JPH0676807A - Compound film for separator of alkaline battery - Google Patents

Compound film for separator of alkaline battery

Info

Publication number
JPH0676807A
JPH0676807A JP5169152A JP16915293A JPH0676807A JP H0676807 A JPH0676807 A JP H0676807A JP 5169152 A JP5169152 A JP 5169152A JP 16915293 A JP16915293 A JP 16915293A JP H0676807 A JPH0676807 A JP H0676807A
Authority
JP
Japan
Prior art keywords
battery
separator
film
hydrophobic
porous
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.)
Withdrawn
Application number
JP5169152A
Other languages
Japanese (ja)
Inventor
Yoshifumi Nishimura
佳史 西村
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.)
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
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 Asahi Chemical Industry Co Ltd filed Critical Asahi Chemical Industry Co Ltd
Priority to JP5169152A priority Critical patent/JPH0676807A/en
Publication of JPH0676807A publication Critical patent/JPH0676807A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Cell Separators (AREA)

Abstract

PURPOSE:To facilitate the gas absorption in a negative electrode at the time of overcharge, and restrict the growth of dendrite crystal to prolong a lifetime of a battery by laminating a nonwoven fabric on a porous film having a non- porous layer between a hydrophilic part and a hydrophobic part. CONSTITUTION:A nonwoven fabric is laminated on a porous film, in which both of a hydrophilic part 1 and a hydrophobic part 2 communicated with each other in the face and the back thereof at the time of moisturizing are formed and a non-porous layer 3 is provided between the hydrophilic part 1 and the hydrophobic part 2. With this structure, in an alkaline battery such as a nickel-zinc battery, the oxygen gas to be generated from a positive electrode at the time of overcharge is easy to arrive the negative electrode through a separator to facilitate the gas absorption in the negative electrode, and furthermore, the generation of dendrite crystal is restricted to prolong the lifetime of a battery. Since the nonwoven fabric is laminated, generation of non-conforming article at the time of assembling a battery is reduced.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ニッケル・カドミウ
ム、ニッケル・水素、ニッケル・亜鉛電池等のアルカリ
電池に用いられるセパレータに適する新規なアルカリ電
池セパレータ用多孔膜及び複合膜に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a novel alkaline battery separator porous membrane and composite membrane suitable for a separator used in alkaline batteries such as nickel-cadmium, nickel-hydrogen and nickel-zinc batteries.

【0002】[0002]

【従来の技術】従来より、ニッケルー亜鉛電池などのア
ルカリ電池においては全体が親水性であるセパレータが
用いられるのが常であった。例えば、公開特許公報昭5
5−83159公報のように微孔性フィルムの微孔内に
セルロ−スを形成させたセパレ−タや、公開特許公報昭
57−55064公報のように疎水性の微孔性膜の少な
くとも一面にセルロ−スエステル並びにポリビニルアル
コ−ルよりなる群から選択されたポリマ−を被覆させた
セパレ−タ等が使用されていた。このような膜では、過
充電時に正極から発生する酸素ガスがセパレータを介し
て負極に到達することができず、負極におけるガス吸収
が困難なものとなっていた。酸素ガスの吸収反応が円滑
に進行しなければ、酸素ガスが電池外に放出されるの
で、その酸素の生成に費やされた電気量だけ負極板の充
電が余分に進行し、ついには負極板から水素ガスが発生
するようになる。そして、負極板から水素ガスが発生す
ると、酸素と水素とが電池外に放出されて電解液中の水
分が失われるという不都合が生じる。また、負極板を過
充電することは樹枝状結晶の生長を促進する要因の一つ
と考えられるので、内部短絡が起こり易くなり、電池の
長寿命化をはばむ原因となっていた。このような問題点
を解決するものとして、例えば、公開特許公報昭58−
18871公報のように親水性多孔膜に孔を設けたセパ
レ−タや、公開特許公報平4−4557公報のように有
機繊維不織布にヒドロゲルを形成する高吸液性高分子を
保持させ、その上にアルカリ難溶性の高分子薄膜を形成
したセパレータ等があるが、このような膜では設けた孔
や、孔となる隙間が大きすぎ、充放電を繰り返している
うちに生成した沈澱活物質が孔や隙間に侵入し、内部短
絡を起こしてしまい、電池寿命の短いものとなってい
た。
2. Description of the Related Art Conventionally, in an alkaline battery such as a nickel-zinc battery, a separator which is entirely hydrophilic has been used. For example, Japanese Patent Publication Sho 5
A separator having celluloses formed in the micropores of a microporous film as in JP-A-5-83159, or at least one surface of a hydrophobic microporous membrane as in JP-A-57-55064. A separator coated with a polymer selected from the group consisting of cellulose ester and polyvinyl alcohol has been used. In such a film, oxygen gas generated from the positive electrode at the time of overcharging cannot reach the negative electrode through the separator, which makes it difficult to absorb gas in the negative electrode. If the oxygen gas absorption reaction does not proceed smoothly, the oxygen gas is released to the outside of the battery, so that the negative electrode plate is additionally charged by the amount of electricity consumed to generate the oxygen, and finally the negative electrode plate. Hydrogen gas comes to be generated from. When hydrogen gas is generated from the negative electrode plate, oxygen and hydrogen are released to the outside of the battery, which causes a disadvantage that water in the electrolytic solution is lost. In addition, since overcharging the negative electrode plate is considered to be one of the factors that promote the growth of dendrites, an internal short circuit is likely to occur, which has been a cause of prolonging the life of the battery. As a means for solving such a problem, for example, Japanese Patent Laid-Open No. Sho 58-58-
As shown in Japanese Patent Laid-Open No. 4-4557, a separator having a hydrophilic porous membrane having pores as in 18871, and a superabsorbent polymer forming a hydrogel in an organic fiber non-woven fabric as in Japanese Patent Laid-Open No. 4-4557 are held on the separator. There is a separator with a polymer thin film that is poorly soluble in alkali, but the pores provided in such a membrane and the gaps that form the pores are too large, and the precipitate active material generated during repeated charging and discharging has pores. The battery life was short due to internal short circuits.

【0003】[0003]

【発明が解決しようとする課題】本発明者は、上記欠点
のないアルカリ電池セパレータ用複合膜について鋭意検
討した結果、本発明に到達した。
The present inventors have arrived at the present invention as a result of extensive studies on a composite membrane for an alkaline battery separator which does not have the above-mentioned drawbacks.

【0004】[0004]

【課題を解決するための手段】本発明は、含水時におい
て表裏連通している親水性の部分と疎水性の部分からな
り、該親水性の部分と疎水性の部分の間に無孔層を有す
る多孔膜に不織布を積層したことを特徴とするアルカリ
電池セパレ−タ用複合膜である。多孔膜の親水性の部分
と疎水性の部分が含水時において各々表裏連通している
とは、疎水性の部分については、含水時において圧力2
kg/cm2 、好ましくは圧力1kg/cm2 において
通気性を持つことを意味し、ここで言う通気性とは、片
方の面から圧力2kg/cm2 、好ましくは圧力1kg
/cm2 以下でエア−を吹き込んだ時、他方の面からエ
ア−が出てくることである。
Means for Solving the Problems The present invention comprises a hydrophilic portion and a hydrophobic portion which are communicated with each other at the time of containing water, and a non-porous layer is provided between the hydrophilic portion and the hydrophobic portion. A composite membrane for an alkaline battery separator, characterized in that a nonwoven fabric is laminated on the porous membrane. The hydrophilic part and the hydrophobic part of the porous membrane communicate with each other in the front and back when water is contained, and the hydrophobic part has a pressure of 2 when water is contained.
It means having air permeability at kg / cm 2 , preferably at a pressure of 1 kg / cm 2 , and the air permeability here means pressure from one side of 2 kg / cm 2 , preferably pressure of 1 kg.
That is, when the air is blown at a rate of less than / cm 2 , the air comes out from the other surface.

【0005】また、親水性の部分が含水時に表裏連通し
ているとは、イオンが透過することを意味し、後述の電
気抵抗測定方法において電解液(苛性カリ水溶液(比重
1.31g/cm3 ))含水時において、少なくとも電
気抵抗が0.3Ω*100cm2 /枚以下、好ましく
は、0.1Ω*100cm2 /枚以下であることであ
る。
In addition, the fact that the hydrophilic part communicates with the front and back when it contains water means that ions are permeated, and in the electrical resistance measuring method described later, the electrolytic solution (caustic potash aqueous solution (specific gravity 1.31 g / cm 3 )) is used. ) at the time of water, at least electrical resistance 0.3Ω * 100cm 2 / sheet or less, it preferably is 0.1 [Omega * 100 cm 2 / sheet or less.

【0006】本発明において、親水性の部分を形成する
ためには、吸液性のポリマーを用いると良い。吸液性ポ
リマーとしては、例えば、ポリビニルアルコール、ポリ
エチレンオキサイド、ポリエチレングリコール、ポリア
クリルアミド、ポリビニルピロリドン、ポリビニルアミ
ン、ポリアクリル酸、ポリメタクリル酸、ポリスチレン
スルホン酸や架橋型ポリアクリル酸ソーダ、架橋型ポリ
アクリル酸カリウム、架橋型ポリアクリル酸アンモニウ
ム、架橋型ポリアクリル酸メチル、架橋型ポリアクリル
酸エチル、架橋型ポリメタクリル酸メチル、架橋型ポリ
メタクリル酸エチル、マレイン酸エチル等のヒドロゲル
形成高分子や澱粉、セルロース及びセルロース誘導体な
どがあげられる。
In the present invention, a liquid-absorbent polymer is preferably used to form the hydrophilic portion. Examples of the liquid-absorbent polymer include polyvinyl alcohol, polyethylene oxide, polyethylene glycol, polyacrylamide, polyvinylpyrrolidone, polyvinylamine, polyacrylic acid, polymethacrylic acid, polystyrene sulfonic acid, crosslinked polyacrylic acid soda, and crosslinked polyacrylic acid. Hydrogel-forming polymers and starches such as potassium acidate, cross-linked poly ammonium acrylate, cross-linked poly methyl acrylate, cross-linked poly ethyl acrylate, cross-linked poly methyl methacrylate, cross-linked poly ethyl methacrylate, ethyl maleate, etc. Examples thereof include cellulose and cellulose derivatives.

【0007】なかでも、価格、性能面において、セルロ
ース及びセルロース誘導体が望ましい。セルロ−スまた
はセルロ−ス誘導体としては、セルロ−スの水酸基の一
部または全部がエステル化されたアセチルセルロ−ス、
ニトロセルロ−スやプロピオン酸、酪酸、リン酸、硫
酸、フタル酸等のセルロ−スエステルや酢酸酪酸セルロ
−ス、酢酸硝酸セルロ−スのような混合エステルや、セ
ルロ−スの水酸基の一部または全部がエ−テル化された
メチルセルロ−ス、エチルセルロ−ス、ベンジルセルロ
−ス、カルボキシメチルセルロ−スなどがあげられる。
Of these, cellulose and cellulose derivatives are desirable in terms of price and performance. As the cellulose or the cellulose derivative, acetyl cellulose in which a part or all of the hydroxyl groups of the cellulose are esterified,
Cellulose esters such as nitrocellulose, propionic acid, butyric acid, phosphoric acid, sulfuric acid, phthalic acid and mixed esters such as cellulose acetate butyrate cellulose acetate acetate nitrate, and some or all of the hydroxyl groups of cellulose And methyl cellulose, ethyl cellulose, benzyl cellulose, carboxymethyl cellulose and the like.

【0008】疎水性の多孔膜の孔内における親水性ポリ
マ−の乾燥時における配置量すなわち含量が該多孔性膜
の空孔体積の100容量%に満たないものであっても、
電解液に接するとポリマ−が膨潤するので空孔内がポリ
マ−で充填され、アルカリ電池セパレ−タとしての機能
を発揮するようになる。従って、多孔膜の孔内における
ポリマ−の乾燥時における配置量すなわち含量は、電解
液(苛性カリ水溶液(比重1.31g/cm3 ))含水
時において、少なくとも電気抵抗が0.3Ω*100c
2 /枚以下にするに足りる量あれば良い。
Even if the arrangement amount of the hydrophilic polymer in the pores of the hydrophobic porous membrane during drying, that is, the content thereof is less than 100% by volume of the pore volume of the porous membrane,
Since the polymer swells when it comes into contact with the electrolytic solution, the inside of the pores is filled with the polymer, and the function as an alkaline battery separator is exerted. Therefore, the amount of the polymer in the pores of the porous film, which is the content of the polymer when dried, is such that the electric resistance is at least 0.3Ω * 100c when the electrolyte solution (caustic potash solution (specific gravity 1.31 g / cm 3 )) contains water.
It is enough if the amount is less than m 2 / sheet.

【0009】本発明において、セパレータ用多孔膜に親
水性の部分と疎水性の部分の両方を形成させる方法とし
ては、基本となる疎水性の多孔膜に、吸液性ポリマ−
の有機溶媒溶液や水溶液を用いて凸版印刷、孔版印刷等
の印刷法で親水性の部分を形成させる方法や、あらか
じめ吸液性ポリマ−が含浸しないように疎水性の多孔膜
に保護を施した後、吸液性ポリマ−の有機溶媒溶液や水
溶液に膜をディッピングするなどの浸漬法等により該吸
液性ポリマ−の有機溶媒溶液や水溶液を染み込ませた
後、該保護を取り除く方法等により基本となる多孔膜に
親水性の部分と疎水性の部分を形成させることができ
る。効率の点から孔版印刷法により、親水性の部分と疎
水性の部分を形成させることが望ましい。
In the present invention, as a method for forming both the hydrophilic portion and the hydrophobic portion on the porous membrane for a separator, a liquid absorbing polymer is formed on the basic hydrophobic porous membrane.
The method of forming a hydrophilic portion by a printing method such as letterpress printing or stencil printing using the organic solvent solution or aqueous solution of, or the hydrophobic porous membrane was protected in advance so as not to be impregnated with the liquid absorbing polymer. After that, after impregnating the organic solvent solution or aqueous solution of the absorbent polymer with an organic solvent solution or aqueous solution of the absorbent polymer by dipping the film, the protection is basically removed. It is possible to form a hydrophilic portion and a hydrophobic portion on the porous film to be formed. From the viewpoint of efficiency, it is desirable to form a hydrophilic portion and a hydrophobic portion by the stencil printing method.

【0010】さらに場合によっては、薬品処理等を施
し、親水性基の導入などにより、親水性強化処理を施し
てもよく、また、樹枝状結晶の生長を抑制する効果のあ
る充填剤、例えば、酸化チタン等を吸液性ポリマ−の有
機溶媒溶液や水溶液に加えても良い。本発明に用いられ
る親水性の部分と疎水性の部分からなる多孔膜の平均孔
径は、樹枝状結晶の生長を抑制するために、5μm以下
であることが好ましい。5μmより大きくなると、孔を
通って樹脂状結晶が成長しやすく、電池寿命の低下につ
ながる。
Further, in some cases, a chemical treatment or the like may be performed to enhance hydrophilicity by introducing a hydrophilic group, and a filler having an effect of suppressing the growth of dendrites, for example, Titanium oxide or the like may be added to the organic solvent solution or aqueous solution of the absorbent polymer. The average pore diameter of the porous membrane used in the present invention, which is composed of the hydrophilic portion and the hydrophobic portion, is preferably 5 μm or less in order to suppress the growth of dendrites. When it is larger than 5 μm, resinous crystals are likely to grow through the holes, leading to a decrease in battery life.

【0011】また、本発明に用いられる多孔膜の厚みは
高密度電池の要求から200μm以下であることが好ま
しい。本発明に用いられる多孔膜の素材としては、アル
カリ電池セパレータとして用いるため耐薬品性に優れた
ポリエチレン系、ポリプロピレン系などのポリオレフィ
ン系樹脂や、ポリフッ化ビニリデン系、ポリテトラフロ
オロエチレン系などのフッ素系樹脂あるいはこれらを組
み合わせた系からなる樹脂が素材として好ましく、中で
も、価格の面からポリオレフィン系樹脂が特に好まし
い。
Further, the thickness of the porous film used in the present invention is preferably 200 μm or less in view of the requirement for a high density battery. The material of the porous film used in the present invention, for use as an alkaline battery separator, has excellent chemical resistance such as polyethylene-based resins, polyolefin-based resins such as polypropylene-based resins, polyvinylidene fluoride-based, polytetrafluoroethylene-based fluorine, etc. A resin made of a system resin or a system obtained by combining these is preferable as a material, and among them, a polyolefin resin is particularly preferable in terms of cost.

【0012】本発明に用いられる不織布の素材として
は、上記の樹脂の他に、セルロース及びセルロース誘導
体よりなる群から選択されたポリマーが素材として好ま
しく、中でも、価格の面からポリオレフィン系樹脂、セ
ルロース及びセルロース誘導体よりなる群から選択され
たポリマーが特に好ましい。本発明に用いられる多孔膜
は、熱可塑性樹脂に溶剤、可塑剤、無機微粉体等を混
合、成形後、抽出及び乾燥を施し、場合により延伸を施
したりする方法、または熱可塑性樹脂に溶剤、可塑剤等
を混合、成形後、抽出及び乾燥を施し、場合により延伸
を施したりする等の手段により得ることができる。
As the material of the non-woven fabric used in the present invention, in addition to the above-mentioned resins, polymers selected from the group consisting of cellulose and cellulose derivatives are preferable as materials, and among them, polyolefin resin, cellulose and Polymers selected from the group consisting of cellulose derivatives are particularly preferred. The porous film used in the present invention, a solvent, a plasticizer, an inorganic fine powder and the like mixed with a thermoplastic resin, after molding, subjected to extraction and drying, a method of performing stretching in some cases, or a solvent to the thermoplastic resin, It can be obtained by means such as mixing and molding a plasticizer and the like, followed by extraction and drying, and optionally stretching.

【0013】例えば、ポリエチレン樹脂、無機微粉体、
有機液状体の混合組成をそれぞれ5〜70容量%、10
〜55容量%、20〜75容量%とし、ヘンシェルミキ
サー等の通常の混合機で混合した後、押出機等の溶融混
練装置により混練し、得られた混練物を押出成形等によ
り50〜300μmの厚さに成形する。さらに、該成形
物から有機液状体の溶剤を用いて有機液状体を抽出し、
引続き無機微粉体の抽出溶剤にて無機微粉体を抽出し多
孔膜を得ることができる。
For example, polyethylene resin, inorganic fine powder,
The mixed composition of the organic liquid is 5 to 70% by volume and 10 respectively.
To 55% by volume, 20 to 75% by volume, and after mixing with an ordinary mixer such as a Henschel mixer, the mixture is kneaded with a melt-kneading device such as an extruder, and the obtained kneaded product is subjected to extrusion molding or the like to give a mixture of 50 to 300 μm. Form to thickness. Furthermore, the organic liquid is extracted from the molded product using a solvent for the organic liquid,
Subsequently, the inorganic fine powder can be extracted with a solvent for extracting the inorganic fine powder to obtain a porous film.

【0014】親水性の部分と疎水性の部分の間に、孔が
完全に埋めつくされ、電解液や空気が透過できない無孔
層を設けるには、親水性の部分と疎水性の部分の境目の
疎水性の部分を熱融着させたり、親水性の部分と疎水性
の部分の境目の疎水性の部分に、印刷法により疎水性の
部分が残るように光硬化型樹脂を塗布し、光により硬化
させる等の手段が用いられる。
In order to form a non-porous layer in which the pores are completely filled and the electrolyte and air cannot pass between the hydrophilic portion and the hydrophobic portion, the boundary between the hydrophilic portion and the hydrophobic portion is required. The heat-bonding of the hydrophobic part of the, or the photo-curable resin is applied to the hydrophobic part of the boundary between the hydrophilic part and the hydrophobic part by the printing method so that the hydrophobic part remains And the like are used for curing.

【0015】親水性の部分と疎水性の部分の間に無孔層
を設けないと、ニッケル・亜鉛二次電池等を組んだ場
合、親水性の部分と疎水性の部分の界面を亜鉛の樹枝状
結晶が成長してしまい、電池寿命が短くなってしまう。
本発明に用いられる多孔膜に不織布を積層する場合、積
層は吸液性ポリマ−の有機溶媒溶液や水溶液を多孔膜に
塗布する前でも後でもよいが、取扱性の面から、塗布前
に多孔膜と不織布を積層するのが望ましい。また、多孔
膜と不織布の積層体に吸液性ポリマ−を塗布した後、多
孔膜のもう一方の面に不織布を積層しても良い。積層す
るには、重ね合わせたり、熱融着や接着剤による接着
等、従来より既知の手法により積層すればよい。
If a non-porous layer is not provided between the hydrophilic portion and the hydrophobic portion, when a nickel-zinc secondary battery or the like is assembled, the interface between the hydrophilic portion and the hydrophobic portion will be a zinc branch. Crystals grow and shorten the battery life.
When a nonwoven fabric is laminated on the porous membrane used in the present invention, the lamination may be performed before or after applying the organic solvent solution or aqueous solution of the liquid-absorbent polymer to the porous membrane, but from the viewpoint of handleability, the porous membrane may be formed before application. It is desirable to laminate the membrane and the non-woven fabric. Alternatively, after applying the liquid-absorbent polymer to the laminate of the porous membrane and the nonwoven fabric, the nonwoven fabric may be laminated on the other surface of the porous membrane. In order to stack the layers, it is possible to stack them by a conventionally known method such as stacking, heat fusion or adhesion with an adhesive.

【0016】不織布を積層することにより、孔内に吸液
性ポリマ−を配置させる際に、基本となる多孔膜の収縮
が防止されたり、電極のすべり性が付与され、取扱が容
易になり、電池組立時における不良の発生が減少する。
本発明のアルカリ電池セパレータ用複合膜は、電解液に
対する濡れ性が良好でかつ気体抜き効果にも優れ、電池
の長寿命化に有用である。
By laminating the non-woven fabrics, when the liquid-absorbent polymer is placed in the pores, the basic porous membrane is prevented from shrinking, and the electrode is provided with slipperiness, which facilitates handling. The occurrence of defects during battery assembly is reduced.
INDUSTRIAL APPLICABILITY The composite film for an alkaline battery separator of the present invention has good wettability with an electrolytic solution and is excellent in a gas venting effect, and is useful for prolonging a battery life.

【0017】[0017]

【実施例】次に実施例をあげて本発明を説明するが、こ
れに限定されるものではない。尚、実施例における試験
方法は次の通りである。 1)膜厚 ダイヤルゲージにて測定(最小目盛1μm) 2)平均孔径 ASTM F−316−80に準拠し、エタノールを使
用し、ハーフドライ法にて評価した。 3)電気抵抗 JIS C−2313に準拠し、評価した。
EXAMPLES The present invention will now be described with reference to examples, but the invention is not limited thereto. The test method in the examples is as follows. 1) Film thickness Measured with a dial gauge (minimum scale 1 μm) 2) Average pore size Based on ASTM F-316-80, ethanol was used and evaluated by a half dry method. 3) Electric resistance It was evaluated according to JIS C-2313.

【0018】電解液に苛性カリ水溶液(比重1.31g
/cm3 )を使用し、あらかじめ室温で1時間浸漬した
後取り出し、Ni板を電流電極に、Cd板を電圧電極に
して電圧を測定し、電気抵抗を算出した。 4)気体透過性 ASTM F−316−80に準拠し、蒸留水にて多孔
膜を浸漬し、窒素ガスが2kg/cm2 にて泡となって
出てくる場合を良好とした。 5)電池寿命 1.5×4cmの正・負極板を交互に重ね合わせたニッ
ケル・亜鉛電池を作製し、1/15C(容量AHの1/
15の電流)充電、1/5C放電にて初期の80%容量
までの劣化サイクルが150回以上の場合を良好とし
た。 6)電池組立性 上記電池寿命テストにおけるニッケル・亜鉛電池組立の
際、20個の電池を作製した時、電池の不良発生が2個
以上を不良、1個以下を良好とした。
An aqueous solution of caustic potash (specific gravity 1.31 g)
/ Cm 3 ) and preliminarily immersed at room temperature for 1 hour and then taken out, and the Ni plate was used as a current electrode and the Cd plate was used as a voltage electrode to measure the voltage and calculate the electric resistance. 4) Gas Permeability According to ASTM F-316-80, the case where the porous membrane was immersed in distilled water and nitrogen gas was bubbled at 2 kg / cm 2 was regarded as good. 5) Battery life A nickel-zinc battery in which positive and negative electrode plates of 1.5 × 4 cm are alternately stacked is manufactured, and the battery is 1/15 C (1/1 of the capacity AH).
(15 current) charge and 1 / 5C discharge, and the deterioration cycle to the initial 80% capacity was 150 times or more was regarded as good. 6) Battery Assembling Property When assembling the nickel-zinc battery in the battery life test, when 20 batteries were manufactured, the occurrence of defective batteries was 2 or more, and 1 or less was good.

【0019】[0019]

【参考例1】微粉珪酸22重量%とジオクチルフタレー
ト44重量%をヘンシェルミキサーで混合し、これに粘
度平均分子量30万のポリエチレン樹脂34重量%を添
加し、再度ヘンシェルミキサーで混合した。該混合物を
30mmφ二軸押出機に450mm幅のTダイスを取り
付けたフィルム製造装置で厚さ100μmの平膜状に成
形した。
Reference Example 1 22% by weight of finely divided silicic acid and 44% by weight of dioctyl phthalate were mixed with a Henschel mixer, 34% by weight of a polyethylene resin having a viscosity average molecular weight of 300,000 was added thereto, and the mixture was again mixed with the Henschel mixer. The mixture was formed into a flat film having a thickness of 100 μm by a film manufacturing apparatus in which a T-die having a width of 450 mm was attached to a 30 mmφ twin-screw extruder.

【0020】成形した膜を、1,1,1−トリクロルエ
タン中に10分間浸漬し、ジオクチルフタレートを抽出
した後乾燥し、さらに60℃の25%苛性ソーダ中に6
0分間浸漬して、微粉珪酸を抽出した後乾燥し、機械方
向に一軸に5倍延伸を施し、厚み40μmの多孔膜を得
た。
The formed membrane is immersed in 1,1,1-trichloroethane for 10 minutes to extract dioctyl phthalate, which is then dried and further added to 6% in 25% caustic soda at 60 ° C.
It was immersed for 0 minutes to extract finely divided silicic acid, which was then dried and uniaxially stretched 5 times in the machine direction to obtain a porous film having a thickness of 40 μm.

【0021】[0021]

【参考例2】粘度平均分子量30万のポリエチレン樹脂
34重量%と流動パラフィン66重量%とを30mmφ
二軸押出機に450mm幅のTダイスを取り付けたフィ
ルム製造装置で厚さ100μmの平膜状に成形した。成
形した膜を、1,1,1−トリクロルエタン中に10分
間浸漬し、流動パラフィンを抽出した後乾燥し、115
℃にて一軸延伸を施し5倍延伸して厚み40μmの多孔
膜を得た。
[Reference Example 2] Polyethylene resin 34% by weight having a viscosity average molecular weight of 300,000 and liquid paraffin 66% by weight are 30 mmφ
A flat film having a thickness of 100 μm was formed by a film manufacturing apparatus in which a T-die having a width of 450 mm was attached to a twin-screw extruder. The formed film is immersed in 1,1,1-trichloroethane for 10 minutes to extract liquid paraffin and then dried.
The film was uniaxially stretched at 0 ° C. and stretched 5 times to obtain a porous film having a thickness of 40 μm.

【0022】[0022]

【実施例1】参考例1で得られた多孔膜の片面に厚み6
0μmの芯鞘型ポリエチレン/ポリプロピレン製不織布
を熱により点融着して積層し、複合膜を得た。次に、該
複合膜にアセチルセルロース(半井タスク製)を乳酸エ
チルに7wt%溶解させた溶液を孔版印刷法にて吸引を
施しながらパターン状に塗布し、該複合膜にアセチルセ
ルロース/乳酸エチル溶液を染み込ませた。無孔層を設
けるために、親水性の部分と疎水性の部分の境目の疎水
性の部分に、UV硬化型樹脂を孔版印刷法により、疎水
性の部分が残るように塗布し、UV光にて硬化させた
後、苛性ソーダにてけん化処理を行い、約1日風乾して
アルカリ電池セパレータ用複合膜を得た。得られた膜の
物性を表1に示す。
Example 1 The thickness of the porous membrane obtained in Reference Example 1 was 6 on one surface.
A 0 μm core / sheath type polyethylene / polypropylene non-woven fabric was spot-fused and laminated by heat to obtain a composite film. Next, a solution in which 7 wt% of acetylcellulose (manufactured by Hanai Task) was dissolved in ethyl lactate was applied to the composite film in a pattern by suction using a stencil printing method, and the acetylcellulose / ethyl lactate solution was applied to the composite film. Soaked in. In order to provide a non-porous layer, UV curable resin is applied to the hydrophobic part of the boundary between the hydrophilic part and the hydrophobic part by the stencil printing method so that the hydrophobic part remains, and UV light is applied. After curing, the mixture was saponified with caustic soda and air-dried for about 1 day to obtain a composite membrane for alkaline battery separator. Table 1 shows the physical properties of the obtained film.

【0023】[0023]

【実施例2】参考例1で得られた多孔膜の片面に厚み6
0μmのポリプロピレン製不織布をポリアミド系接着剤
により積層し、次に、実施例1と同様にしてアルカリ電
池セパレータ用複合膜を得た。得られた膜の物性を表1
に示す。
Example 2 The thickness of the porous film obtained in Reference Example 1 was 6 on one surface.
A 0 μm polypropylene nonwoven fabric was laminated with a polyamide adhesive, and then a composite membrane for an alkaline battery separator was obtained in the same manner as in Example 1. Table 1 shows the physical properties of the obtained film.
Shown in.

【0024】[0024]

【実施例3】厚み60μmのセルロース製不織布を使用
した以外は、実施例2と同様にしてアルカリ電池セパレ
ータ用複合膜を得た。得られた膜の物性を表1に示す。
Example 3 A composite film for an alkaline battery separator was obtained in the same manner as in Example 2 except that a nonwoven fabric made of cellulose having a thickness of 60 μm was used. Table 1 shows the physical properties of the obtained film.

【0025】[0025]

【実施例4】参考例2で得られた多孔膜を使用した以外
は、実施例1と同様にしてアルカリ電池セパレータ用複
合膜を得た。得られた膜の物性を表1に示す。
Example 4 A composite film for an alkaline battery separator was obtained in the same manner as in Example 1 except that the porous film obtained in Reference Example 2 was used. Table 1 shows the physical properties of the obtained film.

【0026】[0026]

【比較例1】アセチルセルロース/乳酸エチル溶液を染
み込ませずに、後は実施例1と同様にして、疎水性多孔
膜に不織布を積層したアルカリ電池セパレータ用複合膜
を得た。得られた膜の物性を表1に示す。
Comparative Example 1 A composite membrane for an alkaline battery separator was obtained by laminating a nonwoven fabric on a hydrophobic porous membrane in the same manner as in Example 1 without impregnating the acetyl cellulose / ethyl lactate solution. Table 1 shows the physical properties of the obtained film.

【0027】[0027]

【比較例2】実施例1で、アセチルセルロース/乳酸エ
チル溶液を孔版印刷法にて吸引を施しながら格子状に塗
布する代わりに、フッ素界面活性剤(大日本インキ社製
F−120)の0.5重量%水溶液に複合膜を浸漬し、
アルカリ電池セパレータ用複合膜を得た。得られた膜の
物性を表1に示す。
Comparative Example 2 Instead of applying the acetyl cellulose / ethyl lactate solution in a grid pattern while applying suction by the stencil printing method in Example 1, 0 of a fluorosurfactant (F-120 manufactured by Dainippon Ink and Chemicals, Inc.) was used. Immersing the composite membrane in a 5 wt% aqueous solution,
A composite film for an alkaline battery separator was obtained. Table 1 shows the physical properties of the obtained film.

【0028】[0028]

【比較例3】不織布を積層せずに、後は実施例1と同様
にして多孔膜を得た。得られた膜の物性を表1に示す。
[Comparative Example 3] A porous film was obtained in the same manner as in Example 1 except that the nonwoven fabric was not laminated. Table 1 shows the physical properties of the obtained film.

【0029】[0029]

【比較例4】無孔層を設けずに、後は実施例1と同様に
してアルカリ電池セパレータ用複合膜を得た。得られた
膜の物性を表1に示す。
Comparative Example 4 A composite film for an alkaline battery separator was obtained in the same manner as in Example 1 except that the non-porous layer was not provided. Table 1 shows the physical properties of the obtained film.

【0030】[0030]

【表1】 [Table 1]

【0031】[0031]

【発明の効果】本発明のアルカリ電池セパレータ用複合
膜は、親水性の部分と疎水性の部分がそれぞれ1か所以
上あり、親水性の部分と疎水性の部分の間に無孔層があ
るため、ニッケルー亜鉛電池などのアルカリ電池におい
て、過充電時に正極から発生する酸素ガスがセパレータ
を介して負極に到達しやすくなり、負極におけるガス吸
収が容易なものとなり、さらに、樹枝状結晶の生長を抑
制し、電池の長寿命化をはかることができる。また、不
織布が積層されているため、電池組立時における不良品
の発生が減少する。
EFFECT OF THE INVENTION The composite membrane for alkaline battery separator of the present invention has at least one hydrophilic portion and one or more hydrophobic portion, and a non-porous layer between the hydrophilic portion and the hydrophobic portion. Therefore, in an alkaline battery such as a nickel-zinc battery, oxygen gas generated from the positive electrode during overcharge easily reaches the negative electrode through the separator, which facilitates gas absorption in the negative electrode and further promotes the growth of dendrites. It can be suppressed and the life of the battery can be extended. In addition, since the nonwoven fabrics are laminated, the number of defective products during battery assembly is reduced.

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

【図1】本発明の複合膜の一例である多孔膜と不織布の
積層体を多孔膜側から見た場合の一例を示す平面図。
FIG. 1 is a plan view showing an example of a laminate of a porous membrane and a nonwoven fabric, which is an example of a composite membrane of the present invention, viewed from the porous membrane side.

【符号の説明】[Explanation of symbols]

1 親水性部分 2 疎水性部分 3 無孔層 1 Hydrophilic part 2 Hydrophobic part 3 Non-porous layer

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成5年7月12日[Submission date] July 12, 1993

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0030[Name of item to be corrected] 0030

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0030】[0030]

【表1】 [Table 1]

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 含水時において表裏連通している親水性
の部分と疎水性の部分からなり、該親水性の部分と疎水
性の部分の間に無孔層を有する多孔膜に不織布を積層し
たことを特徴とするアルカリ電池セパレ−タ用複合膜。
1. A non-woven fabric is laminated on a porous membrane which is composed of a hydrophilic portion and a hydrophobic portion which communicate with each other when water is contained and which has a non-porous layer between the hydrophilic portion and the hydrophobic portion. A composite film for an alkaline battery separator, which is characterized in that
JP5169152A 1992-07-10 1993-07-08 Compound film for separator of alkaline battery Withdrawn JPH0676807A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5169152A JPH0676807A (en) 1992-07-10 1993-07-08 Compound film for separator of alkaline battery

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP18390992 1992-07-10
JP4-183909 1992-07-10
JP5169152A JPH0676807A (en) 1992-07-10 1993-07-08 Compound film for separator of alkaline battery

Publications (1)

Publication Number Publication Date
JPH0676807A true JPH0676807A (en) 1994-03-18

Family

ID=26492590

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5169152A Withdrawn JPH0676807A (en) 1992-07-10 1993-07-08 Compound film for separator of alkaline battery

Country Status (1)

Country Link
JP (1) JPH0676807A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005124895A1 (en) * 2004-06-17 2005-12-29 Kuraray Co., Ltd. Separator for battery and alkaline battery
US7052800B2 (en) 2001-08-29 2006-05-30 Sanyo Electric Co., Ltd. Separator for nickel-metal hydride storage battery and nickel-metal hydride storage battery
DE102018216159A1 (en) 2017-09-22 2019-03-28 Toyota Jidosha Kabushiki Kaisha SEPARATOR FOR SECONDARY BATTERY WITH NON-ACID ELECTROLYTE

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7052800B2 (en) 2001-08-29 2006-05-30 Sanyo Electric Co., Ltd. Separator for nickel-metal hydride storage battery and nickel-metal hydride storage battery
WO2005124895A1 (en) * 2004-06-17 2005-12-29 Kuraray Co., Ltd. Separator for battery and alkaline battery
US7754387B2 (en) 2004-06-17 2010-07-13 Kuraray Co., Ltd. Separator for battery and alkaline battery
DE102018216159A1 (en) 2017-09-22 2019-03-28 Toyota Jidosha Kabushiki Kaisha SEPARATOR FOR SECONDARY BATTERY WITH NON-ACID ELECTROLYTE
US10714725B2 (en) 2017-09-22 2020-07-14 Toyota Jidosha Kabushiki Kaisha Separator for nonaqueous electrolyte secondary battery

Similar Documents

Publication Publication Date Title
KR100727248B1 (en) Organic/inorganic composite separator having porous active coating layer and electrochemical device containing the same
JP5337768B2 (en) Gel electrolyte battery separator
JP5309171B2 (en) Battery separator for lithium polymer battery
US9752063B2 (en) Treatment and adhesive for microporous membranes
US20020110732A1 (en) Battery cell fabrication process
JP4705334B2 (en) Separator for electronic parts and method for manufacturing the same
US9755208B2 (en) Non-aqueous-secondary-battery separator and non-aqueous secondary battery
JP2001118558A (en) Partially coated separator
US11777175B2 (en) Separator for non-aqueous secondary battery, non-aqueous secondary battery, and method of manufacturing non-aqueous secondary battery
JPWO2019054422A1 (en) Separator for non-water secondary battery and non-water secondary battery
JP3419393B2 (en) Non-aqueous electrolyte secondary battery, separator and method of manufacturing the same
JP5008422B2 (en) Polyolefin microporous membrane
JP2006066355A (en) Separator for electronic component and its manufacturing method
WO2020137336A1 (en) Microporous polyolefin membrane and method for producing microporous polyolefin membrane
JP2009242779A (en) Polyolefin fine porous membrane and separator for storage battery
JP2008218085A (en) Polyolefin fine porous membrane
KR101942640B1 (en) Separator for energy storage device
KR102715588B1 (en) Separator, electrochemical device comprising the same and manufacturing method for separator
KR102684714B1 (en) Porous separating film and electrochemical device containing the same
EP3553869B1 (en) Electrode assembly and electrochemical device comprising electrode assembly
JPH0676807A (en) Compound film for separator of alkaline battery
JPH0850890A (en) Composite film for alkaline battery separator
KR101480773B1 (en) Seperator for secondary cell battery, methof of manufacturing thereof, and secondary cell battery having the same
KR101410047B1 (en) Manufacturing method of organic-inorganic hybrid porous seperation membrane and organic-inorganic hybrid porous seperation membrane using the same method
JP2023529114A (en) SEPARATION MEMBRANE FOR LITHIUM SECONDARY BATTERY AND PRODUCTION METHOD THEREOF

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20001003