JPH061700B2 - Composite electrode for fuel cell - Google Patents

Composite electrode for fuel cell

Info

Publication number
JPH061700B2
JPH061700B2 JP62280601A JP28060187A JPH061700B2 JP H061700 B2 JPH061700 B2 JP H061700B2 JP 62280601 A JP62280601 A JP 62280601A JP 28060187 A JP28060187 A JP 28060187A JP H061700 B2 JPH061700 B2 JP H061700B2
Authority
JP
Japan
Prior art keywords
electrode
catalyst layer
cathode
anode
fuel cell
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
JP62280601A
Other languages
Japanese (ja)
Other versions
JPH01122565A (en
Inventor
秀幸 野元
正博 桜井
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 JP62280601A priority Critical patent/JPH061700B2/en
Publication of JPH01122565A publication Critical patent/JPH01122565A/en
Publication of JPH061700B2 publication Critical patent/JPH061700B2/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
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/08Fuel cells with aqueous electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • 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
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0297Arrangements for joining electrodes, reservoir layers, heat exchange units or bipolar separators to each other
    • 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

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は燃料電池用複合電極の構成に係り、特に複合
電極電極触媒層の撥水剤の構成に関する。
TECHNICAL FIELD The present invention relates to the structure of a composite electrode for a fuel cell, and more particularly to the structure of a water repellent agent for a composite electrode electrode catalyst layer.

〔従来の技術〕[Conventional technology]

燃料電池は燃料の持つ化学エネルギを直接電気のエネル
ギに変換するものであり、その構成は第3図に示すよう
なアノード9Aとカソード9Bとをリン酸を含むマトリック
ス8をはさんえ配置したものをセパレート板10を介して
積層し、外部のガス供給系より前記各電極へ燃料ガスお
よび酸化剤ガスを供給し、各電極の電極触媒層5A,5B上
で燃料ガスおよび酸化剤ガスを電気化学的に反応させ、
その結果として系外に電気エネルギーを取り出すように
なっている。
A fuel cell directly converts the chemical energy of the fuel into electric energy, and its structure is such that an anode 9A and a cathode 9B are arranged with a matrix 8 containing phosphoric acid interposed between them as shown in FIG. Are stacked via a separate plate 10, a fuel gas and an oxidant gas are supplied to each electrode from an external gas supply system, and the fuel gas and the oxidant gas are electrochemically supplied on the electrode catalyst layers 5A and 5B of each electrode. Reaction,
As a result, electric energy is taken out of the system.

アノード9A,カソード9Bの各電極は第4図に示すように
リブ付電極基材4の上に電極触媒層5を被着させて構成
される。電極触媒層5は触媒担体2の表面に貴金属微粒
子1を担持させた触媒微粒子7がフッ素樹脂の微粒子3
により結着されて構成される。この電極触媒層5の内部
ではリブ付電極基材4側からのガスとマトリックス8側
からの電解液とが接触し、三相界面が形成され電気化学
的反応が進行する。
Each of the electrodes of the anode 9A and the cathode 9B is constituted by depositing an electrode catalyst layer 5 on a ribbed electrode substrate 4 as shown in FIG. In the electrode catalyst layer 5, the catalyst fine particles 7 in which the precious metal fine particles 1 are carried on the surface of the catalyst carrier 2 are the fine particles 3 of the fluororesin.
It is configured by being bound by. Inside the electrode catalyst layer 5, the gas from the ribbed electrode base material 4 side and the electrolytic solution from the matrix 8 side come into contact with each other to form a three-phase interface and an electrochemical reaction proceeds.

この電気化学的反応を効率良く安定して行わせるために
は電極触媒層内の触媒微粒子7と電解液のガスの接する
三相界面を多くするとともに供給ガス,生成ガスの拡散
を良くすることが必要である。例えば燃料ガス供給側で
あるアノードの電極反応は、 H→2H+2e………………… (1) であり、酸化剤ガス供給側であるカソードの電極反応
は、 1/2O+2H+2e→HO……… (2) である。上記の反応が示すようにカソード電極内部は電
極反応で水蒸気が発生するのであるが、この水蒸気の拡
散能わアノード反応で必要とされる水素の拡散能に比べ
小さいため、電極内の電解質量はアノードに比しカソー
ドの方を相対的に少なくし水蒸気の拡散量の高めること
が必要となる。
In order to efficiently and stably carry out this electrochemical reaction, it is necessary to increase the number of three-phase interfaces between the catalyst fine particles 7 in the electrode catalyst layer and the gas of the electrolytic solution and to improve the diffusion of the supply gas and the generated gas. is necessary. For example, the electrode reaction of the anode on the fuel gas supply side is H 2 → 2H + + 2e (1), and the electrode reaction of the cathode on the oxidant gas supply side is 1 / 2O 2 + 2H. ++ 2e → H 2 O ……… (2). As shown by the above reaction, water vapor is generated in the cathode electrode by the electrode reaction, but since the diffusivity of this water vapor is smaller than the hydrogen diffusivity required for the anode reaction, the electrolytic mass in the electrode is It is necessary to make the cathode relatively smaller than the anode to increase the diffusion amount of water vapor.

そのために従来は撥水剤としてのフッ素樹脂を含む各電
極の焼成温度を変化させて電極触媒層の撥水性を変化さ
せ、これによってアノードとカソードの電解質量を調整
していた。
Therefore, conventionally, the calcination temperature of each electrode containing a fluororesin as a water repellent was changed to change the water repellency of the electrode catalyst layer, thereby adjusting the electrolytic mass of the anode and the cathode.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

ところが最近燃料電池のアノード9Aとカソード9Bを別々
に形成するのではなく、アノードとカソードを一体に形
成する複合電極が提案されるに至った。この複合電極は
第5図に示すようにアノード9Aとカソード9Bとがセパレ
ート板10を介して接合された構成を有するものである。
このような複合電極はリブ付電極基材をセパレート板10
を介して接合して複合電極基板としたのち各電極側の電
極触媒層5A,5Bを同時に被着させて形成される。複合電
極はセパレート板10とアノード9Aやカソード9Bとの間の
電気抵抗や熱抵抗を減少させ、電極の取扱いを容易にす
る効果がある。しかしながらこのような複合電極におい
ては電極触媒層5が同一温度で焼成されるため、焼成温
度を変化させて各電極の撥水性を調整することができな
いという問題を生ずる。
However, recently, instead of forming the anode 9A and the cathode 9B of the fuel cell separately, a composite electrode in which the anode and the cathode are integrally formed has been proposed. As shown in FIG. 5, this composite electrode has a structure in which an anode 9A and a cathode 9B are joined via a separate plate 10.
Such a composite electrode includes a ribbed electrode substrate and a separate plate 10.
The electrode catalyst layers 5A and 5B on the respective electrodes are simultaneously adhered to each other to form the composite electrode substrate after being bonded via. The composite electrode has the effect of reducing the electrical resistance and thermal resistance between the separate plate 10 and the anode 9A or the cathode 9B and facilitating the handling of the electrode. However, in such a composite electrode, since the electrode catalyst layer 5 is fired at the same temperature, there is a problem that the water repellency of each electrode cannot be adjusted by changing the firing temperature.

この発明は上記の点に鑑みてなされ、その目的は同一温
度で焼成してもアノードとカソードの撥水性を異ならし
めることの可能の複合電極を提供することにある。
The present invention has been made in view of the above points, and an object thereof is to provide a composite electrode capable of making the anode and the cathode have different water repellency even if they are fired at the same temperature.

〔問題点を解決するための手段〕[Means for solving problems]

上述の目的はこの発明によればリブ付電極基材をセパレ
ート板を介して接合した複合電極基板の両面に撥水剤を
含む電極触媒層を加熱圧着してアノードとカソードの各
電極を一体に形成してなる燃料電池用複合電極におい
て、アノード側の電極触媒中5A中に含まれる撥水剤3の
含有量がカソード側の電極触媒層5B中に含まれる撥水剤
3の含有量よりも少ない電極触媒層を備えることにより
達成される。撥水剤としてはフッ素樹脂のディスパージ
ョン等が用いられる。アノード側の電極触媒層中の撥水
剤の量はカソード側の電極触媒層中の撥水剤の量30〜80
%になるよう調整される。
According to the invention described above, the electrode catalyst layer containing the water repellent agent is thermocompression bonded to both surfaces of the composite electrode substrate in which the ribbed electrode base material is bonded via the separate plate to integrally integrate the anode and cathode electrodes. In the formed composite electrode for a fuel cell, the content of the water repellent 3 contained in the anode side electrode catalyst 5A is higher than the content of the water repellent 3 contained in the cathode side electrode catalyst layer 5B. This is achieved by providing less electrode catalyst layer. A fluororesin dispersion or the like is used as the water repellent. The amount of the water repellent agent in the anode side electrode catalyst layer is 30 to 80 in the cathode side electrode catalyst layer.
% To be adjusted.

〔作用〕 フッ素樹脂は撥水性がる。アノード側の電極触媒層中の
フッ素樹脂の量はカソード側の電極触媒層中のフッ素樹
脂の量よりも少ないため、同一温度で焼成してもアノー
ド電極触媒層の撥水性がカソードの撥水性よりも小さく
なる。
[Function] The fluororesin has water repellency. Since the amount of fluororesin in the electrode catalyst layer on the anode side is smaller than the amount of fluororesin in the electrode catalyst layer on the cathode side, the water repellency of the anode electrode catalyst layer is better than that of the cathode even if it is fired at the same temperature. Also becomes smaller.

〔実施例〕〔Example〕

白金の微粒子1を担持させたカーボン触媒担体2に界面
活性剤を含む水を加え、超音波によりよく触媒担体を分
散させてからフッ素樹脂デイスパージョンをフッ素樹脂
して40〜60重量%添加してよく混合し触媒担体とフッ素
樹脂の分散液を調製する。この分散液に水溶液有機溶剤
を加え混合して、フッ素樹脂と触媒担体とをともに凝集
させ固液分離を行う。得られた固形分をよく混練し電極
用ペーストが調製される。このペーストをカレンダロー
ルにより圧延し、シート化してから乾燥し、カソード側
の電極触媒層に用いる電極膜が調製される。アノード側
の電極触媒層に用いる電極膜は上記と同様であるがただ
フッ素樹脂量がカソードの電極膜の場合の3〜8割量と
なるように調整される。両電極膜はセパレート板を中心
として両側に多孔質のリブ付電極基材を有する一体型の
複合電極基板の両面へ320〜380℃のフッ素樹脂溶融温度
で同時結着される。得られた複合電極を用い燃料電池を
構成し、電池を電流電圧特性、耐久性能を試験した。
Water containing a surfactant is added to the carbon catalyst carrier 2 supporting the platinum fine particles 1 to disperse the catalyst carrier well by ultrasonic waves, and 40 to 60% by weight of fluororesin dispersion is added as a fluororesin. Well mixed to prepare a dispersion liquid of the catalyst carrier and the fluororesin. An aqueous solution organic solvent is added to and mixed with this dispersion liquid to coagulate the fluororesin and the catalyst carrier together for solid-liquid separation. The obtained solid content is thoroughly kneaded to prepare an electrode paste. This paste is rolled by a calender roll, formed into a sheet, and then dried to prepare an electrode film used for the cathode side electrode catalyst layer. The electrode film used for the electrode catalyst layer on the anode side is the same as that described above, but the amount of fluororesin is adjusted to 30 to 80% of that of the cathode electrode film. Both electrode films are simultaneously bound to both surfaces of a monolithic composite electrode substrate having a porous ribbed electrode base material on both sides of a separate plate at a fluororesin melting temperature of 320 to 380 ° C. A fuel cell was constructed using the obtained composite electrode, and the cell was tested for current-voltage characteristics and durability.

〔比較例〕[Comparative example]

複合電極基板の両面にカソード側の電極触媒層に用いる
電極膜を被着させて複合電極とし、この複合電極を用い
た燃料電池を特性を測定した。
The electrode film used for the electrode catalyst layer on the cathode side was adhered to both surfaces of the composite electrode substrate to form a composite electrode, and the characteristics of the fuel cell using this composite electrode were measured.

第1図は燃料電池の電流電圧特性、第2図は電流密度20
0mA/cm2における時間と電圧の関係の耐久性を示す。第
1図、第2図で21A,21Bは複合電極方式をとらない従来
方式のアノードとカソードを別々に形成する場合、22
A,22Bは比較例による場合、23A,23Bは本発明の実施例
に係る場合である。本実施例による場合の特性が良好で
ある。
Fig. 1 shows the current-voltage characteristics of the fuel cell, and Fig. 2 shows the current density.
The durability of the relationship between time and voltage at 0 mA / cm 2 is shown. In FIG. 1 and FIG. 2, 21A and 21B are 22 when the anode and the cathode of the conventional method which does not adopt the composite electrode method are separately formed.
A and 22B are cases according to the comparative example, and 23A and 23B are cases according to the example of the present invention. The characteristics in the case of this example are excellent.

〔発明の効果〕〔The invention's effect〕

この発明によればリブ付電極基材をセパレート板を介し
て接合した複合電極基板の両面に撥水剤を含む電極触媒
層を加熱圧着してアノードとカソードの各電極を一体に
形成してなる燃料電池用複合電極において、アノード側
に電極触媒層中に含まれる撥水剤の含有量がカソード側
電極触媒層中に含まれる撥水剤の含有量よりも少ない電
極触媒層を備えるので、アノード側の電極触媒層の撥水
性がカソード側の電極触媒層の撥水性よりも少なく、ア
ノードにはカソードに比し相対的により多くの電解質が
含まれ、カソードには電解質がより少なく含まれ、その
ために水分子の拡散が良好となり燃料電池の特性、耐久
性が良好となる。
According to the present invention, the anode and cathode electrodes are integrally formed by thermocompression bonding the electrode catalyst layer containing the water repellent agent on both surfaces of the composite electrode substrate in which the ribbed electrode base material is joined via the separate plate. In the composite electrode for a fuel cell, the anode side is provided with the electrode catalyst layer in which the content of the water repellent agent contained in the electrode catalyst layer is smaller than the content of the water repellent agent contained in the cathode side electrode catalyst layer. Side electrode catalyst layer is less water repellent than the cathode side electrode catalyst layer, the anode contains more electrolyte relative to the cathode, and the cathode contains less electrolyte, which is why In addition, the diffusion of water molecules will be good, and the characteristics and durability of the fuel cell will be good.

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

第1図はこの発明の実施例に係る複合電極を使用した燃
料電池の電流電圧特性図、第2図はこの発明の実施例に
係る複合電極を使用した燃料電池の時間電圧特性図、第
3図は従来の燃料電池の構成を示す斜視図、第4図は電
極の構成を示す断面図、第5図は複合電極の構成を示す
斜視図である。 3:撥水剤、5A:アノード側の電極奥倍層、5B:カソー
ド側の電極触媒層。
1 is a current-voltage characteristic diagram of a fuel cell using a composite electrode according to an embodiment of the present invention, and FIG. 2 is a time-voltage characteristic diagram of a fuel cell using a composite electrode according to an embodiment of the present invention. FIG. 4 is a perspective view showing the structure of a conventional fuel cell, FIG. 4 is a sectional view showing the structure of an electrode, and FIG. 5 is a perspective view showing the structure of a composite electrode. 3: Water repellent agent, 5A: Anode-side electrode back layer, 5B: Cathode-side electrode catalyst layer.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】リブ付電極基材をセパレート板を介して接
合した複合電極基板の両面に撥水剤を含む電極触媒層を
加熱圧着してアノードとカソードの両電極を一体に形成
してなる燃料電池用複合電極において、アノード側の電
極触媒層中に含まれる撥水剤の含有量がカソード側の電
極触媒層中に含まれる撥水剤の含有量よりも少ない電極
触媒層を備えることを特徴とする燃料電池用複合電極。
1. An anode and a cathode are integrally formed by thermocompression bonding an electrode catalyst layer containing a water repellent on both surfaces of a composite electrode substrate in which ribbed electrode base materials are joined via a separate plate. The composite electrode for a fuel cell is provided with an electrode catalyst layer in which the content of the water repellent agent contained in the electrode catalyst layer on the anode side is smaller than the content of the water repellent agent contained in the electrode catalyst layer on the cathode side. Characteristic composite electrode for fuel cell.
JP62280601A 1987-11-06 1987-11-06 Composite electrode for fuel cell Expired - Lifetime JPH061700B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62280601A JPH061700B2 (en) 1987-11-06 1987-11-06 Composite electrode for fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62280601A JPH061700B2 (en) 1987-11-06 1987-11-06 Composite electrode for fuel cell

Publications (2)

Publication Number Publication Date
JPH01122565A JPH01122565A (en) 1989-05-15
JPH061700B2 true JPH061700B2 (en) 1994-01-05

Family

ID=17627306

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62280601A Expired - Lifetime JPH061700B2 (en) 1987-11-06 1987-11-06 Composite electrode for fuel cell

Country Status (1)

Country Link
JP (1) JPH061700B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1947717B1 (en) * 2005-11-01 2013-02-13 JSR Corporation Electrode catalyst layer
KR100659132B1 (en) * 2006-02-07 2006-12-19 삼성에스디아이 주식회사 A membrane electrode assembly for fuel cell, a method for preparing the same and a fuel cell comprising the same
JP2009026526A (en) 2007-07-18 2009-02-05 Toyota Motor Corp Fuel cell

Also Published As

Publication number Publication date
JPH01122565A (en) 1989-05-15

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