JP2759837B2 - Manufacturing method of carbon material - Google Patents
Manufacturing method of carbon materialInfo
- Publication number
- JP2759837B2 JP2759837B2 JP2088247A JP8824790A JP2759837B2 JP 2759837 B2 JP2759837 B2 JP 2759837B2 JP 2088247 A JP2088247 A JP 2088247A JP 8824790 A JP8824790 A JP 8824790A JP 2759837 B2 JP2759837 B2 JP 2759837B2
- Authority
- JP
- Japan
- Prior art keywords
- carbon material
- phenol resin
- resin
- phenolic resin
- strength
- 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
Links
Landscapes
- Ceramic Products (AREA)
- Carbon And Carbon Compounds (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] 本発明はきわめて均一な孔径の空孔を有するポーラス
状のものから、緻密でかつ高強度なものまで多様な炭素
材料を得ることができる製造方法に関し、さらに詳しく
は濾過材料、ガラス工業における治具、型材料、などと
して有用な、黒鉛質または炭素質の炭素材料の製造方法
に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention is capable of producing a variety of carbon materials from a porous material having pores with a very uniform pore size to a dense and high-strength material. More particularly, the present invention relates to a method for producing a graphitic or carbonaceous carbon material useful as a filter material, a jig in the glass industry, a mold material, and the like.
[従来の技術および発明が解決しようとする課題] 従来、濾過材料などに使用されるポーラス状炭素材料
は炭素粉末、黒鉛粉末に熱硬化性樹脂、ピッチ、タール
などをバインダーとして混合し、成形、焼成したものが
用いられてきた。これらの材料は孔径が不均一で、ま
た、きわめて脆いものしか得られないので、上記のほか
に炭素繊維などを強化材として混入する方法も提案され
てきた。[Problems to be Solved by Conventional Techniques and Inventions] Conventionally, porous carbon materials used for filtration materials and the like are prepared by mixing a carbon powder, graphite powder with a thermosetting resin, pitch, tar, etc. as a binder, molding, Fired ones have been used. Since these materials have a nonuniform pore size and can be obtained only in a very brittle form, a method of mixing carbon fiber or the like as a reinforcing material has been proposed in addition to the above.
しかしながら、未だ十分均一な孔径のものは得られて
いない。However, a sufficiently uniform pore size has not yet been obtained.
一方、緻密で高強度な炭素材料としては、コークス微
粉などを原料とし、高炭化率のピッチ等をバインダーと
して、ラパープレスなどにより成形し、焼成したもの、
あるいは特殊な熱硬化性樹脂を成形、硬化、炭化したガ
ラス状炭素が知られている。これらの材料は、前者にお
いては大規模な設備が必要であり、また後者においては
焼成時変形や割れが生じやすく、大型のものが得られな
いなど各々製造上の不都合があった。On the other hand, as a dense and high-strength carbon material, a material obtained by using a coke fine powder or the like as a raw material, using a pitch or the like having a high carbonization ratio as a binder, molding by a rapper press or the like, and firing,
Alternatively, glassy carbon obtained by molding, curing, and carbonizing a special thermosetting resin is known. The former requires large-scale equipment in the former, and the latter is liable to be deformed or cracked during firing, resulting in inconvenience in production such that large-sized ones cannot be obtained.
本発明は上記従来技術の問題を解決し、きわめて均一
な孔径の空孔を有し、かつ高強度なポーラス状のものか
ら、緻密でかつ高強度なものまでの多様な炭素材料をき
わめて簡易な工程で得ることを目的とする。The present invention solves the above-mentioned problems of the prior art, has pores with a very uniform pore size, and from a high-strength porous material to a dense and high-strength carbon material, can be produced in a very simple manner. It is intended to obtain in the process.
[課題を解決するための手段] 本発明者等は鋭意研究の結果、不溶融性フエノール樹
脂と溶融性フエノール樹脂とをメカノケミカル法により
結合したのち、成形、焼成することにより上記目的を達
成できることを見い出した。[Means for Solving the Problems] As a result of earnest studies, the present inventors have found that the above object can be achieved by combining an infusible phenol resin and a fusible phenol resin by a mechanochemical method, followed by molding and firing. I found
すなわち、本発明は粉末状または球状の不溶融性フエ
ノール樹脂と粉末状または球状の溶融性フエノール樹脂
とをメカノケミカル法により乾式混合して、前記不溶融
性フエノール樹脂の表面を該溶融性フエノール樹脂で被
覆したのち、加圧下で成形、硬化し、ついで焼成、炭化
することを特徴とする炭素材料の製造方法にある。That is, the present invention dry-mixes a powdery or spherical insoluble phenolic resin and a powdery or spherically meltable phenolic resin by a mechanochemical method, and cleans the surface of the insoluble phenolic resin with the meltable phenolic resin. , And then molded and cured under pressure, and then calcined and carbonized.
本発明の製造方法において用いられる、粉末状または
球状の不溶融性フエノール樹脂は、たとえばユニベック
スCタイプまたはCXタイプ(ユニチカ(株)の商品
名)、ベルパールRタイプ(鐘紡(株)の商品名)など
に代表されるものを使用することが好ましい。また、溶
融性フエノール樹脂は、たとえばユニベックスSタイプ
またはNタイプ(ユニチカ(株)の商品名)、ベルパー
ルSタイプ(鐘紡(株)の商品名)などに代表されるも
のを使用することが好ましい。The powdery or spherical insoluble phenol resin used in the production method of the present invention is, for example, Univex C type or CX type (trade name of Unitika), Bellpearl R type (trade name of Kanebo Co., Ltd.) It is preferable to use one represented by, for example. Further, as the meltable phenol resin, it is preferable to use, for example, those represented by Univex S type or N type (trade name of Unitika), Bell Pearl S type (trade name of Kanebo Corp.) and the like.
不溶性フエノール樹脂の粒直径は、緻密な炭素材料を
得るには1〜10μm未満、ポーラスな炭素材料を得るに
は10mμ〜1mmのものが好ましく、これに溶融性フエノー
ル樹脂を緻密な炭素材料を得る場合、20〜30重量%、ポ
ーラスな炭素材料を得る場合、5〜10重量%の割合で添
加して、メカノケミカル法により乾式混合を行う。この
場合、溶融性フエノール樹脂は不溶融性フエノール樹脂
と同程度の粒直径のものが好ましく、また、メカノケミ
カル反応は擂潰機を用い、乳棒を乳鉢に押し付ける圧力
を0.2〜2.0kg/cm2、乳棒の回転数/乳鉢の回転数を1/1
〜20/1、混合物の層の厚さを0.2〜3.0mmとすると効率良
く乾式混合できるので好ましい。1バッチを1〜7kgで
混合する場合、混合時間は1〜5時間でよい。The particle diameter of the insoluble phenol resin is preferably from 1 to less than 10 μm to obtain a dense carbon material, and preferably from 10 mμ to 1 mm to obtain a porous carbon material, and the meltable phenol resin is used to obtain a dense carbon material. In this case, when a porous carbon material is obtained at 20 to 30% by weight, a porous carbon material is added at a ratio of 5 to 10% by weight, and dry mixing is performed by a mechanochemical method. In this case, the fusible phenolic resin is preferably of the same particle diameter as the infusible phenolic resin, and the mechanochemical reaction uses a crusher, and the pressure for pressing the pestle against the mortar is 0.2 to 2.0 kg / cm 2. , Pestle rotation speed / mortar rotation speed 1/1
It is preferable that the thickness of the layer of the mixture is 0.2 to 3.0 mm, because dry mixing can be performed efficiently. When mixing 1 batch at 1 to 7 kg, the mixing time may be 1 to 5 hours.
次に、この混合物を成形型に充填し、10〜1500kg/cm2
の加圧下100〜200℃で1〜5時間保持して成形、硬化し
たのち1000℃〜3000℃まで焼成、炭化する。この際の昇
温速度は2〜200℃/hrが好ましい。Next, the mixture is filled into a mold, and 10 to 1500 kg / cm 2
After being molded and cured by holding at 100 to 200 ° C. under pressure for 1 to 5 hours, it is fired and carbonized to 1000 to 3000 ° C. The rate of temperature rise at this time is preferably from 2 to 200 ° C./hr.
上記成形圧は緻密な炭素材料を得る場合、特に100kg/
cm2以上とするのが好ましいが、ポーラスな炭素材料を
得る場合、不溶性フエノール樹脂の粒直径、溶融性フエ
ノール樹脂の添加量により上記範囲内で適宜調節するの
が好ましい。The above molding pressure is 100 kg /
It is preferably at least cm 2, but when a porous carbon material is obtained, it is preferable to appropriately adjust the particle diameter of the insoluble phenol resin and the amount of the meltable phenol resin within the above range.
上記本発明の製造方法によって、ヘリウムガス透過率
5.0×10-3〜1.0×10-10cm/sec、曲げ強さ750〜1200kg/c
m2の高強度で、かつ緻密性を有する炭素材料および空孔
率10〜40%で、曲げ強さ200〜550kg/cm2の高強度ポーラ
ス性炭素材料を得ることが可能である。According to the production method of the present invention, the helium gas permeability
5.0 × 10 -3 to 1.0 × 10 -10 cm / sec, bending strength 750 to 1200 kg / c
It is possible to obtain a high-strength and dense carbon material having a m 2 strength and a high-strength porous carbon material having a porosity of 10 to 40% and a bending strength of 200 to 550 kg / cm 2 .
[実施例] 以下、実施例および比較例に基づいて、本発明をより
具体的に説明する。EXAMPLES Hereinafter, the present invention will be described more specifically based on examples and comparative examples.
実施例1 平均粒直径5μmの球状の不溶融性フエノール樹脂
(ユニチカ(株)製、商品名 ユニベックスCX−10)10
00gと平均粒直径20μmの溶融性フエノール樹脂(鐘紡
(株)製、商品名ベルパールS−890)300gとを擂潰機
で乳棒を乳鉢に押し付ける圧力を1.2kg/cm2とし、乳棒
の回転数/乳鉢の回転数を3/1、混合物の層の厚さを0.5
mmとして、2時間混合して表面に溶融性フエノール樹脂
をコートした不溶融性フエノール樹脂球を得た。Example 1 Spherical infusible phenol resin having an average particle diameter of 5 μm (product name: UNIVEX CX-10, manufactured by Unitika Ltd.) 10
The pressure at which a pestle was pressed against a mortar with a mortar was set at 1.2 kg / cm 2 with 00 g and 300 g of a meltable phenol resin having an average particle diameter of 20 μm (manufactured by Kanebo Co., Ltd., trade name: Bellpearl S-890). / Mortar rotation speed 3/1, mixture layer thickness 0.5
mm, and mixed for 2 hours to obtain an infusible phenol resin ball whose surface was coated with a fusible phenol resin.
次に、この樹脂球を金型に充填し、200kg/cm2の加圧
下、150℃で1時間保持して成形し、厚み5×220×250m
mの寸法の成形体を得た。この成形体を窒素雰囲気下で1
0℃×hrで1000℃まで加熱し、焼成して炭素材料を得
た。この炭素材料は、緻密でクラックなどもなく、ヘリ
ウムガス透過率は1.2×10-8cm2/secであり、かつ、曲げ
強さは1020kg/cm2であった。Next, this resin ball was filled in a mold, and was molded by holding at 150 ° C. for 1 hour under a pressure of 200 kg / cm 2 to have a thickness of 5 × 220 × 250 m
A molded product having a size of m was obtained. This molded body is placed under a nitrogen atmosphere for 1 hour.
The material was heated to 1000 ° C. at 0 ° C. × hr and calcined to obtain a carbon material. This carbon material was dense and free from cracks, had a helium gas permeability of 1.2 × 10 −8 cm 2 / sec, and a bending strength of 1020 kg / cm 2 .
比較例 1 実施例1で使用したと同一の不溶融性フエノール樹脂
1000gと溶融性フエノール樹脂300gとをV型混合機によ
り2時間混合した以外は、実施例1と同一の条件で炭素
材料得た。しかしながら、得られた炭素材料は多数のク
ラックが認められ、強度測定用の試験片を得ることもで
きなかた。Comparative Example 1 The same infusible phenolic resin as used in Example 1
A carbon material was obtained under the same conditions as in Example 1 except that 1000 g and 300 g of the meltable phenol resin were mixed by a V-type mixer for 2 hours. However, many cracks were observed in the obtained carbon material, and a test piece for measuring the strength could not be obtained.
実施例2〜5 実施例1で使用したと同一の不溶融性フエノール樹脂
1000gと溶融性フエノール樹脂250gとを乳棒を乳鉢に押
し付ける圧力を数々変えて混合した以外は実施例1と同
一条件で炭素材料を得た。その特性を第一表に示す。Examples 2-5 Same infusible phenolic resin as used in Example 1
A carbon material was obtained under the same conditions as in Example 1 except that 1000 g and 250 g of the meltable phenol resin were mixed under various pressures for pressing a pestle into a mortar. The characteristics are shown in Table 1.
実施例6 平均粒直径250μmの球状の不溶融性フエノール樹脂
(ユニチカ(株)製、商品名 ユニベックスC−200)1
000gと平均粒直径20μmの溶融性フエノール樹脂(鐘紡
(株)製、商品名 ベルパールS−890)100gとを擂潰
機で乳棒を乳鉢に押し付ける圧力を1.5kg/cm2とし、乳
棒の回転数/乳鉢の回転数を5/1,混合物の層の厚さ1.2m
mとして3時間混合して表面に溶融性フエノール樹脂を
コートした不溶融性フエノール樹脂球を得た。次に、こ
の樹脂球を金型に充填し、80kg/cm2の加圧下150℃で1
時間保持して、厚み10×200×200mmの寸法の成形体を得
た。この成形体を窒素雰囲気下で100℃/hrで1200℃まで
加熱、焼成して炭素材料を得た。この炭素材料は空孔率
35%のポーラスなものであったが、曲げ強さは250kg/cm
2と高強度であった。また、この孔径の分布を水銀ポロ
シメーターで測定したところ、20〜40μmの範囲に孔径
の約90%が集中しており、きわめて均一な孔を有するも
のであった。 Example 6 Spherical infusible phenolic resin having an average particle diameter of 250 μm (product name: UNIVEX C-200, manufactured by Unitika Ltd.) 1
The pressure at which a pestle is pressed against a mortar with a crusher of 000 g and 100 g of a meltable phenol resin having an average particle diameter of 20 μm (manufactured by Kanebo Co., Ltd., trade name: Bellpearl S-890) is 1.5 kg / cm 2, and the rotation speed of the pestle / Mortar rotation speed 5/1, mixture layer thickness 1.2m
The mixture was mixed for 3 hours as m to obtain an infusible phenol resin ball whose surface was coated with a fusible phenol resin. Next, the resin ball is filled in a mold, and pressed at 150 ° C under a pressure of 80 kg / cm 2.
After holding for a time, a molded product having a size of 10 × 200 × 200 mm was obtained. This molded body was heated and fired at 1200 ° C. at 100 ° C./hr in a nitrogen atmosphere to obtain a carbon material. This carbon material has a porosity
Although it was 35% porous, the flexural strength was 250kg / cm
2 and high strength. When the pore size distribution was measured with a mercury porosimeter, about 90% of the pore size was concentrated in the range of 20 to 40 μm, and the pores were extremely uniform.
比較例 2 実施例6で使用したと同一の不溶融性フエノール樹脂
1000gと溶融性フエノール樹脂100gとをリボンミキサー
で3時間混合した以外は、実施例6と同一の条件で炭素
材料を得た。得られた炭素材料は空孔率38%のポーラス
なもので、曲げ強さは65kg/cm2と低く、しかも孔径分布
10〜100μmとは著しく広いものであった。Comparative Example 2 Same infusible phenolic resin as used in Example 6
A carbon material was obtained under the same conditions as in Example 6, except that 1000 g and 100 g of the meltable phenol resin were mixed for 3 hours using a ribbon mixer. The obtained carbon material is porous with a porosity of 38%, the bending strength is as low as 65 kg / cm 2 , and the pore size distribution
It was remarkably wide, 10 to 100 μm.
[発明の効果] 上記実施例からも明らかなように、本発明の方法によ
れば緻密な炭素材料からポーラスな炭素材料まで簡易な
工程で容易に得ることができ、かつ得られた炭素材料
は、きわめて高強度なものとなる。[Effects of the Invention] As is clear from the above examples, according to the method of the present invention, a dense carbon material to a porous carbon material can be easily obtained in a simple step, and the obtained carbon material is , Resulting in extremely high strength.
従って、本発明は炭素材料の製造法として工業上極め
て有用なものである。Therefore, the present invention is industrially extremely useful as a method for producing a carbon material.
Claims (2)
脂と、粉末状または球状の溶融性フェノール樹脂とをメ
カノケミカル法により乾式混合して、前記不溶融性フェ
ノール樹脂の表面を該溶融性フェノール樹脂で被覆した
のち加圧下で成形、硬化し、ついで、焼成、炭化するこ
とを特徴とする炭素材料の製造方法。1. A powdery or spherical insoluble phenolic resin and a powdery or spherical insoluble phenolic resin are dry-mixed by a mechanochemical method, and the surface of the insoluble phenolic resin is melted. A method for producing a carbon material, which comprises coating with a resin, molding and curing under pressure, and then firing and carbonizing.
ノール樹脂との乾式混合が、擂潰機によって0.2〜2.0kg
/cm2の加圧下で行うことを特徴とする請求項1に記載の
炭素材料の製造方法。2. The dry-mixing of the non-melting phenol resin and the melting phenol resin is carried out by a grinder in an amount of 0.2 to 2.0 kg.
2. The method for producing a carbon material according to claim 1, wherein the method is performed under a pressure of / cm 2 .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2088247A JP2759837B2 (en) | 1990-04-04 | 1990-04-04 | Manufacturing method of carbon material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2088247A JP2759837B2 (en) | 1990-04-04 | 1990-04-04 | Manufacturing method of carbon material |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03290362A JPH03290362A (en) | 1991-12-20 |
JP2759837B2 true JP2759837B2 (en) | 1998-05-28 |
Family
ID=13937526
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2088247A Expired - Fee Related JP2759837B2 (en) | 1990-04-04 | 1990-04-04 | Manufacturing method of carbon material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2759837B2 (en) |
-
1990
- 1990-04-04 JP JP2088247A patent/JP2759837B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH03290362A (en) | 1991-12-20 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2938807A (en) | Method of making refractory bodies | |
CA1226304A (en) | Sintered silicon carbide/graphite/carbon composite ceramic body having ultrafine grain microstructure | |
JPH0768066B2 (en) | Heat resistant composite and method for producing the same | |
US4293533A (en) | Method for producing solid carbon material having high flexural strength | |
US4579699A (en) | Method for making α-Si3 N4 whiskers and articles therefrom | |
US4385020A (en) | Method for making shaped silicon-silicon carbide refractories | |
US3459566A (en) | Process for producing silicon carbide articles employing pyromellitic dianhydride-limonene dioxide mixture | |
JP2735151B2 (en) | Method for producing fiber-reinforced silicon carbide composite ceramics molded body | |
JPH0251863B2 (en) | ||
JPS6327305B2 (en) | ||
EP0178753B1 (en) | Process for producing a sintered silicon carbide/carbon composite ceramic body having ultrafine grain microstructure | |
US5783255A (en) | Method for producing shaped article of silicon carbide | |
JP2759837B2 (en) | Manufacturing method of carbon material | |
JP2879675B1 (en) | Method for producing two-dimensional fiber reinforced silicon carbide / carbon composite ceramics | |
EP0257134A1 (en) | A method for producing high-density sintered silicon carbide articles | |
KR100213315B1 (en) | Manufacturing method of carbon-sintered body | |
US4788168A (en) | Method for producing carbon-ceramic composite material | |
JPH0848509A (en) | Production of carbonaceous porous body | |
JP3314383B2 (en) | Method for producing carbon fiber / carbon composite material | |
JP2697482B2 (en) | Method for producing pitch-based material and method for producing carbon material using the same as raw material | |
JPH03197360A (en) | Production of carbon fiber-reinforced carbon material | |
JPH07215775A (en) | Production of carbon-carbon composite material | |
JPH08119741A (en) | Carbon-boron carbide sintered compact and carbon-boron carbide-silicon carbide sintered compact | |
JPH0456789B2 (en) | ||
JPS62270464A (en) | Manufacture of carbon fiber reinforced carbon composite material |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090320 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090320 Year of fee payment: 11 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20100320 Year of fee payment: 12 |
|
LAPS | Cancellation because of no payment of annual fees |