JPS60167271A - Manufacture of porous carbon electrode with rib - Google Patents

Manufacture of porous carbon electrode with rib

Info

Publication number
JPS60167271A
JPS60167271A JP59021813A JP2181384A JPS60167271A JP S60167271 A JPS60167271 A JP S60167271A JP 59021813 A JP59021813 A JP 59021813A JP 2181384 A JP2181384 A JP 2181384A JP S60167271 A JPS60167271 A JP S60167271A
Authority
JP
Japan
Prior art keywords
fibers
carbon
sheet
binder
carbon 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.)
Pending
Application number
JP59021813A
Other languages
Japanese (ja)
Inventor
Osamu Iwaki
岩城 修
Yasuhei Awata
粟田 泰平
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.)
New Oji Paper Co Ltd
Original Assignee
Oji Paper 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 Oji Paper Co Ltd filed Critical Oji Paper Co Ltd
Priority to JP59021813A priority Critical patent/JPS60167271A/en
Publication of JPS60167271A publication Critical patent/JPS60167271A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B35/00Shaped ceramic products characterised by their composition; Ceramics compositions; Processing powders of inorganic compounds preparatory to the manufacturing of ceramic products
    • C04B35/71Ceramic products containing macroscopic reinforcing agents
    • C04B35/78Ceramic products containing macroscopic reinforcing agents containing non-metallic materials
    • C04B35/80Fibres, filaments, whiskers, platelets, or the like
    • C04B35/83Carbon fibres in a carbon matrix
    • 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
    • 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

Abstract

PURPOSE:To produce a porous carbon electrode with rib for a fuel cell by impregnating an organic high molecular substance into a sheet manufactured by using a mixture of carbon fibers, pulp, and binder with a paper making machine, by heat-pressing, cutting, then carbonizing them. CONSTITUTION:A mixture of 60-95wt% organic fibers which are used for manufacturing carbon fibers of carbon fibers and 40-5wt% pulp and binder is produced in a sheet with a paper making machine. The sheet is impregnated with an organic high molecular substance, and molded and cured with a heat press, and cut in a desired form, then carbonized in an atmosphere of inactive gas at 800 deg.C under a pressure of 2-50g/cm<2> to form an electrode substrate with a rib 1 and a groove 2 for a fuel cell. Thereby, a flat carbon electrode having homogeneousness is readily manufactured and productivity is increased.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、リブ付多孔質炭素!、極の新規な製造方法に
関するものである。更に詳しく述べると、抄紙法によシ
得られたシートを含浸後、切削加工を行なった熱焼成す
ることによシ、厚手のリブ付多孔質炭素′亀憔を製造す
る方法に関するものである。
[Detailed Description of the Invention] (Industrial Application Field) The present invention is a porous carbon with ribs! , relates to a novel method for manufacturing poles. More specifically, the present invention relates to a method for producing a thick ribbed porous carbon sludge by impregnating a sheet obtained by a papermaking method, followed by cutting and thermal firing.

添付の第1図は、リブ付炭素電慣の防面であって、図中
の符号1はリブ部を示し、符号2は線部を示す。
FIG. 1 attached herewith shows a ribbed carbon electrolytic shield, in which reference numeral 1 indicates a rib portion and reference numeral 2 indicates a line portion.

(先行技術) 従来、リブ付炭素電極を得る方法として、炭素繊維をバ
インダーと共に抄紙した炭素繊維シートを焼成し、得ら
れた炭素板を機械的に溝切削加工する方法が行われてい
る。しかしながら、上6r2で得られた炭素板は非常に
堅いため細い溝切削加工が容易でないこと、また、柔軟
性が小さいため破損しやすく、そのため取扱いが谷易で
なく、作業性が悪い欠点があった。
(Prior Art) Conventionally, as a method for obtaining a ribbed carbon electrode, a method has been used in which a carbon fiber sheet made of carbon fibers together with a binder is fired, and the obtained carbon plate is mechanically grooved. However, the carbon plate obtained using 6r2 is very hard, so it is difficult to cut thin grooves, and it is less flexible, so it easily breaks, making it difficult to handle and having poor workability. Ta.

(発明の目的) 本発明は上記の欠点を改良すると共に、安価で高品質の
リブ付多孔質炭素電極を製造する方法を提供することを
目的とする。
(Objective of the Invention) An object of the present invention is to improve the above-mentioned drawbacks and to provide a method for manufacturing a ribbed porous carbon electrode of low cost and high quality.

(発明の構成) 本発明は、炭素繊維製造用有機繊維および炭素繊維から
選ばれた少なくとも一棟の繊維60〜95重世%とパル
プおよび/または抄紙用バインダー40〜5重重%から
なる混合物を抄紙して得られたシートに有機高分子vl
J質の浴液を含浸して含浸シートを得、該含浸シートを
、好ましくは積増してプレスで成形硬化処理を行ない、
次いで切削加工を行ない必要に応じて不融化処理を行な
った後、不活性ガス雰囲気中で800℃以上の温度で、
好ましくは2〜502/dの荷1圧力下で加熱炭化させ
ることを特徴とする多孔買炭素寛極の製造方法である。
(Structure of the Invention) The present invention provides a mixture comprising 60 to 95% by weight of at least one fiber selected from organic fibers for producing carbon fibers and carbon fibers and 40 to 5% by weight of a binder for pulp and/or paper making. Organic polymer VL is added to the sheet obtained by papermaking.
Obtain an impregnated sheet by impregnating it with a bath liquid of J quality, preferably pile up the impregnated sheet and perform a molding hardening treatment with a press,
Next, after cutting and performing infusibility treatment if necessary, at a temperature of 800°C or higher in an inert gas atmosphere,
This is a method for producing a porous carbon-containing electrode, which is characterized by heating and carbonizing under a pressure of preferably 2 to 502/d.

本発明の構成要素について以下に評説する。The constituent elements of the present invention will be reviewed below.

〈原料繊維〉 本発明に用いる炭素繊維製造用有機繊維としては、再生
セルロース繊維、ピッチ繊維、フェノール繊維、ポリア
クリロニトリル繊維等、炭素繊維を製造する場合に晋通
に使用される有機繊維、および炭素繊維が適当であシ、
太さ0.5〜15デニール、長さ2〜15m、好ましく
は抄紙性寺の点から太さ0.5〜8デニール、長さ1.
5〜10mmのものを目的に応じて選択し、単独である
いは2種以上を配合して使用する。
<Raw material fibers> The organic fibers for producing carbon fibers used in the present invention include organic fibers used in Jintong when producing carbon fibers, such as regenerated cellulose fibers, pitch fibers, phenol fibers, and polyacrylonitrile fibers; The fiber is suitable,
Thickness: 0.5 to 15 denier, length: 2 to 15 m, preferably 0.5 to 8 denier, length: 1.
Those with a diameter of 5 to 10 mm are selected depending on the purpose and used alone or in combination of two or more.

この発明に用いられるノ々ルプとしては、セルロースパ
ルプのほか、各棟合成パルプが適しておシ、これらのパ
ルプは抄紙の際に有機繊維のつなぎとして作用する。
In addition to cellulose pulp, various synthetic pulps are suitable as the pulp used in this invention, and these pulps act as a binder for organic fibers during paper making.

炭素h1.維製造用有機繊維、炭素繊維は抄紙用混合物
の60〜95重蓋%の割合で使用される。
Carbon h1. Organic fibers for textile manufacturing and carbon fibers are used in a ratio of 60 to 95% of the papermaking mixture.

炭素繊維製造用有機繊維および炭素繊維が60重蓋%以
下になると、孔径、気孔率等のコントロールがむすかし
くなシ、かつ強にも低くなって良好なシートが得られな
くなシ、一方95重童%以上では抄紙の際に良好なシー
ト形成がむすかしい。
If the amount of organic fibers and carbon fibers used for manufacturing carbon fibers is less than 60%, it becomes difficult to control the pore diameter, porosity, etc., and the porosity becomes too low, making it impossible to obtain a good sheet. If it exceeds %, it is difficult to form a good sheet during paper making.

〈バインダー〉 抄紙用バインダーとしては、例えばポリビニルアルコー
ル繊維、各種合成パルプ、抄紙用レーヨン等の冷水中に
溶解しないが熱水に溶解する繊維で、抄紙用バインダー
として一般に市販されているものを使用することができ
る。
<Binder> As a binder for papermaking, for example, fibers that do not dissolve in cold water but dissolve in hot water, such as polyvinyl alcohol fibers, various synthetic pulps, and rayon for papermaking, and are generally commercially available as binders for papermaking are used. be able to.

合成樹脂エマルジョンも抄紙用バインダーとして使用す
ることができる。
Synthetic resin emulsions can also be used as binders for papermaking.

パルプおよびまたは抄紙用バインダーは抄紙用混合物の
40〜5M量%の割合で使用される。
The pulp and/or papermaking binder is used in an amount of 40 to 5M% of the papermaking mixture.

湿潤強度を維持するためには、パルプと抄紙用バインダ
ーとを合計で5N量%以上配合するのが好ましい。
In order to maintain wet strength, it is preferable to mix pulp and papermaking binder in a total amount of 5N or more.

く抄紙方法〉 抄紙は、通常の湿式法でも、乾式法の何れでもよいが、
シート密度が低い場合は乾式法が好適であシ、比較的嶋
密匿では湿式法が好適である。
Paper making method〉 Paper making can be done by either the normal wet method or dry method.
When the sheet density is low, the dry method is suitable, and when the sheet density is relatively dense, the wet method is suitable.

く有機高分子物質〉 含浸に用いる有機高分子物質としては、例えばフェノー
ル樹脂、エポキシ樹脂、不飽和ポリエステル樹脂、ポリ
ジビニルベンゼンの如き熱硬化性樹脂、塩化ビニル樹脂
、塩化ビニリデン樹脂、フッ化ビニル樹脂、フッ化ビニ
リデン樹脂、アクリロニトリル樹脂等の熱可塑性樹脂、
さらにはリグニン、ピッチ又はタールの如きものも使用
される。
Organic polymeric substances> Examples of organic polymeric substances used for impregnation include phenolic resins, epoxy resins, unsaturated polyester resins, thermosetting resins such as polydivinylbenzene, vinyl chloride resins, vinylidene chloride resins, and vinyl fluoride resins. , thermoplastic resins such as vinylidene fluoride resin, acrylonitrile resin,
Furthermore, materials such as lignin, pitch or tar may also be used.

これらの高分子化合物の好ましい性質としては、何等か
の溶剤に溶解するか又は熱処理時の昼温で融解すること
および炭素言有童が30重蓋%以上る9炭化後、炭素質
バインダーとして炭素繊維内のM曾に役立つものであシ
、熱硬化性(1M脂が好ましい。
The preferable properties of these polymer compounds are that they are soluble in some solvent or melt at daytime temperature during heat treatment, and that after carbonization with a carbon content of 30% or more, carbon can be used as a carbonaceous binder. It is a thermosetting resin (preferably 1M resin) that helps with the M content in the fibers.

前記のM機高分子vlJ負の浴液筐たは分散液により混
抄紙を@浸処理する。混抄紙に耐層する含浸量が少なす
ぎると、バインダー効果、及び炭化の際の炭化収率が劣
り、あま9過剰になると目づまシのため気孔率の調整が
むつかしく、又もろくなる。好ましい含浸付着量として
は、混抄紙の重量の20〜200%、更に好ましくは3
0〜120%である。
The mixed paper is immersed in the M machine polymer vlJ negative bath solution or dispersion. If the amount of impregnated paper that resists the layer is too small, the binder effect and the carbonization yield during carbonization will be poor, and if it is too much, it will be difficult to adjust the porosity due to blockage, and it will become brittle. The preferred amount of impregnation is 20 to 200% of the weight of the mixed paper, more preferably 3
It is 0-120%.

〈プレス処理〉 シートの坪量は最終炭素電極の厚さ、密度から必要な重
さのシートを設定して、プレス処理を行なう。プレス成
形は最終炭素電極に必要な厚さ、形状、気孔率、孔径を
付与するために行ない、その際、加熱処理を併用するこ
とにょシ含浸シート中の樹脂7に硬化させる。この硬化
処理によシシートの厚みを一定に保持すると同時に平坦
なシートを得ることが可能になった。またプレス圧力を
調整することにょシ炭素板の気孔率、孔径を任意に変え
ることができる。
<Press treatment> The basis weight of the sheet is set to the required weight based on the thickness and density of the final carbon electrode, and press treatment is performed. Press molding is performed to give the final carbon electrode the necessary thickness, shape, porosity, and pore size, and at this time, heat treatment may also be used to harden the resin 7 in the impregnated sheet. This curing treatment made it possible to maintain a constant thickness of the sheet and at the same time obtain a flat sheet. Furthermore, the porosity and pore diameter of the carbon plate can be changed arbitrarily by adjusting the press pressure.

上記プレス処理の際、薄手の含浸シートを必要枚数、好
ましくは3枚以上重ね合せ、同様にプレス処理を行なう
と、容易に厚手の炭素電極が得られる。通常では剥離を
生じゃすく、製造が困難な多孔質シートの積層が、本発
明のプレス積層、硬化法で可能になった。含浸シートを
重ね合せる際、シートの縦方向と横方向を又互に積ノー
するとシートの方向性が無くなり、加熱炭化の際の歪が
生じにくくなシヵール、ヒビ割れのない厚みの均一な炭
素電極が得られる。プレス加熱条件としては、150〜
220℃、1〜60分間が適当である。
During the above press treatment, a thick carbon electrode can be easily obtained by stacking a required number of thin impregnated sheets, preferably three or more sheets, and performing the press treatment in the same manner. The press lamination and curing method of the present invention has made it possible to laminate porous sheets, which are normally difficult to manufacture due to the risk of peeling. When stacking impregnated sheets, stacking them both vertically and horizontally will eliminate the orientation of the sheets, resulting in a carbon electrode with a uniform thickness without cracks or cracks that are less prone to distortion during heating and carbonization. is obtained. The press heating conditions are 150~
220°C for 1 to 60 minutes is suitable.

〈溝切り〉 プレス成形されたシートは次いで所望の寸法の溝を通常
の機械的切削によりもうける。プレス成形後のシートは
炭化されていないため、柔軟で、取扱いが容易であシ、
又切削加工も炭素板に比べ加工性が容易であシ、加工精
度の良好な製品が得られる。
<Grooving> The press-formed sheet is then grooved with desired dimensions by conventional mechanical cutting. The sheet after press forming is not carbonized, so it is flexible and easy to handle.
Furthermore, machining is easier than with carbon plates, and products with good machining accuracy can be obtained.

く不融化と焼成〉 上記切hυ加工を行なったシートは必要にょシネ融化し
た後に焼成して炭素′電極を形成するが、この不融化処
理に、有機繊維としてポリアクリロニ)IJル稙維、ピ
ッチ繊維を、また有機高分子物質としてフェノール樹脂
等の熱硬化性dRBF1を使用した場合に特に有効であ
り、炭化収率、シート強度向上に顕著な効果がある。不
融化の処理条件は、特に特定しないが、例えば150〜
350℃、数10分〜10数時間、ガス雰囲気としては
空気中で有機高分子物質の付着した混抄紙を加熱するこ
とによシネ融化される。
Infusibility and firing> The sheet subjected to the above-mentioned cutting process is required to be infusible and then fired to form a carbon electrode.For this infusibility treatment, organic fibers such as polyacrylon fibers, IJ fibers, and pitch fibers are added. It is particularly effective when thermosetting dRBF1 such as phenol resin is used as the organic polymer material, and has a remarkable effect on improving carbonization yield and sheet strength. The treatment conditions for infusibility are not particularly specified, but for example, 150~
Cine-melting is carried out by heating the mixed paper to which the organic polymer substance has adhered at 350° C. for several tens of minutes to several tens of hours in an air gas atmosphere.

ついで、不活性ガス雰囲気中で800℃以上の温度下で
加熱焼成して炭素質バインダーを含むリブ付多孔質炭素
電極を形成する。熱処理温度を変えることによシ最終製
品の電気抵抗値の制御が可能である。また、上記の加熱
焼成を2〜501/−の圧力で荷重加圧しながら行なう
と、非常に強度が大きくかつ均一な厚みと平坦性を有す
る炭素板を得ることができる。
Then, the electrode is heated and fired at a temperature of 800° C. or higher in an inert gas atmosphere to form a ribbed porous carbon electrode containing a carbonaceous binder. By changing the heat treatment temperature, it is possible to control the electrical resistance value of the final product. Moreover, when the above-mentioned heating and firing is performed while applying a load at a pressure of 2 to 501/-, a carbon plate having extremely high strength, uniform thickness, and flatness can be obtained.

(発明の効果) 本発明により IJブ付炭素電極の生産性が向上すると
共に、方向性の少ない、均一で平坦な炭素電極が容易に
得られるようになった。また、原料繊維の太さの選択、
配合及びプレス処理の調整によシ、燃料電池用の゛電極
基材として使用する場°合に特に問題になる板の孔径や
気孔率を自由にかつ容易にコントロールすることが可能
になった。
(Effects of the Invention) According to the present invention, the productivity of carbon electrodes with IJ buttons has been improved, and it has become possible to easily obtain uniform and flat carbon electrodes with little directionality. In addition, selection of the thickness of raw material fiber,
By adjusting the formulation and press treatment, it has become possible to freely and easily control the pore size and porosity of the plate, which is a particular problem when used as an electrode base material for fuel cells.

(実施例) 本発明をいっそう理解しやすくするために、以下に実施
例を示すが、下記の実施例は本発明を制限するものでは
ない。
(Examples) In order to make the present invention easier to understand, Examples are shown below, but the following Examples do not limit the present invention.

なお、実施例中、部および%とあるのはそれぞれ重量部
および重量%である。
In addition, parts and % in the examples are parts by weight and % by weight, respectively.

実施例1〜3 太さ3デニール、長さ5餌のポリアクリロニトリル繊維
、ピッチ繊維、カナディアンフリーネス500m+++
のノぐルゾ(NUKP)、ポリビニルアtvコールM維
(り5 Vg、VP B 105−2X 3)を第1表
の割合で水を加えてスラリーを得、丸網式抄紙機で常法
によシ坪量で200 f/−のシートを抄造した。この
シートをフェノール樹脂(住友デュレズ製PR−514
04)40%水溶液に含浸しくフェノール樹脂付N量1
00%/シー))105℃の温度で乾燥した。
Examples 1 to 3 Polyacrylonitrile fiber with a thickness of 3 denier and a length of 5 baits, pitch fiber, Canadian freeness 500 m +++
Add water to Noguruzo (NUKP) and polyvinyla tvcol M fiber (Ri5 Vg, VP B 105-2X 3) in the proportions shown in Table 1 to obtain a slurry, and process using a circular wire paper machine in a conventional manner. A sheet with a basis weight of 200 f/- was made. This sheet was coated with phenol resin (PR-514 manufactured by Sumitomo Durez).
04) N amount 1 with phenol resin impregnated in 40% aqueous solution
00%/c)) was dried at a temperature of 105°C.

次いで第1表に示した枚数を縦、横又互に積層し、プレ
ス厚さ2.5mになるように加圧し、同時に180℃、
15分間加熱地理を行った。
Next, the number of sheets shown in Table 1 were stacked vertically, horizontally, and alternately, pressed to a thickness of 2.5 m, and simultaneously heated at 180°C.
Heating geography was performed for 15 minutes.

次いで得られたプレス成形のシートをメタルンーで切削
加工を行ない2.4■巾X 1.75■高さの溝を2.
4 m間隔でシートの片面に設けた。
Next, the obtained press-formed sheet was cut with a metal tool to form a groove of 2.4 cm wide x 1.75 cm high.
They were placed on one side of the sheet at 4 m intervals.

切削加工シートを220℃で、4時間、空気中で加熱不
融化処理全行なった後、1000℃のチッ素ガス雰囲気
炉で1時間、7f/−の荷重圧力下で加熱炭化を行なっ
た。均一で、層間剥離のない平坦性の良好で、リプ形態
の良好なリブ付多孔買炭素電極が得られた。結果を第1
ffに示す。
The cut sheet was heated and infusible in air at 220° C. for 4 hours, and then heated and carbonized in a nitrogen gas atmosphere furnace at 1000° C. for 1 hour under a load pressure of 7 f/−. A ribbed porous carbon electrode was obtained which was uniform, had good flatness without delamination, and had a good lip shape. Results first
It is shown in ff.

第 1 表 注1)孔径、気孔率は、水銀圧入法によシ測足、した。Table 1 Note 1) Pore diameter and porosity were measured by mercury intrusion method.

注2)抵抗はホイートストンブリッジ法によシ測定した
Note 2) Resistance was measured using the Wheatstone bridge method.

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

第1図は本発明のリプ付き多孔質炭素電極゛の断面図を
示す。 図面中の番号はそれぞれ次のものを表わす。 1、・・リプ部 2・・・蒋部 出 願 人 王子製紙株式会社 代理人 弁理士 井 坂 實 夫 第1図
FIG. 1 shows a sectional view of the lipped porous carbon electrode of the present invention. The numbers in the drawings represent the following, respectively. 1.Reply Department 2.Applicant: Oji Paper Co., Ltd. Agent: Patent Attorney Minoru Isaka Figure 1

Claims (1)

【特許請求の範囲】 1)炭素繊維製造用有機繊維および炭素繊維から選ばれ
た少なくとも一柚の繊維60−951蓋%とパルプおよ
びまたは抄紙用バインダー40〜51量%からなる混合
物を抄紙して得られたシードに有愼高分子wJ買の浴液
を含浸して含浸シートを得、該含浸シートを加熱プレス
して成形および硬化を行ない、次いで切削加工を行ない
、心安に応じて不融化処理を行なった後、不活性ガス柊
囲気中で800℃以上の温度で加熱炭化させることを%
徴とするリブ付多孔貴炭素14L極の製造方法。 2)含浸シートを核層して那熱プレス処理を行なう特許
請求の範囲第1項に記載のリブ付多孔質炭素電極の製造
方法。 3)刀0熱炭化を2〜50t/−の荷亘加圧下で行なう
特許請求の範囲第1項または第2項に記載のリブ付多孔
質炭素amの製造方法。
[Scope of Claims] 1) Making paper from a mixture consisting of 60-951% by weight of at least 100% fibers selected from organic fibers for producing carbon fibers and carbon fibers, and 40-51% by weight of pulp and/or binder for papermaking. The obtained seeds are impregnated with a bath liquid prepared by Yuripolymer WJ to obtain an impregnated sheet, which is heated and pressed to form and harden.Then, cutting is performed, and if necessary, infusible treatment is performed. After that, heat carbonization at a temperature of 800℃ or higher in an inert gas atmosphere.
A method for manufacturing a porous noble carbon 14L pole with ribs. 2) The method for manufacturing a ribbed porous carbon electrode according to claim 1, wherein an impregnated sheet is used as a core layer and thermal press treatment is performed. 3) The method for producing a ribbed porous carbon according to claim 1 or 2, wherein the carbonization is carried out under a load and pressure of 2 to 50 t/-.
JP59021813A 1984-02-10 1984-02-10 Manufacture of porous carbon electrode with rib Pending JPS60167271A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59021813A JPS60167271A (en) 1984-02-10 1984-02-10 Manufacture of porous carbon electrode with rib

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59021813A JPS60167271A (en) 1984-02-10 1984-02-10 Manufacture of porous carbon electrode with rib

Publications (1)

Publication Number Publication Date
JPS60167271A true JPS60167271A (en) 1985-08-30

Family

ID=12065497

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59021813A Pending JPS60167271A (en) 1984-02-10 1984-02-10 Manufacture of porous carbon electrode with rib

Country Status (1)

Country Link
JP (1) JPS60167271A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5932185A (en) * 1993-08-23 1999-08-03 The Regents Of The University Of California Method for making thin carbon foam electrodes
KR101468866B1 (en) * 2012-07-17 2014-12-04 한국에너지기술연구원 Method for preparing carbon paper for fuel cell, the carbon paper prepared using the method and fuel cell comprising the carbon paper

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5932185A (en) * 1993-08-23 1999-08-03 The Regents Of The University Of California Method for making thin carbon foam electrodes
KR101468866B1 (en) * 2012-07-17 2014-12-04 한국에너지기술연구원 Method for preparing carbon paper for fuel cell, the carbon paper prepared using the method and fuel cell comprising the carbon paper

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