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JPH0492806A - Production of fine graphite powder - Google Patents

Production of fine graphite powder

Info

Publication number
JPH0492806A
JPH0492806A JP2210796A JP21079690A JPH0492806A JP H0492806 A JPH0492806 A JP H0492806A JP 2210796 A JP2210796 A JP 2210796A JP 21079690 A JP21079690 A JP 21079690A JP H0492806 A JPH0492806 A JP H0492806A
Authority
JP
Japan
Prior art keywords
fiber
carbon
sulfuric acid
graphite powder
fine graphite
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
JP2210796A
Other languages
Japanese (ja)
Other versions
JP3018428B2 (en
Inventor
Hideki Murayama
英樹 村山
Katsuji Honda
本多 勝治
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.)
Mitsubishi Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
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 Mitsubishi Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP2210796A priority Critical patent/JP3018428B2/en
Publication of JPH0492806A publication Critical patent/JPH0492806A/en
Application granted granted Critical
Publication of JP3018428B2 publication Critical patent/JP3018428B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To produce fine graphite powder in which carbon net planes are oriented in one direction by treating specific carbonaceous fiber with a sulfuric acid-containing solution, then quick heating the treated fiber and disintegrating the fiber. CONSTITUTION:With 97-60vol.% concentrated sulfuric acid at 96wt.% concentration, is mixed 3-40vol.% concentrated nitric acid at 68wt.% concentration. Thereby, an acid solution is prepared and then added to ribbon-like carbon fiber having the carbon networks vertically laminated relatively to the longitudinal direction of the fiber, 3.354-3.380Angstrom spacing (d002) thereof, a rectangular or flat elliptical cross section thereof, the major axis of the cross section of >=2 times based on the minor axis, 0.05-0.7mum width and several mum to tens of mum length without any hollow pore parts so as to provide 1-300 ml sulfuric acid based on 1g fiber. The mixture is heated at >=30 deg.C while being stirred to carry out oxidation treatment. The resultant fiber is then filtered, washed with water and dried. The obtained carbon fiber is heated at >=10 deg.C/min rate, kept at >=600 deg.C for >=1sec and then disintegrated.

Description

【発明の詳細な説明】 [発明の属する技術分野] 本発明は、黒鉛微粉に関するもので、より詳しくは炭素
網面が一方向に揃った黒鉛微粉とその製造法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field to which the Invention Pertains] The present invention relates to fine graphite powder, and more particularly to fine graphite powder in which carbon mesh surfaces are aligned in one direction, and a method for producing the same.

[従来の技術] 黒鉛微粉は、電気伝導性、熱伝導性、慴動性、耐熱性、
化学的安定性に優れ、導電性塗剤、工業用潤滑剤、帯電
防止剤、さらには電池材料、放熱材、各種複合用添加剤
などとして広く用いられている。
[Conventional technology] Fine graphite powder has electrical conductivity, thermal conductivity, mobility, heat resistance,
It has excellent chemical stability and is widely used as conductive coatings, industrial lubricants, antistatic agents, battery materials, heat dissipation materials, and additives for various composites.

これらの用途に関して、黒鉛微粉の大きさがlpm以下
であることを要求されることが多い。
For these applications, it is often required that the graphite fine powder has a size of lpm or less.

従来の黒鉛微粉の製造方法としては、天然黒鉛あるいは
人造黒鉛の塊を機械的に粉砕・分級するのが一般的であ
るが、黒鉛は発達した炭素網面が積層した異方性の大き
な材料であって、炭素網面自体は壊れ難く、それに対し
て網面の積層方向に関しては柔らかく、滑り易い性質を
持っており、このような材料を三次元方向のいずれの方
向についても1μm以下に粉砕することは困難である。
The conventional method for producing fine graphite powder is to mechanically crush and classify lumps of natural graphite or artificial graphite, but graphite is a highly anisotropic material made of laminated layers of developed carbon networks. Therefore, the carbon mesh surface itself is difficult to break, but on the other hand, the layered direction of the mesh surface is soft and slippery, and such materials can be crushed to 1 μm or less in any three-dimensional direction. That is difficult.

また、このように機械的粉砕によりlpm以下の微粉と
することは、部分的には可能でも全体として1μm以下
にすることは非常に困難であるうえ、粉砕してこのよう
な微細な黒鉛微粉を得るためには、その粉砕エネルギー
も極めて大きなものを必要となる。
In addition, although it is possible to reduce the particle size to 1 μm or less by mechanical pulverization in some areas, it is very difficult to reduce the particle size to 1 μm or less as a whole. In order to obtain this, an extremely large amount of crushing energy is required.

これを解決するための手段としては、粉砕しやすい炭素
粉末、例えばコークスなどを粉砕したものを黒鉛化する
方法や、もともと粒径1μm以下の炭素微粉であるカー
ボンブラックを熱処理する等の方法が知られている。
As a means to solve this problem, there are known methods such as graphitizing carbon powder that is easy to crush, such as coke, and heat treating carbon black, which is originally a fine carbon powder with a particle size of 1 μm or less. It is being

[発明が解決しようとする課題] しかしながらコークス等を用いる方法では、黒鉛化処理
中に凝集・合体してしまうため所期の目的であるサブミ
クロンオーダーの黒鉛微粉を得ることは難かしい。
[Problems to be Solved by the Invention] However, in the method using coke or the like, it is difficult to obtain submicron-order fine graphite powder, which is the intended purpose, because it aggregates and coalesces during the graphitization process.

一方カーボンブラックを黒鉛化処理する方法でも、黒鉛
化度を高めること自身にも問題があり、さらにコークス
粉砕法と同様に、黒鉛化処理中の凝集・合体の問題があ
る。
On the other hand, even in the method of graphitizing carbon black, increasing the degree of graphitization itself has its own problems, and, like the coke crushing method, there are problems of agglomeration and coalescence during the graphitization process.

またいずれの場合にも、その黒鉛微粉のミクロ構造に着
目して見ると、炭素網面がきれいに積層したグラファイ
ト構造ではなく乱雑な構造となっており、いわゆるグラ
ファイトと呼ばれるときにイメージされる構造とは異な
った構造となっているものが多い。
In both cases, when we focus on the microstructure of the fine graphite powder, we find that it is not a graphite structure in which the carbon network surfaces are neatly layered, but a disordered structure, which is different from the structure that is imagined when we call it graphite. Many have different structures.

さらにいずれの場合も、黒鉛化処理に際しては2000
°C以上の高温で処理する必要があり、取扱性を含めた
装置上の制約の他、生産コストの面からも難点があった
Furthermore, in both cases, 2000
It is necessary to process at a high temperature of .degree. C. or higher, which poses difficulties in terms of production costs as well as limitations in terms of equipment, including ease of handling.

[課題を解決するための手段] そこで本発明者らは、鋭意検討した結果、出発炭素材料
としてもともと微細なグラファイト網面が集まったよう
な構造のものを選んでそれを解砕すれば、上記のような
従来技術では解決が困難であった課題が解決できるばか
りでなく、これまで不可能と考えられていたほぼ理想に
近い形態とミクロ構造を有する黒鉛微粉の製造を可能に
出来ることに思い至り、本発明を完成した。
[Means for Solving the Problem] As a result of intensive study, the inventors of the present invention found that if they selected a starting carbon material with a structure in which fine graphite networks were originally gathered together and crushed it, the above-mentioned results could be achieved. Not only can we solve problems that were difficult to solve with conventional technology, but we are also able to produce graphite fine powder with an almost ideal morphology and microstructure, which was previously thought to be impossible. As a result, the present invention was completed.

すなわち本発明の目的は、粒径がサブミクロンオーダで
、しかもグラファイト網面が一方向に配向したような制
御されたミクロ構造を有するという、これまでにない黒
鉛微粉の製造方法を提供することにある。
That is, an object of the present invention is to provide an unprecedented method for producing fine graphite powder, which has a particle size on the order of submicrons and a controlled microstructure in which the graphite network surface is oriented in one direction. be.

かかる目的は、繊維の長さ方向に対して炭素網面が実質
的に垂直に積層し、その面間距離(d002)が3.3
54〜3.380人であり、かつ実質的に中空孔部を有
さず、繊維の断面が矩形あるいは扁平な楕円様で、断面
の長軸が短軸に対し2倍以上である炭素質繊維に、硫酸
を含有する酸液中で酸化処理を加えた後、急速加熱処理
して解砕することを特徴とする黒鉛微粉の製造方法によ
り容易に達成される。
This purpose is achieved by laminating the carbon mesh planes substantially perpendicularly to the length direction of the fibers, and the distance between the planes (d002) is 3.3.
54 to 3.380, and has substantially no hollow pores, the cross section of the fiber is rectangular or flat oval, and the long axis of the cross section is at least twice as large as the short axis. This can be easily achieved by a method for producing fine graphite powder, which is characterized in that it is subjected to oxidation treatment in an acid solution containing sulfuric acid, and then subjected to rapid heating treatment and crushed.

以下本発明の詳細な説明する。The present invention will be explained in detail below.

本発明で用いる出発炭素材料は、微細なグラファイト網
面が集まったような構造の炭素材料であれば特に限定さ
れるものではないが、グラファイト細面が一次元方向に
積層したミクロ構造を持ったものが望ましい。
The starting carbon material used in the present invention is not particularly limited as long as it has a structure in which fine graphite network planes are assembled, but it has a microstructure in which fine graphite planes are stacked in a one-dimensional direction. is desirable.

このような炭素材料として、例えば本発明者等が特許出
願しているリボン状炭素繊維(特願平1−286673
号)を挙げることができる。
Examples of such carbon materials include ribbon-shaped carbon fibers (patent application No. 1-286673) for which the present inventors have applied for a patent.
(No.).

該炭素繊維は、−酸化炭素を原料として金属超微粒子の
触媒作用により生成する微細な繊維状炭素で、繊維の幅
が0.05〜0.7μm、長さが数〜数十pmであり、
繊維軸に対して炭素網面が一様に垂直に積層するという
非常に特徴的なミクロ構造を有するとともに、比較的低
温で生成するにもかかわらず黒鉛化度が高いものとなっ
ている。
The carbon fibers are fine fibrous carbon produced by the catalytic action of ultrafine metal particles using carbon oxide as a raw material, and have a fiber width of 0.05 to 0.7 μm and a length of several to several tens of pm,
It has a very characteristic microstructure in which the carbon network planes are uniformly stacked perpendicular to the fiber axis, and has a high degree of graphitization even though it is produced at a relatively low temperature.

例えば700°Cの反応により得た繊維のd002(炭
素網面間の距離)は3.366人であり、黒鉛単結晶の
値3.354人に非常に近い値で、MeringとMe
ireの式より計算すると黒鉛化度は86%と見積もら
れる。
For example, the d002 (distance between carbon network planes) of the fiber obtained by the reaction at 700°C is 3.366, which is very close to the value of 3.354 for graphite single crystal, and the value of Mering and Me
The degree of graphitization is estimated to be 86% when calculated from the ire formula.

このように高度な黒鉛化炭素を得るには通常2500〜
3000°Cの熱処理を必要とすることを考えると、異
例の低い温度で直接黒鉛化度の高い繊維が得られている
To obtain such highly graphitized carbon, it is usually 2500~
Considering that heat treatment at 3000°C is required, fibers with a high degree of direct graphitization were obtained at an unusually low temperature.

該繊維状炭素は、−酸化炭素と水素の混合ガス(混合比
1:1)とともに繊維成長の触媒原料として全炭素原子
重量を100として、鉄重量が1〜20になるよう鉄ペ
ンタカルボニルを添加した原料ガスを、550〜800
0Cに設定した電気炉中に設置した反応管に60e /
 hr前後の割合で連続挿入して得ることができる(特
願平1−286673号)。
The fibrous carbon is used together with a mixed gas of carbon oxide and hydrogen (mixing ratio 1:1) as a catalyst raw material for fiber growth. Iron pentacarbonyl is added so that the total carbon atom weight is 100 and the iron weight is 1 to 20. 550 to 800
60e /
It can be obtained by continuous insertion at a rate of around hr (Japanese Patent Application No. 1-286673).

このようにして得たサブミクロンオーター〇グラファイ
トが一次元方向に積層して繊維状になった、黒鉛微粉を
得るための8発物質として理想的なミクロ構造と形態を
有する繊維状炭素を、第一図に示すように解砕すること
によってミクロ構造の制御された黒鉛微粉を得るもので
ある。
Fibrous carbon, which has an ideal microstructure and morphology as a starting material for obtaining fine graphite powder, in which the submicron autograph obtained in this way is laminated in a one-dimensional direction and becomes fibrous, is By crushing as shown in Figure 1, fine graphite powder with a controlled microstructure is obtained.

該炭素繊維を解砕する方法としては、この繊維の高い黒
鉛化性を利用して、よく知られている膨張黒鉛を製造す
る際に用いられる層間にインターカランとして硫酸を挿
入させた後、熱処理する方法により解砕するのが好適で
ある。酸化処理は、硫酸を含有する酸液中にて行なうが
、より好ましくは硫酸と硝酸の混酸であり、好適な硫酸
と硝酸の混合比は市販の濃硫酸(96wt%溶液)と濃
硝酸(68wt%溶液)を用いた場合、容積比で硫酸l
硝酸が97/3〜60 / 40であり、更に好適には
9515〜80/20である。硫酸と該炭素繊維との配
合については、繊維1gに対して酸液中の硫酸として1
〜300m1、より好ましくは10〜200m1用いる
のが望ましく、また温度については30’C以上、より
好ましくは50°C以上で撹拌しながら行なうとよい。
The method for crushing the carbon fibers is to take advantage of the high graphitizability of this fiber and insert sulfuric acid as an intercalan between the layers used in the production of well-known expanded graphite, followed by heat treatment. It is preferable to crush it by a method such as The oxidation treatment is carried out in an acid solution containing sulfuric acid, more preferably a mixed acid of sulfuric acid and nitric acid. % solution), the volume ratio of sulfuric acid l
Nitric acid is 97/3 to 60/40, more preferably 9515 to 80/20. Regarding the blending of sulfuric acid and the carbon fiber, 1 g of sulfuric acid in the acid solution is used for 1 g of fiber.
It is desirable to use up to 300 ml, more preferably 10 to 200 ml, and the temperature is preferably 30°C or higher, more preferably 50°C or higher, with stirring.

該炭素繊維を処理した酸液を大量の水中に投入し、生成
物を濾過し十分に水洗した後乾燥する。
The acid solution treated with the carbon fibers is poured into a large amount of water, and the product is filtered, thoroughly washed with water, and then dried.

この硫酸処理後の該炭素繊維を、少なくとも100C7
分以上、好ましくは100°CI分以上で昇温し、60
0°C以上、より好ましくは800°C以上で少なくと
も1秒以上保持する。
The carbon fiber after this sulfuric acid treatment is at least 100C7
The temperature is raised for at least 100°C minutes, preferably at least 100°C minutes, and
The temperature is maintained at 0°C or higher, preferably 800°C or higher for at least 1 second.

この昇温にあたっては、電気炉ではあまり急激な昇温は
困難であるが、あらかじめ所定温度に加熱しておいた電
気炉の加熱帯域に、低温度領域に保っておいた試料を速
やかに移動させることで行なってもよい。
Although it is difficult to raise the temperature too rapidly in an electric furnace, the sample, which has been kept at a low temperature, is quickly moved to the heating zone of the electric furnace, which has been preheated to a predetermined temperature. You can also do this by

[実施例] 以下に本発明を実施例に基づきさらに詳細に説明するが
本発明はその要旨を越えない限り、実施例に限定される
ものではない。
[Examples] The present invention will be described in more detail below based on Examples, but the present invention is not limited to the Examples unless the gist thereof is exceeded.

実施例1 ノボン状炭素繊維3.02gに濃硫酸と濃硝酸の混酸(
9:1)60mlを加え、撹拌しながら100°Cで3
0分反応させた。これを600m1の純水中に投下し、
よくかき混ぜた後、濾過、水洗して乾燥した。
Example 1 A mixed acid of concentrated sulfuric acid and concentrated nitric acid (
Add 60 ml of 9:1) and heat at 100°C while stirring.
It was allowed to react for 0 minutes. Drop this into 600m1 of pure water,
After stirring well, the mixture was filtered, washed with water, and dried.

あらかじめ1000°Cに加熱しである電気炉中に設置
した石英製反応管の端の、加熱帯域から離れた100°
C以下の位置にこの硫酸処理された該炭素繊維をいれた
石英容器を置き、窒素雰囲気下この容器を速やかに移動
し3分間保持した。
100° away from the heating zone at the end of a quartz reaction tube preheated to 1000°C and placed in an electric furnace.
A quartz container containing the sulfuric acid-treated carbon fibers was placed at a position below C, and the container was quickly moved and held for 3 minutes under a nitrogen atmosphere.

このようにして得られた試料を電子顕微鏡で観察すると
、該炭素繊維が解砕されて黒鉛微粉が生成し、第2図に
示されるようにこの黒鉛微粉は炭素網面が一方向に配向
したような制御されたミクロ構造を有していることが確
認された。
When the sample thus obtained was observed under an electron microscope, the carbon fibers were crushed to produce fine graphite powder, and as shown in Figure 2, the carbon network surface of this fine graphite powder was oriented in one direction. It was confirmed that it has a controlled microstructure.

得られた黒鉛微粉の物性を表1に示す。Table 1 shows the physical properties of the obtained graphite fine powder.

比表面積は、窒素吸着法によって求めた。The specific surface area was determined by the nitrogen adsorption method.

X線回折は、学振法に基づき、シリコン単結晶粉末を内
部標準として用い、ステラプスキャンニング法で測定し
た。
X-ray diffraction was measured by the staircase scanning method based on the Jakushin method using silicon single crystal powder as an internal standard.

表1 (発明の効果) 本発明によれば、黒鉛化度の高い炭素網面が繊維の長さ
方向に対して実質的に垂直に積層した繊維状炭素を硫酸
を含有する酸液で処理し、続いて急速加熱処理して解砕
することにより、炭素網面が一方向に配向したような制
御されたミクロ構造を有するというこれまでにない黒鉛
微粉を比較的低温条件で簡便に製造することができる。
Table 1 (Effects of the Invention) According to the present invention, fibrous carbon in which highly graphitized carbon network surfaces are stacked substantially perpendicularly to the length direction of the fibers is treated with an acid solution containing sulfuric acid. , followed by rapid heating treatment and crushing to easily produce unprecedented graphite fine powder under relatively low temperature conditions, which has a controlled microstructure in which the carbon network surface is oriented in one direction. I can do it.

そして得られた本発明の黒鉛微粉は、導電性塗剤、工業
用潤滑剤、帯電防止剤、さらには電池材料、放熱材、各
種複合利用添加剤などとして広く使用できる。
The obtained graphite fine powder of the present invention can be widely used as a conductive paint, an industrial lubricant, an antistatic agent, a battery material, a heat dissipating material, and various composite additives.

【図面の簡単な説明】[Brief explanation of drawings]

Claims (2)

【特許請求の範囲】[Claims] (1)繊維の長さ方向に対して炭素網面が実質的に垂直
に積層し、その面間距離(d_0_0_2)が3.35
4〜3.380Åであり、かつ実質的に中空孔部を有さ
ず、繊維の断面が矩形あるいは扁平な楕円様で、断面の
長軸が短軸に対し2倍以上である炭素質繊維に、硫酸を
含有する酸液中で酸化処理を加えた後、急速加熱処理し
て解砕することを特徴とする黒鉛微粉の製造方法
(1) The carbon mesh planes are stacked substantially perpendicularly to the length direction of the fibers, and the distance between the planes (d_0_0_2) is 3.35.
4 to 3.380 Å, and has substantially no hollow pores, the cross section of the fiber is rectangular or flat elliptical, and the long axis of the cross section is at least twice as large as the short axis. A method for producing fine graphite powder, which comprises oxidizing it in an acid solution containing sulfuric acid, followed by rapid heating treatment and crushing it.
(2)該酸化処理が、硫酸と硝酸とを含有する混酸液中
で行なわれる請求項1記載の黒鉛微粉の製造方法。
(2) The method for producing fine graphite powder according to claim 1, wherein the oxidation treatment is performed in a mixed acid solution containing sulfuric acid and nitric acid.
JP2210796A 1990-08-09 1990-08-09 Manufacturing method of graphite fine powder Expired - Fee Related JP3018428B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2210796A JP3018428B2 (en) 1990-08-09 1990-08-09 Manufacturing method of graphite fine powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2210796A JP3018428B2 (en) 1990-08-09 1990-08-09 Manufacturing method of graphite fine powder

Publications (2)

Publication Number Publication Date
JPH0492806A true JPH0492806A (en) 1992-03-25
JP3018428B2 JP3018428B2 (en) 2000-03-13

Family

ID=16595279

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2210796A Expired - Fee Related JP3018428B2 (en) 1990-08-09 1990-08-09 Manufacturing method of graphite fine powder

Country Status (1)

Country Link
JP (1) JP3018428B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003147643A (en) * 2001-03-21 2003-05-21 Morinobu Endo Carbon fiber form produced by vapor growth method
JP2003147644A (en) * 2001-03-21 2003-05-21 Morinobu Endo Carbon fiber produced by vapor growth method, composite material and electrically conductive resin each using the same, and method for adjusting length of the same
EP2489632A1 (en) * 2011-02-16 2012-08-22 Grupo Antolin-Ingenieria, S.A. Process for obtaining graphene oxide nanoplates or graphene nanoplates, and the graphene oxide nanoplates thus obtained

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003147643A (en) * 2001-03-21 2003-05-21 Morinobu Endo Carbon fiber form produced by vapor growth method
JP2003147644A (en) * 2001-03-21 2003-05-21 Morinobu Endo Carbon fiber produced by vapor growth method, composite material and electrically conductive resin each using the same, and method for adjusting length of the same
EP2489632A1 (en) * 2011-02-16 2012-08-22 Grupo Antolin-Ingenieria, S.A. Process for obtaining graphene oxide nanoplates or graphene nanoplates, and the graphene oxide nanoplates thus obtained

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