JPS6322015B2 - - Google Patents

Info

Publication number
JPS6322015B2
JPS6322015B2 JP56069527A JP6952781A JPS6322015B2 JP S6322015 B2 JPS6322015 B2 JP S6322015B2 JP 56069527 A JP56069527 A JP 56069527A JP 6952781 A JP6952781 A JP 6952781A JP S6322015 B2 JPS6322015 B2 JP S6322015B2
Authority
JP
Japan
Prior art keywords
paste
carbon dioxide
atmosphere
lead
discharge
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
Application number
JP56069527A
Other languages
Japanese (ja)
Other versions
JPS57185673A (en
Inventor
Keiichi Watanabe
Naoto Hoshihara
Katsuhiro Takahashi
Hiroshi Yasuda
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 JP56069527A priority Critical patent/JPS57185673A/en
Publication of JPS57185673A publication Critical patent/JPS57185673A/en
Publication of JPS6322015B2 publication Critical patent/JPS6322015B2/ja
Granted legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • H01M4/16Processes of manufacture
    • H01M4/20Processes of manufacture of pasted electrodes
    • H01M4/21Drying of pasted electrodes
    • 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

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Description

【発明の詳細な説明】 本発明は、鉛蓄電池用ペースト式電極の製造法
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for manufacturing a paste-type electrode for lead-acid batteries.

現在2次電池として最もよく普及しているのが
鉛蓄電池であり、この鉛蓄電池でも極板はペース
トを格子に塗着して得られるいわゆるペースト式
鉛蓄電池が主流を占めている。これは、製法が簡
単であり、電極構造も簡単であるので低価格であ
るのが、第1の理由である。さらに性能の上で
も、すぐれていることが第2の理由に上げられ
る。
Currently, the most popular type of secondary battery is a lead-acid battery, and among these lead-acid batteries, so-called paste-type lead-acid batteries, in which the electrode plates are obtained by applying paste to a grid, are the mainstream. The first reason for this is that the manufacturing method is simple and the electrode structure is simple, so the price is low. The second reason is that it has excellent performance.

本発明は、このようなペースト式鉛蓄電池を、
従来の性能より、大巾に向上させることを可能に
する一つの有効な製造法を提供するものである。
The present invention provides such a paste type lead acid battery,
This provides an effective manufacturing method that allows the performance to be significantly improved compared to conventional methods.

従来、このペースト式極板は、鉛または鉛合金
製の格子体、パンチングメタル、エキスパンデツ
ドメタルなどの支持体に、鉛粉、水、希硫酸を主
成分とする鉛ペーストを充てんし、乾燥、熟成な
どの比較的簡単な工程により製作することがで
き、得られた極板の放電特性は、かなり良好であ
る。しかし、例えば高率放電特性や活物質の放電
利用率などについては、さらに特性の向上が望ま
れている。
Conventionally, this paste-type electrode plate is made by filling a support such as a lead or lead alloy grid, punched metal, or expanded metal with lead paste containing lead powder, water, and dilute sulfuric acid as its main components, and then drying it. It can be manufactured through relatively simple processes such as aging, and the discharge characteristics of the obtained electrode plate are quite good. However, it is desired to further improve the characteristics, for example, in terms of high rate discharge characteristics and discharge utilization rate of the active material.

こうした観点から、各種の改良が考えられてい
るが、極板のペースト条件は電極特性を左右する
最大の因子である。したがつて、長い歴史の中
で、鉛粉やそれに練合する水、硫酸という主成分
を中心に幅広い組成が検討され、とくに近年で
は、機械的なペーストの充てんにもからんで、ペ
ースト充てんが効率的に行われると同時に、各種
の電池仕様に適用できる好ましい組成が追求さ
れ、現在に到つている。
From this point of view, various improvements have been considered, but the paste conditions of the electrode plate are the biggest factor that influences the electrode characteristics. Therefore, over a long history, a wide range of compositions have been studied, centering on the main components of lead powder, water mixed with it, and sulfuric acid.In recent years, in particular, mechanical paste filling has been involved, and paste filling has become more popular. A desirable composition that can be efficiently carried out and at the same time applicable to various battery specifications has been sought and reached at present.

しかしながら、先に述べたように、電池のユー
ザー側よりの、より高容量、より高出力で、しか
も高い信頼性を有する電池の開発の要望は、もは
や従来の鉛粉と硫酸と水との練合条件や組成のみ
を主体とするペースト条件内での改良では限界に
達し、その常識の域の逸脱を余儀なくしてきてい
るのである。従つて、より高出力、より高容量で
しかも高い信頼性を有する電池を開発するには、
ペースト条件以外の面からの改善が必要となつて
きた。
However, as mentioned above, the desire from battery users to develop batteries with higher capacity, higher output, and higher reliability has led to the need to develop batteries that have higher capacity, higher output, and higher reliability. Improvements within the paste conditions, mainly based on the application conditions and composition, have reached their limits and have forced us to deviate from common sense. Therefore, in order to develop batteries with higher output, higher capacity, and higher reliability, it is necessary to
Improvements in aspects other than paste conditions have become necessary.

そこで、本発明では、乾燥条件についての改善
によつて、極めて高性能で、しかも高い信頼性を
有する電池を提供するものである。すなわち、本
発明は、ペーストを支持体に塗着充てん後乾燥す
る際に、従来法では自然大気中で行われていたも
のを、炭酸ガスを自然大気より多量に含有した大
気中で行うことを特徴としている。
Therefore, the present invention provides a battery with extremely high performance and high reliability by improving the drying conditions. That is, the present invention allows the paste to be applied and filled onto a support and then dried in an atmosphere containing carbon dioxide gas in a larger amount than in the natural atmosphere, whereas conventional methods require drying in the natural atmosphere. It is a feature.

この製造方法によれば、塗着充てん後の極板中
のペースト(活物質)の表面に、高率放電時の放
電反応を促進するような形状の多孔板を生成し
て、高容量化がはかれる。この極板表面に生成し
た多孔体は、塩基性炭酸鉛と推定できるが、これ
を放電反応に最適な状態とするには、乾燥工程中
雰囲気の炭酸ガス・温度・曝露時間などを調整し
ておく必要がある。本発明者らは、後述の実施例
に示すような実験事実に基づき、乾燥工程中雰囲
気炭酸ガス濃度は10%以上80%未満、雰囲気温度
は+5℃以上40℃未満、曝露時間は好ましくは1
時間以上、雰囲気相対湿度は40%以上80%未満と
いう条件が適していることを見い出した。以下本
発明を実施例により説明する。
According to this manufacturing method, a porous plate with a shape that promotes the discharge reaction during high rate discharge is generated on the surface of the paste (active material) in the electrode plate after coating and filling, thereby increasing the capacity. It is measured. The porous material formed on the surface of the electrode plate can be presumed to be basic lead carbonate, but in order to bring it into the optimal state for the discharge reaction, the carbon dioxide gas in the atmosphere, temperature, exposure time, etc. must be adjusted during the drying process. It is necessary to keep it. Based on experimental facts as shown in Examples below, the present inventors have determined that during the drying process, the atmospheric carbon dioxide concentration is 10% or more and less than 80%, the atmospheric temperature is +5°C or more and less than 40°C, and the exposure time is preferably 1.
It has been found that conditions in which the relative humidity of the atmosphere is 40% or more and less than 80% for a period of time or more are suitable. The present invention will be explained below with reference to Examples.

実施例 1 横巾135mm、高さ110mm、格子厚さ1.4mmのエキ
スパンデツドメタル格子にペーストを充てんして
正極板を製造した。格子へのペースト若てん後の
乾燥は、雰囲気大気中炭酸ガス濃度を、1%、5
%、8%、10%、15%、20%、30%、40%、50
%、60%、70%、80%、85%、90%、95%と変え
た15種類の乾燥条件のもとでの極板を製造して電
池を組んだ。このときの雰囲気の他の条件、即
ち、温度は20℃、曝露時間は15時間、相対湿度は
60%であつた。その後、常法により熟成した。電
池の極板群構成は、上記の正極板4枚と、従来の
構成の負極板5枚である。電解液には比重1.280
の希硫酸を用い、液量は500c.c.とした。試験条件
は−15℃の温度のもとで、300Aの定電流で、端
子電圧が1.0V/セルまで放電することとし、そ
のときの放電時間をみた。
Example 1 A positive electrode plate was manufactured by filling an expanded metal grid with a width of 135 mm, a height of 110 mm, and a grid thickness of 1.4 mm with a paste. For drying after rejuvenating the paste on the grid, the carbon dioxide concentration in the atmosphere should be adjusted to 1%, 5%.
%, 8%, 10%, 15%, 20%, 30%, 40%, 50
Electrodes were manufactured and batteries were assembled under 15 different drying conditions: %, 60%, 70%, 80%, 85%, 90%, and 95%. The other conditions of the atmosphere at this time were: temperature was 20℃, exposure time was 15 hours, and relative humidity was
It was 60%. Thereafter, it was aged in a conventional manner. The electrode plate group configuration of the battery is the above-mentioned four positive electrode plates and five negative electrode plates of the conventional configuration. The electrolyte has a specific gravity of 1.280
dilute sulfuric acid was used, and the liquid volume was 500 c.c. The test conditions were to discharge at a constant current of 300A to a terminal voltage of 1.0V/cell at a temperature of -15°C, and the discharge time at that time was measured.

第1図は、大気中炭酸ガス濃度と電池の放電持
続時間との関係を示す。図から明らかなように、
炭酸ガス濃度が10%未満においては、放電持続時
間は著しく短く、また80%以上においても短くな
ることがわかる。このことは、たとえば、空気中
で自然に存在する炭酸ガスによる影響とは、はる
かに異なることを示している。X線回折分析でも
空気中での自然乾燥の未化成板では、塩基性炭酸
鉛と思われるピークの検出はできない。また表面
の白色化の起こる度合も明らかに目視できる。ま
た炭酸ガスと空気の雰囲気でも類似の効果が与ら
れるが、酸素の若干の存在は、特性に好ましい影
響を与えているものと推察できる。
FIG. 1 shows the relationship between atmospheric carbon dioxide concentration and battery discharge duration. As is clear from the figure,
It can be seen that the discharge duration is extremely short when the carbon dioxide concentration is less than 10%, and also becomes shorter when the carbon dioxide concentration is 80% or more. This shows that the effect is far different from, for example, the effect of carbon dioxide gas naturally present in the air. Even in X-ray diffraction analysis, it is not possible to detect a peak that seems to be caused by basic lead carbonate in an unformed plate that has been air-dried in air. The extent to which surface whitening occurs is also clearly visible. Although similar effects can be obtained in an atmosphere of carbon dioxide gas and air, it can be inferred that the presence of some oxygen has a favorable influence on the characteristics.

実施例 2 実施例1と同じ格子を使つて、格子へのペース
ト充てん後の乾燥は、雰囲気温度を、−5℃、0
℃、3℃、5℃、8℃、10℃、20℃、30℃、40
℃、50℃、60℃、70℃、80℃と変えて13種類の条
件のもとでの極板を製造して電池を組んだ。この
場合も、常法によりこの工程の熟成を行つた。こ
のときの雰囲気の他の条件は、炭酸ガス濃度30
%、曝露時間15時間、相対湿度60%であつた。極
板群構成、電解液、および試験条件は、実施例1
と同じである。
Example 2 Using the same grid as in Example 1, drying after filling the grid with the paste was performed by changing the ambient temperature to -5°C and 0.
℃, 3℃, 5℃, 8℃, 10℃, 20℃, 30℃, 40
Electrodes were manufactured under 13 different conditions (℃, 50℃, 60℃, 70℃, and 80℃) and batteries were assembled. In this case as well, this step of ripening was carried out in a conventional manner. Other atmospheric conditions at this time are carbon dioxide concentration of 30
%, exposure time 15 hours, and relative humidity 60%. The electrode plate group configuration, electrolyte solution, and test conditions are as in Example 1.
is the same as

第2図は、乾燥雰囲気温度と電池の放電持続時
間との関係を示す。図から明らかなように、雰囲
気温度が5℃未満では放電時間は短くなり、また
40℃以上においても短くなることがわかる。
FIG. 2 shows the relationship between drying ambient temperature and battery discharge duration. As is clear from the figure, when the ambient temperature is less than 5℃, the discharge time becomes shorter;
It can be seen that it becomes shorter even at temperatures above 40°C.

実施例 3 実施例1と同じ格子を使つて、格子へのペース
ト充てん後の乾燥雰囲気曝露時間を、2、5、
8、10、12、15、18、20、25、30、35、40、45、
50時間と変えて、14種類の条件のもとで極板を製
造して電池を組んだ。このときの雰囲気の他の条
件は、炭酸ガス濃度30%、雰囲気温度20℃、相対
湿度60%であつた。極板群構成、電解液および試
験条件は、実施例1と同じである。
Example 3 Using the same grid as in Example 1, the drying atmosphere exposure time after filling the grid with paste was varied from 2 to 5.
8, 10, 12, 15, 18, 20, 25, 30, 35, 40, 45,
Instead of 50 hours, they produced electrode plates and assembled batteries under 14 different conditions. Other atmospheric conditions at this time were a carbon dioxide concentration of 30%, an ambient temperature of 20° C., and a relative humidity of 60%. The electrode plate group configuration, electrolyte solution, and test conditions are the same as in Example 1.

第3図は、乾燥雰囲気曝露時間と電池の放電持
続時間との関係を示す。図から明らかなように、
雰囲気曝露時間が10時間未満のとき放電持続時間
は短くなり、また40時間以上においても短くなる
ことがわかる。また別途、上記炭酸ガス濃度を増
加し、80%にすると、第3図Bのように効果の現
れる曝露時間は、1時間以内でも効果が見られ、
好ましくは1時間以上で、長時間のものと大差の
ないものが得られる。逆に、10%に下げた場合
は、長時間の曝露でも低下してこないことをCは
示している。このように炭酸ガスの雰囲気によつ
ては、極度に短時間の処理が可能である。
FIG. 3 shows the relationship between dry atmosphere exposure time and battery discharge duration. As is clear from the figure,
It can be seen that the discharge duration becomes short when the atmosphere exposure time is less than 10 hours, and also becomes shorter when the atmosphere exposure time is 40 hours or more. Separately, when the carbon dioxide concentration is increased to 80%, the effect can be seen even within 1 hour, as shown in Figure 3B.
Preferably, the time is 1 hour or more, and the result is that there is no significant difference between the time and the time. Conversely, when lowered to 10%, C shows that it does not decrease even with long-term exposure. In this way, depending on the carbon dioxide atmosphere, extremely short processing times are possible.

実施例 4 実施例1と同じ格子を使つて、格子へのペース
ト充てん後の乾燥工程中雰囲気の相対湿度が、10
%、20%、30%、40%、50%、60%、70%、80
%、85%、90%、95%と変えて11種類の条件のも
とで極板を製造し、電池を組んだ。このときの雰
囲気の他の条件は、炭酸ガス濃度30%、雰囲気温
度20℃、雰囲気曝露時間15時間であつた。極板群
構成、電解液および試験条件は、実施例1と同じ
である。
Example 4 Using the same grid as in Example 1, the relative humidity of the atmosphere during the drying process after filling the grid with paste was 10
%, 20%, 30%, 40%, 50%, 60%, 70%, 80
%, 85%, 90%, and 95%, and produced electrode plates and assembled batteries under 11 different conditions. Other atmospheric conditions at this time were a carbon dioxide concentration of 30%, an ambient temperature of 20° C., and an atmosphere exposure time of 15 hours. The electrode plate group configuration, electrolyte solution, and test conditions are the same as in Example 1.

第4図は、乾燥工程中雰囲気の相対湿度と放電
時間との関係を示す。図から明らかなように、雰
囲気の相対湿度が、40%未満では放電持続時間は
短くなり、また80%以上になつても短くなること
がわかる。
FIG. 4 shows the relationship between the relative humidity of the atmosphere and the discharge time during the drying process. As is clear from the figure, the discharge duration becomes short when the relative humidity of the atmosphere is less than 40%, and even when it becomes 80% or more.

実施例 5 まず常法によつて、鉛−カルシウム−スズ合金
の格子を用いた。鉛粉、水を混合し、硫酸を滴下
してペースト状に練合した。このペーストを上記
格子体に塗着後充てんした。これを、炭酸ガス30
%含有大気で満たされた室に、20℃にて15時間放
置して乾燥し、その後常法によつて15時間熟成を
して正極板を製造した。練塗量は、熟成後の値で
ほぼ等量となるようにした。上記のように炭酸ガ
ス含有大気中で乾燥した極板をD、従来の自然大
気中で乾燥した極板をEとして、比較試験をし
た。
Example 5 First, a lead-calcium-tin alloy lattice was used in a conventional manner. Lead powder and water were mixed, and sulfuric acid was added dropwise to mix them into a paste. This paste was applied to the grid and then filled. Add this to 30 carbon dioxide gas
% in a chamber filled with air at 20° C. for 15 hours to dry, and then matured for 15 hours in a conventional manner to produce a positive electrode plate. The amount of kneading was made to be approximately equal to the value after ripening. A comparative test was conducted using the electrode plate dried in the carbon dioxide-containing atmosphere as D and the conventional electrode plate dried in the natural atmosphere as E.

これらの正極板4枚と、極板1枚あたりの放電
容量が正極のそれに等しい公知のペースト式負極
板5枚を、ポリエチレンの袋状セパレータを介し
て交互に重ね合わせて単電池を構成し、充電完了
時の硫酸電解液の比重が1.27となるように調整し
た。これらの電池を−15℃の温度において、
300Aの電流で端子電圧が1.0Vになるまで放電す
る急放電試験をした。その試験結果を第5図に示
す。図から明らかなように、急放電試験における
放電持続時間は、DはEより約1.4倍長く、また
放電電圧(5秒目電圧)は、約50mV高いことが
わかり、炭酸ガス含有大気中での乾燥は、高性能
化に大きく効果のあることがわかる。
These four positive electrode plates and five known paste-type negative electrode plates whose discharge capacity per plate is equal to that of the positive electrode are stacked alternately with polyethylene bag-shaped separators interposed to form a single cell, The specific gravity of the sulfuric acid electrolyte was adjusted to 1.27 upon completion of charging. These batteries at a temperature of -15℃,
A rapid discharge test was conducted with a current of 300A until the terminal voltage reached 1.0V. The test results are shown in FIG. As is clear from the figure, the discharge duration in the rapid discharge test was approximately 1.4 times longer for D than for E, and the discharge voltage (5th second voltage) was approximately 50 mV higher, indicating that It can be seen that drying has a great effect on improving performance.

このような効果は、本発明のいくつかの例に示
すように、ペースト塗着後の工程で炭酸ガスに接
触する工程を経ることによつて、化学反応を受
け、良い特性をもたらすものである。実施例で
も、ペースト乾燥の初期に炭酸ガスとの接触を実
施する例を示したが、常法による熟成過程のいか
なる段階でも適用できる。ただし、反応は湿つた
条件の方が好ましいので、完全に乾燥した未化成
板の場合には、水に浸漬するか、霧吹きなどによ
り、極板を湿らせ本発明を適用するとより効果が
ある。なお段階としては、上例のように、ペース
トを乾燥させる段階が、そのまま活用できるの
で、工程は増えず、効率的である。それと同時
に、初期乾燥後、多孔体の構成が決定される前に
処理をするので、活物質のつながりを改めて破壊
する危険性も少なく、若干生成物の状況も、完全
に乾燥した未化成板に適用する場合と異なる。し
たがつて、信頼性のコントロールをする上におい
て有利であろう。なお、実施例においては、エキ
スパンデツドメタルの格子を使用したペースト式
極板について述べたが、本発明の効果は、この実
施例に限らず、格子が鋳造メタル、パンチングメ
タルであつても同様の効果が得られる。
As shown in some examples of the present invention, such an effect is caused by a chemical reaction that occurs through a step of contacting carbon dioxide gas after application of the paste, resulting in good properties. . In the examples, an example was shown in which the contact with carbon dioxide gas was carried out at the beginning of drying the paste, but it can be applied at any stage of the conventional ripening process. However, since the reaction is preferably carried out under moist conditions, in the case of a completely dry unformed plate, it is more effective to apply the present invention by moistening the plate by immersing it in water or by spraying it with water. As for the steps, as in the above example, the step of drying the paste can be used as is, so the number of steps is not increased and it is efficient. At the same time, since the treatment is carried out after the initial drying and before the composition of the porous body is determined, there is less risk of destroying the connections between the active materials, and the state of the product is slightly changed to a completely dried unformed board. Different cases apply. Therefore, it would be advantageous in controlling reliability. In the embodiment, a paste-type electrode plate using an expanded metal lattice was described, but the effects of the present invention are not limited to this embodiment, and the same effect can be obtained even if the lattice is made of cast metal or punched metal. The effect of this can be obtained.

以上のように、本発明によれば、活物質の表面
に、放電反応を促進させるような塩基性炭酸鉛か
らなると推定される多孔体が形成されて、高率放
電における活物質利用率が高まり、従つて、電池
の高出力、高容量化がはかれて、電池性能を著し
く向上改善することができる。
As described above, according to the present invention, a porous body estimated to be made of basic lead carbonate that promotes the discharge reaction is formed on the surface of the active material, and the utilization rate of the active material in high rate discharge is increased. Therefore, high output and high capacity of the battery can be achieved, and the battery performance can be significantly improved.

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

第1図は乾燥工程雰囲気中の炭酸ガス濃度と鉛
電池の急放電持続時間との関係を示す図、第2図
は乾燥工程雰囲気の温度と鉛電池の急放電持続時
間との関係を示す図、第3図は、乾燥工程雰囲気
曝露時間と鉛電池の急放電持続時間との関係を示
す図、第4図は乾燥工程雰囲気中相対湿度と鉛電
池の急放電持続時間との関係を示す図、第5図は
鉛電池の急放電時の電圧変化の比較を示す。
Figure 1 is a diagram showing the relationship between the carbon dioxide concentration in the drying process atmosphere and the rapid discharge duration of a lead battery, and Figure 2 is a diagram showing the relationship between the temperature of the drying process atmosphere and the rapid discharge duration of a lead battery. , Figure 3 is a diagram showing the relationship between the drying process atmosphere exposure time and the rapid discharge duration of the lead battery, and Figure 4 is a diagram showing the relationship between the relative humidity in the drying process atmosphere and the rapid discharge duration of the lead battery. , FIG. 5 shows a comparison of voltage changes during rapid discharge of lead batteries.

Claims (1)

【特許請求の範囲】 1 ペーストを支持体に塗着後、化成充電に至る
までの乾燥熟成工程において、炭酸ガス濃度10%
以上80%未満、温度5℃以上50℃未満、相対湿度
40〜80%の雰囲気に曝露する工程を含むことを特
徴とする鉛蓄電池用ペースト式電極の製造法。 2 炭酸ガスを含む雰囲気への曝露工程が、ペー
スト塗着後の初期乾燥工程で行われる特許請求の
範囲第1項記載の鉛蓄電池用ペースト式電極の製
造法。 3 炭酸ガスを含む雰囲気への曝露工程において
電極を曝露する時間が、1時間以上である特許請
求の範囲第1項記載の鉛蓄電池用ペースト式電極
の製造法。
[Claims] 1. After applying the paste to the support, in the dry aging process up to chemical charging, the carbon dioxide concentration is 10%.
80% or more, temperature 5℃ or more and less than 50℃, relative humidity
A method for producing a paste-type electrode for a lead-acid battery, comprising a step of exposing to an atmosphere of 40 to 80%. 2. The method for producing a paste-type electrode for a lead-acid battery according to claim 1, wherein the step of exposing to an atmosphere containing carbon dioxide gas is performed in an initial drying step after applying the paste. 3. The method for producing a paste-type electrode for a lead-acid battery according to claim 1, wherein the electrode is exposed for one hour or more in the step of exposing the electrode to an atmosphere containing carbon dioxide gas.
JP56069527A 1981-05-08 1981-05-08 Manufacture of pasted electrode for lead acid battery Granted JPS57185673A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56069527A JPS57185673A (en) 1981-05-08 1981-05-08 Manufacture of pasted electrode for lead acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56069527A JPS57185673A (en) 1981-05-08 1981-05-08 Manufacture of pasted electrode for lead acid battery

Publications (2)

Publication Number Publication Date
JPS57185673A JPS57185673A (en) 1982-11-15
JPS6322015B2 true JPS6322015B2 (en) 1988-05-10

Family

ID=13405279

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56069527A Granted JPS57185673A (en) 1981-05-08 1981-05-08 Manufacture of pasted electrode for lead acid battery

Country Status (1)

Country Link
JP (1) JPS57185673A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0642365B2 (en) * 1986-09-09 1994-06-01 新神戸電機株式会社 Method for manufacturing electrode plate for lead acid battery
JP2006120573A (en) * 2004-10-25 2006-05-11 Furukawa Battery Co Ltd:The Negative electrode plate for control valve type lead-acid battery, and control valve type lead-acid battery using the above negative electrode plate

Also Published As

Publication number Publication date
JPS57185673A (en) 1982-11-15

Similar Documents

Publication Publication Date Title
US4338163A (en) Curing of tetrabasic lead pasted battery electrodes
US4381250A (en) Curing of tetrabasic lead pasted battery electrodes
US4331516A (en) Curing of tetrabasic lead pasted battery electrodes
JPS6322015B2 (en)
JP3152770B2 (en) Manufacturing method of thin lead-acid battery
JPS58115775A (en) Lead-acid battery
JPH08138657A (en) Manufacturing method of electrode plate for lead-acid battery
JPS6386258A (en) Manufacture of lead acid battery
US2952726A (en) Storage batteries
JPH05166504A (en) Manufacture of lead-acid battery positive electrode plate
JPS6229064A (en) Manufacture of positive electrode plate for lead storage battery
JP2773311B2 (en) Manufacturing method of sealed lead-acid battery
JPH11273710A (en) Lead-acid battery electrolyte additive, lead-acid battery, method of manufacturing lead-acid battery, and use of lead-acid battery electrolyte additive
JPS6030054A (en) Manufacture of plate for paste type lead-acid battery
JPS59157969A (en) Manufacture of lead storage battery
JP3427402B2 (en) Method for manufacturing electrode plate for lead-acid battery
JPH05205732A (en) Manufacture of anode plate for lead-acid battery
JPH08236106A (en) Manufacturing method of paste for lead-acid battery anode plate
JPH04292859A (en) Manufacture of anode plate for lead battery
JPH0428161A (en) Manufacture of lead battery
JPS61142667A (en) Manufacture of positive plate for lead storage battery
JPS62216167A (en) Cathode active material for lead-acid batteries
JPH03145056A (en) Manufacture of positive plate for lead-acid battery
JPH01307169A (en) Manufacture of organic solvent battery
JPS59157959A (en) Manufacture of lead-acid battery