JPH09289015A - Manufacture of electrode plate for lead-acid battery - Google Patents

Manufacture of electrode plate for lead-acid battery

Info

Publication number
JPH09289015A
JPH09289015A JP8099720A JP9972096A JPH09289015A JP H09289015 A JPH09289015 A JP H09289015A JP 8099720 A JP8099720 A JP 8099720A JP 9972096 A JP9972096 A JP 9972096A JP H09289015 A JPH09289015 A JP H09289015A
Authority
JP
Japan
Prior art keywords
lead
monoxide
powder
electrode plate
aging process
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.)
Withdrawn
Application number
JP8099720A
Other languages
Japanese (ja)
Inventor
Toshio Shibahara
敏夫 柴原
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.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery 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 Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP8099720A priority Critical patent/JPH09289015A/en
Publication of JPH09289015A publication Critical patent/JPH09289015A/en
Withdrawn legal-status Critical Current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

  • Battery Electrode And Active Subsutance (AREA)

Abstract

PROBLEM TO BE SOLVED: To manufacture an electrode plate in a short time aging process without deterioration in cycle life performance by filling paste prepared with the prescribed lead powder for a lead-acid battery in a grid, oxidizing lead, then conducting formation. SOLUTION: Lead powder whose surface is lead monoxide is heated under the existence of coke and/or carbon monoxide to reduce the surface of the lead monoxide into lead by the reaction of PbO+C→Pb+CO. Since coke or carbon monoxide directly react with lead monoxide in this reaction, the reaction starts from the surface of the lead monoxide, and reduced lead is selectively formed on the surface of the lead monoxide. Thereby, in a aging process, metallic lead can easily come in contact with oxygen and water, and the oxidation reaction of the metallic lead easily occur. As a result, time of the aging process is shortened, and since the metallic lead exists on the surface coming in contact with active material particles, bonding between active material particles is strengthened, and the cycle life is lengthened.

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、鉛蓄電池用極板の
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 method for manufacturing a lead storage battery electrode plate.

【0002】[0002]

【従来の技術】鉛蓄電池用極板の製造に用いる鉛粉とし
ては、使用する電池の用途により異なるが、ボールミル
法又はバートンポット法により製造され、鉛粉の粒子径
が0.1〜10μm程度、酸化度が70〜90%程度の物性値を
もつものが使用されている。
2. Description of the Related Art Lead powder used in the production of lead-acid battery electrode plates varies depending on the application of the battery used, but is produced by the ball mill method or the Burton pot method, and the lead powder has a particle diameter of about 0.1 to 10 μm and is oxidized. Those with physical properties of 70 to 90% are used.

【0003】この鉛粉は、鉛と一酸化鉛を主成分として
いるが、どちらの製造方法により製造した場合において
も必ず鉛の表面が酸化されて一酸化鉛となるため、鉛が
表面に露出することはなく、鉛の周囲に一酸化鉛が配置
された形となっている。
This lead powder is mainly composed of lead and lead monoxide. However, no matter which manufacturing method is used, the surface of lead is always oxidized to lead monoxide, so lead is exposed on the surface. There is nothing to do, and lead monoxide is arranged around lead.

【0004】[0004]

【発明が解決しようとする課題】このような従来の鉛蓄
電池用鉛粉では、充分なサイクル寿命性能を得るため
に、当然のことであるが金属鉛の酸化反応により活物質
粒子間の結合を形成する必要がある。
In order to obtain sufficient cycle life performance in such a conventional lead powder for a lead storage battery, it is natural that the bonding between the active material particles is caused by the oxidation reaction of metallic lead. Need to be formed.

【0005】このため、従来の鉛蓄電池用極板の製造方
法では、金属鉛を多く含有する酸化度70〜90%の鉛粉を
用いて、長時間の熟成工程を経なければならないという
問題点があった。
For this reason, in the conventional method of manufacturing the electrode plate for the lead storage battery, the lead powder containing a large amount of metallic lead and having an oxidation degree of 70 to 90% must be used for a long aging step. was there.

【0006】本発明の目的は、サイクル寿命性能を劣化
させることなく、短時間の熟成工程により鉛蓄電池用極
板を製造することができる鉛蓄電池用極板の製造方法を
提供することにある。
An object of the present invention is to provide a method for producing a lead storage battery electrode plate which can produce a lead storage battery electrode plate by a short aging step without deteriorating the cycle life performance.

【0007】本発明の他の目的は、還元される鉛の量を
コントロールすることができる鉛蓄電池用極板の製造方
法を提供することにある。
Another object of the present invention is to provide a method for manufacturing a lead-acid battery electrode plate which can control the amount of lead reduced.

【0008】[0008]

【課題を解決するための手段】本発明は、表面が一酸化
鉛となっている鉛粉からなる鉛蓄電池用鉛粉を用いた鉛
蓄電池用極板の製造方法を改良するものである。
DISCLOSURE OF THE INVENTION The present invention is to improve a method of manufacturing a lead storage battery electrode plate using lead powder for lead storage batteries, which surface is made of lead powder.

【0009】請求項1に記載の鉛蓄電池用極板の製造方
法においては、一酸化鉛の表面の少なくとも一部を鉛に
還元し、この一酸化鉛の表面を鉛に還元した鉛蓄電池用
鉛粉を用いて形成したペーストを格子体に充填し、次い
で熟成工程にて鉛を酸化させてから化成することを特徴
とする。
In the method of manufacturing a lead-acid battery electrode plate according to claim 1, at least a part of the surface of lead monoxide is reduced to lead, and the surface of the lead monoxide is reduced to lead. It is characterized in that the grid body is filled with a paste formed by using powder, and then lead is oxidized in a maturing step to perform chemical conversion.

【0010】請求項2に記載の鉛蓄電池用極板の製造方
法においては、一酸化鉛の表面の少なくとも一部を鉛に
還元する工程は、表面が一酸化鉛となっている鉛粉を、
コークス又は一酸化炭素のいずれか一方又は双方と共存
させて加熱することにより行うことを特徴とする。
In the method for manufacturing a lead-acid battery electrode plate according to claim 2, in the step of reducing at least a part of the surface of lead monoxide to lead, lead powder whose surface is lead monoxide is
It is characterized in that the heating is performed by coexisting with either or both of coke and carbon monoxide.

【0011】表面が一酸化鉛となっている鉛粉を、コー
クス又は一酸化炭素のいずれか一方又は双方と共存させ
て加熱すると、以下の反応により一酸化鉛の表面が鉛に
還元される。
When lead powder whose surface is lead monoxide is coexistent with either or both of coke and carbon monoxide and heated, the surface of lead monoxide is reduced to lead by the following reaction.

【0012】PbO+C→Pb+CO PbO+CO→Pb+CO2 この反応は、コークス又は一酸化炭素が一酸化鉛と直接
反応するため、一酸化鉛の表面から、反応が始まり、還
元された鉛は一酸化鉛の表面に選択的に形成される。こ
のような一酸化鉛を鉛に還元する工程では、共存する還
元手段の量を不足量とし制限することで、還元される鉛
の量をコントロールすることができる。
PbO + C → Pb + CO PbO + CO → Pb + CO 2 In this reaction, since coke or carbon monoxide directly reacts with lead monoxide, the reaction starts from the surface of lead monoxide, and the reduced lead is the surface of lead monoxide. Are selectively formed. In such a step of reducing lead monoxide to lead, the amount of lead to be reduced can be controlled by limiting the amount of coexisting reducing means to an insufficient amount.

【0013】このような工程で製造した鉛粉は、従来の
鉛粉が鉛の周囲に必ず一酸化鉛が存在する形であるのに
対して、逆に一酸化鉛の表面に鉛が存在する形となって
いる。このため、熟成工程において、金属鉛は酸素,水
と容易に接することができ、金属鉛の酸化反応が起こり
易い。その結果、熟成工程時間を短縮することができ
る。更に、粒子の接している表面に金属鉛が存在するた
め、活物質粒子間の結合が強固となり、サイクル寿命特
性が向上する。
In the lead powder produced by such a process, lead monoxide is always present around lead in the conventional lead powder, while lead is present on the surface of lead monoxide. It has a shape. For this reason, in the aging step, metallic lead can easily come into contact with oxygen and water, and the oxidation reaction of metallic lead easily occurs. As a result, the aging process time can be shortened. Furthermore, since metallic lead is present on the surfaces in contact with the particles, the bonds between the active material particles are strengthened and the cycle life characteristics are improved.

【0014】[0014]

【発明の実施の形態】次に、本発明に係る鉛蓄電池用極
板の製造方法における実施の形態の一例を説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Next, an example of an embodiment of the method for manufacturing a lead-acid battery electrode plate according to the present invention will be described.

【0015】常法のボールミル法により、従来の鉛粉と
して、平均粒子径1μm、比表面積約60,000cm2 /cm3
の物性を有する酸化度70%及び73%の鉛粉を作成した。
According to a conventional ball mill method, as a conventional lead powder, an average particle diameter is 1 μm and a specific surface area is about 60,000 cm 2 / cm 3.
A lead powder having the physical properties of 70% and 73% oxidation degree was prepared.

【0016】次に、本発明の鉛粉は、上記の酸化度73%
の鉛粉を原料とし、コークスと一酸化炭素を共存させ80
0 ℃に加熱し、鉛粉の酸化度が70%となるように還元処
理を施した。作成した鉛粉は、平均粒子径0.9 μm、比
表面積約65,000cm2 /cm3 の物性を有していた。
Next, the lead powder of the present invention has the above-mentioned oxidation degree of 73%.
Made from lead powder of coke and coke and carbon monoxide 80
It was heated to 0 ° C and subjected to a reduction treatment so that the degree of oxidation of lead powder would be 70%. The produced lead powder had the average particle diameter of 0.9 μm and the specific surface area of about 65,000 cm 2 / cm 3 .

【0017】次に、上記酸化度70%の従来の鉛粉と本発
明の鉛粉との計2種の鉛粉を用いて、常法に従い硫酸鉛
量10%、水分量11%の陽極ペーストをそれぞれ作成し
た。これらペーストを同一組成の鉛合金格子にそれぞれ
充填した。
Next, using a total of two types of lead powder, the conventional lead powder having an oxidation degree of 70% and the lead powder of the present invention, an anode paste having a lead sulfate content of 10% and a water content of 11% was prepared according to a conventional method. Created respectively. These pastes were filled in lead alloy grids having the same composition.

【0018】従来の鉛粉を用いたペーストを充填した鉛
合金格子を、常法の熟成工程条件と短縮熟成工程条件と
でそれぞれ熟成を行い未化成極板を作成した。
A conventional lead alloy grid filled with a paste containing lead powder was aged under the usual aging process conditions and shortening aging process conditions to prepare an unformed electrode plate.

【0019】本発明の鉛粉を用いたペーストを充填した
鉛合金格子を、常法の熟成工程条件と、短縮熟成工程条
件と、15時間短縮熟成工程条件とでそれぞれ熟成を行い
未化成極板を作成した。
The lead alloy grid filled with the paste using the lead powder of the present invention is aged under the usual aging process conditions, shortening aging process conditions, and 15-hour shortening aging process conditions, respectively, to form unformed electrode plates. It was created.

【0020】この場合、常法の熟成工程条件は、35℃、
98%R.H.雰囲気中に48時間放置である。一方、短縮熟成
工程条件は、35℃、10%R.H.雰囲気に24時間放置であ
る。
In this case, the usual aging process conditions are 35 ° C.
Leave for 48 hours in 98% RH atmosphere. On the other hand, the conditions for the shortening aging process are to leave it in an atmosphere of 35 ° C. and 10% RH for 24 hours.

【0021】次に、得られた5種の未化成極板を常法に
従って化成し、同一の陰極板と組み合わせて、液式の公
称容量28Ah の電池をそれぞれ作成した。
Next, the obtained five kinds of unformed electrode plates were formed by a conventional method and combined with the same cathode plate to prepare liquid type batteries having a nominal capacity of 28 Ah.

【0022】作成した各鉛蓄電池のJISに基くサイク
ル寿命試験の結果を図1に示す。この図1より明らかな
ように、常法の熟成工程条件において、本発明の鉛粉を
用いた電池(本発明品)は、ほぼ同じ物性を有する従来
の鉛粉を用いた電池(従来品)より長寿命である。更
に、短縮熟成工程条件で作成した電池では、本発明の鉛
粉を用いた電池が、常法の熟成工程条件で作成した電池
と同等の寿命性能を有しているのに対して、従来の鉛粉
を用いた電池では性能が劣化していることがわかる。
FIG. 1 shows the result of the cycle life test based on JIS of each of the prepared lead acid batteries. As is clear from FIG. 1, the battery using the lead powder of the present invention (the product of the present invention) is a battery using the conventional lead powder having substantially the same physical properties (conventional product) under the conditions of the usual aging process. It has a longer life. Further, in the battery prepared under the shortened aging process condition, the battery using the lead powder of the present invention has the same life performance as that of the battery prepared under the conventional aging process condition. It can be seen that the performance of the battery using lead powder has deteriorated.

【0023】また、図から明らかなように、従来の鉛粉
を用いて常法の熟成工程条件で作成した電池と寿命性能
を同じにするのであれば、本発明の鉛粉を用いればさら
に熟成時間を24時間から15時間に短縮することができ
る。
Further, as is clear from the figure, if the lead powder of the present invention is used and the life performance is the same as that of the battery prepared under the conventional aging process conditions using the conventional lead powder, further aging is performed. Time can be reduced from 24 hours to 15 hours.

【0024】なお、一酸化鉛の表面を鉛に還元する際に
は、コークスと一酸化炭素との双方を用いる方法以外
に、そのうちのいずれか一方だけを用いてもよい。
When reducing the surface of lead monoxide to lead, only one of coke and carbon monoxide may be used in addition to the method of using both coke and carbon monoxide.

【0025】[0025]

【発明の効果】請求項1に記載の鉛蓄電池用極板の製造
方法においては、一酸化鉛の表面の少なくとも一部が鉛
に還元されている鉛粉を用いるため、熟成工程において
金属鉛が酸素,水と容易に接することができ、このため
金属鉛の酸化反応が起こり易く、その結果、熟成工程時
間を短縮することができる。また、本発明の方法で製造
された鉛蓄電池用極板は、一酸化鉛の表面の少なくとも
一部が鉛に還元されているため、従来の鉛蓄電池用鉛粉
を用いた電池に比べ活物質粒子間の結合が強固となり、
このためサイクル寿命特性を向上させることができ、ま
た熟成工程を短縮しても従来と同等のサイクル寿命特性
もたせることができる利点がある。
In the method for producing a lead-acid battery electrode plate according to the first aspect of the present invention, since lead powder in which at least a part of the surface of lead monoxide is reduced to lead is used, metallic lead is removed in the aging step. Since it can easily come into contact with oxygen and water, the oxidation reaction of metallic lead easily occurs, and as a result, the aging process time can be shortened. Further, the lead-acid battery electrode plate produced by the method of the present invention, since at least a part of the surface of lead monoxide is reduced to lead, compared to a battery using a conventional lead-acid battery lead powder active material The bond between particles becomes strong,
Therefore, there is an advantage that the cycle life characteristics can be improved, and even if the aging step is shortened, the cycle life characteristics equivalent to the conventional one can be provided.

【0026】請求項2に記載の鉛蓄電池用極板の製造方
法においては、一酸化鉛の表面の少なくとも一部を鉛に
還元する工程を、表面が一酸化鉛となっている鉛粉を、
コークス又は一酸化炭素のいずれか一方又は双方と共存
させて加熱することにより行うので、共存する還元手段
の量を不足量とし制限することで、還元される鉛の量を
コントロールすることができる特長がある。
In the method for manufacturing a lead-acid battery electrode plate according to claim 2, the step of reducing at least a part of the surface of lead monoxide to lead is carried out by using lead powder whose surface is lead monoxide,
Since the heating is performed by coexisting with either or both of coke and carbon monoxide, the amount of lead to be reduced can be controlled by limiting the amount of coexisting reducing means to an insufficient amount. There is.

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

【図1】本発明の鉛蓄電池用鉛粉及び従来の鉛蓄電池用
鉛粉を用いて熟成条件を変えた場合のサイクル寿命特性
を示す比較図である。
FIG. 1 is a comparative diagram showing cycle life characteristics when aging conditions are changed using a lead powder for a lead storage battery of the present invention and a conventional lead powder for a lead storage battery.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 表面が一酸化鉛となっている鉛粉からな
る鉛蓄電池用鉛粉を用いた鉛蓄電池用極板の製造方法に
おいて、 前記一酸化鉛の表面の少なくとも一部を鉛に還元し、 この一酸化鉛の表面を鉛に還元した鉛蓄電池用鉛粉を用
いて形成したペーストを格子体に充填し、 次いで熟成工程にて鉛を酸化させてから化成することを
特徴とする鉛蓄電池用極板の製造方法。
1. A method for manufacturing an electrode plate for a lead storage battery using lead powder for a lead storage battery, which comprises lead powder having a surface made of lead monoxide, wherein at least a part of the surface of the lead monoxide is reduced to lead. Then, the paste formed by using the lead powder for lead-acid batteries, in which the surface of the lead monoxide has been reduced to lead, is filled in a grid, and then the lead is oxidized in the aging step before being formed. Manufacturing method of electrode plate for storage battery.
【請求項2】 前記一酸化鉛の表面の少なくとも一部を
鉛に還元する工程は、表面が一酸化鉛となっている鉛粉
を、コークス又は一酸化炭素のいずれか一方又は双方と
共存させて加熱することにより行うことを特徴とする請
求項1に記載の鉛蓄電池用極板の製造方法。
2. The step of reducing at least a part of the surface of the lead monoxide to lead, the lead powder having a surface of lead monoxide is allowed to coexist with either or both of coke and carbon monoxide. The method for producing a lead-acid battery electrode plate according to claim 1, wherein the method is performed by heating.
JP8099720A 1996-04-22 1996-04-22 Manufacture of electrode plate for lead-acid battery Withdrawn JPH09289015A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8099720A JPH09289015A (en) 1996-04-22 1996-04-22 Manufacture of electrode plate for lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8099720A JPH09289015A (en) 1996-04-22 1996-04-22 Manufacture of electrode plate for lead-acid battery

Publications (1)

Publication Number Publication Date
JPH09289015A true JPH09289015A (en) 1997-11-04

Family

ID=14254918

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8099720A Withdrawn JPH09289015A (en) 1996-04-22 1996-04-22 Manufacture of electrode plate for lead-acid battery

Country Status (1)

Country Link
JP (1) JPH09289015A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114678513A (en) * 2022-03-26 2022-06-28 天能集团(河南)能源科技有限公司 Negative plate alloy and preparation process thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114678513A (en) * 2022-03-26 2022-06-28 天能集团(河南)能源科技有限公司 Negative plate alloy and preparation process thereof
CN114678513B (en) * 2022-03-26 2024-02-09 天能集团(河南)能源科技有限公司 Negative plate alloy and configuration process thereof

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Effective date: 20030701