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JPH06104208B2 - Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill - Google Patents
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JPH06104208B2 - Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill - Google Patents

Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill

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Publication number
JPH06104208B2
JPH06104208B2 JP31394489A JP31394489A JPH06104208B2 JP H06104208 B2 JPH06104208 B2 JP H06104208B2 JP 31394489 A JP31394489 A JP 31394489A JP 31394489 A JP31394489 A JP 31394489A JP H06104208 B2 JPH06104208 B2 JP H06104208B2
Authority
JP
Japan
Prior art keywords
raw material
outer cylinder
material supply
crushing
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.)
Expired - Lifetime
Application number
JP31394489A
Other languages
Japanese (ja)
Other versions
JPH03174262A (en
Inventor
聡 奥田
努 山本
Original Assignee
三興空気装置株式会社
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Filing date
Publication date
Application filed by 三興空気装置株式会社 filed Critical 三興空気装置株式会社
Priority to JP31394489A priority Critical patent/JPH06104208B2/en
Publication of JPH03174262A publication Critical patent/JPH03174262A/en
Publication of JPH06104208B2 publication Critical patent/JPH06104208B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、連続乾式混流槽ミルにより原料粒子をミク
ロンオーダ以下の超微粒子に微粉砕する方法およびその
装置に関する。
Description: TECHNICAL FIELD The present invention relates to a method and an apparatus for finely pulverizing raw material particles into ultrafine particles of a micron order or less by a continuous dry mixing tank mill.

従来の技術 粉体の微粉砕は、粒子または粒子層に圧縮、剪断、衝撃
などの力を作用させ、数ミクロン以下まで粉砕すること
であり、その微粉砕機としてはローラミル、ボールミ
ル、ジエットミル、媒体攪拌ミルなどが知られている。
BACKGROUND ART Fine pulverization of powder is performed by applying a force such as compression, shear, or impact to particles or a particle layer to pulverize it to several microns or less. The pulverizers are roller mills, ball mills, jet mills, and media. Stirring mills and the like are known.

また、ミロクオンオーダ以下の超微粒子を得るには、ジ
エットミル、ボールミル、あるいは媒体攪拌ミルなどが
使用されている。
Further, a jet mill, a ball mill, a medium agitation mill, or the like is used to obtain ultrafine particles of a miloquan order or less.

しかし、ジエットミルなどの衝撃方式では、粉砕限界粒
度に限度があり、また媒体攪拌ミル、ボールミルでは、
粉砕媒体としてボールなどを使用するため汚染の原因と
なったり、限界粒度付近では逆粉砕現象を起したりす
る。
However, in impact methods such as jet mill, there is a limit to the crushing limit particle size, and in media stirring mills and ball mills,
Since balls or the like are used as the crushing medium, it may cause pollution or cause a reverse crushing phenomenon near the critical particle size.

したがって、衝撃だけにより粉体を微粉砕するには限度
があり、また汚染を避けるには粉砕媒体を用いないこと
が望まれる。
Therefore, there is a limit to finely pulverize the powder only by impact, and it is desirable to use no pulverizing medium to avoid contamination.

発明が解決しようとする課題 上記のごとく、機械的に衝撃だけを加えて、粉体を微粉
砕するには限界があり、ミクロンオーダ以下の超微粉砕
は困難であった。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention As described above, there is a limit to finely pulverize powder by mechanically applying only impact, and it is difficult to perform ultrafine pulverization on the order of microns or less.

この発明は、機械的な衝撃や粉砕媒体を用いることな
く、原料粒子間の効果的な摩擦力により超微粉砕する方
法および、その装置を提供するものである。
The present invention provides a method and an apparatus for ultrafine pulverization by effective frictional force between raw material particles without using mechanical impact or a pulverization medium.

課題を解決するための手段 上記目的を達成するため、この発明の微粉砕方法は外筒
の上半部に内筒を設けて形成した粉砕部に対し、下半部
に設けた逆円錐状筒体の原料供給部を設け、原料供給部
と外筒との空隙をエアシールし、かつ粉砕部上方から下
向きに空気を吹き込みながら、原料供給部を回転して原
料粒子を旋回上昇させ粉砕部内で混合流動せしめ、原料
粒子間の直接摺動摩擦による表面粉砕により原料を微粉
砕し、内筒上部に設けた分級器を介して超微粒子のみを
外部へ吸引して収集する。
Means for Solving the Problems In order to achieve the above object, the fine pulverization method of the present invention is a crushing part formed by providing an inner cylinder in the upper half of an outer cylinder, and an inverted conical cylinder provided in the lower half. The raw material supply part of the body is provided, the gap between the raw material supply part and the outer cylinder is air-sealed, and while the air is blown downward from above the crushing part, the raw material supply part is rotated to swirl up the raw material particles to mix in the crushing part. The raw material is finely pulverized by fluidizing and surface pulverization by direct sliding friction between the raw material particles, and only ultrafine particles are sucked and collected outside through a classifier provided in the upper part of the inner cylinder.

また、原料を超微粉砕するための連続乾式混流槽ミル
は、外筒の上半部内周面に複数の邪魔板を等間隔で縦向
きに配設し、外筒の上に冠着し回転式分級器と収集孔を
有する蓋体に、上記邪魔板の先端全長にほぼ当接する大
きさの内筒を垂設して、その外筒と内筒の間に邪魔板で
区画された複数の粉砕部を形成し、外筒の下半部に逆円
錐状筒体で内周面に複数の駆動板を等間隔で縦向きに配
設してなる原料供給部を、外筒の底板を貫通した回転軸
に軸支し、モータにより駆動するように設け、かつ外部
に設けた原料供給装置の先端部を外筒および内筒を貫通
して原料供給部上に望ませ、外筒底面および外筒周面上
部より空気を送入するように設ける。
In addition, a continuous dry mixing tank mill for ultra-fine pulverization of raw materials has a plurality of baffle plates arranged vertically at equal intervals on the inner peripheral surface of the upper half of the outer cylinder, and is capped and rotated on the outer cylinder. An inner cylinder of a size that substantially abuts the entire length of the tip of the baffle is hung vertically on a lid having a type classifier and a collection hole, and a plurality of baffle plates partitioned by the baffle are provided between the outer and inner cylinders. The crushing part is formed, and the bottom plate of the outer cylinder is penetrated by the raw material supply section, which is a reverse cone-shaped cylindrical body in the lower half of the outer cylinder and has a plurality of drive plates arranged vertically at equal intervals on the inner peripheral surface. The outer end of the outer cylinder and the bottom of the outer cylinder are made to pass through the outer cylinder and the inner cylinder so that the tip end of the material supply device provided outside is supported by the rotating shaft and is driven by the motor. It is installed so that air can be sent in from the upper part of the cylinder surface.

作用 連続乾式混流槽ミルの原料供給部に装入された原料は、
原料供給部の回転により旋回上昇して粉砕部へ入り、こ
こで粉砕部上方から下向きに吹き込まれる空気により混
合流動する間に、原料粒子間の直接摺動摩擦により表面
破砕が起り微粉砕され、ミクロンオーダ以下の超微粒子
微粉を効率よく作ることができる。
The raw material charged in the raw material supply part of the continuous dry mixed flow mill is
When the raw material supply unit rotates, it rises up to enter the crushing unit, where it is mixed and flowed by the air blown downward from above the crushing unit. It is possible to efficiently produce ultrafine particles of the order or less.

実施例 この発明の実施例を図面に基づいて説明する。Embodiment An embodiment of the present invention will be described with reference to the drawings.

第1図は、この発明の実施による混流槽ミル(1)の断
面図である。この混流槽ミルは、外筒(4)の上半部の
内周面に沿って粉砕部(2)を、下半部に原料供給部
(3)を設けてなる。
FIG. 1 is a sectional view of a mixed flow tank mill (1) according to an embodiment of the present invention. This mixed flow tank mill is provided with a crushing section (2) along the inner peripheral surface of the upper half of the outer cylinder (4) and a raw material supply section (3) in the lower half.

上記粉砕部(2)は、第1図および第2図(a)に示す
ように、円筒(2−1)に複数(図面には4本を示す)
の突条からなる邪魔板(2−2)を等間隔で縦向きに配
設した邪魔板群を外筒(4)の上半部に嵌め込み、邪魔
板の先端全長にほぼ当接する大きさで蓋体(5)に垂設
した内筒(6)を組合せて複数の粉砕室を形成してな
る。
As shown in FIG. 1 and FIG. 2 (a), the crushing section (2) has a plurality of cylinders (2-1) (four are shown in the drawing).
The baffle plates (2-2) consisting of the ridges are arranged vertically at equal intervals, and the baffle group is fitted into the upper half of the outer cylinder (4) so that the baffle plate substantially abuts the entire length of the tip of the baffle plate. A plurality of crushing chambers are formed by combining an inner cylinder (6) suspended from a lid (5).

また、原料供給部(3)は、逆円錐状筒体(3−1)の
内周面に複数(図面には4本を示す)の突条からなる駆
動板(3−2)を等間隔で縦向きに配設してなり、外筒
(4)の底板を貫通した回転軸(7)の上端に原料供給
部(3)の筒底部分を取着して回転自在に設けてなる。
Further, the raw material supply part (3) has a drive plate (3-2) consisting of a plurality of (four in the drawing are shown) ridges on the inner peripheral surface of the inverted conical cylinder (3-1) at equal intervals. In the vertical direction, the cylinder bottom portion of the raw material supply section (3) is attached to the upper end of the rotary shaft (7) penetrating the bottom plate of the outer cylinder (4) so as to be rotatable.

なお逆円錐状筒体(3−1)の上縁外周と外筒(4)と
の間に形成される空隙(3−3)はなるべく小さくし、
かつ原料供給部側の外周にはテフロンを貼着することが
望ましい。外筒(4)の上部には原料送入装置の先端部
(8)を貫通して内筒(6)内に望ませ、原料を原料供
給部(3)に装入できるように構成する。
In addition, the space (3-3) formed between the outer periphery of the upper edge of the inverted conical cylindrical body (3-1) and the outer cylinder (4) is made as small as possible,
In addition, it is desirable to attach Teflon to the outer periphery of the raw material supply unit side. The upper part of the outer cylinder (4) penetrates through the tip part (8) of the raw material feeding device to be desired in the inner cylinder (6) so that the raw material can be charged into the raw material supply part (3).

蓋体(5)は、中心上面にモータ(9−1)が載設さ
れ、下向きに垂設したモータ軸(9−2)の先端に回転
式分級器(9)が設けられている。そして、回転式分級
器(9)の上側の周面に収集孔(5−1)を設ける。こ
の蓋体(5)は、粉砕部(2)との間に所要の空間(1
0)を形成して外筒(4)に冠着されており、その空間
(10)に空気孔(11)が設けられ、送入された空気は粉
砕部(2)内を下降するようにする。また、外筒(4)
の底板には多数の小径の空気孔を穿設した円環状の空気
通路(12−1)が設けられ、底板に貫通した空気孔(1
2)から送入される空気が空気通路(12−1)の空気孔
から噴出して空隙(3−3)を上昇して空隙部分にエア
シールが形成されるように設ける。
A motor (9-1) is mounted on the central upper surface of the lid (5), and a rotary classifier (9) is provided at the tip of a motor shaft (9-2) vertically hung downward. Then, a collection hole (5-1) is provided on the upper peripheral surface of the rotary classifier (9). This lid (5) is a required space (1) between it and the crushing section (2).
0) is formed and is crowned to the outer cylinder (4), an air hole (11) is provided in the space (10), and the introduced air descends in the crushing section (2). To do. Also, the outer cylinder (4)
The bottom plate is provided with an annular air passage (12-1) having a large number of small air holes, and the air holes (1
The air introduced from 2) is ejected from the air hole of the air passage (12-1) and rises in the void (3-3) to form an air seal in the void portion.

上記混流槽ミル(1)を用いて粉体を連続して超微粉砕
する装置の具体例を第3図に示す。
FIG. 3 shows a specific example of an apparatus for continuously finely pulverizing powder using the above mixed flow mill (1).

混流槽ミル(1)の回転軸(7)にはモータ(13)を接
続して原料供給部(3)を回転するように設け、一方蓋
体(5)の収集孔(5−1)にはバグフイルタ(14)と
の間を接続する配管(15)の一端が接合される。また、
空気孔(11)と(12)はルーツブロワ(16)との間を配
管(17)で接続する。図中の(18)は排気用のブロワ、
(19)はモータ(13)の操作盤である。そして、原料送
入装置(20)に付設したホッパに貯留された原料を連続
して原料供給部(3)に装入できるようにする。
A motor (13) is connected to the rotating shaft (7) of the mixed-flow tank mill (1) so as to rotate the raw material supply part (3), and the collection hole (5-1) of the lid (5) is provided. Is joined to one end of a pipe (15) connecting the bag filter (14). Also,
The air holes (11) and (12) are connected to the roots blower (16) by a pipe (17). (18) in the figure is an exhaust blower,
(19) is an operation panel for the motor (13). Then, the raw material stored in the hopper attached to the raw material feeding device (20) can be continuously charged into the raw material supply section (3).

今、原料送入装置(20)を始動して原料を原料供給部
(3)を装入するとともに、モータ(13)を始動して原
料供給部(3)を回転させ、かつルーツブロワ(16)と
ブロワ(18)を始動し、空気孔(12)から吹き込まれる
空気は空隙(3−3)より上昇してエアシールが形成さ
れ、粉砕部(2)から下降する微粉粒子が外筒の下部へ
落下するのを防止し、空気孔(11)から吹き込まれる空
気は空間(10)内を旋回して粉砕部内を下降し粉砕部の
下端から出たのち内筒(6)内を上昇して回転式分級器
(9)、配管(15)、バグフイルタ(14)およびブロワ
(18)を経て混合槽ミル(1)内の空気を吸引して排気
させる。すると、原料供給部(3)の原料は回転に伴う
遠心力の作用により周壁に沿って上昇し、上縁から離れ
たあとも旋回上昇して粉砕部(2)の各粉砕室に至り、
ここで原料粒子は邪魔板(2−2)に近づくにつれ徐々
に圧接され、しまいには滞留する。
Now, the raw material feeding device (20) is started to load the raw material into the raw material supply section (3), the motor (13) is started to rotate the raw material supply section (3), and the roots blower (16) Then, the blower (18) is started, and the air blown from the air hole (12) rises from the gap (3-3) to form an air seal, and the fine powder particles descending from the crushing section (2) go to the lower part of the outer cylinder. The air blown from the air holes (11) swirls in the space (10) and descends inside the crushing unit, exits from the lower end of the crushing unit and then rises and rotates inside the inner cylinder (6) to prevent falling. Air in the mixing tank mill (1) is sucked and exhausted through the type classifier (9), the pipe (15), the bag filter (14) and the blower (18). Then, the raw material of the raw material supply section (3) rises along the peripheral wall due to the action of centrifugal force due to the rotation, and swirls and rises even after being separated from the upper edge to reach each crushing chamber of the crushing section (2),
Here, the raw material particles are gradually brought into pressure contact with each other as they approach the baffle plate (2-2), and eventually stay.

この滞留帯にある粒子の運動速度は、極端に小さくな
り、体積粉砕を起すことなく、粒子間の直接摺動摩擦に
より表面破砕する。
The moving velocity of the particles in this retention zone becomes extremely small, and the surface is crushed by direct sliding friction between the particles without causing volume crushing.

微粉砕化した粒子は、空気孔(11)から吹き込まれる下
向きの空気により降下する。すると、原料供給部(3)
の上方において、微粉砕された粒子はブロワ(18)によ
り吸引される排気に引かれて内筒(6)の中を上昇して
回転式分級器(9)、配管(15)を経てバグフイルタ
(14)に貯留される。
The finely pulverized particles are lowered by the downward air blown from the air holes (11). Then, the raw material supply unit (3)
Above the above, the finely pulverized particles are attracted by the exhaust gas sucked by the blower (18) to rise in the inner cylinder (6) and pass through the rotary classifier (9) and the pipe (15) to the bag filter ( It is stored in 14).

一方、微粉砕が不十分な粒子は、上記回転式分級器
(9)にて分離され排気に吸引されることなく降下して
原料供給部(3)へ収容され、再度循環して微粉砕が行
なわれる。
On the other hand, particles that have not been finely pulverized are separated by the rotary classifier (9), fall without being sucked into the exhaust gas, and are accommodated in the raw material supply unit (3). Done.

なお、粉砕した後の微粒子を分級して超微粒子のみを分
離するための分級器は、回転式分級器を使用した場合に
ついて説明したが、この回転式に限ることなく、気流分
級器など他の形式のものが利用できる。
The classifier for classifying the fine particles after crushing to separate only the ultrafine particles has been described with respect to the case where a rotary classifier is used, but the classifier is not limited to this rotary type, and other types such as an air flow classifier are also used. Formats are available.

発明の効果 この発明は、上部に粉砕部を、下部に原料供給部を設け
た連続乾式混流槽ミルを使って、原料粒子を直接摺動摩
擦による表面粉砕により微粉砕するから、汚染すること
なくミクロンオーダ以下の超微粒子に微粉砕することが
できる。
EFFECTS OF THE INVENTION The present invention uses a continuous dry mixing tank mill having a crushing part in the upper part and a raw material supply part in the lower part to finely pulverize raw material particles by surface pulverization by direct sliding friction. It can be pulverized into ultrafine particles of the order or less.

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

第1図はこの発明の実施による連続乾式混流ミルの縦断
面図、第2図(a)は第1図A−A線上の横断面図、第
2図(b)は第1図B−B線上の横断面図、第3図はこ
の発明の微粉砕方法を実施するための装置の一例を示す
説明図である。 1……混流槽ミル 2……粉砕部 2−1……円筒、2−2……邪魔板 3……原料供給部 3−1……逆円錐状筒体、3−2……駆動板 4……外筒 5……蓋体、5−1……収集孔 6……内筒、7……回転軸 8……先端部、9……回転式分級器 10……空間、11、12……空気孔 13……モータ、14……バグフイルタ 16……ルーツブロワ、18……ブロワ 19……操作盤、20……原料送入装置
FIG. 1 is a longitudinal sectional view of a continuous dry mixed flow mill according to an embodiment of the present invention, FIG. 2 (a) is a lateral sectional view taken along the line AA in FIG. 1, and FIG. 2 (b) is FIG. 1B-B. FIG. 3 is an explanatory view showing an example of an apparatus for carrying out the pulverizing method of the present invention. 1 ... Mixed-flow tank mill 2 ... Crushing part 2-1 ... Cylinder, 2-2 ... Baffle plate 3 ... Raw material supply part 3-1 ... Inverted conical cylinder 3-2 ... Drive plate 4 …… Outer cylinder 5 …… Lid body, 5-1 …… Collection hole 6 …… Inner cylinder, 7 …… Rotating shaft 8 …… Tip, 9 …… Rotary classifier 10 …… Space, 11, 12… … Air holes 13 …… Motor, 14 …… Bag filter 16 …… Roots blower, 18 …… Blower 19 …… Operation panel, 20 …… Raw material feeding device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】外筒の上半部に内筒を設けて形成した粉砕
部に対し、下半部に設けた逆円錐状筒体の原料供給部を
設け、原料供給部と外筒との空隙をエアシールし、かつ
粉砕部上方から下向きに空気を吹き込みながら原料供給
部を回転して原料粒子を旋回上昇させ粉砕部内で混合流
動せしめ、原料粒子間の直接摺動摩擦による表面粉砕に
より原料を微粉砕し、内筒上部に設けた分級器を介して
超微粒子のみを外部へ吸引して収集することを特徴とす
る連続乾式混流槽ミルによる微粉砕方法。
1. A raw material supply part of an inverted conical cylindrical body provided in the lower half part is provided for a crushing part formed by providing an inner cylinder in the upper half part of the outer cylinder. The air gap is air-sealed, and while the air is blown downward from above the crushing part, the raw material supply part is rotated to swirl up the raw material particles to mix and flow them in the crushing part, and the raw material is finely divided by surface sliding by direct sliding friction between the raw material particles. A fine pulverization method using a continuous dry mixing tank mill, which comprises pulverizing, and sucking only ultrafine particles to the outside through a classifier provided on the upper part of the inner cylinder to collect.
【請求項2】外筒の上半部内周面に複数の邪魔板を等間
隔で縦向きに配設し、外筒の上に冠着し回転式分級器と
収集孔を有する蓋体に、上記邪魔板の先端全長にほぼ当
接する大きさの内筒を垂設して、外筒と内筒の間に邪魔
板で区画された複数の粉砕部を形成し、外筒の下半部に
逆円錐状筒体で内周面に複数の駆動板を等間隔で縦向き
に配設してなる原料供給部を、外筒の底板を貫通した回
転軸に軸支し、モータにより駆動するように設け、かつ
外部に設けた原料供給装置の先端部を外筒および内筒を
貫通して原料供給部上に望ませ、外筒底面および外筒周
面上部に空気送入孔を設けた連続乾式混合槽ミル。
2. A lid body having a plurality of baffle plates vertically arranged at equal intervals on an inner peripheral surface of an upper half portion of an outer cylinder, capped on the outer cylinder, having a rotary classifier and a collection hole, An inner cylinder of a size that substantially abuts the entire length of the front end of the baffle plate is hung vertically to form a plurality of crushing parts partitioned by the baffle plate between the outer and inner cylinders, and the lower half part of the outer cylinder is formed. A raw material supply section, which is an inverted conical tubular body and has a plurality of drive plates vertically arranged at equal intervals on its inner peripheral surface, is rotatably supported by a rotary shaft that penetrates the bottom plate of the outer cylinder and driven by a motor. The outer end and the inner end of the raw material supply device are provided on the outer cylinder and the inner cylinder so that they are desired on the raw material supply section. Dry mixing tank mill.
JP31394489A 1989-12-01 1989-12-01 Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill Expired - Lifetime JPH06104208B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31394489A JPH06104208B2 (en) 1989-12-01 1989-12-01 Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31394489A JPH06104208B2 (en) 1989-12-01 1989-12-01 Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill

Publications (2)

Publication Number Publication Date
JPH03174262A JPH03174262A (en) 1991-07-29
JPH06104208B2 true JPH06104208B2 (en) 1994-12-21

Family

ID=18047383

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31394489A Expired - Lifetime JPH06104208B2 (en) 1989-12-01 1989-12-01 Method and apparatus for fine pulverization by continuous dry mixed-flow tank mill

Country Status (1)

Country Link
JP (1) JPH06104208B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8281620B1 (en) * 2011-04-27 2012-10-09 Japan Super Quartz Corporation Apparatus for manufacturing vitreous silica crucible
KR101118568B1 (en) * 2011-05-16 2012-02-27 (주)제이분체 Compound Powder Manufacturing Equipment

Also Published As

Publication number Publication date
JPH03174262A (en) 1991-07-29

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