JP3388265B2 - Lead-acid battery separator - Google Patents
Lead-acid battery separatorInfo
- Publication number
- JP3388265B2 JP3388265B2 JP10364193A JP10364193A JP3388265B2 JP 3388265 B2 JP3388265 B2 JP 3388265B2 JP 10364193 A JP10364193 A JP 10364193A JP 10364193 A JP10364193 A JP 10364193A JP 3388265 B2 JP3388265 B2 JP 3388265B2
- Authority
- JP
- Japan
- Prior art keywords
- battery
- separator
- lead
- acid
- silica powder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000002253 acid Substances 0.000 title claims description 30
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 51
- 239000000843 powder Substances 0.000 claims description 38
- 239000000377 silicon dioxide Substances 0.000 claims description 24
- 239000003365 glass fiber Substances 0.000 claims description 7
- 239000011230 binding agent Substances 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 4
- 229920003002 synthetic resin Polymers 0.000 claims 1
- 239000000057 synthetic resin Substances 0.000 claims 1
- 239000003792 electrolyte Substances 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 10
- 239000011521 glass Substances 0.000 description 8
- -1 Polypropylene Polymers 0.000 description 7
- 239000004743 Polypropylene Substances 0.000 description 7
- 229920001155 polypropylene Polymers 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- 229920002994 synthetic fiber Polymers 0.000 description 6
- 239000012209 synthetic fiber Substances 0.000 description 6
- 229910000978 Pb alloy Inorganic materials 0.000 description 5
- 238000003860 storage Methods 0.000 description 4
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- 239000011812 mixed powder Substances 0.000 description 3
- 239000011164 primary particle Substances 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 239000005909 Kieselgur Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000002003 electrode paste Substances 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- 239000011163 secondary particle Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000004931 aggregating effect Effects 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000008119 colloidal silica Substances 0.000 description 1
- 239000013065 commercial product Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011245 gel electrolyte Substances 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- 239000002142 lead-calcium alloy Substances 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
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
Landscapes
- Cell Separators (AREA)
- Secondary Cells (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は鉛蓄電池用セパレータの
改良に関するものである。
【0002】
【従来の技術】電池の充電中に発生する酸素ガスを負極
で吸収するいわゆる酸素サイクルを利用した密閉形鉛蓄
電池には、リテ−ナ式とゲル式の二種類がある。リテ−
ナ式は正極板と負極板との間に挿入した微細なガラス繊
維を素材とするマット状セパレ−タ(ガラスセパレ−
タ)で電池の充放電に必要な硫酸電解液の保持と両極の
隔離を行っており、無保守、無漏液、ポジションフリ−
などの特徴を生かして、近年ポ−タブル機器、コ−ドレ
ス機器、コンピュ−タ−のバックアップ電源をはじめ、
大型の据置用電池や自動車のエンジン始動用にも使用さ
れるようになってきた。
【0003】しかしガラスセパレ−タは特殊な方法で製
造される直径1ミクロン前後の極細ガラス繊維を抄造し
てマット状としたもので、一般的に用いられている鉛蓄
電池用のセパレ−タに比してかなり高価なことや、目標
の電池性能を得るためには極板群を強く圧迫して電槽内
に組み込まなければならないので極板群の電槽への挿入
が困難なため電池の組立に手数がかかり、必然的に電池
の製造コストが高くなるという欠点があった。また、リ
テ−ナ式密閉形鉛蓄電池は、ガラスセパレ−タに保持で
きる硫酸電解液が少なく、電解液が豊富に存在する開放
形の一般的な鉛蓄電池に比べると電池容量、とくに低率
放電容量が劣るという欠点があった。
【0004】そこで、極間を広くして厚みの大きいガラ
スセパレータを用いて、できるだけ多くの電解液をガラ
スセパレータに保持させて放電容量の改善を図ろうとす
ると、電池の内部抵抗が大きくなって放電時の電圧特性
が悪くなり、逆に、電圧特性を良くするために薄いガラ
スセパレータを使用すると、放電に必要な電解液を確保
できなくなる上に、ガラスセパレータは多孔度が大き
く、孔径も大きいため、セパレータの貫通ショートが起
こりやすく短寿命であるという問題があった。
【0005】一方、ゲル式は硫酸電解液をコロイド状シ
リカや水ガラスによってゲル化した密閉形鉛蓄電池であ
るが、硫酸が離しょうして漏液したり、ゲル中での硫酸
イオンの移動度が悪いために電池性能が劣り、さらにゲ
ル状電解液は正極で発生した酸素ガスが負極に到達する
ためのガス通路がないために、電池の充放電を繰り返し
て水分解を起こさせてゲルに亀裂が入るまで負極におけ
る酸素吸収反応が起こらないなどの欠点があった。
【0006】そこで上記従来形の密閉形鉛蓄電池の欠点
を解消する目的で、微細なシリカ粉体を凝集させて造粒
した顆粒状シリカ粉体を電解液保持体とするリテーナ式
でもなくゲル式でもない密閉形鉛蓄電池が提案されてい
る。これは含水二酸化珪素の微細な一次粒子が凝集して
形成される粗大な二次粒子粉体(以下シリカ粉体と略
す)を正、負極板間および極板群の周囲に充填した構成
の新規な密閉形鉛蓄電池で、電池の放電容量が電解液量
で制限されることのない充分な電解液を前記粉体に含浸
保持させることが可能になり、また極板を取り巻く粉体
層が充放電にともなう活物質の変形を防止するために、
密閉形鉛蓄電池の初期性能や寿命性能を大幅に改善する
ことが可能になった。
【0007】
【発明が解決しようとする課題】ところが上述した新規
な密閉形鉛蓄電池にも種々の解決しなければならない問
題点があった。すなわち、この新規な密閉形鉛蓄電池で
は期待される電池性能を得るためには、シリカ粉体を
正、負極極間に均一な厚みで密に充填しなければならな
い。このために例えば特開平第2−165570号公報
に記載されているような一定厚みの隔離体を使用した
り、特開平第4−51470号公報に記載されているよ
うなリブつきの薄いセパレータを使用して正、負極板の
間隙を一定に保つように組み立てた電池に振動を加えな
がらシリカ粉体を極間および極板群の周囲に充填するわ
けであるが、非常に狭い極板間に一定厚みの粉体層を形
成するのは非常に難しいことであった。
【0008】一定厚みの隔離体を使用した前者の例で
は、極板自身がかならずしも平坦でなく曲がりや反りが
あるために、場所によっては極間が広いところや狭いと
ころが生じ、とくに極間の狭いところでは短絡が起こる
危険性があった。そのため安全性を考慮すれば必然的に
極間を大きくしなければならず、極間を大きくすると内
部抵抗が大きくなって高率放電性能の良い電池を作るこ
とはできなかった。
【0009】一方、後者の例のようにリブつきのセパレ
ータを使用する場合においても、セパレータの抵抗に粉
体層の抵抗が加わってとくに高率放電時の電圧特性が悪
くなる欠点があった。
【0010】また、シリカ粉体の充填が不十分な場合
は、期待通りの電池性能が得られないという致命的な欠
点があり、いずれの場合も極板群の製造に特別な装置が
必要となるうえに、狭い極間に粉体を充填するのに長時
間を要すという電池製造上の大きな問題があった。
【0011】
【課題を解決するための手段】本発明は、上述した新規
な密閉形鉛蓄電池の欠点を解決したもので、その要旨は
ポリフルオロポリマーをバインダーとしてシリカ粉体と
を結合し、さらにシリカ粉体重量の0.5 〜5 重量%の耐
酸性合成繊維またはガラス繊維を添加したことを特徴と
する鉛蓄電池用セパレータを用いることにある。
【0012】
【作用】本発明鉛蓄電池用セパレータは、これを構成す
る粉体を電解液保持体とするものであるが、粉体および
添加繊維はバインダーで結合され弾性を有するシート状
となっているので、従来のシート状セパレータを用いる
のと同様にして電池を組み立てることができ、電池の生
産性がよくなり、また、極板間隔も一定となるため短絡
の危険性がなくなる。さらに、極板間には粉体の層のみ
であるから無駄な抵抗も生じず、本発明セパレータを用
いれば、初期および寿命性能に優れた電池が得られる。
その上、本発明セパレータは耐酸性合成繊維またはガラ
ス繊維の添加によりセパレータの機械的強度および柔軟
性が向上し、電池組立時の作業をより一層容易にすると
ともに組立の多様性が可能となる利点がある。
【0013】
【実施例】本発明による鉛蓄電池用セパレータは次のよ
うにして作製した。
【0014】まず、一次粒子が10〜40nmの微細な
一次粒子が凝集して50〜400μmの粗大な二次粒子
を形成する比表面積180〜250m2 /gの顆粒状シ
リカ粉体を準備した。この顆粒状シリカ粉体にはシリカ
ゾルを噴霧乾燥して製造した市販品を用いた。
【0015】上記顆粒シリカ粉体に添加した合成繊維の
添加量を変えて表1に示す6種類の混合粉体を作製し
た。なお、ここで用いた合成繊維には長さ3mmにカツト
した太さ約20μmのポリブロピレン(P.P.)繊維を
用いた。
【0016】
【表1】
【0017】つぎに、この混合粉体100gを混練機に
入れ、ポリフルオロポリマーとしてポリテトラフルオロ
エチレン(PTFE)を用い、これを30重量%を含む
水性の懸濁液20gに水300g加えて希釈し、これを
混練機内の混合粉体に加えて充分に混練した。
【0018】練り始めは混練機内の内容物は比較的粘り
気はないが、やがてゴム弾性を呈するようになる。この
ような状態になれば内容物を取りだし、一対のロールを
通して厚さ1.00mmのシートに成形し、40〜50
℃で乾燥すれば比較的強度がありクッション性も備える
シートが得られた。これを所定の寸法に切断してセパレ
ータを作製した。
【0019】このようにして作製したセパレータの密度
は0. 33〜0. 36g/cm3 であって、多孔度は約
85〜87%であった。この多孔度は加える水や混練の
程度、ロールを通す際のプレスの程度などである程度コ
ントロールが可能であって、多孔度をさらに向上するこ
とも可能であった。
【0020】上述した鉛電池用セパレータの引張り強度
をJIS C 2313(鉛蓄電池用隔離板)7.2.
3項の引張り強度試験に準じて測定した結果を図2に示
す。図2における添字は表1中のNo.を示す。
【0021】図2からわかるようにポリプロピレンの添
加によりセパレーターの強度は大幅に増加することがわ
かる。また、添加量は最低0. 5%は必要で、これより
少なくては添加した効果が見いだしがたく、さらに添加
量5%で引張り強度はほぼ一定となり、これ以上添加し
てもセパレータの引張り強度の増加につながらないこと
がわかる。
【0022】また、上記セパレータ(1〜6)を用いて
実際の鉛蓄電池のセパレータとして組立てたところ、セ
パレータNo. 1、2ではセパレータの強度が不充分の
ため図3のような形でしか組立てられなかったが、セパ
レータNo3〜6はセパレータの強度が強くかつ柔軟性
を有するため、図4のような波形で組立てることも可能
であった。
【0023】さらに上述した鉛蓄電池用セパレータを用
いて電池No.1〜6をそれぞれ組み立て、性能を調べ
た。図1は表1に示した鉛蓄電池用セパレータを用いた
密閉形鉛蓄電池の要部断面図で、(A)は正面図、
(B)は側面図である。
【0024】まず、正極板1および負極板2および表1
に示したセパレータ3とを組み合わせて極板群を作製し
た。極板群の製造には特別な装置を必要とせず、従来の
組み立て装置がそのまま使用できた。
【0025】次に作製した極板群を電槽4内に挿入した
のち、セパレータ3を作製するのに用いたものと同じ特
性のシリカ粉体6を極板群の周囲に充填した。極板群の
電槽への挿入は極板群にさほど圧迫をかける必要がない
のできわめて容易であった。
【0026】また、本発明ではシリカ粉体を極板群の周
囲に充填するだけでよいので、粉体の充填に要する時間
はわずか1分程度と粉体の充填時間は大幅に短縮するこ
とができた。
【0027】粉体の充填が終了した電池は粉体層6の上
部に連続気泡のフェノール樹脂発泡体のブロック7を詰
めて粉体層6を固定した。電槽ふた5を電槽4に溶着、
液口から所定量の硫酸電解液を注液、排気弁8を装着、
さらに充電を行って容量約30Ahの12V電池を完成
させた。
【0028】なお、正極板1にはアンチモンフリーの鉛
合金からなる鋳造格子に正極ペーストを充填したものを
用いた。アンチモンフリーの鉛合金としては、0.05〜0.
12wt%Ca、0.2 〜1.0 wt%Snを含む一般的な鉛カルシウ
ム系合金が使用できる。
【0029】負極板2はアンチモンフリーの鉛合金を用
いた鋳造格子にリグニンや硫酸バリウムなどの防縮剤を
添加した通常の負極ペーストを充填して製造した。負極
格子の鉛合金は0.05〜0.12wt%Ca、0.001 〜0.5 wt%Sn
を含む一般的な鉛カルシウム系合金が使用できる。
【0030】本実施例では正極および負極に鋳造格子を
使用したが、鉛合金シートを展開したエキスパンド格子
あるいは打ち抜き格子などいずれも使用可能である。ま
た、蓄電池ペーストを充填した極板は30〜80℃の部屋で
熟成してから使用する。とくに、正極板の熟成は電池性
能上重要な工程である。
【0031】つぎに本発明による密閉形鉛蓄電池を25
℃における6A(0.2C)放電、その後JIS規格に
準拠して寿命試験(放電:20A×1h、充電:5A×
5h、温度:40℃)を行った。結果を表2に示す。
【0032】
【表2】【0033】表2より、本発明品の電池No. 3〜5は
放電容量、寿命サイクル数ともにポリプロピレンのまっ
たく添加のない電池No. 1優れていることがわかっ
た。ポリプロピレンを10%添加した電池No. 6は放
電容量、寿命サイクル数ともによくなかった。この原因
は、ポリプロピレンをシリカ粉末中に10%も添加する
と、シリカ粉末の本来の目的である電解液保持特性を妨
げるためと考えられる。
【0034】なお、シリカ粉体中に混入する繊維として
本実施例では、ポリプロピレンを用いたが、ポリエステ
ル、ポリアクリロニトリル等の耐酸性合成繊維またはガ
ラス繊維でも充分な効果がある。さらに、電解液保持材
としてシリカ粉体の代わりにケイソウ土またはケイソウ
土とシリカ粉体との混合物を用いても同様な効果があ
る。
【0035】
【発明の効果】以上詳述したように本発明によれば、ポ
リフルオロポリマーをバインダーとしてシリカ粉体を結
合し、さらにシリカ粉体中に合成繊維またはガラス繊維
を添加することでセパレータの引張り強度を向上させる
のに効果があり、さらに本発明セパレーターを鉛蓄電池
に用いることで新規な密閉形鉛蓄電池が簡単に製造でき
るようになり、そのうえ初期および寿命性能を大幅に改
善することが可能になった。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in a separator for a lead-acid battery. 2. Description of the Related Art There are two types of sealed lead-acid batteries using a so-called oxygen cycle in which oxygen gas generated during charging of a battery is absorbed by a negative electrode, of a retainer type and a gel type. Rete
The mat type separator made of fine glass fiber inserted between the positive electrode plate and the negative electrode plate (glass separator)
(2) to maintain the sulfuric acid electrolyte necessary for charging and discharging the battery and to separate the two electrodes.
Taking advantage of such features as portable power equipment, cordless equipment, and computer backup power supplies in recent years,
It has also been used for large stationary batteries and for starting automobile engines. [0003] However, the glass separator is made by forming a very fine glass fiber having a diameter of about 1 micron manufactured by a special method into a mat shape, and is compared with a separator commonly used for lead-acid batteries. In order to obtain the target battery performance, the electrode group must be strongly pressed and assembled into the battery case, and it is difficult to insert the electrode group into the battery case. This requires a lot of trouble, and inevitably increases the manufacturing cost of the battery. In addition, the closed-type lead-acid storage battery has a small amount of sulfuric acid electrolyte that can be held in the glass separator, and has a lower battery capacity, especially low-rate discharge capacity, than an open-type general lead-acid storage battery with abundant electrolyte. Was inferior. [0004] In order to improve the discharge capacity by using a glass separator having a large gap and a large thickness to hold as much electrolyte as possible on the glass separator, the internal resistance of the battery becomes large and the discharge capacity increases. When a thin glass separator is used to improve the voltage characteristics, on the contrary, when the thin glass separator is used, the electrolyte required for discharging cannot be secured, and the glass separator has a large porosity and a large pore diameter. In addition, there is a problem that a short circuit is likely to occur in the separator and the life is short. On the other hand, the gel type is a sealed lead-acid battery in which a sulfuric acid electrolyte is gelled with colloidal silica or water glass. However, the sulfuric acid separates and leaks, and the mobility of sulfate ions in the gel is reduced. The battery performance is poor due to poor battery performance, and the gel electrolyte has no gas passage for the oxygen gas generated at the positive electrode to reach the negative electrode. There was a drawback that the oxygen absorption reaction in the negative electrode did not occur until cracks were formed. Therefore, in order to solve the above-mentioned drawbacks of the conventional sealed lead-acid battery, a granular silica powder obtained by aggregating and granulating fine silica powder is used not as a retainer type but as a gel type rather than a retainer type. However, a sealed lead-acid battery has been proposed. This is a new configuration in which coarse secondary particle powder (hereinafter abbreviated as silica powder) formed by agglomeration of fine primary particles of hydrous silicon dioxide is filled between positive and negative electrode plates and around the electrode plate group. In a sealed lead-acid battery, it is possible to impregnate the powder with a sufficient amount of electrolyte so that the discharge capacity of the battery is not limited by the amount of electrolyte, and to fill the powder layer surrounding the electrode plate. To prevent deformation of the active material due to discharge,
It has become possible to significantly improve the initial performance and life performance of sealed lead-acid batteries. [0007] However, the above-mentioned novel sealed lead-acid battery has various problems that must be solved. That is, in order to obtain the expected battery performance of this new sealed lead-acid battery, the silica powder must be densely packed with a uniform thickness between the positive and negative electrodes. For this purpose, for example, a separator having a constant thickness as described in JP-A-2-165570 or a thin separator with a rib as described in JP-A-4-51470 is used. The silica powder is filled between the electrodes and around the electrode group while applying vibration to the battery assembled so that the gap between the positive and negative electrode plates is kept constant. It was very difficult to form a thick powder layer. In the former example using a separator having a constant thickness, the pole plate itself is not necessarily flat, but is bent or warped. By the way, there was a risk of a short circuit occurring. Therefore, in consideration of safety, the gap must be increased inevitably. If the gap is increased, the internal resistance increases and it is not possible to manufacture a battery having good high-rate discharge performance. On the other hand, when a separator with ribs is used as in the latter example, there is a disadvantage that the resistance of the powder layer is added to the resistance of the separator, and the voltage characteristics particularly during high-rate discharge are deteriorated. In addition, when the silica powder is not sufficiently filled, there is a fatal drawback that the expected battery performance cannot be obtained. In any case, a special apparatus is required for manufacturing the electrode group. In addition, there is a major problem in battery production that it takes a long time to fill the powder between the narrow poles. SUMMARY OF THE INVENTION The present invention has solved the above-mentioned drawbacks of the novel sealed lead-acid battery. The gist of the present invention is to combine a polyfluoropolymer as a binder with silica powder. It is an object of the present invention to use a separator for a lead-acid battery, wherein acid-resistant synthetic fibers or glass fibers are added in an amount of 0.5 to 5% by weight of the silica powder. The separator for a lead-acid battery according to the present invention uses the powder constituting the separator as an electrolyte holder, but the powder and the added fibers are bound by a binder to form an elastic sheet. Therefore, the battery can be assembled in the same manner as in the case of using the conventional sheet-like separator, the productivity of the battery is improved, and the risk of a short circuit is eliminated because the interval between the electrode plates is constant. Furthermore, since there is only a powder layer between the electrode plates, no useless resistance is generated, and the use of the separator of the present invention can provide a battery having excellent initial and life performance.
In addition, the separator of the present invention has the advantage that the mechanical strength and flexibility of the separator are improved by the addition of acid-resistant synthetic fiber or glass fiber, which makes the work of assembling the battery even easier and allows a variety of assembling. There is. EXAMPLE A separator for a lead storage battery according to the present invention was produced as follows. First, a granular silica powder having a specific surface area of 180 to 250 m 2 / g, in which fine primary particles having primary particles of 10 to 40 nm aggregate to form coarse secondary particles of 50 to 400 μm, was prepared. As the granular silica powder, a commercial product produced by spray-drying silica sol was used. Six kinds of mixed powders shown in Table 1 were prepared by changing the amount of the synthetic fiber added to the granular silica powder. Polypropylene (PP) fibers having a thickness of about 20 μm and cut to a length of 3 mm were used as the synthetic fibers used here. [Table 1] Next, 100 g of the mixed powder was put into a kneader, and polytetrafluoroethylene (PTFE) was used as a polyfluoropolymer. This was diluted by adding 300 g of water to 20 g of an aqueous suspension containing 30% by weight. This was added to the mixed powder in the kneader and kneaded sufficiently. At the beginning of kneading, the contents in the kneading machine are relatively non-sticky, but eventually exhibit rubber elasticity. In such a state, the contents are taken out and formed into a sheet having a thickness of 1.00 mm through a pair of rolls.
When dried at ℃, a sheet having relatively strong and cushioning properties was obtained. This was cut into predetermined dimensions to produce a separator. The density of the separator thus produced was 0.33 to 0.36 g / cm 3 , and the porosity was about 85 to 87%. The porosity could be controlled to some extent by the added water, the degree of kneading, the degree of pressing when passing through a roll, and the like, and the porosity could be further improved. The tensile strength of the above-described separator for a lead battery was measured according to JIS C 2313 (separator for lead-acid battery) 7.2.
FIG. 2 shows the results measured according to the tensile strength test described in Section 3. Subscripts in FIG. 2 indicate No. in Table 1. As can be seen from FIG. 2, the addition of polypropylene significantly increases the strength of the separator. Further, the addition amount is required to be at least 0.5%. If the addition amount is less than 0.5%, it is difficult to find the effect of the addition. Further, when the addition amount is 5%, the tensile strength becomes almost constant. It does not lead to an increase in When the separators (1 to 6) were assembled as an actual separator of a lead-acid battery, the separators No. 1 and 2 were assembled only as shown in FIG. However, since the separators Nos. 3 to 6 had high strength and flexibility, the separators could be assembled in a waveform as shown in FIG. Further, using the above-described separator for a lead storage battery, the battery No. 1 to 6 were assembled and the performance was examined. FIG. 1 is a sectional view of a main part of a sealed lead-acid battery using the lead-acid battery separator shown in Table 1, (A) is a front view,
(B) is a side view. First, the positive electrode plate 1 and the negative electrode plate 2 and Table 1
And the separator 3 shown in FIG. No special equipment was required to manufacture the electrode group, and the conventional assembly equipment could be used as it was. Next, after the prepared electrode group was inserted into the battery case 4, silica powder 6 having the same characteristics as those used for manufacturing the separator 3 was filled around the electrode group. Insertion of the electrode group into the battery case was extremely easy because there was no need to apply much pressure on the electrode group. In the present invention, since it is only necessary to fill the silica powder around the electrode plate group, the time required for filling the powder is only about one minute, and the time required for filling the powder can be greatly reduced. did it. The battery after the filling of the powder was filled with an open-cell phenol resin foam block 7 on top of the powder layer 6 to fix the powder layer 6. The battery case lid 5 is welded to the battery case 4,
Inject a predetermined amount of sulfuric acid electrolyte from the liquid port, attach the exhaust valve 8,
The battery was further charged to complete a 12 V battery having a capacity of about 30 Ah. The positive electrode plate 1 used was a casting grid made of an antimony-free lead alloy filled with a positive electrode paste. As an antimony-free lead alloy, 0.05 to 0.
A general lead-calcium alloy containing 12 wt% Ca and 0.2 to 1.0 wt% Sn can be used. The negative electrode plate 2 was manufactured by filling an ordinary negative electrode paste obtained by adding a shrink-preventing agent such as lignin or barium sulfate to a cast lattice using an antimony-free lead alloy. The lead alloy of the negative electrode grid is 0.05 to 0.12 wt% Ca, 0.001 to 0.5 wt% Sn
A general lead-calcium-based alloy containing In this embodiment, the casting grid is used for the positive electrode and the negative electrode. However, any of an expanded grid or a punched grid obtained by expanding a lead alloy sheet can be used. The electrode plate filled with the battery paste is used after aging in a room at 30 to 80 ° C. In particular, aging of the positive electrode plate is an important step in battery performance. Next, the sealed lead-acid battery according to the present invention is
6A (0.2C) discharge at ℃, then life test according to JIS standard (discharge: 20A × 1h, charge: 5A ×
5 h, temperature: 40 ° C.). Table 2 shows the results. [Table 2] From Table 2, it was found that the batteries Nos. 3 to 5 of the present invention were superior in both the discharge capacity and the number of life cycles to the battery No. 1 in which no polypropylene was added. Battery No. 6 to which 10% of polypropylene was added had poor discharge capacity and poor life cycle count. This is considered to be because addition of as much as 10% of polypropylene to the silica powder interferes with the intended purpose of the silica powder in retaining the electrolyte. In the present embodiment, polypropylene is used as the fiber mixed in the silica powder. However, an acid-resistant synthetic fiber such as polyester or polyacrylonitrile or a glass fiber has a sufficient effect. Further, the same effect can be obtained by using diatomaceous earth or a mixture of diatomaceous earth and silica powder instead of silica powder as the electrolyte retaining material. As described above in detail, according to the present invention, a silica powder is bound by using a polyfluoropolymer as a binder, and a synthetic fiber or a glass fiber is added to the silica powder. It is effective in improving the tensile strength of the lead-acid battery, and furthermore, the use of the separator of the present invention in a lead-acid battery makes it possible to easily produce a new sealed lead-acid battery, and furthermore, the initial and life performance can be significantly improved. It is now possible.
【図面の簡単な説明】
【図1】本発明セパレータを用いた密閉形鉛蓄電池の要
部断面図
【図2】ポリプロピレンの混入量と引張り強度の関係を
示した図
【図3】本発明セパレータを用いた極板群を示した図
【図4】本発明セパレータを用いた極板群を示した図
【符号の説明】
1 正極板
2 負極板
3 セパレータ
4 電槽
5 電槽フタ
6 粉体層
7 発泡体
8 排気弁BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a cross-sectional view of a main part of a sealed lead-acid battery using the separator of the present invention. FIG. FIG. 4 shows an electrode group using the separator of the present invention. [Description of References] 1 Positive electrode plate 2 Negative electrode plate 3 Separator 4 Battery case 5 Battery case lid 6 Powder Layer 7 Foam 8 Exhaust valve
Claims (1)
〜5重量%の耐酸性合成樹脂繊維またはガラス繊維と、
ポリフルオロポリマーバインダーとを有するセパレータ
を介して正負極板が積層された極板群と、前記極板群の
周囲に充填されたシリカ粉体とを備えたことを特徴とす
る鉛蓄電池。 (57) [Claims] (1) Silica powder and 0.5 to silica powder.
~ 5% by weight of acid-resistant synthetic resin fiber or glass fiber;
Separator having polyfluoropolymer binder
An electrode plate group in which positive and negative electrode plates are laminated via
And silica powder filled around.
Lead-acid battery.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10364193A JP3388265B2 (en) | 1993-04-05 | 1993-04-05 | Lead-acid battery separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10364193A JP3388265B2 (en) | 1993-04-05 | 1993-04-05 | Lead-acid battery separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06295718A JPH06295718A (en) | 1994-10-21 |
| JP3388265B2 true JP3388265B2 (en) | 2003-03-17 |
Family
ID=14359398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10364193A Expired - Fee Related JP3388265B2 (en) | 1993-04-05 | 1993-04-05 | Lead-acid battery separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3388265B2 (en) |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5060034B2 (en) * | 2005-09-28 | 2012-10-31 | 日本板硝子株式会社 | Electric storage device separator and electric storage device |
| US9293748B1 (en) | 2014-09-15 | 2016-03-22 | Hollingsworth & Vose Company | Multi-region battery separators |
| US10177360B2 (en) | 2014-11-21 | 2019-01-08 | Hollingsworth & Vose Company | Battery separators with controlled pore structure |
| JP6136080B2 (en) * | 2015-02-18 | 2017-05-31 | 株式会社Gsユアサ | Lead acid battery |
| EP3059796B1 (en) * | 2015-02-18 | 2018-05-16 | GS Yuasa International Ltd. | Lead-acid battery |
| US9786885B2 (en) | 2015-04-10 | 2017-10-10 | Hollingsworth & Vose Company | Battery separators comprising inorganic particles |
| JP7652541B2 (en) * | 2019-09-19 | 2025-03-27 | 株式会社東芝 | Secondary batteries, battery packs, vehicle and stationary power sources |
| US11811088B2 (en) | 2019-09-19 | 2023-11-07 | Kabushiki Kaisha Toshiba | Separator, electrode group, secondary battery, battery pack, vehicle, and stationary power supply |
-
1993
- 1993-04-05 JP JP10364193A patent/JP3388265B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06295718A (en) | 1994-10-21 |
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