JPH0381263B2 - - Google Patents
Info
- Publication number
- JPH0381263B2 JPH0381263B2 JP58143998A JP14399883A JPH0381263B2 JP H0381263 B2 JPH0381263 B2 JP H0381263B2 JP 58143998 A JP58143998 A JP 58143998A JP 14399883 A JP14399883 A JP 14399883A JP H0381263 B2 JPH0381263 B2 JP H0381263B2
- Authority
- JP
- Japan
- Prior art keywords
- fibers
- weight
- separator
- inorganic powder
- fiber diameter
- 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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/446—Composite material consisting of a mixture of organic and inorganic materials
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0002—Aqueous electrolytes
- H01M2300/0005—Acid electrolytes
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Composite Materials (AREA)
- Inorganic Chemistry (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Cell Separators (AREA)
Description
本発明は、密閉形鉛蓄電池に使用する隔離板の
改良に関するものである。
近時、保守不要な密閉形鉛蓄電池に用いる隔離
板として、繊維径が0.2〜5.0μm程度の微細ガラス
繊維を主体としたマツト状の隔離体を使用するも
のが実用化されており、優れた性能を示してい
る。しかし、この種の微細ガラス繊維は高価であ
るので、これを使用した鉛蓄電池も高価になると
いう欠点があつた。
この欠点を解消するために、高価な微細ガラス
繊維の量を少なくし、安価な合成繊維又は10〜
20μm程度の繊維径を有するガラス繊維を混合し
たもの、或は酸化珪素系の無機粉末を混合したも
のが提案されている。しかし前者の場合は、価格
を下げるために合成繊維又は太い繊維径のガラス
繊維の混合量を増やせば、電解液の吸液特性が悪
くなる。また後者の場合は、価格を下げるために
無機粉末の混合量を増やせば、微細ガラス繊維間
の絡み合いが悪くなり、強度が取扱いに耐えられ
ない程に弱くなるため、熱可塑性の合成繊維を混
合して加熱処理をするという改良手段をとつたと
しても、微細ガラス繊維の量は実質的に50重量%
までしか減らすことができず、十分に価格を下げ
ることができなかつた。
本発明は、上記の欠点を解消したもので、吸液
特性、引張強さ、最大孔径等についての良好な特
性を有し、取扱いが容易で安価な蓄電池用隔離板
を提供することを目的としており、10重量%以下
の微細ガラス繊維、10〜20重量%のフイブリル状
合成繊維、20〜40重量%のモノフイラメント状繊
維、30〜60重量%の親水性の無機粉末を混合して
形成され、微細ガラス繊維として平均繊維径が
0.6μm以下のものを用い、フイブリル状合成繊維
として濾水度が5sec/g以上のものを用い、モノ
フイラメント状繊維として繊維径が8〜13μmの
ポリエステル又はガラスを用い、無機粉末として
ケイソウ土又はパーライトを用いていることを特
徴とするものである。
以下、本発明を詳細に説明する。
一般に隔離板にフイブリル化した合成繊維を用
いると、モノフイラメント状繊維を用いた場合に
比して、枝分かれした繊維によつて繊維間の絡み
合いが多くなるため、隔離板強度を向上させるこ
とができることは知られている。しかし、単にフ
イブリル状合成繊維を用いただけでは、前記目的
の蓄電池用隔離板を得ることはできない。本発明
者らは、フイブリル状合成繊維の濾水度及び混合
量を適切に選択し、且つモノフイラメント状繊維
及び親水性の無機粉末を適量併用することによ
り、所望の隔離板を得ることができることを多く
の実験結果から確認した。
第1表は、微細ガラス繊維を主体としてなる従
来の隔離板(サンプルO、P)と、微細ガラス繊
維の量を従来に比して少なくするとともにフイブ
リル状合成繊維、モノフイラメント状繊維、親水
性の無機粉末を種類、量を種々変えて通常の方法
で形成したものであつて良好な特性を有する本発
明の隔離板(サンプルA〜E)と特性不十分な比
較例としての隔離板(サンプルF〜N)とを、混
合組成、混合物の原料価格、特性について示した
ものである。なお原料価格は、サンプルOを100
として、同じ見掛け厚さの隔離板を得るために必
要な原料価格で示している。また吸液特性は、隔
離板を垂直に立て、下方から1.30dの希硫酸を吸
い上げさせ、90mm吸い上げるのに要した時間で示
している。また隔離板の特性としては、吸液特
性、引張強さ、最大孔径の3つを挙げている。吸
液特性は600sec/90mm以上、最大孔径は30μm以
下であることが、電池寿命との関係で望ましく、
引張強さは0.25Kg/15mm以上であることが、電池
組立工程との関係で望ましいことが、知られてい
る。
第1表において、サンプルB、E、Iは、混合
組成においてフイブリル状合成繊維の濾水度のみ
が異なる。濾水度が5sec/gのサンプルB及び
10sec/gのサンプルEでは全てに良好な特性を
備えているが、濾水度が2sec/gのサンプルIで
は特性のうち引張強さが不十分である。従つて、
フイブリル状合成繊維の濾水度は5sec/g以上が
必要と解される。またフイブリル状合成繊維は引
張強さを向上させるものであるが、サンプルJの
ように混合量が5重量%であると引張強さが不十
分である。従つてサンプルCのようにフイブリル
状合成繊維の混合量は10重量%以上は必要と解さ
れる。なおフイブリル状合成繊維としては、ポリ
エチレンを用いているが、アクリル繊維を用いて
もよい。
モノフイラメント状繊維は、20〜40重量%の割
合で用いられる。モノフイラメント状繊維として
は、繊維径が8〜13μmのガラス又はポリエステ
ルが用いられる。なおサンプルE、Kを比較して
みるに、両者は用いるポリエステルの繊維径と無
機粉末の種類のみが異なつており、サンプルKで
は吸液特性が不十分である。これはポリエステル
の繊維径の違いによるものと考えられ、このこと
からポリエステルとしては8μmの繊維径のものを
用いるのが好ましいと解される。また微細ガラス
繊維を用いない場合(サンプルA)には、モノフ
イラメント状繊維としてガラスとポリエステルの
混合物を用いるのが好ましい。
親水性の無機粉末としては、ケイソウ土又はパ
ーライトが用いられる。これらは30〜60重量%の
割合で用いられる。なおサンプルL、M等から、
望ましい吸液特性を得るためには無機粉末の混合
量は少なくとも30重量%以上とする必要があると
解される。また混合量が70重量%を越えると、抄
紙工程において無機粉末を繊維間に固定すること
ができなくなると共に、強度が著しく弱くなり好
ましくない。従つて60重量%までが妥当と解され
る。
なお微細ガラス繊維は、全体の原料価格を下げ
る必要から10重量%以下にまで少なくするのが好
ましい。また第1表の例では平均繊維径が0.6μm
のものを用いているが、もちろんこれ以下であつ
てもよい。なお平均繊維径が1.0μm以下であれ
ば、同様に良好な特性を維持できるが、平均繊維
径が2.0μm以上になると、隔離板の特性に劣化が
見られて好ましくない。
以上のように10重量%以下の微細ガラス繊維、
10〜20重量%のフイブリル状合成繊維、20〜40重
量%のモノフイラメント状繊維、30〜60重量%の
親水性の無機粉末を混合して形成することによ
り、しかも微細ガラス繊維として平均繊維径が
0.6μm以下のものを用い、フイブリル状合成繊維
として濾水度が5sec/g以上のものを用い、モノ
フイラメント状繊維として繊維径が8〜13μmの
ポリエステル又はガラスを用い、無機粉末として
ケイソウ土又はパーライトを用いることにより、
吸液特性、引張強さ、及び最大孔径で示される隔
離板としての特性が良好で、安価な隔離板が得ら
れる。
以上のように本発明は、合成繊維の混合量を増
加させることによる吸液特性の低下を、親水性の
無機粉末を併用することにより防止すると共に、
濾水度が5sec/g以上のフイブリル状合成繊維を
用いることにより、引張強さを保ちながら高価な
微細ガラス繊維の混合量が10重量%以下と少な
く、且つシート加工後の加熱処理を必要としない
安価な隔離板を得ることができる。本発明の隔離
板は、従来の隔離板に比して非常に安価に製造す
ることができると共に、本発明の隔離板を使用す
ることで、安価で且つ性能が従来の隔離板を使用
したものと実質的に同等な蓄電池を提供でき、そ
の工業的価値は大である。
The present invention relates to improvements in separators used in sealed lead-acid batteries. Recently, a pine-like separator mainly made of fine glass fibers with a fiber diameter of about 0.2 to 5.0 μm has been put into practical use as a separator for sealed lead-acid batteries that do not require maintenance. shows performance. However, since this type of fine glass fiber is expensive, lead-acid batteries using it also have the disadvantage of being expensive. In order to eliminate this drawback, we reduced the amount of expensive fine glass fibers and replaced them with cheap synthetic fibers or
A mixture of glass fibers having a fiber diameter of about 20 μm or a mixture of silicon oxide-based inorganic powder have been proposed. However, in the former case, if the amount of synthetic fiber or glass fiber with a large fiber diameter is increased in order to lower the price, the liquid absorption characteristics of the electrolyte will deteriorate. In the latter case, if the amount of inorganic powder mixed is increased to lower the price, the entanglement between the fine glass fibers becomes worse and the strength becomes so weak that it cannot withstand handling, so thermoplastic synthetic fibers are mixed. Even if an improved method of heat treatment is taken, the amount of fine glass fibers is actually 50% by weight.
However, the company was unable to reduce prices sufficiently. The present invention eliminates the above-mentioned drawbacks, and aims to provide a storage battery separator that has good properties such as liquid absorption properties, tensile strength, and maximum pore diameter, and is easy to handle and inexpensive. It is formed by mixing up to 10% by weight of fine glass fibers, 10-20% by weight of fibrillar synthetic fibers, 20-40% by weight of monofilamentous fibers, and 30-60% by weight of hydrophilic inorganic powder. , the average fiber diameter as fine glass fiber is
Use fibers of 0.6 μm or less, use fibrillar synthetic fibers with a freeness of 5 sec/g or more, use polyester or glass with a fiber diameter of 8 to 13 μm as monofilament fibers, and use diatomaceous earth or glass as inorganic powder. It is characterized by the use of perlite. The present invention will be explained in detail below. In general, when fibrillated synthetic fibers are used for separators, the strength of the separator can be improved because the branched fibers cause more entanglement between fibers than when monofilament fibers are used. is known. However, simply using fibrillar synthetic fibers does not make it possible to obtain the above-mentioned separator for a storage battery. The present inventors have discovered that a desired separator can be obtained by appropriately selecting the freeness and mixing amount of fibrillar synthetic fibers, and by using appropriate amounts of monofilament fibers and hydrophilic inorganic powder in combination. was confirmed from many experimental results. Table 1 shows conventional separators mainly made of fine glass fibers (samples O and P), as well as those with a smaller amount of fine glass fibers than conventional separators, fibrillar synthetic fibers, monofilament fibers, and hydrophilic separators. The separators of the present invention (Samples A to E), which were formed using various types and amounts of inorganic powder and had good properties, and the separators as comparative examples with insufficient properties (Samples F to N) are shown in terms of mixture composition, raw material price, and characteristics of the mixture. The raw material price is 100 for sample O.
is the raw material price required to obtain a separator with the same apparent thickness. The liquid absorption characteristics are shown by the time required to suck up 90 mm of dilute sulfuric acid by standing the separator vertically and sucking up 1.30 d of dilute sulfuric acid from below. In addition, three characteristics of the separator are listed: liquid absorption characteristics, tensile strength, and maximum pore diameter. In relation to battery life, it is desirable that the liquid absorption characteristics be 600sec/90mm or more and the maximum pore diameter be 30μm or less.
It is known that a tensile strength of 0.25 kg/15 mm or more is desirable in relation to the battery assembly process. In Table 1, Samples B, E, and I differ only in the freeness of the fibrillar synthetic fibers in the mixed composition. Sample B with freeness of 5sec/g and
Sample E with a freeness of 10 sec/g has all good properties, but sample I with a freeness of 2 sec/g has insufficient tensile strength. Therefore,
It is understood that the freeness of fibrillated synthetic fibers is required to be 5 sec/g or more. Furthermore, fibrillar synthetic fibers improve tensile strength, but when the amount mixed is 5% by weight as in Sample J, the tensile strength is insufficient. Therefore, as in Sample C, it is understood that the amount of fibrillar synthetic fibers mixed is required to be 10% by weight or more. Although polyethylene is used as the fibrillar synthetic fiber, acrylic fiber may also be used. Monofilamentous fibers are used in proportions of 20 to 40% by weight. As the monofilament fiber, glass or polyester having a fiber diameter of 8 to 13 μm is used. A comparison of Samples E and K shows that they differ only in the fiber diameter of the polyester used and the type of inorganic powder, and Sample K has insufficient liquid absorption properties. This is thought to be due to the difference in the fiber diameter of the polyester, and from this it is understood that it is preferable to use a polyester with a fiber diameter of 8 μm. Further, when fine glass fibers are not used (sample A), it is preferable to use a mixture of glass and polyester as the monofilament fibers. Diatomaceous earth or perlite is used as the hydrophilic inorganic powder. These are used in proportions of 30 to 60% by weight. Furthermore, from samples L, M, etc.
It is understood that in order to obtain desirable liquid absorption properties, the amount of inorganic powder mixed must be at least 30% by weight. Moreover, if the mixing amount exceeds 70% by weight, it becomes impossible to fix the inorganic powder between the fibers in the paper-making process, and the strength becomes extremely weak, which is not preferable. Therefore, up to 60% by weight is considered appropriate. Note that the amount of fine glass fibers is preferably reduced to 10% by weight or less in order to reduce the overall raw material cost. In addition, in the example in Table 1, the average fiber diameter is 0.6 μm.
Although the following is used, of course it may be less than this. If the average fiber diameter is 1.0 μm or less, good properties can be maintained, but if the average fiber diameter is 2.0 μm or more, the properties of the separator deteriorate, which is not preferable. Fine glass fiber of 10% by weight or less as above,
By mixing and forming 10 to 20% by weight of fibrillar synthetic fibers, 20 to 40% by weight of monofilamentous fibers, and 30 to 60% by weight of hydrophilic inorganic powder, the average fiber diameter is reduced as fine glass fibers. but
Use fibrillar synthetic fibers with a freeness of 5 sec/g or more, use polyester or glass with a fiber diameter of 8 to 13 μm as monofilament fibers, and use diatomaceous earth or glass as inorganic powder. By using perlite,
An inexpensive separator with good properties as a separator, including liquid absorption properties, tensile strength, and maximum pore diameter, can be obtained. As described above, the present invention prevents a decrease in liquid absorption properties due to an increase in the amount of synthetic fiber mixed by using a hydrophilic inorganic powder in combination, and
By using fibrillated synthetic fibers with a freeness of 5 sec/g or more, the amount of expensive fine glass fibers mixed is as low as 10% by weight or less while maintaining tensile strength, and heat treatment after sheet processing is not required. You can get a cheap separator that doesn't. The separator of the present invention can be manufactured at a much lower cost than conventional separators, and by using the separator of the present invention, it is cheaper and has better performance than conventional separators. It is possible to provide a storage battery that is substantially equivalent to the above, and its industrial value is great.
【表】【table】
【表】
した時間で示した。
[Table] Shown by time.
Claims (1)
%のフイブリル状合成繊維、20〜40重量%のモノ
フイラメント状繊維、30〜60重量%の親水性の無
機粉末を混合して形成され、微細ガラス繊維とし
て平均繊維径が0.6μm以下のものを用い、フイブ
リル状合成繊維として濾水度が5sec/g以上のも
のを用い、モノフイラメント状繊維として繊維径
が8〜13μmのポリエステル又はガラスを用い、
無機粉末としてケイソウ土又はパーライトを用い
ていることを特徴とする蓄電池用隔離板。1 Formed by mixing 10% by weight or less of fine glass fibers, 10 to 20% by weight of fibrillar synthetic fibers, 20 to 40% by weight of monofilamentous fibers, and 30 to 60% by weight of hydrophilic inorganic powder, Fine glass fibers with an average fiber diameter of 0.6 μm or less are used, fibrillar synthetic fibers with a freeness of 5 sec/g or more are used, and monofilament fibers are polyester or glass with a fiber diameter of 8 to 13 μm. use,
A separator for a storage battery characterized by using diatomaceous earth or perlite as an inorganic powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58143998A JPS6035455A (en) | 1983-08-05 | 1983-08-05 | Separator for lead storage battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58143998A JPS6035455A (en) | 1983-08-05 | 1983-08-05 | Separator for lead storage battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6035455A JPS6035455A (en) | 1985-02-23 |
| JPH0381263B2 true JPH0381263B2 (en) | 1991-12-27 |
Family
ID=15351931
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58143998A Granted JPS6035455A (en) | 1983-08-05 | 1983-08-05 | Separator for lead storage battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6035455A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61245463A (en) * | 1985-04-23 | 1986-10-31 | Yuasa Battery Co Ltd | Enclosed lead storage battery |
| JPS62150650A (en) * | 1985-12-25 | 1987-07-04 | Matsushita Electric Ind Co Ltd | lead acid battery |
| JPH01248458A (en) * | 1988-03-30 | 1989-10-04 | Shin Kobe Electric Mach Co Ltd | Sealed lead-acid battery |
| JPH01248457A (en) * | 1988-03-30 | 1989-10-04 | Shin Kobe Electric Mach Co Ltd | Sealed lead-acid battery |
| JP4928137B2 (en) * | 2005-03-31 | 2012-05-09 | 日本板硝子株式会社 | Separator for liquid lead acid battery and liquid lead acid battery |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5422531A (en) * | 1977-07-21 | 1979-02-20 | Nippon Mineral Fiber Mfg | Separator plate for lead storage battery and method of making same |
| US4216281A (en) * | 1978-08-21 | 1980-08-05 | W. R. Grace & Co. | Battery separator |
| JPS5699968A (en) * | 1980-01-12 | 1981-08-11 | Nippon Muki Kk | Separator for battery |
| CA1172310A (en) * | 1980-06-30 | 1984-08-07 | Stanley J. Strzempko | Battery separator material |
-
1983
- 1983-08-05 JP JP58143998A patent/JPS6035455A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6035455A (en) | 1985-02-23 |
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