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JPH07120532B2 - Method for producing carbonaceous composite electrode substrate for fuel cell - Google Patents
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JPH07120532B2 - Method for producing carbonaceous composite electrode substrate for fuel cell - Google Patents

Method for producing carbonaceous composite electrode substrate for fuel cell

Info

Publication number
JPH07120532B2
JPH07120532B2 JP2296334A JP29633490A JPH07120532B2 JP H07120532 B2 JPH07120532 B2 JP H07120532B2 JP 2296334 A JP2296334 A JP 2296334A JP 29633490 A JP29633490 A JP 29633490A JP H07120532 B2 JPH07120532 B2 JP H07120532B2
Authority
JP
Japan
Prior art keywords
adhesive
carbonaceous
fuel cell
adhesive layer
electrode substrate
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 - Fee Related
Application number
JP2296334A
Other languages
Japanese (ja)
Other versions
JPH04169070A (en
Inventor
義雄 鈴木
敏治 上井
和義 灰野
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.)
Tokai Carbon Co Ltd
Original Assignee
Tokai Carbon 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 Tokai Carbon Co Ltd filed Critical Tokai Carbon Co Ltd
Priority to JP2296334A priority Critical patent/JPH07120532B2/en
Publication of JPH04169070A publication Critical patent/JPH04169070A/en
Publication of JPH07120532B2 publication Critical patent/JPH07120532B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • H01M4/96Carbon-based electrodes
    • 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
    • H01M8/0204Non-porous and characterised by the material
    • H01M8/0213Gas-impermeable carbon-containing materials
    • 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

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)
  • Fuel Cell (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、炭素質材料で構成された多孔質電極板と緻密
質セパレーター板が一体化したリン酸型の燃料電池用炭
素質複合電極基板を製造する方法に関する。
The present invention relates to a phosphoric acid type carbonaceous composite electrode substrate for a fuel cell in which a porous electrode plate composed of a carbonaceous material and a dense separator plate are integrated. To a method of manufacturing.

〔従来の技術〕[Conventional technology]

炭素質材料を部材としたリン酸型燃料電池の製作に当た
っては、機械的強度の向上、セル内部における電気的・
熱的抵抗の低減、積層組立の簡素化などを図るため、セ
パレーター板と多孔質電極板の両部材を予め複合一体化
した構造のものが開発され、実用化の段階にある。
When manufacturing a phosphoric acid fuel cell using carbonaceous material as a member, the mechanical strength was improved and the electrical
In order to reduce the thermal resistance and simplify the laminated assembly, a structure in which both members of the separator plate and the porous electrode plate are combined and integrated in advance has been developed and is in the stage of practical application.

このような複合電極基板を製造するための簡易で実用性
の高い手段に、電極板、セパレータ板およびサイドシー
ル板を所定の形態に接着剤で接合したのち焼成する接合
焼成法(特開昭60−20471号公報、実開昭60−15759号公
報)がある。
As a simple and highly practical means for producing such a composite electrode substrate, a bonding and firing method is used in which an electrode plate, a separator plate, and a side seal plate are bonded to each other in a predetermined form with an adhesive and then baked (Japanese Patent Laid-Open No. Sho 60). -20471 and Jitsukai Sho 60-15759).

ところが、前記の接合焼成法による場合には接着材が多
孔質電極の組織内部に浸透する現象が生じ、電極部材の
気孔率を低下させる一方、界面の接着強度が減退して電
極板とセパレーター板とが剥離を起こす欠点があった。
However, in the case of the bonding and firing method described above, a phenomenon occurs in which the adhesive penetrates into the tissue of the porous electrode, which reduces the porosity of the electrode member, while the adhesive strength at the interface decreases and the electrode plate and the separator plate are reduced. There was a defect that and peeled off.

そこで、本発明者らは接合時における接着剤の電極浸透
を防ぎかつ焼成段階で揮散消失する物質で予め電極基材
を処理する方法を先に提案した(特開昭62−126562号公
報)。
Therefore, the present inventors have previously proposed a method of preventing the electrode from penetrating the adhesive at the time of bonding and treating the electrode base material with a substance that volatilizes and disappears during the firing step (Japanese Patent Laid-Open No. 62-126562).

しかしながら、この方法を採る場合には前処理として1
工程が加わるため、生産能率が低下する難点がある。
However, if this method is adopted,
Since the process is added, there is a problem that the production efficiency is reduced.

〔発明が解決しようとする課題〕[Problems to be Solved by the Invention]

近時、セルサイズの大型化に伴って部材接着力の増大な
らびに基板内部での電気抵抗の均一化が一層要求されて
きている。この性能要求に対しては、接着剤の接着強度
を高めるとともに接着界面を均一化してバラツキのない
接着層を形成することが必須の要件となるが、従来技術
による接着剤で前記の要件を全面的に満足する組成のも
のはない。とくに従来の接着剤では接着層の不均一化が
現出する傾向が強く、これは電気抵抗の変動ばかりでな
く、加工時、接着層に剪断力が働くために層薄の部分か
ら電極部材が欠落するなど、加工上の問題点ともなる。
Recently, with the increase in cell size, there has been an increasing demand for an increase in member adhesive force and uniform electric resistance inside the substrate. In order to meet this performance requirement, it is essential to increase the adhesive strength of the adhesive and to form a uniform adhesive interface by making the adhesive interface uniform. There is no composition that satisfies the requirements. Especially with conventional adhesives, there is a strong tendency for non-uniformity of the adhesive layer to appear, which is due to shearing force acting on the adhesive layer during processing, as well as fluctuations in electrical resistance, so that the electrode member from the thin layer It also becomes a problem in processing such as missing.

本発明は、接着剤の組成を改良して上記問題点の解消を
図ったもので、その目的は大型サイズの電極部材とセパ
レーターにおいても界面間に優れた接着強度と均一な電
気抵抗を付与することができる生産効率のよい燃料電池
用炭素質複合電極基板の製造方法を提供することにあ
る。
The present invention aims to solve the above problems by improving the composition of the adhesive, and the object thereof is to provide excellent adhesive strength and uniform electric resistance between the interfaces even in a large size electrode member and a separator. (EN) It is possible to provide a method for producing a carbonaceous composite electrode substrate for a fuel cell, which is capable of high production efficiency.

〔課題を解決するための手段〕[Means for Solving the Problems]

上記の目的を達成するための本発明による燃料電池用炭
素質複合電極基板の製造方法は、平均粒子径1〜10μm
の炭素質粉末10〜40重量部と平均粒子径20〜80μmの炭
素質粉末60〜90重量部を混合したのち残炭率40%以上の
液状熱硬化性樹脂と混練して粘度500〜5000ポイズの接
着剤を調製し、該接着剤を炭素質セパレーター部材の表
面に接着層の厚さが50〜200μmになるように均一塗布
して多孔炭素質電極板と接合し、加圧加熱下で接着層を
硬化したのち非酸化性雰囲気中で800℃以上の温度域で
焼成炭化することを構成上の特徴とする。
The method for producing a carbonaceous composite electrode substrate for a fuel cell according to the present invention for achieving the above-mentioned object has an average particle size of 1 to 10 μm.
10 to 40 parts by weight of carbonaceous powder and 60 to 90 parts by weight of carbonaceous powder having an average particle diameter of 20 to 80 μm are mixed, and then kneaded with a liquid thermosetting resin having a residual carbon ratio of 40% or more to have a viscosity of 500 to 5000 poises. The adhesive is prepared, and the adhesive is uniformly applied to the surface of the carbonaceous separator member so that the thickness of the adhesive layer is 50 to 200 μm, bonded to the porous carbonaceous electrode plate, and bonded under pressure and heating. The structural feature is that after the layer is cured, it is fired and carbonized in a temperature range of 800 ° C. or higher in a non-oxidizing atmosphere.

本発明の構成部材となる炭素質セパレーター板として
は、黒鉛基板にフェノール系、フラン系などの熱硬化性
樹脂液を含浸硬化して焼成する方法、黒鉛微粉末をフェ
ノール樹脂、フラン樹脂あるいはタールピッチなどと混
練して板状成形したのち焼成する方法、フェノール樹脂
またはフラン樹脂の成形板を焼成してガラス状カーボン
化する方法等で得られる不透過性の緻密質組織と表面平
滑性を備える薄板材料が併用される。
As the carbonaceous separator plate which is a constituent member of the present invention, a graphite substrate is impregnated with a thermosetting resin liquid such as a phenol-based or furan-based resin and cured, and graphite fine powder is mixed with phenol resin, furan resin or tar pitch. A thin plate with an impermeable dense structure and surface smoothness obtained by, for example, a method of kneading with the above to form a plate and then firing, or a method of firing a molded plate of phenol resin or furan resin to form a glassy carbon. Materials are used together.

また、多孔炭素質電極板には、炭素繊維あるいはポリア
クリルニトリル、セルローズなどの有機質繊維を例えば
フェノール樹脂のような熱硬化性樹脂と共に薄板状に成
形したのち、焼成炭化した多孔質組織をもつ炭素材料が
使用される。
For the porous carbonaceous electrode plate, carbon fibers or organic fibers such as polyacrylonitrile and cellulose are molded into a thin plate together with a thermosetting resin such as a phenol resin, and then carbonized by firing and carbonization. Material is used.

本発明の要点は、炭素質セパレーターと多孔炭素質電極
板を、平均粒子径1〜10μmの炭素質粉末10〜40重量部
と平均粒子径20〜80μmの炭素質粉末60〜90重量部を混
合したのち残炭率40%以上の液状熱硬化性樹脂と混練し
て調製した粘度500〜5000ポイズの接着剤を介して接合
するところにある。
The gist of the present invention is to mix a carbonaceous separator and a porous carbonaceous electrode plate with 10 to 40 parts by weight of carbonaceous powder having an average particle diameter of 1 to 10 μm and 60 to 90 parts by weight of carbonaceous powder having an average particle diameter of 20 to 80 μm. After that, they are bonded together with an adhesive having a viscosity of 500 to 5000 poise prepared by kneading with a liquid thermosetting resin having a residual carbon rate of 40% or more.

平均粒子径範囲の異なる炭素質粉末を特定された配合比
で混合使用するのは、焼成炭化後の接着強度を向上させ
低い電気抵抗を与えるための組成条件であり、前記の粒
子径範囲と配合範囲を満たさないと効果的な接着強度の
増大および低位の電気抵抗の付与は期待できなくなる。
Mixing and using carbonaceous powders having different average particle diameter ranges in a specified mixing ratio is a composition condition for improving the adhesive strength after firing and carbonization and giving a low electric resistance. If the range is not satisfied, effective increase in adhesive strength and provision of low electrical resistance cannot be expected.

炭素質粉末としては、コークス、炭素、天然黒鉛、人造
黒鉛、ガラス状カーボンなどを所定粒度範囲に粉砕した
ものを適用することができるが、特に高純度で良電導性
を有する人造黒鉛粉末が効果よく用いることができる。
As the carbonaceous powder, it is possible to apply coke, carbon, natural graphite, artificial graphite, glassy carbon, or the like crushed to a predetermined particle size range, but especially artificial graphite powder having high purity and good electrical conductivity is effective. Can be used well.

残炭率40%以上の液状熱硬化性樹脂とは、非酸化性雰囲
気中で1000℃の温度に焼成した際に40重量%以上の炭素
分が残留する性質の熱硬化性樹脂液を指し、例えばフェ
ノール系樹脂、フラン系樹脂、ポリイミド樹脂などの初
期縮合物が該当する。
Liquid thermosetting resin with a residual carbon ratio of 40% or more refers to a thermosetting resin liquid having a property that 40% by weight or more of carbon content remains when baked at a temperature of 1000 ° C. in a non-oxidizing atmosphere, For example, an initial condensate such as a phenol resin, a furan resin, or a polyimide resin is applicable.

接着剤の粘度を500〜5000ポイズの範囲に設定する理由
は、500ポイズを下廻る粘度では接着剤が電極板の多孔
組織内に浸透して接着強度の低下を招き、5000ポイズを
越えると塗布が困難となって接着層の厚さが不均質とな
るためである。この粘度範囲を確保するには、前記炭素
質粉末の混合物100重量部に対し液状熱硬化性樹脂を概
ね50〜150重量部の範囲で量調整し、混練すればよい。
The reason for setting the viscosity of the adhesive in the range of 500 to 5000 poise is that at a viscosity below 500 poise, the adhesive penetrates into the porous structure of the electrode plate and causes a decrease in adhesive strength, and when it exceeds 5000 poise, it is applied. This is because the adhesive layer becomes difficult and the thickness of the adhesive layer becomes non-uniform. In order to secure this viscosity range, the liquid thermosetting resin may be adjusted in an amount of about 50 to 150 parts by weight and kneaded with 100 parts by weight of the mixture of carbonaceous powder.

上記組成の接着剤は、炭素質セパレーター板の表面に接
着層の厚さが50〜200μmになるように均一塗布して多
孔炭素質電極板と接合する。接着層の厚さが50μm未満
であると接着力が不足して部分的な剥離が発生し易くな
り、200μmを上廻る接着層の厚さになると接着界面の
剥離が多発するようになる。
The adhesive having the above composition is uniformly applied to the surface of the carbonaceous separator plate so that the thickness of the adhesive layer is 50 to 200 μm, and bonded to the porous carbonaceous electrode plate. When the thickness of the adhesive layer is less than 50 μm, the adhesive force is insufficient and partial peeling is likely to occur, and when the thickness of the adhesive layer exceeds 200 μm, peeling of the adhesive interface frequently occurs.

接着剤の塗布は、例えばドクターブレード法のような機
械的手段を用いておこなうことが好ましく、接着層の厚
さのバラツキとして±0.03mmの範囲に収めることが望ま
しい。該バラツキの範囲を外れると、部材の局部的な剥
離が起き易くなるうえ電気抵抗の変動が大きくなる。
The application of the adhesive is preferably carried out by using a mechanical means such as a doctor blade method, and it is desirable that the variation in the thickness of the adhesive layer is within ± 0.03 mm. If the variation is out of the range, local peeling of the member is likely to occur and variation in electric resistance increases.

接合処理後の部材は、加圧加熱下で接着層を硬化する。
この場合の好ましい条件は、加圧力1〜20kg/cm2、温度
50〜300℃である。
The member after the bonding treatment cures the adhesive layer under pressure and heating.
In this case, the preferred conditions are pressure 1-20 kg / cm 2 , temperature
50 to 300 ° C.

ついで、接合部材を焼成炉に移し、非酸化性雰囲気中で
800℃以上の温度域で焼成炭化する。このほか、サイド
シール部の設置、所要の加工(平面、外周、溝などの加
工)を施して燃料電池用炭素質複合電極基板を得る。
Then, transfer the joint members to a firing furnace and place them in a non-oxidizing atmosphere.
Carbonizes by firing in a temperature range of 800 ° C or higher. In addition, a side seal portion is installed and required processing (processing of flat surface, outer circumference, groove, etc.) is performed to obtain a carbonaceous composite electrode substrate for a fuel cell.

〔作 用〕[Work]

本発明によれば、接着剤のフィラー成分として平均粒子
径1〜10μmの炭素質粉末10〜40重量部と平均粒子径20
〜80μmの炭素質粉末60〜90重量部を混合使用すること
により、焼成炭化時に粒度分布が2山となる導電性微粒
子が熱硬化性樹脂の炭化組織の内部に混在した独特の接
着層を形成し、この接着層が接着強度を向上させ、同時
に電気抵抗を低減させるために機能する。
According to the present invention, 10 to 40 parts by weight of carbonaceous powder having an average particle diameter of 1 to 10 μm and an average particle diameter of 20 are used as a filler component of an adhesive.
By mixing and using 60 to 90 parts by weight of carbonaceous powder of -80 μm, a unique adhesive layer is formed in which conductive fine particles whose particle size distribution has two peaks during firing and carbonization are mixed inside the carbonized structure of the thermosetting resin. However, this adhesive layer functions to improve the adhesive strength and at the same time reduce the electric resistance.

また、接着剤の粘度を500〜5000ポイズとし、塗布の厚
さを接着層が50〜200μmになる条件を与えることは、
接着層の均一性を確保して電気抵抗の変動を軽減化する
とともに、接着界面の剥離を阻止する働きをなす。
In addition, the viscosity of the adhesive is set to 500 to 5000 poise, and the thickness of the coating is set to 50 to 200 μm for the adhesive layer.
It secures the uniformity of the adhesive layer to reduce the fluctuation of electric resistance and also serves to prevent the peeling of the adhesive interface.

このような作用が相乗して、大型サイズの燃料電池用複
合電極基板に要求される接着層部分の強化と電気抵抗の
均一化を効果的に付与することが可能となる。
By such synergistic effects, it becomes possible to effectively impart the strengthening of the adhesive layer portion and the uniformization of electric resistance required for a large-sized composite electrode substrate for a fuel cell.

〔実施例〕〔Example〕

以下、本発明の実施例を比較例と対比して説明する。 Hereinafter, examples of the present invention will be described in comparison with comparative examples.

実施例1〜5、比較例1〜10 (1)接着剤の調製 平均粒子径3μmの人造黒鉛微粉末と平均粒子径40μm
の人造黒鉛微粉末を用意し、両者を各種の配合比で混合
した。各混合粉末をフェノール樹脂初期縮合物〔住友デ
ュレズ(株)製、PR940〕に加えてニーダーにより十分
に混練し、粘度の異なるペースト状接着剤を調製した。
Examples 1 to 5, Comparative Examples 1 to 10 (1) Preparation of Adhesive Artificial graphite fine powder having an average particle diameter of 3 μm and an average particle diameter of 40 μm
The artificial graphite fine powder of was prepared, and both were mixed at various compounding ratios. Each mixed powder was added to a phenol resin initial condensate [PR940 manufactured by Sumitomo Durres Co., Ltd.] and kneaded sufficiently with a kneader to prepare paste adhesives having different viscosities.

(2)複合電極基板の製造 多孔炭素質電極板として、ピッチ系炭素繊維のチョップ
(平均長さ20mm)をフェノール樹脂と混合してモールド
成形したのち2000℃で焼成して得た縦1010mm、横920m
m、厚さ2mmのサイズで、気孔率64%、平均気孔径50μm
の性状を有する板状体を用いた。炭素質セパレーター板
としては、黒鉛微粉(平均粒径5μm)を混練したフェ
ノール樹脂を圧延成形したのち硬化し、ついで1300℃で
焼成して得た一辺の長さ1000mm、厚さ0.6mmの正方形薄
板を用いた。
(2) Manufacture of composite electrode substrate As a porous carbon electrode plate, a pitch-based carbon fiber chop (average length 20 mm) was mixed with phenol resin, molded, and then baked at 2000 ° C. to obtain 1010 mm in length and 10 mm in width. 920m
m, thickness 2 mm, porosity 64%, average pore diameter 50 μm
A plate-like body having the property of was used. As the carbonaceous separator plate, a square thin plate with a side length of 1000 mm and a thickness of 0.6 mm obtained by rolling and molding a phenol resin in which graphite fine powder (average particle size 5 μm) is kneaded, followed by hardening and then firing at 1300 ° C. Was used.

このセパレーター板の表面にドクターブレード法で接着
剤を塗布し、前記の多孔炭素質電極板を両面に接合し
た。接合は、セパレーター板の表裏面に電極板の長さ方
向が直交し、かつ両端に45mmの間隔があくようにおこな
った。
An adhesive was applied to the surface of this separator plate by the doctor blade method, and the porous carbonaceous electrode plates were joined to both surfaces. The joining was performed so that the front and back surfaces of the separator plate were orthogonal to each other in the length direction of the electrode plate and there was a space of 45 mm at both ends.

接合後の部材は、80℃に加熱しながらプレスにより5kg/
cm2の圧力を加えて接着剤の樹脂成分を硬化した。
The member after joining is heated to 80 ℃ and pressed at 5kg /
A pressure of cm 2 was applied to cure the resin component of the adhesive.

ついで、接合部材を電気焼成炉に移しコークス粉で被包
したのち、5℃/分の昇温速度で1000℃まで上昇させて
焼成処理を施した。
Next, the joint member was transferred to an electric firing furnace, covered with coke powder, and then heated to 1000 ° C. at a heating rate of 5 ° C./min to perform a firing treatment.

焼成して接着層を炭化した一体化部材の両端部に、セパ
レーター板と同一材質のサイドシールを前記接合剤を介
して接合した。引き続き、一辺の長さ1000mm、厚さ2.8m
mのセルサイズになるように外周および平面加工をおこ
ない、更に電極部分に上下直交する状態に溝(幅2mm、
深さ1mm)を設置してリン酸型燃料電池用の炭素質複合
電極基板を製造した。
Side seals made of the same material as the separator plate were joined to both ends of the integrated member obtained by firing and carbonizing the adhesive layer via the joining agent. Continuously, the length of one side is 1000 mm and the thickness is 2.8 m.
The outer periphery and the flat surface are processed so that the cell size becomes m, and the groove (width 2 mm,
A carbonaceous composite electrode substrate for a phosphoric acid fuel cell was manufactured by setting a depth of 1 mm).

(3)特性の評価 得られた各複合電極基板について測定された特性・性状
を、接着剤の組成と対比させて表1に示した。
(3) Evaluation of characteristics The characteristics and properties measured for each of the obtained composite electrode substrates are shown in Table 1 in comparison with the composition of the adhesive.

なお、表1に示した各種性状および特性の測定方法は下
記によった。
The methods for measuring various properties and characteristics shown in Table 1 were as follows.

接着層の厚さ−:試片を16等分し、側面を光学顕微鏡
で観察して層厚を測定する。
Thickness of adhesive layer: The test piece is divided into 16 equal parts, and the side surface is observed with an optical microscope to measure the layer thickness.

電極気孔率、電極気孔径−:接着後の電極部材を水銀
圧入法により気孔径0.01μmまでの気孔率を測定する。
気孔径は、前気孔体積の50%として示した。
Electrode porosity, electrode porosity-: The porosity of the electrode member after adhesion is measured up to 0.01 μm by the mercury porosimetry.
Pore size was shown as 50% of pre-pore volume.

電気抵抗−:電圧降下法で面積当たりの抵抗値を測定
し、面積と全抵抗を乗じて算出する。
Electric resistance: The resistance value per area is measured by the voltage drop method, and the product is calculated by multiplying the area by the total resistance.

接着強度−:セパレーター板試片(30×50×0.8mm)
に接着剤(幅3mm)を塗布し、2枚の試片を接合、硬化
したのち非酸化雰囲気中で1000℃の温度で焼成する。こ
の2枚の接合界面を引張り、剥離に要した力を接着強度
とする。
Adhesive strength-: Separator plate specimen (30 x 50 x 0.8 mm)
An adhesive (width: 3 mm) is applied to the two, the two test pieces are joined, cured, and then fired at a temperature of 1000 ° C. in a non-oxidizing atmosphere. The bonding interface between the two sheets is pulled and the force required for peeling is defined as the adhesive strength.

表1の結果から、本発明の要件を満たす実施例では大型
サイズの電極基板であるにも拘わらず相対的に高い接着
強度とバラツキの少ない低電気抵抗を備えており、かつ
比較例に見られる接着剤の浸透に伴う電極組織の気孔率
低下、接着界面の剥離による加工歩留の減退等の現象は
認められない。
From the results of Table 1, the examples satisfying the requirements of the present invention have relatively high adhesive strength and low electric resistance with little variation, even though they are large-sized electrode substrates, and are found in the comparative examples. No phenomena such as a decrease in the porosity of the electrode structure due to the permeation of the adhesive and a reduction in the processing yield due to the peeling of the adhesive interface are observed.

〔発明の効果〕 以上のとおり、本発明に従えば特定された組成の接着剤
および接着条件を適用することにより、大型サイズであ
っても常に優れた接着強度と均一かつ低位の電気抵抗を
備える燃料電池用炭素質複合電極基板を製造することが
できる。
[Advantages of the Invention] As described above, according to the present invention, by applying the adhesive having the specified composition and the adhesion conditions, it is possible to always provide excellent adhesive strength and uniform and low electric resistance even in a large size. A carbonaceous composite electrode substrate for a fuel cell can be manufactured.

そのうえ、余分な処理工程を必要とせず、剥離現象を伴
う加工歩留の減退もないから生産性が頗る良好である。
In addition, it does not require an extra processing step, and there is no reduction in processing yield due to the peeling phenomenon, so that productivity is excellent.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】平均粒子径1〜10μmの炭素質粉末10〜40
重量部と平均粒子径20〜80μmの炭素質粉末60〜90重量
部を混合したのち残炭率40%以上の液状熱硬化性樹脂と
混練して粘度500〜5000ポイズの接着剤を調製し、該接
着剤を炭素質セパレーター板の表面に接着層の厚さが50
〜200μmになるように均一塗布して多孔炭素質電極板
と接合し、加圧加熱下で接着層を硬化したのち非酸化性
雰囲気中で800℃以上の温度域で焼成炭化することを特
徴とする燃料電池用炭素質複合電極基板の製造方法。
1. A carbonaceous powder having an average particle size of 1 to 10 μm 10 to 40.
After mixing 60 parts by weight and 60 to 90 parts by weight of carbonaceous powder having an average particle size of 20 to 80 μm with a liquid thermosetting resin having a residual carbon ratio of 40% or more to prepare an adhesive having a viscosity of 500 to 5000 poises, The adhesive is applied to the surface of the carbonaceous separator plate so that the thickness of the adhesive layer is 50
~ 200μm evenly applied and bonded to a porous carbonaceous electrode plate, the adhesive layer is cured under pressure and heating, then carbonized in a temperature range of 800 ℃ or more in a non-oxidizing atmosphere Of manufacturing carbonaceous composite electrode substrate for fuel cell.
JP2296334A 1990-11-01 1990-11-01 Method for producing carbonaceous composite electrode substrate for fuel cell Expired - Fee Related JPH07120532B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2296334A JPH07120532B2 (en) 1990-11-01 1990-11-01 Method for producing carbonaceous composite electrode substrate for fuel cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2296334A JPH07120532B2 (en) 1990-11-01 1990-11-01 Method for producing carbonaceous composite electrode substrate for fuel cell

Publications (2)

Publication Number Publication Date
JPH04169070A JPH04169070A (en) 1992-06-17
JPH07120532B2 true JPH07120532B2 (en) 1995-12-20

Family

ID=17832198

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2296334A Expired - Fee Related JPH07120532B2 (en) 1990-11-01 1990-11-01 Method for producing carbonaceous composite electrode substrate for fuel cell

Country Status (1)

Country Link
JP (1) JPH07120532B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111758177B (en) 2017-10-03 2025-02-14 威拓股份有限公司 Carbon-based electrodes with large geometric dimensions

Also Published As

Publication number Publication date
JPH04169070A (en) 1992-06-17

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