JP2000357532A - Manufacturing method of lead storage battery - Google Patents
Manufacturing method of lead storage batteryInfo
- Publication number
- JP2000357532A JP2000357532A JP11166386A JP16638699A JP2000357532A JP 2000357532 A JP2000357532 A JP 2000357532A JP 11166386 A JP11166386 A JP 11166386A JP 16638699 A JP16638699 A JP 16638699A JP 2000357532 A JP2000357532 A JP 2000357532A
- Authority
- JP
- Japan
- Prior art keywords
- electrode plate
- lead
- active material
- sulfuric acid
- battery
- 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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
Landscapes
- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
(57)【要約】
【課題】 薄型極板を用いながらも、高率放電特性およ
びサイクル寿命特性に優れた鉛蓄電池を提供することを
目的とする。
【解決手段】 水溶性シリコーンを結着剤として用い
て、活物質を芯材に塗着した正・負極の薄型極板をセパ
レーターを介して極板群を構成し、この状態で熱処理を
行い熟成工程とする製造法である。
(57) [Problem] To provide a lead storage battery having excellent high-rate discharge characteristics and cycle life characteristics while using a thin electrode plate. SOLUTION: Using a water-soluble silicone as a binder, a positive / negative thin electrode plate in which an active material is coated on a core material is formed into a group of electrodes via a separator, and heat treatment is performed in this state to perform aging. This is a manufacturing method that is a process.
Description
【0001】[0001]
【発明の属する技術分野】本発明は鉛蓄電池の製造法、
特にサイクル寿命特性と高率放電特性に優れた密閉形鉛
蓄電池の製造法に関するものである。The present invention relates to a method for manufacturing a lead storage battery,
In particular, the present invention relates to a method for manufacturing a sealed lead-acid battery having excellent cycle life characteristics and high-rate discharge characteristics.
【0002】[0002]
【従来の技術】現在、鉛蓄電池においてペースト式極板
が生産性に富む工業的製造法としてもっとも普及してい
る。ペースト式極板は鉛または鉛合金製の鋳造またはエ
キスパンド格子からなる集電体の空隙部に鉛と鉛酸化物
との混合粉体(以下鉛粉)に水と希硫酸を加えて混練し
たペーストを充填後、熟成・乾燥して未化成極板を作製
する。また、このペースト充填行程において必要に応じ
て、充填直後の極板を希硫酸に浸す浸酸処理によって極
板表面に硫酸鉛を生成させて強固にしたのちに熟成化し
て極板を完成する。このようにして作成された未化成極
板は、極板単体もしくは電池として組み込まれた状態と
した後に希硫酸電解液中で化成されることにより、正極
および負極をそれぞれ二酸化鉛および海綿状鉛化して極
板もしくは電池が完成される。2. Description of the Related Art At present, paste type electrode plates are most widely used in lead-acid batteries as an industrial production method with high productivity. The paste type electrode plate is a paste obtained by adding water and dilute sulfuric acid to a mixed powder of lead and lead oxide (hereinafter referred to as “lead powder”) in the voids of a current collector made of a cast or expanded lattice made of lead or a lead alloy. After filling, aged and dried to produce an unformed electrode plate. In this paste filling step, if necessary, the electrode plate immediately after filling is immersed in dilute sulfuric acid to generate lead sulfate on the surface of the electrode plate, thereby strengthening the electrode plate, followed by aging to complete the electrode plate. The unformed electrode plate thus formed is converted into a single electrode plate or a state assembled in a battery and then formed in a dilute sulfuric acid electrolytic solution to convert the positive electrode and the negative electrode into lead dioxide and spongy lead, respectively. The electrode plate or battery is completed.
【0003】鉛蓄電池用の鉛粉の主成分は一酸化鉛であ
り、その他に金属鉛を15〜35%含んでいる。鉛粉を
希硫酸で混錬したペーストは、生成する硫酸鉛が過剰に
存在する一酸化鉛によって塩基性硫酸鉛になり適度の硬
さとずれ弾性を保つ。熟成・乾燥中の格子内ペースト
は、金属鉛の酸化と塩基性硫酸鉛の結晶成長とともに部
分的に水分が蒸発して粉体粒子相互間が結着するセメン
テーション現象が起こって硬化する。このペースト式極
板は生産性とコストパフォーマンスに優れ、きわめて有
効な工業的極板製造法といえる。[0003] The main component of the lead powder for a lead storage battery is lead monoxide, and it also contains 15 to 35% of metallic lead. A paste obtained by kneading lead powder with dilute sulfuric acid becomes basic lead sulfate due to lead monoxide in which excess lead sulfate is present, and maintains an appropriate hardness and shear elasticity. During the aging and drying, the intra-lattice paste is hardened by the oxidation of metallic lead and the crystal growth of basic lead sulfate, which partially evaporates moisture and causes a cementation phenomenon in which powder particles are bound to each other. This paste-type electrode plate is excellent in productivity and cost performance, and can be said to be an extremely effective industrial electrode plate manufacturing method.
【0004】近年、各種電動工具用、エンジン始動用、
電気自動車用等の高出力源として非穿孔の鉛シートの両
面に活物質を薄く均一に塗着した薄型正負極板を、セパ
レーターを介して渦巻き状に巻いた極板群からなる円筒
形の密閉形鉛蓄電池が米国特許第5045086号、第
5047300号、第5198313号で提案されてい
る。このような薄型極板は、集電面積を大きくすると共
に硫酸の拡散距離を短縮することによりハイレート放電
における特性向上を目指したものである。In recent years, for various electric tools, for starting an engine,
As a high power source for electric vehicles, etc., a cylindrical hermetic seal consisting of a group of electrode plates in which a thin positive / negative electrode plate in which active material is thinly and uniformly applied to both sides of a non-perforated lead sheet is spirally wound through a separator Lead-acid batteries have been proposed in U.S. Pat. Nos. 5,050,586, 5,047,300 and 5,198,313. Such a thin electrode plate aims to improve characteristics in high-rate discharge by increasing the current collecting area and shortening the diffusion distance of sulfuric acid.
【0005】[0005]
【発明が解決しようとする課題】このような薄型極板の
場合、前記のようなペーストではその粘度が高いために
薄く均一に塗着することはできない。そこで、鉛粉を主
成分とする粉末材料を硫酸を全く用いず、水だけで練っ
た粘性の低いスラリーを鉛シート両面に薄く塗着する方
法がとられている。上記のようにして作られた正負極板
は、セパレーターと共に渦巻き状に群構成し、電槽ケー
スに挿入してそのまま希硫酸中で電槽化成が行われる。
前記したような熟成工程は電池の放電特性を左右する重
要な工程であるが、上記のような薄型極板では硫酸を含
まないスラリーを用いているため、従来のペーストを用
いる極板と同様な熟成処理は行えない。そのため放電容
量の低下やサイクル劣化が問題となっているのが現状で
ある。In the case of such a thin electrode plate, the paste described above cannot be applied thinly and uniformly because of its high viscosity. Therefore, a method has been adopted in which a low-viscosity slurry kneaded only with water is thinly applied to both surfaces of a lead sheet without using sulfuric acid at all as a powder material containing lead powder as a main component. The positive and negative electrode plates produced as described above are spirally grouped together with the separator, inserted into a battery case, and subjected to battery formation in dilute sulfuric acid as it is.
The aging step as described above is an important step that affects the discharge characteristics of the battery.However, since the thin electrode plate as described above uses a slurry that does not contain sulfuric acid, it is similar to an electrode plate using a conventional paste. Aging treatment cannot be performed. Therefore, at present, the discharge capacity is reduced and the cycle is deteriorated.
【0006】このような問題を解決するため、薄型極板
を希硫酸中に浸酸し硫酸を活物質層に含ませた後に、温
度と湿度を管理しながら鉛粉を硫酸と反応させる簡易的
な熟成工程が考えられる。しかし、この方法では鉛粉と
硫酸の反応による粒子の体積膨張によって芯材から活物
質層が脱落する。また、前述した鉛粉のセメンテーショ
ン反応が起こるが、このように硬化した極板を渦巻き状
に群構成することは活物質層が割れたり、脱落して不可
能である。In order to solve such a problem, a thin electrode plate is immersed in dilute sulfuric acid, sulfuric acid is contained in the active material layer, and then the lead powder is reacted with sulfuric acid while controlling the temperature and humidity. Aging process is conceivable. However, in this method, the active material layer falls off from the core material due to the volume expansion of the particles due to the reaction between lead powder and sulfuric acid. Further, although the above-described lead powder cementation reaction occurs, it is impossible to form the cured electrode plates in a spiral group because the active material layer is cracked or falls off.
【0007】このような活物質層の割れや脱落を防止す
るため結着剤としてポリフッ化ビニリデンを添加したN
−メチルピロリドンを練液として活物質スラリーを作成
する技術が特開平10−261432で提案されてい
る。しかし、この方法では、極板製造工程において有機
溶剤を用いるため、工程が複雑化してしまう。[0007] In order to prevent such active material layer from cracking or falling off, N containing polyvinylidene fluoride as a binder is added.
A technique for preparing an active material slurry by using -methylpyrrolidone as a kneading liquid has been proposed in JP-A-10-261432. However, in this method, since an organic solvent is used in the electrode plate manufacturing process, the process is complicated.
【0008】本発明は活物質スラリーの練液として前記
したような有機溶剤を用いることなく、芯材からの活物
質の脱落を抑制して高率放電特性の向上とサイクル寿命
特性の向上の両立を図る、高性能な鉛蓄電池を与えるこ
とを目的とする。The present invention suppresses the fall of the active material from the core material without using the above-mentioned organic solvent as a kneading liquid of the active material slurry, and achieves both improvement of the high rate discharge characteristics and improvement of the cycle life characteristics. The object is to provide a high-performance lead-acid battery.
【0009】[0009]
【課題を解決するための手段】上記目的を達成するため
に、本発明の請求項1の発明は鉛と鉛酸化物との混合物
または鉛丹を主成分とする粉末材料を水溶性ケイ素系ポ
リマーと水とで混練したペーストを導電性シートからな
る芯材に塗着して正極板を形成し、この正極板および負
極板とセパレーターとからなる極板群を希硫酸に浸漬し
た後、極板群を熱処理することを特徴とするものであ
る。In order to achieve the above-mentioned object, a first aspect of the present invention is to provide a powdery material containing a mixture of lead and lead oxide or lead-tin as a water-soluble silicon-based polymer. A paste kneaded with water and water is applied to a core material made of a conductive sheet to form a positive electrode plate, and the electrode plate group including the positive electrode plate and the negative electrode plate and the separator is immersed in dilute sulfuric acid. The heat treatment is performed on the group.
【0010】請求項2の発明は、前記の熱処理を40℃
〜80℃で行うことを示すものである。請求項3の発明
は、前記極板群は前記正極板および前記負極板をセパレ
ーターを介してら旋状に捲回するものである。According to a second aspect of the present invention, the heat treatment is performed at 40 ° C.
This indicates that the process is performed at ~ 80 ° C. According to a third aspect of the present invention, the electrode plate group spirally winds the positive electrode plate and the negative electrode plate via a separator.
【0011】[0011]
【発明の実施の形態】本発明による密閉形鉛蓄電池の製
造フローを図1に示す。鉛粉を主原料とする活物質源粉
末に、結着剤として水溶性ケイ素系ポリマー(以下シリ
コーンとする)、溶媒として水を加え練合した低粘度の
ペーストを、シート状の集電体に薄く均一に塗着したの
ち、溶媒を除いて極板を作成する。次に作製した正極板
と負極板をセパレーターを介して捲回し極板群を構成す
る。これを比重1.20〜1.40の希硫酸に浸漬し、
セパレーターと活物質層に硫酸を含ませた後、40℃〜
80℃の恒温槽中で1〜4時間乾燥する熟成工程を行
う。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows a manufacturing flow of a sealed lead-acid battery according to the present invention. A low-viscosity paste obtained by adding a water-soluble silicon-based polymer (hereinafter referred to as silicone) as a binder and water as a solvent to an active material source powder mainly containing lead powder and kneading the resulting mixture into a sheet-like current collector. After applying thinly and uniformly, remove the solvent to make the electrode plate. Next, the produced positive electrode plate and negative electrode plate are wound via a separator to form an electrode plate group. This is immersed in dilute sulfuric acid having a specific gravity of 1.20 to 1.40,
After impregnating the separator and the active material layer with sulfuric acid,
An aging step of drying in an 80 ° C. constant temperature bath for 1 to 4 hours is performed.
【0012】上記の製造法によれば、活物質と硫酸との
反応による集電体と活物質との間の剥離が、捲回により
極板群にかかる圧力とシリコーンにより抑止され、良好
な熟成の状態の薄型極板群を得ることができ、サイクル
寿命特性と高率放電特性に優れた密閉形鉛蓄電池を得る
ことが出来る。According to the above-mentioned production method, peeling between the current collector and the active material due to the reaction between the active material and sulfuric acid is suppressed by the pressure applied to the electrode plate group by the winding and the silicone, and good aging is achieved. Thus, a sealed lead-acid battery having excellent cycle life characteristics and high-rate discharge characteristics can be obtained.
【0013】[0013]
【実施例】以下の本発明の実施例について図面を参照し
ながら説明する。まず、極板の作成であるが、本実施例
では、正極板または負極板原料として重量比で25%、
一酸化鉛75%(酸化度75%)からなる鉛粉を用い、
負極は、この他に前記鉛粉に対して2%の硫酸バリウム
と1%の炭素粉末、0.5%のリグニンを添加剤として
混合材を調製した。ちなみに、正極用の添加剤としては
上記のほかに鉛丹や塩基性硫酸鉛や二酸化鉛などの鉛化
合物の添加が可能である。DESCRIPTION OF THE PREFERRED EMBODIMENTS The following embodiments of the present invention will be described with reference to the drawings. First, the preparation of the electrode plate was performed. In this example, the raw material of the positive electrode plate or the negative electrode plate was 25% by weight,
Using lead powder consisting of 75% of lead monoxide (degree of oxidation 75%)
For the negative electrode, a mixed material was prepared using, as additives, 2% barium sulfate, 1% carbon powder, and 0.5% lignin based on the lead powder. Incidentally, as an additive for the positive electrode, in addition to the above, it is possible to add a lead compound such as red lead, basic lead sulfate or lead dioxide.
【0014】上記の原料粉末に、結着剤シリコーンを溶
媒である水で50%とした溶液を、シリコーンが原料粉
末に対して3%となるように加え、均一に練合しペース
トとする。ただし、結着剤の濃度は必要とするペースト
の粘度に応じて適度に変えることができる。A solution in which the binder silicone is made 50% with water as a solvent is added to the above raw material powder so that the silicone becomes 3% of the raw material powder, and the mixture is uniformly kneaded to form a paste. However, the concentration of the binder can be changed appropriately according to the required viscosity of the paste.
【0015】次に、得られたペーストをドクターブレー
ド法によって、鉛−スズ合金製で厚みが約50μmのシ
ート状芯材の両面に塗着した。この時の塗着量は、正極
では芯材1cm2当たり両面で理論容量30mAh、負
極では同じく40mAhの塗着量を基準とした。これら
の極板を80℃の温度調整した乾燥機内に2時間放置し
水を除去する。溶解していたシリコーンは析出硬化し活
物質原料粒子相互間および集電体と原料粒子間を結着し
ている。Next, the obtained paste was applied to both surfaces of a sheet-shaped core material made of a lead-tin alloy and having a thickness of about 50 μm by a doctor blade method. The coating amount at this time was based on a coating amount of 30 mAh of theoretical capacity on both sides per 1 cm 2 of the core material for the positive electrode and 40 mAh for the negative electrode. These electrodes are left in a dryer adjusted to a temperature of 80 ° C. for 2 hours to remove water. The dissolved silicone is precipitated and hardened and binds between the active material raw particles and between the current collector and the raw material particles.
【0016】これらの極板の断面図を図2(a)に、そ
して正面図を図2(b)に示す。ペースト1は導電性の
芯材2の全面に塗着するのではなく、図2に示すように
一部は芯材2を露出させておく。正極板および負極板の
露出部がお互いに軸方向に対し反対方向になるように捲
回した状態の極板群の軸方向の断面を図3に示す。FIG. 2A is a sectional view of these electrode plates, and FIG. 2B is a front view thereof. The paste 1 is not applied to the entire surface of the conductive core material 2, but partially exposes the core material 2 as shown in FIG. FIG. 3 shows an axial cross section of the electrode plate group in a state where the exposed portions of the positive electrode plate and the negative electrode plate are wound in directions opposite to each other with respect to the axial direction.
【0017】この正極3および負極板4を厚さ0.7m
mのガラスマットセパレーター5を介して捲芯6の周り
に渦巻き状に捲回し、円筒形の極板群を構成する。この
ように正、負極芯材のペーストを塗着してない部分をそ
れぞれ逆方向に向けセパレーターから露出させる。これ
は特表平5−503604号公報に記載されている手法
に準拠した。この時の極板群にかかる捲回圧力は50k
g/dm2に調整した。なお用いた正極シートは幅50
mm、長さ170mmで理論容量2.6Ah、負極シー
トは幅50mm、長さ220mm、理論容量4.4Ah
で、公称容量1.2Ahの正極容量制限電池となる。Each of the positive electrode 3 and the negative electrode plate 4 has a thickness of 0.7 m.
The glass plate is wound spirally around a winding core 6 via a glass mat separator 5 of m to form a cylindrical electrode group. In this way, the portions where the paste of the positive and negative electrode cores are not applied are respectively directed in opposite directions to be exposed from the separator. This was based on the method described in Japanese Patent Publication No. 5-503604. The winding pressure applied to the electrode plate group at this time is 50 k.
g / dm 2 . The used positive electrode sheet has a width of 50.
mm, length 170 mm, theoretical capacity 2.6 Ah, negative electrode sheet width 50 mm, length 220 mm, theoretical capacity 4.4 Ah
Thus, the positive electrode capacity-limited battery has a nominal capacity of 1.2 Ah.
【0018】密閉できる容器内に比重1.40の硫酸溶
液を入れ、上記発電部全体を硫酸水溶液につけ真空含浸
によって液を十分に含ませ、常圧にもどし、さらに10
分間含漬した。これを取り出し、40℃に温度調整した
乾燥機内に2時間放置する熟成工程によって熟成した。
活物質合剤はシリコーンによって物理的に決着すること
に加えて、熟成による造粒効果によってより強固に結着
した。A sulfuric acid solution having a specific gravity of 1.40 is placed in a sealable container, the entire power generation unit is immersed in a sulfuric acid aqueous solution, the liquid is sufficiently contained by vacuum impregnation, and the pressure is returned to normal pressure.
Impregnated for minutes. This was taken out and ripened by a ripening step in which it was left for 2 hours in a dryer adjusted to a temperature of 40 ° C.
The active material mixture was firmly bound by the granulation effect of aging, in addition to being physically settled by the silicone.
【0019】次に、集電板の取り付けであるが、露出さ
せている正負極の芯材部分に鉛製の集電板をスポット溶
接で取り付ける。この集電板7は図4に示すように、発
電部の両端を完全に覆ってしまわず、後で電解液を注入
するための隙間8と外部出力端子9を設けている。熟成
を終えた発電部をアクリル製の円筒形外装ケースに挿入
し、同じくアクリル製の中央に貫通孔をもつ円盤で円筒
外装ケースの両端に蓋をする。正極と負極の外部出力端
子はこの貫通孔からケース外に出す。尚、正負いずれか
の蓋には安全弁を取り付ける穴を設けておく。両出力端
子と蓋の貫通孔との隙間はエポキシ樹脂で埋める。Next, as for the mounting of the current collector, a current collector made of lead is mounted on the exposed core material portions of the positive and negative electrodes by spot welding. As shown in FIG. 4, the current collecting plate 7 does not completely cover both ends of the power generation unit, but has a gap 8 and an external output terminal 9 for injecting an electrolyte later. The aged power generation unit is inserted into an acrylic cylindrical outer case, and both ends of the cylindrical outer case are also covered with a disk made of acrylic and having a through hole in the center. The external output terminals of the positive electrode and the negative electrode are taken out of the case through the through holes. A hole for attaching a safety valve is provided in either the positive or negative lid. The gap between both output terminals and the through hole of the lid is filled with epoxy resin.
【0020】次に安全弁用に設けられた穴から、希硫酸
(比重1.15)を注入し、0.4Cの定電流で7時間
電槽化成を行った後、電池内の電解液を比重1.30の
希硫酸に置換し、安全弁を取り付けて密閉し、外形22
mm、高さ55mmの円筒形鉛蓄電池を作成した。Next, dilute sulfuric acid (specific gravity: 1.15) was injected through a hole provided for a safety valve, and a battery container was formed at a constant current of 0.4 C for 7 hours. Replace with 1.30 diluted sulfuric acid, attach a safety valve and seal tightly.
A cylindrical lead-acid battery having a height of 55 mm and a height of 55 mm was prepared.
【0021】比較のために、本実施例とは上記の熟成工
程を行わないこと以外は、全く同様の工程で試作した電
池を比較例1とした。また本実施例と同様の活物質原料
粉末を、結着剤を用いずに水だけで混練したスラリーを
用い本実施例と同様の工程で作成した電池を比較例2と
した。さらに比較例2と同様のスラリーを用い本熟成工
程を行わないこと以外は本実施例と同様の工法で作成し
た電池を比較例3とした。For comparison, a battery manufactured as a prototype in exactly the same steps as the present example except that the aging step was not performed was used as Comparative Example 1. A battery prepared in the same process as in this example using a slurry in which the same active material raw material powder as in this example was kneaded with only water without using a binder was used as Comparative Example 2. Further, a battery prepared in the same manner as in this example except that this aging step was not performed using the same slurry as in Comparative Example 2 was used as Comparative Example 3.
【0022】これらの電池をそれぞれ2Cの放電率で放
電した結果を図5に、5Cで放電した結果を図6に示
す。図から明らかなように本実施例の放電特性は、比較
例1、2および3に比べ大きく向上していることが分か
る。この理由は次のように考えられる。FIG. 5 shows the results of discharging these batteries at a discharge rate of 2C, and FIG. 6 shows the results of discharging them at 5C. As is clear from the figure, the discharge characteristics of the present example are significantly improved as compared with Comparative Examples 1, 2 and 3. The reason is considered as follows.
【0023】比較例1に比べ、本実施例では熟成工程を
行っているため、活物質同士がセメンテーションによっ
て強く結びつき導電ネットワークを形成しているため、
特に高率放電での特性が優れると思われる。次に、比較
例2では結着剤を用いてないために、熟成工程で鉛粉が
塩基性硫酸鉛あるいは硫酸鉛に変化する時の活物質膨張
によってストレスがかかり、芯材との結着性が失われ集
電能力がなく、また同じく結着剤を用いないために活物
質同士の結着性が悪く導電性がないためと思われる。さ
らに比較例3では、やはり結着剤がないために、芯材と
の結着性および活物質同士の結着性が悪い上、導電ネッ
トワークの形成が本実施例に比べ劣っているものと思わ
れる。Compared to Comparative Example 1, the aging step is performed in this example, and the active materials are strongly connected to each other by cementation to form a conductive network.
In particular, it seems that the characteristics at high rate discharge are excellent. Next, in Comparative Example 2, since no binder was used, stress was applied due to expansion of the active material when lead powder changed to basic lead sulfate or lead sulfate in the aging step, and the binding property with the core material was increased. It is thought that the active material was poor in binding property and no conductivity because no binder was used. Furthermore, in Comparative Example 3, since there is no binder, the binding property with the core material and the binding property between the active materials are poor, and the formation of the conductive network is considered to be inferior to that of the present example. It is.
【0024】さらに、サイクル寿命を評価するため、本
実施例と比較例1、2、3の電池をそれぞれ1Cで放電
を1.7Vになるまで行い、定電流定電圧(1C、2.
35V)で1.5時間充電を行う条件でサイクル特性を
調査した。サイクル寿命は放電容量が初期容量の50%
まで低下した時点を終点とした。その結果を表1に示
す。Further, in order to evaluate the cycle life, the batteries of this embodiment and Comparative Examples 1, 2, and 3 were each discharged at 1 C until the voltage reached 1.7 V, and the batteries were discharged at a constant current and a constant voltage (1 C, 2.
The cycle characteristics were examined under the condition of charging at 35 V) for 1.5 hours. The cycle life is that the discharge capacity is 50% of the initial capacity
The point when the temperature decreased to the end point was defined as the end point. Table 1 shows the results.
【0025】[0025]
【表1】 [Table 1]
【0026】表1から、本実施例の優位性は明らかであ
る。この原因も上記に述べたとおり、活物質同士の導電
ネットワークおよび芯材との結着性にあると思われる。
この中で比較例2の結果が特に悪いのは結着剤がないた
めに、電池完成前の熟成工程の段階で活物質と芯材との
脱離がおこったためと思われる。Table 1 clearly shows the superiority of this embodiment. It is considered that this is also due to the conductive network between the active materials and the binding property with the core material, as described above.
Among these, the reason why the result of Comparative Example 2 is particularly bad is considered to be that the active material and the core material were detached at the stage of the aging step before the completion of the battery because there was no binder.
【0027】一方、熟成の条件であるが、温度について
は40℃〜80℃の範囲であることが好ましい。この温
度以下では、長時間熟成しても活物質のセメンテーショ
ン効果が薄れ、かえって非常にもろい活物質層となって
しまい放電特性、サイクル特性ともに比較例に比べても
劣化してしまう。また、この温度以上で行うと放電容量
の劣化が著しいという結果が得られている。この理由は
おそらく、高温では4塩基性硫酸鉛が多く生成され、化
成時に放電反応に不利なαPb02が多くなるためと思
われる。On the other hand, under the aging conditions, the temperature is preferably in the range of 40 ° C. to 80 ° C. Below this temperature, the cementation effect of the active material is weakened even after aging for a long time, and the active material layer becomes rather brittle, and both the discharge characteristics and the cycle characteristics deteriorate as compared with the comparative example. Further, it has been found that when the temperature is higher than this temperature, the discharge capacity is significantly deteriorated. This is probably because a large amount of tetrabasic lead sulfate is generated at a high temperature, and αPb02, which is disadvantageous to the discharge reaction during chemical formation, increases.
【0028】本実施例では、極板を円筒形に巻いた電池
について主に説明したが、発電部の断面が楕円形もしく
は小判型に群構成した電池についても同様の結果が得ら
れている。また、極板が積層された角型電池であって
も、本実施例と同様の方法で極板を作成し、その後極板
を積層することにより同様の特性を持つ鉛蓄電池を製造
することができる。In the present embodiment, a battery in which the electrode plates are wound in a cylindrical shape is mainly described. However, similar results are obtained for batteries in which the cross section of the power generation unit is configured in an elliptical or oval shape. Further, even in the case of a prismatic battery in which electrode plates are stacked, it is possible to manufacture a lead storage battery having similar characteristics by creating an electrode plate in the same manner as in the present embodiment and thereafter stacking the electrode plates. it can.
【0029】[0029]
【発明の効果】以上詳述したように本発明によれば、優
れた高率放電特性とサイクル寿命とを兼ね備えた鉛蓄電
池を得ることが出来る。As described in detail above, according to the present invention, it is possible to obtain a lead-acid battery having excellent high-rate discharge characteristics and cycle life.
【図1】本発明の実施の形態による鉛蓄電池の製造フロ
ーを示す図FIG. 1 is a diagram showing a manufacturing flow of a lead storage battery according to an embodiment of the present invention.
【図2】本発明の一実施例による薄型極板を示す図FIG. 2 is a view showing a thin electrode plate according to an embodiment of the present invention;
【図3】本発明の一実施例による円筒形鉛蓄電池の極板
群の断面図FIG. 3 is a sectional view of an electrode group of a cylindrical lead-acid battery according to an embodiment of the present invention.
【図4】本発明の一実施例による円筒形鉛蓄電池の極板
群と出力端子の分解斜視図FIG. 4 is an exploded perspective view of an electrode group and an output terminal of a cylindrical lead-acid battery according to an embodiment of the present invention.
【図5】本発明の一実施例と比較例との放電特性を示す
図FIG. 5 is a diagram showing discharge characteristics of one example of the present invention and a comparative example.
【図6】本発明の一実施例と比較例との放電特性を示す
図FIG. 6 is a diagram showing discharge characteristics of one example of the present invention and a comparative example.
1 活物質層 2 シート状集電体 3 正極 4 負極 5 セパレーター 6 捲芯 7 集電体 8 隙間 9 外部出力端子 DESCRIPTION OF SYMBOLS 1 Active material layer 2 Sheet-shaped current collector 3 Positive electrode 4 Negative electrode 5 Separator 6 Core 7 Current collector 8 Gap 9 External output terminal
フロントページの続き Fターム(参考) 5H016 AA03 AA05 AA10 BB01 BB06 BB09 BB10 EE01 EE05 EE09 HH11 5H028 AA05 AA08 BB03 BB05 BB06 BB08 CC12 EE01 EE05 EE06 EE08 HH08 Continued on the front page F-term (reference)
Claims (3)
成分とする粉末材料と水溶性ケイ素系ポリマーシリコー
ンと水とを混練したペーストを導電性シートからなる芯
材に塗着して正極板を形成し、この正極板および負極板
とセパレーターとからなる極板群を希硫酸に浸漬した
後、極板群を熱処理することを特徴とする鉛蓄電池の製
造法。1. A paste obtained by kneading a mixture of lead and lead oxide or a powder material containing lead as a main component, a water-soluble silicon-based polymer silicone, and water on a core material made of a conductive sheet. A method for producing a lead-acid battery, comprising: forming a positive electrode plate; immersing an electrode plate group including the positive electrode plate, the negative electrode plate, and a separator in dilute sulfuric acid; and heat-treating the electrode plate group.
徴とする請求項1に記載の鉛蓄電池の製造法。2. The method according to claim 1, wherein the heat treatment is performed at 40 ° C. to 80 ° C.
ターを介してら旋状に捲回したことを特徴とする請求項
1あるいは2に記載の鉛蓄電池の製造法。3. The method for producing a lead-acid battery according to claim 1, wherein the electrode plate group is formed by spirally winding a positive electrode plate and a negative electrode plate via a separator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11166386A JP2000357532A (en) | 1999-06-14 | 1999-06-14 | Manufacturing method of lead storage battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11166386A JP2000357532A (en) | 1999-06-14 | 1999-06-14 | Manufacturing method of lead storage battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2000357532A true JP2000357532A (en) | 2000-12-26 |
Family
ID=15830467
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11166386A Pending JP2000357532A (en) | 1999-06-14 | 1999-06-14 | Manufacturing method of lead storage battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2000357532A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004047201A1 (en) * | 2002-11-15 | 2004-06-03 | Gs Yuasa Corporation | Positive plate for lead storage battery and lead storage battery |
JP2005317345A (en) * | 2004-04-28 | 2005-11-10 | Shin Kobe Electric Mach Co Ltd | Lead acid battery |
JP2005317501A (en) * | 2004-11-24 | 2005-11-10 | Shin Kobe Electric Mach Co Ltd | Engine drive system |
JP2006092749A (en) * | 2004-09-21 | 2006-04-06 | Shin Kobe Electric Mach Co Ltd | Method for producing positive active material for paste |
WO2013035387A1 (en) * | 2011-09-09 | 2013-03-14 | ファイラックインターナショナル株式会社 | Solid state secondary battery manufacturing method and solid state secondary battery based on the manufacturing method |
JP2023518236A (en) * | 2020-03-16 | 2023-04-28 | アドバンスト バッテリー コンセプツ エルエルシー | BATTERY ASSEMBLY, METHOD OF MAKING AND THERMAL CONTROL THEREOF |
-
1999
- 1999-06-14 JP JP11166386A patent/JP2000357532A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004047201A1 (en) * | 2002-11-15 | 2004-06-03 | Gs Yuasa Corporation | Positive plate for lead storage battery and lead storage battery |
JP2005317345A (en) * | 2004-04-28 | 2005-11-10 | Shin Kobe Electric Mach Co Ltd | Lead acid battery |
JP2006092749A (en) * | 2004-09-21 | 2006-04-06 | Shin Kobe Electric Mach Co Ltd | Method for producing positive active material for paste |
JP2005317501A (en) * | 2004-11-24 | 2005-11-10 | Shin Kobe Electric Mach Co Ltd | Engine drive system |
WO2013035387A1 (en) * | 2011-09-09 | 2013-03-14 | ファイラックインターナショナル株式会社 | Solid state secondary battery manufacturing method and solid state secondary battery based on the manufacturing method |
CN103000951A (en) * | 2011-09-09 | 2013-03-27 | 富爱乐国际有限公司 | Solid state secondary battery manufacturing method and solid state secondary battery based on the manufacturing method |
CN103000951B (en) * | 2011-09-09 | 2015-04-29 | 富爱乐国际有限公司 | Solid state secondary battery manufacturing method and solid state secondary battery based on the manufacturing method |
JP2023518236A (en) * | 2020-03-16 | 2023-04-28 | アドバンスト バッテリー コンセプツ エルエルシー | BATTERY ASSEMBLY, METHOD OF MAKING AND THERMAL CONTROL THEREOF |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP2001229920A (en) | Manufacturing method of sealed lead-acid battery | |
CN1163995C (en) | Alkaline energy storage battery electrode, production method and alkaline energy storage battery | |
JP2000357532A (en) | Manufacturing method of lead storage battery | |
JP2002141066A (en) | Control valve type lead storage battery | |
JP2003338310A (en) | Lead storage battery | |
JPH10261432A (en) | Manufacturing method of lead storage battery | |
JP4436464B2 (en) | Lithium ion battery | |
JP3903592B2 (en) | Lead acid battery | |
JP2008071717A (en) | Lead acid battery conversion method | |
JP3493900B2 (en) | Electrode plate for lead storage battery and method of manufacturing the same | |
JP3267075B2 (en) | Manufacturing method of electrode plate for lead-acid battery | |
JP4645039B2 (en) | Manufacturing method of cylindrical sealed lead-acid battery | |
JP2000348715A (en) | Manufacturing method of lead storage battery | |
JP3414941B2 (en) | Electrode plate for lead storage battery and method of manufacturing the same | |
JP2004055309A (en) | Method for producing paste-like active material for positive electrode and lead storage battery using the same | |
JP2004055417A (en) | Method for producing paste-like active material for positive electrode and lead storage battery using the same | |
JP4066509B2 (en) | Manufacturing method of lead acid battery | |
JPH0676815A (en) | Anode plate for lead acid battery and manufacturing method thereof | |
JP3284860B2 (en) | Electrode for lead-acid battery and its manufacturing method | |
JPH1040907A (en) | Manufacturing method of positive electrode plate for lead-acid battery | |
JPH1064530A (en) | Method for manufacturing electrode plate for lead-acid battery | |
JPH0410181B2 (en) | ||
JP4501246B2 (en) | Control valve type stationary lead acid battery manufacturing method | |
JP2773311B2 (en) | Manufacturing method of sealed lead-acid battery | |
JPH10223211A (en) | Lead-acid battery and manufacture therefor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |