JPH0283205A - Manufacturing method of high purity graphite fine powder - Google Patents
Manufacturing method of high purity graphite fine powderInfo
- Publication number
- JPH0283205A JPH0283205A JP63233968A JP23396888A JPH0283205A JP H0283205 A JPH0283205 A JP H0283205A JP 63233968 A JP63233968 A JP 63233968A JP 23396888 A JP23396888 A JP 23396888A JP H0283205 A JPH0283205 A JP H0283205A
- Authority
- JP
- Japan
- Prior art keywords
- graphite
- purity
- fine powder
- pulverization
- 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.)
- Granted
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- Carbon And Carbon Compounds (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、so ppm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。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing high-purity graphite fine powder having an impurity content of less than so ppm.
黒鉛の微粉末は潤滑材、導電フィラーなどとして古(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so
ppm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 as a lubricant and conductive filler since ancient times, but recently it has been applied to fields such as electronics and nuclear power, and the impurity content has increased.
There is an increasing demand for graphite fine powder having high purity of ppm or less.
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, as a means for producing high-purity graphite fine powder to meet this requirement, a method of pulverizing a graphite material and treating it with high-temperature halogen gas has been adopted, 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
オン等のハロゲ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−等で微粉砕する。(1) High purification treatment in which graphite material is placed in a deashing furnace and heated while feeding halogen-containing gas such as chlorine and freon into the furnace (hereinafter referred to as "high-temperature halogen gas treatment")
After that, it is coarsely crushed using a crusher such as a hammer crusher, and further finely crushed 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 coarsely and finely pulverized using the same means as above, and then filled into 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1
0W程度のブロック材、「粗粉砕」とは数閣から数10
0u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1n以下の粒度に粉砕することを指す。In these processes, "graphite material" has a particle size of 1
Block material of about 0W, "coarse pulverization" means from several to several 10
The term "fine pulverization" refers to pulverization to a powder having a particle size of 0u, and "fine pulverization" refers to pulverization to an average particle size of 1n 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50ρρ−以下)することができる利点がある。Among the above-mentioned conventional techniques, process (1) can efficiently and inexpensively purify a block-shaped graphite material (impurity content: 50ρρ- or less) because it can be treated with high-temperature halogen gas as it is. It has the advantage of being able to
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−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。However, there is a drawback that the targeted high-purity graphite powder cannot be obtained due to contamination caused by wear of the hammer crusher and 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。In addition, in the case of process (2), since the coarse pulverization and fine pulverization steps that involve contamination are performed in the first stage, high-purity graphite powder that exceeds the target level can be obtained by the high-temperature halogen gas treatment in the next step. However, the graphite fine powder after pulverization is extremely bulky and difficult to handle, and there are also problems such as a decrease in the amount of graphite packed into a graphite container during 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たも
ので、不純物含存150 ppm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 was made to solve these problems, and provides a method for efficiently producing high-purity graphite fine powder containing 150 ppm or less of impurities.
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、黒鉛素材を粗粉
砕する第1工程、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を
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 is as follows:
In the method of converting graphite material into high-purity fine graphite powder by crushing and high-temperature halogen gas treatment, the first step is to coarsely crush the graphite material, the second step is to treat the coarsely crushed material to high purity with high-temperature halogen gas, and high purity. The method is characterized in that it comprises a third step of pulverizing the treated coarsely pulverized material to an average particle size of 1 μm or less by jet mill pulverization.
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、粒径数腫から数
10Onのサイズに粉砕する(第1工程)。The graphite material used as the raw material is artificial graphite block material obtained by normal manufacturing methods, but for example, leftover materials or processing waste of graphitized products generated in the process of manufacturing large graphite electrodes for electrical steel manufacturing are used. You may use waste materials. These graphite materials are roughly pulverized using a commonly used coarse pulverizer such as a hammer crusher to a particle size ranging from a few ounces to several tens of ounces (first step).
粗わ)偉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°Cの温度
に加熱する高純度化処理する(第2工程)。The coarse material is filled into a container made of high-purity graphite material, set in a deashing furnace, and heated to a temperature of approximately 2000°C while feeding halogen-containing gas such as chlorine or freon into the furnace. High purification treatment by heating (second step).
ついで、高純度化処理後の粗粉砕物はジェットミル粉砕
機を用いて平均粒径In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。Next, the coarsely pulverized product after the high-purification treatment is pulverized to a particle size of the average particle size In or less using a jet mill pulverizer (third step
There are two types of jet mill crushers: one type in which the raw materials are collided with each other using a jet stream, and the other type in which the raw materials are sprayed onto a collision plate using a jet stream.In this third process, a mechanism belonging to the former type is used. It is preferable to use one.
(作 用)
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−〜数100n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。(Function) In the present invention, the material to be treated with high-temperature halogen gas in the second step is a granular material obtained by coarsely pulverizing a graphite material and having a particle size of about 100 nanometers, so it is easier to handle than a finely pulverized material. This makes it easier and the amount of container filling increases significantly. Therefore, it functions effectively to improve the work efficiency and treatment efficiency of high purification treatment.
また、引続く第3工程では微粉化をジェットミル粉砕に
よりおこなうから、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1n+以下、不純物含有量50ρp
−以下の高純度黒鉛@粉が製造される。In addition, in the subsequent third step, since pulverization is performed by jet mill pulverization, secondary contamination due to impurity contamination from the pulverizer system is effectively prevented. For this reason, the average particle diameter is always 1n+ or less, and the impurity content is 50ρp.
- The following high purity graphite @ powder is produced.
黒鉛素材を粗粉砕した粒度8駆以下の粉粒体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、502/分の流量で塩素ガス
を流通させながら400°C/時の昇温速度で2000
°C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 coarsely crushed graphite material with a particle size of 8WD or less
was filled into a cylindrical crucible-shaped high-purity graphite container, set in an electric resistance heating type deashing furnace, and heated at a temperature increase rate of 400°C/hour while circulating chlorine gas at a flow rate of 502°C/hour.
The temperature was raised to °C. After performing high purification treatment by maintaining this temperature for 10 hours, it was allowed to cool naturally.
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4i!(セイシン企業製ジヱント粉砕機、5TJ−2
000)を用い4回反復して微粉砕処理をおこなった。The graphite powder after the high purity treatment is then pulverized by jet mill 4i! (Gient crusher manufactured by Seishin Enterprises, 5TJ-2
The pulverization process was repeated four times using 000).
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。In addition, during pulverization, ethanol (special grade reagent) was added to the graphite powder to be treated to improve the pulverization efficiency by increasing its 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5K
C−200O8)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線分析袋Wl(
理学電気型、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 using a particle size analyzer (Micron Fort Sizer 5K, manufactured by Seishin Enterprises).
C-200O8) and the average particle size was measured using ethanol as a dispersion medium. At the same time, a fluorescent X-ray analysis bag Wl (
The impurity content was measured using Rigaku Denki Model 3370.
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.
表1
本発明品 0.6
市販AO16
1,0
〔発明の効果]
以上のとおり、本発明によれば平均粒径1−以下で不純
物含有量50 pp−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。Table 1 Product of the present invention 0.6 Commercially available AO16 1,0 [Effects of the invention] As described above, according to the present invention, high purity graphite fine powder with an average particle size of 1- or less and an impurity content of 50 pp- or less can be constantly and efficiently produced. Because it can be manufactured, it can be safely supplied to all kinds of applications that require high purity performance, including fields such as electronics and nuclear power.
特許出願人 東海カーボン株式会社Patent applicant: Tokai Carbon Co., Ltd.
Claims (1)
て高純度黒鉛微粉に転化する方法において、黒鉛素材を
粗粉砕する第1工程、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
物を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. In the method of converting graphite material into high-purity graphite fine powder by crushing and high-temperature halogen gas treatment, the first step is to coarsely crush the graphite material, the second step is to treat the coarsely crushed material to high purity with high-temperature halogen gas, and high-purity A method for producing high-purity fine graphite powder, comprising a third step of pulverizing the coarsely pulverized material after purification treatment to an average particle size of 1 μm or less by jet mill pulverization.
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 true JPH0283205A (en) | 1990-03-23 |
| JPH0645446B2 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 (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 |
| WO2001038220A1 (en) * | 1999-11-26 | 2001-05-31 | Timcal Ag | Method for producing graphite powder with an 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 |
Families Citing this family (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 |
Citations (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
Patent Citations (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 |
Cited By (13)
| 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 |
| GB2285973A (en) * | 1993-08-03 | 1995-08-02 | Indresco Inc | Beneficiation of flake graphite |
| US5518189A (en) * | 1993-08-03 | 1996-05-21 | Harbison-Walker Refractories Company | Beneficiation of flake graphite |
| GB2285973B (en) * | 1993-08-03 | 1996-12-18 | Indresco Inc | Beneficiation of flake graphite |
| JP2003514753A (en) * | 1999-11-26 | 2003-04-22 | ティムカル アーゲー | Method for producing graphite powder with increased bulk density |
| WO2001038220A1 (en) * | 1999-11-26 | 2001-05-31 | Timcal Ag | Method for producing graphite powder with an increased bulk density |
| KR100769531B1 (en) * | 1999-11-26 | 2007-10-23 | 팀칼 아게 | Method for producing graphite powder with an increased bulk density |
| JP2016175839A (en) * | 1999-11-26 | 2016-10-06 | イメリス グラファイト アンド カーボン スイッツァランド エスアー | Method for producing graphite powder 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 |
| CN104641435A (en) * | 2012-08-30 | 2015-05-20 | 株式会社吴羽 | Carbonaceous material for negative electrode of lithium ion capacitor and manufacturing method thereof |
| JPWO2014034859A1 (en) * | 2012-08-30 | 2016-08-08 | 株式会社クレハ | Carbonaceous material for lithium ion capacitor negative electrode and method for producing the same |
| US9508494B2 (en) | 2012-08-30 | 2016-11-29 | Kureha Corporation | Carbonaceous material for negative electrodes of lithium ion capacitors and method for producing same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0645446B2 (en) | 1994-06-15 |
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