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JPH07211323A - Air electrode, manufacture thereof, and air battery using the electrode - Google Patents

Air electrode, manufacture thereof, and air battery using the electrode

Info

Publication number
JPH07211323A
JPH07211323A JP6006077A JP607794A JPH07211323A JP H07211323 A JPH07211323 A JP H07211323A JP 6006077 A JP6006077 A JP 6006077A JP 607794 A JP607794 A JP 607794A JP H07211323 A JPH07211323 A JP H07211323A
Authority
JP
Japan
Prior art keywords
layer
air
electrode
current collector
gas diffusion
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.)
Pending
Application number
JP6006077A
Other languages
Japanese (ja)
Inventor
Koji Yoshizawa
浩司 芳澤
Akira Miura
晃 三浦
Takafumi Fujiwara
隆文 藤原
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP6006077A priority Critical patent/JPH07211323A/en
Publication of JPH07211323A publication Critical patent/JPH07211323A/en
Pending 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
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Inert Electrodes (AREA)
  • Hybrid Cells (AREA)

Abstract

PURPOSE:To provide an air positive electrode for an air battery with excellent high rate performance and high leakage resistance. CONSTITUTION:An air positive electrode 1 is constituted with a three-layer stack formed by arranging a catalyst layer 2 on the side facing to a gelled zinc negative electrode 6 through a cellophane separator 5, a gas diffusion layer 4 comprising a porous film made of polychlorotrifluoroethylene on an air taking-in side, and a current collecting layer 3 between these layers 2, 4.

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、酸素を活物質とし、強
負荷(ハイレート)の放電特性、耐漏液性に優れた空気
電極及びその製造方法並びにその電極を有する空気電池
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air electrode which uses oxygen as an active material and is excellent in discharge characteristics under high load (high rate) and resistance to liquid leakage, a method for producing the same, and an air battery having the electrode.

【0002】[0002]

【従来の技術】従来の円筒形空気電極においては、ガス
透過能を有し、撥水性のガス拡散層と、触媒層と、集電
体層との三層積層体を圧着して電極体とし、この電極体
を湾曲し、電極体の両端部を合成ゴムやエポキシ系接着
剤で接着したりあるいはスポット溶接などで溶接したり
して円筒体としていた。
2. Description of the Related Art In a conventional cylindrical air electrode, a three-layer laminate having a gas permeable and water-repellent gas diffusion layer, a catalyst layer and a current collector layer is pressure bonded to form an electrode body. The electrode body is curved, and both ends of the electrode body are adhered with a synthetic rubber or an epoxy adhesive or welded by spot welding to form a cylindrical body.

【0003】例えば、撥水性のガス拡散層としては、ポ
リテトラフルオロエチレン、ポリテトラフルオロエチレ
ン−ヘキサフルオロプロピレン共重合体などの弗素樹脂
からなる酸素ガス透過性の撥水性シートを用い、集電体
層としては、ニッケル網、エキスパンドメタルなどから
なる導電性シートを用い、触媒層としては、金属酸化物
と、活性炭と、ポリテトラフルオロエチレン分散媒とを
混合して多孔質のシート状にしたものを用いてシート状
積層電極体とし、この電極体を集電体層が内側になるよ
うに円筒状に湾曲し、両端部を重ね合わせて円筒形空気
電極としていた(特開昭57−208074号公報、特
開昭59−98479号公報、特開昭60−13616
8号公報参照)。
For example, as the water repellent gas diffusion layer, an oxygen gas permeable water repellent sheet made of a fluorine resin such as polytetrafluoroethylene or polytetrafluoroethylene-hexafluoropropylene copolymer is used, and a current collector is used. As the layer, a conductive sheet made of nickel mesh, expanded metal or the like is used, and as the catalyst layer, a metal oxide, activated carbon, and a polytetrafluoroethylene dispersion medium are mixed to form a porous sheet. Was used as a sheet-shaped laminated electrode body, and this electrode body was cylindrically curved so that the current collector layer was on the inside, and both ends were overlapped to form a cylindrical air electrode (JP-A-57-208074). JP-A-59-98479, JP-A-60-13616
No. 8).

【0004】また、この重ね合わせる両端部のガス拡散
層および触媒層は除去して集電体層を露出させ、この露
出した集電体層同志をスポット溶接、ビーム溶接などに
より溶着し、この溶着部分を液密状態にするため、この
溶着部分に弗素系樹脂を充填して液密にし、かつこの重
ね合わせ部分の補強をしていた(特開昭58−7577
3号公報参照)。
Further, the gas diffusion layer and the catalyst layer at both ends of the overlapping are removed to expose the current collector layer, and the exposed current collector layers are welded by spot welding, beam welding or the like, and the welding is performed. In order to make the portion liquid-tight, the welded portion was filled with a fluororesin to make it liquid-tight, and the overlapping portion was reinforced (JP-A-58-7577).
(See Japanese Patent Publication No. 3).

【0005】また、液密で機械的強度の大きい空気電極
にするため、上記のようにシート状積層電極体とせず
に、先ず集電体層を湾曲し、その両端部を溶着して予め
円筒形集電体層を形成し、この円筒形集電体層の外周に
多孔質触媒層を、さらにその触媒層の外周をポリプロピ
レンなどの撥水性を有するガス拡散層により、それぞれ
の両端部を重ね合わせて巻き、その後ガス拡散層を加熱
圧着して円筒形空気電極にしたものがあった(特開昭5
8−198862号公報参照)。
Further, in order to obtain an air electrode which is liquid-tight and has high mechanical strength, the current collector layer is first curved and both ends thereof are welded to each other in advance to form a cylinder without using the sheet-like laminated electrode body as described above. The current collector layer is formed, and a porous catalyst layer is formed on the outer circumference of the cylindrical current collector layer, and the outer circumference of the catalyst layer is further overlapped by a gas diffusion layer having water repellency such as polypropylene. In some cases, the air was wound together, and then the gas diffusion layer was heat-pressed to form a cylindrical air electrode (Japanese Patent Laid-Open No. Sho 5).
No. 8-198862).

【0006】[0006]

【発明が解決しようとする課題】従来の円筒形空気電極
にあっては、最外周に存在する撥水性を有するガス拡散
層により機械的強度を大きくし、漏液を防止している。
In the conventional cylindrical air electrode, the mechanical strength is increased by the water-repellent gas diffusion layer existing on the outermost periphery to prevent liquid leakage.

【0007】しかし、ガス拡散層を構成しているポリテ
トラフルオロエチレン、ポリテトラフルオロエチレン−
ヘキサフルオロプロピレン共重合体、ポリプロピレンな
どの材料は、フィルム類の中では表面エネルギーが低い
ため撥水性には優れているが、粘着性は非常に乏しいこ
とから、ガス拡散層を巻き付けても集電体層および触媒
層との結着力が非常に弱いものであった。
However, polytetrafluoroethylene, polytetrafluoroethylene-that constitutes the gas diffusion layer
Materials such as hexafluoropropylene copolymer and polypropylene are excellent in water repellency because of their low surface energy among films, but their adhesiveness is very poor. The binding force with the body layer and the catalyst layer was very weak.

【0008】そこで、このようにして構成した空気電極
を用いて空気電池にした場合、放電に伴ってガス拡散層
と触媒層の界面、あるいはガス拡散層と集電体層との界
面に電解液が浸透してその部分に液膜が形成され、この
液膜が酸素の供給を遮断することにより放電不可能にな
る惧れがあるという問題点があった。
Therefore, when an air battery is formed by using the air electrode thus constructed, an electrolytic solution is formed at the interface between the gas diffusion layer and the catalyst layer or at the interface between the gas diffusion layer and the current collector layer due to discharge. However, there is a problem in that there is a possibility that discharge will become impossible due to the permeation of oxygen and the formation of a liquid film at that portion, and this liquid film interrupts the supply of oxygen.

【0009】ボタン形空気電池のように大電流を流さな
い電池に用いる空気電極においては、ガス拡散層と触媒
層との界面あるいはガス拡散層と集電体層との界面に弗
素樹脂ディスパージョンを塗布して撥水性を向上させる
だけで容易に液膜の生成が阻止できるが、円筒形空気電
池のように大電流を必要とする電池に用いる空気電極の
場合は、上記のような撥水性処理をしただけでは不十分
で、依然として液膜が生成されるという問題点があっ
た。
In an air electrode used in a battery that does not flow a large current such as a button type air battery, a fluororesin dispersion is formed at the interface between the gas diffusion layer and the catalyst layer or the interface between the gas diffusion layer and the current collector layer. The formation of a liquid film can be easily prevented simply by applying it to improve the water repellency, but in the case of an air electrode used for a battery that requires a large current such as a cylindrical air battery, the above water repellency treatment is applied. However, there is a problem in that a liquid film is still formed by simply performing.

【0010】また、ポリテトラフルオロエチレンのよう
なガス拡散層を用いて融点以上の温度に加熱し、触媒層
などとの界面を熱溶着により接合させて液膜の生成を阻
止した場合、ポリテトラフルオロエチレンは340〜3
80℃に温度を上げても溶融粘度が1011〜1013ポイ
ズと非常に高いため、界面を接合させるためには圧力を
かけたまま冷却して結合する必要があり、その結果、ピ
ンホールがなくこの部分からの漏液のない空気電極を円
筒形に組み立てる場合、非常に複雑で高度の技術を要す
るといった問題点があった。
When a gas diffusion layer such as polytetrafluoroethylene is used to heat above the melting point and the interface with the catalyst layer or the like is joined by heat welding to prevent the formation of a liquid film, polytetrafluoroethylene is used. Fluoroethylene is 340-3
Since the melt viscosity is as high as 10 11 to 10 13 poise even if the temperature is raised to 80 ° C., it is necessary to cool and bond under pressure in order to bond the interface, and as a result, pinholes are formed. However, when assembling an air electrode that does not leak from this portion into a cylindrical shape, there is a problem that it is very complicated and requires a high degree of technology.

【0011】また、ポリテトラフルオロエチレン−ヘキ
サフルオロプロピレン共重合体をガス拡散層に用いた場
合は、逆に溶融粘度が104〜105ポイズと非常に低
く、接合のため溶融させると、流れだし、変形したり、
多孔質の触媒層および多孔性のガス拡散層の孔部を塞い
で機能を低下させたりして、ガス透過能などがなくなる
という問題点があった。
When a polytetrafluoroethylene-hexafluoropropylene copolymer is used for the gas diffusion layer, on the contrary, the melt viscosity is very low at 10 4 to 10 5 poises, and when melted for bonding, the flow Dashi, transform,
There is a problem that the gas permeability is lost by closing the pores of the porous catalyst layer and the porous gas diffusion layer to deteriorate the function.

【0012】したがって、円筒形空気電池のように大電
流を必要とする電池に用いる空気電極の場合、ガス拡散
層と触媒層などとの界面の接合性の確保が、放電特性あ
るいは耐漏液性の点で重要な課題となる。
Therefore, in the case of an air electrode used in a battery requiring a large current such as a cylindrical air battery, it is necessary to secure the bonding property at the interface between the gas diffusion layer and the catalyst layer in order to secure the discharge characteristics or the leakage resistance. This is an important issue in terms of points.

【0013】本発明は、大電流を流すことにより発生す
るガス拡散層と触媒層などとの界面での液膜の生成を阻
止し、強負荷放電特性、耐漏液性に優れた空気電極及び
その製造方法並びにその電極を有する空気電池を提供す
ることを目的としている。
The present invention prevents the formation of a liquid film at the interface between a gas diffusion layer and a catalyst layer, which is generated by passing a large current, and has an air electrode excellent in heavy load discharge characteristics and liquid leakage resistance, and an air electrode thereof. An object is to provide a manufacturing method and an air battery having the electrode.

【0014】[0014]

【課題を解決するための手段】上記目的を達成するため
に、本発明の空気電極においては、集電体層と、この集
電体層の一方側に配したガス透過能を有するガス拡散層
と、前記集電体層の他方側に配した触媒層との積層体に
より電極体を構成するとともに、前記ガス拡散層はポリ
クロロトリフルオロエチレンの多孔性膜で形成したもの
である。
In order to achieve the above object, in the air electrode of the present invention, a current collector layer and a gas diffusion layer having gas permeability which is disposed on one side of the current collector layer. And a catalyst layer disposed on the other side of the current collector layer to form an electrode body, and the gas diffusion layer is formed of a polychlorotrifluoroethylene porous film.

【0015】また、触媒層を内側にして円筒状に湾曲さ
せることによって円筒形の空気電極とすることもでき
る。
Further, a cylindrical air electrode can be obtained by curving the catalyst layer inside with a cylindrical shape.

【0016】さらに、上記目的を達成するために、本発
明の空気電極の製造方法においては、集電体層と触媒層
との積層体を、前記触媒層を内側にして円筒体に形成
し、この円筒体の外周にポリクロロトリフルオロエチレ
ンの多孔性膜を巻回し、ついで熱処理して前記多孔性膜
を円筒体に接合するものである。
Further, in order to achieve the above object, in the method for producing an air electrode of the present invention, a laminate of a current collector layer and a catalyst layer is formed into a cylindrical body with the catalyst layer inside. A porous membrane of polychlorotrifluoroethylene is wound around the outer periphery of this cylindrical body, and then heat treated to bond the porous membrane to the cylindrical body.

【0017】また、熱処理条件は、温度220℃で2時
間熱処理するように設定すると効果的である。
It is effective to set the heat treatment conditions such that the heat treatment is performed at a temperature of 220 ° C. for 2 hours.

【0018】さらに、上記目的を達成するために、本発
明の空気電池においては、集電体層と、この集電体層の
一方側に配したガス透過能を有するポリクロロトリフル
オロエチレン多孔性膜のガス拡散層と、前記集電体の他
方側に配した触媒層との積層体により正極を構成し、こ
の正極にセパレータを介して負極を設けたものである。
Further, to achieve the above object, in the air battery of the present invention, a current collector layer and a gas-permeable polychlorotrifluoroethylene porous layer disposed on one side of the current collector layer. A positive electrode is composed of a laminate of a gas diffusion layer of the membrane and a catalyst layer arranged on the other side of the current collector, and the negative electrode is provided on the positive electrode via a separator.

【0019】また、触媒層を内側とした円筒形正極の内
部に、セパレータを介して負極を位置させて円筒形の空
気電池とすることもできる。
Further, the negative electrode can be positioned inside the cylindrical positive electrode having the catalyst layer inside with a separator interposed therebetween to form a cylindrical air battery.

【0020】[0020]

【作用】上記のように構成される空気電極及びそれを正
極とした空気電池は、以下に記載するように作用する。
The air electrode constructed as described above and the air battery using the air electrode as a positive electrode operate as described below.

【0021】ガス拡散層に用いるポリクロロトリフルオ
ロエチレンは、弗素系の合成樹脂に属するため撥水性が
高く、融点は210〜212℃で、ポリテトラフルオロ
エチレン、ポリテトラフルオロエチレン−ヘキサフルオ
ロプロピレン共重合体の融点に比べ低いので低温で溶融
し、また溶融粘度は107ポイズで、ポリテトラフルオ
ロエチレンのそれよりは小さく、ポリテトラフルオロエ
チレン−ヘキサフルオロプロピレン共重合体のそれより
は大きいものとなっている。
The polychlorotrifluoroethylene used in the gas diffusion layer has a high water repellency because it belongs to a fluorine-based synthetic resin, and has a melting point of 210 to 212 ° C., and polytetrafluoroethylene and polytetrafluoroethylene-hexafluoropropylene Since it is lower than the melting point of the polymer, it melts at a low temperature and has a melt viscosity of 10 7 poise, which is smaller than that of polytetrafluoroethylene and larger than that of polytetrafluoroethylene-hexafluoropropylene copolymer. Has become.

【0022】したがって、界面での液膜の生成を阻止す
るために、ガス拡散層を触媒層あるいは集電体層と接合
させる場合、比較的低温で熱融着が可能となり、その上
溶融粘度がポリテトラフルオロエチレンのそれよりは小
さいので、接合のために圧力をかけたまま冷却して接合
させる必要がなく、また、ポリテトラフルオロエチレン
−ヘキサフルオロプロピレン共重合体の溶融粘度より大
きいので、溶融して流れだし、孔部を塞いでその機能を
阻害することもなくなる。
Therefore, when the gas diffusion layer is joined to the catalyst layer or the current collector layer in order to prevent the formation of the liquid film at the interface, the heat fusion can be performed at a relatively low temperature, and the melt viscosity is increased. Since it is smaller than that of polytetrafluoroethylene, it is not necessary to cool and join while applying pressure for joining, and since it is larger than the melt viscosity of polytetrafluoroethylene-hexafluoropropylene copolymer, Then, it starts to flow, and it does not obstruct the function by blocking the hole.

【0023】そこで、ガス拡散層として撥水性を有する
ポリクロロトリフルオロエチレンを用いると、比較的低
温の熱処理のみで触媒層あるいは集電体層と良好に接合
することができ、強負荷放電特性および耐漏液性に優れ
たものになる。
Therefore, when polychlorotrifluoroethylene having water repellency is used as the gas diffusion layer, it can be bonded well to the catalyst layer or the current collector layer only by heat treatment at a relatively low temperature, and the high load discharge characteristics and It has excellent leakage resistance.

【0024】[0024]

【実施例】本発明の具体的な実施例を図面を参照して説
明する。図1は、円筒形空気亜鉛電池の断面図を示し、
図1において、1は円筒形空気正極で、図2に示すよう
に触媒層2と、この触媒層2に圧着した集電体層3と、
撥水性で多孔性膜であるガス拡散層4との3層積層体を
触媒層2を内側にして円筒状に形成している。5は空気
正極1の内面と接触したセロハンセパレータ、6は空気
正極1の触媒層2とセパレータ5を介して存するゲル状
亜鉛負極、7は空気正極1の外周すなわちガス拡散層4
と接触する空気拡散紙、8は空気正極1、ゲル状亜鉛負
極6などの発電要素を収容した円筒状正極缶、9は正極
缶8の外周を被覆する絶縁チューブ、10は正極缶8お
よび絶縁チューブ9に設けた空気を取り入れる透孔、1
1は透孔10を閉塞する密封シールで、電池を使用する
際に除去する。12は皿紙、13は金属製の正極キャッ
プ、14は金属製の集電キャップで、正極キャップ13
および集電キャップ14とにより空気正極1の端部を圧
着挟持して集電体層3と接触し、正極缶8とはスポット
溶接により一体に導通結合されている。15は有機成分
からなる封止剤、16は合成樹脂封口体、17は負極端
子キャップ、18はゲル状亜鉛負極6内に埋設した負極
集電体である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Specific embodiments of the present invention will be described with reference to the drawings. FIG. 1 shows a cross-sectional view of a cylindrical zinc-air battery,
In FIG. 1, reference numeral 1 is a cylindrical air positive electrode, and as shown in FIG. 2, a catalyst layer 2 and a current collector layer 3 pressure-bonded to the catalyst layer 2,
A three-layer laminate with a water-repellent and porous gas diffusion layer 4 is formed into a cylindrical shape with the catalyst layer 2 inside. Reference numeral 5 is a cellophane separator in contact with the inner surface of the air positive electrode 1, 6 is a gel-like zinc negative electrode existing via the catalyst layer 2 of the air positive electrode 1 and the separator 5, and 7 is an outer periphery of the air positive electrode 1, that is, a gas diffusion layer 4
An air diffusion paper in contact with 8; a cylindrical positive electrode can 8 containing a power generating element such as the air positive electrode 1 and the gelled zinc negative electrode 6; 9 an insulating tube covering the outer periphery of the positive electrode can 8; A through hole provided in the tube 9 for taking in air, 1
Reference numeral 1 denotes a hermetic seal that closes the through hole 10 and is removed when the battery is used. 12 is a dish paper, 13 is a positive electrode cap made of metal, 14 is a current collecting cap made of metal, and the positive electrode cap 13
The end of the air positive electrode 1 is pressed and sandwiched by the current collecting cap 14 to contact the current collector layer 3, and the positive electrode can 8 is integrally conductively connected by spot welding. Reference numeral 15 is a sealant made of an organic component, 16 is a synthetic resin sealing body, 17 is a negative electrode terminal cap, and 18 is a negative electrode current collector embedded in the gel zinc negative electrode 6.

【0025】集電体層3としては、線径0.15mmの
ステンレス線を40メッシュ相当に織ったネットを用
い、触媒層2としては、活性炭3Kg、マンガン酸化物
4Kg、カーボンブラック1.5Kg、弗素樹脂粉末
0.7Kgを混合し、この混合物にエチルアルコールを
加えて混練した後、押し出し成形により偏平帯状にし、
さらに約60℃に加熱した2本のローラ間に通して圧延
して厚さ0.6mmのシート状にしたものを用いる。
As the current collector layer 3, a net formed by weaving stainless wire having a wire diameter of 0.15 mm to a size of 40 mesh is used, and as the catalyst layer 2, 3 kg of activated carbon, 4 kg of manganese oxide, 1.5 kg of carbon black, 0.7 kg of fluororesin powder was mixed, ethyl alcohol was added to this mixture and kneaded, and then flattened into a flat band by extrusion molding.
Further, it is passed through two rollers heated to about 60 ° C. and rolled to form a sheet having a thickness of 0.6 mm.

【0026】集電体層3に触媒層2をプレスにより圧着
して形成した2層の積層シートを、触媒層2が内側にな
るようにして円筒状に湾曲し、両端部の重なった部分の
触媒層2は除去し、露出した集電体層3同志をスポット
溶接して円筒形とする。ガス拡散層4としては、ガス透
過能を有する多孔性膜に成形したポリクロロトリフルオ
ロエチレンを用い、上記触媒層2および集電体層3の積
層体からなる円筒の外周に巻き付け、220℃で2時間
熱処理することによりガス拡散層4を円筒の外周、すな
わち触媒層2および集電体層3の一部に接合して3層積
層体からなる円筒形空気正極1とする。なお、ガス拡散
層4を円筒の外周に巻き付ける回数は、機械的強度およ
び液密性の面から2回以上が好ましい。
A two-layer laminated sheet formed by press-bonding the catalyst layer 2 to the current collector layer 3 by pressing is curved into a cylindrical shape with the catalyst layer 2 on the inside, and the two end portions are overlapped. The catalyst layer 2 is removed, and the exposed current collector layers 3 are spot-welded into a cylindrical shape. As the gas diffusion layer 4, polychlorotrifluoroethylene formed into a porous film having gas permeability is used, and it is wound around the outer circumference of a cylinder made of a laminate of the catalyst layer 2 and the current collector layer 3 at 220 ° C. By heat treatment for 2 hours, the gas diffusion layer 4 is bonded to the outer periphery of the cylinder, that is, a part of the catalyst layer 2 and the current collector layer 3 to form the cylindrical air positive electrode 1 composed of a three-layer laminate. The number of times the gas diffusion layer 4 is wound around the outer circumference of the cylinder is preferably 2 or more in terms of mechanical strength and liquid tightness.

【0027】ゲル状亜鉛負極6は、40重量%の水酸化
カリウム水溶液(酸化亜鉛を3重量%含む)に、3重量
%のポリアクリル酸ソーダと1重量%のカルボキシメチ
ルセルロースとを加えてゲル状電解液とし、つぎに、こ
のゲル状電解液に対して重量比で2倍の亜鉛粉末を添加
して混合することにより調整した。
The gelled zinc negative electrode 6 is a gelled gel obtained by adding 3% by weight of sodium polyacrylate and 1% by weight of carboxymethylcellulose to a 40% by weight potassium hydroxide aqueous solution (containing 3% by weight of zinc oxide). An electrolytic solution was prepared, and then, zinc powder was added and mixed in a weight ratio of 2 to the gel electrolytic solution, and mixed.

【0028】以上のようにして構成した円筒形空気亜鉛
電池についての分極状況を測定した結果は、図3に示す
通りであり、測定試験は、所定の電流で放電したときの
電池の維持電圧の値を示している。なお、図3におい
て、No.1はガス拡散層にポリクロロトリフルオロエ
チレンの多孔性膜を用いた上記実施例による空気亜鉛電
池の維持電圧、No.2はガス拡散層にポリテトラフル
オロエチレンの多孔性膜を用いた従来の空気亜鉛電池の
維持電圧、No.3はガス拡散層にポリテトラフルオロ
エチレン−ヘキサフルオロプロピレン共重合体の多孔性
膜を用いた従来の空気亜鉛電池の維持電圧で、これらN
o.2およびNo.3の場合はガス拡散層を接合するた
めの熱処理は施していない。No.4はNo.2におい
てポリテトラフルオロエチレンの融点以上の340℃で
2時間熱処理した場合の維持電圧、No.5はNo.3
においてポリテトラフルオロエチレン−ヘキサフルオロ
プロピレン共重合体の融点以上の280℃で2時間熱処
理した場合の維持電圧である。
The result of measuring the polarization state of the cylindrical zinc-air battery constructed as described above is as shown in FIG. 3, and the measurement test was carried out by measuring the sustain voltage of the battery when discharged at a predetermined current. Indicates the value. In addition, in FIG. No. 1 is the sustain voltage of the zinc-air battery according to the above-mentioned embodiment using a porous membrane of polychlorotrifluoroethylene for the gas diffusion layer. No. 2 is the sustain voltage of a conventional air zinc battery using a porous film of polytetrafluoroethylene for the gas diffusion layer, No. 2 Reference numeral 3 is the sustaining voltage of a conventional air zinc battery using a porous film of polytetrafluoroethylene-hexafluoropropylene copolymer for the gas diffusion layer.
o. 2 and No. In the case of 3, the heat treatment for joining the gas diffusion layers was not performed. No. No. 4 is No. In No. 2, the sustain voltage when heat-treated at 340 ° C., which is higher than the melting point of polytetrafluoroethylene, for 2 hours. No. 5 is No. Three
Is the sustain voltage when heat-treated at 280 ° C. for 2 hours at or above the melting point of the polytetrafluoroethylene-hexafluoropropylene copolymer.

【0029】図3において、No.2およびNo.3の
場合は電流値100mAで維持電圧が1.0Vを下回っ
ているが、これは触媒層とガス拡散層との接合が弱く、
この接合部分に放電により電解液が浸透して液膜を生成
し、酸素が触媒層に供給できにくくなって維持電圧が低
下したものと思われる。No.4の場合は、No.2の
場合に比べ僅か改善はされているが大電流を必要とする
電池としては不十分である。No.5の場合は、熱処理
によりポリテトラフルオロエチレン−ヘキサフルオロプ
ロピレン共重合体の多孔膜が溶融し、溶融粘度が低いこ
とにより流れだし、多孔性膜の孔部分を塞いで酸素の供
給をできなくしたためと思われる。
In FIG. 2 and No. In the case of 3, the current value was 100 mA and the sustain voltage was less than 1.0 V, but this was because the bond between the catalyst layer and the gas diffusion layer was weak,
It is considered that the electrolytic solution permeated into this joint portion due to the discharge to form a liquid film, and it was difficult to supply oxygen to the catalyst layer, so that the sustain voltage was lowered. No. In the case of No. 4, No. Although it is slightly improved as compared with the case of 2, it is insufficient as a battery requiring a large current. No. In the case of 5, the heat treatment melted the porous film of the polytetrafluoroethylene-hexafluoropropylene copolymer, which started to flow due to the low melt viscosity, blocking the pores of the porous film and making it impossible to supply oxygen. I think that the.

【0030】しかし、No.1の場合は、良好な分極特
性を示しており、これは触媒層とガス拡散層との接合が
強くなっているので、この接合部分に放電により電解液
が浸透して液膜が生成するのを阻止し、酸素を充分に触
媒層に供給できるためと思われる。
However, no. In the case of No. 1, good polarization characteristics are exhibited, and since the bonding between the catalyst layer and the gas diffusion layer is strong, the electrolytic solution permeates into this bonding portion due to discharge, and a liquid film is formed. It is believed that the above can be prevented and oxygen can be sufficiently supplied to the catalyst layer.

【0031】[0031]

【発明の効果】本発明は、以上のように構成されている
ので、以下に記載されるような効果を奏する。
Since the present invention is constituted as described above, it has the following effects.

【0032】空気電極は、集電体層と、この集電体層の
一方側に配したガス透過能を有するガス拡散層と、前記
集電体層の他方側に配した触媒層との積層体により電極
体を構成し、前記ガス拡散層は、撥水性および接合性を
有するポリクロロトリフルオロエチレンの多孔性膜で形
成することにより、ガス拡散層が、良好に触媒層あるい
は集電体層と接合され、強負荷放電特性および耐漏液性
に優れたものが得られる。
The air electrode is a stack of a current collector layer, a gas diffusion layer having gas permeability which is arranged on one side of the current collector layer, and a catalyst layer arranged on the other side of the current collector layer. The electrode body is constituted by a body, and the gas diffusion layer is formed of a porous film of polychlorotrifluoroethylene having water repellency and bonding properties, so that the gas diffusion layer can be satisfactorily used as a catalyst layer or a collector layer. And is excellent in heavy load discharge characteristics and liquid leakage resistance.

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

【図1】本発明の一実施例における円筒形空気亜鉛電池
の断面図
FIG. 1 is a sectional view of a cylindrical zinc-air battery according to an embodiment of the present invention.

【図2】図1におけるA部の拡大説明図FIG. 2 is an enlarged explanatory view of a portion A in FIG.

【図3】円筒形空気亜鉛電池の分極特性線図[Fig. 3] Polarization characteristic diagram of cylindrical zinc-air battery

【符号の説明】[Explanation of symbols]

1 円筒形空気正極 2 触媒層 3 集電体層 4 ガス拡散層 5 セロハンセパレータ 6 ゲル状亜鉛負極 1 Cylindrical Air Positive Electrode 2 Catalyst Layer 3 Current Collector Layer 4 Gas Diffusion Layer 5 Cellophane Separator 6 Gel Zinc Negative Electrode

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 集電体層と、この集電体層の一方側に配
したガス透過能を有するガス拡散層と、前記集電体層の
他方側に配した触媒層との積層体により電極体を構成
し、前記ガス拡散層はポリクロロトリフルオロエチレン
の多孔性膜で形成した空気電極。
1. A laminate of a current collector layer, a gas diffusion layer having gas permeability which is disposed on one side of the current collector layer, and a catalyst layer disposed on the other side of the current collector layer. An air electrode which constitutes an electrode body and in which the gas diffusion layer is formed of a porous membrane of polychlorotrifluoroethylene.
【請求項2】 触媒層を内側にして円筒状にした請求項
1記載の空気電極。
2. The air electrode according to claim 1, which has a cylindrical shape with the catalyst layer inside.
【請求項3】 集電体層と触媒層との積層体を、前記触
媒層を内側にして円筒体に形成し、この円筒体の外周に
ポリクロロトリフルオロエチレンの多孔性膜を巻回し、
ついで熱処理して前記多孔性膜を円筒体に接合する空気
電極の製造方法。
3. A laminated body of a current collector layer and a catalyst layer is formed into a cylindrical body with the catalyst layer inside, and a porous membrane of polychlorotrifluoroethylene is wound around the outer periphery of the cylindrical body,
Then, a method of manufacturing an air electrode in which the porous membrane is joined to the cylindrical body by heat treatment.
【請求項4】 温度220℃で2時間熱処理する請求項
3記載の空気電極の製造方法。
4. The method for producing an air electrode according to claim 3, wherein the heat treatment is performed at a temperature of 220 ° C. for 2 hours.
【請求項5】 集電体層と、この集電体層の一方側に配
したガス透過能を有するポリクロロトリフルオロエチレ
ン多孔性膜のガス拡散層と、前記集電体の他方側に配し
た触媒層との積層体により正極を構成し、この正極にセ
パレータを介して負極を設けた空気電池。
5. A current collector layer, a gas diffusion layer of polychlorotrifluoroethylene porous membrane having gas permeability which is disposed on one side of the current collector layer, and a gas diffusion layer on the other side of the current collector. An air battery in which a positive electrode is constituted by a laminate with the catalyst layer, and a negative electrode is provided on the positive electrode via a separator.
【請求項6】 触媒層を内側とした円筒形正極の内部
に、セパレータを介して負極を設けた請求項5記載の空
気電池。
6. The air battery according to claim 5, wherein a negative electrode is provided inside a cylindrical positive electrode having a catalyst layer inside with a separator interposed therebetween.
JP6006077A 1994-01-25 1994-01-25 Air electrode, manufacture thereof, and air battery using the electrode Pending JPH07211323A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6006077A JPH07211323A (en) 1994-01-25 1994-01-25 Air electrode, manufacture thereof, and air battery using the electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6006077A JPH07211323A (en) 1994-01-25 1994-01-25 Air electrode, manufacture thereof, and air battery using the electrode

Publications (1)

Publication Number Publication Date
JPH07211323A true JPH07211323A (en) 1995-08-11

Family

ID=11628512

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6006077A Pending JPH07211323A (en) 1994-01-25 1994-01-25 Air electrode, manufacture thereof, and air battery using the electrode

Country Status (1)

Country Link
JP (1) JPH07211323A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016533006A (en) * 2013-07-31 2016-10-20 アクアハイドレックス プロプライエタリー リミテッドAquahydrex Pty Ltd Three-dimensional composite electrode and manufacturing method
US10577700B2 (en) 2012-06-12 2020-03-03 Aquahydrex Pty Ltd Breathable electrode structure and method for use in water splitting
US11005117B2 (en) 2019-02-01 2021-05-11 Aquahydrex, Inc. Electrochemical system with confined electrolyte

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6217193A (en) * 1985-07-13 1987-01-26 Shirakawa Seisakusho:Kk Gas permeable membrane
JPS63229122A (en) * 1987-12-25 1988-09-26 Shirakawa Seisakusho:Kk Preparation of gas permeable membrane
JPH05144482A (en) * 1991-11-25 1993-06-11 Matsushita Electric Ind Co Ltd Cylindrical air cell and electrode manufacturing method

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6217193A (en) * 1985-07-13 1987-01-26 Shirakawa Seisakusho:Kk Gas permeable membrane
JPS63229122A (en) * 1987-12-25 1988-09-26 Shirakawa Seisakusho:Kk Preparation of gas permeable membrane
JPH05144482A (en) * 1991-11-25 1993-06-11 Matsushita Electric Ind Co Ltd Cylindrical air cell and electrode manufacturing method

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10577700B2 (en) 2012-06-12 2020-03-03 Aquahydrex Pty Ltd Breathable electrode structure and method for use in water splitting
JP2016533006A (en) * 2013-07-31 2016-10-20 アクアハイドレックス プロプライエタリー リミテッドAquahydrex Pty Ltd Three-dimensional composite electrode and manufacturing method
US10637068B2 (en) 2013-07-31 2020-04-28 Aquahydrex, Inc. Modular electrochemical cells
US11018345B2 (en) 2013-07-31 2021-05-25 Aquahydrex, Inc. Method and electrochemical cell for managing electrochemical reactions
US11005117B2 (en) 2019-02-01 2021-05-11 Aquahydrex, Inc. Electrochemical system with confined electrolyte
US11682783B2 (en) 2019-02-01 2023-06-20 Aquahydrex, Inc. Electrochemical system with confined electrolyte
US12080928B2 (en) 2019-02-01 2024-09-03 Edac Labs, Inc. Electrochemical system with confined electrolyte

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