JPH05258746A - Pole plate of lead-acid storage battery and manufacture thereof - Google Patents
Pole plate of lead-acid storage battery and manufacture thereofInfo
- Publication number
- JPH05258746A JPH05258746A JP4050507A JP5050792A JPH05258746A JP H05258746 A JPH05258746 A JP H05258746A JP 4050507 A JP4050507 A JP 4050507A JP 5050792 A JP5050792 A JP 5050792A JP H05258746 A JPH05258746 A JP H05258746A
- Authority
- JP
- Japan
- Prior art keywords
- electrode plate
- lead
- paste
- pole plate
- plate paste
- 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
Classifications
-
- 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
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は鉛蓄電池の極板とその製
造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a lead-acid battery electrode plate and a method for manufacturing the same.
【0002】[0002]
【従来の技術】従来、鉛蓄電池用の極板ペーストは酸化
鉛に水と希硫酸、さらには各種の添加剤を加え、混合し
ていた。そして酸化鉛と希硫酸の反応による発熱反応に
より、混合中の極板ペーストの温度は上昇し、水分の蒸
発分離あるいは反応の不均一化によって、できあがった
極板ペーストの組成が不均一になったり、生成した極板
ペーストの粒子径が不均一であることが多く、極板ペー
ストの均一化を図ることは困難であった。また、発熱反
応を抑制するため硫酸の添加速度を緩やかにし、混合時
間を長くする方法、あるいは混合機を水冷などにより冷
却する方法、あるいは混合材料の水、希硫酸などをあら
かじめ冷却してから加えるなどの方法がとられていた。
しかしこれらの混合方法は非能率であったり、冷却にコ
ストを要するなどの問題点があった。2. Description of the Related Art Heretofore, an electrode plate paste for a lead storage battery has been prepared by mixing lead oxide with water, dilute sulfuric acid and various additives. Then, the temperature of the electrode plate paste during mixing rises due to the exothermic reaction caused by the reaction of lead oxide and dilute sulfuric acid, and the composition of the electrode plate paste that is completed may become non-uniform due to evaporation and separation of water or nonuniform reaction. In many cases, the particle size of the produced electrode plate paste was not uniform, and it was difficult to make the electrode plate paste uniform. Further, in order to suppress the exothermic reaction, a method of slowing the addition rate of sulfuric acid and prolonging the mixing time, a method of cooling the mixer by water cooling, etc., or a method of adding water and dilute sulfuric acid as a mixed material after cooling them beforehand And so on.
However, these mixing methods have problems such as inefficiency and costly cooling.
【0003】[0003]
【発明が解決しようとする課題】従来の鉛蓄電池の極板
ならびにその製造方法の問題点は酸化鉛と希硫酸の反応
による発熱反応により混合中の極板ペーストの温度は上
昇し、水分の蒸発分離あるいは反応の不均一化により、
できあがった極板ペーストの組成が不均一になったり、
あるいは生成した極板ペーストの粒子径が不均一になる
ことが多く、このため、極板ペースト中の水分量にばら
つきが生じ、その結果熟成乾燥後の未化成活物質の粒子
間の結合にばらつきが生じることであった。そしてこれ
らの極板ペーストの粒子径のばらつきあるいは未化成活
物質の結合のばらつきは、鉛蓄電池として完成した場合
は充放電を繰り返して使用するサイクル寿命の低下を生
じ、電池寿命が短いという問題を引き起こしていた。The problem with the conventional lead-acid battery electrode plate and its manufacturing method is that the temperature of the electrode plate paste during mixing rises due to the exothermic reaction of the reaction between lead oxide and dilute sulfuric acid, and the evaporation of water Separation or heterogeneity of the reaction
The composition of the finished electrode plate paste becomes uneven,
Alternatively, the particle size of the generated electrode plate paste is often non-uniform, which causes variations in the amount of water in the electrode plate paste, resulting in variations in the bond between the particles of the unactivated active material after aging and drying. Was to occur. And variations in the particle size of these electrode plate pastes or variations in the binding of the non-activated material cause a decrease in the cycle life of repeated charge and discharge when the lead storage battery is completed, and the battery life is short. Was causing it.
【0004】本発明は、上記従来の問題点を解決して、
確実な手段により、鉛蓄電池に組立てた場合の充放電サ
イクル寿命の低下がないペーストを有する極板とその製
造方法を提供することを目的とするものである。The present invention solves the above conventional problems,
An object of the present invention is to provide an electrode plate having a paste that does not reduce the charge / discharge cycle life when assembled into a lead storage battery by a reliable means, and a method for manufacturing the same.
【0005】[0005]
【課題を解決するための手段】本発明は、前記従来の問
題点を解決するために、鉛蓄電池の極板ペーストの粒子
径を、250μmより小さい粒子が全体の極板ペースト
の粒子に対して重量比で90%以上としたものである。SUMMARY OF THE INVENTION In order to solve the above-mentioned conventional problems, the present invention has a particle size of the electrode plate paste of a lead storage battery in which particles smaller than 250 μm have a particle size smaller than that of the entire electrode plate paste. The weight ratio is 90% or more.
【0006】また、熟成乾燥後の未化成活物質の比表面
積が1.5m2 /g乃至3.5m2/gとしたものであ
る。The specific surface area of the unformed active material after aging and drying is 1.5 m 2 / g to 3.5 m 2 / g.
【0007】そして、酸化鉛と希硫酸と水とを主体とし
て練り合わせ、混合する混合機の攪拌モーターの負荷電
力または負荷電流を測定して、攪拌モーターの負荷が、
混合する極板ペースト中の重量比で90%以上の粒子が
250μmより小さい径になる攪拌モータ個有の値に安
定するまで攪拌・混合する工程を有する鉛蓄電池の極板
製造方法としたものである。Then, the load power or load current of the stirring motor of the mixer for kneading and mixing lead oxide, dilute sulfuric acid and water as main components is measured, and the load of the stirring motor is
A method for manufacturing an electrode plate for a lead storage battery, comprising a step of stirring and mixing until 90% or more of particles in the electrode plate paste to be mixed have a diameter of less than 250 μm and have a stirring motor-specific value. is there.
【0008】さらに、攪拌・混合工程を攪拌モーターの
負荷によって制御して、熟成乾燥後の未化成活物質の比
表面積を1.5m2 /g乃至3.5m2 /gとする攪拌
・混合を行う工程を有する鉛蓄電池の極板製造方法とし
たものである。Further, the stirring / mixing process is controlled by the load of the stirring motor to perform stirring / mixing in which the specific surface area of the unformed active material after aging and drying is 1.5 m 2 / g to 3.5 m 2 / g. This is a method for manufacturing a lead-acid battery electrode plate having steps to be performed.
【0009】[0009]
【作用】極板ペーストの混合中には水分の逃散がない混
合機を用いると、混合機の攪拌モーターの負荷により、
極板ペーストの混合状態が観測されるため、極板ペース
トの密度の変化すなわち粒子径の変化を攪拌モーターの
負荷として読み取ることができる。この結果、最適な粒
子径となり、均一化されて攪拌モーターの負荷が安定し
たところで混合を終了させると、均一組成の極板ペース
トを得ることができる。そして極板ペーストの粒子径が
熟成乾燥後の未化成活物質の比表面積を決定するもので
ある。従ってこのようにして得られた極板ペーストを用
いて鉛蓄電池の極板を製造すると、従来のばらつきが大
きな粒子による極板ペーストと比べて、極板ペースト中
の水分の保持特性が良好になるため、熟成反応を均一に
進行させることができ、活物質粒子間の結合に優れた三
塩基性硫酸鉛を得ることができる。これらの極板を用い
た鉛蓄電池の充放電サイクル寿命は従来例の鉛蓄電池と
比べて優れたものとなる。When a mixer that does not allow water to escape during mixing of the electrode plate paste is used, the load on the stirring motor of the mixer causes
Since the mixed state of the electrode plate paste is observed, the change in the density of the electrode plate paste, that is, the change in the particle size can be read as the load of the stirring motor. As a result, when the mixing is terminated when the particle size becomes optimum and the load on the stirring motor is stabilized after being made uniform, it is possible to obtain an electrode plate paste having a uniform composition. The particle size of the electrode plate paste determines the specific surface area of the unformed active material after aging and drying. Therefore, when the electrode plate of the lead storage battery is manufactured using the electrode plate paste thus obtained, the retention property of the water content in the electrode plate paste is improved as compared with the conventional electrode plate paste with particles having large variations. Therefore, the aging reaction can be uniformly progressed, and tribasic lead sulfate having excellent bonding between the active material particles can be obtained. The charge / discharge cycle life of the lead acid battery using these electrode plates is superior to that of the conventional lead acid battery.
【0010】[0010]
【実施例】以下に本発明の一実施例を図により説明す
る。An embodiment of the present invention will be described below with reference to the drawings.
【0011】実施例の極板ペーストの製造はブレード形
の混合機によるものである。混合中のモーターの負荷変
動とその時のペースト粒子を目開き250μmのふるい
上のパーセント(重量比)を図1に示した。図1、図2
および図3より明らかなように、モーター負荷とペース
ト粒子径の分布には相関があり、また、そのときの未化
成活物質の比表面積とも相関があるため、本発明の製造
方法によれば均一なペーストと未化成極板の製造が可能
となる。The electrode plate paste of the embodiment is manufactured by a blade type mixer. The load fluctuation of the motor during mixing and the percentage (weight ratio) of paste particles at that time on a sieve having a mesh size of 250 μm are shown in FIG. 1 and 2
As is clear from FIG. 3 and FIG. 3, there is a correlation between the motor load and the distribution of the paste particle size, and also the specific surface area of the unactivated material at that time. It is possible to manufacture various pastes and unformed electrode plates.
【0012】また、このようにして得られた極板ペース
トによる未化成極板は、活物質の比表面積が1.5〜
3.5m2 /gとほぼ一定となるため、活物質の均一さ
が裏づけられる。The unformed electrode plate made of the electrode plate paste thus obtained has a specific surface area of the active material of 1.5 to
Since it is almost constant at 3.5 m 2 / g, the uniformity of the active material is supported.
【0013】実施例では酸化鉛500kgに対し、水5
00リットル、比重1.40の希硫酸500リットルを
用いた時の結果を示すが、水と希硫酸の加える比率を変
えても実施例に示す内容と同様の結果が得られた。In the embodiment, 5 kg of water is added to 500 kg of lead oxide.
The results are shown when 500 liters of dilute sulfuric acid having a specific gravity of 1.40 and 00 liters were used, but the same results as those shown in the examples were obtained even when the ratio of water and dilute sulfuric acid was changed.
【0014】また、これらの極板を用いて作成した電池
のサイクル寿命試験結果を図4に示す。電池は公称電圧
12V、公称容量2.0AHの電池で、充電は定電圧1
4.7V/0.8Aで6時間行い、放電は16オーム
で、放電終止電圧は10.5Vとした。図4より明らか
なように、ペースト粒子が均一に混合攪拌されている本
発明のペーストから作られた電池のサイクル寿命特性は
良好である。FIG. 4 shows the results of the cycle life test of the battery prepared by using these electrode plates. The battery has a nominal voltage of 12 V and a nominal capacity of 2.0 AH, and is charged at a constant voltage of 1
The discharge was performed at 4.7 V / 0.8 A for 6 hours, the discharge was 16 ohms, and the discharge end voltage was 10.5 V. As is clear from FIG. 4, the cycle life characteristics of the battery made from the paste of the present invention in which the paste particles are uniformly mixed and stirred are good.
【0015】なお、実施例では負荷電力の変動を示した
が、負荷が示されるのであれば電流との関係を求めるこ
とによって本発明を実現することができる。Although the load power fluctuation is shown in the embodiment, the present invention can be realized by obtaining the relationship with the current if the load is shown.
【0016】[0016]
【発明の効果】上記のように、本発明によれば均一な極
板ペースト製造が可能となり、得られた極板を用いて製
造された鉛蓄電池のサイクル寿命は優れたものとなるた
め、その効果は極めて大きい。As described above, according to the present invention, it is possible to manufacture a uniform electrode plate paste, and the cycle life of a lead acid battery manufactured using the obtained electrode plate is excellent. The effect is extremely large.
【図1】極板ペースト製造状態における攪拌混合モータ
ーの負荷(電力)と極板ペースト中の粒子の比率を示す
図FIG. 1 is a diagram showing a load (electric power) of a stirring / mixing motor and a ratio of particles in the electrode plate paste in the electrode plate paste manufacturing state.
【図2】モーター負荷とペースト中の粒子の比率の相関
を示す図FIG. 2 is a diagram showing a correlation between a motor load and a ratio of particles in the paste.
【図3】ペースト粒子と未化成活物質の比表面積の関係
を示す図FIG. 3 is a diagram showing the relationship between the specific surface area of paste particles and the non-active material.
【図4】本発明の実施例と従来例の電池による充放電サ
イクル寿命の電池特性の例を示す図FIG. 4 is a diagram showing an example of battery characteristics of charge / discharge cycle life by batteries of an example of the present invention and a conventional example.
Claims (4)
合する極板ペーストにおいて、その極板ペーストの粒子
径を、250μmより小さい粒子が全体の極板ペースト
の粒子に対して重量比で90%以上とした極板ペースト
を充填した鉛蓄電池の極板。1. An electrode plate paste mainly composed of lead oxide, dilute sulfuric acid and water, wherein the particle size of the electrode plate paste is smaller than 250 μm with respect to the particles of the whole electrode plate paste. A lead acid battery electrode plate filled with an electrode plate paste having a ratio of 90% or more.
積が1.5m2 /g乃至3.5m2 /gとした鉛蓄電池
の極板。2. A lead-acid battery electrode plate in which the specific surface area of the unformed active material after aging and drying of the electrode plate is 1.5 m 2 / g to 3.5 m 2 / g.
合する混合機の攪拌モーターの負荷を測定して、攪拌モ
ーターの負荷測定値が、混合する極板ペースト中の重量
比で90%以上の粒子が250μmより小さい径になる
攪拌モーター個有の値に安定するまで攪拌・混合する工
程を有する鉛蓄電池の極板製造方法。3. The load of a stirring motor of a mixer which mainly mixes lead oxide, dilute sulfuric acid, and water is measured, and the measured load of the stirring motor is a weight ratio in the electrode plate paste to be mixed. A method for producing a lead-acid battery electrode plate, which comprises a step of stirring and mixing until 90% or more of the particles have a diameter smaller than 250 μm and the stirring motor has a stable value.
合する混合機の攪拌モーターの負荷によって、塾生乾燥
後の未化成活物質の比表面積を1.5m2 /g乃至3.
5m2 /gに制御する攪拌・混合工程を有する鉛蓄電池
の極板製造方法。4. The specific surface area of the non-activated material after the scholarship drying is 1.5 m 2 / g to 3. depending on the load of a stirring motor of a mixer that mainly mixes lead oxide, dilute sulfuric acid, and water.
A method for manufacturing a lead-acid battery electrode plate, which comprises a stirring / mixing step of controlling to 5 m 2 / g.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4050507A JPH05258746A (en) | 1992-03-09 | 1992-03-09 | Pole plate of lead-acid storage battery and manufacture thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4050507A JPH05258746A (en) | 1992-03-09 | 1992-03-09 | Pole plate of lead-acid storage battery and manufacture thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05258746A true JPH05258746A (en) | 1993-10-08 |
Family
ID=12860876
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4050507A Pending JPH05258746A (en) | 1992-03-09 | 1992-03-09 | Pole plate of lead-acid storage battery and manufacture thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05258746A (en) |
-
1992
- 1992-03-09 JP JP4050507A patent/JPH05258746A/en active Pending
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