JPH0443563A - Manufacturing method of positive electrode plate for sealed lead-acid battery - Google Patents

Manufacturing method of positive electrode plate for sealed lead-acid battery

Info

Publication number
JPH0443563A
JPH0443563A JP2152018A JP15201890A JPH0443563A JP H0443563 A JPH0443563 A JP H0443563A JP 2152018 A JP2152018 A JP 2152018A JP 15201890 A JP15201890 A JP 15201890A JP H0443563 A JPH0443563 A JP H0443563A
Authority
JP
Japan
Prior art keywords
plate
active material
electrode plate
capacity
acid battery
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
JP2152018A
Other languages
Japanese (ja)
Inventor
Akihiko Sano
佐野 昭彦
Kiichi Koike
喜一 小池
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 JP2152018A priority Critical patent/JPH0443563A/en
Publication of JPH0443563A publication Critical patent/JPH0443563A/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

  • Battery Electrode And Active Subsutance (AREA)

Abstract

PURPOSE:To manufacture a positive plate of high reliability for a sealed lead-acid battery by taking out the plate after partial discharge in a jar under formation after plate formation, preliminarily drying the plate until the water content of the plate reaches the predetermined concentration for active material at the predetermined temperature, and further drying the plate at the predetermined temperature. CONSTITUTION:After plate formation, partial discharge is performed in a jar under formation. Then, the plate is taken out from the jar, and subjected to a preliminary drying process at temperature in the range of 30 deg.C to 40 deg.C, until a water content in the plate becomes 0.03 to 0.05 g per gram of active material. Thereafter, the plate is dried at temperature in the range of 150 deg.C to 200 deg.C. As a result, both residual and recovery capacity becomes high, and capacity dispersion becomes approximately con stant, irrespective of a shelving period. According to the aforesaid construction, the dispersion of battery performance can be reduced, and the stability of active material at an interface with a grid can be improved. In addition, an excessive capacity drop after shelving can be prevented, and the sealed lead-acid battery of high reliability can be manufactured.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は密閉形鉛蓄電池用正極板の製造法に関し、とく
に化成終了後の乾燥方法の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for manufacturing a positive electrode plate for a sealed lead-acid battery, and in particular to an improvement in a drying method after completion of chemical formation.

従来の技術 鉛蓄電池は、他の電池と比べて比較的エネルギー密度か
高く経済性に優れているため各分野で用いられている。
BACKGROUND OF THE INVENTION Lead-acid batteries are used in various fields because they have a relatively high energy density and are economical compared to other batteries.

しかし、放置後の容量の回復性について、一部問題を残
している。従来、密閉形鉛蓄電池用正極板は、化成終了
後化成槽中から取り出し、極板表面の硫酸分を水洗除去
したのち、直ちに105℃の乾燥炉中で乾燥していた。
However, some problems remain regarding capacity recovery after being left unused. Conventionally, a positive electrode plate for a sealed lead-acid battery was taken out of the chemical conversion tank after completion of chemical formation, washed with water to remove sulfuric acid from the surface of the electrode plate, and then immediately dried in a drying oven at 105°C.

発明が解決しようとする課題 しかし従来の密閉形鉛蓄電池用正極板の乾燥方法では極
板中に多量の水分を含んだ状態で乾燥を行うため、乾燥
初期には、極板が高温高湿状態となり、正極活物質およ
び正極活物質と格子界面に不安定な鉛酸化物が生成しや
すくなるため以下の欠点があった。
Problems to be Solved by the Invention However, in the conventional method of drying a positive electrode plate for a sealed lead-acid battery, the electrode plate is dried in a state in which a large amount of moisture is contained in the electrode plate. As a result, unstable lead oxide is likely to be generated in the positive electrode active material and the lattice interface with the positive electrode active material, resulting in the following drawbacks.

(1)不安定な鉛酸化物(たとえばt−Pb。(1) Unstable lead oxides (e.g. t-Pb).

Pboxなど)は、注液時に硫酸によりPbSO4を生
成するが、とくに格子と活物質界面にできた硫酸鉛は、
長期間放置すると充電しても回復しない絶縁被膜層を形
成するため、容量か低下するとともに容量バラツキか大
となる。
Pbox, etc.) generates PbSO4 with sulfuric acid during injection, but especially lead sulfate formed at the interface between the lattice and the active material.
If left for a long period of time, an insulating film layer is formed that does not recover even when charged, resulting in a decrease in capacity and large variations in capacity.

(2)正極活物質自体の安定性か低下するため放置中の
自己放電が大となるとともに充電しても容量の回復性が
悪い。
(2) The stability of the positive electrode active material itself decreases, resulting in increased self-discharge during storage and poor capacity recovery even after charging.

本発明はこのような課題を解決するもので、信顕性の高
い密閉形鉛蓄電池用正極板の製造法を提供することを目
的とする。
The present invention solves these problems and aims to provide a method for manufacturing a positive electrode plate for a sealed lead-acid battery with high reliability.

課題を解決するための手段 以上のような課題を解決するため本発明の密閉形鉛蓄電
池用正極板の製造法は、極板化成終了後、化成槽中で部
分放電した後極板を化成槽から取り出し、30〜40℃
の温度で極板中の水分量が活物質1g当たり0.03〜
0.05gとなるまで極板を予備乾燥した後、150〜
200℃の温度で乾燥するものである。
Means for Solving the Problems In order to solve the above-mentioned problems, the method for producing a positive electrode plate for a sealed lead-acid battery of the present invention is to provide a method for producing a positive electrode plate for a sealed lead acid battery of the present invention. Take it out from 30-40℃
The water content in the electrode plate is 0.03 to 1 g of active material at a temperature of
After pre-drying the electrode plate until it weighs 0.05g, 150 ~
It is dried at a temperature of 200°C.

作用 この構成により、極板の格子と活物質界面に、化成槽中
での部分放電により硫酸鉛を形成させて安定化し、電池
形成後充電により容量を回復させるとともに、30〜4
0℃で極板を予備乾燥した後150〜200℃で短時間
で極板を乾燥することにより、高温高湿中において正極
活物質および正極活物質と格子界面に不安定な鉛酸化物
が生成するのを抑制することとなる。
Effect: With this configuration, lead sulfate is formed and stabilized at the interface between the grid of the electrode plate and the active material by partial discharge in the chemical formation tank, and the capacity is restored by charging after battery formation, and the
By pre-drying the electrode plate at 0℃ and then drying the electrode plate at 150-200℃ for a short time, unstable lead oxide is generated in the positive electrode active material and the lattice interface between the positive electrode active material and the positive electrode active material in high temperature and high humidity. This will prevent them from doing so.

実施例 以下本発明の一実施例の密閉形鉛蓄電池用正極板の製造
法について図面をもとにして説明する。
EXAMPLE Hereinafter, a method for manufacturing a positive electrode plate for a sealed lead-acid battery according to an example of the present invention will be described with reference to the drawings.

密閉形鉛蓄電池用正極板となる極板を、比重1.10の
硫酸中で、活物質1gあたり0.50 Ahの電気量で
20時間化成を行った後、■従来法として化成終了後、
極板を水洗したのち105℃で1.5時間乾燥を行う。
After chemically forming the positive electrode plate for a sealed lead-acid battery in sulfuric acid with a specific gravity of 1.10 for 20 hours with an amount of electricity of 0.50 Ah per 1 g of active material, ■ After completing the chemical formation as a conventional method,
After washing the electrode plate with water, it is dried at 105° C. for 1.5 hours.

■本実施例によるものとして化成終了後、活物質1gあ
たり0.02Aの電流で0,5h放電した後、極板を水
洗し40℃で予備乾燥1h後、150℃で0.25 h
乾燥を行う。この2種の正極板を作成し電池性能を比較
した。電池の容量は10時間率容量0.2Ahであり、
容量試験は正極板容量により律則される構成で行った。
(2) As per this example, after completion of chemical formation, after discharging at a current of 0.02 A per 1 g of active material for 0.5 h, the electrode plate was washed with water, pre-dried at 40°C for 1 h, and then dried at 150°C for 0.25 h.
Perform drying. These two types of positive electrode plates were created and their battery performance was compared. The capacity of the battery is 10 hour rate capacity 0.2Ah,
The capacity test was conducted with a configuration determined by the capacity of the positive electrode plate.

放電は0.8CA相当の定電流、充電は2.45 V/
セル定電圧充電で行った。■の本実施例による構成の電
池は、放電量に相当する硫酸量を補正して注液を行い、
絶対硫酸量が■の従来法によるものと同じ量になるよう
にした。注液型電解比重は放置中の容量劣化を加速する
目的により通常1.34のものを1.40に高くして比
較した。電池を作成後、充放電を行い初期容量を測定後
、40℃放置を行った。
Discharging is constant current equivalent to 0.8 CA, charging is 2.45 V/
Cell constant voltage charging was performed. In the battery configured according to the present embodiment (2), the amount of sulfuric acid is corrected and injected according to the amount of discharge,
The absolute amount of sulfuric acid was made to be the same amount as in the conventional method (■). The specific gravity of the injection type electrolysis was increased from the usual 1.34 to 1.40 for the purpose of accelerating capacity deterioration during storage. After creating the battery, it was charged and discharged, the initial capacity was measured, and then left at 40°C.

第1図に40℃放置後の残存容量比率の比較、第2図に
残存容量測定後足電圧充電を行った時の回復容量比率の
比較を示す。
Fig. 1 shows a comparison of the remaining capacity ratio after being left at 40°C, and Fig. 2 shows a comparison of the recovered capacity ratio when performing voltage charging after measuring the remaining capacity.

本実施例によるものでは、残存容量1回復容量とともに
従来法に比べ優れている。とくに容量のバラツキにおい
ては、従来法では放置期間が長くなるにつれ大となる傾
向が見られるが、本実施例によるものでは放置期間によ
らずほぼ同じ値となっている。これは、活物質自体の安
定性が向上していることに起因するものと考えられる。
The method according to this embodiment has a recovery capacity of 1 remaining capacity and is superior to the conventional method. In particular, with respect to the variation in capacity, in the conventional method, there is a tendency for the variation to increase as the standing period becomes longer, but in the case of the present embodiment, the value remains almost the same regardless of the standing period. This is considered to be due to the improved stability of the active material itself.

40℃放置前の正極活物質中のPbO:量、Pb5n量
およびその他の残渣PbO,の定量分析を行い、従来法
と比較した。PbSO4量は本実施例によるものと従来
法との差はなかったが、pbo、量では本実施例による
ものは、従来法に比べ273に低下していた。これは本
実施例によるものが、活物質の安定性か向上しているこ
とを裏付けるものである。40℃X4M放置後残存容量
9回復容量の試験結果において、従来法によるものの中
で容量の低下の著しいものが発生している。これは、放
置中に格子と活物質の界面に硫酸鉛のバリアー層を形成
し、放電反応がこのバリアー層により遮断されることが
原因であることがわかった。このバリアー層は充電して
も回復しないために回復容量は低いままであった。
Quantitative analysis of the amount of PbO, the amount of Pb5n, and other residual PbO in the positive electrode active material before standing at 40° C. was performed and compared with the conventional method. Although there was no difference in the amount of PbSO4 between the present example and the conventional method, the pbo amount was reduced to 273 in the present example compared to the conventional method. This confirms that the stability of the active material in this example is improved. In the test results of residual capacity 9 recovery capacity after being left at 40° C. for 4M, a significant decrease in capacity occurred among those using the conventional method. It was found that this was caused by the formation of a lead sulfate barrier layer at the interface between the lattice and the active material during standing, and the discharge reaction being blocked by this barrier layer. This barrier layer did not recover even after charging, so its recovery capacity remained low.

一方本実施例によるものでは、化成後の部分放電により
、格子と活物質界面の活物質の安定性が向上しているこ
とにより従来法に見られるような容量の低下はなかった
On the other hand, in this example, the stability of the active material at the interface between the lattice and the active material was improved due to the partial discharge after chemical formation, so there was no decrease in capacity as seen in the conventional method.

発明の効果 以上の実施例の説明で明らかなように、本発明の密閉形
鉛蓄電池用正極板の製造法によれば、正極活物質の安定
性向上による放置中の自己放電量低減およびバラツキを
低減できるとともに、格子と活物質界面の活物質の安定
性を向上することによる放置後の急激な容量低下を防止
できるため、信頼性の高い密閉形鉛蓄電池を製造できる
製造法を提供できる。
Effects of the Invention As is clear from the description of the embodiments above, the method for manufacturing a positive electrode plate for a sealed lead-acid battery of the present invention reduces the amount of self-discharge during storage and reduces variation due to improved stability of the positive electrode active material. In addition, it is possible to prevent a sudden decrease in capacity after storage by improving the stability of the active material at the interface between the lattice and the active material, thereby providing a manufacturing method that can manufacture a highly reliable sealed lead-acid battery.

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

第1図は本発明の一実施例の密閉形鉛蓄電池用正極板の
製造法と従来法との40℃放置後の残存容量比率の比較
を示す図、第2図は同回復容量比率の比較を示す図であ
る。 代理人の氏名 弁理士 粟野重孝 ほか1名* l ’
M 7′ii′l(町 旅1瓶r%I′l(M)
Figure 1 is a diagram showing a comparison of the remaining capacity ratio after being left at 40°C between the manufacturing method of a positive electrode plate for a sealed lead-acid battery according to an embodiment of the present invention and the conventional method, and Figure 2 is a comparison of the recovered capacity ratio. FIG. Name of agent: Patent attorney Shigetaka Awano and one other person* l'
M 7'ii'l (Town trip 1 bottle r% I'l (M)

Claims (1)

【特許請求の範囲】[Claims] 極板化成終了後、化成槽中で部分放電した後、極板を化
成槽から取り出し、30℃〜40℃の温度で極板中水分
量が活物質1gあたり0.03〜0.05gとなるまで
極板を予備乾燥した後、150℃〜200℃の温度で極
板を乾燥する密閉形鉛蓄電池用正極板の製造法。
After completing the electrode plate formation, after partially discharging in the formation tank, the electrode plate is taken out from the formation tank, and at a temperature of 30°C to 40°C, the water content in the electrode plate becomes 0.03 to 0.05g per 1g of active material. A method for producing a positive electrode plate for a sealed lead-acid battery, which comprises pre-drying the electrode plate to a temperature of 150°C to 200°C.
JP2152018A 1990-06-11 1990-06-11 Manufacturing method of positive electrode plate for sealed lead-acid battery Pending JPH0443563A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2152018A JPH0443563A (en) 1990-06-11 1990-06-11 Manufacturing method of positive electrode plate for sealed lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2152018A JPH0443563A (en) 1990-06-11 1990-06-11 Manufacturing method of positive electrode plate for sealed lead-acid battery

Publications (1)

Publication Number Publication Date
JPH0443563A true JPH0443563A (en) 1992-02-13

Family

ID=15531262

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2152018A Pending JPH0443563A (en) 1990-06-11 1990-06-11 Manufacturing method of positive electrode plate for sealed lead-acid battery

Country Status (1)

Country Link
JP (1) JPH0443563A (en)

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