JPH01122565A - Composite electrode for fuel cell - Google Patents

Composite electrode for fuel cell

Info

Publication number
JPH01122565A
JPH01122565A JP62280601A JP28060187A JPH01122565A JP H01122565 A JPH01122565 A JP H01122565A JP 62280601 A JP62280601 A JP 62280601A JP 28060187 A JP28060187 A JP 28060187A JP H01122565 A JPH01122565 A JP H01122565A
Authority
JP
Japan
Prior art keywords
electrode
catalyst layer
cathode
anode
composite electrode
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.)
Granted
Application number
JP62280601A
Other languages
Japanese (ja)
Other versions
JPH061700B2 (en
Inventor
Hideyuki Nomoto
野元 秀幸
Masahiro Sakurai
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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Inert Electrodes (AREA)
  • Fuel Cell (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

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。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to the structure of a composite electrode for a fuel cell, and particularly to the structure of a water repellent in 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9八とカソード9Bとをリン酸を含むマトリ
ックス8をはさんで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5
A、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 converts the chemical energy of fuel directly into electrical energy, and its configuration is as shown in Figure 3, in which an anode 98 and a cathode 9B are arranged with a matrix 8 containing phosphoric acid sandwiched between them. The electrode catalyst layers 5 of each electrode are stacked together with a separate plate 10 in between, and fuel gas and oxidant gas are supplied to each electrode from an external gas supply system.
Fuel gas and oxidant gas are electrochemically reacted on A and 5B, and as a result, electrical 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 anodes 9A and cathodes 9B is constructed by depositing an electrode catalyst layer 5 on a ribbed electrode base material 4, as shown in FIG. The electrode catalyst layer 5 is constituted by fine catalyst particles 7 having noble metal fine particles 1 supported on the surface of a catalyst carrier 2 bound by fine particles 3 of fluororesin. Inside this 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, a three-phase interface is formed, and an electrochemical reaction progresses.

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と電解液とガスの接する
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、−= 2 H” + 2 e−−−−−−−−−−
−−−−−−−−−−−−−−−−(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、 1/20z +2 H” +2 e ”Hz O・−−
−−−−−(21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は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
散量を高めることが必要とな・る。
In order to carry out this electrochemical reaction efficiently and stably, it is necessary to increase the number of three-phase interfaces where the catalyst particles 7 in the electrode catalyst layer, the electrolytic solution, and the gas are in contact with each other, and to improve the diffusion of the supplied gas and generated gas. is necessary. For example, the electrode reaction at the anode on the fuel gas supply side is H, -= 2 H" + 2 e
−−−−−−−−−−−−−−−(1), the electrode reaction of the cathode, which is the oxidant gas supply side, is 1/20z +2 H” +2 e”Hz O・−−
--------(21. As shown in the above reaction, water vapor is generated inside the cathode electrode due to the electrode reaction, but the diffusion ability of this water vapor is equal to the hydrogen diffusion ability required in the anode reaction. Since the electrode is relatively small, it is necessary to make the amount of electrolyte within the electrode relatively smaller at the cathode than at the anode to increase the amount of water vapor diffusion.

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。
To this end, conventionally, the firing 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 amounts of electrolyte at the anode and cathode.

〔発明が解決しようとする問題点〕 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プ付電極基材をセパ
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。
[Problems to be Solved by the Invention] Recently, however, a composite electrode has been proposed in which the anode and cathode are integrally formed instead of forming the anode 9A and cathode 9B of a fuel cell separately. This composite electrode has a structure in which an anode 9A and a cathode 9B are joined via a separate plate 10, as shown in FIG. Such a composite electrode is formed by joining electrode base materials with lips through a separate plate 10 to form a composite electrode substrate, and then simultaneously depositing electrode catalyst layers 5A and 5B on each electrode side.

複合電極はセパレート板】0とアノード9八やカソード
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。
The composite electrode has the effect of reducing the electrical resistance and thermal resistance between the separate plate 0 and the anode 98 and cathode 9B, making the electrode easier to handle. However, in such a composite electrode, since the electrode catalyst layer 5 is fired at the same temperature, a problem arises in 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
めることの可能な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 its object is to provide a composite electrode in which the anode and cathode can have different water repellency even when 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プ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層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バー
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の3
0〜80%になるよう調整される。
According to the present invention, the above-mentioned object is to heat and press an electrode catalyst layer containing a water repellent onto both sides of a composite electrode substrate in which electrode base materials with lips are bonded via a separate plate, thereby integrating the anode and cathode electrodes. In the composite electrode for fuel cells formed, the content of the water repellent agent 3 contained in the electrode catalyst layer 5A on the anode side is higher than the content of the water repellent agent 3 contained in the electrode catalyst layer 5B on the cathode side. This is achieved by having fewer electrocatalyst layers. As the water repellent, a fluororesin dispersion or the like is used. The amount of water repellent in the electrode catalyst layer on the anode side is 3 times the amount of water repellent in the electrode catalyst layer on the cathode side.
It is adjusted to be between 0 and 80%.

〔作用〕[Effect]

フッ素樹脂は撥水性がある。アノード側の電極癩媒雇触
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
フン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。
Fluororesin is water repellent. 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 lower than that of the cathode even if fired at the same temperature. water repellency.

〔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ィスバージョンをフン素樹脂
として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。この分散液に水溶性を
機溶剤を加え混合して、フン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プ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、電池の電流電圧特性、耐久性能を
試験した。
Water containing a surfactant is added to the carbon catalyst carrier 2 on which platinum fine particles 1 are supported, and the catalyst carrier is well dispersed by ultrasonic waves, and then 40 to 60% by weight of fluororesin dispersion is added as a fluororesin. Mix well to prepare a dispersion of catalyst carrier and fluororesin. A water-soluble organic solvent is added to this dispersion and mixed to coagulate the fluororesin and the catalyst carrier to perform solid-liquid separation. The obtained solid content is thoroughly kneaded to prepare an electrode paste. This paste is rolled with a calender roll, formed into a sheet, and then dried to prepare an electrode film to be used as an electrode catalyst layer on the cathode side. The electrode film used for the electrode catalyst layer on the anode side is the same as above, except that the amount of fluororesin is 3 to 8 in the case of the cathode electrode film.
The amount will be adjusted accordingly. Both electrode films are simultaneously bonded to both sides of an integrated composite electrode substrate having porous lipped electrode base materials on both sides of the separate plate at a fluororesin melting temperature of 320 to 380°C. A fuel cell was constructed using the obtained composite electrode, and the current-voltage characteristics and durability performance of the cell were tested.

〔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
た燃料電池の特性を測定した。
Electrode films used for the electrode catalyst layer on the cathode side were deposited on both sides of a composite electrode substrate to form a composite electrode, and the characteristics of a 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2
00mA /−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、22A 、 22Bは比較例による場合、23
A、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。
Figure 1 shows the current-voltage characteristics of the fuel cell, Figure 2 shows the current density 2
The durability of the relationship between time and voltage at 00 mA/- is shown. In FIGS. 1 and 2, 21A and 21B are the conventional method in which the anode and cathode are formed separately without using a composite electrode method, 22A and 22B are the comparative example, and 23
A and 23B are cases related to the embodiment of the present invention. The characteristics according to this example are good.

〔発明の効果〕〔Effect of the invention〕

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 this invention, an anode and a cathode electrode are integrally formed by heat-pressing an electrode catalyst layer containing a water repellent agent on both sides of a composite electrode substrate in which a ribbed electrode base material is bonded via a separate plate. The composite electrode for fuel cells includes an electrode catalyst layer in which the content of water repellent contained in the electrode catalyst layer on the anode side is smaller than the content of water repellent contained in the electrode catalyst layer on the cathode side. The water repellency of the electrocatalyst layer on the side is less than the water repellency of the electrocatalyst layer on the cathode side, and the anode contains relatively more electrolyte than the cathode, and the cathode contains less electrolyte, so The diffusion of water molecules becomes better, and the characteristics and durability of the fuel cell are improved.

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

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、5八ニアノード側の電極触媒層、5B:カ
ソード側の電極触媒層。 <<< (△)工専q乎 CD    co    c。 (△)T7専t1.乎
FIG. 1 is a current-voltage characteristic diagram of a fuel cell using a composite electrode according to an embodiment of the present invention, FIG. 2 is a time-voltage characteristic diagram of a fuel cell using a composite electrode according to an embodiment of this invention, and FIG. 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, 58 near-node side electrode catalyst layer, 5B: cathode side electrode catalyst layer. <<< (△)Technical Senq乎CD co c. (△) T7 exclusive t1.乎

Claims (1)

【特許請求の範囲】[Claims] 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) For fuel cells, in which both electrodes, an anode and a cathode, are integrally formed by heat-pressing an electrode catalyst layer containing a water repellent agent on both sides of a composite electrode substrate in which a ribbed electrode base material is bonded via a separate plate. The composite electrode is characterized by comprising 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. Composite electrode for fuel cells.
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 true JPH01122565A (en) 1989-05-15
JPH061700B2 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)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007214102A (en) * 2006-02-07 2007-08-23 Samsung Sdi Co Ltd Membrane electrode assembly, method for producing membrane electrode assembly, and fuel cell
DE112008002184T5 (en) 2007-07-18 2010-08-26 Toyota Jidosha Kabushiki Kaisha, Toyota-shi Fuel cell, which performs an anode dead-end operation
EP1947717A4 (en) * 2005-11-01 2011-01-26 Jsr Corp CATALYTIC LAYER OF ELECTRODE

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1947717A4 (en) * 2005-11-01 2011-01-26 Jsr Corp CATALYTIC LAYER OF ELECTRODE
US8236206B2 (en) 2005-11-01 2012-08-07 Jsr Corporation Electrode catalyst layer
JP2007214102A (en) * 2006-02-07 2007-08-23 Samsung Sdi Co Ltd Membrane electrode assembly, method for producing membrane electrode assembly, and fuel cell
DE112008002184T5 (en) 2007-07-18 2010-08-26 Toyota Jidosha Kabushiki Kaisha, Toyota-shi Fuel cell, which performs an anode dead-end operation

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