JPH05190184A - Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof - Google Patents

Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof

Info

Publication number
JPH05190184A
JPH05190184A JP4020638A JP2063892A JPH05190184A JP H05190184 A JPH05190184 A JP H05190184A JP 4020638 A JP4020638 A JP 4020638A JP 2063892 A JP2063892 A JP 2063892A JP H05190184 A JPH05190184 A JP H05190184A
Authority
JP
Japan
Prior art keywords
electrode
electrolyte
fuel cell
electrolyte membrane
electrolyte film
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
JP4020638A
Other languages
Japanese (ja)
Inventor
Takafumi Okamoto
隆文 岡本
Ichiro Baba
一郎 馬場
Hideo Kato
英男 加藤
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.)
Honda Motor Co Ltd
Original Assignee
Honda Motor 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 Honda Motor Co Ltd filed Critical Honda Motor Co Ltd
Priority to JP4020638A priority Critical patent/JPH05190184A/en
Publication of JPH05190184A publication Critical patent/JPH05190184A/en
Pending legal-status Critical Current

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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
    • H01M8/10Fuel cells with solid electrolytes
    • H01M8/1004Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
    • 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
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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

Abstract

PURPOSE:To improve the water feeding faculty to an electrolyte film and improve the power generation performnce of a fuel battery by forming the part having an electrode catalytic layer from an electrolyte of a solid electrolyte film consisting of only one layer part of a solid electrolyte film. CONSTITUTION:An electrode catalytic paste is applied on a solid electrolyte film through the screen printing, spraying method, coating method, etc., and an electrode catalytic layer part A on which an electrolyte catalytic layer is formed and a water feeding area B consisting of only one layer of tale solid high polymeric electrolyte film are formed. As the electrode catalytic paste, is used the paste which is formed by dispersing the platinum group metal. powders, carbon black, etc., into the solution of an ion exchange film. Accordingly, the water feeding faculty to the electrolyte film is improved to prevent the drying in the electrolyte film, and the power generation performance can be improved.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、電極−電解質接合体お
よびその製造方法に関し、特に揆水性、粘着性を必要と
するアノード極側でも電解質膜への水分供給能力に優
れ、また燃料電池の発電性能向上を図ることが可能とな
る電極−電解質接合体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-electrolyte assembly and a method for producing the same, and in particular, it has an excellent ability to supply water to the electrolyte membrane even on the side of the anode that requires water repellency and adhesiveness. The present invention relates to an electrode-electrolyte assembly capable of improving power generation performance and a method for manufacturing the same.

【0002】[0002]

【従来の技術】燃料電池は、一般に電解質膜とその両側
に設けられたアノードおよびカソードからなる単位電
池、すなわちセルを、セパレータを介して積層してな
る。
2. Description of the Related Art A fuel cell is generally formed by stacking unit cells, ie, cells, each having an electrolyte membrane and an anode and a cathode provided on both sides thereof, that is, a cell.

【0003】反応ガスは、燃料ガスと酸化剤ガスからな
り、セパレータのアノード側には燃料ガスが供給され、
一方、セパレータのカソード側には酸化剤ガスが供給さ
れる。このような反応ガスの供給の結果、電気化学的反
応の進行にともない電子が発生し、この電子を外部回路
に取り出すことにより、電気エネルギーを発生する。
The reaction gas consists of fuel gas and oxidant gas, and the fuel gas is supplied to the anode side of the separator.
On the other hand, the oxidant gas is supplied to the cathode side of the separator. As a result of such supply of the reaction gas, electrons are generated as the electrochemical reaction progresses, and the electrons are taken out to an external circuit to generate electric energy.

【0004】このような燃料電池として、電解質膜をイ
オン交換膜などの固体高分子電解質膜により形成し、そ
の上に電極触媒層を形成してなるものが考えられる。
As such a fuel cell, it is conceivable that an electrolyte membrane is formed of a solid polymer electrolyte membrane such as an ion exchange membrane, and an electrode catalyst layer is formed thereon.

【0005】このような燃料電池において、電解質膜内
をH+ が移動する際にH+ 1個につきn個のH2 Oの移
動をともなう。この数は、電気浸透係数(β)と定義さ
れる。βが低下すると、電解質膜のイオン導電性が低下
し、電解質膜自体の膜抵抗が増大する。この結果、膜抵
抗による発熱が起こり、電解質膜内の温度上昇によって
電解質膜内の含水量がさらに低下し、βの低下は助長さ
れる。これは、固体高分子電解質膜型燃料電池にとって
高電流密度領域での運転を難しくする原因となる。
[0005] In such a fuel cell, the inside of the electrolyte membrane involving mobile H + 1 piece per of n H 2 O in the H + moves. This number is defined as the electroosmotic coefficient (β). When β decreases, the ionic conductivity of the electrolyte membrane decreases, and the membrane resistance of the electrolyte membrane itself increases. As a result, heat is generated due to the membrane resistance, the temperature rise in the electrolyte membrane further reduces the water content in the electrolyte membrane, and the reduction of β is promoted. This causes the solid polymer electrolyte membrane fuel cell to be difficult to operate in a high current density region.

【0006】また、電極触媒層は、H2 が吸着し、原子
状(H2 )がイオン化(2H+ +2e - )反応を行うた
め、H2 の吸着サイトが確保されていなくてはならな
い。このため、電極触媒層にはある程度の揆水性が要求
される。
Further, in the electrode catalyst layer, since H 2 is adsorbed and atomic (H 2 ) undergoes an ionization (2H + + 2e ) reaction, an adsorption site of H 2 must be secured. Therefore, the electrode catalyst layer is required to have a certain degree of water repellency.

【0007】さらに、電極触媒層を層として電解質膜に
所定の厚さで形状保持させるために粘着性のある材料が
必要となる。
Further, a material having an adhesive property is required to keep the shape of the electrolyte membrane in a predetermined thickness by using the electrode catalyst layer as a layer.

【0008】このように、揆水性と粘着性の双方の特徴
と電解質膜への非反応性の観点より、粘着剤としてポリ
テトラフルオロエチレンなどのフッ素樹脂が有効とされ
ている。
As described above, from the viewpoint of both the water repellent property and the adhesive property and the nonreactivity to the electrolyte membrane, the fluororesin such as polytetrafluoroethylene is effective as the adhesive.

【0009】しかし、固体高分子電解質膜型燃料電池で
は、上述のごとくH2 Oの移動および電解質膜内での含
水率の保持が要求されるため、H2 Oの電解質膜への進
入は不可欠である。
However, in the solid polymer electrolyte membrane fuel cell, since it is required to move H 2 O and maintain the water content in the electrolyte membrane as described above, it is indispensable for H 2 O to enter the electrolyte membrane. Is.

【0010】従来、このような電解質膜の含水率を一定
の範囲内に保持させた固体高分子電解質膜型燃料電池と
しては、アノード側に水を供給しかつ冷却を同時に行う
ことのできる固体高分子電解質膜型燃料電池(特開平1
−309263号公報)、アノード極に密着させるガス
セパレータに対し、水素供給溝の間に水供給溝を付設し
た固体高分子電解質膜型燃料電池(特開平3−1027
74号公報)、また電極部分と加湿部分を同じ電解質板
面に備えた固体高分子電解質膜型燃料電池〔FC Se
minar,330(1988)〕などが開示されてい
る。
Conventionally, as a solid polymer electrolyte membrane fuel cell in which the water content of such an electrolyte membrane is kept within a certain range, a solid high fuel cell capable of supplying water to the anode side and simultaneously cooling it. Molecular electrolyte membrane fuel cell (Patent Document 1
No. 309263), a solid polymer electrolyte membrane fuel cell in which a water supply groove is provided between hydrogen supply grooves with respect to a gas separator to be brought into close contact with an anode electrode (JP-A-3-1027).
No. 74), and a solid polymer electrolyte membrane fuel cell [FC Se having an electrode part and a humidifying part on the same electrolyte plate surface].
minar, 330 (1988)] and the like.

【0011】しかしながら、これらの従来技術に示され
ている燃料電池では、上記のような、揆水性、粘着性と
含水率の維持というこれら相反する要求を電極触媒層で
解決することは困難であり、また電解質層、電極触媒層
双方の特性を使いきるには至らず、例えばFC Sem
inar,330(1988)の固体高分子電解質膜型
燃料電池では、電極部分と加湿部分が同じ電解質板面で
もそれぞれ別々のエリアに属しており、それぞれ機能が
独立しているため、電極部分でも加湿部分からの距離に
よって電解質内の水分含有量が異なる場合もあり、また
構造的にも複雑となるなど、充分に水分供給能力を発揮
できるとはいい難い。
However, in the fuel cells disclosed in these prior arts, it is difficult for the electrode catalyst layer to solve these contradictory requirements of water repellent property, tackiness and maintenance of water content. In addition, the characteristics of both the electrolyte layer and the electrode catalyst layer cannot be used up completely. For example, FC Sem
In the solid polymer electrolyte membrane fuel cell of inar, 330 (1988), the electrode part and the humidifying part belong to different areas even on the same electrolyte plate surface, and since the functions are independent, the electrode part and the humidifying part are also humidified. The water content in the electrolyte may differ depending on the distance from the portion, and the structure becomes complicated, so it is difficult to say that the water supply capacity can be sufficiently exhibited.

【0012】さらに、固体高分子電解質膜型燃料電池作
動条件下で電解質板ではアノード側での水分含有率の低
下が著しく、これは、アノード側に水分供給は必要であ
るとの示唆がなされているともいえる。
Further, under the operating conditions of the solid polymer electrolyte membrane fuel cell, the electrolyte plate shows a remarkable decrease in the water content on the anode side, which suggests that the water supply on the anode side is necessary. It can be said that there is.

【0013】[0013]

【発明が解決しようとする課題】本発明は、以上のよう
な従来の技術を背景になされたものであり、電解質膜へ
の水分供給能力を高め、電解質膜内の含水量低下に伴う
乾燥を防ぎ、また揆水能力の高い電極触媒層を用いた場
合でも電解質膜内に水分を供給することができる電極−
電解質接合体その製造方法、およびそれを用いた燃料電
池を提供することを目的とする。
The present invention has been made against the background of the above-mentioned conventional techniques, and enhances the water supply capacity to the electrolyte membrane, and prevents the drying due to the decrease of the water content in the electrolyte membrane. An electrode that can prevent moisture and can supply water into the electrolyte membrane even when an electrode catalyst layer having a high water drainage capacity is used.
It is an object of the present invention to provide an electrolyte joined body, a method for producing the same, and a fuel cell using the same.

【0014】[0014]

【課題を解決するための手段】本発明は、固体高分子電
解質膜上に電極触媒層が形成された電極−電解質接合体
において、電極触媒層が形成されている部分と、形成さ
れず固体高分子電解質膜一層のみの部分とがある、固体
高分子電解質膜を電解質とする電極−電解質接合体その
製造方法、およびそれを用いた燃料電池を提供するもの
である。
Means for Solving the Problems The present invention relates to an electrode-electrolyte assembly in which an electrode catalyst layer is formed on a solid polymer electrolyte membrane, a portion where the electrode catalyst layer is formed and a solid polymer electrolyte membrane which is not formed. An electrode-electrolyte assembly using a solid polymer electrolyte membrane as an electrolyte, which has a portion having only one molecular electrolyte membrane, and a method for producing the same, and a fuel cell using the same.

【0015】本発明の一実施例による燃料電池は、典型
的には、それぞれ複数枚の電解質膜およびセパレータを
交互に積層した積層体を形成し、両端に燃料ガスの流入
口および流出口、および酸化剤ガスの流入口および流出
口を具備するマニホールドを取り付けてなる構造を有す
る。このような燃料電池のセルは、1枚の電解質板とそ
の両側に配置された電極触媒層からなる。
A fuel cell according to one embodiment of the present invention typically forms a laminate in which a plurality of electrolyte membranes and separators are alternately laminated, and has fuel gas inlets and outlets at both ends, and It has a structure in which a manifold having an inflow port and an outflow port for the oxidant gas is attached. A cell of such a fuel cell is composed of one electrolyte plate and electrode catalyst layers arranged on both sides thereof.

【0016】このような本発明の燃料電池に使用可能な
電極−電解質接合体の層構造を図1に示す。電極−電解
質接合体1は、電解質膜1aと、その両側の電極触媒層
1bとからなる。電解質膜として、固体高分子電解質膜
を用いると効果的であり、その膜厚はおおむね50〜2
00μm程度である。
FIG. 1 shows the layer structure of the electrode-electrolyte assembly which can be used in the fuel cell of the present invention. The electrode-electrolyte assembly 1 comprises an electrolyte membrane 1a and electrode catalyst layers 1b on both sides thereof. It is effective to use a solid polymer electrolyte membrane as the electrolyte membrane, and the thickness thereof is approximately 50 to 2
It is about 00 μm.

【0017】また、電極触媒層1bは、白金族金属の粉
末、カーボンブラックまたは白金族金属をカーボンブラ
ックに担持させたものなどをイオン交換膜の溶液に分散
させたペーストから形成する。上記ペーストは、上述し
たイオン交換膜樹脂の溶液の固形分100重量部当た
り、白金族金属粉末1〜200重量部、カーボンブラッ
ク1〜500重量部およびポリテトラフルオロエチレン
などのフッ素樹脂の溶液(乾燥状態で1〜200重量
部)を混合することにより、製造することができる。な
お、白金族金属のほかに、他の金属との合金を用いるこ
ともできる。
The electrode catalyst layer 1b is formed from a paste prepared by dispersing a platinum group metal powder, carbon black or a platinum group metal supported on carbon black in a solution of an ion exchange membrane. The above-mentioned paste is a solution of a fluororesin such as 1 to 200 parts by weight of platinum group metal powder, 1 to 500 parts by weight of carbon black, and polytetrafluoroethylene per 100 parts by weight of the solid content of the solution of the above-mentioned ion exchange membrane resin (dry). It can be produced by mixing 1 to 200 parts by weight). In addition to the platinum group metal, an alloy with another metal can also be used.

【0018】次に、電解質膜1a上に前述した電極触媒
ペーストをスクリーン印刷、スプレー法、塗布法などに
より図2および図3のように塗布し、電極触媒層が形成
されている電極触媒層部分Aと、形成されず固体高分子
電解質膜一層のみからなる水分供給エリアBとを形成す
る。また、上記スクリーン印刷法によるペーストの塗布
量は、乾燥重量で0.5〜20mg/cm2 程度であ
る。この方法によれば、電極触媒層と水分供給エリアを
共に同じ面上に隣接させることができ、また印刷または
塗布パターンなどは自由自在である。
Next, the above-mentioned electrode catalyst paste is applied onto the electrolyte membrane 1a by screen printing, spraying, coating or the like as shown in FIGS. 2 and 3, thereby forming an electrode catalyst layer. A and a water supply area B which is not formed and consists of only one layer of the solid polymer electrolyte membrane are formed. The amount of paste applied by the screen printing method is about 0.5 to 20 mg / cm 2 in dry weight. According to this method, both the electrode catalyst layer and the water supply area can be adjacent to each other on the same surface, and the printing or coating pattern can be freely selected.

【0019】なお、このようにして得られた電極−電解
質接合体1には、通常、ホットプレスなどの加熱加圧処
理を行う。上記加熱加圧処理の条件は、温度60〜20
0℃程度、圧力50〜300kg/cm2 程度、好まし
くは温度100〜120℃程度、圧力100〜150k
g/cm2 程度である。
The electrode-electrolyte assembly 1 thus obtained is usually subjected to a heat and pressure treatment such as hot pressing. The conditions of the heating and pressurizing treatment are a temperature of 60 to 20.
0 ° C, pressure 50-300kg / cm 2 , preferably temperature 100-120 ° C, pressure 100-150k
It is about g / cm 2 .

【0020】以上、本発明を添付図面を参照した説明し
てきたが、本発明はこれに限定されることなく、種々の
形式の積層型燃料電池に適応が可能である。
Although the present invention has been described above with reference to the accompanying drawings, the present invention is not limited to this and can be applied to various types of stacked fuel cells.

【0021】[0021]

【実施例】本発明を以下の実施例によりさらに詳細に説
明する。 実施例1 白金ブラック2gと、カーボンブラック1gと、ポリテ
トラフルオロエチレン粉末1gとを、ナフィオン(登録
商標)溶液(アルドリッチ社製、5重量%溶液)40m
lと混合し、電極触媒用のペーストを調製した。
The present invention will be described in more detail by the following examples. Example 1 2 g of platinum black, 1 g of carbon black, and 1 g of polytetrafluoroethylene powder were mixed with 40 m of a Nafion (registered trademark) solution (5% by weight solution manufactured by Aldrich).
It mixed with 1 and prepared the paste for electrode catalysts.

【0022】次に、ナフィオン(登録商標)の10cm
×10cmのフィルム(厚さ175μm)をアセトンで
洗浄し、続いて塩酸処理を施したのち、乾燥した。これ
に対しスパッタ装置により50mmφの大きさに、30
分間プラズマエッチング処理した。
Next, 10 cm of Nafion (registered trademark)
A × 10 cm film (thickness: 175 μm) was washed with acetone, subsequently treated with hydrochloric acid, and then dried. On the other hand, with a sputtering device, the size of 50 mmφ
A plasma etching process was performed for a minute.

【0023】このフィルムに対して、上述したペースト
を、切り抜き製版スクリーンにより50mmφの大きさ
にパターン印刷を行った。さらに、加熱プレスにて10
0℃、150kg/cm2 で、一分間ホットプレスを行
い、厚さ約230μmの燃料電池用の電極−電解質接合
体を得た。
The above-mentioned paste was pattern-printed on this film by a cut-out plate making screen to a size of 50 mmφ. Furthermore, it is 10 with a heating press.
Hot pressing was performed at 0 ° C. and 150 kg / cm 2 for 1 minute to obtain an electrode-electrolyte assembly for a fuel cell having a thickness of about 230 μm.

【0024】[0024]

【発明の効果】以上に詳述したとおり、本発明の電極−
電解質接合体は、電解質膜への水分供給能力を高め、電
解質膜内の含水量低下に伴う乾燥を防ぎ、また揆水およ
び粘着能力の高い電極触媒層を用いた場合でも電解質膜
内に水分を供給することができ、またさらには燃料電池
の発電性能向上を図ることが可能となる。
As described above in detail, the electrode of the present invention
The electrolyte assembly enhances the ability to supply water to the electrolyte membrane, prevents drying due to a decrease in the water content in the electrolyte membrane, and even when using an electrode catalyst layer with high water repellent and adhesive ability The fuel cell can be supplied, and further the power generation performance of the fuel cell can be improved.

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

【図1】本発明の燃料電池に用いる電極−電解質接合体
の層構成を示す概略図であ
FIG. 1 is a schematic view showing a layer structure of an electrode-electrolyte assembly used in a fuel cell of the present invention.

【図2】本発明の燃料電池に用いる電極−電解質接合体
の表面概略図である。
FIG. 2 is a schematic surface view of an electrode-electrolyte assembly used in the fuel cell of the present invention.

【図3】本発明の燃料電池に用いる電極−電解質接合体
の電極側の断面概略図である。
FIG. 3 is a schematic cross-sectional view on the electrode side of an electrode-electrolyte assembly used in the fuel cell of the present invention.

【符号の説明】[Explanation of symbols]

1 電極−電解質接合体 1a 電解質膜 1b 電解触媒層 A 電極触媒層部分 B 水分供給エリア 1 Electrode-Electrolyte Assembly 1a Electrolyte Membrane 1b Electrolytic Catalyst Layer A Electrode Catalyst Layer Part B Water Supply Area

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 固体高分子電解質膜上に電極触媒層が形
成された電極−電解質接合体において、電極触媒層が形
成されている部分と、形成されず固体高分子電解質膜一
層のみの部分とがある、固体高分子電解質膜を電解質と
する電極−電解質接合体。
1. In an electrode-electrolyte assembly in which an electrode catalyst layer is formed on a solid polymer electrolyte membrane, a portion where an electrode catalyst layer is formed and a portion where the electrode catalyst layer is not formed and only one solid polymer electrolyte membrane is formed. There is an electrode-electrolyte assembly using a solid polymer electrolyte membrane as an electrolyte.
【請求項2】 ペースト状の電極触媒を塗布することに
より、電極触媒層を形成することを特徴とする請求項1
記載の電極−電解質接合体の製造方法。
2. The electrode catalyst layer is formed by applying a paste electrode catalyst.
A method for producing the described electrode-electrolyte assembly.
【請求項3】 請求項1記載の電極−電解質接合体を用
いてなることを特徴とする燃料電池。
3. A fuel cell comprising the electrode-electrolyte assembly according to claim 1.
JP4020638A 1992-01-10 1992-01-10 Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof Pending JPH05190184A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4020638A JPH05190184A (en) 1992-01-10 1992-01-10 Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4020638A JPH05190184A (en) 1992-01-10 1992-01-10 Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof

Publications (1)

Publication Number Publication Date
JPH05190184A true JPH05190184A (en) 1993-07-30

Family

ID=12032772

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4020638A Pending JPH05190184A (en) 1992-01-10 1992-01-10 Electrode-electrolyte joint body, manufacture thereof, and fuel cell using thereof

Country Status (1)

Country Link
JP (1) JPH05190184A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0654837A1 (en) * 1993-11-23 1995-05-24 Johnson Matthey Public Limited Company Manufacture of electrodes
WO1996024958A1 (en) * 1995-02-10 1996-08-15 Stichting Energieonderzoek Centrum Solid polymer fuel cell comprising humidity-exchanging areas
WO2000014819A1 (en) * 1998-09-04 2000-03-16 Kabushiki Kaisha Toshiba Solid polymer type fuel cell system
JP2006040677A (en) * 2004-07-26 2006-02-09 Daihatsu Motor Co Ltd Membrane electrode assembly and fuel cell
JP2006139922A (en) * 2004-11-10 2006-06-01 Hideichiro Hirai Power generating unit and solid polymer fuel cell
US7141328B2 (en) * 2001-08-31 2006-11-28 Mitsubishi Denki Kabushiki Kaisha Fuel cell
CN113314719A (en) * 2021-04-09 2021-08-27 国联汽车动力电池研究院有限责任公司 Integrated cathode with high catalytic performance, preparation method thereof and battery

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0654837A1 (en) * 1993-11-23 1995-05-24 Johnson Matthey Public Limited Company Manufacture of electrodes
US5702839A (en) * 1993-11-23 1997-12-30 Johnson Matthey Public Limited Company Manufacture of electrodes
US5871860A (en) * 1993-11-23 1999-02-16 Johnson Matthey Public Limited Company Manufacture of electrodes
EP1096586A3 (en) * 1993-11-23 2007-04-11 Johnson Matthey Public Limited Company Manufacture of electrodes
EP1096586A2 (en) * 1993-11-23 2001-05-02 Johnson Matthey Public Limited Company Manufacture of electrodes
WO1996024958A1 (en) * 1995-02-10 1996-08-15 Stichting Energieonderzoek Centrum Solid polymer fuel cell comprising humidity-exchanging areas
US6613467B1 (en) 1998-09-04 2003-09-02 Kabushiki Kaisha Toshiba Polymer electrolyte fuel cells system
WO2000014819A1 (en) * 1998-09-04 2000-03-16 Kabushiki Kaisha Toshiba Solid polymer type fuel cell system
US7141328B2 (en) * 2001-08-31 2006-11-28 Mitsubishi Denki Kabushiki Kaisha Fuel cell
JP4519375B2 (en) * 2001-08-31 2010-08-04 三菱電機株式会社 Fuel cell
JP2006040677A (en) * 2004-07-26 2006-02-09 Daihatsu Motor Co Ltd Membrane electrode assembly and fuel cell
JP2006139922A (en) * 2004-11-10 2006-06-01 Hideichiro Hirai Power generating unit and solid polymer fuel cell
CN113314719A (en) * 2021-04-09 2021-08-27 国联汽车动力电池研究院有限责任公司 Integrated cathode with high catalytic performance, preparation method thereof and battery

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