 2% or more is added, carbon fibers tend to adhere to the stripping blade in the step of stripping the paste from the filling belt after filling the lead alloy grid, resulting in poor filling. Furthermore, it was found that when 0.4% or more was added, the performance deteriorated quickly in tests such as the JIS Tsuba-mei test where deep charging and discharging were repeated.

実施例2 厚さ1.0mmのガラスマットを5%のアセチレンブラ
ックを懸濁した水溶液中に浸漬した後、これを乾燥し隔
離板と貼り合わせて作製した導電性を付与したマット4
と通常の隔離板lどを貼り合わせたものの断面を第2図
に示す。
Example 2 Mat 4 with conductivity was prepared by immersing a glass mat with a thickness of 1.0 mm in an aqueous solution containing 5% acetylene black, then drying it and bonding it with a separator.
Figure 2 shows a cross-section of a structure in which a conventional separator plate and a conventional separator plate are laminated together.

この導電性を有するガラスマットの付いた隔離板と実施
例1のカーボン繊維を0.05%含有する陽極板を用い
て電池を組み立て、これを化成すると化成の大部分が完
了する陽極板から酸素ガスが発生するまでは、化成効率
が向上したが酸素ガスが発生すると化成効率は若干低下
した。
A battery is assembled using the separator with this electrically conductive glass mat and the anode plate containing 0.05% carbon fiber of Example 1, and when this is chemically formed, most of the chemical formation is completed and oxygen is supplied from the anode plate. The chemical conversion efficiency improved until gas was generated, but once oxygen gas was generated, the chemical conversion efficiency decreased slightly.

この原因は酸素ガスの気泡によりガラスマットに付着さ
せたアセチレンブラックがM離して、ガラスマットの導
電性が低下したためである。
This is because the acetylene black attached to the glass mat is separated by the bubbles of oxygen gas, and the conductivity of the glass mat is reduced.

1−かじながら、このガラスマット付隔離板を用いても
、化成の大部分が完了する酸素ガスの発生時まで、高効
率で化成が進行するので、実施例1とほぼ同程度の効果
が認められた。なお、ガラスマットから剥離したアセチ
レンブラックは電解液中に浮遊するが、徐々に陽極で酸
化されて減少するので、性能上問題ないことを確認して
いる。
1- However, even if this separator with a glass mat is used, the chemical conversion proceeds with high efficiency until the generation of oxygen gas, when most of the chemical conversion is completed, so the effect is almost the same as in Example 1. It was done. Although the acetylene black peeled off from the glass mat floats in the electrolyte, it is gradually oxidized at the anode and reduced, so we have confirmed that there is no problem with performance.

実施例3 直径十数μm、長さ数量のカーボン繊維を抄紙法により
無加圧状態で0.2mm厚のシート状にし、これに導電
性をさらに向上させるために直径数μmの鉛粉末をカー
ボン繊維に対して体積比率で約5%含浸させ、これを乾
燥させた後0.15mmになるようにプレスして導電性
多孔シート5を得た。これを実施例1のカーボン繊維を
0.05%含有する陽極板6と通常の隔離板1付ガラス
マツトの間に配置し、通常の陰極板7を用も・て電池を
組み立て化成効率を測定した結果、実施例1および2と
同等であることを確認した。
Example 3 Carbon fibers with a diameter of more than 10 μm and length were made into a 0.2 mm thick sheet using a paper-making method without pressure, and in order to further improve the conductivity, lead powder with a diameter of several μm was added to the carbon fiber. The fibers were impregnated in a volume ratio of about 5%, dried, and then pressed to a thickness of 0.15 mm to obtain a conductive porous sheet 5. This was placed between the anode plate 6 containing 0.05% carbon fiber of Example 1 and an ordinary glass mat with a separator 1, and a battery was assembled using the ordinary cathode plate 7 to measure the chemical conversion efficiency. As a result, it was confirmed that the results were the same as in Examples 1 and 2.

本発明の効果を確認するために、実施例1の方式(方式
A)と、比較のために以下に示す四つの方法で5種類の
未化成のHB55D23タイプの電池を試作した。
In order to confirm the effects of the present invention, five types of unformed HB55D23 type batteries were prototyped using the method of Example 1 (method A) and the following four methods for comparison.

方式B:実施例1の方法のカーボン繊維層を設げたガラ
スマット付隔離板を用い、カーボン繊維を添加(−ない
陽極板を用いるもの。
Method B: A separator with a glass mat provided with a carbon fiber layer according to the method of Example 1 was used, and an anode plate without carbon fiber added (-) was used.

方式C:実施例1の方法のカーボン繊維を添加した陽極
板と、カーボン繊維層を設げないガラスマット付隔離板
を用いるもの。
Method C: A method using the anode plate added with carbon fiber according to the method of Example 1 and a separator plate with a glass mat without a carbon fiber layer.

方式D:陽極活物質中に添加するカーボン繊維量が0.
5%である陽極板を用いる以外は、方式Cと同等のもの
Method D: The amount of carbon fiber added to the anode active material is 0.
Same as method C except that a 5% anode plate is used.

方式E:従来のもの。Method E: Conventional method.

まず、本発明の化成効率に関する効果を確認するために
、これらの電池に比重1.22の希硫酸を注入1−10
.4 CAの電流で化成を開始した後、一定間隔毎に電
池をとりだし、0.16CAの電流で放電した結果を第
4図に示す。本発明の方式Aの電池8と方式りの電池9
の化成効率が最も高く、次いで方式cioが高く、方式
BllとEl、2が最も低い。
First, in order to confirm the effect of the present invention on chemical conversion efficiency, dilute sulfuric acid with a specific gravity of 1.22 was injected into these batteries for 1-10 minutes.
.. After starting chemical formation with a current of 4 CA, the battery was taken out at regular intervals and discharged with a current of 0.16 CA. The results are shown in FIG. Battery 8 of method A and battery 9 of method A of the present invention
The chemical conversion efficiency is the highest, followed by the system cio, and the systems Bll, El, and 2 are the lowest.

方式Aの電池8の化成効率が最も高い原因は前述したと
おりであるが、方式りの電池9も方式Aとほぼ同等であ
る原因は陽極活物質中に添加するカーボン繊維の量が0
.5%と多いためである。一方、方式Cの電池10はこ
の量が0,05%と極めて少なく、かつ、導電性を付与
1−たマットがないため、陽極板表面から化成が進行I
−々い0 ので、化成効率は方式BやEに比べるとやや高いものの
方式AやDに比べると、かなり低い。
The reason why the formation efficiency of the battery 8 of method A is the highest is as mentioned above, but the reason why the battery 9 of method A is almost the same as method A is that the amount of carbon fiber added to the anode active material is 0.
.. This is because it is as high as 5%. On the other hand, in the battery 10 of method C, this amount is extremely small at 0.05%, and since there is no mat that imparts conductivity, chemical formation proceeds from the surface of the anode plate.
-0, so the conversion efficiency is slightly higher than methods B and E, but considerably lower than methods A and D.

方式Bが方式Eと同様に最も低い原因は、化成が格子か
ら表面まで進行する間の化成効率は従来品と同一であり
、最後に化成される表面の一部が化成されて初めて、導
電性を付与したマットから表面の残りの未化成部分が化
成されるためである。
The reason why method B has the lowest rate as well as method E is that the conversion efficiency during conversion from the lattice to the surface is the same as that of conventional products, and it is not until the part of the surface that is finally converted that it becomes conductive. This is because the remaining unformed portion of the surface is chemically converted from the mat to which it has been applied.

つぎに、本発明の方式Aの寿命性能を確認するために、
方式Aとこれとほぼ同等の化成効率を示した方式りおよ
び比較に従来の方式Eの電池を使用してJISの寿命試
験を行ない、結果を第5図に示した。方式AとEがほぼ
同等であるのに対して、方式りが極めて短いことがわか
る。
Next, in order to confirm the life performance of method A of the present invention,
A JIS life test was conducted using a battery of Method A, a method showing approximately the same chemical conversion efficiency, and a conventional method E for comparison, and the results are shown in FIG. It can be seen that while methods A and E are almost equivalent, the method is extremely short.

方式りはカーボン繊維が陽極活物質中に0.5%と多量
添加されているために活物質問の結合力が小さくなって
いることが原因であると考える。
The reason for this method is thought to be that carbon fiber is added in a large amount of 0.5% to the anode active material, which reduces the bonding strength of the active material.

以上、本発明の効果な化成効率、寿命性能の面から実施
例1で述べたが、実施例2および3についてもほぼ同一
の効果を有していることを確認している。
As mentioned above, Example 1 has been described in terms of the effective chemical formation efficiency and life performance of the present invention, but it has been confirmed that Examples 2 and 3 have almost the same effects.

発明の効果 上述したごとく、本発明の電池は化成効率が極めて高い
ため、短時間でかつ少電気量で化成ができ、さらに寿命
性能も従来品と同等以上である点、工業的価値甚大であ
る。
Effects of the Invention As mentioned above, the battery of the present invention has extremely high chemical conversion efficiency, so it can be chemically formed in a short time and with a small amount of electricity, and its life performance is equal to or higher than that of conventional products, so it has great industrial value. .

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

第1図は本発明の構成要素である導電性を付与したマッ
ト付隔離板の実施例を示す図、第2図は同じく本発明の
構成要素である導電性を付与したマット付隔離板の実施
例を示す図、第3図は本発明の実施例の極板群を示す断
面図、第4図は本発明品とこれ&比較するための電池を
0.4CAの電流で化成したときの化成時間と0.16
CAの電流で放電したときの放電時間との関係を示す特
性図、第5図は本発明品とこれと比較するための電池の
JISの寿命試験の特性図である。 2ニガラスマット、3:カーボン繊維層、4:アセチレ
ンブラック付着ガラスマット、5:導電性多孔シート、
6:陽極板。
Fig. 1 is a diagram showing an example of a separator with a mat provided with conductivity, which is a component of the present invention, and Fig. 2 is a diagram showing an example of a separator with a mat provided with conductivity, which is also a component of the present invention. Figure 3 is a cross-sectional view showing the electrode plate group of the embodiment of the present invention, and Figure 4 is the chemical composition of the present invention and batteries for comparison at a current of 0.4 CA. time and 0.16
FIG. 5 is a characteristic diagram showing the relationship with discharge time when discharging with a current of CA, and FIG. 5 is a characteristic diagram of a JIS life test of a battery of the present invention and a battery for comparison thereto. 2 glass mat, 3: carbon fiber layer, 4: acetylene black attached glass mat, 5: conductive porous sheet,
6: Anode plate.

Claims (4)

【特許請求の範囲】[Claims] (1)鉛、鉛合金、カーボン等の導電性繊維を活物質中
に含有する陽極板を用い、これに接する面に導電性を付
与したマットをこの陽極板に接するか、あるいは導電性
多孔シートをこの陽極板とガラスマットとの間に配置す
ることを特徴とする鉛蓄電池。
(1) Use an anode plate containing conductive fibers such as lead, lead alloy, carbon, etc. in the active material, and attach a mat with conductivity to the surface in contact with the anode plate, or use a conductive porous sheet. This lead-acid battery is characterized by being placed between this anode plate and a glass mat.
(2)導電性を付与したマットが、ガラスマットの陽極
板に接する側にカーボン繊維より成るマット層を一体に
設けたものである第1項記載の鉛蓄電池。
(2) The lead-acid battery according to item 1, wherein the conductive mat is a glass mat with a mat layer made of carbon fiber integrally provided on the side in contact with the anode plate.
(3)導電性を付与したマットがガラスマットにカーボ
ン粉末を付着させたものである第1項記載の鉛蓄電池。
(3) The lead-acid battery according to item 1, wherein the conductive mat is a glass mat to which carbon powder is attached.
(4)導電性多孔シートが主として鉛、鉛合金、カーボ
ン等の導電性物質よりなる第1項記載の鉛蓄電池。
(4) The lead-acid battery according to item 1, wherein the conductive porous sheet is mainly made of a conductive substance such as lead, lead alloy, or carbon.
JP1340448A 1989-12-28 1989-12-28 Lead-acid battery Pending JPH03203158A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1340448A JPH03203158A (en) 1989-12-28 1989-12-28 Lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1340448A JPH03203158A (en) 1989-12-28 1989-12-28 Lead-acid battery

Publications (1)

Publication Number Publication Date
JPH03203158A true JPH03203158A (en) 1991-09-04

Family

ID=18337058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1340448A Pending JPH03203158A (en) 1989-12-28 1989-12-28 Lead-acid battery

Country Status (1)

Country Link
JP (1) JPH03203158A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012141608A1 (en) * 2011-04-12 2012-10-18 Общеcтво С Ограниченной Отвественностью "Новогородская Аккумуляторная Компания" Lead-acid rechargeable battery
EP2858143A1 (en) * 2013-10-03 2015-04-08 Johns Manville New pasting paper made of glass fiber nonwoven comprising carbon graphite
US20150099153A1 (en) * 2013-10-03 2015-04-09 Johns Manville Conductive mat for battery electrode plate reinforcement and methods of use therefor
US20150099157A1 (en) * 2013-10-03 2015-04-09 Johns Manville Pasting paper made of glass fiber nonwoven comprising carbon graphite
RU2598357C2 (en) * 2012-04-12 2016-09-20 Джонс Мэнвилл Mat made of glass fibers or polyolefin fibers used as a separator in lead-acid battery
US9685646B2 (en) 2013-10-03 2017-06-20 Johns Manville Pasting paper made of glass fiber nonwoven comprising carbon graphite
US11152647B2 (en) 2014-05-05 2021-10-19 Daramic, Llc Lead-acid battery separators, electrodes, batteries, and methods of manufacture and use thereof
JPWO2022034918A1 (en) * 2020-08-14 2022-02-17
US11271270B2 (en) 2015-10-05 2022-03-08 Daramic, Llc Functionalized lead acid battery separators, improved lead acid batteries, and related methods
WO2022191145A1 (en) * 2021-03-10 2022-09-15 旭化成株式会社 Separator for lead acid storage batteries, and lead acid storage battery
US11450924B2 (en) 2006-09-27 2022-09-20 Daramic, Llc Battery separator for extending the cycle life of a battery

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11450924B2 (en) 2006-09-27 2022-09-20 Daramic, Llc Battery separator for extending the cycle life of a battery
WO2012141608A1 (en) * 2011-04-12 2012-10-18 Общеcтво С Ограниченной Отвественностью "Новогородская Аккумуляторная Компания" Lead-acid rechargeable battery
RU2598357C2 (en) * 2012-04-12 2016-09-20 Джонс Мэнвилл Mat made of glass fibers or polyolefin fibers used as a separator in lead-acid battery
US9923196B2 (en) * 2013-10-03 2018-03-20 Johns Manville Conductive mat for battery electrode plate reinforcement and methods of use therefor
US10084170B2 (en) 2013-10-03 2018-09-25 Johns Manville Pasting paper made of glass fiber nonwoven comprising carbon graphite
US20150099153A1 (en) * 2013-10-03 2015-04-09 Johns Manville Conductive mat for battery electrode plate reinforcement and methods of use therefor
EP2858143B1 (en) 2013-10-03 2017-02-01 Johns Manville New pasting paper made of glass fiber nonwoven comprising carbon graphite
US9685646B2 (en) 2013-10-03 2017-06-20 Johns Manville Pasting paper made of glass fiber nonwoven comprising carbon graphite
EP2858142A1 (en) * 2013-10-03 2015-04-08 Johns Manville New pasting paper made of glass fiber nonwoven comprising carbon graphite
US20180159122A1 (en) * 2013-10-03 2018-06-07 Johns Manville Conductive mat for battery electrode plate reinforcement and methods of use therefor
US20150099157A1 (en) * 2013-10-03 2015-04-09 Johns Manville Pasting paper made of glass fiber nonwoven comprising carbon graphite
US11018333B2 (en) 2013-10-03 2021-05-25 Johns Manville Conductive mat for battery electrode plate reinforcement and methods of use therefor
EP2858143A1 (en) * 2013-10-03 2015-04-08 Johns Manville New pasting paper made of glass fiber nonwoven comprising carbon graphite
US11152647B2 (en) 2014-05-05 2021-10-19 Daramic, Llc Lead-acid battery separators, electrodes, batteries, and methods of manufacture and use thereof
US12051783B2 (en) 2014-05-05 2024-07-30 Daramic, Llc Lead-acid battery separators, electrodes, batteries, and methods of manufacture and use thereof
US11271270B2 (en) 2015-10-05 2022-03-08 Daramic, Llc Functionalized lead acid battery separators, improved lead acid batteries, and related methods
JPWO2022034918A1 (en) * 2020-08-14 2022-02-17
WO2022191145A1 (en) * 2021-03-10 2022-09-15 旭化成株式会社 Separator for lead acid storage batteries, and lead acid storage battery

Similar Documents

Publication Publication Date Title
EP0352115B1 (en) Lead-acid battery
US4656706A (en) Formation efficiency of positive plates of a lead-acid battery
WO1989012329A1 (en) Lead-acid rechargeable storage battery
JP5079324B2 (en) Lead acid battery
JPH03203158A (en) Lead-acid battery
JP2926877B2 (en) Lead storage battery
WO1997007553A1 (en) An electrode plate for lead-acid accumulator and producing method thereof
US4873161A (en) Positive paste with lead-coated glass fibers
JPS63279568A (en) Lead storage battery
JP2000357532A (en) Manufacture of lead-acid battery
JP2809634B2 (en) Manufacturing method of sealed lead-acid battery
JP2929894B2 (en) Manufacturing method of sealed lead-acid battery
JP2949767B2 (en) Lead battery manufacturing method
JPH10261432A (en) Manufacture of lead-acid battery
JPS6028171A (en) Manufacture of paste type pole plate for lead storage battery
JPH0461748A (en) Lead-acid battery electrode plate ready to chemical formation and its manufacture
JP2000149932A (en) Lead-acid battery and its manufacture
JPH04162352A (en) Positive plate of lead storage battery
JPH11111275A (en) Manufacture of plate for lead-acid battery
JP2002093459A (en) Sealed lead-acid battery and its manufacturing method
JPH08180857A (en) Electrode plate for lead-acid battery
JPS59138063A (en) Lead storage battery
JPH0587944B2 (en)
JP2003178754A (en) Plate for lead-acid storage battery, and manufacturing method of the same
JPS61143940A (en) Manufacture of cathode plate for lead-acid battery