JP2607397B2 - Method for producing porous glassy carbon material - Google Patents

Method for producing porous glassy carbon material

Info

Publication number
JP2607397B2
JP2607397B2 JP2405365A JP40536590A JP2607397B2 JP 2607397 B2 JP2607397 B2 JP 2607397B2 JP 2405365 A JP2405365 A JP 2405365A JP 40536590 A JP40536590 A JP 40536590A JP 2607397 B2 JP2607397 B2 JP 2607397B2
Authority
JP
Japan
Prior art keywords
sheet
weight
binder
strength
water
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
JP2405365A
Other languages
Japanese (ja)
Other versions
JPH04209773A (en
Inventor
和義 灰野
義雄 鈴木
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 JP2405365A priority Critical patent/JP2607397B2/en
Publication of JPH04209773A publication Critical patent/JPH04209773A/en
Application granted granted Critical
Publication of JP2607397B2 publication Critical patent/JP2607397B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Ceramic Products (AREA)

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、良好な気孔性状と優れ
た骨格強度を備える多孔質ガラス状カーボン材を量産性
よく製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for mass-producing a porous glassy carbon material having good porosity and excellent skeletal strength.

【0002】[0002]

【従来の技術】軽量、導電性、耐熱性および耐食性など
に優れた特性を示す多孔質カーボン材は、工業用のフィ
ルター、電池用電極、吸着材等の用途分野に有用されて
いる。
2. Description of the Related Art Porous carbon materials exhibiting excellent properties such as light weight, conductivity, heat resistance and corrosion resistance are useful in application fields such as industrial filters, battery electrodes and adsorbents.

【0003】従来、多孔質カーボン材の製造技術として
は、粒度を揃えたコークス粉をタールピッチのような炭
化性バインダーとともに捏合したのち粉砕、成形および
焼成炭化処理するプロセスが典型的な製造手段とされて
いるが、均質で安定な気孔構造を付与するための条件設
定が難しいうえ、材質強度が低い欠点がある。
Conventionally, a typical production technique of a porous carbon material includes a process in which coke powder having a uniform particle size is kneaded with a carbonizable binder such as tar pitch, followed by pulverization, molding and calcining. However, it is difficult to set conditions for providing a uniform and stable pore structure, and the material strength is low.

【0004】この点、炭素繊維をパルプおよびバインダ
ー成分とともに抄紙して得られる炭素繊維混合シートに
熱硬化性樹脂液を含浸させたのち焼成炭化処理する方法
(特開昭50−25808 号公報)は、炭素繊維が補強骨格を
形成し、また熱硬化性樹脂がガラス状カーボン組織に転
化するため、材料強度を効果的に向上させることができ
る。ところが、この方法においては、嵩密度、気孔径、
気孔率などの制御に難点があり、加えて高価な炭素繊維
を原料とする関係で製造原価が高騰化する問題がある。
In this regard, a method of impregnating a thermosetting resin liquid into a carbon fiber mixed sheet obtained by paper-making carbon fibers together with pulp and a binder component, followed by calcining and carbonizing (Japanese Patent Application Laid-Open No. 50-25808) has been proposed. Since the carbon fibers form a reinforcing skeleton and the thermosetting resin is converted into a glassy carbon structure, the material strength can be effectively improved. However, in this method, bulk density, pore size,
There is a problem in controlling the porosity and the like, and in addition, there is a problem that the production cost rises because expensive carbon fiber is used as a raw material.

【0005】このため、炭素繊維に代えて炭素繊維製造
用の有機繊維を使用し、これにパルプ、炭素質粉末など
を配合して抄紙したシートに有機高分子物質あるいは炭
素質粉末を懸濁させた有機高分子物質を含浸したのち焼
成処理する方法(特開昭61−23664号公報、同61−23666
5号公報) が提案されている。しかしながら、この方法
では、組織内に局部的に閉塞された空隙部分が多く形成
されるため、均質かつ制御された気孔構造を得ることが
困難となる。
[0005] For this reason, organic fibers for carbon fiber production are used in place of carbon fibers, and pulp, carbonaceous powder, etc. are blended into the sheet and the organic polymer substance or carbonaceous powder is suspended in the sheet. (Japanese Patent Application Laid-Open Nos. 61-23664 and 61-23666)
No. 5) has been proposed. However, in this method, since a locally closed void portion is formed in the tissue, it is difficult to obtain a uniform and controlled pore structure.

【0006】本発明者らは上記問題点の解消を図り、良
好な気孔性状と高強度特性を兼備するガラス状炭素質の
多孔質材を得るためのプロセスとして、α−セルロース
を主成分とする熱揮散性物質を抄紙してシート化する工
程と、シートに残炭率40重量%以上の熱硬化性樹脂溶液
を含浸する工程と、含浸処理後のシート50〜150 ℃の温
度で半硬化する工程と、半硬化シートを積層して全面を
均一加熱しながらシート厚さが70〜20%になるように圧
縮する工程と、圧縮シートを非酸化性雰囲気下で800 ℃
以上の温度により焼成炭化する工程からなるポーラスカ
ーボン材の製造方法を開発し、既に特願平1−321729号
として提案した。
The present inventors have attempted to solve the above-mentioned problems, and as a process for obtaining a vitreous carbonaceous porous material having both good porosity and high strength properties, α-cellulose is mainly used. Paper-making the heat-volatile substance into a sheet, impregnating the sheet with a thermosetting resin solution having a residual carbon ratio of 40% by weight or more, and semi-curing the impregnated sheet at a temperature of 50 to 150 ° C. Laminating the semi-cured sheets and compressing them so that the sheet thickness becomes 70 to 20% while uniformly heating the entire surface; and 800 ° C in a non-oxidizing atmosphere.
A method for producing a porous carbon material comprising a step of calcining and carbonizing at the above temperature has been developed and has already been proposed as Japanese Patent Application No. 1-321729.

【0007】[0007]

【発明が解決しようとする課題】しかし、引き続く研究
において、前記の先行技術には量産化を目的として連続
的な処理工程を実施しようとする際に解決しなければな
らない幾つかの新たな課題が発生した。すなわち、シー
ト化の工程に産業用ペーパーの製造ラインとされている
連続抄紙法を適用しようとすると、製造ラインの途中で
シートの破断トラブルが多発し、その都度ラインを停止
する必要がある。シート破断の原因は、抄紙直後のシー
トには多量の水が含まれており、使用バインダーも水溶
性である関係で抄紙段階で適度なシート強度を確保でき
ず、このためロール移動(特に乾燥段階)の際に僅かな
テンションの変動によって容易に組織破壊につながる現
象に基づいている。このような現象は抄紙条件を制御
し、シート密度を高めることで軽減化することも可能で
あるが、この場合には均質な気孔組織の形成化を損ねる
ため、後工程で連続的な樹脂液含浸処理を施すと含浸樹
脂の偏在が生じて良好な気孔性状を得ることができなく
なる。
However, in the subsequent research, there are some new problems that must be solved when trying to carry out continuous processing steps for mass production in the prior art. Occurred. That is, when the continuous paper making method, which is regarded as a production line for industrial paper, is applied to the sheet forming process, troubles of sheet breakage occur frequently in the middle of the production line, and it is necessary to stop the line each time. The cause of sheet breakage is that the sheet immediately after papermaking contains a large amount of water, and the binder used is also water-soluble, so that an appropriate sheet strength cannot be secured at the papermaking stage. ) Is based on the phenomenon that a slight change in tension easily leads to tissue destruction. Such a phenomenon can be mitigated by controlling the papermaking conditions and increasing the sheet density.However, in this case, since the formation of a uniform pore structure is impaired, a continuous When the impregnation treatment is performed, uneven distribution of the impregnated resin occurs, so that it is not possible to obtain good pore properties.

【0008】本発明の目的は、先行技術における上記の
問題点を解消し、連続工程によってもシートの破断現象
を起こすことなく、常に良好な気孔性状と優れた骨格強
度を備える多孔質ガラス状カーボン材を量産性よく製造
する方法を提供することにある。
An object of the present invention is to solve the above-mentioned problems in the prior art, and to provide a porous glassy carbon which always has good porosity and excellent skeletal strength without causing sheet breakage even in a continuous process. An object of the present invention is to provide a method for manufacturing a material with good mass productivity.

【0009】[0009]

【課題を解決するための手段】上記の目的を達成するた
めの本発明による多孔質ガラス状カーボン材の製造方法
は、α−セルロースを主成分とする有機物質60〜90重量
部、水溶性抄紙バインダー10〜40重量部および水不溶性
で且つ熱揮散性のバインダー1〜10重量部からなる原料
組成の分散水を連続抄紙してシートに成形し、該シート
を残炭率40%以上の熱効果性樹脂溶液に連続的に浸漬し
たのちロール絞り処理を施し、処理後のシートを半硬化
して積層成形し、成形体を非酸性雰囲気下で800 ℃以上
の温度により焼成炭化することを構成上の特徴とする。
In order to achieve the above-mentioned object, a method for producing a porous glassy carbon material according to the present invention comprises: Dispersed water of a raw material composition comprising 10 to 40 parts by weight of a binder and 1 to 10 parts by weight of a water-insoluble and heat-vaporizable binder is continuously formed into a sheet, and the sheet is subjected to a thermal effect of a residual carbon ratio of 40% or more. After continuous immersion in an aqueous resin solution, roll squeezing treatment is performed, the treated sheet is semi-cured, laminated and formed, and the formed body is calcined and carbonized at a temperature of 800 ° C or more in a non-acidic atmosphere. The feature of.

【0010】本発明の主要な原料物質となるα−セルロ
ースを主成分とする有機物質は抄紙時にシートのフィラ
ー成分となるもので、通常のパルプのほか、α−セルロ
ース分90%を含むレーヨンパルプを用いることができ
る。パルプ性状としては、抄紙整形性および高気孔構造
を確保する面から太さ3〜10デニール、長さ5〜10mmの
繊維形状を有するものを選択することが好ましい。
The organic material mainly composed of α-cellulose as a main raw material of the present invention is used as a filler component of a sheet during papermaking. In addition to ordinary pulp, rayon pulp containing 90% of α-cellulose Can be used. As the pulp properties, it is preferable to select a pulp having a fiber shape of 3 to 10 deniers and 5 to 10 mm in length from the viewpoint of ensuring papermaking properties and high pore structure.

【0011】水溶性抄紙バインダーは、抄紙工程でシー
ト成形の結合材として機能する成分で、例えばアカマ
ツ、エゾマツ、トドマツ、カラマツ、モミ、シガ等の針
葉樹系パルプが好適に使用される。
The water-soluble papermaking binder is a component that functions as a binder for sheet formation in the papermaking process. For example, softwood pulp such as red pine, spruce pine, fir pine, larch, fir, and shiga is preferably used.

【0012】水不溶性で且つ熱揮散性のバインダーは、
前記の水溶性バインダーの機能を補強してシートがウエ
ット状態にあるときに十分な強度を付与するために添加
される第三成分で、ポリビニールアルコール(ビニロ
ン)、不溶性澱粉、ミクロフイブリル化パルプなどを用
いることができる。これらのバインダーを併用すること
によりウエット時における抄紙シートの強度が増大し、
連続抄紙操作を適用してもシートの破断現象が生じるこ
とがなくなる。
[0012] The water-insoluble and heat-volatile binder is:
A third component added to reinforce the function of the water-soluble binder and impart sufficient strength when the sheet is in a wet state, such as polyvinyl alcohol (vinylon), insoluble starch, and microfibrillated pulp. Etc. can be used. By using these binders in combination, the strength of the papermaking sheet when wet is increased,
Even when a continuous papermaking operation is applied, the breakage of the sheet does not occur.

【0013】原料物質の配合比率は、α−セルロースを
主成分とする60〜90重量部、水溶性抄紙バインダー10〜
40重量部および水不溶性で且つ熱揮散性のバインダー1
〜10重量部に設定する。有機物質に対するバインダー成
分の配合量の前記の範囲を下廻る場合には抄紙成形性が
悪くなり、他方、前記範囲を越えるバインダー成分の配
合では多孔質組織の形成が困難となる。とくに第三成分
として添加する水不溶性で熱揮散性のバインダーの配合
量は重要で、これが1重量部未満であると湿潤状態にお
ける適度なシート強度を確保することができなくなって
シートの破断が起き易くなり、また10重量部を越えると
気孔率、気孔径等が低下して目的とする気孔分布が均一
な多孔質組織を得ることが不可能となる。
The mixing ratio of the raw materials is 60 to 90 parts by weight mainly composed of α-cellulose, 10 to 10 parts of a water-soluble papermaking binder.
40 parts by weight and water-insoluble and heat-vaporizable binder 1
Set to ~ 10 parts by weight. If the amount of the binder component relative to the organic substance is below the above range, the papermaking moldability will be poor, while if the amount of the binder component exceeds the above range, it will be difficult to form a porous structure. Particularly, the amount of the water-insoluble and heat-vaporizable binder added as the third component is important. If the amount is less than 1 part by weight, it is not possible to secure an appropriate sheet strength in a wet state, and the sheet breaks. When the content exceeds 10 parts by weight, the porosity, the pore size, and the like decrease, and it becomes impossible to obtain a porous structure having a uniform target pore distribution.

【0014】上記の三成分系原料物質は混合して水に均
一分散させ、連続抄紙装置を用いて連続的に抄紙してシ
ートに成形し、乾燥ロールに巻き取る。
The above three-component raw materials are mixed and uniformly dispersed in water, continuously made into paper using a continuous paper making apparatus, formed into a sheet, and wound around a drying roll.

【0015】乾燥シートは、ついで案内ロールを介して
残炭率40%以上の熱硬化性樹脂溶液中に連続的に浸漬す
る機構の処理装置にセットし、浸漬処理をおこなう。熱
硬化性樹脂の残炭率とは、樹脂を非酸化性雰囲気下で80
0 ℃の温度に焼成したときに残留する炭素分の重量を指
し、この残炭率が40%を下廻るときには、得られる多孔
質ガラス状カーボン材の強度を実用水準まで向上させる
ことが極めて困難となる。40重量%以上の残炭率を有す
る熱硬化性樹脂の例としては、フェノール系樹脂、フラ
ン系樹脂、ポリイミド樹脂などが挙げられ、いずれも焼
成炭化後にガラス状カーボンに転化する。これら熱硬化
性樹脂の溶液化に用いる有機溶媒は樹脂の種類によって
選定されるが、通常、メタノール、エタノール、アセト
ン、メチルエチルケトンのような低粘度で浸透性が高
く、容易に熱揮散する性質の有機溶媒が選定される。溶
液に樹脂濃度は、5重量%未満であると強度特性が減退
し、40重量%を越すと粘度が増大して含浸性を損ねるう
え、気孔の閉塞を生じて気孔率および気孔径の調整が困
難となる。したがって、5〜40重量%の範囲の樹脂濃
度に設定することが好適である。
The dried sheet is then set in a processing apparatus having a mechanism for continuously immersing it through a guide roll in a thermosetting resin solution having a residual carbon ratio of 40% or more, and immersion treatment is performed. The residual carbon ratio of a thermosetting resin is 80% under non-oxidizing atmosphere.
Refers to the weight of carbon remaining when fired at a temperature of 0 ° C. When the residual carbon ratio is less than 40%, it is extremely difficult to improve the strength of the resulting porous glassy carbon material to a practical level. Becomes Examples of the thermosetting resin having a residual carbon ratio of 40% by weight or more include a phenol resin, a furan resin, and a polyimide resin, all of which are converted to glassy carbon after firing and carbonization. The organic solvent used to form a solution of these thermosetting resins is selected depending on the type of the resin. Usually, organic solvents having a low viscosity, high permeability, and easily heat-evaporating properties such as methanol, ethanol, acetone, and methyl ethyl ketone are used. A solvent is selected. If the resin concentration in the solution is less than 5% by weight, the strength characteristics decrease, and if it exceeds 40% by weight, the viscosity increases, impairing the impregnation property, and the pores are blocked, and the porosity and the pore size are adjusted. It will be difficult. Therefore, it is preferable to set the resin concentration in the range of 5 to 40% by weight.

【0016】浸漬処理したシートは、引き続き所定間隙
の2本ロール間を通過させてロール絞り処理を施し、余
剰な樹脂溶液を除去するとともに含浸組織を均質化す
る。
The immersed sheet is then passed between two rolls with a predetermined gap and subjected to roll squeezing to remove excess resin solution and homogenize the impregnated structure.

【0017】処理後のシートは、50〜150 ℃の温度に保
持された乾燥器を通して水分等の未反応物や反応生成物
を有機溶媒成分とともに揮散除去し、同時にシートに担
持された樹脂成分を半硬化する。次に、半硬化シートを
所要枚数に積層して全面を均一に加熱しながら、シート
厚さが圧縮前に比べて70〜20%の範囲まで薄くなるよう
な条件で圧縮し積層成形する。該圧縮比率が70%を上廻
る程度の低圧縮率では実用的な強度性能が得られ難く、
20%を下廻るような高圧縮率になると組織が緻密化して
気孔率の大幅低下を招く。また、均質加熱にはヒーター
を内蔵した平面加熱盤を用い、圧縮手段には油圧プレス
または空圧プレスを用いることが工業的である。成形時
の温度は樹脂の性状によって若干の差異はあるが、概ね
80〜200 ℃の範囲で円滑に成形され、同時に樹脂が完全
硬化する。
The processed sheet is passed through a dryer maintained at a temperature of 50 to 150 ° C. to volatilize and remove unreacted substances such as moisture and reaction products together with an organic solvent component, and simultaneously remove a resin component supported on the sheet. Semi-cured. Next, while laminating the required number of semi-cured sheets and uniformly heating the entire surface, the sheets are compressed and laminated and molded under conditions such that the sheet thickness is reduced to a range of 70 to 20% as compared with that before compression. At a low compression ratio such that the compression ratio exceeds 70%, practical strength performance is difficult to obtain,
At a high compression ratio of less than 20%, the structure becomes dense and the porosity is greatly reduced. It is industrial to use a flat heating plate with a built-in heater for the homogeneous heating and to use a hydraulic press or a pneumatic press for the compression means. The molding temperature varies slightly depending on the properties of the resin.
It is molded smoothly in the range of 80 to 200 ° C, and at the same time, the resin is completely cured.

【0018】このようにして積層成形された成形体は、
非酸化性雰囲気中で800 ℃以上の温度により焼成し、熱
揮散性の成分を揮散させるとともに熱硬化性樹脂成分を
炭化してガラス状カーボン材に転化させる。この炭化工
程は、成形体を平滑表面を有する黒鉛板で挟み込んだ形
態でおこなうと反り等の変形を防止する効果がある。
[0018] The molded product thus formed by lamination is
It is baked in a non-oxidizing atmosphere at a temperature of 800 ° C. or higher to volatilize the heat-volatile component and carbonize the thermosetting resin component to be converted into a glassy carbon material. This carbonization step has an effect of preventing deformation such as warpage when the formed body is sandwiched between graphite plates having a smooth surface.

【0019】[0019]

【作用】本発明によれば、原料物質の第三成分である水
不溶性で熱揮散性のバインダーが、抄紙段階においては
主原料相互の接着力を高めて連続抄紙工程のロールテン
ションに耐えるシート強度を付与し、焼成段階では熱分
解を起こして完全に揮散し、良好な多孔質組織を確保す
るために機能する。また、抄紙シートに熱硬化性樹脂溶
液を連続的に浸漬した後の工程として施されるロール絞
り処理は、余剰樹脂を除去してシート組織内に樹脂を均
一に担持させる機能を営む。
According to the present invention, the water-insoluble and heat-vaporizable binder, which is the third component of the raw material, enhances the adhesive force between the main raw materials in the papermaking stage and withstands the roll tension in the continuous papermaking process. In the firing step, it is thermally decomposed to completely volatilize, and functions to secure a favorable porous structure. Further, the roll squeezing treatment performed as a step after the thermosetting resin solution is continuously immersed in the papermaking sheet has a function of removing excess resin and uniformly supporting the resin in the sheet structure.

【0020】これらの機能が、α−セルロースを主成分
とする有機物質による均質な気孔と骨格の形成、熱硬化
性樹脂の炭化によるガラス状カーボン組織の形成化とい
う本来的な作用と相俟って、均一微細な通気性気孔性状
を備えながら材質強度に優れる多孔質ガラス状カーボン
材の連続生産を可能にする。
These functions are combined with the essential functions of forming uniform pores and skeletons by an organic substance containing α-cellulose as a main component, and forming a glassy carbon structure by carbonization of a thermosetting resin. Thus, it is possible to continuously produce a porous glassy carbon material having excellent material strength while having uniform and fine air permeability.

【0021】[0021]

【実施例】以下、本発明の実施例と比較例について説明
する。
EXAMPLES Examples of the present invention and comparative examples will be described below.

【0022】実施例1 α−セルロース分90%以上、太さ5デニール、長さ25mm
のレーヨンパルプ〔大和紡績(株)製〕80重量部、水溶
性抄紙バインダーとして晒し針葉樹パルプ(NBKP)
20重量部および水不溶性で熱揮散性のバインダーとして
ビニロンバインダー〔(株)クラレ製、VPB105〕1重量
部を混合し、水中で撹拌混合して均質に分散させたのち
連続抄紙装置を用いて平均気孔径 110μm 、厚さ0.23m
m、幅1300mmの連続シートを成形した。乾燥前の湿潤シ
ートの強度は45kgf/cm2 で、連続抄紙は円滑に進行しシ
ートの破断現象は生じなかった。
Example 1 α-cellulose content of 90% or more, thickness 5 denier, length 25 mm
80 parts by weight of rayon pulp (manufactured by Daiwa Spinning Co., Ltd.), bleached softwood pulp (NBKP) as a water-soluble papermaking binder
20 parts by weight and 1 part by weight of a vinylon binder (VPB105 manufactured by Kuraray Co., Ltd.) as a water-insoluble and heat-vaporizable binder were mixed, stirred and mixed in water, homogeneously dispersed, and then averaged using a continuous paper machine. Pore diameter 110μm, thickness 0.23m
m, a continuous sheet having a width of 1300 mm was formed. The strength of the wet sheet before drying was 45 kgf / cm 2 , continuous papermaking proceeded smoothly, and no breakage of the sheet occurred.

【0023】乾燥シートを連続樹脂浸漬装置にセット
し、案内ロールを介して残炭率45%のフェノール樹脂
〔住友デュレズ(株)製、スミライトレジンPR940 〕の
20重量%アセトン溶液を満たした槽に連続的に通過させ
て浸漬処理し、引き続き 0.2mmの間隙に調整された2本
ロール間を通してロール絞り処理を施した。
The dried sheet is set in a continuous resin dipping apparatus, and a phenol resin (Sumilite Resin PR940, manufactured by Sumitomo Durez Co., Ltd.) having a residual carbon ratio of 45% is passed through a guide roll.
It was immersed by continuously passing it through a tank filled with a 20% by weight acetone solution, followed by roll squeezing between two rolls adjusted to a gap of 0.2 mm.

【0024】ついで、シートを100 ℃に保持された乾燥
器を通過させて半硬化したのち1辺1300mmの正方形に裁
断し、これを14枚積層して120 ℃に調整された均熱平面
盤の上に置いた状態で上部から平面盤で圧縮率65%にな
るまで圧縮成形して樹脂を完全に硬化させた。
Next, the sheet was passed through a drier maintained at 100 ° C., semi-cured, cut into squares of 1300 mm on a side, and 14 sheets were laminated to form a soaking plate adjusted to 120 ° C. The resin was completely cured by being compression-molded from above on a flat plate until the compression ratio reached 65%.

【0025】得られた成形体を平滑表面をもつ黒鉛板に
挟み付けて電気焼成炉に移し、周囲をコークスパッキン
グ材で被包してから1000℃の温度で焼成炭化処理をし
た。
The obtained molded body was sandwiched between graphite plates having a smooth surface, transferred to an electric firing furnace, and the periphery thereof was covered with a coke packing material, and then fired and carbonized at a temperature of 1000 ° C.

【0026】このようにして製造した多孔質ガラス状カ
ーボン材について各種の特性を測定したところ、嵩密度
0.49g/cc、気孔率(水銀圧入法、以下同様)67%、平均
気孔径(水銀圧入法、以下同様)55μm 、曲げ強度270k
gf/cm2と良好な気孔性状ならびに材質強度を示し、走査
型電子顕微鏡による観察で均質な多孔質組織であること
が確認された。また、本例による10回試作時の製品収率
は100 %であった。
Various properties of the porous glassy carbon material thus manufactured were measured.
0.49 g / cc, porosity (mercury intrusion method, the same applies hereinafter) 67%, average pore diameter (mercury intrusion method, the same applies hereinafter) 55 μm, bending strength 270 k
It exhibited good pore properties and material strength of gf / cm 2, and it was confirmed by observation with a scanning electron microscope that it had a homogeneous porous structure. In addition, the product yield after 10 trial productions in this example was 100%.

【0027】実施例2 ビニロンバインダーの配合量を3重量部に変えたほか
は、全て実施例1と同一のプロセス条件により多孔質ガ
ラス状カーボン材を製造した。この場合の湿潤シートの
強度は49kgf/cm2 で、連続抄紙工程でシート破断は認め
られなかった。
Example 2 A porous glassy carbon material was produced under the same process conditions as in Example 1 except that the amount of the vinylon binder was changed to 3 parts by weight. In this case, the strength of the wet sheet was 49 kgf / cm 2 , and no breakage of the sheet was observed in the continuous papermaking process.

【0028】得られた材料の特性は、嵩密度0.48g/cc、
気孔率65%、平均気孔径54μm 、曲げ強度250kgf/cm2
気孔組織、材質強度ともに良好で、実施例1と同一の顕
微鏡観察結果が得られた。また、10回試作時の製品収率
は100 %であった。
The properties of the material obtained are: bulk density 0.48 g / cc,
The porosity was 65%, the average pore diameter was 54 μm, the bending strength was 250 kgf / cm 2 , the pore structure and the material strength were good, and the same microscopic observation results as in Example 1 were obtained. The product yield after 10 trial productions was 100%.

【0029】実施例3 ビニロンバインダーの配合量を10重量部に変えたほか
は、全て実施例1と同一のプロセス条件により多孔質ガ
ラス状カーボン材を製造した。この場合の湿潤シートの
強度は53kgf/cm2 と高く、連続抄紙工程でのトラブルは
全くなかった。
Example 3 A porous glassy carbon material was produced under the same process conditions as in Example 1 except that the amount of the vinylon binder was changed to 10 parts by weight. In this case, the strength of the wet sheet was as high as 53 kgf / cm 2, and there was no trouble in the continuous papermaking process.

【0030】得られた材料の特性は、嵩密度0.49/cc、
気孔率68%、平均気孔径56μm 、曲げ強度260kgf/cm2
気孔組織、材質強度ともに良好で、実施例1と同様に均
質多孔組織であることが顕微鏡観察で確認された。ま
た、10回試作時の製品収率は100 %であった。
The properties of the material obtained are: bulk density 0.49 / cc,
The porosity was 68%, the average pore diameter was 56 μm, the bending strength was 260 kgf / cm 2 , the pore structure and the material strength were good, and it was confirmed by microscopic observation that the porous structure was homogeneous as in Example 1. The product yield after 10 trial productions was 100%.

【0031】比較例1 水不溶性で且つ熱揮散性のバインダーとしてのビニロン
バインダーを配合せずに実施例1と同一プロセスで連続
抄紙をおこなったところ、シートの破断が多発して製造
不能となった。この場合における湿潤シートの強度を測
定したところ、21kgf/cm2 と低いものであった。
Comparative Example 1 Continuous papermaking was carried out in the same process as in Example 1 without blending a vinylon binder as a water-insoluble and heat-volatile binder. . When the strength of the wet sheet in this case was measured, it was as low as 21 kgf / cm 2 .

【0032】比較例2 ビニロンバインダーの配合量を 0.5重量部としたほか
は、実施例1と同一条件で連続抄紙をおこなったとこ
ろ、シートの破断が生じて製造が困難となった。この場
合における湿潤シートの強度を測定したところ、27kgf/
cm2 であった。
Comparative Example 2 Continuous papermaking was carried out under the same conditions as in Example 1 except that the amount of the vinylon binder was changed to 0.5 part by weight. As a result, the sheet was broken and production was difficult. When the strength of the wet sheet in this case was measured, 27 kgf /
It was cm 2.

【0033】比較例3 ビニロンバインダーの配合量を13重量部とし、ロール絞
り処理を適用しないほかは全て実施例1と同一のプロセ
スと条件により多孔質ガラス状カーボン材を製造した。
この場合の湿潤シートの強度は57kgf/cm2 と高いもの
で、連続抄紙生工程は円滑に進行した。
Comparative Example 3 A porous glassy carbon material was produced by the same process and conditions as in Example 1 except that the blending amount of the vinylon binder was 13 parts by weight and the roll drawing treatment was not applied.
In this case, the strength of the wet sheet was as high as 57 kgf / cm 2, and the continuous paper making process proceeded smoothly.

【0034】得られた材料の特性を測定した結果、嵩密
度0.51g/cc、気孔率55%、平均気孔径45μm 、曲げ強度
230kgf/cm2と実施例に比べて気孔率および材質強度が低
下し、走査型電子顕微鏡による組織観察では気孔の目詰
まりが多く発生していて組織が不均質であることが確認
された。
As a result of measuring the properties of the obtained material, the bulk density was 0.51 g / cc, the porosity was 55%, the average pore diameter was 45 μm, and the bending strength was
The porosity and material strength were reduced to 230 kgf / cm 2 as compared with the examples, and the structure was observed by scanning electron microscope. As a result, many pores were clogged, and it was confirmed that the structure was heterogeneous.

【0035】比較例4 ビニロンバインダーの配合量を3重量部とし、ロール絞
り処理を適用しないほかは全て実施例1と同一のプロセ
スと条件を用いて多孔質ガラス状カーボン材を製造し
た。この場合の湿潤シートの強度は46kgf/cm2 で、連続
抄紙工程にトラブルはなかった。
Comparative Example 4 A porous glassy carbon material was produced using the same process and conditions as in Example 1 except that the blending amount of the vinylon binder was 3 parts by weight and the roll drawing treatment was not applied. In this case, the strength of the wet sheet was 46 kgf / cm 2 , and there was no trouble in the continuous papermaking process.

【0036】得られた材料は、嵩密度0.49g/cc、気孔率
67%、平均気孔径53μm 、曲げ強度270kgf/cm2と特性的
には実施例と同等の測定結果を示したが、走査型電子顕
微鏡による組織観察では気孔の目詰まりが多く、局部的
に気孔率が40%程度を示すところがあって明らかな組織
の不均質性が認められた。
The obtained material has a bulk density of 0.49 g / cc and a porosity.
Although the measurement results were equivalent to those of the example with 67%, an average pore diameter of 53 μm, and a bending strength of 270 kgf / cm 2 , the pores were often clogged by microscopic observation with a scanning electron microscope. There was a place where the rate was about 40%, and clear tissue heterogeneity was recognized.

【0037】[0037]

【発明の効果】以上のとおり、本発明によれば良好な気
孔性状と優れた材質強度を兼備する高品質の多孔質ガラ
ス状カーボン材を連続的な抄紙および浸漬工程を介して
トラブルなく製造することができる。
As described above, according to the present invention, a high quality porous glassy carbon material having both good porosity and excellent material strength is produced without trouble through a continuous paper making and dipping process. be able to.

【0038】したがって、量産硬化による製造原価の低
減化が図れるため、耐熱耐食性のほかに低コスト化が要
求される燃料電池、二次電池用の部材を製造するために
極めて有効となる。
Accordingly, since the production cost can be reduced by mass production curing, it is extremely effective for producing members for fuel cells and secondary batteries which require cost reduction in addition to heat resistance and corrosion resistance.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】α−セルロースを主成分とする有機物質60
〜90重量部、水溶性抄紙バインダー10〜40重量部および
水不溶性で且つ熱揮散性のバインダー1〜10重量部から
なる原料組成の分散水を連続抄紙してシートに成形し、
該シートを残炭率40%以上の熱硬化性樹脂溶液に連続的
に浸漬したのちロール絞り処理を施し、処理後のシート
を半硬化して積層成形し、成形体を非酸化性雰囲気下で
800℃以上の温度により焼成炭化することを特徴とする
多孔質ガラス状カーボン材の製造方法。
An organic substance comprising α-cellulose as a main component.
~ 90 parts by weight, a water-soluble paper binder 10 to 40 parts by weight and a water-insoluble and heat-vaporizable binder 1 to 10 parts by weight of the dispersed water of the raw material composition to form a sheet by continuous paper making,
The sheet is continuously immersed in a thermosetting resin solution having a residual carbon ratio of 40% or more, and then subjected to roll squeezing treatment. The treated sheet is semi-cured to form a laminate, and the molded body is subjected to a non-oxidizing atmosphere.
A method for producing a porous glassy carbon material, characterized by firing and carbonizing at a temperature of 800 ° C or higher.
JP2405365A 1990-12-06 1990-12-06 Method for producing porous glassy carbon material Expired - Fee Related JP2607397B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2405365A JP2607397B2 (en) 1990-12-06 1990-12-06 Method for producing porous glassy carbon material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2405365A JP2607397B2 (en) 1990-12-06 1990-12-06 Method for producing porous glassy carbon material

Publications (2)

Publication Number Publication Date
JPH04209773A JPH04209773A (en) 1992-07-31
JP2607397B2 true JP2607397B2 (en) 1997-05-07

Family

ID=18514969

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2405365A Expired - Fee Related JP2607397B2 (en) 1990-12-06 1990-12-06 Method for producing porous glassy carbon material

Country Status (1)

Country Link
JP (1) JP2607397B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3514903B2 (en) * 1995-08-03 2004-04-05 帝人テクノプロダクツ株式会社 Fluoro-resin-based sheet, sheet laminated composite, method for producing the same and use thereof

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5318603B2 (en) * 1973-07-10 1978-06-16
JPS6270215A (en) * 1985-09-21 1987-03-31 Showa Denko Kk Production of molded carbon article
JPH0633196B2 (en) * 1988-06-23 1994-05-02 東海カーボン株式会社 Method for producing porous carbon material

Also Published As

Publication number Publication date
JPH04209773A (en) 1992-07-31

Similar Documents

Publication Publication Date Title
CA2347432C (en) Porous carbon electrode substrate and its production method and carbon fiber paper
US4064207A (en) Fibrillar carbon fuel cell electrode substrates and method of manufacture
US4434206A (en) Shaped articles of porous carbon fibers
JPS60122711A (en) Manufacture of porous carbon board
JP3356534B2 (en) Electrolyte holding plate and method for manufacturing the same
JP4187683B2 (en) Porous carbon electrode substrate for fuel cells
JP2607397B2 (en) Method for producing porous glassy carbon material
JP3739819B2 (en) Method for producing porous carbon material
JPH0559867B2 (en)
JP3166983B2 (en) Method for producing tubular porous glassy carbon body
JP3131911B2 (en) Method for producing thick porous carbon material
JPH05194056A (en) Production of porous carbon plate having high compression resistance
JPH03183672A (en) Production of porous carbon material
JPH034508B2 (en)
JP4080095B2 (en) Manufacturing method of thick porous carbon material
JPH0825817B2 (en) Method for producing glassy carbon material
CA2485232C (en) Porous carbon electrode substrate
JPH07220732A (en) Manufacture of porous carbon plate for phosphoric acid fuel cell
JP3183681B2 (en) Method for producing highly conductive porous carbon material
JPH0848577A (en) Production of impermeable carbonaceous formed body
JPH05155672A (en) Porous carbon plate and its production
JPH0524950A (en) Production of porous carbon plate
JPH0517258A (en) Production of porous carbon sheet
JPH08283084A (en) Production of porous carbon plate
JPH01320279A (en) Production of porous carbonaceous material

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080213

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090213

Year of fee payment: 12

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100213

Year of fee payment: 13

LAPS Cancellation because of no payment of annual fees