JPS61250968A - Sealed lead-acid battery - Google Patents

Sealed lead-acid battery

Info

Publication number
JPS61250968A
JPS61250968A JP60092123A JP9212385A JPS61250968A JP S61250968 A JPS61250968 A JP S61250968A JP 60092123 A JP60092123 A JP 60092123A JP 9212385 A JP9212385 A JP 9212385A JP S61250968 A JPS61250968 A JP S61250968A
Authority
JP
Japan
Prior art keywords
separator
sealed lead
electrolyte
battery
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.)
Granted
Application number
JP60092123A
Other languages
Japanese (ja)
Other versions
JPH0451943B2 (en
Inventor
Masaaki Sasaki
正明 佐々木
Shigeru Sasabe
笹部 繁
Takakiyo Umeda
梅田 孝清
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 JP60092123A priority Critical patent/JPS61250968A/en
Publication of JPS61250968A publication Critical patent/JPS61250968A/en
Publication of JPH0451943B2 publication Critical patent/JPH0451943B2/ja
Granted 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
    • H01M50/431Inorganic material
    • H01M50/434Ceramics
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Abstract

PURPOSE:To increase life and reduce cost by using a mat made of ceramic fibers having a specified composition ratio of silica and alumina and a specified average diameter in a separator. CONSTITUTION:An electrode group is obtained by stacking two positive plates nd three negative plates both previously impregnated with sulfuric acid with separators interposed between them. A mat made of ceramic fibers whose total composition ratio of silica and alumina is 90% or more and whose average diameter is 40mum or less is used as the separator. The electrode group is accommodated into a container, and electrolyte obtained by dispersing a specified weight ratio of silicon dioxide into dilute sulfuric acid having a specified specific gravity is poured into the container and a battery is allowed to stand to gel the electrolyte..The cost of the separtor is reduced, and by using this separator and gelled electrolyte, the life of the sealed lead-acid battery is increased.

Description

【発明の詳細な説明】 崖1上坐皿里分1 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 sources for voltaple equipment, but also to larger stationary batteries and automobiles. The purpose of the present invention is to provide a sealed lead-acid battery that can also be used for electric vehicles.

従米互技五 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。
Conventional liquid fixing methods for sealed lead-acid batteries include a 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 1μ; 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.

日 (シよ°と る口 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ントが高価であり、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。
However, among this combination method, the one using a fine glass mat had the disadvantage that the fine glass cloak was expensive and its field of use was limited. In those using separators used in electrolyte type lead acid batteries, the separator has a high density and a low porosity of about 60%, so there is a problem that the amount of electrolyte retained is small and the battery capacity is inferior. Furthermore, since the separator has poor elasticity, it lacks active material retention and has a short lifespan.

占   ゛        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 was made with the aim of providing a sealed lead-acid battery that uses a liquid-absorbing separator and a gelled electrolyte at low cost and long life. .

すなわち本発明の特徴とするところは、そのセパレータ
がシリカとアルミナとの合計割合で90%以上を占める
組成を有し、かつ4.0μ以下の平均繊維径を有するセ
ラミックファイバーからなるマットを使用していること
にある。
In other words, the present invention is characterized in that the separator uses a mat made of ceramic fibers having a composition in which the total proportion of silica and alumina is 90% or more and has an average fiber diameter of 4.0μ or less. It is in the fact that

実見皿上 以下、本発明をその一実施例により説明する。On the actual plate 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、シリカ(Si02)が52%、アルミナ
(A 1203 )が47%の割合をそれぞれ占める組
成を有し、かつ285μの平均繊維径を有するセラミッ
クファイバーからなるマットを使用したセパレータを介
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450mm、巾140mm
、厚さ4IIlff11および高さ450mo+、中1
40am、厚さ3IIIII+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。
In other words, two positive electrode plates and three negative electrode plates, which have sulfuric acid groups in advance before assembly, have a composition in which silica (Si02) accounts for 52%, alumina (A 1203 ) accounts for 47%, and 285μ A pole group was obtained by stacking mats made of ceramic fibers with an average fiber diameter of 1 through a separator. The size of this positive electrode plate and negative electrode plate is 450 mm in height and 140 mm in width, respectively.
, thickness 4IIlff11 and height 450mo+, medium 1
It was 40 am 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.

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。
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.

以上のごとき本発明による密閉形鉛蓄電池a、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。
Sealed lead-acid battery a according to the present invention as described above, and conventional sealed lead-acid battery b that uses the same electrode plate and uses a fine glass mat as a separator and a gel electrolyte, and also uses the same electrode plate. A conventional sealed lead-acid battery C using sintered PVC as a separator and a gel electrolyte was used to conduct the following cycle life characteristic test. In other words, alternate charging and discharging is performed by repeating discharging at a depth of discharge of 50% and charging at 120% of the amount of discharge, and during this alternate charging and discharging, a capacity test with a discharge current of 5 A is inserted as appropriate to determine the duration of the discharge. It was measured. The results are shown in FIG. The test temperature at this time was 25°C,
Further, the final voltage of the discharge duration was set to 1.80V.

第1図より本発明におけるセパレータを用いた密閉形鉛
蓄電池aは、微細ガラスマントをセパレータとすムと共
にゲル状の電解液を併用した従来の密閉形鉛蓄電池すに
比べてそのセパレータの価格比において約20%と格段
に安いにもかかわらず、その性能においてほとんど遜色
のないことが分与る。
Figure 1 shows that the sealed lead-acid battery a using the separator of the present invention has a price ratio of the separator compared to the conventional sealed lead-acid battery that uses a fine glass cape as a separator and a gel electrolyte. Although it is much cheaper at about 20%, its performance is almost comparable.

この原因としては次のごとく考えられる。すなわち密閉
形鉛蓄電池aのセパレータとして用いられているセラミ
ックファイバーはその平均繊維径が約2〜4μと微細ガ
ラスマットの1μ以下に比べて太いが、ゲル状の電解液
と組み合わされた場合、実質的に同等の機能を有するた
めと考えられる。またセラミックファイバーのうち安価
のものではショット(非繊維状粒子)が含まれるが、こ
れがむしろ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。
The possible reasons for this are as follows. In other words, the ceramic fibers used as separators in sealed lead-acid batteries a have an average fiber diameter of about 2 to 4 μm, which is thicker than the 1 μm or less diameter of fine glass mats, but when combined with a gel-like electrolyte, This is thought to be because they have essentially the same function. In addition, cheap ceramic fibers contain shot (non-fibrous particles), but these particles have a larger particle size than the silicon dioxide used to gel dilute sulfuric acid, so silicon dioxide This prevents the silica skeleton structure formed from becoming too dense, which has favorable results for battery performance.

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。更にセラミックファイバーに
はガラス繊維に含まれるCaO1Mg01B203、N
a20などの金°属酸化物が含まれておらず、酸に対し
ても安定であり、ゲル化が均一になり安いものと思われ
る。
This is because if this skeletal structure becomes too dense,
This is because it becomes difficult to secure a passage for gas movement, and it also becomes difficult to move the electrolyte, which adversely affects the capacity performance and life performance of the battery. Furthermore, ceramic fiber contains CaO1Mg01B203 and N contained in glass fiber.
It does not contain metal oxides such as a20, is stable against acids, and is thought to be uniformly gelatinous and inexpensive.

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.

またセラミックファイバーを板状に加工してセパレータ
とする際に、有機または無機のバインダー、を使用する
ことも考えられるが、優れた弾力性や高い多孔度を有す
るためにはこれらを使用しないほうが望ましい。
It is also possible to use organic or inorganic binders when processing ceramic fibers into plate shapes to make separators, but in order to have excellent elasticity and high porosity, it is preferable not to use these. .

主班夏班果 このように本発明におけるセパレータは、安価であり、
これをゲル化電解液を併用した密閉形鉛蓄電池に適用す
ることにより、優れた電池を提供することができる。
As described above, the separator of the present invention is inexpensive,
By applying this to a sealed lead-acid battery that uses a gelled electrolyte, an excellent battery can be provided.

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

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

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】[Claims] 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、該セパレータがシリカとアルミナとの
合計割合で90%以上を占める組成を有し、かつ4.0
μ以下の平均繊維径を有するセラミックファイバーから
なるマットを使用していることを特徴とする密閉形鉛蓄
電池。
In a sealed lead-acid battery that uses a liquid-absorbing separator and a gelled electrolyte, the separator has a composition in which the total proportion of silica and alumina is 90% or more, and 4.0
A sealed lead-acid battery characterized by using a mat made of ceramic fibers having an average fiber diameter of μ or less.
JP60092123A 1985-04-26 1985-04-26 Sealed lead-acid battery Granted JPS61250968A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60092123A JPS61250968A (en) 1985-04-26 1985-04-26 Sealed lead-acid battery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60092123A JPS61250968A (en) 1985-04-26 1985-04-26 Sealed lead-acid battery

Publications (2)

Publication Number Publication Date
JPS61250968A true JPS61250968A (en) 1986-11-08
JPH0451943B2 JPH0451943B2 (en) 1992-08-20

Family

ID=14045653

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60092123A Granted JPS61250968A (en) 1985-04-26 1985-04-26 Sealed lead-acid battery

Country Status (1)

Country Link
JP (1) JPS61250968A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7682738B2 (en) 2002-02-07 2010-03-23 Kvg Technologies, Inc. Lead acid battery with gelled electrolyte formed by filtration action of absorbent separators and method for producing it
US8399134B2 (en) 2007-11-20 2013-03-19 Firefly Energy, Inc. Lead acid battery including a two-layer carbon foam current collector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7682738B2 (en) 2002-02-07 2010-03-23 Kvg Technologies, Inc. Lead acid battery with gelled electrolyte formed by filtration action of absorbent separators and method for producing it
US8399134B2 (en) 2007-11-20 2013-03-19 Firefly Energy, Inc. Lead acid battery including a two-layer carbon foam current collector

Also Published As

Publication number Publication date
JPH0451943B2 (en) 1992-08-20

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