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JPH0119626B2 - - Google Patents
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JPH0119626B2 - - Google Patents

Info

Publication number
JPH0119626B2
JPH0119626B2 JP56191943A JP19194381A JPH0119626B2 JP H0119626 B2 JPH0119626 B2 JP H0119626B2 JP 56191943 A JP56191943 A JP 56191943A JP 19194381 A JP19194381 A JP 19194381A JP H0119626 B2 JPH0119626 B2 JP H0119626B2
Authority
JP
Japan
Prior art keywords
acid
air electrode
metal phthalocyanine
carbon
carbon body
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP56191943A
Other languages
Japanese (ja)
Other versions
JPS5894765A (en
Inventor
Katsuo Deguchi
Kunihiko Ootaguro
Denkichi Sasage
Takeshi Toyama
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.)
Pentel Co Ltd
Original Assignee
Pentel 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 Pentel Co Ltd filed Critical Pentel Co Ltd
Priority to JP56191943A priority Critical patent/JPS5894765A/en
Publication of JPS5894765A publication Critical patent/JPS5894765A/en
Publication of JPH0119626B2 publication Critical patent/JPH0119626B2/ja
Granted 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
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9008Organic or organo-metallic compounds
    • 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

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inert Electrodes (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、空気電池や燃料電池などに使用する
空気極の製造方法に関するものである。 従来、空気電池や燃料電池の空気極は、カーボ
ンブラツク、活性炭などの炭素体に酸素還元能力
を高めるために金属フタロシアニンを触媒として
用いていたが、金属フタロシアニンは水に不溶の
ため、キノリンなどの特殊な有機溶媒に溶解し、
この溶液に炭素体を浸漬し、乾燥後、有機溶媒を
飛散させ炭素体に金属フタロシアニンを含浸せし
めていたが、以下の様な欠点を有していた。 即ち、金属フタロシアニンを溶解するために使
用されるキノリン、N・N―ジメチルホルムアミ
ド、α―クロロナフタリンなどの有機溶媒は、金
属フタロシアニンに対する溶解度が1%以下であ
るため、炭素体に必要量の金属フタロシアニンを
含浸せしめるためには、溶液の含浸、溶媒の除去
を何回も繰り返す必要があり、又、各溶媒の沸点
がN・N―ジメチルホルムアミド(153℃)以外
は、キノリン(238℃)、α―クロルナフタリン
(263℃)のように200℃以上であり、乾燥が極め
て困難であり、乾燥させるために高価な装置を使
用する必要があつた。 本発明者らは、金属フタロシアニンの溶媒につ
いて種々検討を行なつた結果、ハロゲノ酢酸が好
適であることを見い出し、遂に本発明を完成した
ものであり、即ち、本発明は金属フタロシアニン
をハロゲノ酢酸に溶解し、炭素体に含浸せしめる
ことを特徴とする空気極の製造方法を要旨とする
ものである。 本発明の金属フタロシアニンの溶媒として使用
されるハロゲノ酢酸は、金属フタロシアニンに対
する溶解度が5〜10%であるため、炭素体に必要
量の金属フタロシアニンを含浸せしめることは容
易であり、又、沸点200℃以下のハロゲノ酢酸を
使用すれば、乾燥も容易であり、高価な装置も必
要としないため、空気電池の製造が容易である。 以下、本発明を組成に従い詳細に説明する。 金属フタロシアニンとしては、遷移金属の鉄、
ニツケル、銅などのフタロシアニンが使用され、
95%硫酸から再結晶させた純度が90%以上のもの
が好ましい。 金属フタロシアニンを溶解させるために使用さ
れるハロゲノ酢酸としては、下表に示されたフロ
ロ、クロル誘導体が望ましく使用される。
The present invention relates to a method for manufacturing an air electrode used in air cells, fuel cells, and the like. Conventionally, the air electrodes of air cells and fuel cells have used metal phthalocyanine as a catalyst to increase the ability to reduce oxygen to carbon materials such as carbon black and activated carbon. Dissolved in special organic solvent,
A carbon body was immersed in this solution, and after drying, the organic solvent was scattered to impregnate the carbon body with metal phthalocyanine, but this method had the following drawbacks. That is, the organic solvents used to dissolve metal phthalocyanine, such as quinoline, N/N-dimethylformamide, and α-chloronaphthalene, have a solubility of 1% or less for metal phthalocyanine, so they do not contain the required amount of metal in the carbon body. In order to impregnate phthalocyanine, it is necessary to repeat impregnation with the solution and removal of the solvent many times, and each solvent has a boiling point other than N-N-dimethylformamide (153°C), quinoline (238°C), Like α-chlornaphthalene (263°C), the temperature is over 200°C, making it extremely difficult to dry and requiring the use of expensive equipment. The present inventors have conducted various studies on solvents for metal phthalocyanine, and as a result, have found that halogenoacetic acid is suitable, and have finally completed the present invention.That is, the present invention has been made by converting metal phthalocyanine into halogenoacetic acid. The gist of the present invention is a method for producing an air electrode, which is characterized by dissolving the material and impregnating it into a carbon body. Since the halogenoacetic acid used as a solvent for the metal phthalocyanine of the present invention has a solubility in the metal phthalocyanine of 5 to 10%, it is easy to impregnate the carbon body with the required amount of metal phthalocyanine, and the boiling point is 200°C. If the following halogenoacetic acid is used, drying is easy and expensive equipment is not required, making it easy to manufacture an air battery. Hereinafter, the present invention will be explained in detail according to the composition. Examples of metal phthalocyanine include transition metal iron,
Phthalocyanines such as nickel and copper are used,
Preferably, the purity is 90% or more when recrystallized from 95% sulfuric acid. As the halogenoacetic acid used to dissolve the metal phthalocyanine, the fluoro and chloride derivatives shown in the table below are preferably used.

【表】 炭素体としては、フアーネスブラツク、チヤン
ネルブラツク、サーマルブラツクなどのカーボン
ブラツクや、木材、木炭、ヤシ殻炭、パーム核
炭、石炭、石油残査、合成樹脂、有機廃棄物など
を使用して作られた活性炭や黒鉛などの1種もし
くは2種以上の混合物が挙げられ、必要に応じて
押出成形、射出成形、加圧成形などにより一定の
形状とする。 上述した金属フタロシアニンをハロゲノ酢酸で
溶解し、5〜10%の金属フタロシアニン溶液を
得、この溶液に炭素体を含浸せしめ、常法により
ハロゲノ酢酸を除去することにより目的の空気極
が得られる。 以下、実施例に従い更に詳細に説明するが、実
施例中「部」とあるのは「重量部」を示す。 実施例 1 粒径0.1〜1μのヤシ殻活性炭10部、粒径0.1〜
0.5μの黒鉛10部、熱可塑性樹脂(塩化ビニル樹
脂)5部を混合し、押出成形により直径10mmの丸
棒を作り、その後、200℃に加熱処理して熱可塑
性樹脂を分解して炭素体とした。 この炭素体を鉄フタロシアニンを10重量%溶解
せしめたトリフロロ酢酸溶液(沸点72℃)に浸漬
し、次に50℃にて真空乾燥することにより炭素体
に5重量%の鉄フタロシアニン・スルホン酸を付
着せしめた空気極を得た。 実施例 2 実施例1の炭素体を銅フタロシアニンを8重量
%溶解せしめたトリクロル酢酸溶液(沸点197℃)
に浸漬し、次に100℃にて真空乾燥することによ
り炭素体に3重量%の銅フタロシアニンを付着せ
しめた空気極を得た。 比較例 1 実施例1の炭素体を銅フタロシアニンの飽和キ
ノリン溶液に浸漬し、次に150℃にて真空乾燥さ
せることにより炭素体に銅フタロシアニンを付着
せしめた空気極を得た。 比較例 2 比較例1の操作を2回繰り返し空気極とした。 実施例1、2及び比較例1、2で得られた空気
極の分極特性を第1図及び第2図に示す。 以上のように本発明で得られた空気極は、1回
の処理により炭素体に触媒として適量の金属フタ
ロシアニンが含浸せしめられるために分極特性に
優れたものであり、空気電池や燃料電池などの空
気極に適したものであるが、繰り返し処理しても
何等本発明の要旨を変更するものではない。
[Table] Carbon materials used include carbon blacks such as furnace black, channel black, and thermal black, as well as wood, charcoal, coconut shell charcoal, palm kernel charcoal, coal, petroleum residue, synthetic resin, and organic waste. Examples include one type or a mixture of two or more of activated carbon and graphite made using carbon and graphite, and are formed into a certain shape by extrusion molding, injection molding, pressure molding, etc. as necessary. The above-mentioned metal phthalocyanine is dissolved in halogenoacetic acid to obtain a 5-10% metal phthalocyanine solution, this solution is impregnated with a carbon material, and the halogenoacetic acid is removed by a conventional method to obtain the desired air electrode. Hereinafter, it will be explained in more detail according to Examples, and in the Examples, "parts" indicate "parts by weight". Example 1 10 parts of coconut shell activated carbon with a particle size of 0.1 to 1μ, particle size of 0.1 to 1μ
10 parts of 0.5μ graphite and 5 parts of thermoplastic resin (vinyl chloride resin) are mixed and extruded to make a round bar with a diameter of 10 mm.Then, the thermoplastic resin is decomposed by heat treatment at 200°C to form a carbon body. And so. This carbon body is immersed in a trifluoroacetic acid solution (boiling point 72°C) in which 10% by weight of iron phthalocyanine is dissolved, and then vacuum-dried at 50°C to attach 5% by weight of iron phthalocyanine/sulfonic acid to the carbon body. Obtained an air electrode. Example 2 A trichloroacetic acid solution (boiling point 197°C) in which the carbon body of Example 1 was dissolved with 8% by weight of copper phthalocyanine
The carbon body was immersed in water and then vacuum dried at 100°C to obtain an air electrode in which 3% by weight of copper phthalocyanine was adhered to the carbon body. Comparative Example 1 The carbon body of Example 1 was immersed in a saturated quinoline solution of copper phthalocyanine, and then vacuum-dried at 150°C to obtain an air electrode with copper phthalocyanine attached to the carbon body. Comparative Example 2 The operation of Comparative Example 1 was repeated twice to prepare an air electrode. The polarization characteristics of the air electrodes obtained in Examples 1 and 2 and Comparative Examples 1 and 2 are shown in FIGS. 1 and 2. As described above, the air electrode obtained by the present invention has excellent polarization characteristics because the carbon body is impregnated with an appropriate amount of metal phthalocyanine as a catalyst in a single treatment, and is suitable for use in air cells, fuel cells, etc. Although it is suitable for an air electrode, repeated treatment does not change the gist of the present invention in any way.

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

第1図は、実施例1、比較例1で得られた空気
極の分極曲線であり、第2図は実施例2、比較例
2で得られた空気極の分極曲線であり、〜は
順に実施例1、比較例1、実施例2、比較例2で
得られた空気極の分極曲線を示し、縦軸は、電流
密度(mA/cm2)、横軸は電位(V/SCE)を示
すものである。
Fig. 1 shows the polarization curve of the air electrode obtained in Example 1 and Comparative Example 1, and Fig. 2 shows the polarization curve of the air electrode obtained in Example 2 and Comparative Example 2. The polarization curves of the air electrodes obtained in Example 1, Comparative Example 1, Example 2, and Comparative Example 2 are shown, where the vertical axis represents the current density (mA/cm 2 ) and the horizontal axis represents the potential (V/SCE). It shows.

Claims (1)

【特許請求の範囲】 1 金属フタロシアニンをハロゲノ酢酸に溶解
し、炭素体に含浸せしめることを特徴とする空気
極の製造方法。 2 金属フタロシアニンが鉄、ニツケル、コバル
ト、銅を含んでいることを特徴とする特許請求の
範囲第1項記載の空気極の製造方法。 3 ハロゲノ酢酸がモノフロロ酢酸、ジフロロ酢
酸、トリフロロ酢酸、モノクロル酢酸、ジクロル
酢酸、トリクロル酢酸の少なくとも1種であるこ
とを特徴とする特許請求の範囲第1項または第2
項記載の空気極の製造方法。
[Claims] 1. A method for producing an air electrode, which comprises dissolving metal phthalocyanine in halogenoacetic acid and impregnating it into a carbon body. 2. The method for producing an air electrode according to claim 1, wherein the metal phthalocyanine contains iron, nickel, cobalt, and copper. 3. Claim 1 or 2, wherein the halogenoacetic acid is at least one of monofluoroacetic acid, difluoroacetic acid, trifluoroacetic acid, monochloroacetic acid, dichloroacetic acid, and trichloroacetic acid.
2. Method for manufacturing an air electrode as described in Section 1.
JP56191943A 1981-11-30 1981-11-30 Production method of air pole Granted JPS5894765A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56191943A JPS5894765A (en) 1981-11-30 1981-11-30 Production method of air pole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56191943A JPS5894765A (en) 1981-11-30 1981-11-30 Production method of air pole

Publications (2)

Publication Number Publication Date
JPS5894765A JPS5894765A (en) 1983-06-06
JPH0119626B2 true JPH0119626B2 (en) 1989-04-12

Family

ID=16283032

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56191943A Granted JPS5894765A (en) 1981-11-30 1981-11-30 Production method of air pole

Country Status (1)

Country Link
JP (1) JPS5894765A (en)

Also Published As

Publication number Publication date
JPS5894765A (en) 1983-06-06

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