JPH0629028A - Fuel cell and its manufacture - Google Patents

Fuel cell and its manufacture

Info

Publication number
JPH0629028A
JPH0629028A JP4180154A JP18015492A JPH0629028A JP H0629028 A JPH0629028 A JP H0629028A JP 4180154 A JP4180154 A JP 4180154A JP 18015492 A JP18015492 A JP 18015492A JP H0629028 A JPH0629028 A JP H0629028A
Authority
JP
Japan
Prior art keywords
catalyst
fuel cell
platinum
electrode
chromium
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
JP4180154A
Other languages
Japanese (ja)
Inventor
Hirobumi Enomoto
博文 榎本
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP4180154A priority Critical patent/JPH0629028A/en
Publication of JPH0629028A publication Critical patent/JPH0629028A/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

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  • Inert Electrodes (AREA)

Abstract

PURPOSE:To provide a fuel cell excellent in the initial characteristics and secular stability by structuring a catalyst so that a ternary alloy of platinum, iron, and chromium is borne by a carrier consisting of carbon, and fastening the catalyst onto an electrode base material using a binder. CONSTITUTION:A catalyst 3 is structured so that a ternary alloy 2A consisting of 8-24% iron, 8-24% chromium, and platinum for remainder is borne by a carrier of carbon. An electrode catalyst layer 5 is formed by laying this catalyst 3 on an electrode base material 1 using a binder. This ternary alloy catalyst has a small dia. of crystallite and presents lesser secular change. This achieves a fuel cell excellent in the initial characteristics and secular stability.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は燃料電池の電極触媒層
に係り、特にその触媒物質およびその製造方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrode catalyst layer of a fuel cell, and more particularly to a catalyst material and a method for producing the same.

【0002】[0002]

【従来の技術】一般に燃料電池用ガス拡散電極は電気伝
導性に優れた多孔質なカーボン電極基材上に、貴金属を
担持した触媒粉末をポリテトラフロロエチレンで結着し
た電極触媒層を積層して形成される。
2. Description of the Related Art In general, a gas diffusion electrode for a fuel cell has a porous carbon electrode substrate having excellent electric conductivity, and an electrode catalyst layer obtained by binding a catalyst powder carrying a noble metal with polytetrafluoroethylene. Formed.

【0003】この電極触媒層において供給される反応ガ
スである酸素または水素と、リン酸電解質および触媒の
三相共存が均一に起こることで電気化学的反応を直接電
気エネルギーとして取り出すことができる。
The three-phase coexistence of oxygen or hydrogen, which is the reaction gas supplied in the electrode catalyst layer, with the phosphoric acid electrolyte and the catalyst uniformly occurs, so that the electrochemical reaction can be directly taken out as electric energy.

【0004】図1は燃料電池の電極構造を示す模式的断
面図である。燃料電池は空気または水素の流通路を有し
た多孔質カーボンを用いた電極基材1と、白金触媒2を
担持した触媒3に適度なはっ水性を付与するPTFE4を混
合した電極触媒層5よりなっている。この電極触媒層に
おいて、供給される反応ガスである空気および水素と電
解質であるリン酸が触媒粒子表面で三相共存状態を起こ
すことで電気化学的反応が生じて直接電気エネルギーを
取り出すことができる。
FIG. 1 is a schematic sectional view showing an electrode structure of a fuel cell. The fuel cell has an electrode catalyst layer 5 in which an electrode base material 1 made of porous carbon having a flow passage for air or hydrogen and a catalyst 3 carrying a platinum catalyst 2 and PTFE 4 for imparting appropriate water repellency are mixed. Has become. In this electrode catalyst layer, the supplied reaction gases, air and hydrogen, and the electrolyte, phosphoric acid, cause a three-phase coexistence state on the surface of the catalyst particles, whereby an electrochemical reaction occurs and electrical energy can be directly extracted. .

【0005】従来よりリン酸型燃料電池用触媒としては
高温リン酸に対して耐食性のある白金を用いた触媒が使
用されている。触媒は電極反応に極めて重要な役割を果
たしており、電池の出力と寿命の向上のために触媒の活
性度と安定性を高めることが必要である。
Conventionally, as a phosphoric acid fuel cell catalyst, a catalyst using platinum, which has corrosion resistance to high-temperature phosphoric acid, has been used. The catalyst plays an extremely important role in the electrode reaction, and it is necessary to enhance the activity and stability of the catalyst in order to improve the output and life of the battery.

【0006】従来の白金触媒の製造方法は、一般に液相
還元法が用いられている。具体的に説明すると白金を担
持するカーボンブラックを液相中に分散し易くするため
に、硝酸や氷酢酸等の酸処理を行い、次に塩化白金酸水
溶液を担持するに必要な白金を加え、液温を40〜90℃に
してから還元剤としてヒドラジンやギ酸を滴下して白金
の還元を行う。
As a conventional method for producing a platinum catalyst, a liquid phase reduction method is generally used. Specifically, in order to facilitate dispersion of carbon black supporting platinum in the liquid phase, acid treatment such as nitric acid or glacial acetic acid is performed, and then platinum necessary for supporting an aqueous chloroplatinic acid solution is added, After adjusting the liquid temperature to 40-90 ℃, hydrazine and formic acid are added dropwise as a reducing agent to reduce platinum.

【0007】さらに触媒の活性度を高めるため白金を担
持した触媒にバナジウム、クロム、コバルト、ニッケ
ル、鉄などの第二金属成分を加えて合金化を行う。まず
前述の白金を還元した触媒を再び水溶液中に分散し、第
二金属の硝酸塩を添加し水酸化カリウム、水酸化ナトリ
ウム、アンモニア水などのアルカリ剤により第二金属を
水酸化物としてカーボン表面に沈着させる。これをろ過
水洗, 乾燥後に不活性雰囲気中で800 〜1000℃の熱処理
をして合金触媒を作製していた。このように白金触媒に
他のIV〜VIII族の遷移金属を添加した合金触媒は触媒活
性の向上が図れることは周知の技術であり、さらに活性
の向上と安定性を求めて白金─クロム─コバルト(特開
昭59─141169号公報) 、白金─鉄─コバルト( 特開昭62
─163746号公報) 、白金─ニッケル─コバルト( 特開昭
63─190254号公報) 等の三元系触媒も紹介されている。
Further, in order to increase the activity of the catalyst, alloying is carried out by adding a second metal component such as vanadium, chromium, cobalt, nickel or iron to the catalyst carrying platinum. First, the platinum-reduced catalyst is dispersed again in an aqueous solution, the nitrate of the second metal is added, and the second metal is converted to hydroxide on the carbon surface with an alkaline agent such as potassium hydroxide, sodium hydroxide, or ammonia water. Deposit. This was filtered, washed with water, dried, and then heat-treated at 800 to 1000 ° C in an inert atmosphere to prepare an alloy catalyst. It is a well-known technique that an alloy catalyst obtained by adding another IV-VIII group transition metal to a platinum catalyst can improve the catalytic activity, and platinum-chromium-cobalt is further sought in order to improve the activity and stability. (JP-A-59-141169), platinum-iron-cobalt (JP-A-62-141169)
─163746), platinum-nickel-cobalt (JP
63-190254) and other three-way catalysts are also introduced.

【0008】[0008]

【発明が解決しようとする課題】しかしながら、これら
の触媒は、初期活性に優れるものの比較的短時間で特性
低下を示すため安定性の向上を図る必要が残されてい
る。この発明は上述の点に鑑みてなされその目的は、新
規な触媒物質とその製法を開発することにより特性と安
定性に優れる燃料電池を提供することにある。
However, although these catalysts are excellent in initial activity, they show deterioration in characteristics in a relatively short time, so that it is necessary to improve stability. The present invention has been made in view of the above points, and an object thereof is to provide a fuel cell having excellent characteristics and stability by developing a novel catalyst substance and a method for producing the same.

【0009】[0009]

【課題を解決するための手段】上述の目的は第一の発明
によれば、電極基材上に電極触媒層を有し、電極触媒層
はカーボン担体上に白金と鉄とクロムの三元合金を担持
した触媒をバインダで結着してなるものであること、又
第二の発明によれば第一工程と、第二工程と、第三工程
とを有し、第一工程は白金の担持されたカーボンに水酸
化クロムと水酸化鉄を沈着させる工程であり、第二工程
は前記水酸化物の沈着したカーボンを温度800ないし
1000℃で熱処理して触媒を調製する工程であり、第
三工程は前記触媒をバインダーで結着して電極触媒層を
調製し次いでこの電極触媒層を電極基材上に積層する工
程であるとすることにより達成される。
According to the first aspect of the present invention, there is provided an electrode catalyst layer on an electrode substrate, and the electrode catalyst layer is a ternary alloy of platinum, iron and chromium on a carbon support. According to the second aspect of the present invention, the catalyst supporting the catalyst is bound with a binder, and has a first step, a second step, and a third step. The first step is platinum loading. The step of depositing chromium hydroxide and iron hydroxide on the formed carbon, the second step is the step of heat-treating the deposited carbon of the hydroxide at a temperature of 800 to 1000 ° C. to prepare a catalyst, The step is achieved by binding the catalyst with a binder to prepare an electrode catalyst layer and then laminating the electrode catalyst layer on an electrode substrate.

【0010】[0010]

【作用】二元系触媒で比較的初期活性が高く、安定性に
優れた鉄とクロムを組み合わせた白金─鉄─クロムの三
元系合金触媒にすることで、触媒活性と安定性の両者を
向上させることができる。
[Function] A platinum-iron-chromium ternary alloy catalyst that combines iron and chromium, which is a binary catalyst with relatively high initial activity and excellent stability, provides both catalytic activity and stability. Can be improved.

【0011】[0011]

【実施例】本発明を実施例に基づき説明する。アセチレ
ンブラック等のカーボンブラックを9g秤取し200ml の純
水に加える。次に白金(pt)として1gの塩化白金酸水溶液
を添加して60℃に昇温する。温度が一定になった後にNa
OH 2N 溶液でpH10に調整して3%ヒドラジン溶液を滴下し
て塩化白金酸の還元を行う。還元終了後にガラスフィル
ターでろ過・洗浄し乾燥することで白金担持触媒が得ら
れる。この白金担持触媒の白金結晶子径は28Åであっ
た。
EXAMPLES The present invention will be described based on examples. Weigh out 9g of carbon black such as acetylene black and add to 200ml of pure water. Next, 1 g of chloroplatinic acid aqueous solution was added as platinum (pt) and the temperature was raised to 60 ° C. Na after the temperature becomes constant
Adjust the pH to 10 with OH 2 N solution and add 3% hydrazine solution dropwise to reduce chloroplatinic acid. After completion of the reduction, a platinum-supported catalyst can be obtained by filtering, washing and drying with a glass filter. The platinum crystallite diameter of this platinum-supported catalyst was 28Å.

【0012】このようにして得られた白金担持触媒の合
金化を次に示す。まず白金担持触媒を純水200ml に分散
する。これとは別にクロム(Cr)として0.30g の酢酸クロ
ムと鉄(Fe)として0.30g の硝酸第一鉄を秤取し純水50ml
中に溶解する。さらにこの溶液中に水酸化ナトリウム溶
液を加えてpH8 に調整し、超音波分散器を用いて水酸化
物となった鉄とクロムの均質混合液を作製する。この溶
液を白金担持触媒が分散された溶液中に加えて水酸化ナ
トリウム溶液を滴加してpH11に調整して1 〜3時間十分
に接触させる。そしてガラスフィルターでろ過・水洗し
乾燥後に窒素気流中で800 〜1000℃で熱処理を行う。こ
のようにして三元合金2Aを担持した触媒が得られる。
The alloying of the platinum-supported catalyst thus obtained is shown below. First, the platinum-supported catalyst is dispersed in 200 ml of pure water. Separately, 0.30 g of chromium acetate as chromium (Cr) and 0.30 g of ferrous nitrate as iron (Fe) were weighed out and purified to 50 ml of pure water.
Dissolves in. Furthermore, a sodium hydroxide solution is added to this solution to adjust the pH to 8, and an ultrasonic disperser is used to prepare a homogeneous mixed solution of iron and chromium that has become hydroxide. This solution is added to the solution in which the platinum-supported catalyst is dispersed, a sodium hydroxide solution is added dropwise to adjust the pH to 11, and the mixture is sufficiently contacted for 1 to 3 hours. Then, it is filtered with a glass filter, washed with water, dried, and then heat-treated at 800-1000 ° C in a nitrogen stream. Thus, the catalyst supporting the ternary alloy 2A is obtained.

【0013】この方法により作製した合金化触媒の結晶
子径は33Åであった。得られた白金─鉄─クロム三元系
合金触媒は従来の合金触媒に比較して初期活性と安定の
両者にすぐれた特性を得ることができた。表1 に初期特
性と500 h 後の結晶子径の変化を示す。
The crystallite diameter of the alloying catalyst produced by this method was 33Å. The obtained platinum-iron-chromium ternary alloy catalyst had excellent initial activity and stability compared with the conventional alloy catalyst. Table 1 shows the initial characteristics and the change in crystallite size after 500 h.

【0014】[0014]

【表1】 [Table 1]

【0015】[0015]

【発明の効果】第一の発明によれば、電極基材上に電極
触媒層を有し、電極触媒層はカーボン担体上に白金と鉄
とクロムの三元合金を担持した触媒をバインダで結着し
てなるものであること、また第二の発明によれば第一工
程と、第二工程と、第三工程とを有し、第一工程は白金
の担持されたカーボンに水酸化クロムと水酸化鉄を沈着
させる工程であり、第二工程は前記水酸化物の沈着した
カーボンを温度800ないし1000℃で熱処理して触
媒を調製する工程であり、第三工程は前記触媒をバイン
ダーで結着して電極触媒層を調製し次いでこの電極触媒
層を電極基材上に積層する工程であるので、結晶子径が
小さい上にその経時変化の少ない三元系合金触媒が得ら
れ、その結果特性と安定性に優れる燃料電池が得られ
る。
According to the first aspect of the present invention, the electrode catalyst layer is provided on the electrode base material, and the electrode catalyst layer is formed by binding the catalyst in which the ternary alloy of platinum, iron and chromium is supported on the carbon support with the binder. According to the second aspect of the present invention, it has a first step, a second step, and a third step, the first step is a platinum-supported carbon and chromium hydroxide. The second step is the step of depositing iron hydroxide, the second step is a step of heat-treating the hydroxide-deposited carbon at a temperature of 800 to 1000 ° C. to prepare a catalyst, and the third step is the step of binding the catalyst with a binder. It is a step of depositing an electrode catalyst layer and then laminating this electrode catalyst layer on an electrode base material, so that a ternary alloy catalyst having a small crystallite diameter and little change over time is obtained. A fuel cell having excellent characteristics and stability can be obtained.

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

【図1】燃料電池の電極構造を示す模式的断面図FIG. 1 is a schematic sectional view showing an electrode structure of a fuel cell.

【符号の説明】[Explanation of symbols]

1 電極基材 2 白金 2A 三元合金 3 触媒 4 PTFE 5 電極触媒層 1 electrode base material 2 platinum 2A ternary alloy 3 catalyst 4 PTFE 5 electrode catalyst layer

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 電極基材上に電極触媒層を有し、 電極触媒層はカーボン担体上に白金と鉄とクロムの三元
合金を担持した触媒をバインダで結着してなるものであ
ることを特徴とする燃料電池。
1. An electrode catalyst layer is provided on an electrode base material, and the electrode catalyst layer is formed by binding a catalyst supporting a ternary alloy of platinum, iron and chromium on a carbon support with a binder. Is a fuel cell.
【請求項2】請求項1記載の燃料電池において、三元合
金の組成は鉄が8ないし24%、クロムが8ないし24
%、残余が白金であることを特徴とする燃料電池。
2. The fuel cell according to claim 1, wherein the composition of the ternary alloy is 8 to 24% iron and 8 to 24 chromium.
%, The balance is platinum, the fuel cell.
【請求項3】 第一工程と、第二工程と、第三工程とを
有し、 第一工程は白金の担持されたカーボンに水酸化クロムと
水酸化鉄を沈着させる工程であり、 第二工程は前記水酸化物の沈着したカーボンを温度80
0ないし1000℃で熱処理して触媒を調製する工程で
あり、 第三工程は前記触媒をバインダーで結着して電極触媒層
を調製し次いでこの電極触媒層を電極基材上に積層する
工程であることを特徴とする燃料電池の製造方法。
3. A first step, a second step, and a third step, wherein the first step is a step of depositing chromium hydroxide and iron hydroxide on carbon carrying platinum. In the process, the carbon deposited with the hydroxide is heated to a temperature of 80.
A step of preparing a catalyst by heat treatment at 0 to 1000 ° C., and a third step is a step of binding the catalyst with a binder to prepare an electrode catalyst layer, and then laminating the electrode catalyst layer on an electrode substrate. A method for manufacturing a fuel cell, characterized in that
【請求項4】請求項3記載の製造方法において、水酸化
物の沈着は、酢酸クロムと硝酸鉄の混合溶液に水酸化ナ
トリウム溶液を加えてpHを8とした懸濁液を超音波分
散して均質混合液を調製し、この均質混合液を白金の担
持されたカーボンと接触させ、さらにpHを11にする
ものであることを特徴とする燃料電池の製造方法。
4. The method according to claim 3, wherein the hydroxide is deposited by ultrasonically dispersing a suspension having a pH of 8 by adding a sodium hydroxide solution to a mixed solution of chromium acetate and iron nitrate. A method for producing a fuel cell, comprising preparing a homogeneous mixed solution by contacting the homogeneous mixed solution with carbon carrying platinum, and further adjusting the pH to 11.
【請求項5】請求項3記載の製造方法において、熱処理
は窒素気流中で行うものであることを特徴とする燃料電
池の製造方法。
5. The method for producing a fuel cell according to claim 3, wherein the heat treatment is performed in a nitrogen stream.
JP4180154A 1992-07-08 1992-07-08 Fuel cell and its manufacture Pending JPH0629028A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4180154A JPH0629028A (en) 1992-07-08 1992-07-08 Fuel cell and its manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4180154A JPH0629028A (en) 1992-07-08 1992-07-08 Fuel cell and its manufacture

Publications (1)

Publication Number Publication Date
JPH0629028A true JPH0629028A (en) 1994-02-04

Family

ID=16078344

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4180154A Pending JPH0629028A (en) 1992-07-08 1992-07-08 Fuel cell and its manufacture

Country Status (1)

Country Link
JP (1) JPH0629028A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6921604B2 (en) 2000-02-02 2005-07-26 Toyota Jidosha Kabushiki Kaisha Device and method for evaluating performance of fuel cells, device and method for evaluating specific surface area of fuel-cell electrode catalysts, fuel-cell electrode catalyst, and method of manufacturing the same
WO2005081340A1 (en) * 2004-02-23 2005-09-01 Cataler Corporation Supported catalyst for fuel cell, method for producing same and fuel cell
JP2005317546A (en) * 2004-04-27 2005-11-10 Samsung Sdi Co Ltd Membrane-electrode assembly for fuel cell and fuel cell system including the same

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6921604B2 (en) 2000-02-02 2005-07-26 Toyota Jidosha Kabushiki Kaisha Device and method for evaluating performance of fuel cells, device and method for evaluating specific surface area of fuel-cell electrode catalysts, fuel-cell electrode catalyst, and method of manufacturing the same
WO2005081340A1 (en) * 2004-02-23 2005-09-01 Cataler Corporation Supported catalyst for fuel cell, method for producing same and fuel cell
US7223493B2 (en) 2004-02-23 2007-05-29 Cataler Corporation Supported catalyst for fuel cell, method of manufacturing the same, and fuel cell
JP2005317546A (en) * 2004-04-27 2005-11-10 Samsung Sdi Co Ltd Membrane-electrode assembly for fuel cell and fuel cell system including the same
US7629072B2 (en) 2004-04-27 2009-12-08 Samsung Sdi Co., Ltd. Membrane-electrode assembly for fuel cell and fuel cell system comprising the same

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