JPH10137609A - Method for operating horizontal ultrafine particle mill - Google Patents
Method for operating horizontal ultrafine particle millInfo
- Publication number
- JPH10137609A JPH10137609A JP29865096A JP29865096A JPH10137609A JP H10137609 A JPH10137609 A JP H10137609A JP 29865096 A JP29865096 A JP 29865096A JP 29865096 A JP29865096 A JP 29865096A JP H10137609 A JPH10137609 A JP H10137609A
- Authority
- JP
- Japan
- Prior art keywords
- balls
- mill
- milling
- outer cylinder
- inner cylinder
- 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.)
- Pending
Links
Landscapes
- Crushing And Grinding (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、超微粉体製造に適
用され、乾式及び湿式粉砕を行う横型超微粒ミルの運転
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for operating a horizontal ultrafine mill for dry and wet pulverization, which is applied to the production of ultrafine powder.
【0002】[0002]
【従来の技術】図2に横型超微粒ミルを回分式粉砕にて
用いる場合の内部断面図を示す。図において、横型超微
粒ミルは、UF(Ultra Fine) ミルとも称し、1は回転
可能な外筒、2は内筒で、外筒1内で回転可能に配置さ
れている。3は粉砕ボール、4は外筒1及び内筒2内周
にそれぞれ設けられた攪拌翼、5は外筒1を回転させる
モータ、6は内筒2を回転させるモータである。2. Description of the Related Art FIG. 2 shows an internal sectional view of a case where a horizontal ultrafine mill is used in batch grinding. In the figure, the horizontal ultrafine mill is also called a UF (Ultra Fine) mill, 1 is a rotatable outer cylinder, 2 is an inner cylinder, and is rotatably arranged in the outer cylinder 1. 3 is a grinding ball, 4 is a stirring blade provided on the inner circumference of the outer cylinder 1 and the inner cylinder 2, 5 is a motor for rotating the outer cylinder 1, and 6 is a motor for rotating the inner cylinder 2.
【0003】上記のように、UFミルは主として、任意
の回転数、回転方向にて回転可能な外筒1と内筒2、及
びそれらの間隙に充填された粉砕ボール3にて構成され
ている。粉砕ボール3の間隙に、乾式粉砕の場合は乾粉
が、湿式粉砕の場合は乾粉と溶媒(水もしくは油)が充
填され、外筒1のモータ5による回転、内筒2のモータ
6による回転、及び内,外筒にそれぞれ設けられた攪拌
翼4により発生する剪断力をボールを介して粉体に加
え、効率的な微粉砕が行われる。[0003] As described above, the UF mill is mainly composed of the outer cylinder 1 and the inner cylinder 2 rotatable at an arbitrary number of revolutions and in the rotating direction, and the crushing balls 3 filled in the gap between them. . The gap between the grinding balls 3 is filled with dry powder in the case of dry grinding, and with dry powder and a solvent (water or oil) in the case of wet grinding, and rotated by the motor 5 of the outer cylinder 1 and rotated by the motor 6 of the inner cylinder 2. Further, the shearing force generated by the stirring blades 4 provided in the inner and outer cylinders is applied to the powder through the ball, and the fine pulverization is performed efficiently.
【0004】[0004]
【発明が解決しようとする課題】前述の従来のミルにお
いては、数ミクロンからサブミクロンまでの微粉砕を行
う場合、より小さいボールが粉砕効率が高い事が広く知
られている。これまでUFミルでは、6〜10mmφの単
一直径を有するボールを用いていたが、更に小径のボー
ルを用いることで、現状の粉砕効率を向上させることが
可能と予想された。In the above-mentioned conventional mill, it is widely known that, when fine grinding from several microns to submicron is performed, smaller balls have higher grinding efficiency. Until now, UF mills used balls having a single diameter of 6 to 10 mmφ. However, it is expected that the current grinding efficiency can be improved by using even smaller diameter balls.
【0005】しかしながら小さいボールを用いると、ミ
ル内部の狭窄部にボールが噛み込むため製造精度の向上
が必要となったり、粉砕原料粒径が大きいもの(例えば
3mmのボールで7mmの原料を粉砕するなど)の粉砕が困
難となりミル粉砕原料粒径を現状より小さくする事前粉
砕が必要となる、等の不具合があった。However, when a small ball is used, it is necessary to improve the manufacturing accuracy because the ball bites into a constricted portion inside the mill, or a ball having a large particle size of the crushed raw material (for example, a 7 mm raw material is crushed with a 3 mm ball). Etc.), which makes it difficult to perform the pulverization, and requires prior pulverization to reduce the particle size of the raw material to be milled.
【0006】[0006]
【課題を解決するための手段】本発明は、前述の課題を
解決するために、次の(1),(2)の手段を提供す
る。The present invention provides the following means (1) and (2) in order to solve the above-mentioned problems.
【0007】(1)回転可能で攪拌翼を装着した内筒及
び外筒を有し、同内,外筒の間隙に粉砕ボールを充填
し、同内筒及び外筒を任意の回転数、回転方向に回転さ
せ、供給された粉体又はスラリーを粉砕して連続排出さ
せる横型超微粒ミルの運転方法において、前記粉砕ボー
ルは異なる大きさのボールを配合したことを特徴とする
横型超微粒ミルの運転方法。(1) It has an inner cylinder and an outer cylinder which are rotatable and equipped with a stirring blade, and a crushed ball is filled in a gap between the inner and outer cylinders, and the inner cylinder and the outer cylinder are rotated at an arbitrary number of revolutions. In the method of operating a horizontal ultra-fine grain mill for rotating in the direction and crushing and continuously discharging the supplied powder or slurry, the grinding ball is characterized in that balls of different sizes are blended. how to drive.
【0008】(2)上記(1)において、前記内筒及び
外筒には水冷ジャケットを装備し、粉体又はスラリーの
粉砕熱を冷却しながら連続排出することを特徴とする横
型超微粒ミルの運転方法。(2) In the above (1), the inner cylinder and the outer cylinder are provided with a water-cooling jacket, and the powder or slurry is continuously discharged while cooling the pulverization heat while cooling. how to drive.
【0009】本発明の(1)の運転方法においては、異
なる直径を有するボールを配合させる事により、粉砕ボ
ールの充填構造が密になり、ミル攪拌エネルギの伝達効
率が向上するようになり、更に、ミル内部の狭窄部やミ
ル入口粒径への制約を新たに設けることもなく、粉砕効
率を向上させることを可能とした。又、(2)において
は、上記運転方法が内筒,外筒を水冷する場合の横型超
微粒ミルにも適用され、同様に粉砕効率を向上させるこ
とができる。In the operation method (1) of the present invention, by blending balls having different diameters, the packing structure of the crushed balls becomes dense, and the transmission efficiency of the mill stirring energy is improved. Thus, it is possible to improve the pulverizing efficiency without newly providing a restriction on the constricted portion inside the mill or the particle diameter at the mill entrance. In (2), the above operation method is also applied to a horizontal ultra-fine grain mill in which the inner cylinder and the outer cylinder are water-cooled, and the pulverization efficiency can be similarly improved.
【0010】[0010]
【発明の実施の形態】以下、本発明の実施の一形態に係
る横型超微粒ミルの運転方法について図面に基づいて具
体的に説明する。本発明の運転方法は、従来用いられて
いる図1に示す横型超微粒ミルにおいて、ミル内部に充
填する粉砕ボールを異なる直径を有するボールの配合と
して、従来の単一径の粉砕ボールを用いる場合に比べて
粉砕性能を良くするようにした運転方法である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, a method of operating a horizontal ultrafine mill according to an embodiment of the present invention will be specifically described with reference to the drawings. The operation method of the present invention is based on the case where a conventional single-diameter crushed ball is used as a mixture of crushed balls having different diameters in a conventionally used horizontal ultrafine mill shown in FIG. This is an operation method in which the pulverization performance is improved as compared with.
【0011】図1は横型超微粒ミルにおける粉砕ボール
を、10mmφのみ(記号丸印で示す)、及び10mmφと
8mmφのボールを配合(記号三角印で示す)、及び10
mmφと6mmφのボールを配合(記号四角印で示す)、
等、ボールの条件を変化させ天然鉱石を湿式回分式粉砕
した結果の比較を示し、(a)は粉砕時間比と平均粒子
径の関係、(b)は粉砕時間比と正味動力原単位比との
関係をそれぞれ示している。なお、ボールの配合はそれ
ぞれ重量割合で50%:50%とした。FIG. 1 shows grinding balls in a horizontal ultrafine mill only with 10 mmφ (indicated by a symbol), 10 mmφ and 8 mmφ balls (indicated by a triangle), and 10 mmφ.
A combination of mmφ and 6mmφ balls (indicated by symbol square)
A comparison of the results of wet batch crushing of natural ore by changing the ball conditions, etc., (a) shows the relationship between the crushing time ratio and the average particle size, (b) shows the crushing time ratio and the net power unit ratio Respectively. The composition of the balls was 50%: 50% by weight.
【0012】図1に2.5μm の同一平均粒子径での粉
砕時間比、正味動力原単位を数値で記入しているが、図
1からの読み取り値を次の表1に粉砕結果比較として示
す。図1から異なる直径のボールを配合させることによ
り、同一粉砕平均粒径までの粉砕時間の短縮比が可能で
あることがわかる。FIG. 1 shows numerical values of the ratio of pulverization time and the net power consumption at the same average particle diameter of 2.5 μm. The values read from FIG. 1 are shown in Table 1 below as a comparison of the pulverization results. . From FIG. 1, it can be seen that by mixing balls having different diameters, a reduction ratio of the pulverization time to the same pulverization average particle diameter is possible.
【0013】[0013]
【表1】 [Table 1]
【0014】上記の表1に示すとおり、10mmφのみの
場合と比較し、10mmφ+8mmφ、10mmφ+6mmφの
粉砕時間が短縮されており、これにより、同一容積のミ
ルでの処理量(単位粉砕容量)が、現状に比べ25〜3
5%向上が可能となった。As shown in Table 1 above, the grinding time of 10 mmφ + 8 mmφ, 10 mmφ + 6 mmφ is shortened as compared with the case of only 10 mmφ, so that the throughput (unit grinding capacity) of the mill having the same volume can be reduced. 25 to 3
5% improvement is possible.
【0015】またボール配合により、ボール径が全体的
に小さくなっても、粉砕粉中の粗粒分の残存(表1中の
1mm↑(wt%) )も、直径の大きなボールで粉砕した場合
と同等である。従って、同一平均粒子径での粉砕粉の粒
度分布もほぼ同等であることがわかる。また粉砕原料粒
径への制約も現状通りで問題ない事もわかった。[0015] Even if the ball diameter is reduced as a whole due to the blending of the balls, the remaining coarse particles in the pulverized powder (1 mm ↑ (wt%) in Table 1) can be reduced even if the balls are pulverized with a large diameter ball. Is equivalent to Therefore, it can be seen that the particle size distribution of the pulverized powder having the same average particle diameter is almost the same. It was also found that there was no problem with the restriction on the particle size of the pulverized raw material as is.
【0016】さらに、単位重量の粉砕原料を目標粉砕平
均粒子径まで粉砕するのに要する電力値、つまり動力原
単位( kWh/T)も、配合ボール粉砕の方が小さくなっ
ている。これは、異なる直径のボールを配合させること
で充填構造が密となり、ミルの攪拌エネルギの伝達効率
が向上した結果であると指定される。Furthermore, the electric power value required to pulverize the unit weight of the pulverized raw material to the target pulverized average particle diameter, that is, the power consumption unit (kWh / T), is smaller in the case of the compound ball pulverization. This is specified to be the result of having a denser filling structure by blending balls of different diameters and improving the transmission efficiency of the mill's stirring energy.
【0017】なお、上記に説明の運転方法は、図1に示
すように外筒1、内筒2をモータ5,6により任意の回
転数、回転方向に回転させ、供給された粉体又はスラリ
ーを粉砕して連続排出させる横型超微粒ミルにおいて、
粉砕ボールを異なる大きさのボール配合としたものであ
るが、この横型超微粒ミルの内筒,外筒に水冷ジャケッ
トを装備し、粉体又はスラリーの粉砕熱を効率良く冷却
しながら粉砕物を連続排出するミルの運転方法としても
当然適用することができ、同様の効果を有するものであ
る。In the operation method described above, as shown in FIG. 1, the outer cylinder 1 and the inner cylinder 2 are rotated by motors 5 and 6 at an arbitrary number of revolutions and in a rotating direction to supply the supplied powder or slurry. In a horizontal ultra-fine grain mill that crushes and continuously discharges,
The milling balls are made of different sized balls, but the inner and outer cylinders of this horizontal ultra-fine mill are equipped with water-cooled jackets to efficiently cool the crushing heat of the powder or slurry while removing the crushed material. Naturally, the present invention can be applied as a method of operating a mill for continuous discharge, and has the same effect.
【0018】又、上記の実施の形態においては、10mm
φと8mmφ及び10mmφと6mmφのように、2種類の直
径のボールを用いた例で示したが、3種類のボールを用
いると粉砕動力は多少増加するが、粉砕能力が向上す
る。Further, in the above embodiment, 10 mm
Although the example using two types of balls, such as φ and 8 mmφ and 10 mmφ and 6 mmφ, has been described, using three types of balls slightly increases the pulverizing power but improves the pulverizing ability.
【0019】[0019]
【発明の効果】以上、具体的に説明したように、本発明
は回転可能で攪拌翼を装着した、内筒及び外筒を有し、
内,外筒の間に粉砕ボールを充填して粉体又はスラリー
を粉砕する横型超微粒ミルの運転方法において、粉砕ボ
ールを異なる直径を有する配合として運転する方法、
又、この運転方法を内,外筒を水冷しながら粉砕するミ
ルにも適用することも提供するので、粉砕ボールの充填
構造を密にしエネルギ伝達効率を向上させることで、従
来の単一直径ボールを用いるミルの運転方法と比較し
て、粉砕処理能力、及び粉砕エネルギ効率を大幅に向上
させることが可能となった。As described above, the present invention has an inner cylinder and an outer cylinder which are rotatable and equipped with stirring blades,
A method of operating a horizontal ultrafine mill in which a grinding ball is filled between an inner cylinder and an outer cylinder to grind a powder or a slurry, wherein the grinding ball is operated as a compound having different diameters;
In addition, since this operation method can be applied to a mill that pulverizes the inner and outer cylinders while cooling the inner and outer cylinders with water, the packing structure of the pulverized balls is made denser to improve the energy transfer efficiency. It has become possible to greatly improve the pulverization processing capacity and the pulverization energy efficiency as compared with the operation method of the mill using the pulverizer.
【図1】本発明の実施の一形態に係る横型超微粒ミルの
運転に適用したボール配合条件と天然鉱石粉砕結果の図
で、(a)は粉砕時間比と正味動力原単位比との関係
を、(b)は粉砕時間比と平均粒子径の関係をそれぞれ
示す。FIG. 1 is a diagram showing ball mixing conditions and the results of natural ore pulverization applied to the operation of a horizontal ultra-fine grain mill according to an embodiment of the present invention. FIG. 1 (a) shows the relationship between the pulverization time ratio and the net power unit ratio. And (b) shows the relationship between the grinding time ratio and the average particle size, respectively.
【図2】本発明の運転方法が適用される横型超微粒ミル
の断面図である。FIG. 2 is a cross-sectional view of a horizontal ultrafine mill to which the operating method of the present invention is applied.
1 外筒 2 内筒 3 粉砕ボール 4 攪拌翼 5,6 モータ DESCRIPTION OF SYMBOLS 1 Outer cylinder 2 Inner cylinder 3 Grinding ball 4 Stirrer blade 5, 6 Motor
───────────────────────────────────────────────────── フロントページの続き (72)発明者 天野 五輪麿 長崎市飽の浦町1番1号 三菱重工業株式 会社長崎造船所内 ──────────────────────────────────────────────────の Continuing from the front page (72) Inventor Amano Olympic Rally No. 1-1 Akunouramachi, Nagasaki City Mitsubishi Heavy Industries, Ltd. Nagasaki Shipyard
Claims (2)
筒を有し、同内,外筒の間隙に粉砕ボールを充填し、同
内筒及び外筒を任意の回転数、回転方向に回転させ、供
給された粉体又はスラリーを粉砕して連続排出させる横
型超微粒ミルの運転方法において、前記粉砕ボールは異
なる大きさのボールを配合したことを特徴とする横型超
微粒ミルの運転方法。1. An inner cylinder and an outer cylinder which are rotatable and equipped with a stirring blade, and a gap between the inner cylinder and the outer cylinder is filled with crushed balls, and the inner cylinder and the outer cylinder are rotated at an arbitrary number of revolutions and rotation directions. In the method of operating a horizontal ultrafine mill, wherein the powder or slurry supplied is pulverized to continuously discharge the powder or slurry, wherein the pulverized balls are mixed with balls of different sizes. Method.
装備し、粉体又はスラリーの粉砕熱を冷却しながら連続
排出することを特徴とする請求項1記載の横型超微粒ミ
ルの運転方法。2. The method for operating a horizontal ultra-fine grain mill according to claim 1, wherein the inner cylinder and the outer cylinder are provided with a water-cooling jacket to continuously discharge the powder or slurry while cooling the pulverization heat. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29865096A JPH10137609A (en) | 1996-11-11 | 1996-11-11 | Method for operating horizontal ultrafine particle mill |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP29865096A JPH10137609A (en) | 1996-11-11 | 1996-11-11 | Method for operating horizontal ultrafine particle mill |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10137609A true JPH10137609A (en) | 1998-05-26 |
Family
ID=17862488
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP29865096A Pending JPH10137609A (en) | 1996-11-11 | 1996-11-11 | Method for operating horizontal ultrafine particle mill |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10137609A (en) |
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-
1996
- 1996-11-11 JP JP29865096A patent/JPH10137609A/en active Pending
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JP2006111909A (en) * | 2004-10-13 | 2006-04-27 | Nasu Denki Tekko Co Ltd | Ball mill device, method for producing hydrogen storage alloy powder using the device and hydrogen storage alloy powder |
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US8241418B2 (en) | 2006-02-27 | 2012-08-14 | Toray Industries, Inc. | Producing method of powder particles by using grinding medium |
JP2010537813A (en) * | 2007-09-06 | 2010-12-09 | ローワン(マネジメント) プロプライエタリー リミテッド | Crushing mill and crushing method |
JP2010090003A (en) * | 2008-10-09 | 2010-04-22 | Idemitsu Kosan Co Ltd | Method of producing sulfide-based solid electrolyte |
JP2010119915A (en) * | 2008-11-17 | 2010-06-03 | National Institute For Materials Science | Method of crushing electronic equipment |
CN113121209A (en) * | 2021-03-26 | 2021-07-16 | 福建华清电子材料科技有限公司 | Preparation method of 996 aluminum oxide ceramic substrate |
CN112916143A (en) * | 2021-05-11 | 2021-06-08 | 上海集熠节能环保技术有限公司 | High-efficient super smart grinder |
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