JPH01117270A - Manufacture of anode plate of lead-acid battery - Google Patents
Manufacture of anode plate of lead-acid batteryInfo
- Publication number
- JPH01117270A JPH01117270A JP62276959A JP27695987A JPH01117270A JP H01117270 A JPH01117270 A JP H01117270A JP 62276959 A JP62276959 A JP 62276959A JP 27695987 A JP27695987 A JP 27695987A JP H01117270 A JPH01117270 A JP H01117270A
- Authority
- JP
- Japan
- Prior art keywords
- anode plate
- active substance
- base board
- current
- immediate use
- 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
Links
- 239000002253 acid Substances 0.000 title claims abstract description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 17
- 239000000126 substance Substances 0.000 claims description 14
- 239000011149 active material Substances 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 6
- 230000003647 oxidation Effects 0.000 abstract description 2
- 238000007254 oxidation reaction Methods 0.000 abstract description 2
- 239000013543 active substance Substances 0.000 abstract 6
- YADSGOSSYOOKMP-UHFFFAOYSA-N lead dioxide Inorganic materials O=[Pb]=O YADSGOSSYOOKMP-UHFFFAOYSA-N 0.000 abstract 1
- 239000000758 substrate Substances 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 230000001133 acceleration Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- PIJPYDMVFNTHIP-UHFFFAOYSA-L lead sulfate Chemical compound [PbH4+2].[O-]S([O-])(=O)=O PIJPYDMVFNTHIP-UHFFFAOYSA-L 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/14—Electrodes for lead-acid accumulators
- H01M4/16—Processes of manufacture
- H01M4/22—Forming of electrodes
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、鉛蓄電池陽極板の製造方法の改良に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION FIELD OF INDUSTRIAL APPLICATION The present invention relates to an improvement in the manufacturing method of a lead-acid battery anode plate.
従来の技術
従来即用式鉛蓄電池は、陽極板および陰極板を化成し、
水洗・乾燥後セパレータを使用して極板群として電槽に
収納して密封保存し、使用時に電解液を注入する電池で
ある。即用式鉛蓄電池に必要とされる性能は、注液後数
分で自動車のエンジンを始動させるに充分な電圧と容量
を有することであり、特に、電圧の確保が重要である。Conventional technology Conventional ready-to-use lead-acid batteries have chemically formed anode plates and cathode plates.
After washing and drying, the battery is sealed and stored in a battery case using a separator as a group of electrode plates, and then filled with electrolyte when used. The performance required of a ready-to-use lead-acid battery is that it has enough voltage and capacity to start an automobile engine within a few minutes after being injected, and securing the voltage is especially important.
以後、注液後の放電電圧性能を即用性能とする。即用式
鉛蓄電池は、保存中に陽極板の基板−活物質界面での高
抵抗体の生成により即用性能が徐々に低下する。即用性
能の低下は、温度や電池内の水分により加速される。そ
のため、性能の低下を抑制するために、電池を低温で保
管する方法や、電池内の水分を少なくする方法が採用さ
れている。Hereinafter, the discharge voltage performance after injection will be considered as the immediate performance. The ready-to-use performance of a ready-to-use lead-acid battery gradually deteriorates during storage due to the formation of a high resistance material at the substrate-active material interface of the anode plate. The decline in ready-to-use performance is accelerated by temperature and moisture in the battery. Therefore, in order to suppress the decline in performance, methods have been adopted to store batteries at low temperatures and to reduce the amount of moisture inside the batteries.
発明が解決しようとする問題点
即用式鉛蓄電池は、充電済の陽極板および陰極板を水洗
・乾燥して電槽にセパレータを使用して極板群として収
納し密封している。しかし、陽極板は、保存中活物質に
よる格子の酸化が起、こり、基板−活物質界面に高抵抗
体が生成する。Problems to be Solved by the Invention In a ready-to-use lead-acid battery, charged anode plates and cathode plates are washed with water, dried, and then stored as a group of plates in a battery case using a separator and sealed. However, during storage, the lattice of the anode plate is oxidized by the active material, resulting in stiffness and formation of a high resistance element at the substrate-active material interface.
この反応速度は、温度及び水分により加速されるが、基
板表面の酸化被膜の組成の影響を大きく受け、酸化被膜
中に酸化数の低い物質が多い場合、早期に即用性能の低
下を招くという欠点を有していた。This reaction rate is accelerated by temperature and moisture, but is greatly affected by the composition of the oxide film on the surface of the substrate, and if the oxide film contains many substances with low oxidation numbers, the ready-to-use performance will quickly deteriorate. It had drawbacks.
化或は、格子表面から始まり、次に極板表面から内部へ
と進行する。しかし、基板表面の一部がpbo、化する
とその場所から表面に向って化成が進行するため、化成
終期においても酸化被膜中に低級酸化物が存在する場合
がある。そのため第2図に示す化成時の電流パターンの
様に、化成終期に断続的に休止を行い、未化成の低級酸
化物を硫酸鉛化し化成を容易にする方法がある。ただし
、第2図の電流パターンは12Ahの陽極板1枚を化成
する時の一例であり、化成電流は1.5Aで、陽極板活
物質の理論容量の200%(1,5Aで16h)通電し
たあと1時間づつ3回休止を行っている。これにより、
基板表面の酸化被膜および活物質の低級酸化物をpbo
、化することができる。しかし、休止中の陽極板の電位
はpbo、とpbso、の平衡電位と等しく、休止中に
生成したPb5O,は、休止中にpbo、化することな
く化成状態が悪い場合や休止時間が長い場合にはpbs
o 、は安定化し、その後化成(充電)してもそのまま
残存する。この様な状態の極板を使用した電池は、保存
中の即用性能が早期に低下する。The process begins at the grating surface and then progresses inward from the plate surface. However, when a part of the substrate surface becomes pbo, the chemical conversion progresses from that location toward the surface, so lower oxides may be present in the oxide film even at the final stage of chemical formation. Therefore, as shown in the current pattern during chemical formation shown in FIG. 2, there is a method in which the process is intermittently paused at the end of chemical formation, and the unformed lower oxide is turned into lead sulfate to facilitate chemical formation. However, the current pattern in Figure 2 is an example when forming one 12Ah anode plate, and the forming current is 1.5A, which is 200% of the theoretical capacity of the anode plate active material (16 hours at 1.5A). After that, I took three breaks of one hour each. This results in
The oxide film on the substrate surface and the lower oxide of the active material are removed by pbo.
, can be converted into However, the potential of the anode plate during rest is equal to the equilibrium potential of pbo and pbso, and the Pb5O generated during rest does not change to pbo during rest. pbs for
o is stabilized and remains as it is even after subsequent chemical formation (charging). A battery using an electrode plate in such a state quickly loses its ready-to-use performance during storage.
問題点を解決するための手段
本発明は上記の点に鑑み、陽極板活物質の理論容量の2
00%通電後の化成途中に、断続的に、セル電圧が2.
2〜2.3Vになる微少電流で化成するものである。Means for Solving the Problems In view of the above points, the present invention solves the problem by reducing the theoretical capacity of the anode plate active material to 2.
During chemical formation after 00% energization, the cell voltage intermittently dropped to 2.
Chemical formation is performed using a minute current of 2 to 2.3V.
作用
基板表面にコンパクトなpbo、の層が形成され保存中
の陽極板の基板−活物質界面の高抵抗体の生成が加速さ
れることな(、即用性能が長期間高いレベルに保たれる
。A compact PBO layer is formed on the surface of the working substrate, which prevents the acceleration of the formation of high resistance at the substrate-active material interface of the anode plate during storage (and keeps the immediate performance at a high level for a long time). .
実施例
36 B 20系鉛蓄電池用陽極板(12Ah)を第1
図に示す電流パターンで化成した。a部における微少電
流値によりセル電圧を変化させた陽極板を作製した。こ
の時の電解液すの時点比重は、20℃換算で1ρ60、
温度は30℃である。これらの基板を用いた電池を作製
し60℃で7月保存した後の即用性能を調べた。即用性
能は0℃で150日で放電した時の5秒目電圧であり、
その結果を第2図に示す。放電方向(セル電圧が低い)
の場合は初期より即用性能が低下している。また、充電
方向も電池圧が高くなると保存後の即用性能が低下した
。Example 36 B The anode plate (12Ah) for 20 series lead acid battery was
Chemical formation was performed using the current pattern shown in the figure. An anode plate was produced in which the cell voltage was changed depending on the minute current value in part a. The specific gravity of the electrolyte at this time is 1ρ60 at 20℃,
The temperature is 30°C. Batteries using these substrates were prepared and stored at 60° C. for July, and then their ready-to-use performance was examined. Immediate performance is the voltage at the 5th second when discharged for 150 days at 0℃,
The results are shown in FIG. Discharge direction (low cell voltage)
In the case of , the ready-to-use performance has deteriorated from the initial stage. In addition, in the charging direction, as the battery pressure increased, the ready-to-use performance after storage decreased.
発明の効果
上述したように、本発明によれば基板表面の酸化被膜の
pbo、化率を向上することにより、陽極板基板−活物
質界面の高抵抗体の成長が抑制され、即用性能が長期間
高いレベルに保たれる等工業的価値極めて大なるもので
ある。Effects of the Invention As described above, according to the present invention, by improving the pbo, conversion rate of the oxide film on the substrate surface, the growth of a high resistance element at the anode plate substrate-active material interface is suppressed, and the ready-to-use performance is improved. It has great industrial value as it can be maintained at a high level for a long period of time.
第1図は本発明による化成時における電流パターンを示
す説明図、第2図は第1図におけるb部の時のセル電圧
と60℃で7日間保存した後の即用性能の関係を示す曲
線図で、第3図は従来の化成時における電流パターンの
一例を示す説明図である。
¥1図
時間(1′L)
第3図
時間(h)Figure 1 is an explanatory diagram showing the current pattern during chemical formation according to the present invention, and Figure 2 is a curve showing the relationship between the cell voltage at section b in Figure 1 and the ready-to-use performance after storage at 60°C for 7 days. In the figure, FIG. 3 is an explanatory diagram showing an example of a current pattern during conventional chemical formation. ¥1 Figure Time (1'L) Figure 3 Time (h)
Claims (1)
理論容量の200%通電後の化成途中に断続的にセル電
圧が2.2〜2.3Vなる微少電流で化成することを特
徴とする鉛蓄電池陽極板の製造方法。In the chemical formation process of anode plates for lead-acid batteries, the process is characterized in that during formation after 200% of the theoretical capacity of the anode plate active material is energized, chemical formation is carried out intermittently with a minute current that produces a cell voltage of 2.2 to 2.3V. A method for producing a lead-acid battery anode plate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62276959A JPH01117270A (en) | 1987-10-30 | 1987-10-30 | Manufacture of anode plate of lead-acid battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62276959A JPH01117270A (en) | 1987-10-30 | 1987-10-30 | Manufacture of anode plate of lead-acid battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01117270A true JPH01117270A (en) | 1989-05-10 |
Family
ID=17576792
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62276959A Pending JPH01117270A (en) | 1987-10-30 | 1987-10-30 | Manufacture of anode plate of lead-acid battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01117270A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007151657A (en) * | 2005-12-01 | 2007-06-21 | Matsushita:Kk | Hanger |
-
1987
- 1987-10-30 JP JP62276959A patent/JPH01117270A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007151657A (en) * | 2005-12-01 | 2007-06-21 | Matsushita:Kk | Hanger |
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