JPH041465B2 - - Google Patents

Info

Publication number
JPH041465B2
JPH041465B2 JP58146001A JP14600183A JPH041465B2 JP H041465 B2 JPH041465 B2 JP H041465B2 JP 58146001 A JP58146001 A JP 58146001A JP 14600183 A JP14600183 A JP 14600183A JP H041465 B2 JPH041465 B2 JP H041465B2
Authority
JP
Japan
Prior art keywords
battery
electrolyte
piston
liquid
gas
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 - Lifetime
Application number
JP58146001A
Other languages
Japanese (ja)
Other versions
JPS6037651A (en
Inventor
Toshiaki Hayashi
Katsuto Takahashi
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.)
Japan Storage Battery Co Ltd
Original Assignee
Japan Storage Battery 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 Japan Storage Battery Co Ltd filed Critical Japan Storage Battery Co Ltd
Priority to JP58146001A priority Critical patent/JPS6037651A/en
Publication of JPS6037651A publication Critical patent/JPS6037651A/en
Publication of JPH041465B2 publication Critical patent/JPH041465B2/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
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/70Arrangements for stirring or circulating the electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/70Arrangements for stirring or circulating the electrolyte
    • H01M50/73Electrolyte stirring by the action of gas on or in the electrolyte
    • 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

Description

【発明の詳細な説明】 本発明は鉛蓄電池の改良に関するもので、その
目的とするところは、充分なガス発生が起らない
充電方式で使用される鉛蓄電池において生じる電
池内部の電解液濃度の不均一化を除くことにより
鉛蓄電池の長寿命化を充電効率の向上とを計るこ
とにある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to improvement of lead-acid batteries, and its purpose is to improve the electrolyte concentration inside the battery, which occurs in lead-acid batteries used in a charging method that does not generate sufficient gas. The aim is to extend the life of lead-acid batteries and improve charging efficiency by eliminating unevenness.

一般にサイクルサービス用鉛蓄電池では、放電
電気量が日々異なり、充電すべき電気量が定まら
ないため、電圧制御法により充電される。
In general, lead-acid batteries for cycle service are charged using a voltage control method because the amount of electricity discharged varies from day to day and the amount of electricity to be charged is not fixed.

この場合、設定電圧が高すぎると、過充電電気
量が増え、エネルギー損失が大きくなると同時に
電池の劣化も加速される。一方、設定電圧が低す
ぎる場合には、電池が十分にガスを発生しないの
で電解液が撹拌されず、電池上部の電解液濃度が
低くなり、逆に下部では高濃度となる。このよう
な電解液濃度の不均一化、いわゆる電解液の成層
化は、充電効率も低下させ、しかも放電容量の低
下を招く。さらにこのような状態で充放電が繰り
返されると、電解液の成層化はますます増大し、
電池の早期容量低下を引き起こすことになる。
In this case, if the set voltage is too high, the amount of overcharged electricity will increase, energy loss will increase, and at the same time, battery deterioration will be accelerated. On the other hand, if the set voltage is too low, the battery will not generate enough gas and the electrolyte will not be stirred, resulting in a low electrolyte concentration at the top of the battery and a high concentration at the bottom. Such non-uniform electrolytic solution concentration, so-called electrolytic solution stratification, also reduces charging efficiency and leads to a reduction in discharge capacity. Furthermore, if charging and discharging are repeated under such conditions, the stratification of the electrolyte will increase,
This will cause early capacity reduction of the battery.

また電池の充電量は、使用される還境温度によ
つても著しく影響され、20〜40℃の温度範囲で適
正な充電が行なえる電圧でも、寒冷地や冬期の使
用ではガス発生量が減少するため、電解液の成層
化が起こり、電池の容量低下を招く。
In addition, the amount of battery charge is significantly affected by the ambient temperature at which it is used, and even if the voltage allows proper charging in the temperature range of 20 to 40 degrees Celsius, the amount of gas generated decreases when used in cold regions or in winter. As a result, stratification of the electrolyte occurs, leading to a decrease in battery capacity.

電池を著しく過充電することなく、電解液の成
層化を防ぐ方法としては、外部から空気を送りこ
んで電解液を撹拌するという方法が知られてい
る。しかし、この方法では、(1)電池への送風装置
を必要とする。(2)全ての電池を送風管で接続する
必要がある。(3)送風装置を作動させるためのエネ
ルギーを必要とする等の欠点がある。
A known method for preventing stratification of the electrolyte without significantly overcharging the battery is to stir the electrolyte by blowing air in from the outside. However, this method requires (1) an air blower to the battery; (2) All batteries must be connected with air pipes. (3) There are drawbacks such as the need for energy to operate the blower device.

本発明は電池内で発生する少量のガスによる電
池の内圧上昇を利用するもので、この少量のガス
により効率的に電解液を撹拌する装置を鉛蓄電池
に取り付けることを特徴とするものである。
The present invention utilizes the increase in internal pressure of the battery due to a small amount of gas generated within the battery, and is characterized by attaching to the lead-acid battery a device that efficiently stirs the electrolyte using this small amount of gas.

以下、図面を用いて本発明を具体的に説明す
る。第1図は本発明による電解液撹拌装置を備え
た鉛蓄電池の一実施例の構造を示すもので、1は
電槽、2は極板群、3は電解液である。4は液撹
拌装置を構成する筒状の容器で、4つの開口、す
なわち液流入口5、液流出口6、ガス流入口7、
ガス流出口8を有し、またガス流入口7の上部に
凸部9が設けられている。液流入口5の位置は電
解液中望ましくは電池底部近辺にくるように配置
する。液流出口6の位置は電解液内でその上部に
あるいは電解液面上であればその近辺にくるよう
に配置する。ガス流入口7の位置は電解液面上で
液流出口6の上部に配置する。ガス流出口8は筒
状の容器4の上部でガス流入口7の上部に配置す
る。
Hereinafter, the present invention will be specifically explained using the drawings. FIG. 1 shows the structure of an embodiment of a lead-acid battery equipped with an electrolyte stirring device according to the present invention, in which 1 is a battery case, 2 is a group of electrode plates, and 3 is an electrolyte. 4 is a cylindrical container constituting a liquid stirring device, which has four openings, namely, a liquid inlet 5, a liquid outlet 6, a gas inlet 7,
It has a gas outlet 8 , and a convex portion 9 is provided above the gas inlet 7 . The liquid inlet 5 is disposed in the electrolyte, preferably near the bottom of the battery. The liquid outlet 6 is located above the electrolytic solution, or near it if it is above the electrolytic solution surface. The gas inlet 7 is located above the liquid outlet 6 on the electrolyte level. The gas outlet 8 is arranged at the upper part of the cylindrical container 4 and above the gas inlet 7.

本実施例では、ガス流出口8は電槽1の外部に
配置されているが、電池内部にあつてもかまわな
い。ただし、そのガス流出口8が電池外部の大気
に対して開口されていてその上部にピストン11
の厚み分の空間があればよい。この筒状容器4内
には軸棒10で連結された上部のピストン11お
よび下部のピストン12の2つのピストンが取り
付けられている。軸棒10の上部のピストン11
はガス流入口7の上部からガス流出口8の上部ま
で動くことができる。軸棒10の下部のピストン
12は液流入弁13を有しており、ピストン12
の下部の電解液がピストン12の上部に流入する
ときにだけ開くようになつている。この下部のビ
ストン12は液流入口5から液流出口6までの筒
状容器4内であつてかつ上部のピストン11の動
くことのできる上下方向の距離を動くことのでき
るように、軸棒10の長さはガス流出口8の上部
から液流出口6の下部までの距離よりも長く、凸
部9から液流入口5までの距離よりも短かくして
ある。これらのピストンは容器4の内壁との間に
もれがないように構成されており、かつスムーズ
に動くことができる。
In this embodiment, the gas outlet 8 is placed outside the battery case 1, but it may be placed inside the battery. However, the gas outlet 8 is open to the atmosphere outside the battery, and a piston 11 is placed above it.
It is sufficient if there is a space equal to the thickness of . Two pistons, an upper piston 11 and a lower piston 12, connected by an axial rod 10 are installed in this cylindrical container 4. Piston 11 at the top of the shaft rod 10
can move from the top of the gas inlet 7 to the top of the gas outlet 8. The piston 12 at the bottom of the shaft 10 has a liquid inflow valve 13, and the piston 12
It opens only when the electrolyte in the lower part of the piston 12 flows into the upper part of the piston 12. This lower piston 12 is located within the cylindrical container 4 from the liquid inlet 5 to the liquid outlet 6, and is attached to the shaft rod 10 so that it can move within the vertical distance that the upper piston 11 can move. The length is longer than the distance from the upper part of the gas outlet 8 to the lower part of the liquid outlet 6 and shorter than the distance from the convex part 9 to the liquid inlet 5. These pistons are constructed so that there is no leakage between them and the inner wall of the container 4, and can move smoothly.

次にかかる本発明実施例の作動原理を説明す
る。今、電池内圧が大気圧で筒状の容器4内のピ
ストン11は凸部9の上部に接している状態であ
るとする。このとき筒状容器4内の電解液面は筒
状容器4外の電解液面と同じ高さにある。充電
中、電池内圧は発生ガスのために徐々に高くな
り、容器4に設けられたガス流入口7より容器4
内のピストン11の下部には電池内圧がかかる。
ピストン11の上部は容器4の上部に設けられた
ガス流出口8が大気に対して開口しているので、
大気圧がかかつていることになる。電池内圧の上
昇に伴いピストン11は容器4内を上昇する。こ
のとき軸棒10で連結された軸棒10の下部のピ
ストン12はピストン11と連動して上昇する。
このとき容器4内の電解液はピストン12により
持ち上げられ液流出口6より電解液上部に流出す
る。電池内圧がさらに上昇しピストン11がガス
流出口8の上部まで上昇すると、ガス流出口8よ
りガスが大気中に流出し、電逃内圧は低下する。
電池内圧が低下するとピストン11は自重により
容器4内を低下し凸部9に接して止まる。このと
き下部のピストン12は液流入弁13を開き、ピ
ストン12の下部の電解液をピストン12の上部
に流入させながら容器4内を低下し、ピストン1
1が凸部9に接すると同時に停止する。このよう
にして電池下部の電解液が電池上部に運ばれる。
さらに充電により電池内圧が上昇し、上述した一
連の動作が繰り返される。この動作の繰返しによ
り、電池下部の高濃度電解液が効率よく電池上部
に運ばれ、電解液の成層化が解消される。
Next, the operating principle of this embodiment of the present invention will be explained. It is now assumed that the internal pressure of the battery is atmospheric pressure and the piston 11 inside the cylindrical container 4 is in contact with the upper part of the convex portion 9. At this time, the electrolytic solution level inside the cylindrical container 4 is at the same height as the electrolytic solution level outside the cylindrical container 4. During charging, the internal pressure of the battery gradually increases due to the generated gas, and the gas inlet 7 provided in the container 4
Battery internal pressure is applied to the lower part of the piston 11 inside.
Since the gas outlet 8 provided at the top of the container 4 is open to the atmosphere at the top of the piston 11,
This means that atmospheric pressure is applied. The piston 11 moves up inside the container 4 as the internal pressure of the battery increases. At this time, the piston 12 at the bottom of the shaft 10 connected by the shaft 10 moves up in conjunction with the piston 11.
At this time, the electrolyte in the container 4 is lifted by the piston 12 and flows out from the liquid outlet 6 to the upper part of the electrolyte. When the battery internal pressure further increases and the piston 11 rises to the upper part of the gas outlet 8, gas flows out from the gas outlet 8 into the atmosphere, and the electric escape internal pressure decreases.
When the internal pressure of the battery decreases, the piston 11 lowers inside the container 4 due to its own weight and comes into contact with the protrusion 9 and stops. At this time, the lower piston 12 opens the liquid inflow valve 13 and lowers the inside of the container 4 while allowing the electrolyte at the lower part of the piston 12 to flow into the upper part of the piston 12.
1 comes into contact with the convex portion 9 and stops at the same time. In this way, the electrolyte in the lower part of the battery is transported to the upper part of the battery.
Furthermore, the internal pressure of the battery increases due to charging, and the series of operations described above are repeated. By repeating this operation, the highly concentrated electrolyte at the bottom of the battery is efficiently transported to the top of the battery, and stratification of the electrolyte is eliminated.

次に本発明の一実施例について詳述する。容量
330Ah(8hR)高さ約50cmの電気車用鉛蓄電池に、
第1図に示した電解液撹拌装置を取り付け(電池
記号A)、環境温度を5℃に設定して、8hR電流
で完全放電し、2.40Vの定電圧で5時間充電する
という充放電サイクルを行なつた。なお、比較の
ため、液撹拌装置を取り付けてない従来の電池
(記号B)、およびプラスチツク製のパイプを電池
内へ挿入し充電中外部からコンプレツサーで空気
を400cc/分の速度で送り込んで液撹拌した電池
(記号C)についても同様の充放電サイクルを行
なつた。これらの電池のサイクル中の充電量はい
ずれも前回放電量の103〜105%の範囲内であつ
た。これらの電池の放電前(充電後)の電池上部
の電解液比重および放電時間の充放電サイクル中
の推移を第2図に示す。
Next, one embodiment of the present invention will be described in detail. capacity
330Ah (8hR) approximately 50cm high lead-acid battery for electric cars,
Attach the electrolyte stirring device shown in Figure 1 (Battery symbol A), set the environmental temperature to 5°C, perform a charge/discharge cycle of fully discharging at 8hR current, and charging at a constant voltage of 2.40V for 5 hours. I did it. For comparison, a conventional battery without a liquid stirring device (symbol B) was used, and a plastic pipe was inserted into the battery and air was pumped in from the outside at a rate of 400 cc/min using a compressor to stir the liquid during charging. A similar charge/discharge cycle was performed on the battery (symbol C). The charge amount of these batteries during the cycle was within the range of 103 to 105% of the previous discharge amount. FIG. 2 shows the changes in the specific gravity of the electrolyte at the top of the battery before discharge (after charging) and the discharge time of these batteries during the charge/discharge cycle.

液撹拌装置を取り付けていない従来形の電池B
では次第に電解液が成層化し、電池上部の電解液
比重は25サイクル目で1.11にまで低下した。また
放電時間も電解液の成層化が増大するに従い短か
くなり、25サイクル目では初期容量の約1/3にな
つた。これに対し本発明による液撹拌装置を取り
つけた鉛蓄電池Aでは、充放電を50回繰返して
も、電池上部の電解液比重の低下は約0.01であ
り、容量低下も2〜3%であつた。
Conventional battery B without a liquid stirring device
The electrolyte gradually became stratified, and the specific gravity of the electrolyte at the top of the battery decreased to 1.11 at the 25th cycle. The discharge time also became shorter as the stratification of the electrolyte increased, and at the 25th cycle, the capacity was about 1/3 of the initial capacity. In contrast, in lead-acid battery A equipped with the liquid stirring device according to the present invention, even after repeated charging and discharging 50 times, the electrolyte specific gravity at the top of the battery decreased by about 0.01, and the capacity decreased by 2 to 3%. .

この値は、外部から空気を送つて液撹拌した場
合とほとんど同じであつた。
This value was almost the same as when the liquid was stirred by supplying air from outside.

以上詳述したように本発明によれば、簡単な液
撹拌装置を取り付けるだけで、鉛蓄電池から発生
する少量のガスにより、効率的に電解液が撹拌さ
れ、電解液濃度の電池内での不均一化いわゆる成
層化による容量低下を防ぐことができる。また本
発明では外部の送風装置やそれを作動させるエネ
ルギーを必要とせず、各電池へ送風するための配
管も不要となり、その工業的価値は大である。
As detailed above, according to the present invention, by simply installing a simple liquid stirring device, the electrolyte can be efficiently stirred by a small amount of gas generated from the lead-acid battery, thereby reducing the concentration of the electrolyte in the battery. It is possible to prevent a decrease in capacity due to uniformity, so-called stratification. Furthermore, the present invention does not require an external blower device or energy to operate it, and also eliminates the need for piping for blowing air to each battery, which has great industrial value.

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

第1図は本発明による電解液撹拌装置を備えた
鉛蓄電池の一実施例の構造を示す概略断面図、第
2図は本発明品と従来品の電解比重および放電時
間の充放電サイクル中の推移を示す特性図であ
る。 1……電槽、2……極板群、3……電解液、4
……筒状容器、5……液流入口、6……液流出
口、7……ガス流入口、8……ガス流出口、9…
…凸部、10……軸棒、11……ピストン、12
……ピストン、13……液流入弁。
Fig. 1 is a schematic cross-sectional view showing the structure of an embodiment of a lead-acid battery equipped with an electrolyte stirring device according to the present invention, and Fig. 2 shows the electrolytic specific gravity and discharge time of the inventive product and the conventional product during charge/discharge cycles. It is a characteristic diagram showing the transition. 1... Battery container, 2... Plate group, 3... Electrolyte, 4
... Cylindrical container, 5... Liquid inlet, 6... Liquid outlet, 7... Gas inlet, 8... Gas outlet, 9...
...Protrusion, 10... Axis rod, 11... Piston, 12
...Piston, 13...Liquid inflow valve.

Claims (1)

【特許請求の範囲】[Claims] 1 電池底部付近に液流入口、電解液面付近に液
流出口、電解液面の上部の電池内にガス流入口、
最上部に大気に対して開口したガス流出口を有す
る筒状容器内に上下に2つのピストンを連結した
軸棒を有し、上部のピストンはガス流入口の上部
からガス流出口の上部まで動くことができ、下部
のピストンは下部ピストンの下から上へのみ電解
液を通すことのできる弁を有し、かつ液流入口の
上部から液流出口の下部まで動くことのできる構
成とし、筒状容器を極板群と電槽内壁との間に配
置したことを特徴とする電解液撹拌装置を備えた
鉛蓄電池。
1. Liquid inlet near the bottom of the battery, liquid outlet near the electrolyte surface, gas inlet in the battery above the electrolyte surface,
It has a cylindrical container with a gas outlet opening to the atmosphere at the top, and a shaft rod connecting two pistons vertically, with the upper piston moving from the top of the gas inlet to the top of the gas outlet. The lower piston has a valve that allows the electrolyte to pass only from the bottom to the top of the lower piston, and is movable from the upper part of the liquid inlet to the lower part of the liquid outlet, and has a cylindrical shape. A lead-acid battery equipped with an electrolyte stirring device characterized in that a container is arranged between a group of electrode plates and an inner wall of a battery case.
JP58146001A 1983-08-09 1983-08-09 Lead storage battery provided with electrolyte stirring device Granted JPS6037651A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58146001A JPS6037651A (en) 1983-08-09 1983-08-09 Lead storage battery provided with electrolyte stirring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58146001A JPS6037651A (en) 1983-08-09 1983-08-09 Lead storage battery provided with electrolyte stirring device

Publications (2)

Publication Number Publication Date
JPS6037651A JPS6037651A (en) 1985-02-27
JPH041465B2 true JPH041465B2 (en) 1992-01-13

Family

ID=15397853

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58146001A Granted JPS6037651A (en) 1983-08-09 1983-08-09 Lead storage battery provided with electrolyte stirring device

Country Status (1)

Country Link
JP (1) JPS6037651A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0230059A (en) * 1988-07-20 1990-01-31 Japan Storage Battery Co Ltd Battery equipped with electrolyte agitator
JPWO2021060326A1 (en) 2019-09-27 2021-04-01

Also Published As

Publication number Publication date
JPS6037651A (en) 1985-02-27

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