JPH08329989A - How to charge a sealed lead acid battery - Google Patents

How to charge a sealed lead acid battery

Info

Publication number
JPH08329989A
JPH08329989A JP7139088A JP13908895A JPH08329989A JP H08329989 A JPH08329989 A JP H08329989A JP 7139088 A JP7139088 A JP 7139088A JP 13908895 A JP13908895 A JP 13908895A JP H08329989 A JPH08329989 A JP H08329989A
Authority
JP
Japan
Prior art keywords
charging
cell
battery
stage
charge
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
JP7139088A
Other languages
Japanese (ja)
Inventor
Harumi Murochi
晴美 室地
Masato Ishiwatari
正人 石渡
Toshihiro Inoue
利弘 井上
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 JP7139088A priority Critical patent/JPH08329989A/en
Publication of JPH08329989A publication Critical patent/JPH08329989A/en
Pending legal-status Critical Current

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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

  • Charge And Discharge Circuits For Batteries Or The Like (AREA)
  • Secondary Cells (AREA)

Abstract

(57)【要約】 【目的】 極板の格子に鉛−カルシウム−すず合金を用
いた密閉形鉛蓄電池の充電電圧を検出し、電流値を変化
させてタイマーにて充電を終了させる多段定電流充電方
式で、充電受入れ性の影響や各セル室の差を少なくし
て、各段の充電電気量を安定化し、電池の長寿命化・高
信頼性化を可能とする。 【構成】 密閉形鉛蓄電池の充電方法において、1段目
の充電電流を0.4CA以下とし、2段目以降は充電電
流(in)をi1>in+1>in+2とし、かつ充電期間(T
n)をT1<Tn+1<Tn+2(n>1)とした多段定電流の
充電において、電池の充電電圧検出値を2.32V/セ
ル〜2.37V/セルとした。
(57) [Summary] [Purpose] A multi-stage constant current that detects the charging voltage of a sealed lead-acid battery using lead-calcium-tin alloy in the grid of the electrode plate and changes the current value to end charging with a timer. The charging system reduces the influence of charge acceptance and the difference between cell chambers, stabilizes the amount of electricity charged at each stage, and enables longer battery life and higher reliability. [Configuration] In the charging method of sealed lead acid battery, the charging current of the first stage and less 0.4CA, the second and subsequent stages charge current (i n) i 1> i n + 1> i n + 2 and then , And the charging period (T
In the multi-stage constant current charging in which n ) is T 1 <T n + 1 <T n + 2 (n> 1), the detected charging voltage of the battery is set to 2.32 V / cell to 2.37 V / cell.

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、民生用ポータブル機器
の電源等のサイクル用途に利用される密閉形鉛蓄電池の
充電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 for charging a sealed lead-acid battery used for cycling such as a power source for portable consumer appliances.

【0002】[0002]

【従来の技術】近年、密閉形鉛蓄電池は、民生用ポータ
ブル電源から電動車両まで幅広い用途で使用されるよう
になってきた。これらの用途のうち充放電サイクルを繰
り返すような用途における充電方法としては、定電圧充
電、定電流充電、Vテーパ充電、2段定電流充電等が提
案されている。このなかで、2段定電流充電方式は取扱
いの容易さの点から、電動車両等の用途では広く採用さ
れている。
2. Description of the Related Art In recent years, sealed lead-acid batteries have come to be used in a wide range of applications from consumer portable power supplies to electric vehicles. Among these applications, constant-voltage charging, constant-current charging, V-taper charging, two-step constant-current charging and the like have been proposed as charging methods for applications in which charge / discharge cycles are repeated. Among them, the two-stage constant current charging method is widely used in applications such as electric vehicles because of its ease of handling.

【0003】従来採用されてきた2段定電流方式は、電
池の充電電圧を検出して、充電末期の電流値を小さく変
化させ、タイマーにて充電を終了させる方式であり、そ
の検出電圧は2.40V〜2.45V/セルに設定され
ていた。
The conventional two-stage constant current system is a system in which the charging voltage of the battery is detected, the current value at the end of charging is changed to a small value, and charging is terminated by a timer. It was set to 0.40V to 2.45V / cell.

【0004】[0004]

【発明が解決しようとする課題】この2段定電流充電に
おいては、充電電池電圧が検出電圧に上昇するまでの時
間が1段目の充電電気量を決定し、1段目の充電電気量
を左右する。通常は1段目の電気量が全体の充電電気量
の80%程度を占めるため、放電量の多少によらず、適
切な充電を行うことが可能となっている。
In this two-stage constant current charging, the time until the charging battery voltage rises to the detection voltage determines the charge electric quantity of the first step, and the charge electric quantity of the first step is determined. It depends. Normally, the amount of electricity in the first stage occupies about 80% of the total amount of electricity charged, so that proper charging can be performed regardless of the amount of discharge.

【0005】しかし、1段目の充電電気量は、放電量が
同じでも一定とは限らず、全体の充電電気量も異なるケ
ースがある。
However, the amount of electricity charged in the first stage is not always constant even if the amount of electricity discharged is the same, and there are cases where the overall amount of electricity charged is different.

【0006】その要因と考えられるのは、鉛蓄電池側の
充電受入れ性がある。鉛蓄電池の電池充電電圧は、負極
より水素ガスが発生した時に急上昇する。負極活物質の
鉛は海綿状で、多数の孔が存在して活物質の表面積が広
くなっており、充放電反応がスムーズにおこるように設
計されている。
It is considered that the factor is the charge acceptability on the lead storage battery side. The battery charging voltage of a lead storage battery rises sharply when hydrogen gas is generated from the negative electrode. The lead of the negative electrode active material is sponge-like, has a large number of pores and has a large surface area of the active material, and is designed so that the charge / discharge reaction can smoothly occur.

【0007】しかし、鉛粒子は充放電の繰り返しにより
徐々に凝集する傾向にあり、その表面積は小さくなる。
表面積が小さくなると、見かけの電流密度は大きくな
り、その結果充放電反応の効率は低下し、水素が発生し
やすくなるとともに、充電電池電圧は上昇しやすくな
る。したがって、1段目の充電電気量は少なくなる。す
なわち、同じ電池を同じ条件で充放電しても、初期と充
放電サイクルを繰り返した後では1段目の充電電気量が
異なる。
However, lead particles tend to gradually aggregate due to repeated charging and discharging, and their surface area becomes smaller.
When the surface area is small, the apparent current density is large, and as a result, the efficiency of the charge / discharge reaction is decreased, hydrogen is easily generated, and the charging battery voltage is easily increased. Therefore, the amount of electricity charged in the first stage decreases. That is, even if the same battery is charged and discharged under the same conditions, the amount of electricity charged in the first stage is different between the initial stage and after repeating the charge and discharge cycle.

【0008】このように、1段目の充電電気量は放電量
と相関があるとは限らず、不安定である。また、通常鉛
蓄電池は3セル室もしくは6セル室を直列に接続して1
個の電池を構成するため、電圧の検出は3セル室もしく
は6セル室を合算した値で行うことになり、各セル室の
差が生じやすい。周囲温度もしくは連続充放電等の使用
条件によっては、負極の充電受入れ性の低下の差が大き
く、適切な充電を行えずに早期に電池の寿命に至ってし
まうことがあった。
As described above, the quantity of electricity charged in the first stage does not always correlate with the quantity of discharge, and is unstable. In addition, a lead-acid battery usually has a 3-cell chamber or a 6-cell chamber connected in series.
Since each battery is configured, the voltage is detected by a value obtained by adding the three cell chambers or the six cell chambers, and a difference between the cell chambers is likely to occur. Depending on the operating conditions such as the ambient temperature or continuous charge and discharge, there is a large difference in the charge acceptability of the negative electrode, which may lead to an early battery life without proper charging.

【0009】本発明は、上記従来の問題点を解決するも
ので、充放電サイクルを繰り返す用途において、密閉形
鉛蓄電池の長寿命化・高信頼性化を可能とする充電方法
を提供することを目的とする。
The present invention solves the above-mentioned conventional problems, and provides a charging method capable of extending the service life and increasing the reliability of a sealed lead-acid battery in applications in which charge and discharge cycles are repeated. To aim.

【0010】[0010]

【課題を解決するための手段】以上の課題を解決するた
めに、本発明は正極板、負極板およびセパレータよりな
り、極板の格子には鉛−カルシウム−すず合金を用いた
密閉形鉛蓄電池の1段目の充電で電池の充電電圧を検出
して電流値を変化させ、2段目以降の充電をタイマーに
て終了させる多段定電流充電方式で、充電電流、充電時
間、検出電圧を制御するものであり、1段目の充電電流
(i1)を0.4CA以下、2段目以降の充電電流
(in)をi1>in+1>in+2(n>1)とするととも
に、タイマーによる充電時間(Tn)をT1<Tn+1<T
n+2(n>1)として、前記検出電圧を2.32V/セ
ル〜2.37V/セルにて検知する充電方法である。
In order to solve the above-mentioned problems, the present invention comprises a positive electrode plate, a negative electrode plate and a separator, and a sealed lead acid battery using a lead-calcium-tin alloy in the grid of the electrode plate. Controls the charging current, charging time, and detection voltage with the multi-stage constant current charging method that detects the charging voltage of the battery in the first step of charging and changes the current value and terminates the charging of the second and subsequent steps with a timer. to is intended, first-stage charging current (i 1) the 0.4CA following, the second and subsequent stages charge current (i n) i 1> i n + 1> i n + 2 (n> 1) And the charging time (T n ) by the timer is T 1 <T n + 1 <T
It is a charging method in which the detected voltage is detected at 2.32 V / cell to 2.37 V / cell as n + 2 (n> 1).

【0011】[0011]

【作用】鉛蓄電池において通常の充電電圧である2.4
0V/セル〜2.45V/セルは水素が発生し始める電
圧であるが、2.37V/セルでは水素発生に至る以前
であるため、負極の充電受入れ性が検出電圧に達するま
での時間に与える影響は少なく、また、各セル室の差の
影響も少ない。すなわち、水素発生に起因する電流効率
の減少を抑制することができる。このように検出電圧を
低くすることによって、充電受入れ性の影響や各セル室
の差は少なくなり、1段目の充電電気量は安定化し、電
池の長寿命化、高信頼性化が可能となる。
[Operation] 2.4 which is a normal charging voltage in a lead storage battery
0V / cell to 2.45V / cell is the voltage at which hydrogen starts to be generated, but since 2.37V / cell is before the hydrogen generation, it is given in the time until the charge acceptability of the negative electrode reaches the detection voltage. There is little effect, and the effect of differences in each cell room is also small. That is, it is possible to suppress a decrease in current efficiency due to hydrogen generation. By lowering the detection voltage in this way, the influence of charge acceptability and the difference between the cell chambers are reduced, the amount of electricity charged in the first stage is stabilized, and the battery life can be extended and reliability can be increased. Become.

【0012】[0012]

【実施例】以下、本発明の充電方法の実施例について、
図面を用いて説明する。
EXAMPLES Examples of the charging method of the present invention will be described below.
This will be described with reference to the drawings.

【0013】電池は電圧、公称容量12V38Ah形電
池を使用した。電池1の外観は図1に示す通りで、I〜
VIの6個のセル室2が一列に並んだモノブロック構造で
ある。極板の格子としては鉛−カルシウム−すず合金を
用いた。充電仕様としては、n=1、すなわち2段定電
流方式とし、1段目を0.2CA、すなわち7.6A、
2段目を0.05CA、すなわち1.9Aとし、2段目
の充電をタイマーにて終了する方式とした。検出電圧お
よびタイマー時間を決める前の予備テストとして、電池
を38A定電流で9.6Vまで放電した後7.6Aで定
電流充電を行い、各セル室の充電電圧と水素発生量およ
び充電電気量を測定した。
As the battery, a voltage, nominal capacity 12V 38Ah type battery was used. The appearance of the battery 1 is as shown in FIG.
It has a monoblock structure in which six cell chambers 2 of VI are lined up in a row. A lead-calcium-tin alloy was used as the grid of the electrode plate. As the charging specification, n = 1, that is, a two-stage constant current system is used, and the first stage is 0.2 CA, that is, 7.6 A,
The second stage is set to 0.05 CA, that is, 1.9 A, and the second stage charging is completed by a timer. As a preliminary test before determining the detection voltage and the timer time, the battery was discharged to 9.6 V with a constant current of 38 A and then charged with constant current at 7.6 A, and the charging voltage of each cell chamber, the amount of hydrogen generation, and the amount of charge electricity Was measured.

【0014】各セル室の充電電圧と水素発生量の関係を
図2に、充電電圧と充電時間・充電電気量の関係を図3
に示す。
FIG. 2 shows the relationship between the charging voltage and the amount of hydrogen generated in each cell chamber, and FIG. 3 shows the relationship between the charging voltage and the charging time / charge amount.
Shown in

【0015】図2の結果より、セルの充電電圧が2.4
0Vまで上昇した時に水素発生が測定されることがわか
った。また図3より、セルの充電電圧は、2.32Vか
ら徐々に上昇が速くなることがわかった。これにより、
検討する検出電圧を、(a)2.30V/セル、(b)
2.32V/セル、(c)2.37V/セル、(d)
2.40V/セル、(e)2.45V/セルの5種類と
した。
From the result of FIG. 2, the charging voltage of the cell is 2.4.
It was found that hydrogen evolution was measured when rising to 0V. Moreover, from FIG. 3, it was found that the charging voltage of the cell gradually increased from 2.32V. This allows
The detection voltage to be examined is (a) 2.30 V / cell, (b)
2.32 V / cell, (c) 2.37 V / cell, (d)
There were five types, 2.40 V / cell and (e) 2.45 V / cell.

【0016】タイマー時間は、1段目の充電で各検出電
圧に達する充電電気量と2段目の充電電気量を合計して
放電電気量の120%となり、かつタイマー時間がT1
<Tn +1(n>1)となるように算出した。放電電気量
は25Ahであったので、各タイマー時間はそれぞれ、
5.4H、5.0H、4.6H、4.3H、4.2Hと
した。
The timer time is 120% of the discharged electricity quantity, which is the sum of the charged electricity quantity that reaches each detection voltage in the first-stage charging and the second-stage charge electricity quantity, and the timer time is T 1
It was calculated to be <T n +1 (n> 1). The amount of electricity discharged was 25 Ah, so each timer time
It was set to 5.4H, 5.0H, 4.6H, 4.3H, and 4.2H.

【0017】これら5種類の充電条件にて、12V38
Ah形電池の充放電サイクルテストを行った。放電条件
は38A定電流放電で9.6V終止とし、放電終了から
充電開始までを0分、充電終了から放電開始までを10
分とする連続充放電サイクルとなるようにした。周囲温
度は25±2℃とした。その充放電サイクルテスト結果
を図4に示す。
Under these five types of charging conditions, 12V38
A charge / discharge cycle test of an Ah battery was performed. The discharge condition was a constant current discharge of 38 A and a termination of 9.6 V, 0 minutes from the end of discharge to the start of charge, and 10 minutes from the end of charge to the start of discharge.
The continuous charge / discharge cycle is defined as minutes. The ambient temperature was 25 ± 2 ° C. The charge / discharge cycle test result is shown in FIG.

【0018】図4より明らかなように、(a)の検出電
圧2.30V/セルの充電条件の電池においては、約2
50サイクルで容量が初期の80%まで低下してしまっ
た。この容量低下品を解析したところ、容量は6セルす
べてにおいて低下しており、放電容量は正極活物質によ
って支配されていた。
As is clear from FIG. 4, in the case of the battery under the condition of the detection voltage of 2.30 V / cell shown in FIG.
After 50 cycles, the capacity had dropped to 80% of the initial capacity. When this capacity-decreased product was analyzed, the capacity was decreased in all 6 cells, and the discharge capacity was dominated by the positive electrode active material.

【0019】次に、この電池を(e)検出電圧2.45
V/セルの充電条件に変更し、充放電を5サイクル繰り
返したところ、容量は初期の95%まで回復した。この
ことから、容量低下の要因は正極板の充電不足と推定さ
れる。これは、1段目での切り替え電圧が低すぎて2段
目の小さい電流での充電量が多いため、正極に対し強制
的に行う充電が不足し、その結果正極の充電効率が低下
し、反応性の高い正極活物質の生成量が少なくなったた
めと考えられる。連続充放電サイクルにおいては、充放
電回数が多いため、反応性の高い正極活物質の量が徐々
に減少し、250サイクル程度で初期の80%に至るも
のと考えられる。
Next, this battery is used (e) with a detection voltage of 2.45.
When the charge condition of V / cell was changed and charging / discharging was repeated 5 cycles, the capacity recovered to 95% of the initial value. From this, it is estimated that the cause of the capacity decrease is insufficient charging of the positive electrode plate. This is because the switching voltage at the first stage is too low and the amount of charge at a small current at the second stage is large, so the amount of charge forcibly performed on the positive electrode is insufficient, resulting in a decrease in the charging efficiency of the positive electrode. This is probably because the amount of highly reactive positive electrode active material produced was reduced. It is considered that since the number of times of charge and discharge is large in the continuous charge and discharge cycle, the amount of the positive electrode active material having high reactivity gradually decreases, and reaches about 80% of the initial value in about 250 cycles.

【0020】また、(d)の検出電圧2.40V/セル
及び(e)の2.45V/セルの充電条件の電池では、
両方とも負極の容量が低下しており、特に、図1におけ
るセル3もしくはセル4、すなわち電槽中央に位置する
セルの劣化が大きかった。また、容量低下した電池の負
極活物質の硫酸保持量を初期品と比較したところ、
(d)の検出電圧2.40V/セルの電池で約12%、
(e)の検出電圧2.45V/セルの電池で約15%少
なかった。このことから、容量低下要因は、負極活物質
の表面積が低下して硫酸保持量が低下したための反応性
低下と考えられる。また、負極活物質の表面積減少は温
度が高いほど起こりやすく、放熱性の劣るセル3もしく
はセル4の劣化が他に比べて高くなっていた。
Further, in the battery under the charging condition of (d) the detection voltage of 2.40 V / cell and (e) of 2.45 V / cell,
In both cases, the capacity of the negative electrode was reduced, and in particular, the deterioration of cell 3 or cell 4 in FIG. 1, that is, the cell located in the center of the battery case was large. In addition, comparing the amount of sulfuric acid retained in the negative electrode active material of the battery with reduced capacity with the initial product,
Approximately 12% with the battery of detection voltage 2.40V / cell of (d),
It was about 15% less in the battery with the detection voltage of 2.45 V / cell in (e). From this, it is considered that the cause of the capacity decrease is the decrease in reactivity due to the decrease in the surface area of the negative electrode active material and the decrease in the amount of sulfuric acid retained. Further, the surface area of the negative electrode active material was more likely to decrease as the temperature was higher, and the deterioration of the cell 3 or cell 4 having poor heat dissipation was higher than the others.

【0021】一方、1段目の充電電気量に関しては、
(d)2.40V/セルの電池については初期は放電量
の87%であったのに対して200サイクル時点で放電
量の83%、2.45V/セルの電池については初期は
放電量の88%であったのに対して200サイクル時点
で放電量の80%と減少していた。また、(b)の2.
32V/セルの電池では初期は放電量の82%であった
のに対して500サイクル時点で放電量の78%、
(c)の2.37V/セルの電池については初期は放電
量の85%であったのに対して500サイクル時点で8
1%であり、1段目の充電電気量の減少量は少なかっ
た。なお、(a)の2.30V/セルの電池については
初期は放電量の79%であったのに対して200サイク
ル時点で78%であり、負極活物質の表面積減少の防止
という点では改善されているものと考えられる。
On the other hand, regarding the amount of electricity charged in the first stage,
(D) For the 2.40 V / cell battery, the initial discharge amount was 87%, whereas at 200 cycles, the discharge amount was 83%, and for the 2.45 V / cell battery, the initial discharge amount was 87%. While it was 88%, it decreased to 80% of the discharge amount at the time of 200 cycles. Also, in (b) 2.
In the case of the battery of 32V / cell, the discharge amount was 82% in the initial stage, but it was 78% of the discharge amount at the time of 500 cycles.
In the case of the 2.37 V / cell battery of (c), it was 85% of the discharge amount at the beginning, but 8 at the time of 500 cycles.
It was 1%, and the decrease in the amount of electricity charged in the first step was small. For the 2.30 V / cell battery of (a), the discharge amount was 79% in the initial stage, but was 78% at the time of 200 cycles, which is an improvement in terms of preventing reduction in the surface area of the negative electrode active material. It is thought to have been done.

【0022】以上の実施例で明らかなように、検出電圧
2.30V/セル、2.40V/セル、2.45V/セ
ルの充電条件では、比較的早期に容量が低下し、寿命に
至ってしまったが、2.32V/セル、2.37V/セ
ルの充電条件の電池においては、十分な充放電サイクル
寿命特性を得ることができた。
As is clear from the above embodiments, under the charging conditions of the detection voltage of 2.30 V / cell, 2.40 V / cell, and 2.45 V / cell, the capacity decreases relatively early and the life is reached. However, in a battery under the charging conditions of 2.32 V / cell and 2.37 V / cell, sufficient charge / discharge cycle life characteristics could be obtained.

【0023】また、検出電圧2.45V/セルの充電条
件の電池においては、充放電サイクルが進むにしたがっ
て電池中央部分の表面温度が徐々に上昇し、最大43℃
になった。これに伴い、検出電圧の直前において充電電
圧の上昇速度が遅くなる現象が観察された。これはガス
吸収反応が促進されたためと考えられる。
Further, in a battery under the condition that the detection voltage is 2.45 V / cell, the surface temperature of the central portion of the battery gradually rises as the charging / discharging cycle progresses, and the maximum temperature is 43 ° C.
Became. Along with this, it was observed that the rising speed of the charging voltage slowed down immediately before the detection voltage. This is probably because the gas absorption reaction was promoted.

【0024】密閉形鉛蓄電池においては、充電中に発生
する酸素と負極活物質である鉛とが反応し、酸素ガスの
吸収が生じる。この反応は発熱反応であるため、充電中
には電池の温度は上昇する。周囲の温度や充放電の頻度
によっては、電池の温度上昇が大きくなり、過電圧が小
さくなって電池電圧の上昇が少なくなるため、検出電圧
に達するまでの時間が長くなる場合がある。このような
場合には、1段目の充電電気量及び全体の充電電気量が
多くなる。周囲温度が高く検出電圧が高い場合には、充
電電圧が検出電圧まで到達せず、充電電流が切り変わら
ずに過充電になってしまうケースも考えられる。しか
し、検出電圧が2.32V/セル〜2.37V/セルの
範囲であれば、上記のような可能性はないと推定され
る。
In the sealed lead-acid battery, oxygen generated during charging reacts with lead, which is the negative electrode active material, to absorb oxygen gas. Since this reaction is an exothermic reaction, the temperature of the battery rises during charging. Depending on the ambient temperature and the frequency of charging / discharging, the temperature of the battery increases significantly, the overvoltage decreases, and the increase in the battery voltage decreases. Therefore, it may take a long time to reach the detection voltage. In such a case, the amount of electricity charged in the first stage and the amount of electricity charged as a whole increase. When the ambient temperature is high and the detection voltage is high, the charging voltage may not reach the detection voltage, and the charging current may not change to cause overcharging. However, if the detected voltage is in the range of 2.32 V / cell to 2.37 V / cell, it is estimated that there is no possibility as described above.

【0025】また、水素発生し始めた段階での電池電圧
は、その時の充電電流によって異なるが、0.4CA以
下であれば、2.37V/セルで水素が発生することは
ないことが確認されているため、充電電流値としては、
0.4CA以下が適切である。
Further, the battery voltage at the stage of starting hydrogen generation varies depending on the charging current at that time, but it is confirmed that hydrogen will not be generated at 2.37 V / cell at 0.4 CA or less. Therefore, as the charging current value,
0.4 CA or less is suitable.

【0026】さらに、1段目の充電電流に対して、2段
目以降の充電電流(in)をi1>i n+1>in+2(n>
1)とするとともに水素発生電圧に電池電圧が到達しな
いように充電電流を制御し、充電効率が低下しないよう
に制御することが肝要である。同時に、タイマーによる
充電時間はT1<Tn+1<Tn+2(n>1)とし、水素発
生による充電効率の低下と電池の発熱をセル間で均一に
なるようにすることにより、上記の充電方法の効果はよ
り明らかになる。
Further, for the charging current of the first stage, two stages
Charging current after the eye (in) I1> I n + 1> In + 2(N>
1) and the battery voltage does not reach the hydrogen generation voltage.
Control the charging current to prevent the charging efficiency from decreasing.
It is essential to control to. At the same time, by timer
Charging time is T1<Tn + 1<Tn + 2(N> 1), hydrogen generation
Reduces charging efficiency due to raw material and uniform heat generation of battery between cells
By doing so, the effect of the above charging method is improved.
Will be clear.

【0027】すなわち、充電検出電圧を2.32V/セ
ル〜2.37V/セルにて検知するとともに、充電電流
と充電時間を制御することで、サイクル寿命特性に優れ
た電池の提供が可能となる。
That is, by detecting the charge detection voltage at 2.32 V / cell to 2.37 V / cell and controlling the charge current and the charge time, it is possible to provide a battery having excellent cycle life characteristics. .

【0028】なお、本発明の検出電圧は、水素過電圧の
異なる鉛−アンチモン合金等を極板格子の使用した場合
には適用されない。
The detection voltage of the present invention is not applied when lead-antimony alloys having different hydrogen overvoltages are used for the electrode plate grid.

【0029】[0029]

【発明の効果】以上のように、本発明の密閉形鉛蓄電池
の充電方法によれば、充電受入れ性の影響や各セル室の
差は少なくなり、1段目の充電電気量が安定化するた
め、電池の長寿命化・高信頼性化が可能となる。
As described above, according to the method for charging a sealed lead-acid battery of the present invention, the influence of charge acceptance and the difference between cell chambers are reduced, and the amount of electricity charged in the first stage is stabilized. Therefore, it is possible to extend the life of the battery and increase its reliability.

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

【図1】本発明の実施例における電池の外観図FIG. 1 is an external view of a battery according to an embodiment of the present invention.

【図2】充電電圧と水素発生量との関係図[Fig. 2] Relationship between charging voltage and hydrogen generation amount

【図3】充電電圧と充電時間・充電電気量との関係図[Fig. 3] Relationship diagram between charging voltage and charging time / charge quantity

【図4】充放電サイクルテストにおける容量変化を示す
FIG. 4 is a diagram showing a capacity change in a charge / discharge cycle test.

【符号の説明】[Explanation of symbols]

1 鉛蓄電池 2 セル室 1 lead acid battery 2 cell room

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】正極板、負極板およびセパレータよりな
り、極板の格子には鉛−カルシウム−すず合金を用いた
密閉形鉛蓄電池の1段目の充電で、電池の充電電圧を検
出して電流値を変化させ、2段目以降の充電はタイマー
にて終了させる多段定電流充電方式において、1段目の
充電電流(i1)を0.4CA以下、2段目以降の充電
電流(in)をi1>in+1>in+2(n>1)とするとと
もにタイマーによる充電時間(Tn)をT1<Tn+1<T
n+2(n>1)とし、前記検出電圧を2.32V〜2.
37V/セルで検知することを特徴とした密閉形鉛蓄電
池の充電方法。
1. A battery comprising a positive electrode plate, a negative electrode plate and a separator, wherein the grid of the electrode plate uses lead-calcium-tin alloy to detect the charging voltage of the battery by first-stage charging. In the multi-stage constant current charging method in which the current value is changed and the charging in the second and subsequent stages is terminated by a timer, the charging current (i 1 ) in the first stage is 0.4 CA or less and the charging current in the second and subsequent stages (i n ) is i 1 > i n + 1 > i n + 2 (n> 1), and the charging time (T n ) by the timer is T 1 <T n + 1 <T
n + 2 (n> 1), and the detection voltage is 2.32V to 2.
A method for charging a sealed lead-acid battery, which is characterized by detecting at 37 V / cell.
JP7139088A 1995-06-06 1995-06-06 How to charge a sealed lead acid battery Pending JPH08329989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7139088A JPH08329989A (en) 1995-06-06 1995-06-06 How to charge a sealed lead acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7139088A JPH08329989A (en) 1995-06-06 1995-06-06 How to charge a sealed lead acid battery

Publications (1)

Publication Number Publication Date
JPH08329989A true JPH08329989A (en) 1996-12-13

Family

ID=15237214

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7139088A Pending JPH08329989A (en) 1995-06-06 1995-06-06 How to charge a sealed lead acid battery

Country Status (1)

Country Link
JP (1) JPH08329989A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE40223E1 (en) 1998-05-27 2008-04-08 Matsushita Electric Industrial Co., Ltd. Method for charging secondary battery
CN109038704A (en) * 2018-06-25 2018-12-18 中国人民解放军陆军炮兵防空兵学院 A kind of intelligent multi-control accumulator charging control method based on capacity

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
USRE40223E1 (en) 1998-05-27 2008-04-08 Matsushita Electric Industrial Co., Ltd. Method for charging secondary battery
CN109038704A (en) * 2018-06-25 2018-12-18 中国人民解放军陆军炮兵防空兵学院 A kind of intelligent multi-control accumulator charging control method based on capacity
CN109038704B (en) * 2018-06-25 2021-01-15 中国人民解放军陆军炮兵防空兵学院 Intelligent multi-mode storage battery charging control method based on capacity

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