JPH0654681B2 - Sealed lead acid battery - Google Patents
Sealed lead acid batteryInfo
- Publication number
- JPH0654681B2 JPH0654681B2 JP1130892A JP13089289A JPH0654681B2 JP H0654681 B2 JPH0654681 B2 JP H0654681B2 JP 1130892 A JP1130892 A JP 1130892A JP 13089289 A JP13089289 A JP 13089289A JP H0654681 B2 JPH0654681 B2 JP H0654681B2
- Authority
- JP
- Japan
- Prior art keywords
- battery
- plate
- cathode
- sealed lead
- separator
- 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.)
- Expired - Lifetime
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
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- Secondary Cells (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明は密閉形鉛蓄電池に係り、特に過充電寿命性能に
優れ、極板ピッチが一定である高特性密閉形鉛蓄電池に
関する。Description: TECHNICAL FIELD The present invention relates to a sealed lead acid battery, and more particularly to a high performance sealed lead acid battery having excellent overcharge life performance and a constant electrode plate pitch.
[従来の技術] 蓄電池の陽極の形式としては、従来よりペースト式極板
とクラッド式極板とが知られている。近年、蓄電池につ
いてその密閉化が試みられつつあり、ペースト式密閉電
池は極板間に平均直径2μm以下の微細ガラス繊維を主
体とするセパレータに流動する遊離した電解液が存在し
ないように吸収させて構成されている。[Prior Art] As a form of an anode of a storage battery, a paste type electrode plate and a clad type electrode plate have been conventionally known. In recent years, it has been attempted to hermetically seal a storage battery, and the paste-type hermetically sealed battery is made by absorbing free electrolytic solution flowing into a separator mainly composed of fine glass fibers having an average diameter of 2 μm or less between electrode plates. It is configured.
この密閉電池では、従来のものに比べ液重が少なくなる
ので電解液比重を高くしなければならない。その結果、
自己放電は増加傾向となり、それに加えて陰極活物質内
に不還元性硫酸鉛が生成されやすくなる。In this sealed battery, the liquid weight is smaller than that of the conventional battery, and therefore the specific gravity of the electrolyte must be increased. as a result,
Self-discharge tends to increase, and in addition, non-reducing lead sulfate is likely to be generated in the cathode active material.
このように、折角の高比重電解液の電池も製造後の在庫
期間,工場出荷後の輸送状況と保管状況,期間によっ
て、電池内の硫酸分は電池にとってなんの役にもたたな
い自己放電によって消耗し、この結果電池の開路電圧は
低下する。電池内部抵抗も次第に増加して来て、電池の
放電性能は低下傾向をたどる。In this way, even in the case of batteries with high specific gravity electrolyte, the sulfuric acid content in the battery is self-discharging, which is useless for the battery, depending on the stock period after manufacture, the transportation and storage conditions after shipment from the factory, and the period. Is consumed, and as a result, the open circuit voltage of the battery decreases. The internal resistance of the battery also gradually increases, and the discharge performance of the battery tends to decrease.
従って、電解液の比重を高くする事には限界があるの
で、できるだけ液量は多くしたい。また、電解液量を極
度に少なく抑えている為、極板とセパレータの接触が可
成りの緊圧度で接しておらないと、電池の充電・放電の
ときに必要なイオンの移動が電解液中を経由して十分出
来ない事になる。この恐れの為、緊圧度は強くするほう
が安全と必要以上に強くなり槽入れ組み立ての生産性は
悪くなり、しかも、セパレータにかかる緊圧度も極板・
セパレータの厚みのバラツキのこともあって、極板の局
部・局部の活物質面に対応したセパレータの多孔度も影
響を受けて、緊圧を強く受けたところは多孔度が小さく
なり、電解液の含み具合がまちまちになる。これは電池
の放電性能のバラツキを生ずる。Therefore, there is a limit to increasing the specific gravity of the electrolytic solution, so the amount of the liquid should be increased as much as possible. Also, since the amount of electrolyte is kept extremely low, if the electrode plate and separator do not come in contact with each other with a certain degree of tightness, the movement of ions necessary for battery charging / discharging will not occur. You will not be able to do enough through the inside. Because of this fear, it is safer to make the pressure tighter and it becomes stronger than necessary, resulting in poor productivity in the tank container assembly.
Due to the variation in the thickness of the separator, the porosity of the separator corresponding to the local and local active material surfaces of the electrode plate is also affected, and the porosity decreases where the pressure is applied strongly. The implications of are mixed up. This causes variations in the discharge performance of the battery.
陽極板の両面に接するセパレータには電池の放電・充電
の繰り返し使用に必要な電解液の入り込める十分な多孔
が均一に存在することが好ましい。It is preferable that the separators in contact with both sides of the anode plate are uniformly provided with sufficient porosity for allowing the electrolyte solution to be required for repeated use of discharging and charging the battery.
ところで、密閉形鉛蓄電池の場合、電池充電時、陽極板
から発生してくる酸素ガスを陰極活物質に化学反応によ
って吸収させるのが、活物質の表面に液膜が存在したの
では、実用になるような反応はおこらない。By the way, in the case of a sealed lead-acid battery, when the battery is charged, the oxygen gas generated from the anode plate is absorbed into the cathode active material by a chemical reaction. No reaction will occur.
陰極活物質表面の電解液の薄膜を透して陽極から発生し
た酸素ガスが陰極活物質と化学反応することが知られて
おり、この化学反応が主力反応となってガス吸収が進行
すると解釈される。しかし、本発明者の研究では、液膜
を透しての酸素ガスと陰極活物質との化学反応は極めて
スローモーションで、微量しか反応せず、主力反応とは
なり得ず、主力反応は、乾いたフレッシュな状態の陰極
活物質が適度の湿気を帯びた酸素ガスとが適度の温度雰
囲気中で出会って反応した時、急激におこるのである。It is known that the oxygen gas generated from the anode through the thin film of the electrolyte solution on the surface of the cathode active material chemically reacts with the cathode active material, and it is interpreted that this chemical reaction becomes the main reaction and gas absorption progresses. It However, in the study of the present inventor, the chemical reaction between the oxygen gas and the cathode active material through the liquid film is extremely slow motion, only a small amount reacts, it cannot be the main reaction, and the main reaction is This occurs rapidly when the dry and fresh cathode active material reacts with oxygen gas, which has an appropriate amount of moisture, in an atmosphere of an appropriate temperature to react.
また、密閉形鉛蓄電池では、電解液が制限され、自由電
解液を持たないため、過充電領域(水素ガス発生を抑制
する)での使用を避ける必要があり、主に温度範囲を限
定した定電圧充電方式を採用してきた。そのため、不適
切な温度、充電条件以外では、陰極板での酸素ガス吸収
能力以上の酸素ガスが発生蓄積して電池内圧が上昇す
る。この場合安全弁の作動と同時に、電池外部にガス並
に応々に電解液中の水分が電池外部に逸散して電解液が
減少する。更に、陽、陰極板の活物質表面と微細なガラ
ス繊維マットからなる隔離体との密着性低下による容量
低下を生じていた。従って、密閉形鉛蓄電池では、陰極
板での酸素ガス吸収能力が電池寿命の支配要因となり、
優れた寿命性能が得られないという欠点もある。Also, in sealed lead-acid batteries, the electrolytic solution is limited and does not have a free electrolytic solution, so it is necessary to avoid using it in the overcharge region (which suppresses hydrogen gas generation). It has adopted the voltage charging method. Therefore, under conditions other than inappropriate temperature and charging conditions, oxygen gas having a capacity higher than the oxygen gas absorption capacity of the cathode plate is generated and accumulated, and the internal pressure of the battery rises. In this case, at the same time as the operation of the safety valve, the moisture in the electrolytic solution diffuses to the outside of the battery as much as the gas, and the amount of the electrolytic solution decreases. In addition, the capacity of the positive and negative electrode plates was lowered due to the reduced adhesion between the surface of the active material and the separator made of a fine glass fiber mat. Therefore, in a sealed lead-acid battery, the oxygen gas absorption capacity at the cathode plate becomes the dominant factor in battery life,
There is also a drawback that excellent life performance cannot be obtained.
ところで、電解液中に極板群が浸漬された状態の鉛蓄電
池では、充電中の発熱は主として極板の充電が完了した
水の電気分解により酸素ガス、水素ガスが発生する反応
で起こる。しかし、稀硫酸を主成分とする電解液を使用
し、実質的に遊離の電解液が殆どない状態で、充電時に
陽極板から発生する酸素ガスと陰極板が反応する機構を
利用した密閉形鉛蓄電池においては、陽陰極から発生す
る酸素ガスが、陰極板と反応するときの発熱は大きい。
この反応は、完全に電解液に覆われた陰極板では起こり
難く、半乾燥状態の部分でよく起こるため、極板群の端
部陰極板の外側面において局部的に温度上昇が大きくな
り易い。このため、寸法調整として極板群に当接された
合成樹脂板や合成樹脂性電槽が変形したり破損したりす
ることがあるという欠点もある。By the way, in the lead storage battery in which the electrode plate group is immersed in the electrolytic solution, heat generation during charging mainly occurs due to a reaction in which oxygen gas and hydrogen gas are generated by electrolysis of water in which the electrode plate is completely charged. However, a sealed lead that uses a mechanism in which the oxygen gas generated from the anode plate and the cathode plate react during charging with an electrolyte containing dilute sulfuric acid as the main component and substantially no free electrolyte. In the storage battery, the oxygen gas generated from the positive and negative electrodes generates a large amount of heat when reacting with the cathode plate.
This reaction is unlikely to occur in the cathode plate completely covered with the electrolytic solution and often occurs in the semi-dried portion, so that the temperature rise tends to be locally large on the outer surface of the end cathode plate of the electrode plate group. For this reason, there is also a drawback that the synthetic resin plate or the synthetic resin battery case abutting on the electrode plate group may be deformed or damaged as a dimension adjustment.
このように、従来の密閉形鉛蓄電池では、 極板間隔が不揃いとなり易い。又、緊圧により電解
液の量が不足又不均一となりやすい。As described above, in the conventional sealed lead-acid battery, the electrode plate intervals are likely to be uneven. Moreover, the amount of the electrolytic solution tends to be insufficient or uneven due to the pressure.
陰極板の酸素吸収能力が電池寿命を支配するため、
寿命が短い。特に陰極板の表面を乾いた状態としにく
い。Since the oxygen absorption capacity of the cathode plate governs battery life,
Life is short. In particular, it is difficult to keep the surface of the cathode plate dry.
電池内の発熱により電槽が変形、破損することもあ
る。The battery case may be deformed and damaged due to the heat generated in the battery.
といった欠点があり、その解決が望まれていた。There is a drawback, and the solution is desired.
〜の問題点のうち、については、陰極板の外側に
特定の多孔板を設けることにより陰極板の酸素吸収能力
を向上させ、電池寿命を延長すうことが提案されている
(特開昭63−155259号)。しかしながら多孔板
の孔でない部分についての陰極板面積が活用されないと
の不満がある。With regard to the problems (1) to (4), it has been proposed that a specific porous plate be provided outside the cathode plate to improve the oxygen absorption capacity of the cathode plate and prolong the battery life (JP-A-63-63). 155259). However, there is a complaint that the cathode plate area for the non-hole portion of the perforated plate is not utilized.
また、については、孔径の小さい液吸収体を極板群の
外側に設けることにより、熱を吸収して電槽の変形や破
損を防ぐことが提案されている。(特開昭63−152
162号)。しかしながらこの方法では陰極板の表面を
乾いた状態にする事は難しい。With regard to the above, it is proposed that a liquid absorber having a small pore size is provided outside the electrode plate group to absorb heat and prevent deformation or damage of the battery case. (JP-A-63-152
162). However, it is difficult to make the surface of the cathode plate dry by this method.
[発明が解決しようとする課題] このように、上記〜の問題点を同時に解決し得る密
閉形鉛蓄電池は未だ提供されておらず、その改善が強く
望まれている。[Problems to be Solved by the Invention] As described above, a sealed lead-acid battery capable of simultaneously solving the above-mentioned problems (1) to (3) has not been provided yet, and improvement thereof is strongly desired.
本発明は上記従来の実情に鑑みてなされたものであっ
て、上記〜の問題点を同時に解決し得る、即ち、極
板ピッチが一定で、緊圧に耐え、過充電寿命性能に優
れ、陰極板の表面を乾いた状態としてガス吸収能力を高
め、しかも発熱による電槽の変形の問題もない高特性密
閉形鉛蓄電池を提供することを目的とする。The present invention has been made in view of the above-mentioned conventional circumstances, and can simultaneously solve the above-mentioned problems (1), that is, the electrode plate pitch is constant, withstands pressure, and is excellent in overcharge life performance. It is an object of the present invention to provide a high performance sealed lead acid battery in which the surface of the plate is in a dry state to enhance the gas absorption capacity and there is no problem of deformation of the battery case due to heat generation.
[課題を解決するための手段] 本発明の密閉形鉛蓄電池は、交互に配列された陽極板、
セパレータ及び陰極板を電槽内に備え、陽極板及び陰極
板よりなる極板群の両端部の極板は陰極板とされている
密閉形鉛蓄電池に関する。[Means for Solving the Problems] The sealed lead-acid battery of the present invention is a positive electrode plate which is alternately arranged,
The present invention relates to a sealed lead storage battery in which a separator and a cathode plate are provided in a battery case, and the electrode plates at both ends of an electrode plate group including the anode plate and the cathode plate are cathode plates.
本発明では、陽極板は、平均直径2μm以下のガラス繊
維を主体として構成され、かつ、耐酸性熱可塑性樹脂よ
りなるリブを内蔵するセパレータで被包されている。こ
れにより前記の問題が解決される。In the present invention, the anode plate is mainly composed of glass fibers having an average diameter of 2 μm or less, and is covered with a separator containing ribs made of an acid-resistant thermoplastic resin. This solves the above problem.
また、本発明では、前記極板群の両端部の陰極板の外側
面は平均13〜25μmのガラス繊維を有機系バインダ
で接着してなるシートで被われている。Further, in the present invention, the outer surface of the cathode plate at both ends of the electrode plate group is covered with a sheet obtained by bonding glass fibers having an average of 13 to 25 μm with an organic binder.
陽極板の両面のシートは電池が各種レートで放電をする
とき、十分に実力が発揮出来るように配慮したもので外
側面の活物質に乾きを生じさせて、酸素を吸収しやすく
させるためのものである。13〜25μmの太い繊維の
配列はマバラであり、陰極板の全面積が有効に働くので
前記の問題が解決され、又この層は断熱層となるので
前記の問題も解決される。The sheets on both sides of the anode plate are designed so that when the battery discharges at various rates, they will be able to exert their full potential, and to make the active material on the outside dry and to absorb oxygen easily. Is. The arrangement of thick fibers having a thickness of 13 to 25 μm is sparse, and the above-mentioned problem is solved because the entire area of the cathode plate works effectively, and this problem is also solved because this layer serves as a heat insulating layer.
以下、本発明につき図面を参照して更に詳細に説明す
る。Hereinafter, the present invention will be described in more detail with reference to the drawings.
第1図は本発明の実施例に係る密閉形鉛蓄電池を示す概
略断面図、第2図は本発明の密閉形鉛蓄電池に用いられ
るセパレータの一例を示す斜視図である。FIG. 1 is a schematic sectional view showing a sealed lead acid battery according to an embodiment of the present invention, and FIG. 2 is a perspective view showing an example of a separator used in the sealed lead acid battery of the present invention.
図示の如く、本発明の密閉形鉛蓄電池1は、電槽2内
に、交互に配列された陽極板3及び陰極板4と、セパレ
ータ5とを備える。陽極板3及び陰極板4よりなる極板
群(第1図においては2枚の陽極板3A、3Bと3枚の
陰極板4A、4B、4Cよりなる極板群)の両端部の極
板は陰極板4A、4Cとされている。陽極板3A、3B
は、それぞれ直径2μm以下のガラス繊維を主体として
構成され、耐酸性熱可塑性樹脂よりなるリブを内蔵する
セパレータ5A、5Bで被包されている。また、前記極
板群の両端部の陰極板4A、4Cの外側面は、それぞ
れ、直径13〜25μmのガラス繊維を有機系バインダ
で接着してなるシート6A、6Bで被われている。As shown in the figure, the sealed lead-acid battery 1 of the present invention is provided with an anode plate 3 and a cathode plate 4 and a separator 5 arranged alternately in a battery case 2. The electrode plates at both ends of an electrode plate group consisting of the anode plate 3 and the cathode plate 4 (in FIG. 1, an electrode plate group consisting of two anode plates 3A, 3B and three cathode plates 4A, 4B, 4C) are The cathode plates 4A and 4C are used. Anode plate 3A, 3B
Are mainly composed of glass fibers each having a diameter of 2 μm or less, and are covered with separators 5A and 5B containing ribs made of an acid-resistant thermoplastic resin. The outer surfaces of the cathode plates 4A and 4C at both ends of the electrode plate group are covered with sheets 6A and 6B formed by bonding glass fibers having a diameter of 13 to 25 μm with an organic binder.
第1図において、陽極板4を被包するセパレータ5は、
例えば、第2図に示す如く、平均直径2μm以下のガラ
ス繊維を主体として構成されたセパレータ本体7内に耐
酸性熱可塑性樹脂よりなるリブ8を内蔵するものであ
る。In FIG. 1, the separator 5 covering the anode plate 4 is
For example, as shown in FIG. 2, ribs 8 made of acid-resistant thermoplastic resin are built in a separator body 7 mainly composed of glass fibers having an average diameter of 2 μm or less.
第2図に示すセパレータ5は、セパレータ本体7の厚さ
方向と直交する方向であって、その長さ方向(図面にお
ける上下方向)に2本のリブ8が設けられているが、リ
ブの本数には特に制限はなく、3本或いは4本以上であ
っても良い。The separator 5 shown in FIG. 2 is provided with two ribs 8 in a direction orthogonal to the thickness direction of the separator body 7 and in the length direction (vertical direction in the drawing). There is no particular limitation on the number, and it may be three or four or more.
通常の場合、2本又は3本のリブを対称位置に設けるの
が好ましい。またその配設方向にも特に制限はないが、
セパレータ本体の厚さ方向のほぼ中心位置であって、電
池の正立方向(セパレータの長さ方向)とするのが好ま
しい。もちろん、リブは、セパレータの幅方向又は長さ
方向と交叉する斜め方向に設けることもできる。また、
リブは直線状に配置させなくても良く、セパレータ平面
内であれば、曲がっていても良い。Usually, it is preferable to provide two or three ribs at symmetrical positions. Also, there is no particular limitation on the arrangement direction,
It is preferable to set it at a substantially central position in the thickness direction of the separator body and in an upright direction of the battery (length direction of the separator). Of course, the ribs can be provided in an oblique direction that intersects the width direction or the length direction of the separator. Also,
The ribs do not have to be arranged linearly, and may be curved as long as they are in the plane of the separator.
一方、セパレータ本体7を構成するガラス繊維は、平均
直径2μm以下、好ましくは平均直径1μm以下のガラ
ス繊維を主体とするものである。On the other hand, the glass fibers constituting the separator body 7 are mainly glass fibers having an average diameter of 2 μm or less, preferably 1 μm or less.
このようなセパレータ5であれば、例えば、第3図に示
す装置を用い、次のようにして製造することができる。Such a separator 5 can be manufactured as follows, for example, using the apparatus shown in FIG.
即ち、ガラス繊維又は必要に応じて有機繊維を配合した
ガラス繊維20を抄紙タンク21より抄造用ネット22
上に供給して抄造する過程で、第3図のように、ノズル
23からホットメルト樹脂を熱溶解したもの24を幅方
向に所定間隔で帯状に流出して並列供給して、押えロー
ル25にて抄紙マット26中に埋め込む。抄造後は、例
えばドラムドライヤにて乾燥される。That is, the glass fiber 20 or the glass fiber 20 mixed with organic fiber as required is fed from the papermaking tank 21 to the papermaking net 22.
As shown in FIG. 3, in the process of supplying and papermaking to the above, hot melt resin 24 is melted from the nozzle 23 in a strip shape at predetermined intervals in the width direction and is supplied in parallel to the press roll 25. Embedded in the paper making mat 26. After the papermaking, it is dried by, for example, a drum dryer.
本発明において、セパレータの厚さは0.5〜3.5m
m程度、リブの厚さはセパレータの厚さの50〜95%
程度、その体積割合は1〜5%程度とするのが好まし
い。In the present invention, the thickness of the separator is 0.5 to 3.5 m.
m, rib thickness is 50 to 95% of separator thickness
The volume ratio is preferably about 1 to 5%.
なお、リブを形成する耐酸性熱可塑性樹脂としては粘度
が150〜200℃の溶解温度で1300ないし10,
000センチポイズで、常温でのショアー硬度70度以
上、好ましくは85度以上のホットメルト樹脂が好まし
い。このようなホットメルト樹脂の好ましい例として、
エチレン酢酸ビニル共重合樹脂(東洋インキ製「トプコ
H−017」)及びアタックティックポリプロピレン樹
脂の数種混合物を挙げることができる。The acid-resistant thermoplastic resin forming the ribs has a viscosity of 1300 to 10 at a melting temperature of 150 to 200 ° C.
A hot melt resin having a Shore hardness of 70 degrees or more, preferably 85 degrees or more at a room temperature of 000 centipoise is preferable. As a preferable example of such a hot melt resin,
Mention may be made of a mixture of ethylene vinyl acetate copolymer resin (“Topco H-017” manufactured by Toyo Ink) and several kinds of attack polypropylene resin.
ホットメルトは吐出ノズルの径を大きくしたり小さくし
たりして必要な直径のリブを容易に作り出す事ができ
る。With hot melt, the diameter of the discharge nozzle can be increased or decreased to easily create ribs with the required diameter.
一方、極板群の両端部の陰極板4A,4Cの外側面を被
覆するシート6A,6Bは、平均直径13〜25μmの
ガラス繊維を有機系バインダで接着してなるものであ
る。On the other hand, the sheets 6A and 6B covering the outer surfaces of the cathode plates 4A and 4C at both ends of the electrode plate group are formed by adhering glass fibers having an average diameter of 13 to 25 μm with an organic binder.
このシート6を構成するガラス繊維としては、特に平均
直径18μ〜22μ、繊維長さ6〜25mmの湿式法で
製造されたものでも、フエルト展綿法で得られる乾式法
のマットでもよい。また、用いられる有機系バインダと
してはアクリル系バインダ,コーンスターチ等が挙げら
れる。これらの有機系バインダの使用量はガラス繊維重
量の10〜25重量%であることが好ましい。The glass fiber constituting the sheet 6 may be a glass fiber manufactured by a wet method having an average diameter of 18 μm to 22 μm and a fiber length of 6 mm to 25 mm, or a dry mat obtained by a felt spreading method. Examples of the organic binder used include acrylic binder and corn starch. The amount of these organic binders used is preferably 10 to 25% by weight of the glass fiber weight.
また、本発明において、このシート6は、密度0.12
〜0.18g/cm3程度であることが好ましい。In the present invention, the sheet 6 has a density of 0.12.
It is preferably about 0.18 g / cm 3 .
このようなシートは、通常、厚さ0.3〜3.5mm程
度のガラスマットとするのが好ましい。Such a sheet is usually preferably a glass mat having a thickness of about 0.3 to 3.5 mm.
なお、第1図において、極板群の枚数は合計5枚として
あるが、実際の電池においては、陽板枚数+1枚=陰板
枚数を配設する。In FIG. 1, the total number of the electrode plates is five, but in the actual battery, the number of positive plates + 1 the number of negative plates is provided.
[作用] 本発明の密閉形鉛蓄電池において、陽極板を被包するセ
パレータは、平均直径2μm以下の細径ガラス繊維を主
体とするため、吸液率、保液量が高く、電池性能の向上
に有効である。しかも、リブを内蔵するため、耐圧迫力
が高く、セパレータ厚さを一定に保ち、従って、極板間
隔を一定に保つことができる。[Operation] In the sealed lead-acid battery of the present invention, since the separator enclosing the anode plate is mainly composed of thin glass fibers having an average diameter of 2 μm or less, the liquid absorption rate and the liquid retention amount are high, and the battery performance is improved. Is effective for. Moreover, since the ribs are built in, the pressure resistance is high, the separator thickness can be kept constant, and therefore the electrode plate spacing can be kept constant.
また、極板群の両端部の陰極板の外側綿を被覆するシー
トは、平均直径13〜25μmのガラス繊維を有機系バ
インダで接着してなる、保液率の非常に低い、かつ気孔
率の高いシートであるため、陰極板の外側面全面を被う
ことなく、また、このシートが接する陰極板面は電解液
で濡れることも少なく、所々乾いている状態であるた
め、陰極板表面の活用化率を高めることができる。従っ
て、陰極板の酸素吸収能力が向上され、電池寿命が延長
される。Further, the sheet covering the outer side cotton of the cathode plate at both ends of the electrode plate group is formed by adhering glass fibers having an average diameter of 13 to 25 μm with an organic binder and has a very low liquid retention rate and porosity. Because it is a high sheet, it does not cover the entire outer surface of the cathode plate, and the cathode plate surface that this sheet is in contact with is not likely to get wet with the electrolyte, and it is in a dry state in some places, so the cathode plate surface can be used The conversion rate can be increased. Therefore, the oxygen absorption capacity of the cathode plate is improved, and the battery life is extended.
更に、このシート及びシート中の電解液による断熱効果
で電槽等の熱変形等も防止される。Further, the sheet and the electrolytic solution in the sheet can prevent thermal deformation of the battery case due to the heat insulating effect.
[実施例] 以下、実施例及び比較例について説明する。[Examples] Examples and comparative examples will be described below.
実施例1 陽極板3、陰極板4、セパレータ5及びシート6とし
て、下記のものを用い、第1図に示す密閉形鉛蓄電池
(6V×6AH)を組立てた。Example 1 The following were used as the anode plate 3, the cathode plate 4, the separator 5 and the sheet 6, and the sealed lead-acid battery (6V × 6AH) shown in FIG. 1 was assembled.
陽極板 3枚/単セル 幅 =43 mm 厚さ=3.4mm 長さ=64 mm 陰極板 4枚/単セル 幅 =43 mm 厚さ=2.4mm 長さ=64 mm セパレータ 幅 = 53mm 厚さ=2.0mm 長さ=144mm 平均直径0.8μmのガラス繊維よりなり、第2図に示
す如く、直径1.85mmの2本のリブ(東洋インキ製
「トプコH−017」)を内蔵するもの。密度0.14
g/cm3 シート 幅 = 53mm 厚さ=0.5mm 長さ= 62mm 平均直径19μmのガラス繊維を15重量%のアクリル
樹脂で接着したガラスマット。密度0.14g/cm3 得られた密閉形鉛蓄電池について、極板間隔のバラツ
キ、過充電寿命特性等を調べ、結果を第1表、第4図、
第5図に示した。Anode plate 3 sheets / single cell width = 43 mm Thickness = 3.4 mm Length = 64 mm Cathode plate 4 sheets / single cell width = 43 mm Thickness = 2.4 mm Length = 64 mm Separator width = 53 mm Thickness = 2.0 mm Length = 144 mm Made of glass fiber with an average diameter of 0.8 μm, and as shown in FIG. 2, incorporates two ribs with a diameter of 1.85 mm (“Topco H-017” manufactured by Toyo Ink). . Density 0.14
g / cm 3 sheet Width = 53 mm Thickness = 0.5 mm Length = 62 mm A glass mat in which glass fibers having an average diameter of 19 μm are bonded with an acrylic resin of 15% by weight. With respect to the sealed lead-acid battery having a density of 0.14 g / cm 3 , variations in electrode plate intervals, overcharge life characteristics, etc. were examined, and the results are shown in Table 1 and FIG.
It is shown in FIG.
比較例1 セパレータとしてリブのないものを用い、またシートを
配設しなかったこと以外は実施例1と同様にして密閉形
鉛蓄電池を組立て、得られた密閉形鉛蓄電池について、
比較し結果を第1表、第4図、第5図に示した。Comparative Example 1 A sealed lead acid battery was assembled in the same manner as in Example 1 except that a separator having no ribs was used and no sheet was provided.
The comparison results are shown in Table 1, FIG. 4 and FIG.
第4図及び第5図は約60ケ月弱の過充電テストを常温
環境下で行った結果である(図中、温度は室温を示
す。)これを日本蓄電池工業会規格(SBA3018過
充電寿命による総過充電量(AH))に準じて計算する
と(C20;20時間率容量)、 実施例1:0.00025C20×24h/日×30月/月当り×60月
= 10.8C20以上 比較例1:0.00025C20×24h/日×30月/月当り×40月
=7.2C20 という数値に実験結果は括められ、実施例1の過充電寿
命性能は格段に改良された。 Figures 4 and 5 show the results of an overcharge test of about 60 months under normal temperature environment (in the figure, temperature indicates room temperature). This is based on the Japan Storage Battery Industry Association standard (SBA3018 overcharge life). When calculated according to the total overcharge (AH) (C 20 ; 20 hour rate capacity), Example 1: 0.00025C 20 × 24h / day × 30 months / month × 60 months = 10.8C 20 or more Comparative Example The experimental result was summarized in the numerical value of 1: 0.00025C 20 × 24 h / day × 30 months / month × 40 months = 7.2 C 20, and the overcharge life performance of Example 1 was remarkably improved.
第1表、第4図、第5図より明らかなように、本発明に
よれば、極板間隔のバラツキが低減され、極板間隔がほ
ぼ一定となる上に、過充電寿命性能が大幅に向上した。As is clear from Table 1, FIG. 4 and FIG. 5, according to the present invention, variations in electrode plate spacing are reduced, the electrode plate spacing becomes almost constant, and overcharge life performance is significantly improved. Improved.
[発明の効果] 以上詳述した通り、本発明の密閉形鉛蓄電池によれば、
極板間隔が一定で、従って、電池性能に優れた密閉形鉛
蓄電池であって、その過充電寿命が著しく長い、優れた
特性を有する密閉形鉛蓄電池が提供される。[Effects of the Invention] As described in detail above, according to the sealed lead-acid battery of the present invention,
Provided is a sealed lead acid battery having a constant electrode plate spacing and therefore excellent battery performance, and having excellent characteristics in which the overcharge life thereof is remarkably long.
第1図は本発明の実施例に係る密閉形鉛蓄電池を示す概
略断面図、第2図は本発明に用いられるセパレータの一
例を示す斜視図、第3図は本発明のセパレータを製造す
るに好適な装置の概略的な側面図、第4図は実施例1の
過充電寿命測定結果を示す図、第5図は比較例1の過充
電寿命測定結果を示す図である。 1……密閉形鉛蓄電池、2……電槽、 3……陽極板、4……陰極板、 5……セパレータ、6……シート。1 is a schematic cross-sectional view showing a sealed lead-acid battery according to an embodiment of the present invention, FIG. 2 is a perspective view showing an example of a separator used in the present invention, and FIG. 3 is a view showing a separator of the present invention. FIG. 4 is a schematic side view of a suitable apparatus, FIG. 4 is a diagram showing the result of measuring the overcharge life of Example 1, and FIG. 5 is a diagram showing the result of measuring the overcharge life of Comparative Example 1. 1 ... Sealed lead acid battery, 2 ... Battery case, 3 ... Anode plate, 4 ... Cathode plate, 5 ... Separator, 6 ... Sheet.
Claims (1)
陰極板を電槽内に備え、陽極板及び陰極板よりなる極板
群の両端部の極板は陰極板とされている密閉形鉛蓄電池
において、 平均直径2μm以下のガラス繊維を主体として構成さ
れ、かつ、耐酸性熱可塑性樹脂よりなるリブを内蔵する
セパレータで前記陽極板が被包されると共に、 平均直径13〜25μmのガラス繊維を有機系バインダ
で接着してなるシートで前記極板群の両端部の陰極板の
外側面が被われていることを特徴とする密閉形鉛蓄電
池。1. A sealed lead in which an anode plate, separators and cathode plates arranged alternately are provided in a battery case, and the electrode plates at both ends of an electrode plate group consisting of the anode plate and the cathode plate are cathode plates. In a storage battery, the anode plate is encapsulated by a separator mainly composed of glass fibers having an average diameter of 2 μm or less and having ribs made of an acid-resistant thermoplastic resin, and glass fibers having an average diameter of 13 to 25 μm. A sealed lead acid battery, characterized in that the outer surface of the cathode plate at both ends of the electrode plate group is covered with a sheet bonded with an organic binder.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1130892A JPH0654681B2 (en) | 1989-05-24 | 1989-05-24 | Sealed lead acid battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1130892A JPH0654681B2 (en) | 1989-05-24 | 1989-05-24 | Sealed lead acid battery |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02309567A JPH02309567A (en) | 1990-12-25 |
JPH0654681B2 true JPH0654681B2 (en) | 1994-07-20 |
Family
ID=15045154
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1130892A Expired - Lifetime JPH0654681B2 (en) | 1989-05-24 | 1989-05-24 | Sealed lead acid battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0654681B2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04296464A (en) * | 1991-03-26 | 1992-10-20 | Shin Kobe Electric Mach Co Ltd | Sealed-type lead-acid battery |
-
1989
- 1989-05-24 JP JP1130892A patent/JPH0654681B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPH02309567A (en) | 1990-12-25 |
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