JPH0871439A - Crusher - Google Patents
CrusherInfo
- Publication number
- JPH0871439A JPH0871439A JP6211070A JP21107094A JPH0871439A JP H0871439 A JPH0871439 A JP H0871439A JP 6211070 A JP6211070 A JP 6211070A JP 21107094 A JP21107094 A JP 21107094A JP H0871439 A JPH0871439 A JP H0871439A
- Authority
- JP
- Japan
- Prior art keywords
- rotor
- stator
- crusher
- crushing
- solid substance
- 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
- Developing Agents For Electrophotography (AREA)
- Crushing And Grinding (AREA)
- Crushing And Pulverization Processes (AREA)
Abstract
(57)【要約】 (修正有)
【目的】機内発熱が小さく、所定の粒子径に粉砕する際
の粉砕性が良好な粉砕機を提供。
【構成】回転軸に支持され、外側表面の母線に沿って多
数の凹凸部を有する回転子Aと、回転子との間に間隙を
存して嵌装された内側表面の母線に沿って多数の凹凸部
を有する固定子Bとを有し、固定子の外側表面一端の口
1から固体物質を供給し、回転子を回転させながら、一
端から当該固定子の外側表面一端の口2に向けて気体の
流れで固体物質を移動させながら、回転子と固定子との
間で固体物質を所定の大きさに粉砕する粉砕機におい
て、
1.回転子の外側表面の凹凸を、内壁に曲線部分と直線
部分を含む凹部形状が連続する歯形となし、
2.固定子と対向する様に、回転子の凹部内壁の回転方
向に向いた壁の直線部(粉砕面)を回転子の接線に対し
て70〜30°となる様に、直線部(粉砕面)先端を回転子
の回転方向の反対側に傾けた。
(57) [Summary] (Corrected) [Purpose] To provide a crusher with low heat generation inside the machine and good crushability when crushing to a specified particle size. [Structure] A rotor A supported by a rotating shaft and having a large number of irregularities along the generatrix of an outer surface, and a large number along a generatrix of an inner surface fitted with a gap between the rotor and the rotor A. And a stator B having a concavo-convex portion, and a solid substance is supplied from a mouth 1 at one end of the outer surface of the stator, and while the rotor is rotated, the solid substance is directed from one end to a mouth 2 at one end of the outer surface of the stator. In a crusher for crushing a solid substance into a predetermined size between a rotor and a stator while moving the solid substance with a gas flow. 1. The unevenness of the outer surface of the rotor is a tooth profile in which the inner wall has a continuous recessed portion including a curved portion and a straight portion. The straight portion (crushing surface) of the inner wall of the recess of the rotor facing the direction of rotation so that the straight portion (crushing surface) of the wall is 70 to 30 ° with respect to the tangent of the rotor so as to face the stator. The tip was tilted to the opposite side of the rotor rotation direction.
Description
【0001】[0001]
【産業上の利用分野】本発明は、固体の粉砕に利用でき
るが特に熱可塑性の樹脂、粉体トナーや熱変質を嫌うコ
ーヒー等の粉砕に有効な粉砕機に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a crusher which can be used for crushing solids, but is particularly effective for crushing thermoplastic resins, powder toners, coffee, etc. which are not susceptible to thermal alteration.
【0002】[0002]
【従来の技術】一般に熱可塑性物質を10ミクロンぐら
いに粉砕するための機械衝撃式粉砕機は、回転軸に支持
されその軸を中心に回転しうる外側表面の母線に沿って
多数の凹凸部を有する回転子(A)と、当該回転子
(A)との間に間隙を存して嵌装された内側表面の母線
に沿って多数の凹凸部を有する固定子(B)とを有し、
当該固定子(B)の外側表面一端の口(1)から固体物
質を供給し、当該回転子(A)を回転させながら、一端
(1)から当該固定子(B)の外側表面一端の口(2)
に向けて気体の流れで固体物質を移動させながら、回転
子(A)と固定子(B)との間で固体物質を所定の大き
さに粉砕する。2. Description of the Related Art Generally, a mechanical impact type crusher for crushing a thermoplastic material to about 10 microns has a large number of uneven portions along a generatrix of an outer surface which is supported by a rotary shaft and can rotate about the shaft. A rotor (A) having and a stator (B) having a large number of uneven portions along a generatrix of an inner surface fitted with a gap between the rotor (A) and
The solid substance is supplied from the mouth (1) at one end of the outer surface of the stator (B), and while rotating the rotor (A), the mouth of the one end of the outer surface of the stator (B) is fed from the one end (1). (2)
The solid substance is crushed to a predetermined size between the rotor (A) and the stator (B) while moving the solid substance with the flow of gas toward.
【0003】しかし、ここで得られる粉砕物には粗粒子
と微粒子が含まれている、粗粒子は粗粉分級機により分
級して粉砕機に戻し再粉砕される。微粒子も分級機によ
りカットされる、この様な工程を経て粉砕物は、所定の
粒度分布を持つ製品となる。この機械衝撃式粉砕機の問
題点は粉砕物に粗粒子が多く、戻し粗粒子の滞留量が原
料のフイード量の2〜3倍になり、そのため、粉砕機の
通過量が多いことにより機内発熱が多く又エア通過量も
落ちるため温度上昇によりフイード量が制約される。そ
の上過粉砕による微粉量も少なくない。However, the pulverized product obtained here contains coarse particles and fine particles. The coarse particles are classified by a coarse powder classifier and returned to the pulverizer for re-pulverization. The fine particles are also cut by the classifier, and the pulverized product becomes a product having a predetermined particle size distribution through such a process. The problem of this mechanical impact type crusher is that the crushed material contains many coarse particles, and the amount of retained coarse particles stays 2 to 3 times the feed amount of the raw material. Since the amount of air flow is large and the amount of air passing through is low, the amount of feed is restricted by the temperature rise. Moreover, the amount of fine powder due to over-pulverization is not small.
【0004】[0004]
【発明が解決しようとする課題】この解決策として回転
子の粉砕面先端を回転方向の後方に接線に対し70°以
下にすると粉砕性は上がるが、粉砕面が固定子凹凸面に
エアを押し付けるためエアの抜けが悪くなり焼き付いて
しまう。これは、その粉砕機に冷却ジャケットを設ける
とともに、冷気を通気させる様にして、機内を冷却して
も同様である。さらに粉砕すべき固体物質が、結着剤樹
脂を含む静電荷像現像用トナーの場合には、平均粒子径
7ミクロン以下に粉砕は出来ないものが多い。As a solution to this problem, if the tip of the crushing surface of the rotor is set to 70 ° or less with respect to the tangent to the rear in the rotation direction, the crushability is improved, but the crushing surface presses air against the uneven surface of the stator. As a result, the air will not escape properly and will burn. This is also the same as when the crusher is provided with a cooling jacket and the inside of the machine is cooled by ventilating cold air. Further, when the solid substance to be pulverized is a toner for developing an electrostatic charge image containing a binder resin, it is often impossible to pulverize it to an average particle size of 7 microns or less.
【0005】本発明は、必要とする大きさ範囲の粒子を
高収率で得られる様に粉砕することが出来、しかも機内
発熱が少ない粉砕機の提供を目的とするものである。It is an object of the present invention to provide a pulverizer which can pulverize particles in a required size range so as to obtain a high yield, and which generates less heat inside the pulverizer.
【0006】[0006]
【課題を解決するための手段】即ち本発明は、回転軸に
支持されその軸を中心に回転しうる外側表面の母線に沿
って多数の凹凸部を有する回転子(A)と、当該回転子
(A)との間に間隙を存して嵌装された内側表面の母線
に沿って多数の凹凸部を有する固定子(B)とを有し、
当該固定子(B)の外側表面一端の口(1)から固体物
質を供給し、当該回転子(A)を回転させながら、一端
(1)から当該固定子(B)の外側表面一端の口(2)
に向けて気体の流れで固体物質を移動させながら、回転
子(A)と固定子(B)との間で固体物質を所定の大き
さに粉砕する粉砕機において、 1.回転子(A)の外側表面の凹凸を、内壁に曲線部分
と直線部分を含む凹部形状が連続する歯形となし、 2.固定子(B)と対向する様に、回転子(A)の当該
凹部内壁の回転方向に向いた壁の直線部(粉砕面)を回
転子(A)の接線に対して70〜30°となる様に、直線部
(粉砕面)先端を回転子(A)の回転方向の反対側に傾
けた、ことを特徴とする粉砕機を提供するものである。That is, the present invention provides a rotor (A) having a large number of uneven portions along a generatrix of an outer surface which is supported by a rotary shaft and can rotate about the shaft, and the rotor. (A) and a stator (B) having a large number of concavo-convex portions along the generatrix of the inner surface fitted with a gap therebetween,
The solid substance is supplied from the mouth (1) at one end of the outer surface of the stator (B), and while rotating the rotor (A), the mouth of the one end of the outer surface of the stator (B) is fed from the one end (1). (2)
In a crusher for crushing a solid substance into a predetermined size between a rotor (A) and a stator (B), while moving the solid substance by a gas flow toward 1. 1. The unevenness on the outer surface of the rotor (A) has a tooth profile in which a recessed shape including a curved portion and a straight portion is continuous on the inner wall. The straight portion (crushing surface) of the wall of the rotor (A) facing the rotation direction of the inner wall of the recess so as to face the stator (B) is 70 to 30 ° with respect to the tangent line of the rotor (A). As described above, the present invention provides a crusher characterized in that the tip of the linear portion (crushing surface) is inclined to the opposite side of the rotation direction of the rotor (A).
【0007】次に本発明の粉砕機を図面に基づいて説明
する。第1図は、本発明の一例である、横型の粉砕機の
斜視図を示したものである。この図では、回転子Aと固
定子Bとの位置関係がわかる様に、開閉可能な固定子B
の一部を開いた開放状態が示されている。Next, the crusher of the present invention will be described with reference to the drawings. FIG. 1 is a perspective view of a horizontal crusher which is an example of the present invention. In this figure, the stator B that can be opened and closed is shown so that the positional relationship between the rotor A and the stator B can be seen.
The open state is shown with a part of the open.
【0008】この粉砕機は、横向きに固定された固定子
Bの内部に、横向きの回転子Aを有し、この回転子A
は、動力3により軸中心に回転出来る様になっている。
実際の粉砕機運転時には、この開いた部分の固定子Bは
閉じられる。機内メインテナンスや故障時には、上記し
た様に、この固定子Bはその一部を開放することが出来
る。This crusher has a horizontally oriented rotor A inside a horizontally fixed stator B.
Can be rotated about the axis by power 3.
During the actual operation of the crusher, the stator B in this open portion is closed. At the time of maintenance or failure in the aircraft, as described above, this stator B can be partially opened.
【0009】本発明において回転子(A)とは、回転軸
に支持され、外側表面の母線に沿って多数の凹凸部を有
するものであり、その軸を中心に回転することが出来る
部材を言う。一方、固定子(B)は、内側表面の母線に
沿って多数の凹凸部を有するものであり、固定されてい
るものを言う。第1図においては、これら回転子A及び
固定子Bは、いずれも円柱状である。In the present invention, the rotor (A) is a member which is supported by a rotating shaft and has a large number of uneven portions along the generatrix of the outer surface and which can rotate about the shaft. . On the other hand, the stator (B) has a large number of concave and convex portions along the generatrix of the inner surface and is fixed. In FIG. 1, the rotor A and the stator B are both columnar.
【0010】また、回転子Aの外径は、固定子Bの内径
よりも小さく、この回転子Aは、固定子B内に、所定の
間隙を設けて嵌装されている。そして、この固定子B内
で、回転子Aが回転することにより、それらの間隙を固
体物質が移動することにより、その固体物質を所定の大
きさに粉砕することが出来る。The outer diameter of the rotor A is smaller than the inner diameter of the stator B, and the rotor A is fitted in the stator B with a predetermined gap. Then, in the stator B, the rotor A rotates, so that the solid substance moves in the gap between them, so that the solid substance can be crushed to a predetermined size.
【0011】尚、本発明の粉砕機には、固定子(B)の
外側表面に少なくとも2つの口が設けられている。この
2つの口(1)及び(2)は、通常、回転子(A)と固
定子(B)との間隙に、粉砕すべき固体物質を供給する
ための供給口と、粉砕された固体物質を取り出すための
取出口である。In the crusher of the present invention, at least two ports are provided on the outer surface of the stator (B). These two ports (1) and (2) are usually a feed port for feeding a solid substance to be crushed into a gap between the rotor (A) and the stator (B), and a crushed solid substance. It is an outlet for taking out.
【0012】これら2つの口は、固定子(B)の外側表
面に設けられていればよく、供給口と取出口との間の間
隔やレイアウトは特に限定されない。固体物質の粉砕を
効率的かつ充分に行うためには、それらの間隔は出来る
だけ長くとることが好ましい。第1図では、横向きの固
定子Bの外側表面上部一端に供給口1を設け、同じくも
う一端に取出口2を設けた粉砕機を示してある。These two ports need only be provided on the outer surface of the stator (B), and the spacing and layout between the supply port and the take-out port are not particularly limited. In order to efficiently and sufficiently grind the solid substance, it is preferable that the distance between them is as long as possible. FIG. 1 shows a crusher in which a feed port 1 is provided at one end on the upper side of the outer surface of a horizontally oriented stator B and a take-out port 2 is provided at the other end.
【0013】さて本発明の粉砕機では、例えば上記した
固定子(B)の外側表面の一端の口(1)から、固定子
(B)と回転子(A)との間隙に供給された、粉砕すべ
き固体物質は、気体の流れを利用して、第1図に示した
矢印の向きに、前記したのと別の、固定子(B)の外側
表面のもう一端の口(2)に移動させながら、粉砕が行
われる。In the crusher of the present invention, for example, it is supplied to the gap between the stator (B) and the rotor (A) from the mouth (1) at one end of the outer surface of the stator (B). The solid substance to be crushed utilizes the flow of gas in the direction of the arrow shown in FIG. 1 and into the mouth (2) at the other end of the outer surface of the stator (B) which is different from that described above. Crushing is performed while moving.
【0014】つまり、気体の流れ方向と同一方向に、そ
の気体とともに粉砕すべき固体物質が、回転する回転子
(A)の凹凸部分と固定子(B)の凹凸部分で繰り返し
粉砕されながら、間隙を移動して、粉砕すべき固体物質
は、所定の大きさへと粉砕される。第1図には、運転時
における機内の気体の流れ、粉砕すべき固体物質及び粉
砕された固体物質の流れの一例を矢印で例示してある。That is, in the same direction as the flow direction of the gas, the solid substance to be crushed together with the gas is repeatedly crushed by the uneven portion of the rotating rotor (A) and the uneven portion of the stator (B), and the gap is formed. The solid substance to be crushed is crushed into a predetermined size. In FIG. 1, an example of the flow of gas inside the machine, the solid substance to be crushed, and the flow of the crushed solid substance during operation is illustrated by arrows.
【0015】粉砕すべき固体物質は、固定子(B)の外
側表面の一端の口(1)から、強制的に気体とともに吹
き込んで、それを移動させても良いし、逆に、前記した
のとは別の固定子(B)の外側表面のもう一方の一端の
口(2)から吸気を行い、それを移動させても良い。The solid substance to be crushed may be forcedly blown together with the gas from the mouth (1) at one end of the outer surface of the stator (B) to move it, or vice versa. Intake may be carried out from the mouth (2) at the other end of the outer surface of the stator (B), which is different from the above, and it may be moved.
【0016】この時の気体は、公知慣用のものがいずれ
も使用出来るが、例えば窒素、酸素、ヘリウム、空気等
が挙げられる。この気体としては、粉砕すべき固体物質
を劣化させることのないものを用いることが好ましい。
尚、この気体としては、予め冷却されたものでも、そう
でないものでも使用出来るが、常温よりも低い温度に予
め冷却された気体を用いると、粉砕すべき固体粒子の劣
化や軟化を防止できる上、機内温度をより低く保つこと
が出来、安全性作業環境も良好となるので好ましい。As the gas at this time, any known and commonly used gas can be used, and examples thereof include nitrogen, oxygen, helium and air. It is preferable to use a gas that does not deteriorate the solid substance to be crushed.
It should be noted that this gas may be either pre-cooled or non-pre-cooled, but the use of gas pre-cooled to a temperature lower than room temperature can prevent deterioration and softening of solid particles to be crushed. It is preferable because the temperature inside the machine can be kept lower and the safety work environment becomes better.
【0017】また固定子(B)の外側に冷却ジャケット
16(第4図参照。第1図では記載を省略してある。)
を設けて、粉砕時に発生する熱で加熱された固定子
(B)を冷却する様にしてもよい。A cooling jacket 16 (see FIG. 4; not shown in FIG. 1) is provided outside the stator (B).
May be provided to cool the stator (B) heated by the heat generated during the pulverization.
【0018】第1図では、横型の粉砕機を示したが、回
転子(A)及び固定子(B)を縦型に設置する様にして
もよいのは勿論である。In FIG. 1, a horizontal type crusher is shown, but it goes without saying that the rotor (A) and the stator (B) may be installed vertically.
【0019】本発明の粉砕機の特徴は、回転子(A)の
粉砕面先端を、回転方向反対側に接線に対して70°以
下とした、粉砕性の良い回転子の凹部形状をさらに工夫
したところにある。尚、この回転子(A)の粉砕面と
は、第2図における数字4で示される部分である。The feature of the crusher of the present invention is that the tip of the crushing surface of the rotor (A) is 70 ° or less with respect to the tangent line on the opposite side in the direction of rotation, and the recessed shape of the rotor having good crushability is further devised. It is in the place where it was done. The crushed surface of the rotor (A) is a portion indicated by numeral 4 in FIG.
【0020】その具体的な工夫は、次の通りである。 1.回転子(A)の外側表面の凹凸を、内壁に曲線部分
と直線部分を含む凹部形状が連続する歯形とする。The concrete measures are as follows. 1. The unevenness on the outer surface of the rotor (A) is a tooth profile in which the inner wall has a continuous concave portion including a curved portion and a straight portion.
【0021】2.固定子(B)と対向する様に、回転子
(A)の当該凹部内壁の回転方向に向いた壁の直線部
(粉砕面)を回転子(A)の接線に対して70〜30°とな
る様に、直線部(粉砕面)先端を回転子(A)の回転方
向の反対側に傾ける。2. The straight portion (crushing surface) of the wall of the rotor (A) facing the rotation direction of the inner wall of the recess so as to face the stator (B) is 70 to 30 ° with respect to the tangent line of the rotor (A). Inclining the tip of the linear portion (crushing surface) to the opposite side of the rotation direction of the rotor (A).
【0022】回転子(A)の凹部としては、上記した条
件1及び2を満足するものであればいずれも採用でき
る。具体的には、例えば第3図に示した様に、(ニ)〜
(ヘ)の形状が挙げられる。回転子(A)の凹部形状に
おいて、一方の直線部(粉砕面)の延長線を引いた場
合、その線より内側に曲線部を有するのが、形状(ニ)
であり、回転子(A)の凹部形状において、一方の直線
部(粉砕面)でない凹部先端部より回転子(A)の中心
線を引いたとき、その中心線の回転方向側に曲線部を有
するのが、形状(ホ)であり、及びこれらが組み合わさ
れたのが、形状(ヘ)である。As the concave portion of the rotor (A), any one can be adopted as long as it satisfies the above conditions 1 and 2. Specifically, for example, as shown in FIG.
The shape of (f) is mentioned. In the concave shape of the rotor (A), when an extension line of one straight line portion (crushing surface) is drawn, it has a curved portion inside the line is the shape (d)
In the concave shape of the rotor (A), when the center line of the rotor (A) is drawn from the tip of the concave portion which is not one straight line portion (crushing surface), a curved portion is formed on the rotational direction side of the center line. It has a shape (e), and a combination of these is a shape (f).
【0023】この時、回転子(A)の回転半径と、その
凹部の深さの関係は凹部の深さが回転半径の1/15以
内とすることが好ましい。また、凹部に設けられた曲線
部の半径Rと凹部の深さの関係は、前記粉砕面の角度で
変化するが、おおよそRが深さの1/5〜1/2となる
様にするのが良い。At this time, the relationship between the radius of rotation of the rotor (A) and the depth of the recess is preferably such that the depth of the recess is within 1/15 of the radius of rotation. Further, the relationship between the radius R of the curved portion provided in the concave portion and the depth of the concave portion changes depending on the angle of the crushing surface, but R is set to be approximately 1/5 to 1/2 of the depth. Is good.
【0024】尚、回転子(A)に設けられた多数の凹凸
と間隙を介して対向する、固定子(B)の多数の凹凸自
体は、どの様な形状の凹凸のいずれでも採用できる。こ
の様な凹凸としては、例えば第3図(イ)〜(ハ)の形
状のものが挙げられる。勿論、上記回転子(A)の凹凸
として示した形状(ニ)〜(ヘ)でも良い。It should be noted that the numerous irregularities of the stator (B), which are opposed to the numerous irregularities provided on the rotor (A) via a gap, can be any irregularities of any shape. Examples of such irregularities include those having the shapes shown in FIGS. 3 (a) to 3 (c). Of course, the shapes (d) to (f) shown as the irregularities of the rotor (A) may be used.
【0025】本発明の粉砕機においては、回転子(A)
として、上記した形状を有するものを用いれば、回転子
(A)と固定子(B)のそれぞれの凹凸の組み合わせ
は、特に制限されるものではない。本発明者の知見で
は、回転子(A)の凹部の形状及び固定子(B)凹部形
状との組み合わせは、前記(イ)〜(ハ)からなる群か
ら選択された固定子(B)凹部形状と、前記(ニ)〜
(ヘ)からなる群から選択された回転子の凹部形状とを
どの様に組み合わせても、本発明の効果のうえでは、い
ずれも有効であった。In the crusher of the present invention, the rotor (A)
As long as the one having the above-mentioned shape is used, the combination of the concave and convex portions of the rotor (A) and the stator (B) is not particularly limited. According to the knowledge of the present inventor, the combination of the shape of the concave portion of the rotor (A) and the shape of the concave portion of the stator (B) is the concave portion of the stator (B) selected from the group consisting of (a) to (c) above. Shape and the above (d)
Any combination of the shape of the rotor recesses selected from the group (f) was effective in terms of the effect of the present invention.
【0026】この時の固定子(B)と回転子(A)との
間隙は、粉砕すべき固体物質の大きさ及び粉砕後の固体
物質の粒子径をどの程度にするかにより、適宜選択すれ
ばよい。この間隙は、精度を考慮すると、通常0.5m
m〜3mmである。この間隙は、狭いほど粉砕された固
体物質としては小粒径のものが得られ、広いほど大粒径
のものが得られる。At this time, the gap between the stator (B) and the rotor (A) is appropriately selected depending on the size of the solid substance to be crushed and the particle size of the solid substance after crushing. Good. Considering accuracy, this gap is usually 0.5m
It is m to 3 mm. The narrower the gap, the smaller the particle size of the pulverized solid substance can be obtained, and the wider the gap, the larger the particle size can be obtained.
【0027】回転子(A)の回転速度は、粉砕すべき固
体物質の硬度や大きさ等に依存するため、特に限定され
るものではないが、粉砕効率等の観点から、通常、周速
90〜200m/秒とするのが一般的である。The rotating speed of the rotor (A) depends on the hardness and size of the solid substance to be crushed, and is not particularly limited, but from the viewpoint of crushing efficiency, the peripheral speed is usually 90. It is generally set to 200 m / sec.
【0028】回転子(A)の外側表面の母線に沿った凹
凸部及び固定子(B)の内側表面の母線に沿った凹凸部
の材質は、固体物質の粉砕に耐え得る強度を有する材質
の材料であればいずれも使用出来る。具体的には、例え
ばステンレス、SK材等の金属材料が挙げられる。The material of the concavo-convex portion along the generatrix of the outer surface of the rotor (A) and the concavo-convex portion along the generatrix of the inner surface of the stator (B) is made of a material having a strength capable of withstanding pulverization of solid substances. Any material can be used. Specifically, for example, a metal material such as stainless steel or SK material can be used.
【0029】本発明の粉砕機は、公知慣用の固体物質が
いずれも粉砕できるが、例えば熱可塑性樹脂、顔料、静
電荷像現像用粉体トナー、化粧品、薬品、飼料、コーヒ
ー豆等の粉砕に使用できる。The pulverizer of the present invention can pulverize any known and commonly used solid substance. For example, for pulverizing thermoplastic resin, pigment, powder toner for electrostatic image development, cosmetics, chemicals, feed, coffee beans and the like. Can be used.
【0030】[0030]
【作用】本発明の粉砕機では、第2図の様に、回転子A
の凹部と固定子Bの凹部とを対向させて用いた場合に
は、回転子Aをその上に示した矢印方向に回転させる
と、各凹部内壁に気体の渦流ができる。第2図では、一
つの凹部内壁を用いてこの渦流の発生する箇所及び渦流
の回転の向きを示した。In the crusher of the present invention, as shown in FIG.
When the concave portions of (1) and the concave portions of the stator B are used so as to face each other, when the rotor A is rotated in the direction of the arrow shown above, a swirl of gas is formed on the inner wall of each concave portion. In FIG. 2, the location where the vortex flow is generated and the direction of rotation of the vortex flow are shown using one inner wall of the recess.
【0031】この渦は、気体の吸引又は吹き込みによ
り、回転しながら、螺旋状に回転子(A)の一端からも
う一方の一端に向けて移動する(第4図)。このため第
4図に矢印で示した様に、粉砕すべき固体物質のうち、
粒子径の大きい、粗い粒子は、回転子(A)の遠心力と
渦流の遠心力により、凹部からはじきだされ、間隙(粉
砕ゾーン)に戻される。This vortex spirally moves from one end of the rotor (A) to the other end while rotating by the suction or blowing of gas (FIG. 4). Therefore, among the solid substances to be crushed, as indicated by the arrow in Fig. 4,
Coarse particles having a large particle diameter are repelled from the concave portion by the centrifugal force of the rotor (A) and the centrifugal force of the vortex and returned to the gap (crushing zone).
【0032】一方、粉砕され細かくなった粒子は、第4
図に点線で示した様に、これら力の作用を受けず、回転
子の凹部内を、その気体の渦流に乗り、回転子(A)の
もう一端方向に移動され、最終的には、固定子(B)の
外表面に設けられたもう一方の口から排出される。On the other hand, the finely ground particles are
As shown by the dotted line in the figure, it is not affected by these forces, rides in the gas vortex inside the recess of the rotor, moves toward the other end of the rotor (A), and finally becomes fixed. It is discharged from the other mouth provided on the outer surface of the child (B).
【0033】回転子(A)の回転と固定子(B)との抵
抗で、前者凹部に気体の渦流を発生させ、必要とする大
きさよりも大きな粒子(粗粒子)を回転子(A)の遠心
力と渦流の遠心力で、粉砕ゾーンに戻し、必要とする大
きさ範囲の粒子(適正粒子)を渦流により、粉砕系外へ
移動させると共に気体の乱流を整流にし、流れを良く
し、機内の温度上昇を押さえ、焼き付き等がなく、回転
子(A)及び固定子(B)の凹凸部分の切れ味を従来よ
りも長期間に亘って良好に保つことが出来る。Due to the rotation of the rotor (A) and the resistance of the stator (B), a swirl of gas is generated in the former concave portion, and particles (coarse particles) larger than the required size are generated in the rotor (A). By centrifugal force and centrifugal force of vortex flow, it returns to the crushing zone, and particles of the required size range (appropriate particles) are moved to the outside of the crushing system by vortex flow, and turbulent flow of gas is rectified to improve the flow, The temperature rise in the machine can be suppressed, no seizure, etc., and the sharpness of the uneven portions of the rotor (A) and the stator (B) can be kept better for a longer period of time than before.
【0034】粉砕すべき固体物質は、一般的に粉砕によ
り、適正粒子、必要とする大きさよりも小さい粒子(過
粉砕微粉)、(粗粒子)とを含んだ組成に粉砕される。
本発明の粉砕機を用いれば、過粉砕微粉及び粗粒子の発
生を従来より抑制し、適正粒子の収率を格段に向上させ
ることが出来る。The solid substance to be pulverized is generally pulverized into a composition containing proper particles, particles smaller than a required size (over-pulverized fine powder), and (coarse particles).
By using the crusher of the present invention, generation of over-pulverized fine powder and coarse particles can be suppressed more than ever before, and the yield of appropriate particles can be significantly improved.
【0035】本発明の粉砕機で、粉砕された固体物質
は、必要に応じて分級される。粗粒子は、過粉砕微粉及
び適正粒子とは分離して、再度、粉砕機で適正粒子とな
る様に粉砕を行う操作(戻し粗粒子の粉砕操作)を行う
のが一般的である。本発明の粉砕機で粉砕された固体物
質(粉砕物)組成は、従来の粉砕機で得られた粉砕物の
組成と対比すると、粗粒子の含有率が極端に少ないの
で、改めて、戻し粗粒子の粉砕操作の頻度或いは処理量
を減らすことが出来るし、また、過粉砕微粉の含有率も
極端に少ないので、得られた粉砕粒子を、分級が難しい
適正粒子と過粉砕微粉との分級をする必要もなくなる。The solid material crushed by the crusher of the present invention is classified according to need. The coarse particles are generally separated from the over-pulverized fine powder and the proper particles, and are then pulverized again by a pulverizer so as to be proper particles (pulverization operation of returned coarse particles). The composition of the solid substance (pulverized product) pulverized by the pulverizer of the present invention has an extremely small content of coarse particles as compared with the composition of the pulverized product obtained by the conventional pulverizer. It is possible to reduce the frequency of pulverization operation or the amount of treatment, and since the content of over-pulverized fine powder is extremely low, the obtained pulverized particles are classified into proper particles that are difficult to classify and over-pulverized fine powder. There is no need.
【0036】[0036]
【実施例】次の本発明を実施例により詳しく説明する。
尚、本発明は実施例の記載により何等限定されるもので
はないことは、勿論である。The present invention will be described in more detail with reference to the following examples.
Needless to say, the present invention is not limited to the description of the embodiments.
【0037】実施例1 この実施例では、静電荷像現像用粉体トナーの粉砕を本
発明の粉砕機で行った場合の例を示す。Example 1 In this example, an example in which the powder toner for electrostatic image development is pulverized by the pulverizer of the present invention is shown.
【0038】固定子Bと回転子Aの凹部形状を第5図の
組み合わせとしてセットした粉砕機に、分級機等を組み
合わせてシステムを作製した(システム構成は第図参
照。)。回転子Aは、別に設けられたモーター9の回転
をベルト10で回転子Aの軸に伝達してそれを回転させ
る様にした。A system was produced by combining a classifier and the like with a crusher in which the concave shapes of the stator B and the rotor A were set as the combination of FIG. 5 (see FIG. 5 for the system configuration). In the rotor A, the rotation of the separately provided motor 9 is transmitted to the shaft of the rotor A by the belt 10 to rotate the same.
【0039】粉砕機の設定・運転条件は、回転子Aの半
径198mm、回転数を4500rpm/分とし、機内
を通過させる冷却空気温度を15℃、その空気量を16
m/分とした。The setting and operating conditions of the crusher are as follows: the radius of the rotor A is 198 mm, the rotation speed is 4500 rpm, the temperature of the cooling air passing through the machine is 15 ° C., and the amount of air is 16
m / min.
【0040】回転子Aの凹部形状については、粉砕面角
度60°、凹部深さ8mm、凹部R半径3mm、凹部個
数150個である。Regarding the shape of the recesses of the rotor A, the crushing surface angle is 60 °, the recess depth is 8 mm, the recess R radius is 3 mm, and the number of recesses is 150.
【0041】このシステムを上記条件で運転し、原料ホ
ッパー6の粉体トナーの塊粒(原料)は定量供給機7に
より、吸引ブロア15で引かれた冷却空気(その供給源
は図示せず。)と共に、粉砕機の固定子外側表面一端の
口1より、回転子Aと固定子Bとの間隙に相当する粉砕
ゾーンに入れられた。The system is operated under the above conditions, and the agglomerates (raw material) of the powder toner in the raw material hopper 6 are drawn by the suction blower 15 by the constant quantity feeder 7 (cooling air is not shown). ), Through a port 1 at one end of the outer surface of the stator of the crusher, and was put into a crushing zone corresponding to a gap between the rotor A and the stator B.
【0042】また冷却ジャケット16には、機内を冷却
するための冷却するための冷却水を通過させる様にし
た。運転中の機内平均温度は35℃であった。In addition, cooling water for cooling the inside of the machine is passed through the cooling jacket 16. The average temperature inside the machine during operation was 35 ° C.
【0043】粉砕ゾーン中に入った原料は、冷却空気と
固定子Bのジャケット16で冷却されながら、回転子A
の回転によりそれと固定子Bの間の粉砕ゾーンで粉砕さ
れ、回転子Aの凹部では、回転子Aの遠心力と渦流によ
り、粗粒子と粉砕粒子(適正粒子と過粉砕微粉)に分け
る機能がはたらきながら、吸引空気により粉砕機の固定
子の外側表面のもう一端の口2に移動し、粗粒子分級機
11に入り、粉砕機8内を通過した粗粒子はここで分離
され、粗粒子戻りライン(配管)12により粉砕機8の
固定子B外側表面に設けた口1に戻され、再度粉砕され
た。The raw material that has entered the crushing zone is cooled by the cooling air and the jacket 16 of the stator B, while being rotated by the rotor A.
Is pulverized in the pulverization zone between the rotor and the stator B by the rotation of the rotor, and in the concave portion of the rotor A, the centrifugal force and the vortex of the rotor A have a function of dividing into coarse particles and pulverized particles (appropriate particles and over-pulverized fine powder). While working, the suction air moves to the mouth 2 at the other end of the outer surface of the stator of the crusher, enters the coarse particle classifier 11, and the coarse particles that have passed through the crusher 8 are separated here and returned to the coarse particles. It was returned to the mouth 1 provided on the outer surface of the stator B of the crusher 8 by a line (pipe) 12 and crushed again.
【0044】一方、粗粒子分級機11を通過した平均粒
子径10μmの適正粒子からなる粉砕品は、バグフィル
ター13で捕集され、ロータリーバルブ14より排出さ
れ製品とされた。On the other hand, the crushed product made of proper particles having an average particle size of 10 μm which passed through the coarse particle classifier 11 was collected by the bag filter 13 and discharged from the rotary valve 14 to be a product.
【0045】比較例1 上記した粉砕機のうち、凹部形状が従来の形状(イ)の
回転子を用いた以外は実施例1と同様の条件で運転を行
ったところ、粗粒子量が実施例1の10倍も発生し、機
内温度は、50℃であった。しかも、粗粒子を分離して
得られた粉砕粒子中に含まれる3.5μm以下の過粉砕
微粉は、実施例1の粉砕粒子のそれに比べると、2倍以
上も含まれていた。Comparative Example 1 In the above-mentioned crusher, operation was carried out under the same conditions as in Example 1 except that a rotor having a conventional concave shape (a) was used. 10 times as much as 1 was generated, and the internal temperature was 50 ° C. Moreover, the over-pulverized fine powder having a size of 3.5 μm or less contained in the pulverized particles obtained by separating the coarse particles was more than twice as large as that of the pulverized particles of Example 1.
【0046】尚、上記実施例1の装置を用いたところ、
従来の比較例1の粉砕機を用いた装置では粉砕が難しか
った、平均粒子径6ミクロンの粉体トナーも得ることが
できた。When the apparatus of Example 1 was used,
It was possible to obtain a powder toner having an average particle diameter of 6 microns, which was difficult to pulverize with the conventional apparatus using the pulverizer of Comparative Example 1.
【0047】[0047]
【発明の効果】本発明の粉砕機では、回転子の外側表面
の凹部形状を、内壁に曲線部分と直線部分を含む凹部形
状が連続する歯形とし、固定子と対向する様に、回転子
の当該凹部内壁の回転方向に向いた壁の直線部(粉砕
面)を回転子の接線に対して70〜30°となる様に、
直線部(粉砕面)先端を回転子の回転方向の反対側に傾
けたものを用いるので、必要とする大きさ範囲の固体物
質粒子を高収率で得ることが出来、しかも機内発熱を抑
制できるので、安全性・作業環境を向上させることも出
来るという格別顕著な効果を奏する。In the crusher of the present invention, the shape of the recess on the outer surface of the rotor is a tooth shape in which the shape of the recess including the curved portion and the straight portion is continuous on the inner wall, and the rotor is formed so as to face the stator. In order that the straight part (crushing surface) of the wall of the inner wall of the recess facing the rotation direction may be 70 to 30 ° with respect to the tangent of the rotor,
Since the tip of the straight part (crushing surface) is inclined to the opposite side of the rotation direction of the rotor, solid substance particles in the required size range can be obtained in high yield, and heat generation inside the machine can be suppressed. Therefore, it has a particularly remarkable effect that the safety and working environment can be improved.
【図1】本発明の粉砕機の固定子の開放時の斜視図であ
る。FIG. 1 is a perspective view of a crusher of the present invention when a stator is opened.
【図2】固定子と回転子の部分拡大断面図である。FIG. 2 is a partially enlarged sectional view of a stator and a rotor.
【図3】回転子及び固定子の凹部形状の一例を示す断面
図である。FIG. 3 is a cross-sectional view showing an example of recessed shapes of a rotor and a stator.
【図4】回転子凹部の気体と粉砕すべき固体物質の動き
の説明図である。FIG. 4 is an explanatory view of the movement of the gas in the rotor recess and the solid substance to be crushed.
【図5】実施例1で用いた固定子と回転子の部分拡大断
面図である。5 is a partially enlarged sectional view of a stator and a rotor used in Example 1. FIG.
【図6】本発明の粉砕機を用いた、実施例で示したシス
テム構成の説明図である。FIG. 6 is an explanatory diagram of the system configuration shown in the embodiment using the crusher of the present invention.
A 回転子 B 固定子 1 粉砕機の固定子外側表面の一端の口 2 粉砕機の固定子外側表面のもう一端の口 3 動力 4 回転子の凹部内壁の粉砕面 5 気体の渦流 6 原料ホッパー 7 定量供給機 8 粉砕機 9 モーター 10 ベルト 11 粗粒子分級機 12 粗粒子戻りライン(配管) 13 補集用バグフィルター 14 ロータリーバルブ 15 吸引ブロア 16 冷却ジャケット A rotor B stator 1 mouth of the outer surface of the stator of the grinder 2 mouth of the outer surface of the stator of the grinder 3 power 4 grinding surface of the inner wall of the recess of the rotor 5 gas vortex 6 raw material hopper 7 Quantitative feeder 8 Crusher 9 Motor 10 Belt 11 Coarse particle classifier 12 Coarse particle return line (piping) 13 Collection bag filter 14 Rotary valve 15 Suction blower 16 Cooling jacket
Claims (3)
る外側表面の母線に沿って多数の凹凸部を有する回転子
(A)と、当該回転子(A)との間に間隙を存して嵌装
された内側表面の母線に沿って多数の凹凸部を有する固
定子(B)とを有し、当該固定子(B)の外側表面一端
の口(1)から固体物質を供給し、当該回転子(A)を
回転させながら、一端(1)から当該固定子(B)の外
側表面一端の口(2)に向けて気体の流れで固体物質を
移動させながら、回転子(A)と固定子(B)との間で
固体物質を所定の大きさに粉砕する粉砕機において、 1.回転子(A)の外側表面の凹凸を、内壁に曲線部分
と直線部分を含む凹部形状が連続する歯形となし、 2.固定子(B)と対向する様に、回転子(A)の当該
凹部内壁の回転方向に向いた壁の直線部(粉砕面)を回
転子(A)の接線に対して70〜30°となる様に、直線部
(粉砕面)先端を回転子(A)の回転方向の反対側に傾
けたことを特徴とする粉砕機。1. A rotor (A) having a large number of irregularities along a generatrix of an outer surface which is supported by a rotary shaft and can rotate about the shaft, and a gap is provided between the rotor (A). And a stator (B) having a large number of uneven portions along the generatrix of the inner surface, which is fitted and installed, and supplies the solid substance from the mouth (1) at one end of the outer surface of the stator (B). Then, while rotating the rotor (A), while moving the solid substance by the flow of gas from the one end (1) toward the mouth (2) at one end of the outer surface of the stator (B), the rotor ( In a crusher for crushing a solid substance into a predetermined size between A) and a stator (B), 1. 1. The unevenness on the outer surface of the rotor (A) has a tooth profile in which a recessed shape including a curved portion and a straight portion is continuous on the inner wall. The straight portion (crushing surface) of the wall of the rotor (A) facing the rotation direction of the inner wall of the recess so as to face the stator (B) is 70 to 30 ° with respect to the tangent line of the rotor (A). Thus, the crusher is characterized in that the tip of the linear portion (crushing surface) is inclined to the opposite side of the rotation direction of the rotor (A).
直線部(粉砕面)の延長線を引いた場合、その線より内
側に曲線部をもつことを特徴とする請求項1記載の粉砕
機。2. In the concave shape of the rotor (A), when an extension line of one straight line portion (crushing surface) is drawn, a curved portion is provided inside the extended line. Crusher.
直線部(粉砕面)でない凹部先端部より回転子(A)の
中心線を引いたとき、その中心線の回転方向側に曲線部
があることを特徴とする請求項1記載の粉砕機。3. In the concave shape of the rotor (A), when the center line of the rotor (A) is drawn from the tip of the concave portion which is not one straight line portion (crushing surface), a curve is drawn in the direction of rotation of the center line. The crusher according to claim 1, wherein there is a part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6211070A JPH0871439A (en) | 1994-09-05 | 1994-09-05 | Crusher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6211070A JPH0871439A (en) | 1994-09-05 | 1994-09-05 | Crusher |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0871439A true JPH0871439A (en) | 1996-03-19 |
Family
ID=16599914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6211070A Pending JPH0871439A (en) | 1994-09-05 | 1994-09-05 | Crusher |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0871439A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002221828A (en) * | 2000-11-15 | 2002-08-09 | Canon Inc | Manufacturing method of toner |
| DE10255800A1 (en) * | 2002-11-29 | 2004-06-17 | Hosokawa Micron Gmbh | Sifting mill with grinder has grinding tools formed as relatively flat teeth extending radially outwards in their rotating plane to prevent clogging |
| CN118649733A (en) * | 2024-07-09 | 2024-09-17 | 广东海洋大学 | A grinding rotor and a grinding assembly |
-
1994
- 1994-09-05 JP JP6211070A patent/JPH0871439A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002221828A (en) * | 2000-11-15 | 2002-08-09 | Canon Inc | Manufacturing method of toner |
| DE10255800A1 (en) * | 2002-11-29 | 2004-06-17 | Hosokawa Micron Gmbh | Sifting mill with grinder has grinding tools formed as relatively flat teeth extending radially outwards in their rotating plane to prevent clogging |
| CN118649733A (en) * | 2024-07-09 | 2024-09-17 | 广东海洋大学 | A grinding rotor and a grinding assembly |
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