JPH09161766A - Electrolyte circulating device for lead-acid battery - Google Patents

Electrolyte circulating device for lead-acid battery

Info

Publication number
JPH09161766A
JPH09161766A JP7316977A JP31697795A JPH09161766A JP H09161766 A JPH09161766 A JP H09161766A JP 7316977 A JP7316977 A JP 7316977A JP 31697795 A JP31697795 A JP 31697795A JP H09161766 A JPH09161766 A JP H09161766A
Authority
JP
Japan
Prior art keywords
electrolytic solution
electrolyte
gas
tank
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
JP7316977A
Other languages
Japanese (ja)
Inventor
Akira Namiki
公 並木
Noriaki Itou
令朗 伊藤
Mitsugi Shinyashiki
貢 新屋敷
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.)
Honda Motor Co Ltd
Original Assignee
Honda Motor 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 Honda Motor Co Ltd filed Critical Honda Motor Co Ltd
Priority to JP7316977A priority Critical patent/JPH09161766A/en
Publication of JPH09161766A publication Critical patent/JPH09161766A/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

  • Filling, Topping-Up Batteries (AREA)
  • Secondary Cells (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the reduction of the capability of a battery by providing a discharging means for the gas generated from an electrolyte above the electrolyte in an electrolyte tank. SOLUTION: The electrolyte E in an electrolyte tank 3 is fed to a battery 7 by the first conduit 4 and an injection pump 5. The electrolyte E in the battery 7 is again returned to the electrolyte tank 3 by the second pipe 8 and a discharge pump 9. The hydrogen gas generated in the battery 7 is sent together, and it is collected at the upper section of the air layer A of the electrolyte tank 3. The gas is discharged by a gas discharging means 16 above the tank 3. The gas generated from the electrolyte E and accumulated in the electrolyte tank 3 is also discharged by the discharging means 16. The quantity of the gas again mixed in the electrolyte E is reduced, gas rarely exists between a positive electrode and a negative electrode in the battery 7, and the chemical reaction between the electrodes is not impaired. The reduction of the capability of the battery 7 can be suppressed.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は鉛蓄電池用電解液循
環装置に関する。
TECHNICAL FIELD The present invention relates to an electrolytic solution circulating device for a lead storage battery.

【0002】[0002]

【従来の技術】図3は従来の鉛蓄電池の断面図(要部)
であり、まず、構成について説明する。鉛蓄電池100
は、陽極板101…(…は複数個を示す。以下同様)
と、これらの陽極板101…に対向する陰極板102…
と、陽極板101…と陰極板102…とを隔てるセパレ
ータ103…と、これらの陽極板101…、陰極板10
2…及びセパレータ103…を収納する電そう104
と、この電そう104に満たした電解液105と、電そ
う104上部に設けた液口栓106と、図示せぬ陽極・
陰極端子とからなる。なお、107は通気孔である。
2. Description of the Related Art FIG. 3 is a sectional view of a conventional lead-acid battery (main part).
First, the configuration will be described. Lead acid battery 100
Is an anode plate 101 ... (... indicates a plurality, the same applies hereinafter)
, And the cathode plate 102 facing these anode plates 101.
, A separator 103 separating the anode plate 101 and the cathode plate 102, and the anode plate 101 and the cathode plate 10.
2 ... and separator 103 ...
An electrolytic solution 105 filled in the electrolytic cell 104, a liquid port stopper 106 provided on the upper part of the electrolytic cell 104, and an anode (not shown).
It consists of a cathode terminal. In addition, 107 is a ventilation hole.

【0003】陽極板101は鉛・アンチモン合金等でで
きた格子体の目に活物質として二酸化鉛を充填したもの
である。陰極板102は鉛・アンチモン合金等でできた
格子体の目に活物質として海綿状鉛を充填したものであ
る。セパレータ103は多孔質体であり、電解液105
である希硫酸を自由に通すことができる。
The anode plate 101 is a grid body made of lead-antimony alloy or the like and filled with lead dioxide as an active material in the eyes. The cathode plate 102 is a lattice body made of lead / antimony alloy or the like, in which spongy lead is filled as an active material in the eyes. The separator 103 is a porous body, and the electrolytic solution 105
It is possible to freely pass dilute sulfuric acid.

【0004】次に作用を説明する。充電済みの鉛蓄電池
100の陽極・陰極端子に負荷を接続すると、鉛蓄電池
100は放電状態となる。この時、陽極板101の二酸
化鉛と陰極板102の海綿状鉛は、電解液105である
希硫酸と化学反応して、陽極・陰極では硫酸鉛が生成
し、同時に水ができる。この反応を化学式に表わすと、
下記化1のようになる。
Next, the operation will be described. When a load is connected to the anode / cathode terminals of the charged lead storage battery 100, the lead storage battery 100 is in a discharged state. At this time, the lead dioxide of the anode plate 101 and the spongy lead of the cathode plate 102 chemically react with dilute sulfuric acid which is the electrolytic solution 105 to produce lead sulfate at the anode and cathode, and at the same time water is formed. When this reaction is represented by the chemical formula,
It becomes like the following chemical formula 1.

【0005】[0005]

【化1】 Embedded image

【0006】放電を続けると、電解液105中の水が増
え、電解液105は次第に薄められ、比重は小さくな
る。
When the discharge is continued, the amount of water in the electrolytic solution 105 increases, the electrolytic solution 105 is gradually diluted, and the specific gravity becomes small.

【0007】放電後の鉛蓄電池100を充電すると、放
電によって硫酸鉛に変った陽極・陰極板101,102
は硫酸を分離し、陽極板101では二酸化鉛に、陰極板
102では海綿状鉛に戻る。硫酸が生成されるため、比
重はもとに戻る。また、この時に電解液105中の水は
電気分解され、陽極から酸素ガス、陰極から水素ガスが
発生し、電解液105は次第に減少して電解液液面10
8は下がる。発生したガスは、液口栓106の通気孔1
07から外部に排出される。この反応を化学式に表わす
と、下記化2のようになる。
When the lead-acid battery 100 after discharging is charged, the anode / cathode plates 101 and 102 are converted into lead sulfate by discharging.
Separates sulfuric acid and returns to lead dioxide on the anode plate 101 and to spongy lead on the cathode plate 102. Sulfuric acid is generated, so the specific gravity returns to the original value. At this time, the water in the electrolytic solution 105 is electrolyzed, oxygen gas is generated from the anode, and hydrogen gas is generated from the cathode.
8 goes down. The generated gas is the vent hole 1 of the liquid mouth plug 106.
It is discharged from 07 to the outside. This reaction is represented by the chemical formula below.

【0008】[0008]

【化2】 Embedded image

【0009】従来、上記鉛蓄電池と電解液注入用ポンプ
と電解液排出用ポンプと電解液タンクとを連通管で接続
し、電解液を循環させる鉛蓄電池用電解液循環装置に
は、例えば、特公昭51−28328号公報「電解液循
環型鉛蓄電池」がある。この公報は、鉛蓄電池の活物質
の脱落を防止する為に、電解液室に液透過性で弾力性の
ある隔離材を圧縮状態で挿入し、充電時には吸引循環、
放電時には圧入循環とすることにより、隔離材にガス溜
まりを発生させないようにしたものである。
[0009] Conventionally, a lead storage battery electrolyte circulating apparatus for circulating the electrolyte by connecting the lead storage battery, the electrolyte injection pump, the electrolyte discharge pump, and the electrolyte tank by a communication pipe is, for example, There is Japanese Laid-Open Patent Publication No. 51-28328 “Electrolyte circulating type lead storage battery”. In this publication, in order to prevent the active material of the lead-acid battery from falling off, a liquid-permeable and elastic separator is inserted into the electrolyte chamber in a compressed state, and suction circulation is performed during charging.
The gas is not accumulated in the separator by the press-fit circulation during discharge.

【0010】[0010]

【発明が解決しようとする課題】しかしながら、従来の
装置は電解液タンクに溜まる水素ガス及び酸素ガスの排
出が充分に行える構成になっていないので、これらの水
素ガス及び酸素ガスが再び電解液に混在して鉛蓄電池に
戻り、これが気泡となって電解液と陽・陰極板との間に
介在し、電解液と活物質との化学反応を阻害して、鉛蓄
電池の能力を低下させるという不都合がある。本発明の
目的は、電解液から発生したガスが再び電解液に混在す
ることを防止する鉛蓄電池用電解液循環装置を提供する
ことにある。
However, since the conventional apparatus is not configured to sufficiently discharge the hydrogen gas and the oxygen gas accumulated in the electrolytic solution tank, these hydrogen gas and the oxygen gas are reused as the electrolytic solution. It returns to the lead-acid battery mixedly, and it becomes a bubble and intervenes between the electrolytic solution and the positive / cathode plate, which hinders the chemical reaction between the electrolytic solution and the active material, and reduces the capacity of the lead-acid battery. There is. An object of the present invention is to provide an electrolytic solution circulating device for a lead storage battery, which prevents gas generated from the electrolytic solution from being mixed with the electrolytic solution again.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するため
に本発明の請求項1は、電解液タンク内の電解液上方に
電解液から発生したガスを排出するための排出手段を設
けた。電解液から発生したガスを排出手段により外部に
排出する。電解液中に発生ガスが戻らないので、鉛蓄電
池の能力低下を抑えることができる。
In order to achieve the above object, the first aspect of the present invention provides a discharge means for discharging a gas generated from the electrolytic solution above the electrolytic solution in the electrolytic solution tank. The gas generated from the electrolytic solution is discharged to the outside by the discharging means. Since the generated gas does not return to the electrolytic solution, it is possible to suppress deterioration in the capacity of the lead storage battery.

【0012】[0012]

【発明の実施の形態】本発明の実施の形態を添付図に基
づいて以下に説明する。なお、図面は符号の向きに見る
ものとする。図1は本発明に係る鉛蓄電池用電解液循環
装置の斜視図であり、鉛蓄電池用電解液循環装置1(以
下「循環装置1」と記す。)は、電解液タンク3内の電
解液E(図2参照)を、第1導管4及びこの第1導管4
に介設した注入ポンプ5にて、注入ポンプ5下流に設け
た電解液流量を測定するための流量計6を介して、鉛蓄
電池7に供給し、鉛蓄電池7内の電解液Eを第2導管8
及びこの第2導管8に介設した排出ポンプ9にて、排出
ポンプ9下流に設けた電解液流量を測定するための流量
計12を介して、電解液タンク3に戻すという装置であ
る。14は透明なプレートを合せて構成した電解液飛散
防止用のカバー、13は鉛蓄電池7をメンテナンスする
ための扉、2は循環装置1のベース、15は鉛蓄電池7
載置用のトレーである。なお、カバー14は、循環装置
1全体を覆うものでもよい。
Embodiments of the present invention will be described below with reference to the accompanying drawings. The drawings should be viewed in the direction of reference numerals. FIG. 1 is a perspective view of an electrolytic solution circulating device for a lead storage battery according to the present invention, and an electrolytic solution circulating device 1 for a lead storage battery (hereinafter referred to as “circulating device 1”) is an electrolytic solution E in an electrolytic solution tank 3. (See FIG. 2), the first conduit 4 and the first conduit 4
The injection pump 5 installed in the lead storage battery 5 supplies the lead storage battery 7 through the flow meter 6 for measuring the flow rate of the electrolyte solution provided downstream of the injection pump 5 to supply the electrolyte solution E in the lead storage battery 7 to the second position. Conduit 8
Also, the discharge pump 9 provided in the second conduit 8 returns it to the electrolytic solution tank 3 via a flow meter 12 provided downstream of the discharge pump 9 for measuring the flow rate of the electrolytic solution. Reference numeral 14 is a cover for preventing dispersion of the electrolytic solution, which is formed by combining transparent plates, 13 is a door for maintaining the lead storage battery 7, 2 is a base of the circulation device 1, and 15 is a lead storage battery 7
It is a tray for placing. The cover 14 may cover the entire circulation device 1.

【0013】電解液タンク3は、電解液Eから発生した
ガスの排出手段16として吸気管17(図2参照)と、
排気管18と、この排気管18に設けたファン19とを
備える。排出ポンプ9の排出能力(出力)は、注入ポン
プ5の注入能力(出力)よりも大きい。
The electrolyte tank 3 has an intake pipe 17 (see FIG. 2) as a means 16 for discharging the gas generated from the electrolyte E.
The exhaust pipe 18 and a fan 19 provided in the exhaust pipe 18 are provided. The discharge capacity (output) of the discharge pump 9 is larger than the injection capacity (output) of the injection pump 5.

【0014】図2は本発明に係る循環装置の模式図(断
面図)であり、鉛蓄電池7は、上部に第2導管8、下部
に第1導管4が各セルC毎に接続され、第2導管8との
接続部近傍に各セルC毎に通気孔22…(…は複数個を
示す。以下同様。)を備える。この通気孔22によって
各セルC内が極端に負圧となるのを防ぐことができる。
排出ポンプ9に接続する第2導管8の吸入口8a…を、
各セルCとも鉛蓄電池7の電解液液面Sの上限レベルU
と下限レベルLとの中間位置に設置する。
FIG. 2 is a schematic view (cross-sectional view) of the circulation device according to the present invention. In the lead storage battery 7, the second conduit 8 is connected to the upper part and the first conduit 4 is connected to the lower part for each cell C. 2 Vents 22 ... (... indicates a plurality, the same applies hereinafter) for each cell C in the vicinity of the connection portion with the conduit 8. The vent holes 22 can prevent the inside of each cell C from becoming extremely negative pressure.
The suction port 8a of the second conduit 8 connected to the discharge pump 9 is
For each cell C, the upper limit level U of the electrolyte solution surface S of the lead storage battery 7
And the lower limit level L.

【0015】電解液タンク3は、内部の電解液E上方に
空気層Aを有し、この空気層Aに臨んで外気を取り入れ
る吸気管17と、内部のガスを強制的に排出するための
排気管18及びこの排気管18に設置されたファン19
とを備える。電解液タンク3は、電解液Eから発生する
ガスを上部に集めるために上部を断面積が小となるボト
ル形状とした。
The electrolytic solution tank 3 has an air layer A above the internal electrolytic solution E, an intake pipe 17 which faces the air layer A to take in outside air, and an exhaust gas for forcibly discharging the gas inside. The pipe 18 and the fan 19 installed in the exhaust pipe 18
And The electrolytic solution tank 3 has a bottle shape with a small cross-sectional area in order to collect the gas generated from the electrolytic solution E in the upper part.

【0016】電解液タンク3に接続した第1導管4の吸
入口4aは、電解液タンク3の底近傍に設置し、第2導
管8の吐出口8bは、空気層A内に設置する。これらの
吸入口4a及び吐出口8bの配置により、電解液タンク
3に戻される電解液Eに含まれるガスは、電解液Eが吐
出口8bから吐出されるときに空気層Aに排出しやす
く、また、電解液タンク3内の電解液E内にガスが混じ
っても、吸入口4aから吸入されにくい。
The inlet 4a of the first conduit 4 connected to the electrolytic solution tank 3 is installed near the bottom of the electrolytic solution tank 3, and the outlet 8b of the second conduit 8 is installed in the air layer A. Due to the arrangement of the suction port 4a and the discharge port 8b, the gas contained in the electrolytic solution E returned to the electrolytic solution tank 3 is easily discharged to the air layer A when the electrolytic solution E is discharged from the discharge port 8b, Further, even if gas is mixed in the electrolytic solution E in the electrolytic solution tank 3, it is difficult to be sucked through the suction port 4a.

【0017】循環装置1は、流量計6,12からの流量
信号F1,F2を受け、これらの流量信号F1,F2に応じ
て給水・排水ポンプ5,9に駆動信号D1,D2を送り、
これら給水・排水ポンプ5,9の出力を調整する電解液
流量制御部24を備える。
The circulation device 1 receives flow rate signals F1 and F2 from the flow meters 6 and 12, and sends drive signals D1 and D2 to the water supply / drainage pumps 5 and 9 in accordance with these flow rate signals F1 and F2.
An electrolytic solution flow rate control unit 24 for adjusting the outputs of the water supply / drainage pumps 5 and 9 is provided.

【0018】以上に述べた循環装置の作用を次に説明す
る。電解液タンク3に貯めた電解液Eは、注入ポンプ5
によって第1導管4の吸入口4aから吸入され、流量計
6を通って、第1導管4の各セルC毎の吐出口4bから
鉛蓄電池7内に供給され、セルC内の極板間のセパレー
タ(図3の符号103に相当)内を上昇し、排出ポンプ
9によって極板上部の電解液Eの上限レベルU、下限レ
ベルLの間に設置した第2導管8の吸入口8aから吸入
され、流量計12を通って、電解液タンク3内の吐出口
8bから吐出される。
The operation of the circulation device described above will be described below. The electrolytic solution E stored in the electrolytic solution tank 3 is supplied to the injection pump 5
Is sucked from the suction port 4a of the first conduit 4, passes through the flow meter 6, and is supplied into the lead storage battery 7 from the discharge port 4b of each cell C of the first conduit 4 between the electrode plates in the cell C. The separator (corresponding to reference numeral 103 in FIG. 3) rises and is sucked by the discharge pump 9 from the suction port 8a of the second conduit 8 installed between the upper limit level U and the lower limit level L of the electrolytic solution E above the electrode plate. After passing through the flow meter 12, the liquid is discharged from the discharge port 8b in the electrolytic solution tank 3.

【0019】排出ポンプ9は、注入ポンプ5より出力を
大きく設定しているが、電解液Eを循環中は注入・排出
ポンプ5,9の下流に設けた流量計6,12で電解液流
量を計測し、この結果から、例えば排出ポンプ9下流の
流量計12の流量が注入ポンプ5下流の流量計6より少
ないか又は等しい時には、各ポンプ5,9の出力を調整
し、流量計12の流量が多くなるようにする。このよう
にして、鉛蓄電池7内の各セルCの電解液液面Sを電解
液Eの上限レベルUと下限レベルLの間に保つことがで
きる。
Although the output of the discharge pump 9 is set higher than that of the injection pump 5, the flow rate of the electrolytic solution is controlled by the flowmeters 6 and 12 provided downstream of the injection / discharge pumps 5 and 9 during circulation of the electrolytic solution E. When the flow rate of the flow meter 12 downstream of the discharge pump 9 is less than or equal to that of the flow meter 6 downstream of the injection pump 5, the outputs of the pumps 5 and 9 are adjusted to measure the flow rate of the flow meter 12 based on the measurement results. To increase. In this way, the electrolytic solution surface S of each cell C in the lead storage battery 7 can be maintained between the upper limit level U and the lower limit level L of the electrolytic solution E.

【0020】従って、電解液面Sは下限レベルLより下
がらず、電解液Eと陽極、陰極との接触面積が小さくな
るということはなく、鉛蓄電池7の能力が落ちることは
ない。また、電解液液面Sは上限レベルUより上がら
ず、電解液Eが鉛蓄電池7上部から洩れたり、電解液E
から発生するガスによってセル内の圧力が異常に上昇す
ることはない。
Therefore, the electrolytic solution surface S does not drop below the lower limit level L, the contact area between the electrolytic solution E and the anode or cathode does not decrease, and the capacity of the lead storage battery 7 does not decrease. Further, the electrolytic solution surface S does not rise above the upper limit level U, and the electrolytic solution E leaks from the upper portion of the lead storage battery 7 or the electrolytic solution E
The gas in the cell does not cause an abnormal increase in the pressure in the cell.

【0021】鉛蓄電池にて発生した水素ガスは、電解液
Eと一緒に循環して電解液タンク3内に送られ、電解液
タンク3の空気層Aの上方に集まる。ここで電解液タン
ク3上部に設けたガスの排出手段16である吸気管1
7、排出管18及び排出管18に設けたファン19によ
りガスを排出する。電解液タンク3に溜まった電解液E
から発生したガスもこの排出手段16で排出する。
The hydrogen gas generated in the lead storage battery is circulated together with the electrolytic solution E and sent into the electrolytic solution tank 3, where it is collected above the air layer A of the electrolytic solution tank 3. Here, the intake pipe 1 which is the gas discharge means 16 provided above the electrolyte tank 3
7, the exhaust pipe 18 and the fan 19 provided in the exhaust pipe 18 exhaust the gas. Electrolyte E accumulated in the electrolyte tank 3
The gas generated from the gas is also discharged by this discharge means 16.

【0022】このように、電解液Eから発生するガスを
排出手段16にて外部に排出することにより、電解液E
中に再び混在するガスの量は減少し、鉛蓄電池7内の陽
極、陰極間にガスが介在しにくくなり、両極間の化学反
応が阻害されず、鉛蓄電池7の能力低下を抑えることが
できる。
In this way, by discharging the gas generated from the electrolytic solution E to the outside by the discharging means 16, the electrolytic solution E is discharged.
The amount of gas mixed again in the lead storage battery 7 is reduced, the gas is less likely to be present between the anode and the cathode in the lead storage battery 7, the chemical reaction between the two electrodes is not hindered, and the deterioration of the capacity of the lead storage battery 7 can be suppressed. .

【0023】[0023]

【発明の効果】本発明は上記構成により次の効果を発揮
する。請求項1の鉛蓄電池用電解液循環装置は、電解液
タンク内の電解液上方に電解液から発生したガスを排出
するための排出手段を設けたので、電解液から発生した
ガスは排出手段により外部に排出され、電解液中に再び
混在するガス量は減少する。従って、鉛蓄電池内の陽
極、陰極間にガスが介在しにくくなり、電解液と両極の
活物質との化学反応が阻害されず、鉛蓄電池の能力を充
分に発揮することができる。
The present invention has the following effects due to the above configuration. In the electrolytic solution circulating device for a lead storage battery according to claim 1, since the discharging means for discharging the gas generated from the electrolytic solution is provided above the electrolytic solution in the electrolytic solution tank, the gas generated from the electrolytic solution is discharged by the discharging means. The amount of gas discharged outside and mixed again in the electrolytic solution decreases. Therefore, it becomes difficult for gas to intervene between the anode and the cathode in the lead storage battery, the chemical reaction between the electrolytic solution and the active materials of both electrodes is not hindered, and the capacity of the lead storage battery can be fully exhibited.

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

【図1】本発明に係る鉛蓄電池用電解液循環装置の斜視
FIG. 1 is a perspective view of an electrolyte circulating device for a lead storage battery according to the present invention.

【図2】本発明に係る循環装置の模式図(断面図)FIG. 2 is a schematic diagram (cross-sectional view) of a circulation device according to the present invention.

【図3】従来の鉛蓄電池の断面図(要部)FIG. 3 is a sectional view of a conventional lead-acid battery (main part)

【符号の説明】[Explanation of symbols]

1…鉛蓄電池用電解液循環装置、3…電解液タンク、4
…第1導管、5…注入ポンプ、7…鉛蓄電池、8…第2
導管、9…排出ポンプ、16…排出手段、17…吸気
管、18…排気管、19…ファン、A…空気層、E…電
解液。
1 ... Electrolyte circulation device for lead-acid battery, 3 ... Electrolyte tank, 4
… First conduit, 5… Injection pump, 7… Lead storage battery, 8… Second
Conduit, 9 ... Discharge pump, 16 ... Discharge means, 17 ... Intake pipe, 18 ... Exhaust pipe, 19 ... Fan, A ... Air layer, E ... Electrolyte.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 電解液タンク内の電解液を第1導管及び
この導管に介設した注入ポンプにて、鉛蓄電池に供給
し、鉛蓄電池内の電解液を第2導管及びこの導管に介設
した排出ポンプにて電解液タンクに戻す電解液循環装置
において、前記電解液タンク内の電解液上方に電解液か
ら発生したガスを排出するための排出手段を設けたこと
を特徴とする鉛蓄電池用電解液循環装置。
1. An electrolytic solution in an electrolytic solution tank is supplied to a lead storage battery by a first conduit and an injection pump installed in this conduit, and the electrolytic solution in the lead storage battery is installed in a second conduit and this conduit. In the electrolytic solution circulating device for returning the electrolytic solution to the electrolytic solution tank by the discharge pump, a discharging means for discharging a gas generated from the electrolytic solution is provided above the electrolytic solution in the electrolytic solution tank. Electrolyte circulation device.
JP7316977A 1995-12-05 1995-12-05 Electrolyte circulating device for lead-acid battery Pending JPH09161766A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7316977A JPH09161766A (en) 1995-12-05 1995-12-05 Electrolyte circulating device for lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7316977A JPH09161766A (en) 1995-12-05 1995-12-05 Electrolyte circulating device for lead-acid battery

Publications (1)

Publication Number Publication Date
JPH09161766A true JPH09161766A (en) 1997-06-20

Family

ID=18083050

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7316977A Pending JPH09161766A (en) 1995-12-05 1995-12-05 Electrolyte circulating device for lead-acid battery

Country Status (1)

Country Link
JP (1) JPH09161766A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101535975B1 (en) * 2011-07-25 2015-07-10 주식회사 엘지화학 Secondary battery and power storage apparatus including the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101535975B1 (en) * 2011-07-25 2015-07-10 주식회사 엘지화학 Secondary battery and power storage apparatus including the same

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