JPH04155759A - Manufacturing method for positive electrode plates for lead-acid batteries - Google Patents
Manufacturing method for positive electrode plates for lead-acid batteriesInfo
- Publication number
- JPH04155759A JPH04155759A JP2281198A JP28119890A JPH04155759A JP H04155759 A JPH04155759 A JP H04155759A JP 2281198 A JP2281198 A JP 2281198A JP 28119890 A JP28119890 A JP 28119890A JP H04155759 A JPH04155759 A JP H04155759A
- Authority
- JP
- Japan
- Prior art keywords
- lead
- electrode plates
- electrode plate
- positive electrode
- manufacturing
- 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
Links
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
Landscapes
- Battery Electrode And Active Subsutance (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明は鉛蓄電池用正極板の製造法に関し、特にペース
ト式極板のペースト塗着後の熟成条件の改善に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for manufacturing a positive electrode plate for a lead-acid battery, and more particularly to improving the aging conditions of a paste-type electrode plate after applying the paste.
従来の技術
鉛蓄電池の極板は、一般に鉛粉と水と硫酸を主成分とし
、これに必要に応じて樹脂などの短繊維や炭素の微粉末
、有機添加剤などを添加し、練合によって得られたペー
ストを鋳造格子体や連続エキスパンド格子体に塗着し、
必要に応じて極板の形状に切断し、懸垂状態で熟成乾燥
して極板とするペースト式極板が多く用いられている。Conventional technology Plate plates for lead-acid batteries generally have lead powder, water, and sulfuric acid as their main components, to which short fibers such as resin, fine carbon powder, organic additives, etc. are added as necessary, and they are made by kneading. Apply the obtained paste to a cast lattice body or a continuous expanded lattice body,
Paste-type electrode plates are often used, which are cut into the shape of the electrode plate as needed, aged and dried in a suspended state, and then made into an electrode plate.
この熟成乾燥段階において、格子体やペースト内の金属
鉛を酸化させた後、乾燥させる事によって、活物質と格
子体および活物質相互間の結合を強くするとともに三塩
基性硫酸鉛を生成させている。In this aging and drying stage, the metal lead in the lattice and paste is oxidized and then dried to strengthen the bonds between the active material and the lattice and between the active materials and to generate tribasic lead sulfate. There is.
従来はこの熟成段階では、ペースト中の水分率を5〜8
%程度の範囲に長時間保つことが望ましいため、加温し
ない状態で極板を密着させて熟成を行なえば、ある程度
安定した状態で極板を製造できる。しかし、乾燥に長時
間を必要とする欠点があった。そのため1枚ずつ極板を
離して懸垂した状態で加温し反応速度を速めると、水分
の蒸発もそれに応じて速くなるため、水分率を5〜8%
程度に保つためには、熟成乾燥の初期段階では加湿を行
ない、その後乾燥する方法がとられている。Conventionally, at this stage of ripening, the moisture content of the paste was reduced to 5 to 8.
% range for a long period of time. Therefore, if the electrode plates are aged in close contact with each other without heating, the electrode plates can be manufactured in a somewhat stable state. However, it has the drawback of requiring a long time for drying. Therefore, if you separate the electrode plates one by one and heat them in a suspended state to accelerate the reaction rate, the evaporation of water will also be faster, so the moisture content can be reduced to 5 to 8%.
In order to maintain this level, a method is used in which humidification is performed during the initial stage of ripening and drying, followed by drying.
発明が解決しようとする課題
前記従来の構成では、ロット内では懸垂状態の極板間隔
、場所、塗着してからの時間経過などによる変動が大き
く、またロット間でも、ペーストの初期状態すなわち綜
合時の温度、水分量などで、変動が生じることはまぬが
れない。また極板厚みにより熟成乾燥速度が変動するた
め設定厚みごとに違うパターンの熟成乾燥が必要であっ
た。Problems to be Solved by the Invention In the above-mentioned conventional configuration, there are large variations within a lot due to the spacing and location of the suspended electrode plates, the elapsed time after application, etc., and even between lots, the initial state of the paste, that is, the overall It is inevitable that fluctuations will occur depending on the temperature, moisture content, etc. Furthermore, since the ripening and drying speed varies depending on the thickness of the electrode plate, different patterns of ripening and drying were required for each set thickness.
課題を解決するための手段
このような課題を解決するため、本発明の鉛蓄電池用正
極板の製造法は、熟成段階で極板同士を前記極板の厚み
方向に密着して懸垂し、熟成途中のtI紀補極板“)表
面温度か雰囲気温度より3℃埼上、−、昇した時点から
加湿を行ない、その後乾燥するものである。Means for Solving the Problems In order to solve these problems, the method for manufacturing a positive electrode plate for a lead-acid battery of the present invention includes suspending the electrode plates in close contact with each other in the thickness direction of the electrode plates during the aging stage. Humidification is performed from the time when the surface temperature of the interpolated electrode plate () rises by 3° C. above the ambient temperature, and then it is dried.
作用
この構成により本発明の鉛蓄電池用正極板の製造法は、
極板を密着させる事によって懸垂状、態での間隔や場所
による変動か低減され、加温による過度の水分の蒸発を
おさえる事かできろ、また棟板厚みの影響は考慮しなく
てもよくなる。また、金属鉛の酸化時の発熱による極板
の表面温度が雰囲気温度より3℃以上上昇した時点で加
湿を行なうことにより、最良の活物質相互間および活物
質と格子体間の結合強度が得られることとなる。またこ
れにより熟成乾燥時間も短縮する事ができることとなる
。さらに酸化時の発熱は反応効率の良(15〜8%の水
分率に達した時に起こるためその時点から加湿を行なう
ということはその前の段階の綜合時の温度、水分量、塗
着してからの時間経過などの変動を考慮に入れる事な(
最良の水分率を保てるという事である。それによって活
物質と格子および活物質相互間の結合強度を強く安定さ
せる事ができることとなる。Effect: With this configuration, the method for manufacturing a positive electrode plate for a lead-acid battery of the present invention is as follows:
By bringing the electrode plates into close contact with each other, it is possible to reduce fluctuations due to spacing and location in the suspended state, suppress excessive moisture evaporation due to heating, and eliminate the need to consider the effect of ridge plate thickness. . In addition, the best bonding strength between active materials and between active materials and lattice bodies can be achieved by humidifying when the surface temperature of the electrode plate rises by 3°C or more above the ambient temperature due to heat generated during oxidation of lead metal. It will be. This also makes it possible to shorten the ripening and drying time. Furthermore, heat generation during oxidation occurs when the reaction efficiency reaches 15 to 8% (15 to 8% moisture content is reached, so humidification from that point onwards means that the temperature, moisture content, and coating temperature at the previous stage of synthesis are the same). Do not take into account changes such as the passage of time since (
This means that you can maintain the best moisture content. This makes it possible to strongly stabilize the bonding strength between the active material and the lattice and between the active materials.
実施例
以下本発明の一実施例の鉛蓄電池用正極板の製造法につ
いて図面を基にして説明する。EXAMPLE Hereinafter, a method for manufacturing a positive electrode plate for a lead-acid battery according to an example of the present invention will be described with reference to the drawings.
酸化度72?oの鉛酸化物粉末100kgにアクリル繊
維200gを混合したものに、比重1.40の希硫酸1
0.、’l、i留水10Cを加えで練り合わせたペース
トを、鋳造格子体に塗着し重ね合わせ、両端には水蒸気
を透さない素材で極板と同じ形状のものを重ねて端部と
中央部の状態が違わないようにして懸垂する。それをあ
らかじめ温度設定しである65℃の乾燥炉に入れ中央部
の極板表面で温度を測定し、その温度が68℃となった
時点で、90%の湿度を加えはじめ、8時間加湿を続け
る。その後加湿をとりやめ同じ温度で8時間乾燥したも
のを極板Aとする。この際極板の表面温度が68℃にな
るまで1時間であった6塗着まで極板Aと同じ条件で作
成した極板を極板Aと同じように懸垂し、温度65℃、
湿度90%下に9時間存在させその後同様に65℃で8
時間乾燥させたものを極板Bとする。さらに、塗着まで
Aと同じ条件で作成し適当な間隔をあけて懸垂し、Bと
同じパターンで熟成乾燥したものを極板Cとする。第1
図に加湿開始時の雰囲気温度に対する極板表面の温度の
上昇と落下脱落量の関係を示すが、第1図からも明らか
なように温度上昇が充分でない時に加湿を開始すると、
活物質相互間および活物質と格子体間の結合強度は弱(
、またばらつきも大きいため、雰囲気温度より3℃以上
の極板表面の温度上昇があった時に加湿を開始すること
が必要である。Oxidation degree 72? A mixture of 100 kg of lead oxide powder of
0. ,'l,i A paste made by adding 10C of distilled water is applied to the cast grid body and overlapped, and on both ends, a material that does not allow water vapor to pass through and has the same shape as the electrode plate is placed over the ends and the center. Do a pull-up without changing the condition of the parts. We put it in a drying oven with a preset temperature of 65℃, measured the temperature on the surface of the electrode plate in the center, and when the temperature reached 68℃, we started adding 90% humidity and kept it humidified for 8 hours. continue. Thereafter, humidification was stopped and the plate was dried at the same temperature for 8 hours, which was designated as electrode plate A. At this time, the electrode plate made under the same conditions as electrode plate A was suspended in the same way as electrode plate A until the surface temperature of electrode plate A reached 68°C, which took 1 hour for 6 coatings, and the temperature reached 65°C.
It was kept under 90% humidity for 9 hours, and then kept at 65℃ for 8 hours.
The plate that has been dried for a period of time is referred to as electrode plate B. Further, the electrode plate C was prepared under the same conditions as A until coating, suspended at appropriate intervals, and aged and dried in the same pattern as B. 1st
The figure shows the relationship between the rise in temperature of the electrode plate surface and the amount of falling off against the ambient temperature at the start of humidification.As is clear from Fig. 1, if humidification is started when the temperature rise is not sufficient,
The bond strength between active materials and between active materials and lattice bodies is weak (
Also, since the variation is large, it is necessary to start humidification when the temperature of the electrode plate surface rises by 3° C. or more above the ambient temperature.
第1図の試験条件は後述の第4図の試験条件と同一であ
る。The test conditions in FIG. 1 are the same as those in FIG. 4, which will be described later.
これら3種類の極板の熟成乾燥中の活物質中の水分率の
変化を第2図に、また活物質中の金属鉛量の変化を第3
図に示す。第2図、第3図からも明らかなように極板B
では金属鉛量の減少すなわち酸化は進行しているが、水
分量の減少が遅(、同じ時間で乾燥が終了しない。極板
Cでは水分量の減少は速いが金属鉛の減少が遅く、すな
わち酸化が進行していない。また極板B、Cとも最終的
な金属鉛量のばらつきが極板Aより大きい。すなわち活
物質相互間および活物質と格子体間の結合を強化するた
めの鉛酸化物粉末の酸化か均一にされていないと考えら
れる。また前記結合の強度を確認するために落下強度を
測定した。A、B、Cの極板をランダムに5枚ずつ抜き
取り、80cm高さよりコンクリート上に5回ずつ落下
し、その活物質の脱落量により判定した(第4図)。第
4図からも明らかなように、極板Bは乾燥が完全でない
ため落下脱落量が非常に多くまた極板Cは落下脱落量の
バラツキが大きかった。また前記結合の強度の違いが電
池性能に与える影響を確かめるため、極板AとCを用い
て、容量2.0Ahの電池を100個ずつ作成し、40
℃で1ケ月放置し放電容量を測定した(第5図)。第5
図に示す通り、極板Cで作成した電池の中には、放電容
量が0.6Ah〜1.2Ahしかないものが3個あった
。その3個の電池を解析すると、いずれも正極電位が急
激に卑となる現象であり、その極板は、充電状態にもか
かわらず、格子表面や活物質内部に層状に、多量の硫酸
鉛が生成していた。極板Aより作成した電池や極板Cよ
り作成しても、容量の出ている電池の極板には、この現
象は見られなかった。Figure 2 shows the change in moisture content in the active material during aging and drying of these three types of electrode plates, and Figure 3 shows the change in the amount of metallic lead in the active material.
As shown in the figure. As is clear from Figures 2 and 3, the electrode plate B
In Plate C, the amount of metallic lead decreases, that is, oxidation progresses, but the amount of moisture decreases slowly (and drying does not finish in the same amount of time. In Plate C, the amount of moisture decreases quickly, but the amount of metallic lead decreases slowly, i.e. Oxidation has not progressed.Furthermore, the variation in the final amount of metal lead in plates B and C is larger than that in plate A.In other words, lead acid is added to strengthen the bonds between the active materials and between the active materials and the lattice. It is thought that the oxidation of the compound powder was not uniform.Also, to confirm the strength of the bond, the drop strength was measured.Five electrode plates A, B, and C were randomly pulled out and placed on concrete from a height of 80 cm. It was determined by the amount of active material that fell off the top five times (Figure 4).As is clear from Figure 4, Plate B was not completely dried, so a very large amount of active material fell off. Plate C had a large variation in the amount of falling and falling off.In addition, in order to confirm the effect of the difference in bond strength on battery performance, 100 batteries each with a capacity of 2.0 Ah were made using Plate A and C. 40
The discharge capacity was measured after being left at ℃ for one month (Figure 5). Fifth
As shown in the figure, among the batteries made with the electrode plate C, there were three batteries with a discharge capacity of only 0.6 Ah to 1.2 Ah. Analysis of these three batteries revealed that the positive electrode potential suddenly became less base in all cases, and the electrode plate had a large amount of lead sulfate in a layer on the lattice surface and inside the active material, despite the charged state. It was generating. This phenomenon was not observed in the batteries made from plate A or plate C, which had a high capacity.
これは、もともと活物質と格子体及び活物質相互間の結
合か弱かった部分に、電解液である希硫酸が集中して入
り込み、不活性な硫酸鉛を生成したためと考えられる。This is thought to be because dilute sulfuric acid, which is an electrolytic solution, concentrated and entered the parts where the bond between the active material and the lattice and between the active materials was originally weak, producing inactive lead sulfate.
発明の効果
以上の実施例の説明で明らかなように本発明の鉛蓄電池
用正極板の製造法によれば、熟成乾燥段階で極板同士を
極板厚み方向に密着させて懸垂し、熟成途中の極板の表
面温度が雰囲気温度より3℃以上上昇した時点から加湿
を行ない、その後乾燥することにより、熟成状態での活
物質中の水分量と金属鉛量のばらつきを低減することに
より、電池性能のばらつきを低減し、さらに熟成乾燥時
間を短縮することができる。Effects of the Invention As is clear from the description of the embodiments above, according to the method for producing a positive electrode plate for a lead-acid battery of the present invention, the electrode plates are suspended in close contact with each other in the thickness direction during the aging and drying stage. Humidification is performed from the time when the surface temperature of the electrode plate rises by 3°C or more above the ambient temperature, and then drying reduces the variation in the amount of water and the amount of metal lead in the active material in the aged state. It is possible to reduce variations in performance and further shorten aging and drying time.
第1図は本発明の一実施例の鉛蓄電池用正極板の製造法
における加湿開始時点の雰囲気温度に対する極板表面の
温度上昇と落下脱落量との関係を示すグラフ、第2図は
本発明の一実施例の鉛蓄電池用正極板の製造法と比較量
との熟成乾燥条件の違いによる活物質中の水分量の変化
を示すグラフ、第3図は同熟成乾燥条件の違いによる活
物質中の金属鉛量の変化を示すグラフ、第4図は同熟成
乾燥条件の違いによる活物質の落下脱落量を示すグラフ
、第5図は同熟成乾燥条件の違いによる保存後の放電容
量のばらつきを示すグラフである。
代理人の氏名 弁理士小鍜治明 ほか2名第1図
見17;Ih3R&のlEliM%、;MJ 1;欠R
口11d擬a+JJ¥ k4 (’c>第2図
G5と
軽裔BJ!聞()l)
第 4 図FIG. 1 is a graph showing the relationship between the temperature rise on the surface of the electrode plate and the amount of falling off relative to the ambient temperature at the start of humidification in the manufacturing method of a positive electrode plate for a lead-acid battery according to an embodiment of the present invention, and FIG. A graph showing changes in the amount of water in the active material due to differences in aging and drying conditions between the manufacturing method of a positive electrode plate for a lead-acid battery according to an example and a comparative amount. Figure 4 is a graph showing the amount of active material falling off due to differences in aging and drying conditions. Figure 5 is a graph showing variations in discharge capacity after storage due to differences in aging and drying conditions. This is a graph showing. Name of agent: Patent attorney Haruaki Ogata and two others Figure 1: Ih3R &IEliM%,;MJ1; Missing R
Mouth 11d pseudo a+JJ¥ k4 ('c>Figure 2 G5 and light descendant BJ! ()l) Figure 4
Claims (1)
練合したペーストを、鋳造格子体または連続エキスパン
ド格子体に塗着し、熟成、乾燥する鉛蓄電池用正極板の
熟成段階で、極板同士を前記極板の厚み方向に密着させ
て懸垂し、熟成途中の前記極板の表面温度が雰囲気温度
より3℃以上上昇した時点から加湿を行ない、その後乾
燥する鉛蓄電池用正極板の製造法。In the maturing stage of positive electrode plates for lead-acid batteries, a paste made by kneading lead oxide powder containing metallic lead, water, and sulfuric acid as main ingredients is applied to a cast grid or continuous expanded grid, aged, and dried. A positive electrode plate for a lead-acid battery is made by suspending the electrode plates in close contact with each other in the thickness direction of the electrode plates, humidifying the electrode plates from the time when the surface temperature of the electrode plates in the middle of aging rises by 3°C or more above the ambient temperature, and then drying them. Manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2281198A JPH04155759A (en) | 1990-10-18 | 1990-10-18 | Manufacturing method for positive electrode plates for lead-acid batteries |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2281198A JPH04155759A (en) | 1990-10-18 | 1990-10-18 | Manufacturing method for positive electrode plates for lead-acid batteries |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH04155759A true JPH04155759A (en) | 1992-05-28 |
Family
ID=17635715
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2281198A Pending JPH04155759A (en) | 1990-10-18 | 1990-10-18 | Manufacturing method for positive electrode plates for lead-acid batteries |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH04155759A (en) |
-
1990
- 1990-10-18 JP JP2281198A patent/JPH04155759A/en active Pending
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