JPH09167619A - Plate for lead-acid battery and its manufacture - Google Patents

Plate for lead-acid battery and its manufacture

Info

Publication number
JPH09167619A
JPH09167619A JP7328606A JP32860695A JPH09167619A JP H09167619 A JPH09167619 A JP H09167619A JP 7328606 A JP7328606 A JP 7328606A JP 32860695 A JP32860695 A JP 32860695A JP H09167619 A JPH09167619 A JP H09167619A
Authority
JP
Japan
Prior art keywords
lead
polypyrrole
electrode plate
plate
powder
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.)
Granted
Application number
JP7328606A
Other languages
Japanese (ja)
Other versions
JP3284860B2 (en
Inventor
Takeshi Hatanaka
剛 畑中
Katsuhiro Takahashi
勝弘 高橋
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP32860695A priority Critical patent/JP3284860B2/en
Publication of JPH09167619A publication Critical patent/JPH09167619A/en
Application granted granted Critical
Publication of JP3284860B2 publication Critical patent/JP3284860B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

Abstract

PROBLEM TO BE SOLVED: To abundantly supply electrolyte to an active material without changing a service life characteristic by mixing podwer-like porous polypyrrole, filling paste by kneading this by water and sulfuric acid in an aggregate, and forming it as a plate. SOLUTION: An aqueous solution by dissolving a prescribed quantity of persulfuric acid ammonium in water is put in a vessel, and it is agitated, and pyrrole being a monomer is dripped in this aqueous solution. The dripped pyrrole is oxidized and polymerized by the persulfuric acid ammonium, and produces powder. Polypyrrole powder is also washed by water, and the remaining persulfuric acid ammonium is removed, and hot blast drying or vacuum drying is performed, and moisture is removed to make a plate. Then, since a part of an active material is substituted with powder polypyrrole 1 and forms a porous structure of high density, active material particles 2 are firmly bound to each other. Therefore, the volume occupied by a pore 3 and a void part increases, and a holding quantity of electrolyte can be increased. The plate is made by filling paste by kneading resin in a solvent in a current collecting body lattice 4.

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】本発明は鉛蓄電池の改良に関
するもので、特に高率放電特性に優れた長寿命の鉛電池
を構成できる極板を提供するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a lead storage battery, and in particular to an electrode plate which can form a long life lead battery excellent in high rate discharge characteristics.

【0002】[0002]

【従来の技術】鉛蓄電池は二次電池として比較的安価で
安定な性能を有しているため一般に普及している。また
近年ではポータブル機器や電動車の電源に用いられるサ
イクル使用の移動用電源、コンピュータなどのバックア
ップに用いる据え置き用電源としても普及してきた。
2. Description of the Related Art Lead acid batteries are popular as secondary batteries because they are relatively inexpensive and have stable performance. In recent years, it has also become popular as a mobile power supply for cycle use, which is used as a power supply for portable devices and electric vehicles, and a stationary power supply used for backup of computers and the like.

【0003】近年、自動車の低公害化対策として電気自
動車の開発が脚光を浴びている、またポータブル機器の
コードレス化も進んでおり、これにつれて電源として価
格の安い鉛蓄電池の高性能化への要望が高まってきてい
る。これらの鉛蓄電池の高性能化にはとりわけ高率放電
特性の向上が課題となっている。
In recent years, the development of electric vehicles has been in the limelight as a measure for reducing the pollution of automobiles, and the cordless portable devices have been developed, and along with this, there has been a demand for high performance of lead acid batteries which are inexpensive as a power source. Is increasing. In order to improve the performance of these lead-acid batteries, improvement of high-rate discharge characteristics has been a problem.

【0004】高率放電特性は電解液の活物質への供給に
支配されるところが大きい。鉛蓄電池は正極に二酸化鉛
(PbO2),負極に鉛(Pb)、電解液に硫酸(H2
4)水溶液を用いており、その電池放電反応は以下に
示す通りである。 正極:PbO2+2H++H2SO4+2e- → PbS
4+2H2O 負極:Pb+SO4 2-→ PbSO4+2e- 上記の反応式から明らかなように、放電反応により、正
極、負極とも活物質が硫酸鉛(PbSO4)に変化して
いく。鉛、二酸化鉛が硫酸鉛に変化するとその体積は約
2倍に増大する。そのため放電反応が進むにつれて極板
中の空孔が析出した硫酸鉛によって塞がれ、硫酸イオン
の拡散能力が劣化してくる。このようなことが、電池電
圧の低下ならびに活物質利用率の低下につながってい
る。また、この硫酸鉛は充電時には正極で二酸化鉛に、
負極では鉛に変化するが、極板内への電解液供給能力が
乏しい場合には、この反応が円滑に進まず充電効率が低
下する。特に、高電流密度での充放電ほどこの影響が大
きくなる。
The high rate discharge characteristics are largely controlled by the supply of the electrolytic solution to the active material. Lead-acid batteries have lead dioxide (PbO 2 ) for the positive electrode, lead (Pb) for the negative electrode, and sulfuric acid (H 2 S) for the electrolyte.
O 4 ) aqueous solution is used, and the battery discharge reaction is as shown below. Positive electrode: PbO 2 + 2H + + H 2 SO 4 + 2e → PbS
O 4 + 2H 2 O negative electrode: Pb + SO 4 2- → PbSO 4 + 2e As is clear from the above reaction formula, the active material of both the positive electrode and the negative electrode changes to lead sulfate (PbSO 4 ) due to the discharge reaction. When lead and lead dioxide are converted to lead sulfate, the volume increases about twice. Therefore, as the discharge reaction progresses, pores in the electrode plate are blocked by the precipitated lead sulfate, and the ability to diffuse sulfate ions deteriorates. This leads to a decrease in battery voltage and a decrease in active material utilization rate. Also, this lead sulfate becomes lead dioxide at the positive electrode during charging,
Although it changes to lead at the negative electrode, if the electrolyte supply capacity into the electrode plate is poor, this reaction does not proceed smoothly and charging efficiency decreases. In particular, the effect becomes larger as the charge and discharge at a higher current density occur.

【0005】このように、極板内への硫酸供給能力の劣
化が鉛蓄電池の高率放電特性の向上や長寿命化への大き
な課題となっている。
As described above, the deterioration of the supply capacity of sulfuric acid into the electrode plate has become a major issue for improving the high rate discharge characteristics and extending the life of the lead storage battery.

【0006】これらの課題を解決するための方策とし
て、従来は活物質の充填密度を低下させて、極板内に電
解液を保持あるいは拡散させる空隙を多く形成するとい
う手法が提案されている。
As a measure for solving these problems, conventionally, there has been proposed a method in which the packing density of the active material is lowered to form a large number of voids for holding or diffusing the electrolytic solution in the electrode plate.

【0007】[0007]

【発明が解決しようとする課題】上記の充填密度を低下
させる手法は極板内の電解液量を増加させることができ
るので高率放電特性が向上する。しかし、極板中に空隙
が形成され活物質粒子間の結合力が低下して極板の機械
的強度が弱くなり、充放電をくり返すと活物質の脱落が
激しく、寿命特性が大きく低下するという欠点があっ
た。本発明はこのような問題を解決し、寿命特性に悪影
響を与えることなく電解液を豊富に活物質に供給を行え
る極板を構成し、高率放電特性に優れた長寿命の鉛蓄電
池を提供することを目的とする。
The above-mentioned method of reducing the packing density can increase the amount of the electrolytic solution in the electrode plate, so that the high rate discharge characteristics are improved. However, the voids are formed in the electrode plate, the bonding force between the active material particles is reduced, and the mechanical strength of the electrode plate is weakened. When the charge and discharge are repeated, the active material falls off sharply and the life characteristics are greatly reduced. There was a drawback. The present invention solves such problems, and provides a long-life lead-acid battery excellent in high rate discharge characteristics by configuring an electrode plate that can supply an electrolyte in abundance to an active material without adversely affecting life characteristics. The purpose is to do.

【0008】[0008]

【課題を解決するための手段】本発明の鉛蓄電池用極板
は、極板中に電解液の保持材として粉末状の多孔質ポリ
ピロールを含有させることを特徴とするものである。こ
の極板を用いることにより、前記の目的が達成され、高
率放電特性に優れた長寿命の鉛蓄電池を提供できる。
The electrode plate for a lead storage battery of the present invention is characterized in that the electrode plate contains a powdery porous polypyrrole as a holding material for an electrolytic solution. By using this electrode plate, the above-mentioned object can be achieved, and a long-life lead-acid battery excellent in high rate discharge characteristics can be provided.

【0009】[0009]

【発明の実施の形態】ポリピロールは耐酸性に優れ、導
電性高分子としても知られている材料であり、特開平6
−76821号に見られるようにフィルム状に加工し集
電体の被覆材として用いることが提案されている。
BEST MODE FOR CARRYING OUT THE INVENTION Polypyrrole is a material which has excellent acid resistance and is also known as a conductive polymer.
It has been proposed to process the material into a film and use it as a coating material for a current collector, as seen in No. -76821.

【0010】一方、本発明は粉末状の多孔質ポリピロー
ルを極板中に含有させることを特徴とするものであり、
さらにこれに適した多孔質ポリピロール粉末として、モ
ノマーであるピロールを化学酸化剤溶液中で酸化・重合
させて得たものを、必要に応じて粉砕によって任意の粒
径に調整して使用するものである。本発明はこの粉末状
ポリピロールが吸液性に優れ、鉛電池の電解液保持材と
してきわめて適切であることを見出し、これを極板中に
含有させることにより、電解液を多量に保持でき、しか
も機械的強度の優れた極板を構成することを可能にした
ものである。
On the other hand, the present invention is characterized in that a powdery porous polypyrrole is contained in the electrode plate.
Further, as a porous polypyrrole powder suitable for this, one obtained by oxidizing and polymerizing a pyrrole as a monomer in a chemical oxidant solution and adjusting the particle size to an arbitrary particle size by pulverization as needed, is used. is there. The present invention has found that this powdery polypyrrole is excellent in liquid absorbability and is extremely suitable as an electrolyte holding material for lead batteries, and by containing it in an electrode plate, a large amount of electrolyte can be held, and This makes it possible to construct an electrode plate having excellent mechanical strength.

【0011】本発明による粉末状ポリピロールを適量含
んだ極板には、粒子相互間の接合によって形成される多
孔構造の空孔によって保持される電解液の他に、粉末状
ポリピロール自身の多孔構造の空孔に保持される電解液
が加わり、極板中に多量の電解液が含有されることにな
る。しかも粉末状ポリピロールが極板の高密度多孔構造
の形成に寄与しているため、極板の強度が増し、単に充
填密度を下げただけの従来極板に見られるような活物質
の脱落による放電性能の劣化やサイクル寿命の低下とい
った問題も回避できる。
The electrode plate containing an appropriate amount of the powdery polypyrrole according to the present invention has the porous structure of the powdery polypyrrole itself in addition to the electrolytic solution held by the pores of the porous structure formed by the bonding between the particles. The electrolytic solution held in the pores is added, so that the electrode plate contains a large amount of electrolytic solution. Moreover, since the powdery polypyrrole contributes to the formation of the high-density porous structure of the electrode plate, the electrode plate strength is increased, and the discharge due to the active material falling off, which is the case with the conventional electrode plate, which merely reduces the packing density. Problems such as performance deterioration and cycle life reduction can also be avoided.

【0012】[0012]

【実施例】以下、本発明の一実施例を図面を用いて説明
する。
An embodiment of the present invention will be described below with reference to the drawings.

【0013】本発明の実施例に用いた極板の断面図を図
1に、また図2と図3には従来例1と従来例2の極板の
断面図をそれぞれ示す。ここで1はポリピロール粉末粒
子、2は活物質、3は粒子間空孔、4は集電体格子、5
は空隙部である。本発明では図1に示す通り活物質の一
部が粉末ポリピロール1に置き換わり高密度の多孔構造
を形成することにより、活物質粒子間が強固に結着して
いる。
FIG. 1 is a sectional view of an electrode plate used in an embodiment of the present invention, and FIGS. 2 and 3 are sectional views of electrode plates of Conventional Example 1 and Conventional Example 2, respectively. Here, 1 is a polypyrrole powder particle, 2 is an active material, 3 is an interparticle void, 4 is a current collector lattice, 5
Is a void. In the present invention, as shown in FIG. 1, a part of the active material is replaced with the powdered polypyrrole 1 to form a high density porous structure, so that the active material particles are firmly bound to each other.

【0014】ここで、多孔質の粉末状ポリピロールの製
造法について示す。まず水1000g に対して過硫酸アンモ
ニウム20g 〜50g を溶かした水溶液を容器に入れ撹拌し
た。この水溶液にモノマーであるピロール15cc〜30ccを
約1分から2分かけて滴下した。滴下されたピロールは
過硫酸アンモニウムによって酸化・重合され、粉末状の
ポリピロールが生成する。このポリピロール粉末を水洗
し、残留している過硫酸アンモニウムを取り除き、100
〜130 ℃で1時間熱風乾燥あるいは真空乾燥し、水分を
除いて極板の作成に用いた。
Here, a method for producing a porous powdery polypyrrole will be described. First, an aqueous solution prepared by dissolving 20 g to 50 g of ammonium persulfate in 1000 g of water was placed in a container and stirred. Pyrrole (15 cc to 30 cc) as a monomer was added dropwise to this aqueous solution over about 1 to 2 minutes. The dropped pyrrole is oxidized and polymerized by ammonium persulfate to produce powdery polypyrrole. This polypyrrole powder is washed with water to remove residual ammonium persulfate,
It was dried with hot air or vacuum at 1 to 130 ° C for 1 hour to remove water, and then used to prepare an electrode plate.

【0015】尚、過硫酸アンモニウムの代わりに塩化第
2鉄などの酸化剤を使っても同様の方法で多孔質の粉末
状ポリピロールが得られる。その中でも、過硫酸アンモ
ニウムやそれに硫酸成分を加えて酸化・重合すると、硫
酸イオンがポリピロールにドーピングされるので、電解
液成分が取り込まれた多孔質の粉末状ポリピロールが得
られるので、この方法で得られらた材料を本発明の実施
に用いるのがが好ましい。また、ポリピロールは電解酸
化によっても形成されるが、この場合は生成効率がガス
の発生にともない低下する以外に、多孔度の調整が困難
である。その点、本実施例のような化学的酸化法ではピ
ロールの滴下速度や温度、酸化剤の濃度などによって容
易にポリピロール粉末の多孔度を調整できる利点があ
る。
A porous powdery polypyrrole can be obtained in the same manner by using an oxidizing agent such as ferric chloride instead of ammonium persulfate. Among them, when ammonium persulfate or a sulfuric acid component is added and oxidized and polymerized, the sulfate ion is doped into the polypyrrole, so that a porous powdery polypyrrole in which the electrolytic solution component is incorporated can be obtained. Such materials are preferably used in the practice of the present invention. Polypyrrole is also formed by electrolytic oxidation, but in this case, it is difficult to adjust the porosity in addition to the decrease in production efficiency with the generation of gas. In this respect, the chemical oxidation method as in this embodiment has an advantage that the porosity of the polypyrrole powder can be easily adjusted by the dropping rate and temperature of the pyrrole, the concentration of the oxidizing agent, and the like.

【0016】次にペーストの練合工程であるが、本実施
例では重量比で金属鉛25%、一酸化鉛75%の鉛粉(酸化
度75%の鉛粉)に対して、正極用には重量比2 %の合成
樹脂のカット繊維、負極用には2 %の硫酸バリウムと1
%の炭素粉末と0.5 %のリグニンを添加して混合材を調
製した。この混合材中に鉛粉中の鉛成分の重量に対して
1.0%の多孔質の粉末ポリピロールを添加し均一に混
合し、この混合物に水と希硫酸を加えて混練しペースト
とした。
Next, in the paste kneading step, in the present embodiment, a lead powder containing 25% by weight metallic lead and 75% lead monoxide (lead powder having an oxidation degree of 75%) was used for the positive electrode. Is 2% by weight of synthetic resin cut fiber, 2% barium sulfate and 1% for negative electrode
% Carbon powder and 0.5% lignin were added to prepare a mixed material. Porous powder polypyrrole of 1.0% based on the weight of the lead component in the lead powder was added to this mixed material and uniformly mixed, and water and dilute sulfuric acid were added to this mixture and kneaded to form a paste.

【0017】ちなみに、混合材中には上記のほか鉛丹
や、硫酸鉛、塩基性硫酸鉛、二酸化鉛粉末などの鉛化合
物などの添加物が添加される場合も多いが、本発明はこ
のような場合にも適用できる。
By the way, in addition to the above, lead oxide, lead sulfate and other lead compounds such as lead dioxide powder are often added to the mixed material in many cases. It can be applied in any case.

【0018】次に、上記のペーストを鉛−カルシウム系
合金製の鋳造格子に充填し、常法に従い高温高湿中で熟
成し、次いで化成を行って正極板および負極板を作成し
た。これらの工程中で混合材中の鉛成分を含む鉛粉など
の原料は、硫酸との練合および熟成によって硫酸鉛と塩
基性炭酸鉛などに変化し、これらが化成によって、正極
板の場合は酸化されて二酸化鉛に、負極板の場合は還元
されて鉛に変化することによって、各々、正負極の活物
質となる。
Next, the above-mentioned paste was filled in a casting grid made of a lead-calcium alloy, aged in a high temperature and high humidity according to a conventional method, and then subjected to chemical conversion to prepare a positive electrode plate and a negative electrode plate. In these steps, raw materials such as lead powder containing lead components in the mixed material are converted into lead sulfate and basic lead carbonate by kneading with sulfuric acid and aging, and in the case of positive electrode plate due to chemical conversion. By being oxidized and converted to lead dioxide, and in the case of the negative electrode plate, reduced and converted to lead, they become positive and negative electrode active materials, respectively.

【0019】上記の正極板2枚と負極板3枚を用い、そ
の間にガラス繊維からなるマット状セパレータを介在さ
せて組合せ、電解液として希硫酸を含浸させて容量2A
h、2Vの電池を作成した。ちなみに、本実施例では集
電体に鋳造格子を用いたが、エキスパンド格子を用いて
も本発明を実施できる。
The above two positive electrode plates and three negative electrode plates were used, and a mat-like separator made of glass fiber was interposed between them to combine them, and dilute sulfuric acid was impregnated as an electrolytic solution to obtain a capacity of 2A.
A 2 h battery was prepared. Incidentally, although the casting grid is used as the current collector in this embodiment, the present invention can be carried out by using the expanded grid.

【0020】比較のために、粉末ポリピロールを含まな
いこと以外は上記の極板と全く同じ条件で試作した電池
(従来例1)と粉末ポリピロールを含まずペースト調整
時に加える水の量を多くし活物質密度を低下させた電池
(従来例2)を試作した。
For comparison, a battery (conventional example 1) manufactured under the same conditions as those of the above-mentioned electrode plates except that the powdered polypyrrole was not included, and the powdered polypyrrole was not included, and the amount of water added at the time of preparing the paste was increased. A battery (Conventional Example 2) having a reduced material density was manufactured as a prototype.

【0021】本発明の電池と従来例1、2の電池を0.
1C〜3.0Cの定電流で放電した場合の放電容量を
(表1)に示す。
The battery of the present invention and the batteries of Conventional Examples 1 and 2 were compared with each other.
The discharge capacity when discharged at a constant current of 1 C to 3.0 C is shown in (Table 1).

【0022】[0022]

【表1】 [Table 1]

【0023】また各電池の1C放電(終止電圧1.3
V)、1C充電(放電容量の150%充電)での充放電
サイクルの寿命性能を(表2)に示す。なお、サイクル
寿命数は初期放電容量の50%に低下するまでのサイク
ル数とした。なお電気量は充填されたぺーストに含まれ
る鉛原子のモル数を計算し、それらが全て2電子反応を
行ったと仮定した場合の理論容量を用いた。
Further, 1C discharge of each battery (final voltage 1.3
V) The life performance of the charge / discharge cycle at 1 C charge (150% charge of the discharge capacity) is shown in (Table 2). The cycle life number was the number of cycles until the initial discharge capacity was reduced to 50%. The amount of electricity was calculated by calculating the number of moles of lead atoms contained in the filled paste, and using the theoretical capacity when it is assumed that they all carry out a two-electron reaction.

【0024】[0024]

【表2】 [Table 2]

【0025】(表1)から明らかなように、本発明によ
る極板を用いた電池は従来例2と同様に、従来例1より
高率放電特性が著しく優れている。一方、(表2)のサ
イクル特性に関しては、本発明による極板を用いた電池
が従来例1と同様に従来例2よりもサイクル寿命数が大
きい。これらのことから、本発明を適用することによ
り、優れた高率放電特性と長寿命を兼ね備えた電池が構
成できることが実証された。上記の結果が得られた理由
は以下のように説明出来る。図1の本発明による極板に
おいては、粉末ポリピロール内部の空孔に電解液が保持
され、しかもポリピロール自身にドーピングされた硫酸
イオンを含んでいる。そのため、極板の粒子間空孔にの
み電解液を含む図2に示すような従来例1の高密度に充
填された極板に比べて極板中に多くの電解液が含有され
ており、高率放電でも反応が円滑に進行する。また、図
3の従来例2の低密度充填の極板では活物質が少なくな
り、その分だけ空孔3と空隙部の占める容積が多くな
り、電解液の保持量は従来例1に比べ多くなるが、多孔
構造の強度が低下し活物質の脱落が発生、サイクル寿命
が劣化する。それに比べ本発明品では、粉末ポリピロー
ルが高密度多孔構造の形成に寄与しているので粒子間の
結合力が高くなり、サイクル寿命の劣化が効果的に抑制
される。
As is clear from (Table 1), the battery using the electrode plate according to the present invention is significantly superior to the conventional example 1 in the high rate discharge characteristics as in the conventional example 2. On the other hand, regarding the cycle characteristics of (Table 2), the battery using the electrode plate of the present invention has a larger cycle life number than that of Conventional Example 2 as in Conventional Example 1. From these facts, it was demonstrated that by applying the present invention, a battery having both excellent high-rate discharge characteristics and a long life can be configured. The reason why the above results are obtained can be explained as follows. In the electrode plate according to the present invention shown in FIG. 1, the electrolyte solution is held in the pores inside the powdery polypyrrole, and the polypyrrole itself contains the doped sulfate ions. Therefore, compared with the electrode plate filled with high density of Conventional Example 1 as shown in FIG. 2 in which only the interparticle pores of the electrode plate contain the electrolyte solution, the electrode plate contains more electrolyte solution, The reaction proceeds smoothly even at high rate discharge. In addition, in the low-density packed electrode plate of Conventional Example 2 in FIG. 3, the active material is reduced, and the volume occupied by the pores 3 and voids is increased accordingly, and the amount of electrolyte retained is greater than in Conventional Example 1. However, the strength of the porous structure decreases, the active material falls off, and the cycle life deteriorates. On the other hand, in the product of the present invention, since the powdered polypyrrole contributes to the formation of the high-density porous structure, the bonding force between particles is increased, and the deterioration of the cycle life is effectively suppressed.

【0026】次に粉末ポリピロールの添加量について
は、上記実施例と同様の方法に従い粉末ポリピロールの
添加量を変えて正極板と負極板を試作して検討した。極
板の理論容量はそれぞれ1Ah、0.8Ahとし、粉末
ポリピロールの添加量はそれぞれ混合材中の鉛成分に対
して重量比で3%、2%、1%、0.3%、0.1%とした。
Next, the amount of powdered polypyrrole to be added was examined by making a positive electrode plate and a negative electrode plate by changing the amount of powdered polypyrrole added according to the same method as in the above-mentioned embodiment. The theoretical capacity of the electrode plate was 1 Ah and 0.8 Ah, respectively, and the amount of the powdered polypyrrole added was 3%, 2%, 1%, 0.3% and 0.1% by weight relative to the lead component in the mixed material.

【0027】これらの極板を純鉛板を対極として電解液
を大過剰に含む系で1Cの定電流放電を行い、参照極
(HgSO4/Hg)を用い初期電圧に対して0.2V
分極するまでの放電容量を測定した。正極の放電結果を
図4に示す。なお比較として粉末ポリピロールを含まな
い極板の放電性能も合わせて示す。
A constant current discharge of 1 C was carried out in a system containing a large amount of an electrolyte solution using these electrode plates with a pure lead plate as a counter electrode, and a reference electrode (HgSO 4 / Hg) was used to obtain 0.2 V with respect to the initial voltage.
The discharge capacity until polarization was measured. The result of discharging the positive electrode is shown in FIG. For comparison, the discharge performance of an electrode plate containing no powdered polypyrrole is also shown.

【0028】図4に示す通り、粉末ポリピロールを0.1%
以上添加することで放電容量の向上が見られるが、添加
量が混合材中の鉛成分に対して重量比で2%を越える当
たりからその効果が薄れ、3%では従来品に比べ優位性
が見られない。この結果から粉末ポリピロールの添加量
は混合材中の鉛成分に対して重量比で0.1%〜2%の
範囲が好ましい。負極についても同様の実験を行ったが
正極の場合と同様な結果が得られ、添加量は混合材中の
鉛成分に対して重量比で0.1%〜2%の範囲が適切で
あることが明らかになった。
As shown in FIG. 4, 0.1% of powdered polypyrrole was added.
Although the addition of the above makes it possible to improve the discharge capacity, the effect becomes weaker when the added amount exceeds 2% by weight relative to the lead component in the mixed material, and the effect becomes weaker at 3% than the conventional product. can not see. From this result, the amount of powdered polypyrrole added is preferably in the range of 0.1% to 2% by weight with respect to the lead component in the mixed material. The same experiment was performed for the negative electrode, but the same results as for the positive electrode were obtained, and it is appropriate that the addition amount is in the range of 0.1% to 2% by weight with respect to the lead component in the mixed material. Became clear.

【0029】さらに、鉛粉を主体とする混合材に、混合
材中の鉛成分の重量に対して1%の多孔性ポリピロール
粉末を混合し、これを、結着剤としてのポリフッ化ビニ
リデンを溶媒としてのN−メチルピロリドンに溶解させ
た液で練合したペーストを用い、上記の実施例と同様に
電池を作成した。この電池の1C以上の高率放電での放
電容量は多孔性ポリピロール粉末を添加しない電池に比
べ、10〜15%増大し、サイクル寿命数も250サイ
クルが得られた。このことから、有機高分子系樹脂を結
着剤として用い、これを溶媒に溶解させた液で混合材を
練合したペーストを用いて極板を構成する場合にも、本
発明を適用することが効果的であることが確認された。
Further, 1% of porous polypyrrole powder based on the weight of the lead component in the mixed material is mixed with a mixed material mainly containing lead powder, and this is mixed with polyvinylidene fluoride as a binder. Using the paste kneaded with the liquid dissolved in N-methylpyrrolidone as described above, a battery was prepared in the same manner as in the above example. The discharge capacity at a high rate discharge of 1 C or more of this battery was increased by 10 to 15% as compared with the battery in which the porous polypyrrole powder was not added, and the cycle life number was 250 cycles. From this, the present invention can be applied to the case where an organic polymer resin is used as a binder, and the electrode plate is formed by using a paste prepared by kneading a mixed material with a liquid obtained by dissolving the organic polymer resin in a solvent. Was confirmed to be effective.

【0030】[0030]

【発明の効果】以上のように鉛蓄電池の極板中に、多孔
質の粉末ポリピロールを添加することにより、極板中に
多量の電解液を保持させることができ、同時に極板強度
を増大できるので、この極板を用いることにより優れた
高率放電特性とサイクル寿命を兼ね備えた鉛蓄電池用を
得ることができる。
As described above, by adding porous powdery polypyrrole to the electrode plate of the lead storage battery, a large amount of electrolytic solution can be retained in the electrode plate, and at the same time, the electrode plate strength can be increased. Therefore, by using this electrode plate, it is possible to obtain a lead-acid battery having excellent high rate discharge characteristics and cycle life.

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

【図1】本発明による鉛蓄電池極板の断面図FIG. 1 is a sectional view of a lead-acid battery electrode plate according to the present invention.

【図2】従来の高密度充填極板の断面図FIG. 2 is a cross-sectional view of a conventional high-density packed electrode plate.

【図3】従来の低密度充填極板の断面図FIG. 3 is a cross-sectional view of a conventional low-density packed electrode plate.

【図4】粉末ポリピロールの添加量と正極放電特性の関
係図
FIG. 4 is a diagram showing the relationship between the amount of powdered polypyrrole added and the positive electrode discharge characteristics.

【符号の説明】[Explanation of symbols]

1 粉末ポリピロール 2 活物質粒子 3 粒子間空孔 4 集電体格子 5 空隙部 1 powdered polypyrrole 2 active material particles 3 interparticle voids 4 current collector lattice 5 voids

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】活物質が鉛、或いは二酸化鉛である鉛蓄電
池用極板であって、粉末状で多孔質のポリピロールを含
有することを特徴とする鉛蓄電池用極板。
1. An electrode plate for a lead storage battery, wherein the active material is lead or lead dioxide, which contains a powdery and porous polypyrrole.
【請求項2】鉛粉を主体とする混合材に、粉末状で多孔
質のポリピロールを混合し、これらを水および硫酸で練
合したぺーストを鉛合金製の集電体に充填し、熟成工
程、化成工程を経て極板とする鉛蓄電池用極板の製造
法。
2. A mixed material mainly composed of lead powder is mixed with powdery and porous polypyrrole, and the mixture is kneaded with water and sulfuric acid to fill a current collector made of lead alloy with aging. A method of manufacturing an electrode plate for a lead storage battery, which is made into an electrode plate through a process and a chemical conversion process.
【請求項3】鉛粉を主体とする混合材に、粉末状で多孔
質のポリピロールを混合し、これらを結着材としての有
機高分子系の樹脂を溶媒に溶解させた液で練合したぺー
ストを鉛合金製の集電体に塗着し、乾燥、化成工程を経
て極板とする鉛蓄電池用極板の製造法。
3. A powdery and porous polypyrrole is mixed with a lead powder-based mixture, and these are kneaded with a solution prepared by dissolving an organic polymer resin as a binder in a solvent. A method for manufacturing an electrode plate for a lead storage battery in which the paste is applied to a lead alloy current collector, dried, and then subjected to a chemical conversion process to form an electrode plate.
【請求項4】化学的酸化剤を含む溶液とピロールを混合
することによって生成したポリピロールを含有した請求
項1に記載の鉛蓄電池用極板。
4. The lead plate for a lead storage battery according to claim 1, which contains polypyrrole produced by mixing pyrrole with a solution containing a chemical oxidant.
【請求項5】化学的酸化剤が過硫酸アンモニウムである
請求項4に記載の鉛蓄電池用極板。
5. The lead plate for a lead storage battery according to claim 4, wherein the chemical oxidant is ammonium persulfate.
JP32860695A 1995-12-18 1995-12-18 Electrode for lead-acid battery and its manufacturing method Expired - Fee Related JP3284860B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32860695A JP3284860B2 (en) 1995-12-18 1995-12-18 Electrode for lead-acid battery and its manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32860695A JP3284860B2 (en) 1995-12-18 1995-12-18 Electrode for lead-acid battery and its manufacturing method

Publications (2)

Publication Number Publication Date
JPH09167619A true JPH09167619A (en) 1997-06-24
JP3284860B2 JP3284860B2 (en) 2002-05-20

Family

ID=18212157

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32860695A Expired - Fee Related JP3284860B2 (en) 1995-12-18 1995-12-18 Electrode for lead-acid battery and its manufacturing method

Country Status (1)

Country Link
JP (1) JP3284860B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2778270A1 (en) * 1998-04-30 1999-11-05 Centre Nat Rech Scient LEAD ACCUMULATOR OF IMPROVED PERFORMANCE
CN114477174A (en) * 2020-11-12 2022-05-13 中国科学院大连化学物理研究所 Composite carbon material, preparation thereof and application of composite carbon material in lead-carbon battery

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2778270A1 (en) * 1998-04-30 1999-11-05 Centre Nat Rech Scient LEAD ACCUMULATOR OF IMPROVED PERFORMANCE
WO1999057782A1 (en) * 1998-04-30 1999-11-11 Centre National De La Recherche Scientifique Lead battery with improved performance
US6458489B1 (en) 1998-04-30 2002-10-01 Centre National De La Recherche Scientifique Lead acid battery with improved performance
CN114477174A (en) * 2020-11-12 2022-05-13 中国科学院大连化学物理研究所 Composite carbon material, preparation thereof and application of composite carbon material in lead-carbon battery

Also Published As

Publication number Publication date
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