JPH074553B2 - Friction grinding method for raw materials - Google Patents
Friction grinding method for raw materialsInfo
- Publication number
- JPH074553B2 JPH074553B2 JP2136840A JP13684090A JPH074553B2 JP H074553 B2 JPH074553 B2 JP H074553B2 JP 2136840 A JP2136840 A JP 2136840A JP 13684090 A JP13684090 A JP 13684090A JP H074553 B2 JPH074553 B2 JP H074553B2
- Authority
- JP
- Japan
- Prior art keywords
- rotating body
- particle size
- raw material
- raw materials
- friction
- 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 - Fee Related
Links
Landscapes
- Crushing And Grinding (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は農産物や鉱物等の原料を旋回運動させ、その原
料が互いにすり合って摩擦粉砕することにより、粒径が
非常に小さな超微粉を得ることが出来ると共に平均粒径
及び粒径分布を制御することが可能である原料の摩擦粉
砕方法に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention makes raw materials such as agricultural products and minerals rotate, and the raw materials rub against each other and frictionally pulverize to produce ultrafine powder having a very small particle size. The present invention relates to a friction grinding method for raw materials which can be obtained and whose average particle size and particle size distribution can be controlled.
(従来の技術) 従来、殻物や鉱物等の原料を細かく粉砕する方法として
は、ボールミル,振動ミル,ハンマーミル等を用いて粉
砕していた。しかし、この場合には、ボール,ランナ
ー,ハンマー等の摩耗が著しく、粉砕物の中に異物の混
入が多くなる。また従来の粉砕方法ではサブミクロン粒
子を得るためには粉砕機を長時間駆動する必要がある。(Prior Art) Conventionally, as a method for finely crushing raw materials such as shells and minerals, a ball mill, a vibration mill, a hammer mill or the like has been used. However, in this case, the wear of the balls, runners, hammers, etc. is remarkable, and the amount of foreign matter mixed in the pulverized material increases. Further, in the conventional crushing method, it is necessary to drive the crusher for a long time in order to obtain submicron particles.
(発明が解決しようとする問題点) 従来の粉砕方法では、原料を微粉粉砕するために要する
エネルギー消費が大きく、粉砕時間も長い。従って粉砕
効率が非常に悪く、且つ処理能力に限界がある。また粉
砕物の粒径分布は粉砕機によりほぼ決定されており、そ
の粒径分布を変えることは極めて困難である等の問題点
があった。(Problems to be Solved by the Invention) In the conventional pulverizing method, the energy consumption required for pulverizing the raw material into a fine powder is large and the pulverizing time is long. Therefore, the grinding efficiency is very poor and the processing capacity is limited. Further, the particle size distribution of the crushed product is almost determined by the crusher, and it is extremely difficult to change the particle size distribution.
本発明は粒径が非常に小さな超微粉を作業能率良く、且
つ簡単に得ることが出来ると共に平均粒径及び粒径分布
を制御可能とした原料の摩擦粉砕方法を提供することを
目的とする。An object of the present invention is to provide a raw material friction pulverization method capable of obtaining ultrafine powder having a very small particle size with good working efficiency and easily and controlling the average particle size and particle size distribution.
(問題点を解決するための手段) 本発明は上記問題点を解決するために成されたものであ
り、つまりケーシング内に対向し独立駆動する第1回転
体と第2回転体間に原料を供給し、その原料を、高速回
転する第1回転体と第2回転体によって旋回運動させる
ことで、前記原料が互いにすり合い摩擦粉砕され、該摩
擦粉砕された原料を回転中心側から回収する原料の摩擦
粉砕方法と成す。(Means for Solving Problems) The present invention has been made to solve the above problems, that is, a raw material is provided between a first rotating body and a second rotating body that face each other in a casing and are independently driven. A raw material which is supplied and swirled by a first rotating body and a second rotating body which rotate at high speed, so that the raw materials are rubbed against each other and frictionally ground, and the frictionally ground raw material is recovered from the rotation center side. The friction grinding method of.
(作 用) 次に本発明の作用について説明する。先ず原料(7)は
投入口(4)から投入し、第1回転体(2)と第2回転
体(3)との間に供給される。この第1回転体(2)と
第2回転体(3)との間及びケーシング(1)内壁とで
囲まれた空間、以降はこの空間を粉砕ゾーン(6)と呼
ぶ。この粉砕ゾーン(6)に於て原料(7)は径方向一
定位置に集められて動的充填層が形成される(第1図参
照)。前記粉砕ゾーン(6)で動的充填層を形成した原
料(7)は、第1回転体(2)と第2回転体(3)の回
転により旋回運動するため原料(7)の粒子には遠心力
が作用し、この遠心力によって各粒子が互いに径方向で
押付けられた状態で運動する。この時の旋回速度は、第
1回転体(2)或は第2回転体(3)から離れるに従っ
て速度が変化するため、原料(7)が互いにすり合いな
がら摩擦粉砕され、その摩擦粉砕された微粉は回転中心
に向い、前記微粉が適宜位置に集まって層を形成し、更
にその層に於ても摩擦粉砕され一層粒径を小さくしてい
くのである(第2図参照)。このように粉砕ゾーン
(6)のあらゆる位置で摩擦粉砕が行われ、これを繰返
せば粒径は限りなく小さくなるのである。尚、粒子の大
きさは遠心力の作用で外周から回転中心に向って順次小
さなものが集まり、その最も細かい粒径のものは、図示
しない吸引ファン等の回収手段を用いて第2回転体
(3)の中心部から排出口(5)に運ばれて回収される
のである。(Operation) Next, the operation of the present invention will be described. First, the raw material (7) is charged through the charging port (4) and is supplied between the first rotating body (2) and the second rotating body (3). A space surrounded by the first rotating body (2) and the second rotating body (3) and the inner wall of the casing (1), and hereinafter, this space is referred to as a crushing zone (6). In the crushing zone (6), the raw material (7) is collected at a fixed position in the radial direction to form a dynamic packed bed (see FIG. 1). The raw material (7) having a dynamic packed bed formed in the crushing zone (6) is swirled by the rotation of the first rotating body (2) and the second rotating body (3), so that the particles of the raw material (7) are A centrifugal force acts, and the centrifugal force causes the particles to move while being pressed against each other in the radial direction. The turning speed at this time changes as it moves away from the first rotating body (2) or the second rotating body (3), so that the raw materials (7) are rubbed and rubbed with each other, and the pulverized rubbed. The fine powder is directed toward the center of rotation, and the fine powder gathers at appropriate positions to form a layer, and the layer is further friction-ground to further reduce the particle size (see FIG. 2). In this way, frictional pulverization is performed at every position in the pulverization zone (6), and if this is repeated, the particle size becomes extremely small. In addition, the size of the particles is gradually reduced from the outer periphery toward the center of rotation by the action of centrifugal force, and the smallest size of the particles is collected by a second rotating body (not shown) using a collecting means such as a suction fan. It is transported from the center of 3) to the discharge port (5) and collected.
また前記原料(7)の摩擦粉砕時、粉砕ゾーン(6)に
於ては吸引ファンの吸引作用等で回転中心に向う気流が
発生するため、原料(7)の粒子層はケーシング(1)
内壁に接触することなく旋回運動でき、前記内壁が粒子
の運動によって摩耗されない。更に、第1回転体(2)
と第2回転体(3)は接触する粒子とほぼ同じ速度で運
動しているので、前記第1回転体(2)と第2回転体
(3)には摩耗が少なく、長時間連続させて粉砕し続け
ても効率良く粉砕が行われる。しかもこの時、第1回転
体(2)と第2回転体(3)の回転速度と、微粒子の吸
引速度とを制御することにより、粉砕物の平均粒径と粒
径分布が制御可能となる。つまり、吸引ファン等の吸引
速度を一定にさせ、第1回転体(2)と第2回転体
(3)の回転速度を大きくすれば平均粒径は小さくな
り、また前記吸引速度を速くさせていくに従って平均粒
径は大きくなるが、粉砕粒径分布は揃うのである。Further, when the raw material (7) is frictionally pulverized, an air flow toward the center of rotation is generated in the pulverization zone (6) due to the suction action of the suction fan, etc., so that the particle layer of the raw material (7) is formed in the casing (1).
It can be swiveled without contacting the inner wall, and the inner wall is not worn by the movement of particles. Furthermore, the first rotating body (2)
Since the second rotating body (3) and the second rotating body (3) move at almost the same speed as the particles that come into contact with each other, the first rotating body (2) and the second rotating body (3) are less worn and can be continuously used for a long time. Even if the crushing is continued, the crushing is efficiently performed. Moreover, at this time, by controlling the rotation speeds of the first rotating body (2) and the second rotating body (3) and the suction speed of the fine particles, it becomes possible to control the average particle size and the particle size distribution of the pulverized product. . That is, if the suction speed of the suction fan or the like is kept constant and the rotation speeds of the first rotating body (2) and the second rotating body (3) are increased, the average particle size is reduced, and the suction speed is increased. The average particle size increases as it goes, but the crushed particle size distribution becomes uniform.
(実施例) 以下本発明の実施例を図面に基づいて説明すると、
(1)はケーシングであり、(2)はケーシング(1)
内に設けた回転自在な回転翼或は円板状の第1回転体で
ある。(3)は第1回転体(2)と対向させてケーシン
グ(1)内に設けた回転自在な回転翼或は円板状の第2
回転体であり、該第2回転体(3)の中心部には、適宜
大きさの吸引穴が穿設されている。また前記第2回転体
(3)は水平方向にスライドさせて第1回転体(2)と
の間隔を調節可能と成す。又、各回転体(2),(3)
の回転速度及び回転方向は独立に設定可能である。尚、
この構造については一般的なものを使えば容易に可能で
あるので、これ以上の説明は省略する。(4)はケーシ
ング(1)の側面に設けた投入口である。(5)は投入
口(4)と反対方向のケーシング(1)側面に設けた排
出口であり、この排出口(5)は第2回転体(3)の中
心部と連通する。(6)はケーシング(1)内壁と第1
回転体(2)及び第2回転体(3)とによって囲まれた
空間、つまり粉砕ゾーンである。(Example) Hereinafter, an example of the present invention will be described with reference to the drawings.
(1) is a casing, (2) is a casing (1)
It is a rotatable rotary blade or a disk-shaped first rotating body provided inside. (3) is a rotatable rotor or disk-shaped second rotor provided inside the casing (1) facing the first rotor (2).
It is a rotating body, and a suction hole of an appropriate size is bored in the center of the second rotating body (3). Further, the second rotating body (3) can be slid in the horizontal direction to adjust the distance between the second rotating body (3) and the first rotating body (2). Also, each rotating body (2), (3)
The rotation speed and rotation direction of can be set independently. still,
This structure can be easily made by using a general structure, and therefore further description will be omitted. (4) is an inlet provided on the side surface of the casing (1). Reference numeral (5) is an outlet provided on the side surface of the casing (1) opposite to the inlet (4), and the outlet (5) communicates with the central portion of the second rotating body (3). (6) is the inner wall of the casing (1) and the first
A space surrounded by the rotating body (2) and the second rotating body (3), that is, a crushing zone.
次に本発明の方法についてに説明すると、予め第1回転
体(2)と第2回転体(3)とを高速回転回転させてお
く。先ず原料(7)を投入口(4)から投入すると、そ
の原料(7)は第1回転体(2)と第2回転体(3)と
の間に供給されて粉砕ゾーン(6)に入る。該粉砕ゾー
ン(6)に入った大きな粒径の原料(7)は遠心力のた
め外周へ追いやられ、動的充填層を第1回転体(2)と
第2回転体(3)の間に形成する。粉砕ゾーン(6)で
動的充填層を形成した原料(7)は、第1回転体(2)
と第2回転体(3)の回転によって原料(7)は第2図
に示す如く同粒径が互いにすり合いながら摩擦粉砕さ
れ、この摩擦粉砕された原料(7)は回転中心に向い、
径方向の適宜位置に集まり、それが更に摩擦粉砕され
る。すると順次小さな粒径に従って外周から分級した粒
子充填層が形成される。前記回転中心には最も細かい粒
径のものが集まり、その最も粉かい粒径のものを第2回
転体(3)の中心部から排出口(5)へ図示しない回収
手段を用いて運び、その後、排出口(5)から微粉のみ
を回収する。Next, the method of the present invention will be described. The first rotating body (2) and the second rotating body (3) are rotated in advance at high speed. First, when the raw material (7) is charged from the charging port (4), the raw material (7) is supplied between the first rotating body (2) and the second rotating body (3) and enters the crushing zone (6). . The raw material (7) having a large particle size, which has entered the crushing zone (6), is driven to the outer periphery by centrifugal force, and the dynamic packed bed is placed between the first rotating body (2) and the second rotating body (3). Form. The raw material (7) that has formed the dynamic packed bed in the crushing zone (6) is the first rotating body (2).
By the rotation of the second rotating body (3), the raw material (7) is frictionally crushed while having the same particle diameters as shown in FIG. 2, and the frictionally pulverized raw material (7) faces the center of rotation.
Collected at appropriate positions in the radial direction, and further crushed by friction. Then, a particle-packed layer is formed which is classified from the outer periphery in order of smaller particle size. The finest particle size is collected at the rotation center, and the finest particle size is carried from the central portion of the second rotating body (3) to the discharge port (5) by using a recovery means (not shown), and thereafter. , Collect only fine powder from the outlet (5).
(発明の効果) 本発明は以上説明したように構成されているので、以下
に記載されるような効果を奏する。(Effects of the Invention) Since the present invention is configured as described above, it has the effects described below.
従来の如き粉砕機で長時間粉砕を行わなくとも原料
(7)が互いにすり合いながら摩擦粉砕されるので、短
時間に効率良く微粉となり、しかも粉砕するために要す
るエネルギーが従来に比べて激減する。The raw materials (7) are friction crushed while rubbing each other even if they are not crushed for a long time with a conventional crusher, so they become fine powder efficiently in a short time, and the energy required for crushing is drastically reduced compared to the conventional one. .
粉砕能率が極めて良いため、微粉の大幅なコストダウ
ンが可能となる。Since the pulverization efficiency is extremely good, it is possible to significantly reduce the cost of fine powder.
摩擦粉砕を粉砕ゾーン(6)で繰返し行うことによ
り、サブミクロン粒子を得ることができ、且つ平均粒径
の大きさも限りなく小さくすることが可能である。By repeating friction grinding in the grinding zone (6), submicron particles can be obtained, and the average particle size can be made as small as possible.
第1回転体(2)と第2回転体(3)との間隔、それ
らの各回転速度及び回転方向、そして吸引速度を変える
ことにより、原料(7)の粉砕粒径及び粒径分布を容易
に制御することが可能である。The crushed particle size and particle size distribution of the raw material (7) can be easily changed by changing the interval between the first rotator (2) and the second rotator (3), their respective rotation speeds and directions, and the suction speeds. It is possible to control.
装置の摩耗部分が少ないので、摩擦粉砕物中への異物
の混入が非常に少なく、良質の微粉が得られる。Since the wear portion of the device is small, foreign matter is not significantly mixed into the friction pulverized product, and fine powder of good quality can be obtained.
連続運転時に於ける装置の摩耗による粉砕物の平均粒
径と粒径分布の経時変化が殆ど無いため、メンテナンス
が非常に簡単である。Maintenance is very easy because there is almost no change over time in the average particle size and particle size distribution of the ground product due to wear of the device during continuous operation.
第1図は本発明に係る実施例を示す説明図、第2図は原
料が互いに繰返し摩擦粉砕される状態を示す説明図であ
る。 (1)……ケーシング、(2)……第1回転体 (3)……第2回転体、(7)……原料FIG. 1 is an explanatory view showing an embodiment according to the present invention, and FIG. 2 is an explanatory view showing a state in which raw materials are repeatedly crushed by friction. (1) …… Casing, (2) …… First rotating body (3) …… Second rotating body, (7) …… Raw material
Claims (1)
第1回転体(2)と第2回転体(3)間に原料(7)を
供給し、その原料(7)が互いにすり合い摩擦粉砕さ
れ、該摩擦粉砕された原料(7)を回転中心側から回収
することを特徴とする原料の摩擦粉砕方法。1. A raw material (7) is supplied between a first rotating body (2) and a second rotating body (3) which face each other in a casing (1) and are independently driven, and the raw materials (7) are rubbed with each other. A friction pulverizing method of a raw material, which is friction pulverized and recovers the friction pulverized raw material (7) from a rotation center side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2136840A JPH074553B2 (en) | 1990-05-25 | 1990-05-25 | Friction grinding method for raw materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2136840A JPH074553B2 (en) | 1990-05-25 | 1990-05-25 | Friction grinding method for raw materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0429757A JPH0429757A (en) | 1992-01-31 |
| JPH074553B2 true JPH074553B2 (en) | 1995-01-25 |
Family
ID=15184734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2136840A Expired - Fee Related JPH074553B2 (en) | 1990-05-25 | 1990-05-25 | Friction grinding method for raw materials |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH074553B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH682465A5 (en) * | 1988-06-09 | 1993-09-30 | Buehler Ag | Agitator-type grinder assembly |
-
1990
- 1990-05-25 JP JP2136840A patent/JPH074553B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0429757A (en) | 1992-01-31 |
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