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JPH0766809B2 - Raw material powder for gas diffusion electrode - Google Patents

Raw material powder for gas diffusion electrode

Info

Publication number
JPH0766809B2
JPH0766809B2 JP61207600A JP20760086A JPH0766809B2 JP H0766809 B2 JPH0766809 B2 JP H0766809B2 JP 61207600 A JP61207600 A JP 61207600A JP 20760086 A JP20760086 A JP 20760086A JP H0766809 B2 JPH0766809 B2 JP H0766809B2
Authority
JP
Japan
Prior art keywords
catalyst
gas diffusion
diffusion electrode
raw material
carbon black
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 - Lifetime
Application number
JP61207600A
Other languages
Japanese (ja)
Other versions
JPS6364266A (en
Inventor
長一 古屋
哲 本尾
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.)
Tanaka Kikinzoku Kogyo KK
Original Assignee
Tanaka Kikinzoku Kogyo KK
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 Tanaka Kikinzoku Kogyo KK filed Critical Tanaka Kikinzoku Kogyo KK
Priority to JP61207600A priority Critical patent/JPH0766809B2/en
Priority to US07/034,499 priority patent/US4816431A/en
Publication of JPS6364266A publication Critical patent/JPS6364266A/en
Priority to US07/283,782 priority patent/US5124018A/en
Publication of JPH0766809B2 publication Critical patent/JPH0766809B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • H01M4/88Processes of manufacture
    • H01M4/8803Supports for the deposition of the catalytic active composition
    • 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
    • H01M4/9075Catalytic material supported on carriers, e.g. powder carriers
    • H01M4/9083Catalytic material supported on carriers, e.g. powder carriers on carbon or graphite
    • 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
    • H01M4/96Carbon-based electrodes
    • 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)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Electrodes For Compound Or Non-Metal Manufacture (AREA)
  • Inert Electrodes (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、燃料電池、二次電池、電気化学的リアクタ
ー、めっき用陽極等に用い、ガス、電解液、触媒の三相
界面での反応を起こさせるガス拡散電極の素材である原
料粉に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention is used in fuel cells, secondary batteries, electrochemical reactors, anodes for plating, etc., and reacts at the three-phase interface of gas, electrolyte, and catalyst. The present invention relates to a raw material powder that is a raw material of a gas diffusion electrode that causes a phenomenon.

(従来の技術) ガス拡散電極を作る素材である原料粉には、従来触媒を
担持した親水性カーボンブラックに、ポリ四弗化エチレ
ン微粉末と撥水性カーボンブラックとを混合したものが
用いられてきた。
(Prior Art) As a raw material powder for forming a gas diffusion electrode, a mixture of hydrophilic carbon black carrying a conventional catalyst, polytetrafluoroethylene fine powder and water repellent carbon black has been used. It was

(発明が解決しようとする問題点) ところで、上記の混合粉で作ったガス拡散電極は、比較
的短い使用期間中に、親水性カーボンブラックに担持さ
れた触媒が遊離して集合凝縮する。その結果、触媒の分
散密度が粗くなり、電解液が浸透したり、ガスが拡散透
過したりしても、集合凝縮した触媒の表面にのみ接触
し、内部の触媒には接触しないので、有効に働く触媒が
少ない。従って、触媒の単位重量当り流せる電流が少な
く、甚だ効率が悪いものである。
(Problems to be Solved by the Invention) By the way, in the gas diffusion electrode made of the above-mentioned mixed powder, the catalyst supported on the hydrophilic carbon black is released and aggregated and condensed during a relatively short period of use. As a result, the dispersion density of the catalyst becomes coarse, and even if the electrolytic solution permeates or the gas diffuses and permeates, it only contacts the surface of the aggregated condensed catalyst, not the internal catalyst, so it is effective. There are few working catalysts. Therefore, the amount of current that can be passed per unit weight of the catalyst is small, and the efficiency is extremely low.

また触媒の遊離、流動による劣下が早く、ガス拡散電極
の寿命が短いものである。
In addition, the deterioration of the catalyst due to the liberation and flow of the catalyst is quick, and the life of the gas diffusion electrode is short.

そこで本発明は、触媒が親水性カーボンブラックから遊
離したりすることの無いガス拡散電極を作る為の原料粉
を提供しようとするものである。
Therefore, the present invention is intended to provide a raw material powder for producing a gas diffusion electrode in which the catalyst is not liberated from the hydrophilic carbon black.

(問題点を解決するための手段) 上記問題点を解決するための本発明のガス拡散電極用原
料粉は、触媒を担持した親水性カーボンブラックに、イ
オン交換樹脂をコーティングして成る微粉末と、ポリ四
弗化エチレン微粉末と、撥水性カーボンブラックとが混
合されて成るものである。
(Means for Solving the Problems) The raw material powder for gas diffusion electrode of the present invention for solving the above problems is a fine powder formed by coating a hydrophilic carbon black carrying a catalyst with an ion exchange resin. , Polytetrafluoroethylene fine powder and water-repellent carbon black are mixed.

(作用) 上記構成の原料粉でガス拡散電極を作ると、親水性カー
ボンブラックに担持された触媒は、イオン交換樹脂がコ
ーティングされている為、長期間使用しても親水性カー
ボンブラックから遊離しない。従って、触媒は集合凝縮
せず、均一微細に分散したままで、触媒の分散密度が細
かく、電解液が浸透したり、ガス拡散透過したりする
と、陽イオンがイオン交換樹脂を透過して殆んどの触媒
に接触して活発に反応が行われる。かくして触媒の単位
重量当り流せる電流が多くなり、著しく効率が向上する
ものである。
(Function) When a gas diffusion electrode is made of the raw material powder having the above-mentioned constitution, the catalyst supported on the hydrophilic carbon black is not separated from the hydrophilic carbon black even if it is used for a long time because the ion exchange resin is coated. . Therefore, the catalyst does not aggregate and condense, but remains dispersed in a uniform and fine manner, and the dispersion density of the catalyst is fine, and when the electrolyte permeates or gas diffuses and permeates, the cations hardly permeate the ion exchange resin. The catalyst is actively contacted with any catalyst. Thus, the amount of current that can be passed per unit weight of the catalyst is increased, and the efficiency is remarkably improved.

(実施例1) 本発明のガス拡散電極用原料粉の一実施例について説明
する。平均粒径30Åの白金微粉末を担持した平均粒径42
0Åの親水性カーボンブラックに、イオン交換樹脂、本
例ではナフィオン(商品名)を厚さ0.05μコーティング
して成る微粉末と、平均粒径0.3μのポリ四弗化エチレ
ン微粉末と、平均粒径420Åの撥水性カーボンブラック
微粉末とを3:4:3の割合で混合して成る。
(Example 1) An example of the raw material powder for a gas diffusion electrode of the present invention will be described. An average particle size of 42 with platinum fine powder having an average particle size of 30Å
0 Å hydrophilic carbon black is coated with ion exchange resin, Nafion (trade name) in this example, with a thickness of 0.05μ, polytetrafluoroethylene fine powder with an average grain size of 0.3μ, and average grain It is made by mixing water-repellent carbon black fine powder with a diameter of 420Å at a ratio of 3: 4: 3.

この実施例1の混合微粉末の原料粉を、ベースプレート
上に0.45mmの厚さに配し、プレスして結着し、厚さ0.1m
mの反応層により成るガス拡散電極を作った。
The raw material powder of the mixed fine powder of Example 1 was placed on a base plate in a thickness of 0.45 mm, pressed and bound to a thickness of 0.1 m.
A gas diffusion electrode consisting of m reaction layers was made.

このように作ったガス拡散電極を、空気極として、電解
液20%硫酸の燃料電池に使用した処、空気極中の親水性
カーボンブラックに担持された白金微粉末は、1000時間
経過しても親水性カーボンブラックからは遊離せず、イ
オン交換樹脂により白金微粉末の集合凝縮が防止され、
白金微粉末は均一微細に分散したままで、白金微粉末の
分散密度が細かかった。従って、浸透した電解液は、陽
イオンがイオン交換樹脂を透過して殆んどの白金微粉末
に接触して活発に反応が行われる結果、白金微粉末の単
位重量当り流せる電流が従来のものより1.5倍程度多く
なり、著しく効率が向上した。
When the gas diffusion electrode thus produced was used as an air electrode in a fuel cell containing 20% sulfuric acid as an electrolyte, the platinum fine powder supported on the hydrophilic carbon black in the air electrode remained for 1000 hours. Not released from the hydrophilic carbon black, the ion-exchange resin prevents the platinum fine powder from condensing and condensing.
The platinum fine powder was dispersed uniformly and finely, and the dispersion density of the platinum fine powder was fine. Therefore, as a result of the cations permeating the ion-exchange resin and contacting most of the platinum fine powder in the infiltrated electrolytic solution, a vigorous reaction is carried out, resulting in a current that can flow per unit weight of the platinum fine powder that is higher than that of the conventional one. It is about 1.5 times more, and the efficiency is remarkably improved.

尚、上記実施例では触媒が白金であるが,これに限るも
のではなく、他の貴金属或いはその合金、卑金属或いは
その合金であっても良いものである。
In the above embodiment, the catalyst is platinum, but the catalyst is not limited to this, and other precious metals or their alloys, base metals or their alloys may be used.

また、上記実施例におけるナフィオンをコーティングし
た親水性カーボンブラックは、液体ナフィオンをアルコ
ールでうすめ、これに親水性カーボンブラックを混ぜた
後、溶媒を蒸発して除去したものである。
Further, the hydrophilic carbon black coated with Nafion in the above examples is obtained by diluting liquid Nafion with alcohol, mixing the hydrophilic carbon black with this, and then removing the solvent by evaporation.

(発明の効果) 以上の説明で判るように本発明のガス拡散電極陽原料粉
によれば、使用中に触媒が親水性カーボンブラックから
遊離せず、従って触媒が集合凝縮することが無く、均一
微細に分散したままで、触媒の単位重量当りの流せる電
流が大きくて、著しく効率の高いガス拡散電極を得るこ
とができる。
(Effects of the Invention) As can be seen from the above description, according to the positive electrode raw material powder of the gas diffusion electrode of the present invention, the catalyst is not released from the hydrophilic carbon black during use, and therefore the catalyst does not aggregate and condense. While finely dispersed, a large amount of current can be passed per unit weight of the catalyst, and a gas diffusion electrode having extremely high efficiency can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】触媒を担持した親水性カーボンブラック
に、イオン交換樹脂をコーティングして成る微粉末と、
ポリ四弗化エチレン微粉末と、触媒無担持の撥水性カー
ボンブラックとが混合されて成るガス拡散電極用原料
粉。
1. A fine powder obtained by coating a hydrophilic carbon black carrying a catalyst with an ion exchange resin,
A raw material powder for a gas diffusion electrode, which is a mixture of polytetrafluoroethylene fine powder and water-repellent carbon black without a catalyst.
JP61207600A 1986-04-03 1986-09-03 Raw material powder for gas diffusion electrode Expired - Lifetime JPH0766809B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP61207600A JPH0766809B2 (en) 1986-09-03 1986-09-03 Raw material powder for gas diffusion electrode
US07/034,499 US4816431A (en) 1986-04-03 1987-04-03 Process for preparing materials for reaction layer of gas permeable electrode
US07/283,782 US5124018A (en) 1986-04-03 1988-12-13 Process for preparing raw materials for reaction layer of gas permeable electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61207600A JPH0766809B2 (en) 1986-09-03 1986-09-03 Raw material powder for gas diffusion electrode

Publications (2)

Publication Number Publication Date
JPS6364266A JPS6364266A (en) 1988-03-22
JPH0766809B2 true JPH0766809B2 (en) 1995-07-19

Family

ID=16542458

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61207600A Expired - Lifetime JPH0766809B2 (en) 1986-04-03 1986-09-03 Raw material powder for gas diffusion electrode

Country Status (1)

Country Link
JP (1) JPH0766809B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9160672B2 (en) 1998-12-08 2015-10-13 Nomadix, Inc. Systems and methods for controlling user perceived connection speed

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3251580B2 (en) * 1990-11-30 2002-01-28 尚正 砂野 Electrode sheet
WO2002073722A1 (en) 2001-03-08 2002-09-19 Sony Corporation Gas diffusive electrode body, method of manufacturing the electrode body, and electrochemical device
JP4501357B2 (en) * 2003-05-08 2010-07-14 ソニー株式会社 Catalyst electrode and method for producing the same, membrane-electrode assembly, and electrochemical device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6167788A (en) * 1984-09-10 1986-04-07 Japan Storage Battery Co Ltd Production of joined body of ion exchange resin film and electrode

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9160672B2 (en) 1998-12-08 2015-10-13 Nomadix, Inc. Systems and methods for controlling user perceived connection speed
US9548935B2 (en) 1998-12-08 2017-01-17 Nomadix, Inc. Systems and methods for providing content and services on a network system

Also Published As

Publication number Publication date
JPS6364266A (en) 1988-03-22

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