JPH0848577A - Production of impermeable carbonaceous formed body - Google Patents

Production of impermeable carbonaceous formed body

Info

Publication number
JPH0848577A
JPH0848577A JP6187433A JP18743394A JPH0848577A JP H0848577 A JPH0848577 A JP H0848577A JP 6187433 A JP6187433 A JP 6187433A JP 18743394 A JP18743394 A JP 18743394A JP H0848577 A JPH0848577 A JP H0848577A
Authority
JP
Japan
Prior art keywords
resin
carbonaceous
thermoplastic resin
molding
pulp
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
JP6187433A
Other languages
Japanese (ja)
Inventor
Shigeru Murakami
繁 村上
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko KK
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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP6187433A priority Critical patent/JPH0848577A/en
Publication of JPH0848577A publication Critical patent/JPH0848577A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

  • Fuel Cell (AREA)
  • Ceramic Products (AREA)

Abstract

PURPOSE:To produce an impermeable carbonaceous formed body having stable quality. CONSTITUTION:A mixed paper making sheet made of a blend of 40-60wt.% pulp with 5-25wt.% carbonaceous powder and 30-50wt.% thermoplastic resin having >=30% rate of residual carbon is heated to a temp. above the m.p. of the resin and press-formed or such sheets are laminated, heated and press- formed. The resultant green formed body is carbonized by firing.

Description

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

【0001】[0001]

【産業上の利用分野】本発明はリン酸型燃料電池のセパ
レータ板等に使用される不浸透炭素質成形体の製造法に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an impervious carbonaceous molding used for a separator plate of a phosphoric acid fuel cell.

【0002】[0002]

【従来の技術】従来、リン酸型燃料電池等に使用される
セパレータ板は、炭素繊維や、パルプ等のセルロース質
繊維を抄紙後、熱硬化性樹脂を含浸し、積層、加熱、加
圧工程を経て炭素化してつくられる(特開昭60−16
114、特開昭62−70215)。
2. Description of the Related Art Conventionally, a separator plate used in a phosphoric acid fuel cell or the like has a carbon fiber or a cellulosic fiber such as pulp made into paper, and then impregnated with a thermosetting resin, followed by lamination, heating and pressurizing steps. Made by carbonization through
114, JP-A-62-70215).

【0003】[0003]

【発明が解決しようとする課題】しかしながら上記抄紙
工程は、均質製品を大量生産できるにもかかわらず、樹
脂含浸工程、積層、加熱、加圧工程を経る際にシート間
の接着性、均一性に問題を生じ易く、又炭素化工程にお
いても反りや、表面模様を生じやすく、これを回避する
ため様々な工夫をしなければならなかった。
However, although the above paper-making process can mass-produce homogeneous products, the adhesiveness and uniformity between the sheets are not improved during the resin impregnation process, lamination, heating, and pressurization process. Problems are likely to occur, and warpage and surface patterns are likely to occur even in the carbonization process, and various measures have to be taken to avoid this.

【0004】一般に不浸透炭素質成形体を作るためのシ
ートは、クラフト紙やリンター紙等と同様に緊度の高い
シートが必要であり、このシートにフェノール樹脂等の
熱硬化性樹脂を含浸させた後、積層、加熱、加圧成形
し、所望のグリーン成形体を得ようとすると以下の点に
注意しなければならない。
Generally, a sheet for making an impervious carbonaceous molded article needs to have a high tenacity as in the case of kraft paper or linter paper, and this sheet is impregnated with a thermosetting resin such as phenol resin. After stacking, heating and pressure molding to obtain a desired green molded body, the following points must be noted.

【0005】積層、加熱、加圧時におけるシート間の
接着性を保持するため、熱硬化性樹脂含浸後の予備加熱
による樹脂硬化の程度を抑制しなければならない。
In order to maintain the adhesiveness between the sheets during lamination, heating, and pressing, the degree of resin curing by preheating after impregnation with the thermosetting resin must be suppressed.

【0006】上記によって熱硬化性樹脂を含浸した
シート(以下プリプレグシートという)は、樹脂の硬化
が進んでおらず、又シートが緊密であるため含浸時に樹
脂の浸透量に不均一が生じ易い。そのためこれを解消す
べく、含浸液を適度な粘度に溶剤で希釈したり、含浸後
プリプレグシートを数日間放置、熟成したり、含浸時の
余剰の樹脂をかき取棒でのかき取りに工夫する等含浸樹
脂の均一性を確保する必要がある。
A sheet impregnated with a thermosetting resin (hereinafter referred to as a prepreg sheet) as described above does not undergo hardening of the resin, and since the sheet is tight, the amount of resin permeation tends to be non-uniform during impregnation. Therefore, in order to eliminate this, devise a method of diluting the impregnating liquid with a solvent to an appropriate viscosity, leaving the prepreg sheet for several days after impregnation and aging, and scraping off the excess resin at the time of impregnation with a scraping rod. It is necessary to ensure the homogeneity of the equal impregnation resin.

【0007】上記プリプレグシートは、長時間放置す
ると揮発分が散逸し、接着性を悪くし、これが次の積
層、加熱、加圧工程に影響を与える。これを回避するた
め、プリプレグシートを冷暗所等で保管する必要があ
る。そして、上記プリプレグシートを炭化焼成する場
合、熱硬化性樹脂の分解、揮散による空隙を生じやす
く、又含浸樹脂の均一性が確保されないと反りや表面模
様が生じやすい。これを避けるには相当長時間をかけて
昇温するなどの工夫が必要であり、歩留りも悪かった。
本発明は品質の安定した不浸透炭素質成形体を安価に効
率よく生産する方法を提供することを目的とするもので
ある。
[0007] When the prepreg sheet is left for a long time, volatile components are dissipated and the adhesiveness is deteriorated, which affects the next lamination, heating and pressing steps. In order to avoid this, it is necessary to store the prepreg sheet in a cool and dark place. When the prepreg sheet is carbonized and fired, voids are likely to be formed due to decomposition and volatilization of the thermosetting resin, and warping and surface patterns are likely to occur unless the uniformity of the impregnated resin is ensured. In order to avoid this, it was necessary to devise such as raising the temperature over a considerably long time, and the yield was also poor.
It is an object of the present invention to provide a method for efficiently producing an impervious carbonaceous molded article of stable quality at low cost.

【0008】[0008]

【課題を解決するための手段】本発明者らは上記事情を
鑑み、常に製品物性の安定した不浸透炭素質成形体を得
るべく、鋭意研究した結果、パルプ/炭素質粉末/熱可
塑性樹脂を配合した混合抄紙シートを用い、熱硬化性樹
脂の含浸工程を省略することによって上記問題を解決す
ることを発明した。
In view of the above circumstances, the inventors of the present invention have earnestly studied in order to obtain an impermeable carbonaceous molding having stable product properties, and as a result, pulp / carbonaceous powder / thermoplastic resin was selected. The inventors have invented that the above-mentioned problems are solved by using a mixed papermaking sheet that has been blended and omitting the step of impregnating a thermosetting resin.

【0009】すなわち、本発明による不浸透炭素質成形
体の製造方法は、40〜60重量%のパルプ、5〜25
重量%の炭素質粉末、30〜50重量%の残炭率30%
以上の熱可塑性樹脂を配合した混合抄紙シートを、前記
熱可塑性樹脂の融点以上の温度に加熱、加圧成形し、又
は前記シートを積層し加熱、加圧成形し、グリーン成形
体となし、焼成炭化することを構成の特徴とする。
That is, the method for producing an impervious carbonaceous molded article according to the present invention is as follows: 40-60 wt% pulp, 5-25
% Carbonaceous powder, 30-50% by weight residual carbon rate 30%
A mixed papermaking sheet containing the above thermoplastic resin is heated to a temperature not lower than the melting point of the thermoplastic resin, pressure-molded, or the sheets are laminated and heated, pressure-molded to form a green molded body, and fired. Carbonization is a feature of the structure.

【0010】以下、本発明を詳細に説明する。パルプは
固相炭化する繊維で、不浸透炭素質成形体の機械的強度
等の製品物性を支配する因子であり、抄紙性を確保す
る。すなわち炭化する際に、パルプの繊維が固相炭化を
辿るためグリーン成形体の形状がそのまま製品まで保持
される。固相炭化を辿る繊維としてはパルプの他、レー
ヨン繊維、綿糸等の他のセルロース系繊維もあるが、入
手しやすく安価なパルプが本発明の目的に適している。
Hereinafter, the present invention will be described in detail. Pulp is a solid-phase carbonized fiber that is a factor that governs the physical properties of products such as the mechanical strength of impermeable carbonaceous compacts and ensures papermaking properties. That is, when carbonized, the fibers of the pulp follow solid-phase carbonization, so that the shape of the green molded body is maintained as it is until the product. Fibers that follow solid-phase carbonization include not only pulp but also other cellulosic fibers such as rayon fiber and cotton yarn, but pulp that is easily available and inexpensive is suitable for the purpose of the present invention.

【0011】炭素質粉末は不浸透炭素質成形体の電気伝
導性、熱伝導性等の製品物性を支配する因子であり、抄
紙性に問題を生じない範囲の粒度のものが使用される。
この炭素質粉末の粒度は50μm以下の範囲であり、好
ましくは1μm〜30μmであり、電気伝導性、熱伝導
性をよくするため黒鉛化したもの、例えば炭素繊維粉
末、天然黒鉛粉末、人造黒鉛粉末等が望ましい。
The carbonaceous powder is a factor that governs the physical properties of the impervious carbonaceous compact such as electrical conductivity and thermal conductivity, and the grain size of the range which does not cause a problem in the papermaking property is used.
The particle size of this carbonaceous powder is in the range of 50 μm or less, preferably 1 μm to 30 μm, and graphitized to improve electric conductivity and thermal conductivity, for example, carbon fiber powder, natural graphite powder, artificial graphite powder. Etc. are desirable.

【0012】熱可塑性樹脂は、不浸透炭素質成形体の不
浸透性、機械的強度を支配する因子であり、残炭率が3
0%以上のものが望ましい。即ち、熱可塑性樹脂は積
層、加熱、加圧成形時に溶融し、パルプと炭素質粉末と
のバインダー機能を発揮でき、かつ混合抄紙シート内の
空隙を埋め、不浸透性に寄与し、この不浸透性が焼成炭
化工程を経て製品まで保持される。
The thermoplastic resin is a factor which controls the impermeability and mechanical strength of the impervious carbonaceous molded article, and the residual carbon rate is 3
It is preferably 0% or more. That is, the thermoplastic resin melts during lamination, heating, and pressure molding, can exhibit the binder function between the pulp and the carbonaceous powder, and fills the voids in the mixed papermaking sheet to contribute to impermeability. The product retains its properties up to the product through the firing and carbonization process.

【0013】熱可塑性樹脂としては、塩化ビニル樹脂、
塩素化塩化ビニル樹脂、ポリアクリロニトリル系樹脂、
ポリビニルアルコール、ポリフェニレンエーテル、ポリ
アミドイミド、ポリジビニルベンゼン等があり、特にポ
リアクリロニトリル系樹脂、ポリビニルアルコール、ポ
リアミドイミドが好ましい。
As the thermoplastic resin, vinyl chloride resin,
Chlorinated vinyl chloride resin, polyacrylonitrile resin,
There are polyvinyl alcohol, polyphenylene ether, polyamide imide, polydivinyl benzene and the like, and polyacrylonitrile resin, polyvinyl alcohol and polyamide imide are particularly preferable.

【0014】樹脂の形状は特に限定されないが、抄紙性
の面から繊維形態のものが望ましく、繊維径として4デ
ニール以下、長さとしては1〜10mmのものが望まし
い。すなわち繊維径が太すぎると積層、加熱、加圧工程
を経る際均一な接着性が得られにくく、繊維の長さが長
いと抄紙しにくくなる。
The shape of the resin is not particularly limited, but a fiber form is preferable from the viewpoint of paper making property, and a fiber diameter of 4 denier or less and a length of 1 to 10 mm are preferable. That is, if the fiber diameter is too large, it is difficult to obtain uniform adhesiveness during the lamination, heating, and pressing steps, and if the fiber length is long, it becomes difficult to make paper.

【0015】混合抄紙シートの配合は、パルプ、炭素質
粉末、熱可塑性樹脂の重量比が40〜60重量%、5〜
25重量%、30〜50重量%が好ましい。この重量比
からはずれると、抄紙性の低下、層間接着性の低下等に
よるグリーン成形体の不具合、反り、割れ等の焼成炭化
時の不具合を生じ、製品特性の劣化を生じる。
The mixed papermaking sheet is blended in such a manner that the weight ratio of pulp, carbonaceous powder and thermoplastic resin is 40 to 60% by weight, 5 to 5% by weight.
25 wt% and 30 to 50 wt% are preferable. If it deviates from this weight ratio, defects in the green molded product due to deterioration of paper-making property, deterioration of interlayer adhesiveness, defects during firing and carbonization such as warpage and cracking, and deterioration of product properties occur.

【0016】このように調整配合された混合抄紙シート
は加熱、加圧成形又は積層、加熱、加圧成形され、成形
温度、成形圧力のコントロールにより所望のグリーン成
形体とする。当然のことながら成形温度が高く、成形圧
力が大きい程グリーン成形体の嵩密度は高くなる。
The mixed papermaking sheet thus adjusted and blended is heated, pressure-molded or laminated, heated and pressure-molded to obtain a desired green molded body by controlling the molding temperature and molding pressure. As a matter of course, the higher the molding temperature and the higher the molding pressure, the higher the bulk density of the green molded body.

【0017】成形は前記シート又は積層した所定形状の
混合抄紙シートを加圧して行う。加圧成形方法は特に限
定されず、一般的にはプレス、ロール等で行う。又例え
ば円筒状の複雑な形状を作製する場合は、予め所定形状
の金型を作製し、所定形状の混合抄紙シートを設置し、
プレス等で加熱した金型を加圧、成形し作製することが
できる。成形圧力は面内の均一性、不浸透性等を保持す
るためには5kg/cm2 以上、特に10kg/cm2
以上にすることが望ましい。
The molding is performed by pressing the above-mentioned sheet or the laminated papermaking sheet having a predetermined shape. The pressure molding method is not particularly limited and is generally performed by a press, a roll or the like. Further, for example, in the case of producing a cylindrical complicated shape, a mold having a predetermined shape is prepared in advance, and a mixed papermaking sheet having a predetermined shape is installed,
It can be manufactured by pressurizing and molding a mold heated by a press or the like. The molding pressure is 5 kg / cm 2 or more, especially 10 kg / cm 2 in order to maintain the in-plane uniformity and impermeability.
It is desirable to set the above.

【0018】加熱温度は熱可塑性樹脂が十分な流動性を
示す温度で行う。加熱温度の設定は、熱可塑性樹脂の種
類で異なるが熱可塑性樹脂の融点、流動性を考慮する。
通常、加熱温度は選択した熱可塑性樹脂の融点上10〜
100℃の温度範囲で、好ましくは20〜80℃の範囲
である。
The heating temperature is such that the thermoplastic resin exhibits sufficient fluidity. The setting of the heating temperature differs depending on the type of thermoplastic resin, but the melting point and fluidity of the thermoplastic resin are considered.
Generally, the heating temperature is 10 to 10 above the melting point of the selected thermoplastic resin.
In the temperature range of 100 ° C., preferably in the range of 20-80 ° C.

【0019】焼成、炭化はグリーン成形体を多数積層
し、黒鉛板で挟持し荷重をかけた状態で常法により非酸
化性雰囲気下で800〜3000℃で焼成される。荷重
は数g/cm2 〜数10g/cm2 程度で、好ましくは
5g/cm2 〜50g/cm2 程度である。荷重が少な
いと被焼成体に反り等が発生し易くなる。一方、数10
0g/cm2 以上の荷重を与えようとすると不浸透炭素
質成形体の形状によって、数tonの重量の黒鉛板が必
要となり、焼成時のハンドリングが煩雑となり現実的で
ない。
For firing and carbonization, a large number of green compacts are laminated, sandwiched between graphite plates, and subjected to a load, and then fired at 800 to 3000 ° C. in a non-oxidizing atmosphere by a conventional method. Load a few g / cm 2 ~ Number 10 g / cm 2 or so, preferably from 5g / cm 2 ~50g / cm 2 approximately. When the load is small, the object to be fired is likely to be warped. On the other hand, the number 10
If a load of 0 g / cm 2 or more is applied, a graphite plate with a weight of several tons is required due to the shape of the impervious carbonaceous compact, and handling during firing becomes complicated, which is not realistic.

【0020】[0020]

【作用】本発明によれば、パルプ、炭素質粉末、熱可塑
性樹脂の混合抄紙シートを加熱、加圧成形し、又は積
層、加熱、加圧成形することによりシート内に均一に分
散した熱可塑性樹脂が溶融し、パルプ繊維間に浸透し炭
素質粉末との密着性を高める。そして焼成炭化時におい
ても、シート内に均一に熱可塑性樹脂が浸透しているた
め、炭化が均一に進み反りや表面模様が少なくなる。
又、加熱、加圧成形、又は積層、加熱、加圧成形するだ
けで、グリーン成形体を製造することが可能となるので
工程が簡単になり、低コスト化が図れる。
According to the present invention, a mixed papermaking sheet of pulp, carbonaceous powder and thermoplastic resin is heated and pressure-molded, or laminated, heated and pressure-molded to obtain a thermoplastic resin uniformly dispersed in the sheet. The resin melts and penetrates between pulp fibers to improve the adhesion with the carbonaceous powder. Even at the time of firing and carbonization, the thermoplastic resin is evenly permeated into the sheet, so that carbonization proceeds uniformly and warpage and surface pattern are reduced.
Further, the green molded body can be manufactured only by heating, pressure molding, or laminating, heating, and pressure molding, so that the process is simplified and the cost can be reduced.

【0021】[0021]

【実施例】【Example】

実施例1〜5 以下本発明を実施例とともに説明する。パルプ(カナデ
ィアンフリーネス650mlに叩解した木材パルプ)、
人造黒鉛粉末(昭和電工(株)製 UFG−30、10
μm)、アクリロニトリル繊維(東邦レーヨン(株)製
スペリア、3デニール、5mm)を表1に示す所定の
配合に従って調整し、混合スラリー水溶液とした後、丸
網抄紙機((株)東洋精機製作所製、TSS式シートマ
シン)を用いて混合抄紙シートを作成した。
Examples 1 to 5 The present invention will be described below with examples. Pulp (wood pulp beaten to 650 ml Canadian Freeness),
Artificial graphite powder (Showa Denko KK UFG-30, 10
μm), acrylonitrile fiber (Toho Rayon Co., Ltd. Superior, 3 denier, 5 mm) were prepared according to the prescribed composition shown in Table 1 to prepare a mixed slurry aqueous solution, and then a round net paper machine (Toyo Seiki Seisakusho KK) , TSS type sheet machine) was used to prepare a mixed papermaking sheet.

【0022】この混合抄紙シートを150mm角に切出
し、6枚積層し平板形状金型にセットした。この金型を
200℃、240℃に加熱し、10kg/cm2 、20
kg/cm2 、30kg/cm2 の加圧力で成形し、グ
リーン成形体を作製した。
This mixed papermaking sheet was cut into 150 mm square pieces, 6 sheets were laminated and set in a flat plate-shaped mold. This mold is heated to 200 ° C. and 240 ° C. and heated to 10 kg / cm 2 , 20
A green molded body was produced by molding with a pressure of kg / cm 2 and 30 kg / cm 2 .

【0023】これらのグリーン成形体を常法に従い黒鉛
板に挟持して5g/cm2 、10g/cm2 、30g/
cm2 の荷重をかけ、N2 雰囲気下、1000℃以上で
10日間焼成して不浸透炭素質成形体を作製した。
These green compacts were sandwiched between graphite plates according to a conventional method to obtain 5 g / cm 2 , 10 g / cm 2 and 30 g / cm 2 .
A load of cm 2 was applied, and firing was performed at 1000 ° C. or higher for 10 days in a N 2 atmosphere to produce an impermeable carbonaceous molded body.

【0024】[0024]

【実施例】【Example】

実施例6〜10 パルプ(カナディアンフリーネス650mlに叩解した
木材パルプ)、炭素繊維粉末(呉羽化学工業(株)製
ミドルファイバー、10μm)、ビニルアルコール繊維
((株)クラレ製 ビニロン、2デニール、4mm)を
表2に示す所定の配合に従って調整し、混合スラリー水
溶液とした後、丸網抄紙機((株)東洋精機製作所製、
TSS式シートマシン)を用いて混合抄紙シートを作成
した。
Examples 6 to 10 Pulp (wood pulp beaten to 650 ml Canadian Freeness), carbon fiber powder (Kureha Chemical Industry Co., Ltd.)
Middle fiber (10 μm) and vinyl alcohol fiber (Kuraray Co., Ltd., vinylon, 2 denier, 4 mm) were adjusted according to the prescribed composition shown in Table 2 to prepare a mixed slurry aqueous solution, and then a round net paper machine (Toyo Corporation) Made by Seiki Seisakusho,
A mixed papermaking sheet was prepared using a TSS type sheet machine.

【0025】この混合抄紙シートを150mm角に切出
し、6枚積層し平板形状金型にセットした。この金型を
200℃、210℃、220℃に加熱し、10kg/c
2 、30kg/cm2 の加圧力で成形し、グリーン成
形体を作製した。
This mixed papermaking sheet was cut into 150 mm square pieces, 6 sheets were laminated and set in a flat plate-shaped mold. This mold is heated to 200 ° C, 210 ° C, 220 ° C and 10 kg / c
It was molded under a pressure of m 2 of 30 kg / cm 2 to prepare a green molded body.

【0026】これらのグリーン成形体を常法に従い黒鉛
板に挟持して10g/cm2 、20g/cm2 の荷重を
かけ、N2 雰囲気下、1000℃で10日間焼成して不
浸透炭素質成形体を作製した。
The sandwiching these green compact graphite plate according to a conventional method under a load of 10g / cm 2, 20g / cm 2 and, N 2 atmosphere, firing the impermeable carbonaceous molding 10 days at 1000 ° C. The body was made.

【0027】各実施例の作製条件は表1、表2に示し
た。尚各特性値は表3に示した。各特性は以下の測定を
行い評価した。 曲げ強さ :3点曲げ法(JIS K6911) 電気比抵抗:面内4端子法(JIS R7202) 熱伝導率 :レーザーフラッシュ法200℃、厚さ方
向 通気率 :N2 ガス 室温下、差圧 1気圧
The manufacturing conditions of each example are shown in Tables 1 and 2. The characteristic values are shown in Table 3. Each characteristic was evaluated by the following measurements. Bending strength: Three-point bending method (JIS K6911) Electrical resistivity: In-plane four-terminal method (JIS R7202) Thermal conductivity: Laser flash method 200 ° C, Thickness direction Air permeability: N 2 gas Room temperature, differential pressure 1 Barometric pressure

【0028】本発明において得られた炭素質成形体は、
曲げ強さ、電気比抵抗、熱伝導率も良好で通気率も10
-5cc・cm/cm2 sec以下で良好な不浸透性を有
する。
The carbonaceous molded body obtained in the present invention is
Bending strength, electrical resistivity, thermal conductivity are good, and air permeability is 10
-5 cc · cm / cm 2 sec or less has good impermeability.

【0029】[0029]

【表1】 [Table 1]

【0030】[0030]

【表2】 [Table 2]

【0031】[0031]

【表3】 [Table 3]

【0032】[0032]

【発明の効果】以上のように本発明に従えば、熱硬化性
樹脂の含浸工程が省略でき、これに伴う樹脂硬化の程度
を決める予備加熱、重力による樹脂の偏在、含浸樹脂の
不均一性等、製品物性を左右する条件が軽減される。従
って得られる炭素質成形体の物性も安定し、生産性も良
好で、低コストな不浸透炭素質成形体の製造が可能とな
る。特にリン酸型燃料電池等に使用されるセパレータを
安価に提供できる。
As described above, according to the present invention, the step of impregnating the thermosetting resin can be omitted, and the preheating for determining the degree of resin curing, the uneven distribution of the resin due to gravity, and the non-uniformity of the impregnated resin. The conditions that affect the physical properties of the product are reduced. Therefore, the obtained carbonaceous molded article has stable physical properties, good productivity, and a low-cost impervious carbonaceous molded article can be produced. In particular, a separator used for a phosphoric acid fuel cell or the like can be provided at low cost.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 40〜60重量%のパルプ、5〜25重
量%の炭素質粉末、30〜50重量%の残炭率30%以
上の熱可塑性樹脂を配合した混合抄紙シートを、前記熱
可塑性樹脂の融点以上の温度に加熱、加圧成形し又は前
記シートを積層し加熱、加圧成形し、グリーン成形体と
なし、焼成炭化することを特徴とする不浸透炭素質成形
体の製造方法。
1. A mixed papermaking sheet containing 40-60% by weight of pulp, 5-25% by weight of carbonaceous powder, and 30-50% by weight of a thermoplastic resin having a residual carbon content of 30% or more is used as the thermoplastic resin. A method for producing an impervious carbonaceous molded article, which comprises heating to a temperature equal to or higher than the melting point of a resin, press-molding or laminating the above-mentioned sheets, heating and press-molding to form a green molded article, and calcining and carbonizing.
【請求項2】 残炭率30%以上の熱可塑性樹脂の融点
上20〜80℃以上で加熱することを特徴とする請求項
1記載の不浸透炭素質成形体の製造方法。
2. The method for producing an impervious carbonaceous molded article according to claim 1, wherein heating is performed at 20 to 80 ° C. or higher on the melting point of the thermoplastic resin having a residual carbon rate of 30% or higher.
JP6187433A 1994-08-09 1994-08-09 Production of impermeable carbonaceous formed body Pending JPH0848577A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6187433A JPH0848577A (en) 1994-08-09 1994-08-09 Production of impermeable carbonaceous formed body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6187433A JPH0848577A (en) 1994-08-09 1994-08-09 Production of impermeable carbonaceous formed body

Publications (1)

Publication Number Publication Date
JPH0848577A true JPH0848577A (en) 1996-02-20

Family

ID=16205981

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6187433A Pending JPH0848577A (en) 1994-08-09 1994-08-09 Production of impermeable carbonaceous formed body

Country Status (1)

Country Link
JP (1) JPH0848577A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013534505A (en) * 2010-06-25 2013-09-05 エスゲーエル カーボン ソシエタス ヨーロピア Manufacturing method of ceramic material for ceramic material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013534505A (en) * 2010-06-25 2013-09-05 エスゲーエル カーボン ソシエタス ヨーロピア Manufacturing method of ceramic material for ceramic material

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