JPS61245463A - Enclosed lead storage battery - Google Patents

Enclosed lead storage battery

Info

Publication number
JPS61245463A
JPS61245463A JP60087296A JP8729685A JPS61245463A JP S61245463 A JPS61245463 A JP S61245463A JP 60087296 A JP60087296 A JP 60087296A JP 8729685 A JP8729685 A JP 8729685A JP S61245463 A JPS61245463 A JP S61245463A
Authority
JP
Japan
Prior art keywords
separator
weight
fibers
fibrillar
sealed lead
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
Application number
JP60087296A
Other languages
Japanese (ja)
Inventor
Masaaki Sasaki
正明 佐々木
Shigeru Sasabe
笹部 繁
Ken Kono
河野 研
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.)
Yuasa Corp
Original Assignee
Yuasa Battery Corp
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 Yuasa Battery Corp filed Critical Yuasa Battery Corp
Priority to JP60087296A priority Critical patent/JPS61245463A/en
Publication of JPS61245463A publication Critical patent/JPS61245463A/en
Pending legal-status Critical Current

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/44Fibrous material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/40Separators; Membranes; Diaphragms; Spacing elements inside cells
    • H01M50/409Separators, membranes or diaphragms characterised by the material
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/417Polyolefins
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0002Aqueous electrolytes
    • H01M2300/0005Acid electrolytes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

PURPOSE:To achieve long service life of enclosed lead storage battery through an inexpensive separator having good liquid suction performance and high tensile strength by forming the separator with compound of fibrillar synthetic fiber having water filtering factor higher than specific level, mono-filament fiber and inorganic powder. CONSTITUTION:Liquid suction separator is formed with compound of 10-30wt% of fibrillar synthetic fiber having the water filtering factor higher than 5sec/g, 10-40wt% of mono-filament fiber and 30-70wt% of inorganic powder such as diatom earth, perlite, etc. Said separator and gelatinized electrolyte are combined to produce an enclosed lead storage battery employing an inexpensive separator having good liquid suction performance and high tensile strength, resulting in a cell suitable for emergency power source in vehicle.

Description

【発明の詳細な説明】 主l上互■且分り 本発明は非常用電源、ボータプル機器用電源などの従来
の小形の密閉形鉛蓄電池のみならず、これより大形の据
置用、自動車用、電気自動車用としても使用可能な密閉
形鉛蓄電池を提供することを目的とするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is applicable not only to conventional small sealed lead-acid batteries such as emergency power supplies and power supplies for portable equipment, but also to larger-sized stationary batteries, automotive batteries, etc. The purpose of this invention is to provide a sealed lead-acid battery that can also be used for electric vehicles.

従米坐孜血 従来の密閉形鉛蓄電池の液固定方式としては、平均繊維
径が1μ程度の微細なガラス繊維から形成された微細ガ
ラスマットセパレータに液状の電解液を保持させた微細
ガラスマット方式、ゲル状の電解液を使用するゲル方式
、およびこれらの長所を生かすべく、セパレータを用い
かつゲル状の電解液を使用する併用方式がある。
The conventional liquid fixing method for sealed lead-acid batteries is the fine glass mat method, in which a liquid electrolyte is held in a fine glass mat separator made of fine glass fibers with an average fiber diameter of about 1 μm. There is a gel method that uses a gel electrolyte solution, and a combination method that uses a separator and a gel electrolyte solution to take advantage of these advantages.

またこの併用方式としては、そのセパレータとして微細
ガラスマットを用いるもの、およびシンターPvCや紙
製セパレータなどのいわゆる流動電解液式の鉛蓄電池に
使用されるセパレータを用いるものがある。
In addition, as the combination method, there are a method using a fine glass mat as the separator, and a method using a separator such as a sintered PvC or a paper separator used in a so-called flowing electrolyte type lead-acid battery.

■(ゝ占 しかしながらこの併用方式のうち微細ガラスマットを用
いるものにおいては微細ガラスマットが高価であり、そ
の利用分野が限られるという欠点があった。また併用方
式のうちいわゆる流動電解液式の鉛蓄電池に使用される
セパレータを用いるものにおいてはセパレータの密度が
高くかつ多孔度が約60%と低いためその電解液の保持
量が少なくなり電池容量が劣るという問題点が有り、ま
たセパレータに弾力性が乏しいため活物質の保持性に欠
は短寿命であるという欠点が有った。
■(Account) However, among these combined methods, those using fine glass mats had the disadvantage that the fine glass mats were expensive and the field of use was limited. In those using separators used in storage batteries, the density of the separator is high and the porosity is low at about 60%, so there is a problem that the amount of electrolyte retained is small and the battery capacity is inferior. Due to the lack of active material retention, the active material has a short lifespan.

占  ° るための 本発明は上記のごとき点に鑑み、吸液性のセパレータと
ゲル化電解液を併用した密閉形鉛蓄電池において、長寿
命かつ安価な製品を提供することを目的としてなされた
ものである。
In view of the above points, the present invention has been made with the aim of providing a long-life and inexpensive sealed lead-acid battery that uses a liquid-absorbing separator and a gelled electrolyte in combination. It is.

すなわち本発明のうち第1の発明の特徴とするところは
、そのセパレータが、10〜30重量%のフィブリル状
合成繊維、10〜40重量%のモノフィラメント状繊維
、および30〜70重量%の無機粉末の混合物から形成
され、かつ該フィブリル状合成繊維が5秒/g以上の濾
水度を有している(以下、高透過フィブリル状合成繊維
という)ことにある。
That is, the first aspect of the present invention is characterized in that the separator contains 10 to 30% by weight of fibrillar synthetic fibers, 10 to 40% by weight of monofilamentous fibers, and 30 to 70% by weight of inorganic powder. The fibrillar synthetic fibers have a freeness of 5 seconds/g or more (hereinafter referred to as high permeability fibrillar synthetic fibers).

また第2の発明の特徴とするところはそのセパレータが
、15重量%以下のガラス繊維、10〜30重量%の高
透過フィブリル状合成繊維、10〜40重量%のモノフ
ィラメント状繊維、および30〜70重量%の無機粉末
の混合物から形成され、かつ該ガラス繊維が1.0μ以
下の平均繊維径を有している”(以下、微細ガラス繊維
という)ことにある。
Further, the second invention is characterized in that the separator contains 15% by weight or less of glass fiber, 10 to 30% by weight of highly permeable fibrillar synthetic fiber, 10 to 40% by weight of monofilament fiber, and 30 to 70% by weight of highly permeable fibrillar synthetic fiber. % by weight of an inorganic powder, and the glass fibers have an average fiber diameter of 1.0 μm or less (hereinafter referred to as fine glass fibers).

実110− 以下、本発明をその一実施例により説明する。Fruit 110- The present invention will be explained below with reference to one embodiment thereof.

すなわち組立前に予め硫酸根をもたせた正極板2枚と負
極板3枚とを、第1表に示されるごとき組成のセパレー
タを介して積み重ねて極群を得た。なおこの正極板およ
び負極板の大きさは、それぞれ高さ450as、巾14
0m5.厚さ4mm、および高さ450Il1m、巾1
40m++w、厚さ3IIII+であった。この極群を
電槽に収納したのち、比重1.220〜1.280の希
硫酸に3重量%の二酸化珪素を分散させた電解液を極群
空間容積より5〜15%多く注液し、電池を静置させて
電解液をゲル化させた。こののち電槽に弁を配した上蓋
を接着し充電して、本発明による密閉形鉛蓄電池を完成
した。なお第1表のセパレータは、高透過フィブリル状
合成繊維としてポリエチレンを成分とする濾水度10秒
/gのものを、モノフィラメント状繊維としてポリエス
テルを成分とした繊維径8μのものを、また無機粉末と
して珪藻土をそれぞれ用いたものである。
That is, before assembly, two positive electrode plates and three negative electrode plates, which had been provided with sulfate groups in advance, were stacked with a separator having the composition shown in Table 1 interposed therebetween to obtain an electrode group. The size of this positive electrode plate and negative electrode plate is 450 as in height and 14 in width, respectively.
0m5. Thickness 4mm, height 450Il1m, width 1
It was 40m++w and 3III+ thick. After storing this electrode group in a battery container, an electrolytic solution in which 3% by weight of silicon dioxide is dispersed in dilute sulfuric acid with a specific gravity of 1.220 to 1.280 is injected in an amount of 5 to 15% more than the space volume of the electrode group. The battery was allowed to stand still to allow the electrolyte to gel. Thereafter, a top cover with a valve was attached to the battery case and the battery was charged, completing a sealed lead-acid battery according to the present invention. The separators shown in Table 1 are those with a freeness of 10 seconds/g made of polyethylene as a highly permeable fibrillar synthetic fiber, those with a fiber diameter of 8μ made of polyester as a monofilament fiber, and those made with inorganic powder. Diatomaceous earth was used as the material.

以上のごとき本発明による密閉形鉛蓄電池a。Sealed lead acid battery a according to the present invention as described above.

および同一の極板を用い、微細ガラスマットをセパレー
タとすると共にゲル状の電解液を併用した従来の密閉形
鉛蓄電池b、同じく同一の極板を用い、シンターPvC
をセパレータとする第1表 と共にゲル状の電解液を併用した従来の密閉形鉛蓄電池
Cを供試して、次のごときサイクル寿命特性試験を行っ
た。すなわち放電深度50%の放電、放電量に対比して
120%の充電を繰り返す交互充放電を行い、この交互
充放電中に適宜、放電電流5Aの容量試験を挿入して、
その放電持続時間を測定した。この結果を第1図に示す
、なおこのときの試験温度は25℃であり、また放電持
続時間はその終止電圧を1.80Vとした。
A conventional sealed lead-acid battery b using the same electrode plate and using a fine glass mat as a separator and a gel electrolyte, and a sintered PvC battery using the same electrode plate.
A conventional sealed lead-acid battery C using a gel electrolyte as well as the separator shown in Table 1 was tested for cycle life characteristics as follows. That is, alternate charging and discharging is performed by repeating discharging at a depth of discharge of 50% and charging at 120% relative to the discharge amount, and a capacity test with a discharge current of 5 A is inserted as appropriate during this alternate charging and discharging.
The discharge duration was measured. The results are shown in FIG. 1. The test temperature at this time was 25° C., and the final voltage of the discharge duration was 1.80V.

第1図より本発明による密閉形鉛蓄電池aの性能が極め
て優れていることが分かる。
It can be seen from FIG. 1 that the performance of the sealed lead-acid battery a according to the present invention is extremely excellent.

この原因としては次のごとくである。すなわち密閉形鉛
蓄電池aのセパレータの高透過フィブリル状合成繊維と
して使用されているポリエチレンや、モノフィラメント
状繊維として使用されているポリエステルは本来親水性
に乏しく、これによりゲル化電解液と併用した場合、通
切なガスの移動通路が形成されると考えられる。
The reasons for this are as follows. In other words, the polyethylene used as the highly permeable fibrillar synthetic fiber of the separator of the sealed lead-acid battery a and the polyester used as the monofilament fiber are inherently poor in hydrophilicity, so when used in combination with a gelled electrolyte, It is believed that a continuous gas movement path is formed.

またパーライトや珪藻土などのシリカ系の無機粉末は、
希硫酸をゲル化させるために用いる二酸化珪素よりもそ
の粒子径が大きく、よって二酸化珪素がゲル化に伴って
形成するシリカの骨格構造が密になり過ぎるのを防ぎ、
電池の性能に好ましい結果を与える。なぜならば、もし
もこの骨格構造が密になり過ぎると、ガスの移動通路が
確保されにくく、また電解液の移動も難しくなり、これ
により電池の容量性能や寿命性能に悪影響を与えるから
である。
In addition, silica-based inorganic powders such as perlite and diatomaceous earth,
Its particle size is larger than that of silicon dioxide used to gel dilute sulfuric acid, thus preventing the silica skeleton structure formed by silicon dioxide from becoming too dense as it gels.
Gives favorable results to battery performance. This is because if this skeletal structure becomes too dense, it will be difficult to secure a passage for gas movement, and it will also be difficult for the electrolyte to move, which will adversely affect the capacity and life performance of the battery.

なお上記実施例1ではペースト式の密閉形鉛蓄電池に本
発明を適用したが、本発明はこれに限らずクラッド式の
密閉形鉛蓄電池にも適用可能である。
Although the present invention was applied to a paste-type sealed lead-acid battery in the first embodiment, the present invention is not limited thereto, and can also be applied to a clad-type sealed lead-acid battery.

スJLi糺l 実施例1を踏まえ、本発明に通したセパレータの条件に
つき考察すると、孔径が小さいこと、および引張強さが
大きいことなどが挙げられる。
Based on Example 1, the conditions for the separator used in the present invention include small pore diameter and high tensile strength.

そしてこの孔径の大きさを示す実験としては、セパレー
タを垂直方向に立て、下方から液を吸い上げさせ、一定
高さまで吸い上げるのに要した時間を測定する方法があ
る。すなわちこの実験では吸い上げる時間が長くかかる
ほど、セパレータの孔径が小さいと認められる。
As an experiment to show the size of this pore diameter, there is a method in which a separator is stood vertically, the liquid is sucked up from below, and the time required to suck up the liquid to a certain height is measured. In other words, in this experiment, it was recognized that the longer the suction time was, the smaller the pore diameter of the separator was.

これらの点を総合して本発明に通したセパレータの条件
を列挙するとa ”−cのごとくなる。
Taking all these points into consideration, the conditions for the separator according to the present invention are listed as follows: a''-c.

a、セパレータを垂直方向に立て、下方から1.30d
の希硫酸を吸い上げさせ、90IIm吸い上げるのに要
する吸液特性が600秒以上であること。
a. Stand the separator vertically, 1.30d from the bottom
The liquid absorption property required to suck up 90 IIm of dilute sulfuric acid is 600 seconds or more.

b、引張強さが0. 25Kg/ 15++n以上であ
ること。
b, tensile strength is 0. Must be 25Kg/15++n or more.

C0最大孔径が30μ以下であること。C0 maximum pore diameter is 30μ or less.

ここにおいていくつかのセパレータを供試し、上記の条
件について試験したところ、第2表の結果を得た。また
第2表には合わせてセパレータ原料の価格を、従来のい
わゆる微細ガラスマットセパレータNを100とした指
数で示した。
Here, several separators were tested under the above conditions, and the results shown in Table 2 were obtained. Table 2 also shows the price of separator raw materials as an index with the conventional so-called fine glass matte separator N set as 100.

なお該第2表において用いられている微細ガラス繊維は
いずれも平均繊維径が0.6μのものである。
The fine glass fibers used in Table 2 all have an average fiber diameter of 0.6 μm.

第2表より次のことが言える。すなわちフィブリル状合
成繊維を用いると、モノフィラメント状繊維を用いた場
合に比べて枝分かれした繊維により繊維間の絡み合いが
多くなるため、セパレータの強度を向上させることがで
きることが、一般に知られている。しかしながら混合物
の組成割合は同じで、ただフィブリル状合成繊維の濾水
度を変えただけのセパレータB、E、■を比較して判る
ごとく、どのようなフィブリル状合成繊維を用いても良
いというわけではない。すなわち濾水度が低くなると引
張強さが弱くなるので、このフィブリル状合成繊維の濾
水度は最低でも5秒/g必要である。
From Table 2, the following can be said. That is, it is generally known that when fibrillar synthetic fibers are used, the strength of the separator can be improved because the branched fibers cause more intertwining between the fibers than when monofilament fibers are used. However, as can be seen by comparing separators B, E, and ■, in which the composition ratio of the mixture is the same but the freeness of the fibrillar synthetic fibers is changed, any fibrillar synthetic fiber can be used. isn't it. That is, as the freeness decreases, the tensile strength decreases, so the freeness of this fibrillar synthetic fiber must be at least 5 seconds/g.

またフィブリル状合成繊維の混合割合が10重量%未満
のセパレータJでは、その引張強さが充分ではなく、逆
にその混合割合が30重量%を越えた場合は、得られる
セパレータの密度が高くなるため、価格的に高価となり
望ましくない。なお実施例ではフィブリル状合成繊維と
してポリエチレンを用いたが、これに限られるものでは
なく、アクリル等を用いても同等の効果を期待できる。
Furthermore, separator J in which the mixing ratio of fibrillar synthetic fibers is less than 10% by weight does not have sufficient tensile strength, and conversely, when the mixing ratio exceeds 30% by weight, the resulting separator has a high density. Therefore, it is expensive and undesirable. In the examples, polyethylene was used as the fibrillar synthetic fiber, but it is not limited to this, and the same effect can be expected even if acrylic or the like is used.

無機粉末の混合割合をそれぞれ変化させたセパレータC
,E、に、Lを比較すると、吸液特性を向上させるため
には無機粉末の混合割合を少なくとも30重量%にする
必要がある。しかしながらこの混合割合が70重量%を
越えた場合は、抄紙工程において無機粉末を繊維間に固
定することができなくなるとともに、強度が著しく弱く
なり実用が難しい。
Separator C with different mixing ratios of inorganic powder
, E, and L, the mixing ratio of inorganic powder must be at least 30% by weight in order to improve the liquid absorption properties. However, if this mixing ratio exceeds 70% by weight, it becomes impossible to fix the inorganic powder between the fibers in the papermaking process, and the strength becomes extremely weak, making it difficult to put it into practical use.

モノフィラメント状繊維の混合割合は、フィブリル状合
成繊維および無機粉末の混合割合との関係で、10〜4
0重量%にするのが適当である。またモノフィラメント
状繊維の種類は1種類でなくともよく、セパレータAの
ごとく2種類以上混合してもよい。
The mixing ratio of monofilament fibers is 10 to 4, depending on the mixing ratio of fibrillar synthetic fibers and inorganic powder.
It is appropriate to set it to 0% by weight. Further, the number of types of monofilament fibers does not need to be one, and two or more types may be mixed as in separator A.

微細ガラス繊維が多くなると吸液特性が悪くなる傾向が
あり、また価格も高くなるので、出来れば少ない量とし
たい。こうした見地から15重量%以下の割合で混合さ
せるのが適当である。
As the amount of fine glass fibers increases, the liquid absorption properties tend to deteriorate and the price also increases, so it is desirable to keep the amount as small as possible. From this point of view, it is appropriate to mix at a ratio of 15% by weight or less.

また微細ガラス繊維は平均繊維径が1.0μ以下であれ
ば、同様に良好な結果を得られるが、平均繊維径が2.
0μ以上になると、セパレータの特性に劣化が見られて
好ましくない。
Similarly, good results can be obtained with fine glass fibers if the average fiber diameter is 1.0μ or less, but if the average fiber diameter is 2.
If it exceeds 0μ, the characteristics of the separator will deteriorate, which is undesirable.

光肌■立来 このように15重量%以下の微細ガラス繊維、10〜3
0重量%の高透過フィブリル状合成繊維、10〜40重
量%のモノフィラメント状繊維、および30〜70重量
%の無機粉末の混合物から形成されたセパレータは、吸
液特性が良好で、引張強さが強く、かつ安価で、その加
工も容易である。
Kohada ■Tachiki Like this, 15% by weight or less of fine glass fibers, 10-3
The separator formed from a mixture of 0% by weight of highly permeable fibrillar synthetic fibers, 10-40% by weight of monofilamentary fibers, and 30-70% by weight of inorganic powder has good liquid absorption properties and high tensile strength. It is strong, inexpensive, and easy to process.

そして実施例1において述べたごとく、こうしたセパレ
ータをゲル化電解液を併用した密閉形鉛蓄電池に通用す
ることにより、優れた電池を提供することができる。
As described in Example 1, by applying such a separator to a sealed lead-acid battery using a gelled electrolyte, an excellent battery can be provided.

畝上、本発明はその工業的価値の極めて大きいものであ
る。
In other words, the present invention has extremely great industrial value.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例における密閉形鉛蓄電池a、
および本発明によらない密閉形鉛蓄電池す、cを供試し
て試験したときのサイクル寿命特性を示すグラフである
FIG. 1 shows a sealed lead-acid battery a in an embodiment of the present invention.
FIG. 2 is a graph showing cycle life characteristics when sealed lead-acid batteries A and C not according to the present invention were tested.

Claims (1)

【特許請求の範囲】 1)吸液性のセパレータとゲル化電解液を併用した密閉
形鉛蓄電池において、該セパレータが、10〜30重量
%のフィブリル状合成繊維、10〜40重量%のモノフ
ィラメント状繊維、および30〜70重量%の無機粉末
の混合物から形成され、かつ該フィブリル状合成繊維が
5秒/g以上の濾水度を有していることを特徴とする密
閉形鉛蓄電池。 2)吸液性のセパレータとゲル化電解液を併用した密閉
形鉛蓄電池において、該セパレータが、15重量%以下
のガラス繊維、10〜 30重量%のフィブリル状合成繊維、10〜40重量%
のモノフィラメント状繊維、および30〜70重量%の
無機粉末の混合物から形成され、かつ該ガラス繊維が1
.0μ以下の平均繊維径を有しており、またフィブリル
状合成繊維が5秒/g以上の濾水度を有していることを
特徴とする密閉形鉛蓄電池。
[Scope of Claims] 1) A sealed lead-acid battery using a liquid-absorbing separator and a gelled electrolyte in combination, in which the separator is composed of 10 to 30% by weight of fibrillar synthetic fibers and 10 to 40% by weight of monofilament-like synthetic fibers. 1. A sealed lead-acid battery formed from a mixture of fibers and 30 to 70% by weight of inorganic powder, wherein the fibrillar synthetic fibers have a freeness of 5 seconds/g or more. 2) In a sealed lead-acid battery that uses a liquid-absorbing separator and a gelled electrolyte in combination, the separator comprises 15% by weight or less of glass fiber, 10-30% by weight of fibrillar synthetic fiber, and 10-40% by weight.
of monofilamentary fibers and 30 to 70% by weight of an inorganic powder, and the glass fibers are
.. A sealed lead-acid battery having an average fiber diameter of 0μ or less and a fibrillar synthetic fiber having a freeness of 5 seconds/g or more.
JP60087296A 1985-04-23 1985-04-23 Enclosed lead storage battery Pending JPS61245463A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60087296A JPS61245463A (en) 1985-04-23 1985-04-23 Enclosed lead storage battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60087296A JPS61245463A (en) 1985-04-23 1985-04-23 Enclosed lead storage battery

Publications (1)

Publication Number Publication Date
JPS61245463A true JPS61245463A (en) 1986-10-31

Family

ID=13910854

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60087296A Pending JPS61245463A (en) 1985-04-23 1985-04-23 Enclosed lead storage battery

Country Status (1)

Country Link
JP (1) JPS61245463A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01253153A (en) * 1988-03-31 1989-10-09 Shin Kobe Electric Mach Co Ltd Sealed lead-acid battery
EP0715367A1 (en) * 1994-12-01 1996-06-05 COMPAGNIE EUROPEENNE D'ACCUMULATEURS, Société anonyme dite: Separator electrolyte combination for recombining lead-acid accumulator and accumulator using said combination
JP2005108617A (en) * 2003-09-30 2005-04-21 Nippon Sheet Glass Co Ltd Separator for lead storage battery
JP2006310274A (en) * 2005-03-31 2006-11-09 Nippon Sheet Glass Co Ltd Separator for liquid type lead acid battery and liquid type lead acid battery
JP2016513861A (en) * 2013-03-07 2016-05-16 ダラミック エルエルシー Oxidation-resistant laminated separator

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6035455A (en) * 1983-08-05 1985-02-23 Yuasa Battery Co Ltd Separator for lead storage battery
JPS6035456A (en) * 1983-08-05 1985-02-23 Yuasa Battery Co Ltd Separator for lead storage battery

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6035455A (en) * 1983-08-05 1985-02-23 Yuasa Battery Co Ltd Separator for lead storage battery
JPS6035456A (en) * 1983-08-05 1985-02-23 Yuasa Battery Co Ltd Separator for lead storage battery

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01253153A (en) * 1988-03-31 1989-10-09 Shin Kobe Electric Mach Co Ltd Sealed lead-acid battery
EP0715367A1 (en) * 1994-12-01 1996-06-05 COMPAGNIE EUROPEENNE D'ACCUMULATEURS, Société anonyme dite: Separator electrolyte combination for recombining lead-acid accumulator and accumulator using said combination
FR2727793A1 (en) * 1994-12-01 1996-06-07 Europ Accumulateurs COMBINATION OF A SEPARATOR AND ELECTROLYTE FOR GAS RECOMBINANT LEAD BATTERY, AND ACCUMULATOR USING SUCH COMBINATION
JP2005108617A (en) * 2003-09-30 2005-04-21 Nippon Sheet Glass Co Ltd Separator for lead storage battery
JP2006310274A (en) * 2005-03-31 2006-11-09 Nippon Sheet Glass Co Ltd Separator for liquid type lead acid battery and liquid type lead acid battery
JP2016513861A (en) * 2013-03-07 2016-05-16 ダラミック エルエルシー Oxidation-resistant laminated separator
JP2020115490A (en) * 2013-03-07 2020-07-30 ダラミック エルエルシー Oxidation resistant laminated separator

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