JPH0817953B2 - Method of dry grinding of graphite - Google Patents
Method of dry grinding of graphiteInfo
- Publication number
- JPH0817953B2 JPH0817953B2 JP1019724A JP1972489A JPH0817953B2 JP H0817953 B2 JPH0817953 B2 JP H0817953B2 JP 1019724 A JP1019724 A JP 1019724A JP 1972489 A JP1972489 A JP 1972489A JP H0817953 B2 JPH0817953 B2 JP H0817953B2
- Authority
- JP
- Japan
- Prior art keywords
- graphite
- crushing
- pulverization
- chamber
- graphite powder
- 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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- Crushing And Grinding (AREA)
- Carbon And Carbon Compounds (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、振動ミルにより黒鉛粉末を効率良く粉砕
する方法に関する。The present invention relates to a method for efficiently pulverizing graphite powder with a vibration mill.
黒鉛は、固体潤滑剤、ブラウン管用導電塗料、鉛筆の
芯等として工業的に広く用いられているが、これらに使
用する場合、なるべく流度の細かい微粉末であることが
要求される。Graphite is industrially widely used as a solid lubricant, a conductive paint for cathode ray tubes, a pencil lead, and the like, but when used for these, it is required to be a fine powder having a finest flow as possible.
従来、黒鉛粉の粉砕は、ジェットミル等を用いて、平
均粒子等が数ミクロンないし数十ミクロンになるように
原鉱粉を一次粉砕した後、一般的には振動ミルを用いて
微粉化される。Conventionally, graphite powder is pulverized using a jet mill or the like to primarily pulverize the raw ore powder so that the average particles become several microns to several tens of microns, and then it is generally pulverized using a vibration mill. It
振動ミルを用いて微粉体を製造する場合、粉砕室内に
鋼球等のメディアと被粉砕黒鉛を入れ乾式状態で粉砕す
る方法、水分等を投入し被粉砕黒鉛をスラリー状態で粉
砕する湿式粉砕方法、乾式粉砕する際に粉砕室内に真空
ポンプで排気し真空状態を保持しながら粉砕する方法が
ある。When producing fine powder using a vibrating mill, a method of crushing in a dry state by putting media such as steel balls and graphite to be crushed in a crushing chamber, a wet crushing method of crushing graphite to be crushed in a slurry state by adding water etc. When dry pulverizing, there is a method of exhausting with a vacuum pump into the pulverizing chamber and pulverizing while maintaining a vacuum state.
これらの方法はそれぞれ必要に応じ採用されている公
用技術であるが、各々の特徴を述べると、次の通りであ
る。Each of these methods is a publicly-used technique that is adopted as necessary, and the features of each are as follows.
乾式粉砕方法は黒鉛粉末同士が付着し合って凝集粉を
形成しやすく、従って粉砕効率に欠点がある。The dry pulverization method has a drawback in pulverization efficiency because graphite powders are easily attached to each other to form agglomerated powders.
湿式粉砕法は凝集の問題を解消されるものの、粉砕後
に水分等の除去が必要であったり、黒鉛の用途に応じて
媒体の種類が限定されるなど処理方法に欠点がある。Although the wet pulverization method solves the problem of agglomeration, it has drawbacks in the treatment method, such as the need to remove water and the like after pulverization and the type of medium being limited depending on the application of graphite.
一方、真空中粉砕法によれば、真空下では黒鉛粉末の
付着力が弱くなる性質があり、乾式で効率良く微粉砕す
ることができる。この真空粉砕に関連する文献として
は、例えば特公昭40−22099号公報、および特開昭63−1
6052号公報が挙げられる。On the other hand, according to the pulverization method in vacuum, the adhesive force of the graphite powder is weakened under vacuum, and it is possible to efficiently perform fine pulverization by a dry method. Documents related to this vacuum pulverization include, for example, Japanese Patent Publication No. 40-22099 and Japanese Patent Laid-Open No. 63-1.
6052 publication is mentioned.
前述した真空粉砕方法によれば、乾式で効率良く微粉
化できるのであるが、半面、粉砕室内を真空にする前処
理時間がかかること、排気中に粉砕室内から黒鉛粉が放
出されない特別な装置を要し装置の保全にも手間がかか
るなどによってコストがかさむという問題があった。According to the above-mentioned vacuum pulverizing method, it is possible to efficiently pulverize by a dry method, but on the other hand, it takes a pretreatment time to vacuum the pulverizing chamber, and a special device that does not release graphite powder from the pulverizing chamber during evacuation. There is a problem in that the cost is increased due to the troublesome maintenance of the device.
この発明は、上述した先例方法に照らして、乾式粉砕
であって粉砕効率が良く、トータルコストが安い黒鉛の
微粉砕手段を目標としてなされた。The present invention has been made in the light of the above-described method of the prior art, and is aimed at a fine pulverization means of graphite which is a dry pulverization, has a high pulverization efficiency and a low total cost.
本発明は、振動ミルの粉砕室内にメディア被粉砕黒鉛
粉を投入し、該粉砕室を密閉し、密封状態で常圧のまま
黒鉛微粉の粉砕を開始し、粉砕の進行に伴ない該粉砕室
内のガスを黒鉛に吸着させて原圧粉砕することを特徴と
する黒鉛の乾式粉砕方法である。The present invention is to put graphite powder to be pulverized into a medium into a pulverizing chamber of a vibration mill, to close the pulverizing chamber, to start pulverizing graphite fine powder at a normal pressure in a sealed state, and to pulverize the pulverizing chamber as the pulverization progresses. The dry pulverization method for graphite is characterized in that the gas of (1) is adsorbed on graphite and pulverized under original pressure.
振動ミルの粉砕室内に鋼球等のメディアと共に被粉砕
黒鉛粉を投入し、粉砕室を密閉して振動を与えると、黒
鉛粉はメディアにより剪断や切断作用を受けて粉砕され
比表面積が増加する。すると粉末のガス吸着能が増加す
る。この結果、粉砕室内の空気等は黒鉛粉に吸着され、
粉砕室内は減圧状態になる。更に粉砕すると、粉砕室内
の空気等は稀薄であるから、黒鉛粉に吸着する十分な空
気等が無く、即ち、真空中粉砕と同様な粉砕形態を示す
ことになり、粉砕効率は真空粉砕法と同等程度を示す。When graphite powder to be crushed is put together with media such as steel balls into the crushing chamber of the vibration mill and the crushing chamber is closed and vibration is applied, the graphite powder is crushed by the shearing and cutting action of the media and the specific surface area increases. . Then, the gas adsorption capacity of the powder increases. As a result, the air in the crushing chamber is adsorbed by the graphite powder,
The crushing chamber is in a reduced pressure state. When further crushing, the air and the like in the crushing chamber are diluted, so there is not enough air and the like to adsorb on the graphite powder, that is, the crushing form similar to that in vacuum crushing is exhibited, and the crushing efficiency is the same as the vacuum crushing method. Indicates the same degree.
粉砕された黒鉛粉の形状は、常圧による乾式粉砕や湿
式粉砕による場合の偏平形状に比べると、比較的塊状に
なるのが特徴である。The shape of the crushed graphite powder is characterized in that it is relatively agglomerated as compared with the flat shape in the case of dry crushing under normal pressure or wet crushing.
被粉砕黒鉛粉(出発黒鉛粉末)の粒度は、市販されて
いる一般的なものであれば同じ作用効果を示すので特に
限定はしないが、平均粒子径が100μmを越えるような
粒度の粗い粉末は、比表面積の変化量が多くなる分、上
述した減圧作用があり、振動ミル粉砕としては効率良い
が、産業上はジェットミルのような他の高効率粉砕法に
よって5〜50μm程度とした後、本発明方法を適用した
方が合理的である。一方、2μmとか3μmというよう
に仕上がり平均粒子径に近い出発黒鉛粉末を用いること
は、他の粉砕手段でも収率が低く高価になるが、本発明
方法でも、比表面積の変化が小さく減圧作用が少なくな
るので、不経済であり好ましくない。The particle size of the pulverized graphite powder (starting graphite powder) is not particularly limited as long as it is the same as the commercially available general one, but it is not limited to a coarse powder having an average particle size of more than 100 μm. Since the amount of change in the specific surface area is large, the above-described depressurizing effect is exerted, and it is efficient as a vibration mill crushing, but industrially, after being made to be about 5 to 50 μm by another high efficiency crushing method such as a jet mill, It is more rational to apply the method of the present invention. On the other hand, using a starting graphite powder having a finished average particle diameter of 2 μm or 3 μm, which is close to the average particle diameter, results in a low yield and high cost even with other pulverizing means. Since it decreases, it is uneconomical and not preferable.
なお、本発明における平均粒子径は、コールター・カ
ウンターと呼ばれている電気抵抗法により粒度を測定し
た分布の平均値をいう。In addition, the average particle diameter in the present invention means an average value of a distribution in which the particle size is measured by an electric resistance method called a Coulter counter.
振動ミルを用いて、平均粒子径が8.8μmの市販の天
然鱗状黒鉛粉を本発明方法により微粉砕した。Using a vibration mill, commercially available natural scaly graphite powder having an average particle diameter of 8.8 μm was finely pulverized by the method of the present invention.
用いた振動ミルは、軸着された円筒状の粉砕室を円周
方向に偏心回転することにより振動を与える機構で、円
筒室内に鋼球が入っている。粉砕室の上部に材料出し入
れ口があり、バルブ付きの蓋で覆い、解放および密封状
態にすることができる。またホースを介して真空ポンプ
を接続し、粉砕室内に減圧することができる。The vibration mill used is a mechanism that gives vibration by eccentrically rotating a cylindrical crushing chamber axially mounted in the circumferential direction, and a steel ball is contained in the cylindrical chamber. There is a material access port at the top of the grinding chamber, which can be covered with a valved lid and opened and sealed. A vacuum pump can be connected via a hose to reduce the pressure in the crushing chamber.
下記に示す粉砕条件により、粉砕室を開放状態と、密
封状態および真空ポンプで1〜10Torrに減圧した状態の
3種類の粉砕を行い、粉砕された粉体の平均粒子径およ
び比表面積を測定した。Under the pulverization conditions shown below, three types of pulverization were performed, with the pulverization chamber being in an open state, a closed state, and a state in which the pressure was reduced to 1 to 10 Torr by a vacuum pump, and the average particle diameter and specific surface area of the pulverized powder were measured. .
なお、比表面積はBET法による比表面積を用いた。 As the specific surface area, the specific surface area measured by the BET method was used.
粉砕容器の内容積:3.4リットル 鋼球の直径:10mm 鋼球の充填量:68% 黒鉛粉投入量:600g 振動数:1600cpm 振幅:7mm 粉砕時間:5、10、15時間 第1図は粉砕容器内の圧力を示したもので、密封容器
の場合、粉砕時間5時間で100Torrになり、15時間では1
6Torrを示した。Inner volume of crushing container: 3.4 liter Diameter of steel ball: 10 mm Filling amount of steel ball: 68% Graphite powder input amount: 600 g Vibration frequency: 1600 cpm Amplitude: 7 mm Grinding time: 5, 10, 15 hours Figure 1 shows the crushing container The internal pressure is shown. In the case of a sealed container, the crushing time is 100 Torr in 5 hours and 1 in 15 hours.
It showed 6 Torr.
第2図は粉砕黒鉛粉の平均粒子径を粉砕時間を横軸に
して表わしたもので、本発明の密封粉砕は減圧粉砕より
も僅かに粉砕効率が劣るものの開放粉砕に比較すると一
段優れていることが分る。FIG. 2 shows the average particle size of pulverized graphite powder with the pulverization time as the horizontal axis. The sealed pulverization of the present invention is slightly inferior to decompression pulverization in pulverization efficiency, but is far superior to open pulverization. I understand.
なお、この測定値は前述したようにコールターカウン
ターにより測定したもので、光透過法による測定置と比
較すると約2.4倍大きい値を示す傾向がある。This measured value is measured by a Coulter counter as described above, and tends to show a value about 2.4 times larger than that measured by the light transmission method.
第3図は同様に比表面積について表わしたもので、粒
子径の場合と同様な傾向を示している。Similarly, FIG. 3 shows the specific surface area and shows the same tendency as in the case of the particle size.
以上説明したように、本発明の黒鉛粉砕方法は通常の
振動ミルを用い、粉砕室を密閉して粉砕することにより
内部気圧が下がり、粉砕が促進されるものであるから、
繁雑な粉砕装置および操作を必要とせず、短時間で効率
よく微粉末に粉砕することができる。As described above, the graphite crushing method of the present invention uses a normal vibration mill, the internal pressure is lowered by closing the crushing chamber and crushing, and the crushing is promoted.
It is possible to efficiently pulverize into fine powder in a short time without requiring a complicated pulverizing device and operation.
第1図は実施例における粉砕室内気圧を示すグラフ、第
2図は粉砕時間と粉砕黒鉛粉の平均粒子径の関係を示す
グラフ、第3図は粉砕時間と粉砕黒鉛粉の比表面積の関
係を示すグラフである。FIG. 1 is a graph showing the pressure inside the crushing chamber in the example, FIG. 2 is a graph showing the relationship between the crushing time and the average particle size of the crushed graphite powder, and FIG. 3 is a relationship between the crushing time and the specific surface area of the crushed graphite powder. It is a graph shown.
Claims (1)
鉛粉を投入し、該粉砕室を密閉し、密封状態で常圧のま
ま黒鉛微粉の粉砕を開始し、粉砕の進行に伴ない該粉砕
室内のガスを黒鉛に吸着させて減圧粉砕することを特徴
とする黒鉛の乾式粉砕方法。1. A medium and a graphite powder to be crushed are put into a crushing chamber of a vibration mill, the crushing chamber is sealed, and pulverization of fine graphite powder is started in a sealed state at normal pressure. A dry pulverization method of graphite, characterized in that gas in a pulverization chamber is adsorbed to graphite and pulverized under reduced pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1019724A JPH0817953B2 (en) | 1989-01-31 | 1989-01-31 | Method of dry grinding of graphite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1019724A JPH0817953B2 (en) | 1989-01-31 | 1989-01-31 | Method of dry grinding of graphite |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02203944A JPH02203944A (en) | 1990-08-13 |
| JPH0817953B2 true JPH0817953B2 (en) | 1996-02-28 |
Family
ID=12007256
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1019724A Expired - Lifetime JPH0817953B2 (en) | 1989-01-31 | 1989-01-31 | Method of dry grinding of graphite |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0817953B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19857190B4 (en) * | 1998-12-11 | 2005-03-03 | Leibniz-Institut Für Festkörper- Und Werkstoffforschung Dresden E.V. | Material for reducing or eliminating unwanted admixtures in gases, process for its preparation and use |
| CN103956494B (en) * | 2014-04-04 | 2016-03-02 | 洛阳市冠奇工贸有限责任公司 | The preparation method of the natural micro powder graphite of a kind of Subnano-class |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60168548A (en) * | 1984-02-13 | 1985-09-02 | 郷地 俊介 | Powder extraction apparatus |
| JPS6316052A (en) * | 1986-07-07 | 1988-01-23 | 川崎重工業株式会社 | Vibrating mill |
-
1989
- 1989-01-31 JP JP1019724A patent/JPH0817953B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02203944A (en) | 1990-08-13 |
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