JPH0480515B2 - - Google Patents
Info
- Publication number
- JPH0480515B2 JPH0480515B2 JP58114687A JP11468783A JPH0480515B2 JP H0480515 B2 JPH0480515 B2 JP H0480515B2 JP 58114687 A JP58114687 A JP 58114687A JP 11468783 A JP11468783 A JP 11468783A JP H0480515 B2 JPH0480515 B2 JP H0480515B2
- Authority
- JP
- Japan
- Prior art keywords
- cathode
- plates
- electrode plate
- electrolyte
- plate
- 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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/34—Gastight accumulators
- H01M10/342—Gastight lead accumulators
-
- 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
- Secondary Cells (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
Description
【発明の詳細な説明】
本発明は陰極吸収式の密閉形鉛蓄電池の改良に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a cathode absorption type sealed lead acid battery.
一般に陰極吸収式密閉形鉛蓄電池なるものは充
電中において陽極板より発生する酸素ガスを陰極
板に吸収させ、陰極活物質に反応せしめて外部へ
のガス逃出を阻止せしめる構造のものである。 In general, a cathode absorption type sealed lead acid battery has a structure in which oxygen gas generated from an anode plate during charging is absorbed into the cathode plate, reacts with the cathode active material, and prevents the gas from escaping to the outside.
従来この種鉛蓄電池は、必要枚数の陰、陽極板
にそれぞれ電解液を含浸保持させるリテーナを間
に介在せしめ交互に積層して構成した極板群を以
つて電槽内に収納し、該極板群の全面が浸漬する
か、又はそれより若干多量の電解液を注入浸漬せ
しめて充放電するのであつて、液面高さは常時極
板全面を浸漬せしめておかねばならないのが一般
的であつた。従つて酸素ガスの陰極板での吸収反
応が良好でない等の問題があつた。 Conventionally, this type of lead-acid battery has a group of electrode plates that are stacked alternately with a retainer interposed between the required number of negative and anode plates to impregnate and hold the electrolyte, and the electrodes are housed in a battery case. Generally, the entire surface of the plate group is immersed, or a slightly larger amount of electrolyte is injected and immersed for charging and discharging, and the liquid level is such that the entire surface of the electrode plate must be immersed at all times. It was hot. Therefore, there were problems such as poor absorption reaction of oxygen gas on the cathode plate.
本発明は上記欠点を除去するもので、電槽内の
液面高さを極板の高さの1/2乃至1/10の位置まで
とし、該電解液面上部において電槽壁と極板群両
端の陰極板間の少なくとも一方の側に空隙部を設
けて、ガスの陰極吸収反応を良好にせしめ以て蓄
電池の性能を向上させた構造の密閉形鉛蓄電池を
提供するものである。 The present invention eliminates the above-mentioned drawbacks by setting the liquid level in the battery case to 1/2 to 1/10 of the height of the electrode plate, and above the electrolyte level, the battery case wall and the electrode plate are connected to each other. To provide a sealed lead-acid battery having a structure in which a gap is provided on at least one side between the cathode plates at both ends of the group to improve the cathode absorption reaction of gas and improve the performance of the battery.
本発明の実施例を図面について説明すると、1
は陰極板2、リテーナ3、陽極板4を必要枚数交
互に積層し、上部に極柱5を植立してなる極板
群、6は該極板群1を槽底部7に載置収納せる電
槽、8は極板群1を電槽6内に収納するときに極
板群1に所定の群加圧をかけるために極板群1の
両端板(陰極板)2′と電槽6の壁部9との間に
強挿入せしめたスペーサ、10は電解液で、Aは
液面位をあらわす。11は電槽6の上部、即ち上
蓋12の裏面との間における壁部9ち極板群1の
両端の陰極板2′間の空隙部である。 Embodiments of the present invention will be explained with reference to the drawings: 1
6 is a group of electrode plates formed by alternately stacking the required number of cathode plates 2, retainers 3, and anode plates 4, with a pole column 5 planted on top; 6 is a group of electrode plates 1 placed and stored on the tank bottom 7. A battery case 8 includes both end plates (cathode plates) 2' of the electrode plate group 1 and the battery case 6 in order to apply a predetermined group pressure to the electrode plate group 1 when storing the electrode plate group 1 in the battery case 6. 10 is an electrolytic solution, and A indicates the liquid level. Reference numeral 11 denotes a wall portion 9 between the upper part of the battery case 6, that is, the back surface of the upper lid 12, or a gap between the cathode plates 2' at both ends of the electrode plate group 1.
電槽6内に注液する電解液10の液面位Aを極
板の高さの1/2乃至1/10とすることによつて極板
群1の両端陰極板2′と壁部9との間に電槽6の
高さ−電解液10の液面位Aの高さの空隙部11
が現出する。陰極吸収式密閉形鉛蓄電池において
は、陽極板4より発生する酸素ガスを陰極板2に
よつて吸収し反応させるのであるが、その吸収反
応する部分の殆どが極板群1の両端に有する陰極
板2′によるものであつて、この両端の陰極板
2′は放電作用とガス吸収反応作用の両方の作用
を担当するものであり、極板群1上部に電解液中
に浸漬しない板面があると云えども、陰陽両極板
間に介在せしめたリテーナ3には電解液が含浸さ
れ保持されてあり、更に極板高さの1/2乃至1/10
高さの液面位を有する電解液10よりの電解液滲
透があつてリテーナ3は常に十分なる電解液に含
浸させて常時液リツチの状態であつて、これらよ
り本発明鉛蓄電池の性能を向上せしめると共に陰
極吸収反応を良好な状態にすることが可能となる
ものである。 By setting the liquid level A of the electrolytic solution 10 injected into the battery container 6 to 1/2 to 1/10 of the height of the electrode plates, the cathode plates 2' at both ends of the electrode plate group 1 and the wall portion 9 There is a gap 11 between the height of the battery container 6 and the liquid level A of the electrolytic solution 10.
appears. In a cathode absorption type sealed lead-acid battery, oxygen gas generated from the anode plate 4 is absorbed by the cathode plate 2 and reacted with it, but most of the absorption and reaction portion occurs in the cathode at both ends of the electrode plate group 1. The cathode plates 2' at both ends are responsible for both the discharge action and the gas absorption reaction action, and there is a plate surface on the top of the electrode plate group 1 that is not immersed in the electrolyte. However, the retainer 3 interposed between the negative and positive electrode plates is impregnated with and retained an electrolyte, and furthermore, the retainer 3 is impregnated with an electrolytic solution and has a height of 1/2 to 1/10 of the plate height.
There is electrolyte seepage from the electrolyte 10 having a high liquid level, so that the retainer 3 is always impregnated with a sufficient amount of electrolyte and is always in a liquid-rich state, thereby improving the performance of the lead-acid battery of the present invention. At the same time, it becomes possible to bring the cathode absorption reaction into a favorable state.
第2図は本発明蓄電池のガス反応効率と、容量
との液面位高さに対する効果の一例を示すもの
で、これによれば液面位高さを高くするに従いガ
ス反応効率は若干の低下があるが、通常の使用状
態(浮動充電状態)では殆ど問題とならない。 Figure 2 shows an example of the effect of the gas reaction efficiency and capacity on the liquid level height of the storage battery of the present invention. According to this figure, as the liquid level height increases, the gas reaction efficiency slightly decreases. However, under normal usage conditions (floating charge state), this is hardly a problem.
この場合の陰極吸収反応は液面位上部における
電槽6の壁部9と極板群1の両端にある陰極板
2′との間に空隙部11を設けたことによつて所
謂、三相状態、即ち極板、電解液、空気(この場
合酸素ガス)が接している状態が形成され、陽極
板4より発生する酸素ガスとの反応は、この部分
で容易に作用することになる。電解液10の液面
位高さAを極板高さの1/2から1/10とした理由は
極板数量や極板高さ(大きさ)により、その効果
が若干ずれる為である。かくの如く密閉形鉛蓄電
池に用いられるリテーナ3はガラス繊維よりなる
袋状を予め電解液10を含浸させた該袋中に極板
(陽極板4又は陰極板2)を挿入させて極板群1
を構成するものであり、この極板群1を電槽6内
に挿入した後も電解液を注入することなくリテー
ナ3に含浸させた電解液により充放電を行なうの
であるのが通常であるが、本発明は更にリテーナ
3含浸の電解液量を潤決に保持させるべく、極板
高さの1/2から1/10の液面位にて電解液を注入す
るものである。ところでこの液量をこの限定液面
位より多量とするときには陽極板4より発生する
酸素ガスを吸収する陰極板の吸収面積が減少する
こになつて反応作用が阻害される。従つて電解液
量を陰極へのガス吸収反応に影響を与えない範囲
にして電池性能の向上を図つたものである。 In this case, the cathode absorption reaction is carried out in a so-called three-phase manner by providing a gap 11 between the wall 9 of the battery container 6 above the liquid level and the cathode plates 2' at both ends of the electrode plate group 1. A state is formed in which the electrode plate, electrolyte, and air (in this case, oxygen gas) are in contact with each other, and the reaction with the oxygen gas generated from the anode plate 4 easily occurs at this portion. The reason why the liquid level height A of the electrolytic solution 10 is set to 1/2 to 1/10 of the electrode plate height is that the effect varies slightly depending on the number of electrode plates and the electrode plate height (size). As described above, the retainer 3 used in a sealed lead-acid battery is constructed by inserting an electrode plate (anode plate 4 or cathode plate 2) into a bag-shaped bag made of glass fiber impregnated with electrolyte 10 in advance. 1
Even after inserting this electrode plate group 1 into the battery case 6, charging and discharging is normally performed using the electrolytic solution impregnated into the retainer 3 without injecting any electrolytic solution. In the present invention, the electrolytic solution is further injected at a liquid level of 1/2 to 1/10 of the height of the electrode plate in order to maintain the amount of electrolytic solution impregnated in the retainer 3 at a constant level. By the way, when this liquid amount is made larger than this limited liquid level, the absorption area of the cathode plate which absorbs the oxygen gas generated from the anode plate 4 decreases, and the reaction action is inhibited. Therefore, the battery performance is improved by setting the amount of electrolyte within a range that does not affect the gas absorption reaction to the cathode.
上述せる如く本発明の密閉形鉛蓄電池は陰極吸
収反応を極めて良好な状態として蓄電池性能を大
巾に向上せしめる等その工業的価値は極めて大な
るものである。 As mentioned above, the sealed lead-acid battery of the present invention has extremely good industrial value, as it allows the cathode absorption reaction to occur in an extremely good condition, greatly improving the storage battery performance.
第1図は本発明の実施例を示す密閉形鉛蓄電池
の断面図、第2図は本発明密閉形鉛蓄電池のガス
反応効率と容量との電解液面高さに対する効果を
示す特性曲線図である。
1は極板群、2は陰極板、2′は両端の陰極板、
3はリテーナ、4は陽極板、6は電槽、9は壁
部、10は電解液、Aは液面位、11は空隙部。
FIG. 1 is a cross-sectional view of a sealed lead-acid battery according to an embodiment of the present invention, and FIG. 2 is a characteristic curve diagram showing the effects of gas reaction efficiency and capacity on electrolyte level height of the sealed lead-acid battery of the present invention. be. 1 is a group of electrode plates, 2 is a cathode plate, 2' is a cathode plate at both ends,
3 is a retainer, 4 is an anode plate, 6 is a battery case, 9 is a wall, 10 is an electrolytic solution, A is a liquid level, and 11 is a gap.
Claims (1)
介在させ、充電中に陽極板より発生する酸素ガス
を陰極板に吸収して陰極活物質に反応させること
により外部へのガス逃出を阻止せしめる構造を有
する陰極吸収式の密閉形鉛蓄電池において、電解
液面高さを極板高さの1/2乃至1/10となし、該電
解液面上で電槽壁と極板群両端の陰極板間の少な
くとも一方の側に空隙部を形成せしめることを特
徴とする密閉形鉛蓄電池。1 A retainer impregnated with electrolyte is interposed between the negative and anode plates, and oxygen gas generated from the anode plate during charging is absorbed into the cathode plate and reacted with the cathode active material, thereby preventing gas from escaping to the outside. In a sealed lead-acid battery of cathode absorption type, the electrolyte level is set at 1/2 to 1/10 of the electrode plate height, and the cell wall and both ends of the electrode plate group are A sealed lead-acid battery characterized by forming a void on at least one side between the cathode plates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58114687A JPS607071A (en) | 1983-06-24 | 1983-06-24 | Sealed lead-acid battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58114687A JPS607071A (en) | 1983-06-24 | 1983-06-24 | Sealed lead-acid battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS607071A JPS607071A (en) | 1985-01-14 |
| JPH0480515B2 true JPH0480515B2 (en) | 1992-12-18 |
Family
ID=14644123
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58114687A Granted JPS607071A (en) | 1983-06-24 | 1983-06-24 | Sealed lead-acid battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS607071A (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62122076A (en) * | 1985-11-21 | 1987-06-03 | Japan Storage Battery Co Ltd | Large sealed lead-acid battery |
| JPH0628169B2 (en) * | 1987-03-09 | 1994-04-13 | 日本電池株式会社 | Sealed lead acid battery |
| JPH0624144B2 (en) * | 1987-03-09 | 1994-03-30 | 日本電池株式会社 | Sealed lead acid battery |
| JPH0495360A (en) * | 1990-07-31 | 1992-03-27 | Shin Kobe Electric Mach Co Ltd | Closed type lead storage battery |
| JP2002260717A (en) * | 2001-03-01 | 2002-09-13 | Matsushita Electric Ind Co Ltd | Control valve type lead storage battery |
| JP4507483B2 (en) * | 2002-06-06 | 2010-07-21 | パナソニック株式会社 | Control valve type lead acid battery |
| JP2006318879A (en) * | 2005-05-11 | 2006-11-24 | Mase Shunzo | Sealed lead-acid battery |
| JP5012047B2 (en) * | 2007-01-29 | 2012-08-29 | パナソニック株式会社 | Lead acid battery |
-
1983
- 1983-06-24 JP JP58114687A patent/JPS607071A/en active Granted
Non-Patent Citations (2)
| Title |
|---|
| JOURNAL OH THE ELECTROCHEMICAL SOCIETY=1969 * |
| LEAD 68 EDITED PROCEEDINGS THIRD INTERNATIONAL CONFERENCE ON LEADVENICE 155-167 * |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS607071A (en) | 1985-01-14 |
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