JPH0645446B2 - Method for producing high-purity graphite fine powder - Google Patents
Method for producing high-purity graphite fine powderInfo
- Publication number
- JPH0645446B2 JPH0645446B2 JP63233968A JP23396888A JPH0645446B2 JP H0645446 B2 JPH0645446 B2 JP H0645446B2 JP 63233968 A JP63233968 A JP 63233968A JP 23396888 A JP23396888 A JP 23396888A JP H0645446 B2 JPH0645446 B2 JP H0645446B2
- Authority
- JP
- Japan
- Prior art keywords
- graphite
- fine powder
- purity graphite
- purity
- particle size
- 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 - Lifetime
Links
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- 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、50ppm以下の不純物含有量を有する高純度黒
鉛微粉の製造方法に関する。TECHNICAL FIELD The present invention relates to a method for producing high-purity fine graphite powder having an impurity content of 50 ppm or less.
黒鉛の微粉末は潤滑材、導電フィラーなどとして古くか
ら汎用されているが、近時、エレクトロニクスあるいは
原子力等の分野に適用されるに至り不純物含有量50ppm
以下の高純度性を有する黒鉛微粉の要求が高まってい
る。Fine graphite powder has been widely used for a long time as a lubricant, conductive filler, etc., but recently it has come to be applied to fields such as electronics and nuclear power, and the impurity content is 50 ppm.
The demand for the following fine graphite powder having high purity is increasing.
従来、この要求に対する高純度黒鉛微粉の製造手段とし
ては、黒鉛素材を粉砕および高温ハロゲンガス処理する
方法が採用されており、以下のような具体的プロセスの
ものが知られている。Conventionally, a method of pulverizing a graphite material and treating it with a high-temperature halogen gas has been adopted as a means for producing high-purity graphite fine powder to meet this requirement, and the following specific processes are known.
(1)黒鉛素材を脱灰処理炉に填めて炉内に塩素、フレオ
ン等のハログン含有ガスを送入しながら加熱する高純度
化処理(以下、「高温ハロゲンガス処理」という。)を
施したのち、ハンマークラッシャーのような粉砕機を用
いて粗粉砕し、更にアトマイザー等で微粉砕する。(1) A graphite material was placed in a deashing treatment furnace and subjected to a high-purification treatment (hereinafter referred to as “high-temperature halogen gas treatment”) in which chlorine-containing gas such as freon was heated while being fed into the furnace. After that, coarse pulverization is performed using a pulverizer such as a hammer crusher, and then fine pulverization is performed using an atomizer or the like.
(2)黒鉛素材を最初に上記と同様の手段を用いて粗粉砕
および微粉砕したのち、黒鉛容器に充填して高温ハロゲ
ンガス処理をおこなう。(2) The graphite material is first roughly pulverized and finely pulverized by the same means as described above, and then filled in a graphite container and subjected to high temperature halogen gas treatment.
これらのプロセスにおいて、「黒鉛素材」とは粒度数10
mm程度のブロック材、「粗粉砕」とは数mmから数100μ
mの粒径を有する粉粒体までの粉砕、そして「微粉砕」
とは平均粒径1μm以下の粒度に粉砕することを指す。In these processes, "graphite material" means a particle size of 10
mm block material, "coarse crushing" means several mm to several 100μ
Grinding to a granule with a particle size of m, and "fine grinding"
Means to pulverize to an average particle size of 1 μm or less.
上記従来技術のうち、(1)のプロセスはブロック状の
黒鉛素材をそのままの状態で高温ハロゲンガス処理する
ことができる関係で効率的かつ安価に高純度化(不純物
含有量50ppm以下)することができる利点がある。とこ
ろが、次の粗粉砕および微粉砕の工程においてハンマー
クラッシャーやアトマイザーの摩耗による汚染現象によ
って目標とする高純度黒鉛粉が得られなくなる欠点があ
る。Among the above-mentioned conventional techniques, the process (1) can efficiently and inexpensively purify (impurity content 50 ppm or less) because the block-shaped graphite material can be treated with a high-temperature halogen gas as it is. There are advantages. However, there is a drawback that the target high-purity graphite powder cannot be obtained due to a contamination phenomenon due to wear of a hammer crusher or an atomizer in the subsequent coarse pulverization and fine pulverization steps.
また、(2)のプロセスの場合には汚染を伴う粗粉砕お
よび微粉砕工程を前段でおこなうため、次工程の高温ハ
ロゲンガス処理により目標水準を越える高純度黒鉛粉を
得ることができる。しかしながら、微粉砕後の黒鉛微粉
は極めて嵩高くてハンドリングしにくいうえに、高温ハ
ロゲンガス処理時、黒鉛容器に入る充填量が少なくなる
等の問題点がある。Further, in the case of the process (2), the coarse pulverization and fine pulverization steps accompanied by contamination are performed in the preceding stage, so that high-purity graphite powder exceeding the target level can be obtained by the high temperature halogen gas treatment in the next step. However, the finely pulverized graphite powder is extremely bulky and difficult to handle, and there is a problem that the amount of filling into the graphite container becomes small during the high temperature halogen gas treatment.
本発明は、これらの問題点を解消するためになされもの
で、不純物含有量50ppm以下の高純度黒鉛微粉を効率よ
く製造する方法を提供するものである。The present invention has been made in order to solve these problems, and provides a method for efficiently producing high-purity graphite fine powder having an impurity content of 50 ppm or less.
すなわち、本発明による高純度黒鉛微粉の製造方法は、
黒鉛素材を粉砕および高温ハロゲンガス処理によって高
純度黒鉛微粉に転化する方法において、黒鉛素材を粒度
数mm以下に粗粉砕する第1工程、該粗粉砕物を高温ハロ
ゲンガスにより高純度化処理する第2工程、高純度化処
理後の粗粉砕物にエタノールを添加してジェットミル粉
砕により平均粒径1μm以下に微粉化する第3工程とか
らなることを構成上の特徴とする。That is, the method for producing high-purity graphite fine powder according to the present invention,
In the method of converting graphite material into high-purity graphite fine powder by pulverization and high-temperature halogen gas treatment, the first step of coarsely pulverizing the graphite material to a particle size of several mm or less, the first step of high-purifying the coarse-pulverized material with high-temperature halogen gas The constitutional feature is composed of two steps, that is, a third step of adding ethanol to the coarsely pulverized product after the high-purification treatment and pulverizing by jet mill pulverization to an average particle size of 1 μm or less.
原料となる黒鉛素材としては、通常の製法手段により得
られる人造黒鉛のブロック材が用いられるが、例えば電
気製鋼用の大型黒鉛電極を製造する過程で発生する黒鉛
化品の残材あるいは加工屑などの廃物材を利用してもか
まわない。これら黒鉛素材の粗粉砕は、ハンマークラッ
シャーのような常用の粗粉砕機を用い、粒径数mmから数
100μmのサイズに粉砕する(第1工程)。As the graphite material used as a raw material, a block material of artificial graphite obtained by a usual manufacturing method is used, but for example, a residual material or a processing waste of a graphitized product generated in the process of manufacturing a large graphite electrode for electric steelmaking. You may use the waste materials of. For coarse crushing of these graphite materials, use a conventional coarse crusher such as a hammer crusher, and use a particle size of several mm to several mm.
Grind to a size of 100 μm (first step).
粗粉砕物は高純度黒鉛材で形成された容器に充填して脱
灰炉にセットし、炉内に塩素、あるいはフレオン等のハ
ロゲン含有ガスを送入しながら約2000℃の温度に加熱す
る高純度化処理する(第2工程)。The coarsely crushed material is filled in a container made of high-purity graphite material and set in a deashing furnace. While the halogen-containing gas such as chlorine or freon is fed into the furnace, it is heated to a temperature of about 2000 ° C. Purify (second step).
ついで、高純度化処理後の粗粉砕物にエタノールを添加
してジェットミル粉砕機を用いて平均粒径1μm以下の
粒度に微粉化する(第3工程)。ジェットミル粉砕機に
は、通常、ジェット気流で原料相互を衝突させるタイプ
とジェット気流により原料を衝突板に吹付けるタイプと
があるが、本第3工程では前者のタイプに属する機構の
ものを用いることが望ましい。Then, ethanol is added to the coarsely pulverized product after the high-purification treatment, and finely pulverized into particles having an average particle diameter of 1 μm or less using a jet mill pulverizer (third step). There are two types of jet mill crushers, one of which makes the raw materials collide with each other by a jet stream, and the other of which the raw material is sprayed onto the collision plate by the jet stream. In the third step, a machine belonging to the former type is used. Is desirable.
本発明において、第2工程で高温ハロゲンガス処理され
る材料は黒鉛素材を粗粉砕した粒度数mm〜数100μm程
度の粉粒体であるから、微粉砕物に比較して取扱いが容
易となり容器充填量も大幅に増大する。したがって、高
純度化処理の作業能率ならびに処理効率を向上させるた
めに有効機能する。In the present invention, the material to be treated with the high-temperature halogen gas in the second step is a powder material obtained by coarsely crushing a graphite material and having a particle size of several millimeters to several hundreds of micrometers. The amount will also increase significantly. Therefore, it works effectively in order to improve the work efficiency of the purification treatment and the treatment efficiency.
また、引続く第3工程の微粉化は粗粉砕物にエタノール
を添加してジェットミル粉砕によりおこなうから粉砕効
率の向上が図られ、また粉砕機系統からの不純物混入に
基づく二次的汚染は効果的に防止される。このため、常
に目標とされる平均粒径1μm以下、不純物含有量50pp
m以下の高純度黒鉛微粉が製造される。In addition, since the subsequent pulverization in the third step is performed by jet mill pulverization by adding ethanol to the coarse pulverized product, the pulverization efficiency is improved, and the secondary contamination due to the inclusion of impurities from the pulverizer system is effective. Be prevented. For this reason, the target average particle size is 1 μm or less and the impurity content is 50 pp.
High-purity graphite fine powder of m or less is produced.
黒鉛素材を粗粉砕した粒度8mm以下の粉粒体200kgを円
筒るつぼ形の高純度黒鉛容器に充填して電気抵抗加熱式
の脱灰炉にセットし、50/分の流量で塩素ガスを流通
させながら400℃/時の昇温速度で2000℃まで温度を上
げた。この温度に10時間保持して高純度化処理をおこな
ったのち、自然放冷した。200 kg of a granular material with a particle size of 8 mm or less obtained by coarsely crushing a graphite material is filled in a cylindrical crucible-shaped high-purity graphite container, set in an electric resistance heating type deashing furnace, and chlorine gas is circulated at a flow rate of 50 / min. Meanwhile, the temperature was raised to 2000 ° C at a temperature rising rate of 400 ° C / hour. After maintaining at this temperature for 10 hours to perform a purification treatment, it was naturally cooled.
高純度化処理後の黒鉛粉粒体は、ついでジェットミル粉
砕機(セイシン企業製ジェット粉砕機、STJ−2000)
を用い4回反復して微粉砕処理をおこなった。なお、粉
砕に際しては、処理すべき黒鉛粉粒体にエタノール(試
薬特級)を添加して自重の増加による粉砕効率の向上を
図った。The graphite powder after high-purification treatment is then jet mill crusher (jet crusher manufactured by Seishin Enterprise, STJ-2000).
Was used to perform fine pulverization treatment four times. At the time of crushing, ethanol (special grade reagent) was added to the graphite powder to be treated to improve the crushing efficiency by increasing the own weight.
このようにして得られた高純度黒鉛微粉を粒度分析装置
(セイシン企業製、ミクロン・フォート・サイザーSK
C−2000S)にかけ、エタノールを分散媒として平均粒
径を測定した。また、同時に蛍光X線分析装置(理学電
気製、3370)を用いて不純物含有量の測定をおこなっ
た。The high-purity graphite fine powder thus obtained was analyzed by a particle size analyzer (manufactured by Seishin Enterprise, Micron Fort Sizer SK
C-2000S) and the average particle size was measured using ethanol as the dispersion medium. At the same time, the content of impurities was measured using a fluorescent X-ray analyzer (3370, manufactured by Rigaku Denki Co., Ltd.).
これらの測定結果を、従来技術による市販の高純度黒鉛
微粉の測定結果と対比させて表1に示した。These measurement results are shown in Table 1 in comparison with the measurement results of commercially available high-purity graphite fine powder according to the prior art.
〔発明の効果〕 以上のとおり、本発明によれば平均粒径1μm以下で不
純物含有量50ppm以下の高純度黒鉛微粉を常に効率よく
製造することができるため、エレクトロニクス、原子力
等の分野をはじめ高純度性能が要求されるあらゆる用途
に対して安全に供給することができる。 [Effects of the Invention] As described above, according to the present invention, high-purity graphite fine powder having an average particle size of 1 µm or less and an impurity content of 50 ppm or less can be efficiently manufactured at all times, and thus, it is possible to improve the efficiency in fields such as electronics and nuclear power. It can be safely supplied for any application requiring purity performance.
Claims (1)
理によって高純度黒鉛微粉に転化する方法において、黒
鉛素材を粒度数mm以下に粗粉砕する第1工程、該粗粉砕
物を高温ハロゲンガスにより高純度化処理する第2工
程、高純度化処理後の粗粉砕物にエタノールを添加して
ジェットミル粉砕により平均粒径1μm以下に微粉化す
る第3工程とからなることを特徴とする高純度黒鉛微粉
の製造方法。1. A method of pulverizing a graphite material and converting it into high-purity graphite fine powder by high-temperature halogen gas treatment. High-purity graphite, comprising a second step of purifying treatment, and a third step of adding ethanol to the coarsely pulverized product after the high-purification treatment and pulverizing by jet mill pulverization to an average particle size of 1 μm or less. Method for producing fine powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63233968A JPH0645446B2 (en) | 1988-09-19 | 1988-09-19 | Method for producing high-purity graphite fine powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63233968A JPH0645446B2 (en) | 1988-09-19 | 1988-09-19 | Method for producing high-purity graphite fine powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0283205A JPH0283205A (en) | 1990-03-23 |
| JPH0645446B2 true JPH0645446B2 (en) | 1994-06-15 |
Family
ID=16963460
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63233968A Expired - Lifetime JPH0645446B2 (en) | 1988-09-19 | 1988-09-19 | Method for producing high-purity graphite fine powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0645446B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI607966B (en) * | 2016-12-22 | 2017-12-11 | 國家中山科學研究院 | Method for making graphite structure of different phases |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1994027909A1 (en) * | 1993-05-21 | 1994-12-08 | Stratmin Inc. | Process and apparatus for the purification of graphite |
| WO1995003890A1 (en) * | 1993-08-03 | 1995-02-09 | Indresco Inc. | Beneficiation of flake graphite |
| CH710862B1 (en) * | 1999-11-26 | 2016-09-15 | Imerys Graphite & Carbon Switzerland Sa | Process for the production of graphite powders with increased bulk density. |
| WO2014034859A1 (en) * | 2012-08-30 | 2014-03-06 | 株式会社クレハ | Carbonaceous material for negative electrodes of lithium ion capacitors and method for producing same |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61101408A (en) * | 1984-10-19 | 1986-05-20 | Hitachi Chem Co Ltd | Graphite material refining method and refining equipment |
| JPS63147810A (en) * | 1986-12-11 | 1988-06-20 | Hitachi Chem Co Ltd | High electroconductive graphite having high lubricity |
-
1988
- 1988-09-19 JP JP63233968A patent/JPH0645446B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI607966B (en) * | 2016-12-22 | 2017-12-11 | 國家中山科學研究院 | Method for making graphite structure of different phases |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0283205A (en) | 1990-03-23 |
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