JPH08283084A - Production of porous carbon plate - Google Patents

Production of porous carbon plate

Info

Publication number
JPH08283084A
JPH08283084A JP7083798A JP8379895A JPH08283084A JP H08283084 A JPH08283084 A JP H08283084A JP 7083798 A JP7083798 A JP 7083798A JP 8379895 A JP8379895 A JP 8379895A JP H08283084 A JPH08283084 A JP H08283084A
Authority
JP
Japan
Prior art keywords
sheet
impregnated
sheets
papermaking
porous carbon
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
JP7083798A
Other languages
Japanese (ja)
Inventor
Osamu Iwaki
修 岩城
Shiyouji Hamu
昇次 羽牟
Tatsuhiro Kaneda
竜大 金田
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
New 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 New Oji Paper Co Ltd filed Critical New Oji Paper Co Ltd
Priority to JP7083798A priority Critical patent/JPH08283084A/en
Publication of JPH08283084A publication Critical patent/JPH08283084A/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
    • C04B38/00Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof
    • C04B38/0022Porous mortars, concrete, artificial stone or ceramic ware; Preparation thereof obtained by a chemical conversion or reaction other than those relating to the setting or hardening of cement-like material or to the formation of a sol or a gel, e.g. by carbonising or pyrolysing preformed cellular materials based on polymers, organo-metallic or organo-silicon precursors
    • 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
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/00612Uses not provided for elsewhere in C04B2111/00 as one or more layers of a layered structure

Abstract

PURPOSE: To obtain a production method by which a porous carbon plate having a pore size gradient excellent in phosphoric acid electrolyte retention properties and gas permeability can be produced at a low cost through using a conventional paper-making method and an impregnation method. CONSTITUTION: In this production, at least two paperlike felted sheets having different bulk density from each other within the range of 0.1 to 0.5g/cm<3> are formed by using a mixture of 20 to 95 pts.wt. of organic fiber for producing carbon fiber and 5 to 80 pts.wt. of pulp. Then, these paperlike felled sheets are impregnated with an organic polymer material solution and thereafter, dried to form dried impregnated sheets. Subsequently, with the impregnated sheet formed from the felled sheet having the lowest bulk density and the impregnated sheet formed from the felled sheet having the highest bulk density as the outermost layers, the impregnated sheets are laminated in order of bulk density of the felted sheets from which they are formed, from lower to higher to form a laminate. The resulting laminate is successively subjected to hot-press treatment, oxidation treatment in air and heating and carbonization treatment in an inert gas atmosphere at >=800 deg.C to produce the objective porous carbon plate.

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、多孔質炭素板の新規な
製造方法に関するものである。更に詳しく述べると、炭
素繊維製造用有機繊維およびパルプを混合し、抄紙した
抄紙シートから含浸シートを得、緊度の最も小さい抄紙
シートから得た含浸シート上に、緊度の大きい抄紙シー
トから得た含浸シートを順次積層し、熱プレス処理後、
炭化処理することにより、耐薬品性、電気伝導性、ガス
透過性および強度の優れた嵩高な厚手の多孔質炭素板で
あって、厚さ方向に気孔径が変化する多孔質炭素板を製
造する方法に関するものである。
FIELD OF THE INVENTION The present invention relates to a novel method for producing a porous carbon plate. More specifically, the organic fiber for producing carbon fiber and pulp are mixed to obtain an impregnated sheet from a papermaking sheet that is paper-made. The impregnated sheets are sequentially laminated, and after hot press treatment,
By carbonizing, a bulky and thick porous carbon plate having excellent chemical resistance, electrical conductivity, gas permeability and strength, in which the pore diameter changes in the thickness direction, is produced. It is about the method.

【0002】[0002]

【従来の技術】従来、気孔径勾配をもつ多孔質炭素板を
得る方法としては、特開昭59−46763号公報に粗
密の2層構造をもたせるため、焼成後に粗または密にな
る2種類のシートを、焼成前に粗なシートおよび密なシ
ートの2枚を積層し、プレス成形した後、焼成した2層
構造をもつ多孔質炭素板が知られている。本発明者ら
は、特開昭61−195875号公報で湿式抄紙法によ
る方法を開示したが、この方法では2層構造の多孔質板
しか得られず、充分なりん酸電解液保持性およびガス透
過性があり、軽量で、曲げ強度の高い多孔質炭素板は得
られなかった。
2. Description of the Related Art Conventionally, as a method for obtaining a porous carbon plate having a pore diameter gradient, there are two types of coarse or dense after firing because a coarse and dense two-layer structure is provided in JP-A-59-46763. There is known a porous carbon plate having a two-layer structure in which two sheets, a rough sheet and a dense sheet, are laminated before firing, press-formed, and fired. The present inventors disclosed a method by a wet papermaking method in Japanese Patent Laid-Open No. 61-195875, but this method can only obtain a porous plate having a two-layer structure, and has sufficient phosphoric acid electrolyte retention and gas. It was not possible to obtain a porous carbon plate that is permeable, lightweight and has high bending strength.

【0003】[0003]

【発明が解決しようとする課題】本発明は、上記の欠点
であるりん酸電解液保持性やガス透過性を改良すると共
に、気孔径勾配を付与した多孔質炭素板が、通常用いら
れる抄紙法によるシート化設備および含浸法による含浸
シート化設備を用い、電気伝導性が高く、耐薬品性に優
れた高品質の多孔質炭素板を安価に製造方法を提供する
ことを目的とする。
DISCLOSURE OF THE INVENTION The present invention improves the phosphoric acid electrolyte retention and gas permeability which are the above-mentioned drawbacks, and at the same time, a porous carbon plate having a pore diameter gradient is usually used in a papermaking method. An object of the present invention is to provide a method for inexpensively producing a high-quality porous carbon plate having high electric conductivity and excellent chemical resistance by using the sheet forming equipment according to the above and the impregnating sheet forming equipment according to the impregnation method.

【0004】[0004]

【課題を解決するための手段】本発明は、繊度が0.0
1〜30デニールおよび繊維長が0.2〜15mmの炭
素繊維製造用有機繊維20〜95重量部、およびパルプ
5〜80重量部を用いて緊度0.1〜0.5g/cm3
の範囲で、緊度の異なる抄紙シートを少なくとも二種類
作成する工程、該抄紙シートを有機高分子物質の溶液を
含浸し、乾燥した含浸シートを作成する工程、緊度の最
も小さい抄紙シートより作成した含浸シートと、緊度の
最も大きい抄紙シートより作成した含浸シートとの間
に、抄紙シートの緊度の小さい順に含浸シートを積層
し、積層シートを作成する工程、該積層シートを熱プレ
ス処理後、空気中で酸化処理して前駆体シートを作成す
る工程、および該前駆体シートを不活性ガス雰囲気中で
800℃以上の温度で加熱炭化処理させる工程、を含ん
で成ることを特徴とする多孔質炭素板の製造方法によっ
て達成される。
The present invention has a fineness of 0.0
Using 1 to 30 denier and 20 to 95 parts by weight of organic fibers for producing carbon fibers having a fiber length of 0.2 to 15 mm, and 5 to 80 parts by weight of pulp, a tightness of 0.1 to 0.5 g / cm 3
In the range of, at least two types of papermaking sheets having different tenacity, a step of impregnating the papermaking sheet with a solution of an organic polymer substance, a step of producing a dried impregnated sheet, and a papermaking sheet having the lowest tenacity Between the impregnated sheet and the impregnated sheet prepared from the papermaking sheet having the highest tenacity, a step of laminating the impregnated sheets in the order of decreasing paperboard tenacity to prepare a laminated sheet, and subjecting the laminated sheet to a hot press treatment. After that, the method is characterized by including a step of forming a precursor sheet by oxidizing in air, and a step of heating and carbonizing the precursor sheet at a temperature of 800 ° C. or higher in an inert gas atmosphere. This is achieved by the method for manufacturing a porous carbon plate.

【0005】本発明に用いる炭素繊維製造用有機繊維と
しては、通常のレーヨン繊維、ピッチ繊維、リグニン繊
維、フェノール樹脂繊維、アクリル繊維等通常炭素繊維
を製造する場合に原料として使用される有機繊維であっ
て、繊度が0.01〜30デニール、好ましくは0.1
〜15デニールであり、かつ繊維長さが0.2〜15m
m、好ましくは0.5〜5mmであるものを目標の緊度
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。
The organic fibers for producing carbon fibers used in the present invention include ordinary rayon fibers, pitch fibers, lignin fibers, phenol resin fibers, acrylic fibers, and other organic fibers used as a raw material when producing ordinary carbon fibers. And has a fineness of 0.01 to 30 denier, preferably 0.1
~ 15 denier and 0.2 ~ 15 m fiber length
m, preferably 0.5 to 5 mm, is selected according to the target tightness and used alone or in combination of two or more.

【0006】抄紙シートの形成には、炭素繊維製造用有
機繊維60〜95重量部およびパルプ5〜40重量部を
混合した紙料を用いて、手抄き、丸網、長網、傾斜ワイ
ヤ等通常の湿式抄紙方法が使用出来、地合の良い抄紙シ
ートを得るには抄紙濃度を低くすれば良い。金網で脱水
した後の強度が弱く、湿紙シート切れが起きるときは、
叩解を進めた天然パルプを加えれば、強度が上がり、湿
紙シート切れが防止出来る。また通常、湿紙抄紙工程で
脱水プレス処理を行なうが、脱水プレス処理を行わなく
てもよい。
For the formation of a papermaking sheet, a paper stock obtained by mixing 60 to 95 parts by weight of organic fibers for producing carbon fibers and 5 to 40 parts by weight of pulp is used to make paper, circular nets, Fourdrinier, slanted wires, etc. An ordinary wet papermaking method can be used, and the papermaking concentration may be lowered to obtain a papermaking sheet having a good texture. When the strength of the wet paper sheet is weak after dehydration with a wire mesh,
By adding beaten natural pulp, strength is increased and wet paper sheet breakage can be prevented. Further, usually, the dewatering press treatment is performed in the wet papermaking process, but the dewatering press treatment may not be performed.

【0007】通常の湿式抄紙機で使われている多筒式、
ヤンキー式のようなシリンダー型ドライヤー以外に、バ
ンドドライヤー、ハニカムドライヤーのような熱風式ド
ライヤーや、赤外線式ドライヤー等が使用可能である。
熱風式ドライヤーまたは赤外線式ドライヤーを使用する
場合では、抄紙シートが嵩高になり、緊度の小さい抄紙
シートが得られる。
The multi-cylinder type used in ordinary wet paper machines,
In addition to the cylinder type dryer such as the Yankee type, a hot air type dryer such as a band dryer and a honeycomb dryer, an infrared type dryer and the like can be used.
When a hot-air dryer or an infrared dryer is used, the papermaking sheet becomes bulky and a papermaking sheet with low tenacity is obtained.

【0008】抄紙の際、湿紙の引張り強度は弱い場合に
は、必要に応じカンバスまたはフェルトを用いるのが好
ましい。
In the case of papermaking, when the tensile strength of the wet paper is weak, it is preferable to use a canvas or felt if necessary.

【0009】抄紙シートに含浸させ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、フラン樹脂、ポリジビニルベンゼン
のような熱硬化性樹脂、または塩化ビニル樹脂、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、アクリル樹脂のような熱可塑性樹脂、またはリグニ
ン、ピッチまたはタールのようなものが使用される。
Examples of the organic polymer substance to be impregnated in the papermaking sheet include phenol resin, epoxy resin, unsaturated polyester resin, furan resin, thermosetting resin such as polydivinylbenzene, vinyl chloride resin, vinylidene chloride resin, Thermoplastic resins such as vinyl fluoride resin, vinylidene fluoride resin, acrylic resin, or such as lignin, pitch or tar are used.

【0010】これらの有機高分子物質の好ましい性質と
しては、有機溶剤に溶解するかまたは熱処理時の高温で
融解すること、および炭素含有量が30重量%以上であ
って、炭化後、炭素質バインダーとして炭素繊維内の結
合に寄与するものであり、熱硬化性樹脂が好ましい。
The preferred properties of these organic polymeric substances are that they dissolve in an organic solvent or melt at a high temperature during heat treatment, and that they have a carbon content of 30% by weight or more, and have a carbonaceous binder after carbonization. As it contributes to the bond in the carbon fiber, a thermosetting resin is preferable.

【0011】前記の有機高分子物質の溶液または分散液
を使用して、抄紙シートを含浸処理し、含浸シートを得
る。抄紙シートに付着する含浸量が少なすぎると、バイ
ンダー効果、および炭化の際の炭化収率が劣り、あまり
過剰になると目づまりのため、気孔率の調整が困難とな
り、かつ多孔質炭素板が脆くなる。好ましい含浸付着量
としては、抄紙シートの重量の20〜160重量%であ
る。
A papermaking sheet is impregnated with the solution or dispersion of the above organic polymer to obtain an impregnated sheet. If the amount of impregnation adhered to the papermaking sheet is too small, the binder effect and the carbonization yield during carbonization will be poor, and if it is too much, it will cause clogging, making it difficult to adjust the porosity and making the porous carbon plate brittle. . The preferable impregnated adhesion amount is 20 to 160% by weight of the weight of the papermaking sheet.

【0012】本発明により得られる気孔径は、例えば繊
度が0.1デニールの有機繊維を80重量%、天然パル
プを20重量%配合した抄紙シート単独で得た多孔質炭
素板では、約8μmであり、繊度が3デニールの有機繊
維を80重量%、天然パルプを20重量%配合した抄紙
シート単独で得た多孔質炭素板では、約27μmであ
り、繊度が10デニールの有機繊維を80重量%、天然
パルプを20重量%配合した抄紙シート単独で得た多孔
質炭素板では、約50μmである。
The pore diameter obtained by the present invention is, for example, about 8 μm in the case of a porous carbon plate obtained from a papermaking sheet alone containing 80% by weight of an organic fiber having a fineness of 0.1 denier and 20% by weight of a natural pulp. A porous carbon plate obtained by using a papermaking sheet alone containing 80% by weight of an organic fiber having a fineness of 3 denier and 20% by weight of a natural pulp has a thickness of about 27 μm and 80% by weight of an organic fiber having a fineness of 10 denier. With a porous carbon plate obtained by using a papermaking sheet alone containing 20% by weight of natural pulp, the thickness is about 50 μm.

【0013】多孔質炭素板の厚み方向の気孔径勾配を付
与するには、緊度の最も小さい抄紙シートより作成した
含浸シートと、緊度の最も大きい抄紙シートより作成し
た含浸シートとの間に、抄紙シートの緊度の小さい順に
含浸シートを積層し、積層シートを作成し、熱プレス
後、空気中で酸化処理し、不活性ガス雰囲気中で加熱炭
化処理を行ない、気孔径勾配のある多孔質炭素板を得
る。
In order to impart a pore diameter gradient in the thickness direction of the porous carbon plate, an impregnated sheet made from the papermaking sheet having the lowest tenacity and an impregnated sheet made from the papermaking sheet having the highest tenacity are provided. , Laminating impregnated sheets in ascending order of papermaking sheet, make a laminated sheet, heat press, oxidize in air, heat carbonize in an inert gas atmosphere, and perforate with pore diameter gradient. Quality carbon plate.

【0014】前記熱プレス処理は、多孔質炭素板に所定
の厚さ、形状、密度および厚さ方向の気孔径勾配を付与
するために行う。
The hot press treatment is carried out in order to impart a predetermined thickness, shape, density and pore diameter gradient in the thickness direction to the porous carbon plate.

【0015】以上のようにして得た多孔質炭素板におい
て、緊度の最も小さい抄紙シートから得た側は、気孔径
が大きく、緊度の最も大きい抄紙シートから得た側は、
気孔径が小さくなり、多孔質炭素板の厚み方向に気孔径
勾配を付与する。
In the porous carbon plate obtained as described above, the side obtained from the papermaking sheet having the smallest tenacity has the large pore diameter and the side obtained from the papermaking sheet having the greatest tenacity is
The pore diameter becomes smaller, and a pore diameter gradient is given in the thickness direction of the porous carbon plate.

【0016】前記多孔質炭素板の気孔径の大きい側は、
ガス透過性が良好であり、気孔径の小さい側は、リン酸
電解液保持性が良好となり、炭素電極としてセパレータ
ー側に使用するのに適する。
The side of the porous carbon plate with the larger pore diameter is
The gas permeability is good, and the smaller pore size side has better phosphoric acid electrolyte retention, and is suitable for use as a carbon electrode on the separator side.

【0017】熱プレスおよび加熱炭化処理により、多孔
質炭素板の厚みを一定に保持すると同時に平坦な多孔質
炭素板を得ることが可能になった。またプレス圧力、ま
たはプレス時のスペーサーの厚さを調整することによ
り、多孔質炭素板全体の厚さ、気孔径を任意に変えるこ
とが可能である。
By the hot pressing and heat carbonization treatment, it became possible to keep the thickness of the porous carbon plate constant and at the same time obtain a flat porous carbon plate. Further, by adjusting the pressing pressure or the thickness of the spacer at the time of pressing, it is possible to arbitrarily change the thickness and the pore diameter of the entire porous carbon plate.

【0018】熱プレス処理での加熱条件としては、15
0〜220℃、1〜60分間が好ましい。前記熱プレス
処理を行った積層シートは、炭化収率、黒鉛化率を向上
させるため空気中で酸化処理を行った後、不活性ガス雰
囲気中で、800℃以上の温度で炭化処理されて本発明
の多孔質炭素板が得られる。
The heating conditions in the hot press treatment are 15
0-220 degreeC and 1-60 minutes are preferable. The laminated sheet that has been subjected to the hot press treatment is subjected to an oxidation treatment in air to improve the carbonization yield and the graphitization rate, and then carbonized at a temperature of 800 ° C. or higher in an inert gas atmosphere. The porous carbon plate of the invention is obtained.

【0019】ここで前記酸化処理は、熱プレス工程後に
行うが、その酸化処理条件は、特に限定されないが、1
50〜350℃、10分〜20時間、空気中で処理する
ことが適当である。
Here, the oxidation treatment is performed after the hot pressing step, but the conditions of the oxidation treatment are not particularly limited.
It is suitable to treat in air at 50 to 350 ° C. for 10 minutes to 20 hours.

【0020】[0020]

【実施例】実施例により本発明の構成および効果をさら
に説明するが、もちろん本発明はこれらの態様に制限さ
れるものではない。なお、実施例中、部とあるのは重量
部を表す。また多孔質炭素板の見掛け密度は、炭素板を
表面研磨して測定し、深さ方向の気孔径は、水銀ポロシ
メーターを用いて測定した。また曲げ試験は、3点曲げ
試験法により測定した。
EXAMPLES The constitution and effects of the present invention will be further described with reference to examples, but of course the present invention is not limited to these modes. In the examples, "parts" means "parts by weight". The apparent density of the porous carbon plate was measured by polishing the surface of the carbon plate, and the pore size in the depth direction was measured using a mercury porosimeter. Further, the bending test was measured by a three-point bending test method.

【0021】実施例 繊度10デニールおよび繊維長3mmのポリアクリロニ
トリル繊維を80部、針葉樹晒クラフトパルプをカナデ
ィアンフリーネス250mlに叩解したものを20部よ
りなるスラリーを得、250mm角の手抄きマシンで常
法により坪量200g/m2、緊度0.18g/cm3
抄紙シートを抄造し、この抄紙シートをフェノール樹脂
(商標:KP743 荒川化学工業社製)で、抄紙シー
ト当りの付着量が50%となるように含浸し、これを含
浸シートAとする。
EXAMPLE A slurry consisting of 80 parts of polyacrylonitrile fiber having a fineness of 10 denier and a fiber length of 3 mm and beaten conifer bleached kraft pulp to a Canadian freeness of 250 ml to obtain 20 parts of slurry was prepared with a 250 mm square hand-making machine. A papermaking sheet having a basis weight of 200 g / m 2 and a tenacity of 0.18 g / cm 3 is made by a method, and the papermaking sheet is made of a phenol resin (trademark: KP743 manufactured by Arakawa Chemical Industry Co., Ltd.), and the adhesion amount per papermaking sheet is 50. The impregnated sheet A is impregnated so that the content becomes%.

【0022】繊度5デニールおよび繊維長3mmのポリ
アクリロニトリル繊維を80部、針葉樹晒クラフトパル
プをカナディアンフリーネス250mlに叩解したもの
を20部よりなるスラリーを得、250mm角の手抄き
マシンで常法により坪量200g/m2、緊度0.20
g/cm3の抄紙シートを抄造し、この抄紙シートをフ
ェノール樹脂(商標:KP743 荒川化学工業社製)
で、抄紙シート当りの付着量が50%となるように含浸
し、これを含浸シートBとする。
A slurry comprising 80 parts of polyacrylonitrile fiber having a fineness of 5 denier and a fiber length of 3 mm and beaten conifer bleached kraft pulp to 250 ml of Canadian freeness to obtain 20 parts of slurry was prepared by a conventional method with a 250 mm square hand-making machine. Basis weight 200g / m 2 , tenacity 0.20
A papermaking sheet of g / cm 3 is produced, and the papermaking sheet is phenolic resin (trademark: KP743 manufactured by Arakawa Chemical Industry Co., Ltd.)
Then, impregnation is performed so that the amount of adhesion per paper making sheet becomes 50%, and this is used as impregnation sheet B.

【0023】繊度3デニールおよび繊維長3mmのポリ
アクリロニトリル繊維を80部、針葉樹晒クラフトパル
プをカナディアンフリーネス250mlに叩解したもの
を20部よりなるスラリーを得、250mm角の手抄き
マシンで常法により坪量200g/m2、緊度0.22
g/cm3の抄紙シートを抄造し、この抄紙シートをフ
ェノール樹脂(商標:KP743 荒川化学工業社製)
で、抄紙シート当りの付着量が50%となるように含浸
し、これを含浸シートCとする。
A slurry consisting of 80 parts of polyacrylonitrile fiber having a fineness of 3 denier and a fiber length of 3 mm and 20 parts of bleached softwood kraft pulp with a Canadian freeness of 20 ml was obtained by a conventional method with a 250 mm square hand-making machine. Basis weight 200g / m 2 , tenacity 0.22
A papermaking sheet of g / cm 3 is produced, and the papermaking sheet is phenolic resin (trademark: KP743 manufactured by Arakawa Chemical Industry Co., Ltd.)
Then, impregnation is performed so that the amount of adhesion per paper making sheet is 50%, and this is referred to as impregnation sheet C.

【0024】繊度0.5デニールおよび繊維長3mmの
ポリアクリロニトリル繊維を80部、針葉樹晒クラフト
パルプをカナディアンフリーネス250mlに叩解した
ものを20部よりなるスラリーを得、250mm角の手
抄きマシンで常法により坪量200g/m2、緊度0.
25g/cm3の抄紙シートを抄造し、この抄紙シート
をフェノール樹脂(商標:KP743 荒川化学工業社
製)で、抄紙シート当りの付着量が50%となるように
含浸し、これを含浸シートDとする。
A slurry consisting of 80 parts of polyacrylonitrile fiber having a fineness of 0.5 denier and a fiber length of 3 mm and beaten conifer bleached kraft pulp to 250 ml of Canadian freeness to obtain 20 parts of slurry was prepared with a 250 mm square hand-making machine. According to the method, the basis weight is 200 g / m 2 , the tenacity is 0.
A 25 g / cm 3 papermaking sheet is made into paper, and the papermaking sheet is impregnated with a phenolic resin (trademark: KP743 manufactured by Arakawa Chemical Industry Co., Ltd.) so that the adhered amount per papermaking sheet is 50%. And

【0025】含浸シートAを4枚、その上に含浸シート
Bを4枚、その上に含浸シートCを4枚、その上に含浸
シートDを4枚順次重ね合わせ、積層シートを作成し、
180℃、15分間熱プレスし、次いで220℃、4時
間、空気中で酸化処理を行い前駆体シートを作成し、1
000℃の窒素ガス雰囲気中で1時間、黒鉛化炭素板に
挟んで加熱し、さらにアルゴンガス雰囲気中で、温度2
800℃、30分間黒鉛化処理を行って、多孔質炭素板
を得た。
Four sheets of the impregnated sheet A, four sheets of the impregnated sheet B, four sheets of the impregnated sheet C, and four sheets of the impregnated sheet D are sequentially laminated on each other to form a laminated sheet,
Heat-press at 180 ° C. for 15 minutes, then oxidize at 220 ° C. for 4 hours in air to prepare a precursor sheet.
It is sandwiched between graphitized carbon plates in a nitrogen gas atmosphere at 000 ° C. for 1 hour and heated, and then in an argon gas atmosphere, the temperature is set to 2
Graphitization was performed at 800 ° C. for 30 minutes to obtain a porous carbon plate.

【0026】比較例1 含浸シートAを16枚順次重ね合わせ、積層シートを作
成し、次いで実施例1と同様条件で酸化処理および黒鉛
化処理を行って多孔質炭素板を得た。
Comparative Example 1 16 sheets of impregnated sheets A were sequentially laminated to form a laminated sheet, and then subjected to oxidation treatment and graphitization treatment under the same conditions as in Example 1 to obtain a porous carbon plate.

【0027】比較例2 含浸シートCを16枚順次重ね合わせ、積層シートを作
成し、次いで実施例1と同様条件で酸化処理および黒鉛
化処理を行って多孔質炭素板を得た。
Comparative Example 2 Sixteen impregnated sheets C were sequentially laminated to form a laminated sheet, and then oxidation treatment and graphitization treatment were performed under the same conditions as in Example 1 to obtain a porous carbon plate.

【0028】[0028]

【表1】 [Table 1]

【0029】[0029]

【発明の効果】本発明は、気孔径勾配を有する多孔質炭
素板を、通常用いられる抄紙法によるシート化設備、お
よび含浸法による含浸シート化設備を用い、電気伝導性
が高く、耐薬品性に優れた高品質の多孔質炭素板を安価
に製造することが可能となり、本発明に係る多孔質炭素
板は、気孔径勾配を付与しても見掛け密度や曲げ強度が
変わらず、気孔径の大きい部分でのリン酸電解液を多量
に含有することが出来、かつガス透過性が良好であり、
また気孔径の小さい部分でのリン酸電解液の保持性能が
大きく、燃料電池用電極として有効なものである。
INDUSTRIAL APPLICABILITY The present invention uses a porous carbon plate having a pore diameter gradient with sheeting equipment by a papermaking method and an impregnation sheeting equipment by an impregnation method which are commonly used, and has high electric conductivity and chemical resistance. It becomes possible to inexpensively produce an excellent high-quality porous carbon plate, the porous carbon plate according to the present invention does not change the apparent density and bending strength even if a pore diameter gradient is applied, Can contain a large amount of phosphoric acid electrolyte in a large portion, and has good gas permeability,
Further, the phosphoric acid electrolyte retainability is large in the portion having a small pore diameter, which is effective as a fuel cell electrode.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 繊度が0.01〜30デニールおよび繊
維長が0.2〜15mmの炭素繊維製造用有機繊維20
〜95重量部、およびパルプ5〜80重量部を用いて、
緊度0.1〜0.5g/cm3の範囲で、緊度の異なる
抄紙シートを少なくとも二種類作成する工程、 該抄紙シートを有機高分子物質の溶液を含浸し、乾燥し
た含浸シートを作成する工程、 緊度の最も小さい抄紙シートより作成した含浸シート
と、緊度の最も大きい抄紙シートより作成した含浸シー
トとの間に、抄紙シートの緊度の小さい順に含浸シート
を積層し、積層シートを作成する工程、 該積層シートを熱プレス処理後、空気中で酸化処理して
前駆体シートを作成する工程、および該前駆体シートを
不活性ガス雰囲気中で800℃以上の温度で加熱炭化処
理させる工程、を含んで成ることを特徴とする多孔質炭
素板の製造方法。
1. An organic fiber 20 for producing a carbon fiber having a fineness of 0.01 to 30 denier and a fiber length of 0.2 to 15 mm.
~ 95 parts by weight, and 5-80 parts by weight of pulp,
A step of producing at least two kinds of papermaking sheets having different tenacity within a range of the tenacity of 0.1 to 0.5 g / cm 3 , and impregnating the papermaking sheet with a solution of an organic polymer substance to prepare a dried impregnated sheet The laminated sheet is formed by stacking the impregnated sheet made from the papermaking sheet with the lowest tenacity and the impregnated sheet made from the papermaking sheet with the highest tenacity, in the order of the tightest papermaking sheet. A step of producing a precursor sheet by subjecting the laminated sheet to a hot press treatment and then an oxidizing treatment in air, and a heating carbonization treatment of the precursor sheet at a temperature of 800 ° C. or higher in an inert gas atmosphere. A method of manufacturing a porous carbon plate, comprising:
JP7083798A 1995-04-10 1995-04-10 Production of porous carbon plate Pending JPH08283084A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7083798A JPH08283084A (en) 1995-04-10 1995-04-10 Production of porous carbon plate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7083798A JPH08283084A (en) 1995-04-10 1995-04-10 Production of porous carbon plate

Publications (1)

Publication Number Publication Date
JPH08283084A true JPH08283084A (en) 1996-10-29

Family

ID=13812680

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7083798A Pending JPH08283084A (en) 1995-04-10 1995-04-10 Production of porous carbon plate

Country Status (1)

Country Link
JP (1) JPH08283084A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003087470A1 (en) * 2002-04-17 2003-10-23 Mitsubishi Rayon Co., Ltd. Carbon fiber paper and porous carbon electrode substrate for fuel cell therefrom

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7510626B2 (en) 2001-10-09 2009-03-31 Mitsubishi Rayon Co., Ltd. Carbon fiber paper and porous carbon electrode substrate for fuel cell therefrom
WO2003087470A1 (en) * 2002-04-17 2003-10-23 Mitsubishi Rayon Co., Ltd. Carbon fiber paper and porous carbon electrode substrate for fuel cell therefrom

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