JPH02256156A - Manufacture of separator - Google Patents

Manufacture of separator

Info

Publication number
JPH02256156A
JPH02256156A JP1077802A JP7780289A JPH02256156A JP H02256156 A JPH02256156 A JP H02256156A JP 1077802 A JP1077802 A JP 1077802A JP 7780289 A JP7780289 A JP 7780289A JP H02256156 A JPH02256156 A JP H02256156A
Authority
JP
Japan
Prior art keywords
separator
water
graft
silver
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
JP1077802A
Other languages
Japanese (ja)
Other versions
JP2734617B2 (en
Inventor
Taku Tokita
時田 卓
Yoshio Tanada
棚田 義男
Hajime Inagaki
稲垣 始
Masahito Yoshida
雅人 吉田
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.)
Mitsui Petrochemical Industries Ltd
Original Assignee
Mitsui Petrochemical Industries 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 Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP1077802A priority Critical patent/JP2734617B2/en
Publication of JPH02256156A publication Critical patent/JPH02256156A/en
Application granted granted Critical
Publication of JP2734617B2 publication Critical patent/JP2734617B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • H01M50/411Organic material
    • H01M50/414Synthetic resins, e.g. thermoplastics or thermosetting resins
    • H01M50/42Acrylic resins
    • 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
    • H01M50/489Separators, membranes, diaphragms or spacing elements inside the cells, characterised by their physical properties, e.g. swelling degree, hydrophilicity or shut down properties
    • 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

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Cell Separators (AREA)

Abstract

PURPOSE:To extend the life of a battery by having a specific graft film neutralized with alkali hydroxide water solution and cleansed with mixture of water and water soluble organic solvent. CONSTITUTION:A graft film, which is obtained by using a polyethylene film as base material and giving it graft copolymerization of acrylic acid, is neutralized with alkali hydroxide water solution and then cleansed with mixture of water and water soluble organic solvent to manufacture a separator. As a result, the separator can be obtained which prevents the transmission of active anode material such as silver ion and has excellent characteristics. It is thus possible to extend the life of the separator itself and also a battery or others which is mounted with the separator.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はセパレータの製造方法に関し、さらに詳しくは
、酸化銀電池などの電池内で銀イオンなどの陽極活物質
の透過阻止に優れた能力を発揮するセパレータの製造方
法に関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method for manufacturing a separator, and more specifically, to a method for manufacturing a separator, which has an excellent ability to block the permeation of anode active materials such as silver ions in a battery such as a silver oxide battery. The present invention relates to a method for manufacturing a separator that exhibits the following properties.

〔従来の技術〕[Conventional technology]

一般に電池用セパレータとしては、電気抵抗が小さく、
かつ均一であることが求められている。
Generally speaking, battery separators have low electrical resistance;
It is also required to be uniform.

このような性質を有する電池用セパレータの製造方法と
して、例えば特開昭55−105963号公報には、ポ
リオレフィン膜にアクリル酸等の親水性モノマーをグラ
フト重合したのち、水酸化カリウム水溶液で処理する方
法が知られているが、銀イオンなどの陽極活物質の透過
を阻止する機能を付与すれば電池の寿命はさらに延びる
As a method for manufacturing a battery separator having such properties, for example, JP-A-55-105963 discloses a method in which a polyolefin membrane is graft-polymerized with a hydrophilic monomer such as acrylic acid, and then treated with an aqueous potassium hydroxide solution. However, if a function is added to prevent the permeation of positive electrode active materials such as silver ions, the life of the battery can be further extended.

〔発明の課題〕[Problem of invention]

本発明の目的は、酸化銀電池などの電池内で、銀イオン
などの陽極活物質の透過阻止に優れた能力を発揮するセ
パレータの製造方法を提案することである。
An object of the present invention is to propose a method for producing a separator that exhibits excellent ability to block the permeation of positive electrode active materials such as silver ions in batteries such as silver oxide batteries.

本発明の他の目的は、耐ブロッキング性が良好で、電池
作成時の作業性の良いセパレータの製造方法を提案する
ことである。
Another object of the present invention is to propose a method for producing a separator that has good anti-blocking properties and is easy to work with when producing a battery.

〔発明の概要〕[Summary of the invention]

本発明に係るセパレータの製造方法は、ポリエチレンを
基材とし、この基材に(メタ)アクリル酸をグラフト重
合し、得られたグラフト膜を水酸化アルカリ水溶液で中
和し、次いで水と水溶性有機溶媒との混合液で洗浄する
ことを特徴とするセパレータの製造方法である。
The method for producing a separator according to the present invention uses polyethylene as a base material, graft-polymerizes (meth)acrylic acid onto this base material, neutralizes the obtained graft film with an aqueous alkali hydroxide solution, and then mixes water and water-soluble This is a method for producing a separator characterized by washing with a mixed solution with an organic solvent.

本発明において基材として用いるポリエチレンは、高密
度、中密度、または低密度ポリエチレンのいずれでも良
い。これらポリエチレンは、0〜10モル%の割合で炭
素数3〜20のα−オレフィンまたはビニルモノマーを
コモノマーとして含有していてもよい。α−オレフィン
としてはプロピレン、1−ブテン、1−ヘキセン、4−
メチル−1−ペンテン、1−デセンなどをあげることが
できる。ビニルモノマーとしてはアクリル酸、メタクリ
ル酸、酸ルビニルなどをあげることができる。
The polyethylene used as the base material in the present invention may be high density, medium density, or low density polyethylene. These polyethylenes may contain an α-olefin having 3 to 20 carbon atoms or a vinyl monomer as a comonomer in a proportion of 0 to 10 mol%. α-olefins include propylene, 1-butene, 1-hexene, 4-
Examples include methyl-1-pentene and 1-decene. Examples of vinyl monomers include acrylic acid, methacrylic acid, and rubinyl acid.

また、本発明に用いるポリエチレンは、デカリン溶媒中
135℃で測定した極限粘度〔η〕が通常0.5dQ/
g以上、好ましくは1.0〜5.OdQ/g、特に好ま
しくは2.0〜4.0d12/gのものが適当である。
Furthermore, the polyethylene used in the present invention usually has an intrinsic viscosity [η] of 0.5 dQ/
g or more, preferably 1.0 to 5. OdQ/g, particularly preferably 2.0 to 4.0 d12/g, is suitable.

本発明において基材はフィルムの形で用いられる。この
ような基材フィルムとして用いられるポリエチレン膜は
5〜100μm、好ましくは7〜40μm程度の膜厚を
有していることが電池容量および成形性の観点から好ま
しい。
In the present invention, the substrate is used in the form of a film. The polyethylene film used as such a base film preferably has a thickness of about 5 to 100 μm, preferably about 7 to 40 μm, from the viewpoint of battery capacity and moldability.

基材としてのポリエチレンに(メタ)アクリル酸をグラ
フト重合するには、ポリエチレン膜に1〜30Mrad
の電子線を照射した後、このポリエチレン膜を充分に脱
気された5〜50重量%のアクリル酸および/またはメ
タクリル酸水溶液中に、20〜50℃で1〜60分間浸
漬してグラフト重合を行う。
In order to graft-polymerize (meth)acrylic acid to polyethylene as a base material, 1 to 30 Mrad is added to the polyethylene film.
After being irradiated with an electron beam, the polyethylene film was immersed in a sufficiently degassed 5 to 50% by weight aqueous solution of acrylic acid and/or methacrylic acid at 20 to 50°C for 1 to 60 minutes to initiate graft polymerization. conduct.

次に、このようにして得られたポリエチレンのグラフ1
〜膜を水酸化アルカリ水溶液に浸漬して中和処理を行う
。この中和処理に使用する水酸化アルカリとしては水酸
化カリウム、水酸化ナトリウム等があげられるが、水酸
化カリウムが好ましい。
Next, graph 1 of the polyethylene obtained in this way
~Perform neutralization treatment by immersing the membrane in an aqueous alkali hydroxide solution. Examples of the alkali hydroxide used in this neutralization treatment include potassium hydroxide and sodium hydroxide, with potassium hydroxide being preferred.

中和処理に用いるアルカリ水溶液の濃度は、セパレータ
として装着されるアルカリ電池の電解液としての水酸化
アルカリ水溶液濃度をα重量%とじた場合、α±5重量
%以内とするのが好ましい。
The concentration of the alkaline aqueous solution used for the neutralization treatment is preferably within α±5% by weight, where α% by weight is the concentration of the alkaline hydroxide aqueous solution as the electrolyte of the alkaline battery installed as a separator.

例えば装着される電池電解液としての水酸化カリウムの
濃度が40重量%である場合には、40±5重量%の水
酸化カリウム溶液を用いることが好ましい。グラフ1−
膜のアルカリ水溶液による中和処理は、常温ないし70
℃の温度で、10〜60分間行うことが好ましい。
For example, when the concentration of potassium hydroxide as the battery electrolyte to be installed is 40% by weight, it is preferable to use a potassium hydroxide solution of 40±5% by weight. Graph 1-
Neutralization treatment of membrane with alkaline aqueous solution is carried out at room temperature to 70℃.
It is preferable to carry out the reaction at a temperature of 10 to 60 minutes.

一 次に、このようにして水酸化アルカリ水溶液により中和
処理されたグラフト膜を、水と水溶性有機溶媒との混合
液で洗浄する。このような水溶性有機溶媒としては、ア
ルコール系、ケトン系およびカルボン酸系などの有機溶
媒をあげることができ、これらの有機溶媒の中でもメタ
ノール、エタノール、エチレングリコールなどのアルコ
ール系有機溶媒、およびアセトンなどのケトン系有機溶
媒が好ましい。このような有機溶媒は、単独であるいは
2種以上混合して用いられるが、特にエチレングリコー
ルとメタノールと水との混合液が好ましい。
First, the graft membrane thus neutralized with an aqueous alkali hydroxide solution is washed with a mixed solution of water and a water-soluble organic solvent. Such water-soluble organic solvents include alcohol-based, ketone-based, and carboxylic acid-based organic solvents, and among these organic solvents, alcohol-based organic solvents such as methanol, ethanol, and ethylene glycol, and acetone are preferred. Ketone organic solvents such as the like are preferred. Such organic solvents may be used alone or in a mixture of two or more, and a mixture of ethylene glycol, methanol, and water is particularly preferred.

本発明で用いられる水溶性有機溶媒は、20℃における
水に対する溶解度が1体積%以上、好ましくは10体積
%以上、より好ましくは20体積%以上であることが望
ましく、特に完全相溶性の有機溶媒であることが望まし
い。
The water-soluble organic solvent used in the present invention desirably has a solubility in water at 20° C. of 1% by volume or more, preferably 10% by volume or more, more preferably 20% by volume or more, and especially completely compatible organic solvents. It is desirable that

本発明で用いられる水と水溶性有機溶媒との混合物にお
ける水と水溶性有機溶媒との混合比は、重量比で5=9
5〜95:5、好ましくは20 : 80〜80 : 
20、特に好ましくは30 : 70〜70 : 30
であることが望ましい。
The mixing ratio of water and water-soluble organic solvent in the mixture of water and water-soluble organic solvent used in the present invention is 5=9 by weight.
5-95:5, preferably 20:80-80:
20, particularly preferably 30:70 to 70:30
It is desirable that

上記のような水と水溶性有機溶媒との混合液によりグラ
フト膜を洗浄する際の洗浄温度は5〜70℃、好ましく
は常温以上50°C未満が望ましい。洗浄時間は1〜6
0分間、好ましくは2〜5分間が望ましい。
When cleaning the graft membrane with the above-mentioned mixture of water and a water-soluble organic solvent, the cleaning temperature is preferably 5 to 70°C, preferably room temperature or higher and lower than 50°C. Washing time is 1-6
0 minutes, preferably 2 to 5 minutes.

上記の水と水溶性有機溶媒との混合液によりグラフト膜
を洗浄するには、たとえばグラフト膜を上記の混合液に
浸漬する方法、上記混合液をシャワーする方法などがあ
る。
In order to wash the graft membrane with the above mixture of water and a water-soluble organic solvent, there are, for example, a method of immersing the graft membrane in the above mixture, a method of showering the graft membrane with the above mixture, and the like.

上記の洗浄によりセパレータの製造は完了し、洗浄を終
ったグラフト膜はセパレータとして使用される。本発明
により製造されるセパレータは、銀イオン等の陽極活物
質の透過阻止を必要とする酸化銀電池などの電池用のセ
パレータとして用いるのに適しているが、イオン等の透
過を阻止する他の用途のセパレータとしても用いること
ができる。
The manufacture of the separator is completed by the above washing, and the washed graft membrane is used as a separator. The separator produced according to the present invention is suitable for use as a separator for batteries such as silver oxide batteries that require blocking the permeation of anode active materials such as silver ions, but it is suitable for use as a separator for batteries such as silver oxide batteries that require blocking the permeation of anode active materials such as silver ions. It can also be used as a separator for other purposes.

本発明のセパレータは単独で、または複数枚を積層して
、電池等のセパレータに用いることができるが、耐ブロ
ッキング性が優れているため、電池等の作成時の作業性
は良好である。
The separator of the present invention can be used alone or in a stack of a plurality of sheets as a separator for batteries, etc., and since it has excellent blocking resistance, workability during production of batteries, etc. is good.

〔発明の効果〕〔Effect of the invention〕

本発明に係るセパレータの製造方法では、ポリエチレン
膜を基材とし、このポリエチレン膜に(メタ)アクリル
酸をグラフト重合し、得られたグラフト膜を水酸化アル
カリ水溶液で中和し、次いで水と水溶性有機溶媒との混
合液で洗浄してセパレータを製造するため、銀イオンな
どの陽極活物質の透過を阻止し、優れた特性を有するセ
パレータが得られ、セパレータ自体の寿命が延びるとと
もに、このセパレータが装着された電池等の寿命も延び
る。
In the method for producing a separator according to the present invention, a polyethylene film is used as a base material, (meth)acrylic acid is graft-polymerized onto this polyethylene film, the obtained graft film is neutralized with an aqueous alkali hydroxide solution, and then mixed with water and an aqueous solution. Since the separator is manufactured by washing with a mixed solution with a neutral organic solvent, the permeation of anode active materials such as silver ions is blocked, and a separator with excellent properties is obtained.The life of the separator itself is extended, and this separator The lifespan of batteries etc. equipped with this will also be extended.

また、得られたセパレータは耐ブロッキング性も良く、
電池等の作成の作業性も良くなる。
In addition, the obtained separator has good blocking resistance,
The workability of producing batteries and the like also improves.

〔実施例〕〔Example〕

以下、本発明を実施例により説明するが、本発明はこれ
ら実施例に限定されるものではない。
EXAMPLES The present invention will be explained below with reference to Examples, but the present invention is not limited to these Examples.

実施例1 高密度ポリエチレンフィルム(厚さ20μm、密度0.
955、〔η] 3.2dQ/g)に、電子線照射装置
を用いて10Mradの電子線を窒素雰囲気下で冷却し
ながら照射した。次に電子線の照射されたこのポリエチ
レン膜を、あらかじめ充分に脱気され、かつモール塩が
0.25重景%添加された30重量%アクリル酸水溶液
中に、40℃で10分間浸漬してグラフト重合を行い、
グラフト膜を得た。得られたグラフト膜のグラフ1〜率
は55%であった。
Example 1 High-density polyethylene film (thickness 20 μm, density 0.
955, [η] 3.2 dQ/g), was irradiated with an electron beam of 10 Mrad using an electron beam irradiation device while cooling under a nitrogen atmosphere. Next, this polyethylene film irradiated with an electron beam was immersed for 10 minutes at 40°C in a 30% by weight acrylic acid aqueous solution that had been sufficiently degassed in advance and to which 0.25% Mohr's salt had been added. Perform graft polymerization,
A graft membrane was obtained. The graph 1~ ratio of the obtained graft membrane was 55%.

次にこのようにアクリル酸水溶液に浸漬して得られたグ
ラフト膜(I)を、40重量%水酸化カリウム水溶液に
40℃で10分間浸漬して中和処理し、次いでエチレン
グリコールとメタノールと水との混合比が1:5:4で
ある水溶液を用いて室温で洗浄し、次いで乾燥してセパ
レータ(1)を得た。
Next, the graft membrane (I) obtained by immersing in the acrylic acid aqueous solution was neutralized by immersing it in a 40% by weight potassium hydroxide aqueous solution at 40°C for 10 minutes, and then immersed in ethylene glycol, methanol and water. The separator (1) was obtained by washing at room temperature using an aqueous solution having a mixing ratio of 1:5:4 and then drying.

次にセパレータ(1)を酸化亜鉛飽和の30重量%水酸
化カリウム水溶液に浸漬してセパレータ(II)を得た
。次いでセパレータ(1)1枚とセパレータ(■)7枚
とを、セパレータ(1)が最上部にくるように積層して
セパレータ積層体を得た。
Next, the separator (1) was immersed in a 30% by weight aqueous potassium hydroxide solution saturated with zinc oxide to obtain a separator (II). Next, one separator (1) and seven separators (■) were stacked so that the separator (1) was on top to obtain a separator laminate.

このセパレータ積層体を第1図に示すような銀透過試験
用セルに装着して、各セパレータを透過した銀イオンの
量を測定した。なおセパレータ(II)は実際の電池の
状態に合わせるために、上記の含浸を行った。
This separator laminate was installed in a silver permeation test cell as shown in FIG. 1, and the amount of silver ions that passed through each separator was measured. Note that the separator (II) was impregnated as described above in order to match the state of the actual battery.

第1図に示す銀透過試験用セルにおいて、1はガラス板
、2はセパレータ積層体、3は壁面、4はシール部材、
5は酸化銀、6は30重斌%水酸化カリウム水溶液、7
は空気抜きである。
In the silver permeation test cell shown in FIG. 1, 1 is a glass plate, 2 is a separator laminate, 3 is a wall surface, 4 is a sealing member,
5 is silver oxide, 6 is 30% potassium hydroxide aqueous solution, 7
is an air vent.

このように形成した銀透過試験用セルを70℃で24時
間静置した後、セパレータ積層体2を取り出し、各セパ
レータにおける銀の浸透状態を肉眼観察したところ、1
枚目のセパレータ(I)にだけ銀が浸透していたが2〜
8枚目のセパレータ(n)には銀は認められなかった。
After leaving the silver permeation test cell thus formed at 70°C for 24 hours, the separator laminate 2 was taken out and the state of silver permeation in each separator was visually observed.
Silver had penetrated only into the second separator (I), but 2~
No silver was observed in the 8th separator (n).

また、各セパレータの銀の保持量をICP発光分析で測
定したところ、1枚目7205μg、2枚目35μg、
3枚目5μgの銀が検知され、4枚目以後には、銀が検
知されなかった。
In addition, when the amount of silver retained in each separator was measured by ICP emission spectrometry, the first sheet was 7205 μg, the second sheet was 35 μg,
5 μg of silver was detected on the third sheet, and no silver was detected after the fourth sheet.

比較例1 実施例1で得られたグラフト膜(1)を純水で水洗した
後、乾燥してセパレータ(m)を得た。このセパレータ
(m)に酸化亜鉛飽和の30重量%水酸化カリウム水溶
液を含浸させてセパレータ(IV)を得た。これらを用
いて実施例1と同様の試験を施したところ、銀は7枚目
まで観察された。
Comparative Example 1 The graft membrane (1) obtained in Example 1 was washed with pure water and then dried to obtain a separator (m). This separator (m) was impregnated with a 30% by weight aqueous potassium hydroxide solution saturated with zinc oxide to obtain a separator (IV). When the same test as in Example 1 was conducted using these, silver was observed up to the 7th sheet.

また実施例1と同様に各セパレータの銀の保持量を測定
したところ、1枚目245μg、2枚目70μg、3枚
目41μg、4枚目39μg、 5枚目26μg、6枚
目20μg、7枚目21μg、 8枚目21μgの銀が
検知された。
In addition, when the amount of silver retained in each separator was measured in the same manner as in Example 1, the results were 245 μg for the first sheet, 70 μg for the second sheet, 41 μg for the third sheet, 39 μg for the fourth sheet, 26 μg for the fifth sheet, 20 μg for the sixth sheet, and 7 21 μg of silver was detected in the 8th sheet and 21 μg in the 8th sheet.

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

第1図は実施例において銀透過試験に用いた銀透過試験
用セルの断面図である。 1・・ガラス板     2・・・セパレータ積層体3
・・・壁面 代理人 弁理士 柳 原   成
FIG. 1 is a cross-sectional view of a silver permeation test cell used in the silver permeation test in Examples. 1...Glass plate 2...Separator laminate 3
...Wall agent Patent attorney Sei Yanagihara

Claims (1)

【特許請求の範囲】[Claims] (1)ポリエチレンを基材とし、この基材に(メタ)ア
クリル酸をグラフト重合し、得られたグラフト膜を水酸
化アルカリ水溶液で中和し、次いで水と水溶性有機溶媒
との混合液で洗浄することを特徴とするセパレータの製
造方法。
(1) Using polyethylene as a base material, (meth)acrylic acid is graft-polymerized onto this base material, the resulting graft film is neutralized with an aqueous alkali hydroxide solution, and then treated with a mixture of water and a water-soluble organic solvent. A method for producing a separator, which includes washing.
JP1077802A 1989-03-29 1989-03-29 Manufacturing method of separator Expired - Fee Related JP2734617B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1077802A JP2734617B2 (en) 1989-03-29 1989-03-29 Manufacturing method of separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1077802A JP2734617B2 (en) 1989-03-29 1989-03-29 Manufacturing method of separator

Publications (2)

Publication Number Publication Date
JPH02256156A true JPH02256156A (en) 1990-10-16
JP2734617B2 JP2734617B2 (en) 1998-04-02

Family

ID=13644139

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1077802A Expired - Fee Related JP2734617B2 (en) 1989-03-29 1989-03-29 Manufacturing method of separator

Country Status (1)

Country Link
JP (1) JP2734617B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11289917B1 (en) 2007-10-15 2022-03-29 Ampt, Llc Optimized photovoltaic conversion system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11289917B1 (en) 2007-10-15 2022-03-29 Ampt, Llc Optimized photovoltaic conversion system

Also Published As

Publication number Publication date
JP2734617B2 (en) 1998-04-02

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