JPH03103375A - Production of cellular carbon grain - Google Patents

Production of cellular carbon grain

Info

Publication number
JPH03103375A
JPH03103375A JP1237668A JP23766889A JPH03103375A JP H03103375 A JPH03103375 A JP H03103375A JP 1237668 A JP1237668 A JP 1237668A JP 23766889 A JP23766889 A JP 23766889A JP H03103375 A JPH03103375 A JP H03103375A
Authority
JP
Japan
Prior art keywords
resin
carbonizable
binder
pulp
solution
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.)
Granted
Application number
JP1237668A
Other languages
Japanese (ja)
Other versions
JPH0672066B2 (en
Inventor
Akira Yamakawa
山川 昭
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 JP1237668A priority Critical patent/JPH0672066B2/en
Publication of JPH03103375A publication Critical patent/JPH03103375A/en
Publication of JPH0672066B2 publication Critical patent/JPH0672066B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

PURPOSE:To obtain cellular carbon grains having a wide pore distribution and excellent bulk density and pore volume characteristics by defibrating wood pulp in a carbonizable resin solution, blending the resultant pulp component with carbon black, granulating the prepared blend using a volatile binder and carbonizable binder, then coating the prepared granulated pellets with a carbonizable binder and calcining the coated pellets. CONSTITUTION:Wood pulp (preferably long fibrous kraft pulp) is subjected to defibration treatment in a carbonizable resin solution, preferably in an aqueous solution of a phenolic resin using a stirrer having a rotating cutter and subsequently dried. The resultant pulp component and carbon black are mixed at (10:90)-(80:20), preferably (20:80)-(70:30) weight ratio and a solution or emulsion of a heat-volatile binder composed of a thermoplastic resin and a carbonizable binder composed of a thermoplastic resin or tar.pitch is added to tumble and granulated the aforementioned mixture. The surfaces of the granulated pellets are then subjected to coating treatment with a resin of the same kind as that of the above-mentioned carbonizable binder, calcined and carbonized to afford cellular carbon grains.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、触媒担体、土壌改良材などとして好適な球形
ペレット状の多孔質炭素粒を製造する方法に関する. 〔従来の技術〕 多孔質炭素粒としては、断熱材を目的としてカーボンブ
ラックペレットの表層部にガラス状カーボンを形威被着
した構造のものが本出願人により開発されている(特開
昭63−190767号公報)。この種カーボンブラッ
ク系の多孔質炭素粒に形戒される細孔分布の状態、細孔
容積、比表面積などの特性は、基材として用いるカーボ
ンブラックの粒子径およびストラクチャ一のグレードに
大きく依存する.例えば、粒組織の平均細孔半径につい
てみると、ストラクチャーの指標となるDBP吸油量の
レベルが同等のカーボンブラックの場合には粒子径の大
きさに応じてかなり正確に変動する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for producing porous carbon particles in the form of spherical pellets suitable as catalyst carriers, soil improvement materials, and the like. [Prior Art] As porous carbon grains, a structure in which glassy carbon is deposited on the surface layer of carbon black pellets has been developed by the present applicant for the purpose of heat insulation (Japanese Patent Laid-Open No. 63 -190767). The characteristics such as the state of pore distribution, pore volume, and specific surface area that are determined by this type of carbon black-based porous carbon particles largely depend on the particle size of the carbon black used as a base material and the grade of the structure. .. For example, when looking at the average pore radius of the grain structure, in the case of carbon blacks having the same level of DBP oil absorption, which is an index of structure, it varies quite accurately depending on the particle size.

しかし、粒子径15〜3000入、DBP吸油160〜
200 1II./100gの特性をもつ通常品種のカ
ーボンブラックを基材としたときの平均細孔半径は、0
.01〜0.1 μ麟という極めて果クロな範囲内でし
か変動しない。
However, particle size 15~3000, DBP oil absorption 160~
200 1II. /100g when using a standard type of carbon black as a base material, the average pore radius is 0.
.. It fluctuates only within a very narrow range of 0.01 to 0.1 μm.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記のような理由で、カーボンブラック単味を基材とし
て形成される多孔質炭素粒は、幅広い細孔分布が要求さ
れる触媒担体や土壌改良材等に対して通用することがで
きない問題点があった。
For the reasons mentioned above, porous carbon particles formed using carbon black as a base material have the problem that they cannot be used as catalyst supports or soil improvement materials that require a wide pore distribution. there were.

したがって、本発明の目的は、カーボンブラックを原料
成分として0.Ol〜100μ―範囲の広い細孔分布を
備え、優れた嵩密度と細孔容積特性を有する多孔質炭素
粒の製造方法を提供するところにある。
Therefore, the object of the present invention is to use carbon black as a raw material component with 0. The object of the present invention is to provide a method for producing porous carbon particles having a wide pore distribution in the range of O1 to 100μ and excellent bulk density and pore volume characteristics.

〔課題を解決するための手段〕[Means to solve the problem]

上記の目的を達或するための本発明による多孔質炭素粒
の製造方法は、木材パルブを炭化性樹脂溶液中で解繊・
乾燥したパルブ成分とカーボンブラックとを配合し、熱
可塑性樹脂からなる熱揮散性バインダーと熱硬化性樹脂
またはタール・ピッチからなる炭化性バイングーを混合
した溶液もしくはエマルジョンを造粒媒体として転動造
粒化し、造粒ベレットの表面を前記炭化性バインダーと
同種の樹脂で被覆処理したのち焼成炭化することを構成
上の特徴とするものである。
In order to achieve the above object, the method for producing porous carbon particles according to the present invention involves defibrating and disintegrating wood pulp in a carbonizing resin solution.
Rolling granulation using a solution or emulsion of a mixture of dried pulp components and carbon black, and a mixture of a thermovolatile binder made of a thermoplastic resin and a carbonizable binder made of a thermosetting resin or tar/pitch as a granulation medium. The structure is characterized in that the surface of the granulated pellet is coated with the same type of resin as the carbonizable binder, and then fired and carbonized.

本発明に用いる木材パルブの種類としては、溶解パルプ
、あるいはサルファイドパルプ、クラフトパルプ、セミ
ヶごカルパルプ、ケごグラウンドパルプ、サーモメカニ
カルパルプ、リファイナリーグラウンドパルブ、砕木パ
ルプ、そのほか藁、麻等のパルプを含む各種の製紙パル
ブを挙げることができるが、特に不純物含有量が少なく
強度の高い長繊維質のクラフトパルブが効果的に使用さ
れる.これら木材パルプは、まず炭化性樹脂溶液中でジ
ューサー5キサーのような回転カッターを有する攪拌装
置で解繊処理し、濾過、乾燥して炭化性樹脂が付着した
解繊パルプ或分を作製するも炭化性樹脂溶液にはフラン
系樹脂を有機溶媒に溶解した溶液などの通用も可能であ
るが、濃度管理および取扱の容易なフェノール樹脂の水
溶液を用いることが望ましい。
Types of wood pulp used in the present invention include dissolving pulp, sulfide pulp, kraft pulp, semi-cage pulp, cage ground pulp, thermomechanical pulp, refinery ground pulp, groundwood pulp, and other pulps such as straw and hemp. Various types of paper pulp can be used, but kraft pulp, which has long fibers and has low impurity content and high strength, is particularly effectively used. These wood pulps are first defibrated in a carbonizing resin solution using a stirrer equipped with a rotary cutter such as a juicer 5 kisser, then filtered and dried to produce defibrated pulp to which the carbonizing resin is attached. Although a solution prepared by dissolving a furan-based resin in an organic solvent can be used as the carbonizable resin solution, it is preferable to use an aqueous solution of a phenol resin, which is easy to control the concentration and handle.

カーボンブランクの適用品種には特に限定を受けること
はなく、通常のファーネスブラック、サーマルブラック
、チャンネルブラック、ランプブランク、アセチレンフ
゛ラックなどから目的とする細孔径の形或に適合する粒
子径およびストラクチャーを備えるものを選択使用する
There are no particular restrictions on the applicable type of carbon blank, and it can be selected from ordinary furnace black, thermal black, channel black, lamp blank, acetylene black, etc., and has a particle size and structure that matches the desired pore size. Select and use.

パルプ成分とカーボンブラックの混合割合は、目的とす
る細孔分布、細孔容積、比表面積などを配慮して定めら
れるが、重量比(P/CB)として10:90〜80 
: 20、特に20 : 80〜7〇二30の範囲に設
定することが好適である。この範囲を越えるパルプ威分
の配合は焼威炭化後における組織の強度低下を招き、ま
たカーボンブラックが前記範囲を上廻る場合には粒強度
は上昇するものの、パルブ添加によるマクロ細孔の形成
が減殺される。
The mixing ratio of the pulp component and carbon black is determined by taking into consideration the desired pore distribution, pore volume, specific surface area, etc., but the weight ratio (P/CB) is 10:90 to 80.
:20, particularly preferably in the range of 20:80 to 70230. Combinations with pulp content exceeding this range will lead to a decrease in the strength of the structure after carbonization, and if carbon black exceeds the above range, grain strength will increase, but the formation of macropores due to the addition of pulp will result. will be reduced.

ついで、パルプ成分とカーボンブラックの配合物は、カ
ーボンブラックのペレット化に常用されているようなビ
ン型造粒機を用いて小球形に転動造粒される。この際、
造粒媒体として熱可塑性樹脂からなる熱揮散性バインダ
ーと熱硬化性樹脂またはタール・ピッチからなる炭化性
六イングーを混合した溶液もしくはエマルジョンを使用
する。
The pulp component and carbon black blend is then tumble granulated into small spheres using a bottle-type granulator, such as those commonly used to pelletize carbon black. On this occasion,
As the granulation medium, a solution or emulsion is used in which a heat-volatile binder made of a thermoplastic resin is mixed with a carbonizable six-ingredient made of a thermosetting resin or tar pitch.

熱可塑性樹脂からなる熱揮散性バインダーとは、後工程
の焼或炭化段階で成分の大部分が分解散失する性質の粘
結材で、樹脂の種類としてはポリビニルアルコール、ボ
リスチレンなどが該当するが本発明の目的にはポリビニ
ルアルコールが効果的に用いられる. また、炭化性バインダーとは後工程の焼成段階で成分の
大部分が炭化残留する性質の粘結材で、フェノール系あ
るいはフラン系の熱硬化性樹脂またはタール・ピッチが
使用される。
A thermovolatile binder made of a thermoplastic resin is a caking material whose components are mostly dissociated and lost during the subsequent sintering or carbonization step, and the types of resin include polyvinyl alcohol, polystyrene, etc. Polyvinyl alcohol is effectively used for the purpose of the invention. Furthermore, the carbonizable binder is a binding material in which most of the components remain carbonized during the subsequent firing stage, and phenolic or furan thermosetting resin or tar pitch is used.

これら熱揮散性バインダーと炭化性バインダーの混合比
率は目的とする細孔組織に応して適宜に設定されるが、
パルプ成分とカーボンブラックの総量に対するバインダ
ー全体の樹脂分としては40重量%以下になるように量
設定することが良好であり、これ以上の添加は円滑な細
孔形戒に対して弊害となる。
The mixing ratio of these heat-volatile binders and carbonizable binders is appropriately set depending on the desired pore structure.
It is best to set the resin content of the entire binder to 40% by weight or less based on the total amount of pulp components and carbon black; addition of more than this will be detrimental to smooth pore formation.

得られた造粒ペレットは乾燥したのち、前記炭化性バイ
ンダーと同種のフェノール系またはフラン系樹脂で被覆
処理を施す。この表面被覆処理は、例えばフェノール樹
脂あるいはフラン樹脂の溶液をカラム中に充填した造粒
ベレット層に散布流下するか、回転円筒管中で造粒ペレ
ットを転動させながら同樹脂溶液を噴霧したのち、加熱
硬化する方法でおこなうことができる。
After the obtained granulated pellets are dried, they are coated with a phenolic or furan resin of the same type as the carbonizable binder. This surface coating treatment can be carried out, for example, by spraying a solution of phenol resin or furan resin onto a layer of granulated pellets filled in a column, or by spraying the same resin solution while rolling the granulated pellets in a rotating cylindrical tube. This can be done by heating and curing.

このようにして表面被覆処理された造粒ベレットは、最
終的に非酸化性雰囲気中で700゜C以上の温度条件に
より焼威して熱揮散性樹脂威分を揮散させるとともに炭
化性樹脂或分を炭化させることにより本発明の多孔質炭
素粒が製造される.〔作 用〕 上記の工程で原材料として配合したパルブ成分は、造粒
段階においてカーボンブラック中に均一に分散して繊維
質骨格を組織し、焼威段階において一部は揮散してボア
形或に寄与し、残部はそのまま炭化して粒強度の保持に
機能する。
The granulated pellets surface-coated in this way are finally burned in a non-oxidizing atmosphere at a temperature of 700°C or higher to volatilize the heat-volatile resin and release the carbonizable resin. The porous carbon grains of the present invention are produced by carbonizing. [Function] The pulp component blended as a raw material in the above process is uniformly dispersed in the carbon black in the granulation stage to form a fibrous skeleton, and in the burning stage, a part of it evaporates and forms a bore shape or The remaining part is carbonized as it is and functions to maintain grain strength.

また、造粒媒体となるバインダーのうち熱揮散性樹脂或
分は、造粒過程において共用する炭化性バインダーとと
もに賦形化を助け、焼成段階では揮敗して主にマクロな
細孔を形或する作用をなす。
In addition, among the binders that serve as the granulation medium, thermovolatile resins or other resins help shape the resin together with the carbonizable binder, which is also used in the granulation process, and volatilizes during the firing stage to mainly form macroscopic pores. It has the effect of

一方、炭化性バインダーを構戒する熱硬化性樹脂は、そ
のまま炭化残留して強固な粒組織を形戒するために機能
する。
On the other hand, the thermosetting resin that binds the carbonizable binder functions to remain carbonized and form a strong grain structure.

さらに造粒ベレットを被覆した炭化性樹脂は炭化して極
めて強固、平滑な表面層を形威し、力一ボンブラック成
分の飛散を防止すると共に、真球形となってハンドリン
グに要求される良好な転流動性を与える. このような機能が複合かつ相乗的に作用して、カーボン
ブラック構造の有する0.01〜0.1 μm範囲のミ
クロ細孔から100μm単位のマクロ細孔に至る広い細
孔分布を有し、低嵩密度、高細孔容積、高比表面積およ
び優れた強度特性を具備する多孔質炭素粒を製造するこ
とが可能となる。
Furthermore, the carbonized resin that coats the granulated pellets carbonizes to form an extremely strong and smooth surface layer, which prevents the scattering of Rikibon black components, and also forms a perfect spherical shape, which is required for good handling. Provides translocation properties. These functions act in a complex and synergistic manner, resulting in carbon black having a wide pore distribution ranging from micropores in the 0.01 to 0.1 μm range to macropores in the 100 μm range, resulting in low It becomes possible to produce porous carbon grains with bulk density, high pore volume, high specific surface area and excellent strength properties.

〔実施例〕〔Example〕

以下、本発明の実施例を比較例と対比して説明する。 Examples of the present invention will be described below in comparison with comparative examples.

実施例1〜5、比較例 木材パルブ(LBKP)をlO%濃度のフェノール樹脂
〔住友デュレズ■製、“スミライトレジンPR − 5
0781″〕水冫容液とともにジューサー亀キサーに投
入し、攪拌して解繊したのち濾過処理した。
Examples 1 to 5, Comparative Example Wood pulp (LBKP) was mixed with 10% phenolic resin [Sumitomo Durez ■, "Sumilight Resin PR-5"
0781″] The mixture was put into a juicer and a water bottle, stirred and defibrated, and then filtered.

これを170゜Cで乾燥後、再びジューサー【キサーに
入れて乾式撹拌して十分に解繊した。
After drying this at 170°C, it was again placed in a juicer and dry stirred to thoroughly defibrate it.

解繊したパルプ或分と、平均粒子径3811#l、よう
素吸着153+eg/g, D B P吸油量133 
iN/100gの特性を有するMAF級ファーネスブラ
ックCB[東清カーボン■製、“シースト116”]を
表1に示す割合で秤量した。
A certain amount of defibrated pulp, average particle size 3811#l, iodine adsorption 153+eg/g, DBP oil absorption 133
MAF grade furnace black CB [manufactured by Tosei Carbon ■, "Sheest 116"] having a characteristic of iN/100g was weighed in the proportions shown in Table 1.

表  1 上記パルプ或分とカーボンブラックを、その総量に対し
、10重量%(樹脂分)に相当する熱揮散性バインダー
となるポリビニルアルコール〔関東化学■製、分子量2
700、ケン化度78〜82モル%〕7%溶液と、同1
0%(樹脂分)に相当する量の炭化性バインダーとなる
フェノール樹脂(住友デュレズ■製、“スミライトレジ
ンPR − 5078 )水冫容冫夜を混合した造粒媒
体と共にピン型造粒機に入れて造粒し、粒径1〜2問の
ものを分級採取して170゜Cで乾燥した. 造粒ベレットを回転ドラムに移し、10rpmで回転さ
せながら炭化性バインダーと同一フェノール樹脂の20
%水溶液を噴霧して表面を均等に湿潤させた。ついで、
表面の樹脂を200℃の温度で加熱硬化してのち、窒素
ガス雰囲気に保持された焼威炉で1000“Cの温度で
焼成炭化した。
Table 1 A certain amount of the above pulp and carbon black were mixed with polyvinyl alcohol (manufactured by Kanto Kagaku ■, molecular weight: 2
700, degree of saponification 78-82 mol%] 7% solution and the same 1
0% (resin content) of a phenolic resin (manufactured by Sumitomo Durez ■, "Sumilight Resin PR-5078"), which becomes a carbonizable binder, was mixed with a granulating medium mixed with a phenol resin (manufactured by Sumitomo Durez ■, "Sumilight Resin PR-5078") in a pin-type granulator. The granulated pellets were separated and collected, and dried at 170°C.The granulated pellets were transferred to a rotating drum, and while rotating at 10 rpm, 20% of the same phenolic resin as the carbonizable binder was added.
% aqueous solution was sprayed to evenly wet the surface. Then,
After the resin on the surface was heated and hardened at a temperature of 200°C, it was fired and carbonized at a temperature of 1000"C in an incinerator maintained in a nitrogen gas atmosphere.

このようにして得られた多孔質炭素粒の各種特性を測定
し、その値を表2に示した。
Various properties of the porous carbon particles thus obtained were measured, and the values are shown in Table 2.

表lの結果から、樹脂処理後の解繊パルプを配合した実
施例による多孔質炭素粒は比較例に比べ、嵩比重、比表
面積、細孔容積などの多孔組織特性が全て改善されてお
り、また熱伝導率も有意に減少していることが認められ
る.なお、実施例の強度特性は比較例より若干低下傾向
にある.この程度の強度低下は実用上問題はないが、パ
ルプ配合比が90の実施例5の場合には強度不足が顕著
となった。
From the results in Table 1, the porous carbon grains according to the examples containing the resin-treated defibrated pulp have all improved porous structure characteristics such as bulk specific gravity, specific surface area, and pore volume, compared to the comparative examples. It is also observed that the thermal conductivity decreases significantly. Note that the strength properties of the examples tend to be slightly lower than those of the comparative examples. Although this degree of decrease in strength is not a practical problem, in the case of Example 5 where the pulp blending ratio was 90, the strength was noticeably insufficient.

〔発明の効果〕〔Effect of the invention〕

以上のとおり、本発明に従えば広範囲の多孔分布を有し
、低密度、高比表面積、高細孔容積の組織でありながら
優れた粒強度を兼ね備えた高性能の多孔質炭素質粒を製
造することができる.したがって、特に幅広い細孔分布
性状が要求される触媒担体、土壌改良材等の用途分野に
有用性が期待される.
As described above, according to the present invention, it is possible to produce high-performance porous carbonaceous grains that have a wide range of porosity distribution, have a structure of low density, high specific surface area, and high pore volume, and have excellent grain strength. be able to. Therefore, it is expected to be particularly useful in applications such as catalyst supports and soil improvement materials, which require a wide range of pore distribution properties.

Claims (1)

【特許請求の範囲】 1、木材パルプを炭化性樹脂溶液中で解繊・乾燥したパ
ルプ成分とカーボンブラックとを配合し、熱可塑性樹脂
からなる熱揮散性バインダーと熱硬化性樹脂またはター
ル・ピッチからなる炭化性バインダーを混合した溶液も
しくはエマルジョンを造粒媒体として転動造粒化し、造
粒ペレットの表面を前記炭化性バインダーと同種の樹脂
で被覆処理したのち焼成炭化することを特徴とする多孔
質炭素粒の製造方法。 2、炭化性樹脂溶液がフェノール樹脂水溶液、熱揮散性
バインダーを構成する熱可塑性樹脂がポリビニルアルコ
ール、そして炭化性バインダーを構成する熱可塑性樹脂
がフェノール樹脂またはフラン樹脂である請求項1記載
の多孔質炭素粒の製造方法。
[Claims] 1. A pulp component obtained by defibrating and drying wood pulp in a carbonizing resin solution is blended with carbon black, and a thermovolatile binder made of a thermoplastic resin and a thermosetting resin or tar pitch are blended. A porous pellet is characterized in that a solution or emulsion mixed with a carbonizable binder consisting of is granulated by rolling as a granulation medium, the surface of the granulated pellets is coated with a resin of the same type as the carbonizable binder, and then fired and carbonized. A method for producing quality carbon grains. 2. The porous material according to claim 1, wherein the carbonizable resin solution is an aqueous phenol resin solution, the thermoplastic resin constituting the heat-volatile binder is polyvinyl alcohol, and the thermoplastic resin constituting the carbonizable binder is a phenol resin or a furan resin. Method for producing carbon grains.
JP1237668A 1989-09-12 1989-09-12 Method for producing porous carbon particles Expired - Lifetime JPH0672066B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1237668A JPH0672066B2 (en) 1989-09-12 1989-09-12 Method for producing porous carbon particles

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1237668A JPH0672066B2 (en) 1989-09-12 1989-09-12 Method for producing porous carbon particles

Publications (2)

Publication Number Publication Date
JPH03103375A true JPH03103375A (en) 1991-04-30
JPH0672066B2 JPH0672066B2 (en) 1994-09-14

Family

ID=17018737

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1237668A Expired - Lifetime JPH0672066B2 (en) 1989-09-12 1989-09-12 Method for producing porous carbon particles

Country Status (1)

Country Link
JP (1) JPH0672066B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100440592B1 (en) * 2001-06-08 2004-07-15 이화형 Method of the manufacture for porous carbon material by molded products with thermosetting resin impregnation of fibrous element from fibrous plant material
JP2010285470A (en) * 2009-06-09 2010-12-24 Sumitomo Rubber Ind Ltd Manufacturing method for rubber composition
JP2011001478A (en) * 2009-06-19 2011-01-06 Tigers Polymer Corp Highly electroconductive fluororubber composition containing carbon black

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102292684B1 (en) * 2019-09-25 2021-08-24 대우조선해양 주식회사 Foul release type paint composition and antifouling coating film formed using same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5441296A (en) * 1977-09-07 1979-04-02 Mitsubishi Chem Ind Ltd Production of porous carbon particles
JPS57145017A (en) * 1981-02-26 1982-09-07 Mitsubishi Chem Ind Ltd Preparation of porous carbonaceous particle
JPS6112918A (en) * 1984-06-25 1986-01-21 Oji Paper Co Ltd Production of porous carbon plate

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5441296A (en) * 1977-09-07 1979-04-02 Mitsubishi Chem Ind Ltd Production of porous carbon particles
JPS57145017A (en) * 1981-02-26 1982-09-07 Mitsubishi Chem Ind Ltd Preparation of porous carbonaceous particle
JPS6112918A (en) * 1984-06-25 1986-01-21 Oji Paper Co Ltd Production of porous carbon plate

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100440592B1 (en) * 2001-06-08 2004-07-15 이화형 Method of the manufacture for porous carbon material by molded products with thermosetting resin impregnation of fibrous element from fibrous plant material
JP2010285470A (en) * 2009-06-09 2010-12-24 Sumitomo Rubber Ind Ltd Manufacturing method for rubber composition
JP2011001478A (en) * 2009-06-19 2011-01-06 Tigers Polymer Corp Highly electroconductive fluororubber composition containing carbon black

Also Published As

Publication number Publication date
JPH0672066B2 (en) 1994-09-14

Similar Documents

Publication Publication Date Title
JP3611600B2 (en) Method for producing activated carbon
EP0484176B1 (en) Packing material for liquid chromatography and method of manufacturing thereof
DE2202174C3 (en) Process for making microspherical carbon particles
JPH0566886B2 (en)
EP0276563B1 (en) Carbonaceous granular heat insulator and process for preparing the same
JPH03103375A (en) Production of cellular carbon grain
DE19538373A1 (en) Process for the production of spherical activated carbon and its use
JP2595296B2 (en) Vapor-grown carbon fiber granulated material
JP5303698B2 (en) Carbide manufacturing method and carbide
KR102181924B1 (en) Method for manufacturing high-efficiency activated carbon for removal of harmful gas using nano metal powder
US5447624A (en) Packings for liquid chromatography and process for producing the same
JPH03215307A (en) Production of porous sic whisker pellet
JPS6320762B2 (en)
Monika et al. Porous structure improvement of coal activated carbon using steam activation in pilot scale
RU2174949C1 (en) Method of preparing activated carbon
JPH01294573A (en) Production of heat-insulating carbonaceous structure
KR100286662B1 (en) Method for manufacturing activated carbon by using waste paper and pulp residue
JPS6096516A (en) Molded article of active carbon
JPH085722B2 (en) Molded insulation manufacturing method
JP2700354B2 (en) Method for producing packing material for liquid chromatography
JP3006918B2 (en) Carrier for gas chromatography using aggregated carbon particles and method for producing the same
JPS6252115A (en) Production of spherical carbonized material and activated carbon
RU2602264C1 (en) Method of producing activated carbon
CN110407602A (en) Conductive honeycomb silicon carbide and preparation method thereof
JPH066515B2 (en) Method for producing porous carbon tubular body