JPH0533504B2 - - Google Patents
Info
- Publication number
- JPH0533504B2 JPH0533504B2 JP59158198A JP15819884A JPH0533504B2 JP H0533504 B2 JPH0533504 B2 JP H0533504B2 JP 59158198 A JP59158198 A JP 59158198A JP 15819884 A JP15819884 A JP 15819884A JP H0533504 B2 JPH0533504 B2 JP H0533504B2
- Authority
- JP
- Japan
- Prior art keywords
- electrolyte
- cell
- gas
- groove
- lead
- 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
Links
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/70—Arrangements for stirring or circulating the electrolyte
- H01M50/73—Electrolyte stirring by the action of gas on or in the electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/70—Arrangements for stirring or circulating the electrolyte
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Filling, Topping-Up Batteries (AREA)
- Secondary Cells (AREA)
Description
[産業上の利用分野]
本発明は鉛蓄電池の改良に関するものである。
[従来の技術と発明が解決しようとする課題]
鉛蓄電池は希硫酸を電解液としており、周知の
ように充放電反応は次式で表わされる。
PbO2+Pb+2H2SO42PbSO4+2H2O
すなわち電解液の硫酸は、放電で消費され、充
電で生成し、それにつれて液比重は低下あるいは
上昇する。放電で生じた水は極板面に沿つて上昇
し、充電で生じた硫酸は降下するので、充放電サ
イクルによつて電解液は上部が低比重、下部が高
比重という成層化を生じる。これは電池を過充電
すればガツシングによつて解消するが、最近の充
電器は定電圧充電方式のものが多く、成層化はな
かなか解消しないので、極板下部のサルフエーシ
ヨンや容量低下をきたすという問題点がある。
さらに電解液をゲル状にするか、または多孔体
に含浸、保持させたもの、すなわち電解液を非流
動化した密閉形鉛蓄電池にあつては、過充電を行
なつてもガツシングによる液の対流を生じないの
で、成層化の解消が困難であつた。
[課題を解決するための手段]
本発明は鉛蓄電池の上記問題点を解消したもの
で、その要旨は上下に連通し、内部にガスを充満
させた空〓溝をセル内に設け、該溝内の上端部の
ガスは、該溝上縁に配置した多孔体に含浸してい
る電解液を介するかまたはセル内の上部空間を介
して、セル内上部の電解液と平衡するように接触
しており、該溝内の下端部のガスは、該溝下縁に
配置した多孔体に含浸している電解液を介するか
またはセル内の下部空間を介して、セル内下部の
電解液と平衡するように接触していることにあ
る。
本発明になる鉛蓄電池の作用機構は次の通りで
ある。
まず、鉛蓄電池のセル内に、上下に連通し内部
にガスを充満させた空〓溝を設けてあるが、該溝
の上端部のガスはセル内上部の電解液とセル内上
部空間を介して直接に、あるいは周囲と同じ内容
の電解液を含浸している多孔体を介して間接に接
触することで、セル内上部の電解液の濃度および
温度で定まる平衡圧力の水蒸気をガスとして含む
ことになる。他方、該溝の下端部のガスは、セル
内下部の電解液とセル内下部空間を介して直接
に、あるいは周囲と同じ内容の電解液を含浸して
いる多孔体を介して間接に接触することで、セル
内下部の電解液の濃度および温度で定まる平衡圧
力の水蒸気をガスとして含むことになる。すなわ
ち、成層化してセル内上部の電解液が低比重、下
部の電解液が高比重となると、上下に連通する空
〓溝の上部のガスの水蒸気分圧は高く、下部のガ
スの水蒸気分圧は低くなる。下部のガスの水蒸気
分圧を小さくする手段としては、空〓溝下端の多
孔体の温度を低くしてもよい。
ガス空間内は、基体粒子のブラウン運動によつ
て、場所による濃度差は比較的早期に解消する。
したがつて、空〓溝内の上下の水蒸気分圧の差を
解消する方向、すなわち上方から下方へ水蒸気が
移動し、下端の多孔体に水が凝縮生成する。この
空〓溝内の水の移動によつて、セル内の電解液の
成層化が解消される。
液状電解液を用いる通常の鉛蓄電池において
は、空〓溝内への電解液の流入を防ぐために、上
縁部および下縁部に多孔体を充填しておくことが
必要である。また、電解液の侵入を防ぎかつ下端
で生成した水を排出させるために、空〓溝内にガ
ス発生機構、例えば水電解電極を接地して、空隙
溝内のガス圧力をセル内空間の圧力よりも若干高
くしておくことが必要である。
電解液をゲル状とするかまたは、隔離部などの
多孔体に含浸保持させた密閉形鉛蓄電池にあつて
も同様の作用機構で成層化を解消できるが、この
場合にはセル内の電解液は非流動化されているか
ら、空〓溝内に電解液は流入しない。したがつ
て、空〓溝内をセル内空間の圧力よりも高くして
おく必要はなく、ガス発生機構を設置する必要は
ない。
また、空〓溝の上縁部および下縁部には、多孔
体を充填してもしなくてもよい。どちらも空隙溝
内の上端部または下端部のガスは、セル内上部ま
たは下部の空間を介してセル内上部または下部の
電解液と平衡する水蒸気を含むからである。
[実施例]
以下、本発明鉛蓄電池を図面を用いて説明す
る。第1図は本発明鉛蓄電池の一実施例を示すも
ので、図中、1は正極板、2は負極板、3はセパ
レータ、4は希硫酸電解液、5は電槽、6は電槽
底、7は蓋、8は排気部、9は正極端子、10は
負極端子である。また11はプラスチツク管で、
その上縁部と下縁部には多孔体12,12′が装
着されている。また13はプラスチツク管11と
多孔体12,12′とで形成される空間で、セル
内の上下に連通する空〓溝、14は水電解電極で
ある。前記空〓溝13はガスで充満されており、
上端部のガスは上縁部の多孔体12に含浸された
電解液と接し、下端部のガスは下縁部の多孔体1
2′に含浸された電解液と接している。
かかる構造の本発明実施例において、電解液4
が成層化したときには、上縁部の多孔体12に含
浸された低比重の電解液から蒸発した水蒸気が空
〓溝13を充満し、下縁部の多孔体12′に含浸
された高比重の電解液に吸収され、成層化が解消
する。水電解電極14は空間13内に電解液が侵
入したとき、ガスを発生させて電解液を押し戻す
ために用いる。第2図で、15で冷却器で、下縁
部の多孔体12′を冷却する。この場合には上縁
部の多孔体12に含浸されて高温度の希硫酸から
蒸発した水蒸気が空〓溝13を充満し、下縁部の
低温度の多孔体12′で凝縮して水となる。
上記実施例では空〓溝は通常の電解液の液面下
に配置したものを示したが、電解液をゲル状とす
るか、または多孔板に含浸、保持させたもの、す
なわち電解液を非流動化した密閉形鉛蓄電池にも
適用できる。
つぎに、鉛−カルシウム系合金格子を用いた、
高さ約100mmの正、負極板を使用して容量約30Ah
の電池を試作し、成層化解消の実験を行つた結果
を示す。
上縁部および下縁に常用の鉛蓄電池用セパレー
タを張り付けた内径約25mm、長さ100mmのブラス
チツクパイプを極板群の側部に上下方向に配置し
た。液式電池の場合には、下端のセパレータ上約
2mmのところに直径1mmの被覆鉛線2本の先端を
5mmだけ露出させて配し、プラスチツクパイプお
よび電池蓋を貫通して電池外へ引き出した。また
プラスチツクパイプの下端のセパレータの下面に
接して、薄いプラスチツクフイルムで被覆した厚
さ2mmの銅板を配置し、この銅板はセパレータと
接する以外は発泡プラスチツクで被覆、断熱し
た。
このようにして液式電池およびコロイダルシリ
カと希硫酸との混合によるゲル式電池を試作し
た。このとき、極板の中央部以下には液比重約
1.30、中央部以上には約1.20の希硫酸を満たし
て、約25℃で1週間放置後極板上縁部および下縁
部から電解液を採取し濃度を滴定で求めて比重に
換算した。なお、この放置期間中、本発明になる
液式電池に対しては2本の鉛線間に3.0Vを印加
しておいた。
この結果を表1にまとめて示す。
[Industrial Field of Application] The present invention relates to improvements in lead-acid batteries. [Prior Art and Problems to be Solved by the Invention] A lead-acid battery uses dilute sulfuric acid as an electrolyte, and as is well known, the charge/discharge reaction is expressed by the following equation. PbO 2 +Pb+2H 2 SO 4 2PbSO 4 +2H 2 O In other words, sulfuric acid in the electrolytic solution is consumed during discharging and generated during charging, and the specific gravity of the liquid decreases or increases accordingly. Water produced by discharge rises along the electrode plate surface, and sulfuric acid produced by charging descends, so that the electrolytic solution becomes stratified with low specific gravity in the upper part and high specific gravity in the lower part during charge/discharge cycles. This problem can be solved by overcharging the battery through gassing, but many recent chargers use a constant voltage charging method, and stratification is difficult to eliminate, resulting in problems such as sulfation at the bottom of the electrode plate and a decrease in capacity. There is a point. Furthermore, in the case of sealed lead-acid batteries in which the electrolyte is made into a gel or impregnated and held in a porous body, in other words, the electrolyte is made non-fluid, convection of the liquid due to gassing occurs even if overcharged. Therefore, it was difficult to eliminate stratification. [Means for Solving the Problems] The present invention solves the above-mentioned problems of lead-acid batteries. The gas at the upper end of the cell comes into contact with the electrolyte at the upper part of the cell through the electrolyte impregnated in the porous body disposed at the upper edge of the groove or through the upper space within the cell so as to be in equilibrium with the electrolyte at the upper part of the cell. The gas at the lower end of the groove is in equilibrium with the electrolyte at the lower part of the cell via the electrolyte impregnated in a porous body disposed at the lower edge of the groove or via the lower space within the cell. It's about being in contact with each other. The mechanism of action of the lead-acid battery according to the present invention is as follows. First, inside the cell of a lead-acid battery, there is an air groove that communicates vertically and is filled with gas. By contacting the cell directly or indirectly through a porous body impregnated with the same electrolyte as the surroundings, it contains water vapor as a gas at an equilibrium pressure determined by the concentration and temperature of the electrolyte in the upper part of the cell. become. On the other hand, the gas at the lower end of the groove comes into contact with the electrolytic solution in the lower part of the cell either directly through the lower space inside the cell or indirectly through a porous body impregnated with the same electrolytic solution as the surroundings. As a result, water vapor with an equilibrium pressure determined by the concentration and temperature of the electrolytic solution in the lower part of the cell is contained as a gas. In other words, when stratification occurs, and the electrolyte at the top of the cell has a low specific gravity and the electrolyte at the bottom has a high specific gravity, the water vapor partial pressure of the gas at the top of the vertically communicating air groove is high, and the water vapor partial pressure of the gas at the bottom is high. becomes lower. As a means of reducing the water vapor partial pressure of the gas in the lower part, the temperature of the porous body at the lower end of the cavity may be lowered. In the gas space, differences in concentration depending on location are eliminated relatively quickly due to Brownian motion of the base particles.
Therefore, the water vapor moves in a direction that eliminates the difference in water vapor partial pressure between the upper and lower parts of the air groove, that is, from the upper side to the lower side, and water is condensed in the porous body at the lower end. This movement of water within the groove eliminates the stratification of the electrolyte within the cell. In a typical lead-acid battery using a liquid electrolyte, it is necessary to fill the upper and lower edges with a porous material in order to prevent the electrolyte from flowing into the cavity. In addition, in order to prevent the electrolyte from entering and to discharge water generated at the lower end, a gas generation mechanism, such as a water electrolysis electrode, is grounded in the cavity, and the gas pressure in the cavity is reduced to the pressure in the cell space. It is necessary to keep it slightly higher than that. Stratification can be eliminated by the same mechanism of action in sealed lead-acid batteries in which the electrolyte is in gel form or impregnated into a porous body such as an isolation part, but in this case, the electrolyte in the cell Since it is non-fluidized, the electrolyte does not flow into the cavity. Therefore, there is no need to keep the pressure inside the air groove higher than the pressure inside the cell, and there is no need to install a gas generation mechanism. Further, the upper and lower edges of the hollow groove may or may not be filled with a porous material. This is because the gas at the upper end or lower end of the air gap groove contains water vapor that is in equilibrium with the electrolyte at the upper or lower part of the cell via the space at the upper or lower part of the cell. [Example] The lead-acid battery of the present invention will be described below with reference to the drawings. Figure 1 shows an embodiment of the lead-acid battery of the present invention, in which 1 is a positive electrode plate, 2 is a negative electrode plate, 3 is a separator, 4 is a dilute sulfuric acid electrolyte, 5 is a container, and 6 is a container. 7 is a lid, 8 is an exhaust part, 9 is a positive terminal, and 10 is a negative terminal. Also, 11 is a plastic tube,
Porous bodies 12, 12' are attached to the upper and lower edges thereof. Further, 13 is a space formed by the plastic tube 11 and the porous bodies 12, 12', and is a hollow groove that communicates with the upper and lower parts of the cell, and 14 is a water electrolysis electrode. The empty groove 13 is filled with gas,
The gas at the upper end is in contact with the electrolyte impregnated in the porous body 12 at the upper edge, and the gas at the lower end is in contact with the porous body 1 at the lower edge.
2' is in contact with the electrolyte impregnated. In the embodiment of the present invention having such a structure, the electrolyte 4
When the electrolyte is stratified, the water vapor evaporated from the low specific gravity electrolyte impregnated in the porous body 12 at the upper edge fills the air groove 13, and the high specific gravity electrolyte impregnated in the porous body 12' at the lower edge is filled. It is absorbed by the electrolyte, eliminating stratification. The water electrolysis electrode 14 is used to generate gas and push back the electrolyte when the electrolyte enters the space 13. In FIG. 2, a cooler 15 cools the porous body 12' at the lower edge. In this case, water vapor impregnated into the porous body 12 at the upper edge and evaporated from the high-temperature dilute sulfuric acid fills the air groove 13, and condenses in the low-temperature porous body 12' at the lower edge to form water. Become. In the above example, the cavity was shown as being placed below the surface of a normal electrolyte, but it is also possible to use a gel-like electrolyte or a porous plate impregnated and held in the electrolyte. It can also be applied to fluidized sealed lead-acid batteries. Next, using a lead-calcium alloy lattice,
Capacity: Approximately 30Ah using positive and negative electrode plates with a height of approximately 100mm
The results of an experiment on eliminating stratification using a prototype battery are shown below. Plastic pipes with an inner diameter of approximately 25 mm and a length of 100 mm, with regular lead-acid battery separators attached to the upper and lower edges, were placed vertically on the side of the electrode plate group. In the case of a liquid type battery, the tips of two coated lead wires of 1 mm in diameter were placed about 2 mm above the separator at the bottom end with only 5 mm exposed, and the wires were passed through the plastic pipe and battery lid and pulled out of the battery. . In addition, a 2 mm thick copper plate covered with a thin plastic film was placed in contact with the lower surface of the separator at the lower end of the plastic pipe, and this copper plate was covered with foamed plastic and insulated except for the area in contact with the separator. In this way, we prototyped a liquid battery and a gel battery using a mixture of colloidal silica and dilute sulfuric acid. At this time, the liquid density below the center of the electrode plate is approximately
1.30, dilute sulfuric acid of about 1.20 was filled above the center, and after being left at about 25°C for one week, electrolytic solution was collected from the upper and lower edges of the electrode plate, and the concentration was determined by titration and converted to specific gravity. Note that during this standing period, 3.0 V was applied between the two lead wires to the liquid battery according to the present invention. The results are summarized in Table 1.
【表】
表の結果から明らかなように、液式電池では本
発明になる電池No.2はNo.1に比較して放置後の上
下の液比重の差が小さくなつている。またゲル式
電池でも本発明になる電池No.4,No.5はNo.3に比
較して比重差が小さくなつており、成層化の解消
に顕著な効果を有している。
[発明の効果]
以上述べたように、本発明は過充電の少ない充
放電サイクルにおいて発生する鉛蓄電池の電解液
の成層化を解決したもので、極板下部のサルフエ
ーシヨンや容量低下を防いで、鉛蓄電池について
安定した性能を長期間維持することが可能となる
効果を有している。[Table] As is clear from the results in the table, among liquid batteries, battery No. 2 according to the present invention has a smaller difference in the specific gravity of the upper and lower liquids after being left as compared to battery No. 1. Further, among gel type batteries, batteries No. 4 and No. 5 according to the present invention have a smaller specific gravity difference than No. 3, and have a remarkable effect on eliminating stratification. [Effects of the Invention] As described above, the present invention solves the stratification of the electrolyte of lead-acid batteries that occurs during charge/discharge cycles with little overcharging, and prevents sulfation and capacity reduction at the bottom of the electrode plate. This has the effect of allowing lead-acid batteries to maintain stable performance for a long period of time.
第1図は本発明鉛蓄電池の一実施例の概略構造
を示す要部縦断面図、第2図は本発明の鉛蓄電池
に用いる電槽内の下部あるいは底部において水を
生成する機構の他実施例を示す要部縦断面図であ
る。
1……正極板、2……負極板、3……セパレー
タ、4……希硫酸電解液、5……電槽、11……
プラスチツク管、12,12′……多孔体、13
……空〓溝、14,14′……水電解電極、15
……冷却器。
Fig. 1 is a vertical cross-sectional view of the main parts showing the schematic structure of one embodiment of the lead-acid battery of the present invention, and Fig. 2 shows other embodiments of the mechanism for generating water in the lower part or bottom of the battery case used in the lead-acid battery of the present invention. FIG. 3 is a vertical cross-sectional view of a main part showing an example. 1... Positive electrode plate, 2... Negative electrode plate, 3... Separator, 4... Dilute sulfuric acid electrolyte, 5... Battery container, 11...
Plastic tube, 12, 12'...Porous body, 13
...Empty groove, 14, 14'...Water electrolysis electrode, 15
……Cooler.
Claims (1)
溝をセル内に設け、該溝内の上端部のガスは、該
溝上縁に配置した多孔体に含浸している電解液を
介するかまたはセル内の上部空間を介して、セル
内上部の電解液と平衡するように接触しており、
該溝内の下端部のガスは、該溝下縁に配置した多
孔体に含浸している電解液を介するかまたはセル
内の下部空間を介して、セル内下部の電解液と平
衡するように接触していることを特徴とする鉛蓄
電池。1. An air space that connects the top and bottom and is filled with gas.
A groove is provided in the cell, and the gas at the upper end of the groove flows through the electrolytic solution impregnated in the porous body disposed at the upper edge of the groove or through the upper space within the cell. It is in equilibrium contact with the liquid,
The gas at the lower end of the groove is brought into equilibrium with the electrolyte at the lower part of the cell via the electrolyte impregnated in a porous body disposed at the lower edge of the groove or via the lower space within the cell. A lead-acid battery characterized by contact.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15819884A JPS6134858A (en) | 1984-07-27 | 1984-07-27 | Lead-acid battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15819884A JPS6134858A (en) | 1984-07-27 | 1984-07-27 | Lead-acid battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6134858A JPS6134858A (en) | 1986-02-19 |
| JPH0533504B2 true JPH0533504B2 (en) | 1993-05-19 |
Family
ID=15666413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15819884A Granted JPS6134858A (en) | 1984-07-27 | 1984-07-27 | Lead-acid battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6134858A (en) |
-
1984
- 1984-07-27 JP JP15819884A patent/JPS6134858A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6134858A (en) | 1986-02-19 |
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