[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JPS61246394A - Diaphragm for electrolysis - Google Patents

Diaphragm for electrolysis

Info

Publication number
JPS61246394A
JPS61246394A JP60084590A JP8459085A JPS61246394A JP S61246394 A JPS61246394 A JP S61246394A JP 60084590 A JP60084590 A JP 60084590A JP 8459085 A JP8459085 A JP 8459085A JP S61246394 A JPS61246394 A JP S61246394A
Authority
JP
Japan
Prior art keywords
diaphragm
ion exchange
exchange resin
halogen
electrolysis
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
JP60084590A
Other languages
Japanese (ja)
Other versions
JPH0575835B2 (en
Inventor
Hiroshi Kato
博 加藤
Ichiro Komada
一郎 駒田
Satoru Kazuyasu
一安 哲
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.)
Japan Gore Tex Inc
Original Assignee
Japan Gore Tex Inc
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 Japan Gore Tex Inc filed Critical Japan Gore Tex Inc
Priority to JP60084590A priority Critical patent/JPS61246394A/en
Publication of JPS61246394A publication Critical patent/JPS61246394A/en
Publication of JPH0575835B2 publication Critical patent/JPH0575835B2/ja
Granted 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 obtain a diaphragm for electrolysis having superior dimensional stability and mechanical strength and used in a halogen-zinc cell or the like by uniformly sticking a perfluoror type ion exchange resin to a polytetrafluoroethylene resin film having a specified porosity. CONSTITUTION:A perfluoro type ion exchange resin is uniformly impregnated into or stuck to a polytetrafluoroethylene resin film having >=35%, especially >=40% porosity by 10-30%, and the resulting membrane of 204n504mm thickness is used as a diaphragm for electrolysis used in a halogen-zinc cell or an alkaline cell. The diaphragm has superior mechanical strength even under dry conditions, lowers hardly the electric resistance by reduction in thickness and also has superior coulomb efficiency.

Description

【発明の詳細な説明】 「発明の目的」 本発明は電解隔膜の創案に係り、ノ・ロゲンー亜鉛電池
やアルカリ電池などにおける電解隔膜としてその液中な
どにおける寸法安定性に優れ、又乾燥条件下においても
機械的強度の優れた製品を提供しようとするものである
Detailed Description of the Invention ``Object of the Invention'' The present invention relates to the creation of an electrolytic diaphragm, which has excellent dimensional stability in liquid, etc. as an electrolytic diaphragm in zinc-carbon batteries, alkaline batteries, etc., and also under dry conditions. The aim is to provide products with excellent mechanical strength.

産業上の利用分野 ハロゲン−亜鉛電池やアルカリ電池などにおける電解隔
膜。
Industrial applications Electrolytic diaphragms in halogen-zinc batteries, alkaline batteries, etc.

従来の技術 ハロゲン−亜鉛電池やアルカリ電池などにおけるセパレ
ータとしてはイオン交換樹脂を製膜したものが従来から
知られ、既に実用化されている。又セロファン等の微孔
性天然高分子フィルムやプラスチックフィルムにアクリ
ル酸やメタクリル酸をグラフト重合させた膜なども知ら
れている。
BACKGROUND OF THE INVENTION As a separator for halogen-zinc batteries, alkaline batteries, etc., ion exchange resin films have been known and have already been put into practical use. Also known are membranes in which acrylic acid or methacrylic acid is graft-polymerized onto microporous natural polymer films such as cellophane or plastic films.

発明が解決しようとする問題点 然し上記したような従来のものにおいては夫夫になお問
題点を有している。即ちイオン交換樹脂を製膜したもの
においては酸化剤などに侵されない有利性があるが、薄
膜状となし或いは交換容量をよけたりすると強度や液中
などにおける寸法安定性に劣ることとなるものであって
、乾燥状態では機械的強度が激減してクラックを発生し
易いことになり、水を含むような条件下では極端に膨潤
し、何れにしても作業性に劣る。
Problems to be Solved by the Invention However, the above-mentioned conventional devices still have problems. In other words, films made of ion exchange resins have the advantage of not being attacked by oxidizing agents, but if they are made into thin films or have a low exchange capacity, they will have poor strength and dimensional stability in liquids. However, in a dry state, the mechanical strength is drastically reduced and cracks are likely to occur, and in a condition containing water, it swells extremely, and in any case, the workability is poor.

微孔性天然高分子フィルムによるものでけ陽極合剤に用
いる二酸化マンガン等の酸化剤によって酸化され、劣化
が著しい。プラスチックフィルムにアクリル酸などをグ
ラフト重合させたものにおいては電気抵抗は小さいが陽
極活物質の対極への拡散が起り、電池寿命が短かくなる
Made of microporous natural polymer film, it is oxidized by oxidizing agents such as manganese dioxide used in the anode mixture, resulting in significant deterioration. In the case of a plastic film in which acrylic acid or the like is graft-polymerized, the electrical resistance is low, but the positive electrode active material diffuses to the counter electrode, shortening the battery life.

特にハロゲン−亜鉛電池用隔膜の場合においてはハロゲ
ンの自己放電が多くなってクーロン効率が低下したり、
ハロゲン化ガスがハロゲン化亜鉛に溶解した状態で使用
するため腐食性が強い。
Particularly in the case of diaphragms for halogen-zinc batteries, self-discharge of halogen increases and coulombic efficiency decreases.
It is highly corrosive because the halogenated gas is used dissolved in zinc halide.

「発明の構成」 問題点を解決するための手段 気孔率35%以上のポリテトラフルオロエチレンフィル
ムにパーフロロ系イオン交換m 脂を均一状態に添着一
体化したことを特徴とする電解隔膜。
``Structure of the Invention'' Means for Solving the Problems An electrolytic diaphragm characterized in that a perfluorinated ion exchange resin is uniformly impregnated and integrated with a polytetrafluoroethylene film having a porosity of 35% or more.

作用 気孔率が少くとも35%以上であるポリテトラフルオロ
エチレンフィルムは機械的強度や寸法安定性を得しめる
。又との工うなフィルムを基材とすることによりパーフ
ロロ系イオン交換樹脂膜が薄膜として得られ、電気抵抗
を低くすると共にクーロン効率を高め得る。含浸、混合
、ラミネートするイオン交換樹脂の量を調整し、PTF
E膜の比重を調整することにより活物質の拡散量を制御
する。
A polytetrafluoroethylene film having a working porosity of at least 35% provides mechanical strength and dimensional stability. A perfluoro-based ion exchange resin membrane can be obtained as a thin film by using a ferrous film as a base material, which can lower electrical resistance and increase coulombic efficiency. Adjust the amount of ion exchange resin to be impregnated, mixed, and laminated, and PTF
The amount of diffusion of the active material is controlled by adjusting the specific gravity of the E membrane.

実施例 上記したような本発明によるものの具体的な実施態様を
添附図面に示すものについて説明すると、不発明による
ものは気孔率35%以上、特に40%以上のポリテトラ
フルオロエチレン(以下PTFEという)樹脂フィルム
にパーフロロ系イオン交換樹脂を均一状態に添着一体化
する。
Examples Specific embodiments of the invention as described above are shown in the accompanying drawings.The non-invention is polytetrafluoroethylene (hereinafter referred to as PTFE) with a porosity of 35% or more, particularly 40% or more. A perfluorinated ion exchange resin is uniformly attached and integrated with a resin film.

前記したPTFEフィルムとパーフロロ系イオン交換樹
脂との均一な接着一体化をなす具体的な方法としては以
下のような手法の何れによってもよい。
As a specific method for uniformly adhering and integrating the above-mentioned PTFE film and perfluorinated ion exchange resin, any of the following methods may be used.

■延伸処理して得られた多孔質PTFEフィルムにパー
フロロ系イオン交換樹脂液を充分に含浸させて緻密な隔
膜とする。
(2) The porous PTFE film obtained by stretching is sufficiently impregnated with a perfluorinated ion exchange resin solution to form a dense diaphragm.

■上記■において、パーフロロ系イオン交換樹脂液を不
充分な状態に含浸させてなお多孔質性を有する隔膜とす
る。
(2) In the above (2), the membrane is impregnated with a perfluorinated ion exchange resin liquid in an insufficient state to obtain a diaphragm that still has porous properties.

■PTPK樹脂にイオン交換樹脂液を混合して緻密な隔
膜として製膜する。
■ Mix ion exchange resin liquid with PTPK resin to form a dense diaphragm.

■上記■において製膜に当って延伸し多孔質の隔膜とす
る。
(2) During film formation in (2) above, the film is stretched to form a porous diaphragm.

■イオン交換樹脂を先ず薄膜状に成形し、これをかTF
E多孔質膜にラミネート接着する。
■Ion exchange resin is first formed into a thin film, and this is then
E Laminate and adhere to the porous membrane.

何れの場合においてもPTFEに対するパーフロロ系イ
オン交換樹脂との割合は一般的に重量比で3〜90チで
あり、特に10〜30%とすることが好ましい。又隔膜
の厚さについては一般的に3〜300μm1特に20〜
50μmである。
In either case, the ratio of perfluorinated ion exchange resin to PTFE is generally 3 to 90% by weight, particularly preferably 10 to 30%. The thickness of the diaphragm is generally 3 to 300 μm, especially 20 to 300 μm.
It is 50 μm.

上記のよう圧して得られた隔膜をハロゲン−亜鉛電池用
セパレータとして用いた場合においてはPTFE膜を基
材として成形されたものであるから薄くても機械的強度
や寸法安定性に優れたものとな秒、又パーフロロ系であ
るため電解質による劣化を受けることがないものであっ
て、電気抵抗が低く、シかもクーロン効率の優れたもの
として得られる。又電池寿命も従来のめることかでき、
その性能を著しく改善できる。
When the diaphragm obtained by pressing as described above is used as a separator for a halogen-zinc battery, it has excellent mechanical strength and dimensional stability even if it is thin because it is molded using a PTFE membrane as a base material. Furthermore, since it is a perfluoro-based material, it is not subject to deterioration due to electrolytes, has low electrical resistance, and has excellent coulombic efficiency. Also, the battery life can be compared to the conventional one.
Its performance can be significantly improved.

このことはアルカリ電池用セパレータとする場合におい
ても同様であって上記のように電気抵抗を小さくできる
ことから陽極活物質の対極への拡散防止能に優れたもの
となり好ましい製品が得られる。
This also applies to separators for alkaline batteries, and since the electric resistance can be reduced as described above, a desirable product can be obtained with excellent ability to prevent diffusion of the positive electrode active material to the counter electrode.

本発明によるものの具体的な製造例について説明すると
以下の如くである。
A specific manufacturing example of the product according to the present invention will be described below.

延伸処理によって多数の微小結節部の間に無数の微細繊
維をくもの果状に形成した気孔率5O1sの多孔質PT
FE膜材に対しパーフロロ系イオン交換樹脂液を含浸さ
せて厚さが25μmの緻密な組織を有するハロゲン−亜
鉛電池用の隔膜を得た。
Porous PT with a porosity of 5O1s in which countless fine fibers are formed in a spider-like shape between many micronodules by stretching treatment.
A diaphragm for a halogen-zinc battery having a dense structure with a thickness of 25 μm was obtained by impregnating an FE membrane material with a perfluorinated ion exchange resin liquid.

「発明の効果」 以上説明したような本発明によるときは、この徨電解隔
膜の機械的強度を改善して充分に薄膜化した製品を得し
め、又寸法安定性などにおいても卓越した特性を示すと
共に上記のような薄膜化に伴い電気抵抗が低く、又クー
ロン効率の如きに優れた隔膜を提供し得るものであるか
ら工業的にその効果の大きい発明である。
"Effects of the Invention" According to the present invention as explained above, the mechanical strength of the electrolytic diaphragm can be improved to obtain a product with a sufficiently thin film, and it also exhibits excellent characteristics such as dimensional stability. In addition, it is a highly effective invention industrially because it can provide a diaphragm with low electrical resistance and excellent Coulombic efficiency due to the thinning of the film as described above.

s  許 出 m  人 ジャパンゴアテツクス株式会
社発 明 者加 藤  博 同           駒   1)  −即問  
        −安       哲5′− 代理人 弁理士 白  川  −・二1iIE? ”’
”+’
s Permission m People Japan Gore Texts Co., Ltd. Inventor Hirodo Kato Koma 1) - Immediate question
-An Tetsu 5'- Agent Patent Attorney Shirakawa -21iIE? ”'
"+'

Claims (1)

【特許請求の範囲】[Claims] 気孔率35%以上のポリテトラフルオロエチレンフィル
ムにパーフロロ系イオン交換樹脂を均一状態に添着一体
化したことを特徴とする電解隔膜。
An electrolytic diaphragm comprising a polytetrafluoroethylene film having a porosity of 35% or more and a perfluoro ion exchange resin uniformly attached and integrated therein.
JP60084590A 1985-04-22 1985-04-22 Diaphragm for electrolysis Granted JPS61246394A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60084590A JPS61246394A (en) 1985-04-22 1985-04-22 Diaphragm for electrolysis

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60084590A JPS61246394A (en) 1985-04-22 1985-04-22 Diaphragm for electrolysis

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP62240627A Division JPH0610277B2 (en) 1987-09-28 1987-09-28 Membrane material

Publications (2)

Publication Number Publication Date
JPS61246394A true JPS61246394A (en) 1986-11-01
JPH0575835B2 JPH0575835B2 (en) 1993-10-21

Family

ID=13834889

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60084590A Granted JPS61246394A (en) 1985-04-22 1985-04-22 Diaphragm for electrolysis

Country Status (1)

Country Link
JP (1) JPS61246394A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04139237A (en) * 1990-05-18 1992-05-13 Japan Gore Tex Inc Hydrophilic porous fluororesin material
US7622215B2 (en) 2004-03-04 2009-11-24 Panasonic Corporation Composite electrolyte membrane, catalyst-coated membrane assembly, membrane-electrode assembly and polymer electrolyte fuel cell
CN103066306A (en) * 2012-12-22 2013-04-24 大连理工大学 Ion exchange membrane used for zinc-bromine flow battery and preparation method thereof

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4015168B2 (en) 2003-09-10 2007-11-28 旭化成ケミカルズ株式会社 Stabilized fluoropolymer and method for producing the same
JP4581477B2 (en) * 2004-05-12 2010-11-17 トヨタ自動車株式会社 Method for producing solid polymer electrolyte, solid polymer electrolyte membrane, and fuel cell
EP1674508B1 (en) 2004-12-22 2009-05-13 Asahi Glass Company, Limited Electrolyte membrane, process for its production and membrane-electrode assembly for polymer electrolyte fuel cells
US7776970B2 (en) 2006-02-03 2010-08-17 Daikin Industries, Ltd. Method for producing -SO3H group-containing fluoropolymer and -SO3H group-containing fluoropolymer
JP5151063B2 (en) 2006-04-19 2013-02-27 トヨタ自動車株式会社 Porous material for electrolyte membrane for fuel cell, production method thereof, electrolyte membrane for polymer electrolyte fuel cell, membrane-electrode assembly (MEA), and fuel cell
JP5251515B2 (en) 2006-12-14 2013-07-31 旭硝子株式会社 Solid polymer electrolyte membrane and membrane electrode assembly for polymer electrolyte fuel cell
EP2405517B1 (en) 2009-03-04 2014-08-13 Asahi Kasei E-Materials Corporation Fluorine-containing polymer electrolyte membrane
US9017899B2 (en) 2010-06-18 2015-04-28 Shandong Huaxia Shenzhou New Material Co., Ltd. Fluorine containing ionomer composite with ion exchange function, preparation method and use thereof
CA2802948C (en) 2010-06-18 2018-08-07 Shandong Huaxia Shenzhou New Material Co., Ltd Fluorine-containing ionomer composite material with ion exchange function, preparation method and use thereof
EP2584627B1 (en) 2010-06-18 2016-10-05 Shandong Huaxia Shenzhou New Material Co., Ltd. Composite having ion exchange function and preparation method and use thereof
KR20130060358A (en) 2010-10-07 2013-06-07 아사히 가세이 이-매터리얼즈 가부시키가이샤 Fluorine-based polymer electrolyte membrane
WO2015090571A1 (en) 2013-12-19 2015-06-25 Treofan Germany Gmbh & Co. Kg ION-EXCHANGE MEMBRANE MADE OF A BIAXIALLY STRETCHED β-POROUS FILM
CN110366576A (en) 2017-02-23 2019-10-22 旭化成株式会社 Composition, composite membrane, membrane-electrode assembly

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52114710A (en) * 1976-03-23 1977-09-26 Daikin Ind Ltd Process for making paper mixed with polytetrafluoroethylene
JPS5663770A (en) * 1979-10-26 1981-05-30 Asahi Glass Co Ltd Alkaline battery

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52114710A (en) * 1976-03-23 1977-09-26 Daikin Ind Ltd Process for making paper mixed with polytetrafluoroethylene
JPS5663770A (en) * 1979-10-26 1981-05-30 Asahi Glass Co Ltd Alkaline battery

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04139237A (en) * 1990-05-18 1992-05-13 Japan Gore Tex Inc Hydrophilic porous fluororesin material
US7622215B2 (en) 2004-03-04 2009-11-24 Panasonic Corporation Composite electrolyte membrane, catalyst-coated membrane assembly, membrane-electrode assembly and polymer electrolyte fuel cell
CN103066306A (en) * 2012-12-22 2013-04-24 大连理工大学 Ion exchange membrane used for zinc-bromine flow battery and preparation method thereof

Also Published As

Publication number Publication date
JPH0575835B2 (en) 1993-10-21

Similar Documents

Publication Publication Date Title
JPS61246394A (en) Diaphragm for electrolysis
CA2320696C (en) Ion conductive matrixes and their use
JP2604734B2 (en) Ion-permeable membrane and method for producing the same
WO2013183584A1 (en) Ion permeable diaphragm
JPWO2013100083A1 (en) Redox flow secondary battery and electrolyte membrane for redox flow secondary battery
EP2784861B1 (en) Diaphragm for redox flow batteries
JPS6399246A (en) Filmy raw material
CN109075369A (en) Composite membrane for flow battery
JPH06260183A (en) Diaphragm for aqueous solvent electrochemical device and battery with aqueous solvent using same
US2884387A (en) Porous membrane materials and process for producing the same
JP2673336B2 (en) Air-metal hydride secondary battery
JP2005285549A (en) Electrolyte film for solid polymer fuel cell
JP2005158383A (en) Redox cell
JP2019525387A (en) Ion exchange membrane and method for producing the same, membrane electrode assembly, and redox flow battery
JPS62252067A (en) Composite separator for battery
JPS6051505A (en) Gas selective composite membrane
JPS59166541A (en) Production of porous membrane of chemical resistance
JP2008144262A (en) Ion permeable diaphragm
JPS6352431B2 (en)
JPH0129310B2 (en)
JPS6151754A (en) Sealed lead storage battery
JPS62247093A (en) Novel multilayered diaphragm
JPH05326035A (en) Battery
JP2009104810A (en) Electrolyte membrane, membrane electrode assembly, fuel cell, and method of manufacturing electrolyte membrane
JPS62226581A (en) Redox flow battery

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term