JPH10270029A - Active material for lead-acid battery and lead-acid battery using the same - Google Patents

Active material for lead-acid battery and lead-acid battery using the same

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Publication number
JPH10270029A
JPH10270029A JP9074048A JP7404897A JPH10270029A JP H10270029 A JPH10270029 A JP H10270029A JP 9074048 A JP9074048 A JP 9074048A JP 7404897 A JP7404897 A JP 7404897A JP H10270029 A JPH10270029 A JP H10270029A
Authority
JP
Japan
Prior art keywords
lead
active material
metal
pbo
particles
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
JP9074048A
Other languages
Japanese (ja)
Other versions
JP3646462B2 (en
Inventor
Toshio Shibahara
敏夫 柴原
Ichiro Mukoya
一郎 向谷
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 JP07404897A priority Critical patent/JP3646462B2/en
Publication of JPH10270029A publication Critical patent/JPH10270029A/en
Application granted granted Critical
Publication of JP3646462B2 publication Critical patent/JP3646462B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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

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  • Secondary Cells (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

PROBLEM TO BE SOLVED: To improve the cycle service life without damaging the charging efficiency by forming a surface layer of Pb3 O4 and forming a core layer of metal Pb. SOLUTION: A raw material of an active material is formed by using lead powder subject to a ball mill and with the degree of oxidation 20-40%, and baking the powder for 4 hours at a temperature of 200-300 deg.C (lower than the melting point of lead). In the main process, the surface is oxidized to have PbO mainly with metal Pb remained in a core layer of the particle of raw material of active material without fusing the particle with the metal Pb. Then, a baking process is applied for 20 hours at 350 deg.C to oxidize the PbO and the like on the surface is oxidized to have Pb3 O4 . Through the two-step baking a part of metal Pb which is not oxidized can be formed at the core part. By containing the particles having the structure in positive electrode active material paste of a lead-acid battery, the metal Pb and PbO in the intermediate layer combined with the active material particles themselves are combined with the metal Pb, PbO and basic lead surfate in the paste at the time of aging and drying. Accordingly, the contribution to hold the active material is attained and the service life is improved.

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、鉛蓄電池用活物質
原料及びそれを用いた鉛蓄電池に関するものであり、特
にペースト式極板を用いる場合の鉛蓄電池の寿命性能を
向上する技術に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an active material for a lead storage battery and a lead storage battery using the same, and more particularly to a technique for improving the life performance of a lead storage battery when a paste type electrode plate is used. is there.

【0002】[0002]

【従来の技術】鉛蓄電池の化成工程、特に正極板の化成
工程においては、化成充電効率が低いという問題があ
る。そこで化成充電における電力や時間のロスを回避す
るために、正極活物質原料に鉛丹(Pb34)を混合す
る技術が一般に知られている。鉛丹は化成工程の電解液
として用いる硫酸に接触するだけで化学的に下式のよう
に不均化反応を起こして化成充電の生成物である二酸化
鉛へ変化すると共に生成した二酸化鉛が高い導電性を有
するため正極の化成充電効率が向上する。
2. Description of the Related Art In the formation process of a lead storage battery, particularly in the formation process of a positive electrode plate, there is a problem that the formation charge efficiency is low. Therefore, in order to avoid a loss of power and time in chemical charging, a technique of mixing lead red (Pb 3 O 4 ) with a positive electrode active material is generally known. Just by contacting sulfuric acid used as an electrolyte in the chemical conversion process, leadtan chemically causes a disproportionation reaction as shown below and changes to lead dioxide, which is a product of formation charge, and the generated lead dioxide is high Since it has conductivity, the formation charge efficiency of the positive electrode is improved.

【0003】Pb34→PbO2+2PbO しかしながら、鉛丹を添加した場合には、活物質粒子間
の結合が弱くなるためサイクル寿命特性が劣化するとい
う問題があり、特にいわゆるペースト式極板において顕
著であった。
Pb 3 O 4 → PbO 2 + 2PbO However, when lead tin is added, there is a problem that the bond between active material particles is weakened and the cycle life characteristic is deteriorated. It was remarkable.

【0004】従来、この問題を解決するための手法とし
て、特公平8−8097号公報に示されるように、正極
活物質原料に鉛丹と同時に金属Pbを添加する手法、特
公平8−15081号公報に示されるように鉛丹を含む
活物質粒子中のPbOの割合を増した低鉛丹化率の活物
質粒子を用いる手法があった。
Conventionally, as a method for solving this problem, as disclosed in Japanese Patent Publication No. 8-8097, a method in which metal Pb is added to a raw material of a positive electrode active material at the same time as lead in Japanese Patent Publication No. 8-15081. As shown in the gazette, there has been a method of using active material particles having a low lead content ratio by increasing the ratio of PbO in the active material particles containing lead.

【0005】[0005]

【発明が解決しようとする課題】鉛丹を添加した場合に
寿命が劣化する原因の詳細は不明であるが、一般的に
は、ペーストの熟成・乾燥時に形成される活物質間の結
合力が弱いためと考えられる。つまり、ペースト中に存
在している金属鉛あるいは塩基性硫酸鉛等は格子等の集
電体へ充填した直後には互いの結合はないが、熟成・乾
燥時に酸化などの化学的変化を受けるとともに互いの結
合が形成され、これが電池寿命末期まで活物質内の骨格
構造を形成し活物質の保持に寄与するものと考えられ
る。ところが、ペースト中の鉛丹は、熟成・乾燥時に化
学的変化を起こしにくく、また粒子間の結合も作りにく
い。そのため鉛丹を添加したペースト式極板の寿命が劣
化するものと考えられる。従来の手法では、いずれも、
上記の熟成・乾燥中に形成される活物質間の結合を強め
るものであるが、上記特公平8−8097号公報の技術
の場合、添加した金属Pbと鉛丹は別の粒子とした構成
であるため、直接の結合を形成しない。また比重の異な
る粒子(金属Pb、鉛丹)を均一に混合、混練すること
は困難である。また上記特公平8−15081号公報の
技術の場合も鉛丹化率を低くしたことにより、鉛丹を含
む活物質粒子中のPbOが活物質間の結合を形成する
が、PbOだけでは結合が十分に形成されない。そのた
め寿命向上の効果が小さいという問題点がある。従来か
らPbOの割合の高い高酸化度鉛粉を原料に用いる場合
にも、同様な活物質間の結合力不足による寿命劣化の問
題が有り、金属Pbを添加する特許出願が多くされてい
ることからも明らかなように、活物質間の結合力を向上
させるにはPbOでは不十分で金属Pbによる効果が非
常に大きい。本発明が解決しようとする課題は、従来法
よりも活物質粒子間の結合を強化し、サイクル寿命特性
の向上した鉛蓄電池を製造することのできる鉛蓄電池用
活物質原料を提供することである。
The details of the cause of the deterioration of the life when lead tin is added are unknown, but in general, the bonding force between the active materials formed during the aging and drying of the paste is low. Probably because it is weak. In other words, the metallic lead or basic lead sulfate present in the paste does not bond to each other immediately after filling in the current collector such as a lattice, but undergoes a chemical change such as oxidation during aging and drying. It is considered that a mutual bond is formed, which forms a skeletal structure in the active material until the end of the battery life and contributes to retention of the active material. However, the red lead in the paste hardly undergoes a chemical change during aging and drying, and hardly forms a bond between particles. Therefore, it is considered that the life of the paste-type electrode plate to which lead tin is added is deteriorated. In traditional approaches,
This is to strengthen the bond between the active materials formed during the aging and drying. In the case of the technique disclosed in Japanese Patent Publication No. 8-8097, the added metal Pb and the lead are composed of different particles. As such, they do not form a direct bond. Further, it is difficult to uniformly mix and knead particles (metal Pb, lead red) having different specific gravities. Also, in the case of the technique disclosed in Japanese Patent Publication No. 8-15081, PbO in the active material particles containing lead-tan forms a bond between the active materials by reducing the lead-tanning rate, but the bond is formed only by PbO. Not sufficiently formed. Therefore, there is a problem that the effect of improving the life is small. Conventionally, even when a high-oxidation lead powder having a high ratio of PbO is used as a raw material, there is a similar problem of deterioration in life due to insufficient bonding force between active materials, and there are many patent applications in which metal Pb is added. As is clear from the above, PbO is not enough to improve the bonding force between active materials, and the effect of metal Pb is very large. The problem to be solved by the present invention is to provide an active material material for a lead storage battery capable of producing a lead storage battery having enhanced cycle life characteristics by strengthening the bond between active material particles as compared with the conventional method. .

【0006】[0006]

【課題を解決するための手段】上記課題を解決するため
に、本発明の鉛蓄電池用活物質原料は、粒子の中心層が
金属Pbであり、表面層がPb34であることを特徴と
する。上記Pb34層と金属Pbとの中間には主にPb
Oの層が存在するが、何も存在しなくてもよい。またP
34層と金属Pbとの中間にPbOの層が存在する場
合でも、当該層は化学量論的にPbOのみならず金属P
bよりも酸化の価数が大きく、Pb34よりも酸化の価
数が小さい層であってもよいし、PbO層のみでもよ
い。
In order to solve the above-mentioned problems, an active material for a lead-acid battery according to the present invention is characterized in that the central layer of particles is metal Pb and the surface layer is Pb 3 O 4. And Pb is mainly located between the Pb 3 O 4 layer and the metal Pb.
There is an O layer, but nothing may be present. Also P
Even if a PbO layer is present between the b 3 O 4 layer and the metal Pb, the layer is not only stoichiometrically PbO but also metal Pb.
The layer may have a higher valence of oxidation than b and a lower valence of oxidation than Pb 3 O 4 , or may be a PbO layer alone.

【0007】上記本発明の鉛蓄電池用活物質原料は、鉛
丹粒子自体に集電体との結合力形成に有効である金属P
bの中心層を形成したものである。従って活物質粒子間
の結合を強める作用を有する金属Pbを極板全体に亘り
均一に分布させることができる。前記均一に分布させる
工程は、一旦上記構成の粒子を作製してしまえば非常に
簡単である。このような構成の粒子により、熟成、乾燥
後の極板の活物質粒子間結合強度が高まり、それにより
鉛蓄電池の充放電サイクル寿命特性が向上する。
The active material for a lead-acid battery according to the present invention comprises a metal P which is effective for forming a bonding force with a current collector on the lead-acid particles themselves.
The center layer of b is formed. Therefore, the metal Pb having an effect of strengthening the bond between the active material particles can be uniformly distributed over the entire electrode plate. The step of uniformly distributing the particles is very simple once the particles having the above-mentioned structure are produced. With the particles having such a configuration, the bond strength between the active material particles of the electrode plate after aging and drying is increased, thereby improving the charge-discharge cycle life characteristics of the lead storage battery.

【0008】[0008]

【発明の実施の形態】以下、本発明の実施の形態の一例
を説明する。従来法の鉛丹は、量産性の面から、鉛の一
部又は全部があらかじめPbOに酸化された酸化度が7
0〜100%と比較的高いモールテンフロー式又はボー
ルミル式の鉛粉を400〜500℃で焼成して製造され
る。焼成時間を短くして鉛丹化率(以降本明細書での鉛
丹化率とは、金属Pb換算で粒子を占める鉛丹のモル%
である。)を低下させるにせよ、粒子中の金属鉛は全て
酸化されてしまうので金属Pbは存在しない。本発明の
活物質原料は、従来法と異なり、ボールミル式の酸化度
20〜40%の鉛粉を原料とし、まず、鉛の融点327
℃を越えない200〜300℃で4時間焼成を行う。本
過程では活物質原料粒子と金属Pbを融合させずに、活
物質原料粒子の中心層に金属Pbを残し表面を主にPb
Oに酸化する。さらに350℃で20時間焼成を行い表
面のPbO等をPb34に酸化する。この様に二段階で
焼成を行うことにより中心部に金属Pbの未酸化部分を
形成することが出来る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below. In the conventional method, from the viewpoint of mass productivity, a part of or all of lead is previously oxidized to PbO and has an oxidation degree of 7.
It is manufactured by calcining a relatively high molten flow type or ball mill type lead powder of 0 to 100% at 400 to 500 ° C. By shortening the sintering time, the ratio of lead tin (hereinafter referred to as the ratio of lead tin in the present specification is the mole percent of lead tin occupying particles in terms of metal Pb).
It is. ), The metal lead in the particles is completely oxidized, so that no metal Pb is present. The active material raw material of the present invention is different from the conventional method in that a ball mill type lead powder having an oxidation degree of 20 to 40% is used as a raw material.
The baking is performed at 200 to 300 ° C. for 4 hours which does not exceed the temperature. In this step, the metal Pb is left in the center layer of the active material raw particles without fusing the active material raw particles and the metal Pb, and the surface is mainly made of Pb.
Oxidizes to O. Further, baking is performed at 350 ° C. for 20 hours to oxidize PbO and the like on the surface to Pb 3 O 4 . By performing firing in two stages in this manner, an unoxidized portion of metal Pb can be formed at the center.

【0009】上記構造を備えた粒子を鉛蓄電池の正極活
物質ペーストに含ませると、活物質粒子自体と結合した
金属Pb及び中間層のPbOが熟成・乾燥時にペースト
中の金属PbやPbO及び塩基性硫酸鉛と結合を形成す
る。従来の鉛丹では、金属Pbを添加する場合は鉛丹自
身に結合力がないため、また鉛丹化率を低めた鉛丹では
結合形成能力の弱いPbOによるペースト中の粒子との
結合しか得られないため結合力が本発明の活物質原料を
用いた場合より弱くなる。その結果、本発明鉛丹を用い
て得られる電池は電池寿命末期まで活物質内の骨格構造
を維持し、活物質の保持に寄与するため寿命特性が大幅
に向上する。
When the particles having the above structure are included in the positive electrode active material paste of the lead-acid battery, the metal Pb bonded to the active material particles themselves and the PbO of the intermediate layer are ripened and dried. Form a bond with lead sulfate. In the case of conventional leadtan, when metal Pb is added, leadtan itself does not have a binding force, and in the case of leadtan with a reduced ratio of leadtan, the bond between the particles in the paste by PbO, which has a weak bond-forming ability, can only be obtained. Therefore, the bonding force is weaker than when the active material of the present invention is used. As a result, the battery obtained using the lead tin of the present invention maintains the skeletal structure in the active material until the end of the battery life and contributes to the retention of the active material, so that the life characteristics are greatly improved.

【0010】[0010]

【実施例】本発明と従来とを比較検討する。まず酸化度
20〜40%のボールミル式鉛粉を原料として、発明の
実施の形態に記載した焼成条件を基本に原料鉛粉の酸化
度と焼成時間を調節することでPb34、PbO、金属
Pbの比率の異なる鉛蓄電池用活物質原料(実施例1〜
6)を作製した。
The present invention will be compared with the prior art. First, using a ball mill type lead powder having an oxidation degree of 20 to 40% as a raw material, Pb 3 O 4 , PbO, and the like are adjusted by adjusting the degree of oxidation and the firing time of the raw material lead powder based on the firing conditions described in the embodiment of the invention. Active material raw materials for lead-acid batteries having different ratios of metal Pb (Examples 1 to 3)
6) was produced.

【0011】活物質原料粒子の断面観察を実施した。実
施例5と従来例1の活物質原料粒子を樹脂に埋め硬化さ
せた後、切断面を研磨して金属顕微鏡にて観察した。実
施例5の活物質原料粒子は、中心層に金属Pbを有して
いることがわかった。また従来例1の活物質原料粒子
は、中心層に金属Pbを有していないこともわかった。
A cross section of the active material particles was observed. After embedding and curing the active material material particles of Example 5 and Conventional Example 1 in a resin, the cut surface was polished and observed with a metallographic microscope. The active material particles of Example 5 were found to have metal Pb in the center layer. It was also found that the active material raw particles of Conventional Example 1 did not have metal Pb in the central layer.

【0012】次いで酸化度80%のボールミル式鉛粉を
用い、焼成条件を調整することで表1に示す各活物質原
料(従来例1〜4の活物質原料)とした。また従来例2
の活物質原料については、特公平8−8097号公報に
対応させるため、金属Pb粉を活物質原料に対し10w
t%添加した。
Next, using a ball mill type lead powder having an oxidation degree of 80%, the firing conditions were adjusted to obtain each active material raw material shown in Table 1 (active material raw materials of Conventional Examples 1 to 4). Conventional example 2
In order to comply with Japanese Patent Publication No. 8-8097, metal Pb powder is added to the active material raw material in an amount of 10 w
t% was added.

【0013】製造した活物質原料(実施例1〜6、従来
例1〜4)はさらに分級し目的の粒度分布に調節した。
なお鉛蓄電池に用いられる鉛粉の粒度は一般的にはDp
50(篩い下50%径)が1〜20μmの範囲であるの
で、本例では粒径をDp50=10μmに統一して比較
した。製造した活物質原料の物性は以下の装置を用いて
確認した。 平均粒子径:レーザー回折式粒度分布測定装置HORI
BA製LA−500(分散媒:H2O+非イオン系界面
活性剤) 上記した実施例1〜6、従来例1〜4の活物質原料を用
い、これらをそれぞれ常法に従って水と硫酸で練合して
ペーストとし、格子体に充填後、熟成乾燥して未化成の
正極板を得た。未化成の正極板と、常法により作製した
未化成の負極板及びガラス繊維セパレータと組み合わ
せ、ABS製電槽に組み込んだ後、電解液を注入し化成
を行う電槽化成の工程を経て、公称容量7Ah(20時
間率容量)の密閉型鉛蓄電池を作った。上記電池に関し
て、化成充電の効率(PbO2化率)の把握と初期容量
試験及びサイクル寿命試験を実施した。その結果を表1
に示す。初期容量試験は、完全充電状態から0.25
C、20Aで終止電圧1.7V/セルまで放電した。サ
イクル寿命試験は、JIS C8702に基づき、以下
の条件で行った。
The produced active material raw materials (Examples 1 to 6 and Conventional Examples 1 to 4) were further classified and adjusted to a target particle size distribution.
The particle size of the lead powder used in the lead storage battery is generally Dp
Since 50 (50% diameter under the sieve) is in the range of 1 to 20 μm, in this example, the particle diameter was unified to Dp50 = 10 μm and compared. The physical properties of the manufactured active material material were confirmed using the following apparatus. Average particle size: Laser diffraction particle size distribution analyzer HORI
BA made LA-500 (dispersion medium: H 2 O + nonionic surfactant) Examples 1 to 6 described above, using the raw active material in the conventional example 1-4, kneading them with water and sulfuric acid according to a conventional method, respectively The paste was combined, filled into a lattice, aged and dried to obtain an unformed positive electrode plate. After combining with an unformed positive electrode plate, an unformed negative electrode plate and a glass fiber separator produced by a conventional method, and incorporating it into an ABS battery case, the electrolytic solution is injected to form a battery case. A sealed lead-acid battery having a capacity of 7 Ah (20 hour rate capacity) was produced. Regarding the battery, the efficiency of formation charge (PbO 2 conversion ratio) was grasped, and an initial capacity test and a cycle life test were performed. Table 1 shows the results.
Shown in The initial capacity test is 0.25
C, the battery was discharged at 20 A to a final voltage of 1.7 V / cell. The cycle life test was performed under the following conditions based on JIS C8702.

【0014】(a)試験温度:周囲温度25±2℃ (c)容量確認:約25サイクル毎に、完全充電状態か
ら0.25C、20Aで終止電圧1.7V/セルまで放
電する。
(A) Test temperature: ambient temperature 25 ± 2 ° C. (C) Capacity confirmation: Discharge from a fully charged state to a final voltage of 1.7 V / cell at 0.25 C and 20 A every about 25 cycles.

【0015】(d)電池寿命判定時期:(c)で求めた
容量が初期容量の50%以下に劣化するまでとする。
(D) Battery life judging time: until the capacity obtained in (c) is reduced to 50% or less of the initial capacity.

【0016】PbO2化率(金属Pb換算で粒子を占め
るPbO2のモル%)は、次のように測定した。まず試
料を秤量びんに1g精秤し、10vol%硝酸水溶液を
そこに20ml加えて超音波振動器に90分間かけた
後、遠心分離機にて溶け残ったPbO2とPbSO4を分
離する。この上澄み液を1mlとり、緩衝溶液10ml
と指示薬を加えた溶液を0.01MのEDTA溶液で滴
定し、以下の式からPbOx値を求める。
[0016] PbO 2 ratio (mole% of PbO 2 occupying the particles of metal Pb conversion) was measured as follows. First, 1 g of a sample is precisely weighed in a weighing bottle, 20 ml of a 10 vol% nitric acid aqueous solution is added thereto, and the mixture is subjected to an ultrasonic vibrator for 90 minutes. Then, PbO 2 and PbSO 4 remaining undissolved are separated by a centrifuge. Take 1 ml of this supernatant and add 10 ml of buffer solution
The solution to which the and the indicator were added was titrated with a 0.01 M EDTA solution, and the PbO x value was determined from the following equation.

【0017】[0017]

【数1】 (Equation 1)

【0018】次に、試料を秤量びんに1g精秤し、硝酸
+過酸化水素水溶液を30ml添加し、30分間静置す
る。溶け残ったPbSO4を濾紙で濾過後、蒸留水で水
洗し、るつぼにて濾紙ごと焼き(濾紙の灰化)さらに5
50℃で30分間保持し、灰を気化、除去し、サンプル
中のPbSO4のみの重量比(%)を得る。そして以下
の式によりPbO2化率を算出する。
Next, 1 g of the sample is precisely weighed in a weighing bottle, 30 ml of an aqueous solution of nitric acid and hydrogen peroxide are added, and the mixture is left to stand for 30 minutes. The remaining PbSO 4 is filtered through filter paper, washed with distilled water, and baked in a crucible with the filter paper (ashing of filter paper).
The sample is kept at 50 ° C. for 30 minutes to vaporize and remove the ash to obtain a weight ratio (%) of only PbSO 4 in the sample. Then, the PbO 2 conversion rate is calculated by the following equation.

【0019】PbO2(%)=100-PbOx(%)-PbSO4(%) 活物質粒子の鉛丹化率は、次のように測定した。まずサ
ンプルを1g秤量する。次に酢酸ナトリウム3水和物を
60g秤量し、5%酢酸溶液に溶解させ100mlとし
たものを50ml用意し、それに前記サンプルを加え
る。さらに0.1規定のチオ硫酸ナトリウム水溶液を5
0ml加える。これらを常圧で加熱沸騰させ、前記サン
プルを溶解させる。そして0.1規定のヨウ素溶液で、
サンプルが溶解した溶液に滴定する(指示薬:0.5%
でんぷん溶液3ml、ドラフト内で褐色のビュレットを
使用する)。この時の滴定量をVml、サンプルを投入
しない溶液に滴定した場合の滴定量(ブランク)をV0
とし、以下の式により活物質粒子の鉛丹化率(金属Pb
換算でのモル%)を算出する。
PbO 2 (%) = 100-PbO x (%)-PbSO 4 (%) The lead tinification rate of the active material particles was measured as follows. First, 1 g of a sample is weighed. Next, 60 g of sodium acetate trihydrate is weighed, dissolved in a 5% acetic acid solution to make 100 ml, 50 ml is prepared, and the sample is added thereto. Then, add 0.1N aqueous sodium thiosulfate solution
Add 0 ml. These are heated and boiled at normal pressure to dissolve the sample. And with 0.1N iodine solution,
Titrate to the solution in which the sample was dissolved (indicator: 0.5%
3 ml of starch solution, use brown burette in draft). The titer at this time was Vml, and the titer (blank) when titrated to a solution not charged with the sample was V 0.
And the lead nitanification rate of the active material particles (metal Pb
(Mol% in conversion).

【0020】[0020]

【数2】 (Equation 2)

【0021】活物質粒子の金属Pb含有率(モル%)及
びPbO含有率(モル%)は、次のように測定、算出し
た。ここでは、実施例1〜6の鉛蓄電池用活物質粒子の
中心部の金属Pbと、表面層のPb34との中間層をす
べてPbOとみなして算出した。所定重量の活物質粒子
を、NaOH300gを1リットルの水に溶解した溶液
と、マンニット60gを1リットルの水に溶解した溶液
と、塩酸ヒドラジン30gを1リットルの水に溶解した
溶液との混合溶液に、超音波で加振しながら常温で30
分間浸漬し、この浸漬操作前後の固形分(活物質粒子)
重量を差し引いた値がPb34とPbOの重量の和であ
る。サンプルである活物質粒子中のPb34重量は前述
した鉛丹化率(金属Pb換算でのモル%)から算出可能
である。従って前記Pb34とPbOの重量の和から活
物質粒子中のPbO重量が算出される。また前記浸漬後
の固形分重量は金属Pb分である。このようにして得ら
れた活物質粒子の鉛丹化率(金属Pb換算でのモル
%)、活物質粒子中のPb34重量、PbO重量、金属
Pb重量の数値から、活物質粒子中のPb34、Pb
O、金属Pbの、金属Pb換算モル%(表1のモル%)
を得ることができる。
The metal Pb content (mol%) and PbO content (mol%) of the active material particles were measured and calculated as follows. Here, all the intermediate layers between the metal Pb at the center of the active material particles for lead storage batteries of Examples 1 to 6 and the surface layer of Pb 3 O 4 were regarded as PbO and calculated. A mixed solution of a solution in which 300 g of NaOH is dissolved in 1 liter of water, a solution in which 60 g of mannitol is dissolved in 1 liter of water, and a solution in which 30 g of hydrazine hydrochloride is dissolved in 1 liter of water. And at room temperature while vibrating with ultrasonic waves.
And the solid content before and after this dipping operation (active material particles)
The value obtained by subtracting the weight is the sum of the weights of Pb 3 O 4 and PbO. The weight of Pb 3 O 4 in the active material particles as the sample can be calculated from the above-mentioned lead tinification rate (mol% in terms of metal Pb). Therefore, the weight of PbO in the active material particles is calculated from the sum of the weights of Pb 3 O 4 and PbO. The solid content weight after the immersion is the metal Pb content. From the lead tinification ratio (mol% in terms of metal Pb) of the active material particles thus obtained and the values of Pb 3 O 4 weight, PbO weight and metal Pb weight in the active material particles, Pb 3 O 4 , Pb
O, metal Pb conversion mol% of metal Pb (mol% in Table 1)
Can be obtained.

【0022】[0022]

【表1】 [Table 1]

【0023】表1より以下のことが明らかである。サイ
クル寿命回数に関しては、特公平8−8097号公報に
対応した金属Pbを活物質原料に加え別に添加したもの
(従来例2)、特公平8−15081号公報に対応した
低鉛丹化率のもの(従来例3、4)と比して、本発明の
実施例1〜4はサイクル寿命回数が増加する。同一鉛丹
化率における比較(実施例1、2、従来例3)及び(実
施例3、4、従来例4)においても活物質粒子中の金属
Pb量が0の従来の活物質粒子と比較して本発明による
ものでは金属鉛が0.4モル%(活物質粒子の金属Pb
換算でのモル%)存在するだけでサイクル数の大幅な増
加が認められる。これは、活物質粒子の中心に金属Pb
が存在する本発明の構成を有する活物質原料を用いてい
るため発明の実施の形態で記載した効果が得られたもの
と考えられる。但し、本発明の構成を有する活物質粒子
の金属Pb量が約5モル%を越えると、初期容量が劣る
おそれがある。従って本発明の構成を有する活物質粒子
の金属Pb量は5モル%以下が望ましい。鉛丹化率が金
属Pb換算で75モル%を下回ると(実施例5、6)サ
イクル寿命は最もよい結果となるが初期容量が低下し、
また化成充電効率(PbO2化率)も低下するため自己
放電特性等別の電池特性面への悪影響があらわれるおそ
れがある。また鉛丹化率が97モル%を越える活物質粒
子は、その製造の際に粒子中心部に金属Pb部を残留さ
せる焼成の制御が困難である上に、サイクル寿命特性の
点で不利なおそれがある。従って鉛丹化率は75〜97
%の範囲が望ましい。当該範囲であればPbO2化率は
80%以上の十分な化成性が得られ初期容量はほぼ同等
であり、サイクル寿命の向上も顕著である。
The following is clear from Table 1. Regarding the number of cycle life, the metal Pb corresponding to Japanese Patent Publication No. 8-8097 was separately added to the active material material (conventional example 2), and the lead reduction rate corresponding to Japanese Patent Publication No. 8-15081 was low. Examples 1 to 4 of the present invention have an increased number of cycle life times as compared with the prior art (conventional examples 3 and 4). Also in the comparison (Examples 1, 2, Conventional Example 3) and (Examples 3, 4, Conventional Example 4) at the same lead tinification ratio, the comparison was made with the conventional active material particles in which the amount of metal Pb in the active material particles was 0. According to the present invention, 0.4% by mole of metallic lead (metal Pb of active material particles) is used.
(Mole% in terms of conversion), the presence of which leads to a significant increase in the number of cycles. This is because the metal Pb is located at the center of the active material particles.
It is considered that the effect described in the embodiment of the present invention was obtained because the active material raw material having the structure of the present invention in which is present was used. However, when the amount of metal Pb in the active material particles having the configuration of the present invention exceeds about 5 mol%, the initial capacity may be inferior. Therefore, the metal Pb content of the active material particles having the structure of the present invention is desirably 5 mol% or less. When the lead tin reduction ratio is less than 75 mol% in terms of metal Pb (Examples 5 and 6), the cycle life is the best, but the initial capacity is reduced.
In addition, the formation charge efficiency (PbO 2 conversion rate) also decreases, so that there is a possibility that other battery characteristics such as self-discharge characteristics may be adversely affected. Further, active material particles having a lead tinification ratio of more than 97 mol% are difficult to control in firing to leave a metal Pb portion in the center of the particles at the time of production, and may be disadvantageous in terms of cycle life characteristics. There is. Therefore, the rate of lead tinification is 75-97.
% Is desirable. Within this range, a sufficient conversion property with a PbO 2 conversion ratio of 80% or more is obtained, the initial capacity is almost the same, and the cycle life is remarkably improved.

【0024】[0024]

【発明の効果】上述したように、本発明に係る鉛蓄電池
用活物質原料は、表面層がPb34であり、中心層が金
属Pbとしたため、従来の鉛丹化率を低める方法や、金
属Pbを添加する手法に比べ、化成充電効率を損なうこ
となくサイクル寿命特性を向上できる点で優れている。
As described above, the active material for a lead-acid battery according to the present invention has a surface layer of Pb 3 O 4 and a central layer of metal Pb. Compared with the method of adding metal Pb, the method is excellent in that the cycle life characteristics can be improved without impairing the formation charging efficiency.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】粒子の中心層が金属Pbであり、表面層が
Pb34であることを特徴とする鉛蓄電池用活物質原
料。
1. An active material material for a lead-acid battery, wherein the central layer of the particles is metal Pb and the surface layer is Pb 3 O 4 .
【請求項2】粒子の鉛丹化率(金属Pb換算で粒子を占
めるPb34のモル%)が、75〜97%であり、且つ
含有する金属Pb量が5モル%以下であることを特徴と
する請求項1記載の鉛蓄電池用活物質原料。
2. The lead tinification ratio (mol% of Pb 3 O 4 occupying particles in terms of metal Pb) of the particles is 75 to 97%, and the amount of metal Pb contained is 5 mol% or less. The active material raw material for a lead storage battery according to claim 1, wherein:
【請求項3】請求項1又は2に記載した活物質原料を正
極板に含む鉛蓄電池。
3. A lead-acid battery comprising the positive electrode plate containing the active material raw material according to claim 1.
JP07404897A 1997-03-26 1997-03-26 Method for producing active material for lead-acid battery Expired - Lifetime JP3646462B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07404897A JP3646462B2 (en) 1997-03-26 1997-03-26 Method for producing active material for lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07404897A JP3646462B2 (en) 1997-03-26 1997-03-26 Method for producing active material for lead-acid battery

Publications (2)

Publication Number Publication Date
JPH10270029A true JPH10270029A (en) 1998-10-09
JP3646462B2 JP3646462B2 (en) 2005-05-11

Family

ID=13535916

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3646462B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008276980A (en) * 2007-04-25 2008-11-13 Gs Yuasa Corporation:Kk Raw material of active material for lead-acid storage battery, and lead-acid storage battery using it
JP2009123433A (en) * 2007-11-13 2009-06-04 Gs Yuasa Corporation:Kk Method of manufacturing control valve type lead-acid battery
WO2018088309A1 (en) * 2016-11-08 2018-05-17 日立化成株式会社 Production method for lead storage battery active material

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008276980A (en) * 2007-04-25 2008-11-13 Gs Yuasa Corporation:Kk Raw material of active material for lead-acid storage battery, and lead-acid storage battery using it
JP2009123433A (en) * 2007-11-13 2009-06-04 Gs Yuasa Corporation:Kk Method of manufacturing control valve type lead-acid battery
WO2018088309A1 (en) * 2016-11-08 2018-05-17 日立化成株式会社 Production method for lead storage battery active material
KR20190077486A (en) 2016-11-08 2019-07-03 히타치가세이가부시끼가이샤 Method for manufacturing active material for lead-acid battery
JP2019212639A (en) * 2016-11-08 2019-12-12 日立化成株式会社 Manufacturing method of active material for lead acid battery
TWI757362B (en) * 2016-11-08 2022-03-11 日商日立化成股份有限公司 Manufacturing method of active material for lead storage battery

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