JPH0716539A - Air classifier - Google Patents

Air classifier

Info

Publication number
JPH0716539A
JPH0716539A JP18722493A JP18722493A JPH0716539A JP H0716539 A JPH0716539 A JP H0716539A JP 18722493 A JP18722493 A JP 18722493A JP 18722493 A JP18722493 A JP 18722493A JP H0716539 A JPH0716539 A JP H0716539A
Authority
JP
Japan
Prior art keywords
classified
casing
rotary
powder
dispersion plate
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
Application number
JP18722493A
Other languages
Japanese (ja)
Inventor
Shinichiro Saito
紳一郎 斎藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nihon Cement Co Ltd
Original Assignee
Nihon Cement Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nihon Cement Co Ltd filed Critical Nihon Cement Co Ltd
Priority to JP18722493A priority Critical patent/JPH0716539A/en
Publication of JPH0716539A publication Critical patent/JPH0716539A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide an air classifier capable of easily altering the number of rotations of a dispersing plate in matching relation to the aggregating properties of a powder to be classified. CONSTITUTION:This air classifier is constituted so that the rotary dispersing plate 6 dispersing the raw material W to be classified charged in a casing 1 and the rotary blade 7 forming revolving streams in the casing 1 are respectively rotated by separate rotary shafts 3, 4 and drive devices 10, 13.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、気流分級機に関し、特
に分級する粉体の凝集性状等に合わせて、その分級操作
が可能な気流分級機に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an air stream classifier, and more particularly to an air stream classifier capable of classifying the powder according to the agglomeration properties of the powder to be classified.

【0002】[0002]

【従来の技術及びその課題】従来より、種々の産業分野
において粉砕した粉体等を粗粉と微粉とに分級すること
が成され、その分級方法として気流分級機を用いた方法
が広く採用されている。
2. Description of the Related Art Conventionally, pulverized powder or the like has been classified into coarse powder and fine powder in various industrial fields, and a method using an air stream classifier has been widely adopted as the classification method. ing.

【0003】かかる気流分級機は、例えば図3に示した
構造のもので、原料投入口101から被分級原料Wを投
入し、該投入された被分級原料Wを回転する分散板10
2によって一次粒に解きほぐし、外周方向に飛散させな
がら分級室103内に落下させる。
Such an air stream classifier has, for example, the structure shown in FIG. 3, and the raw material to be classified W is charged from the raw material inlet 101, and the dispersed plate 10 which rotates the charged raw material to be classified W is introduced.
It is disentangled into primary particles by 2 and dropped into the classification chamber 103 while being scattered in the outer peripheral direction.

【0004】分級室103内に落下した上記原料Wは、
回転翼104によってケーシング105内に形成される
旋回流による遠心力と、旋回しながら中心に向かう空気
流の粘性力との釣合いから分級が行われ、粗粉Aは、上
記遠心力が勝って内筒106内を旋回しながら下降し、
下端の出口107より排出される。また、微粉Bは、空
気流の粘性力が勝り、該空気流に乗って回転翼104の
間隙を通ってダクト108内に入り、図示しない捕集装
置で回収される。
The raw material W dropped into the classification chamber 103 is
Classification is performed based on the balance between the centrifugal force due to the swirling flow formed in the casing 105 by the rotary blades 104 and the viscous force of the air flow that is swirling toward the center, and the coarse powder A has a higher centrifugal force than the internal force. While descending while turning in the cylinder 106,
It is discharged from the outlet 107 at the lower end. Further, the viscous force of the air flow prevails, and the fine powder B enters the duct 108 through the gap of the rotary blades 104 by riding on the air flow, and is collected by a collecting device (not shown).

【0005】ここで、上記気流分級機における粗粉Aと
微粉Bとの分離限界粒子のストークス径Dpcは、周知の
如く次式のように表される。
Here, as is well known, the Stokes diameter D pc of the separation limit particles of the coarse powder A and the fine powder B in the air stream classifier is expressed by the following equation.

【0006】[0006]

【式1】 ここで、Vt は回転翼の周速、μは空気の粘度、rは回
転翼の半径、Vr はrの位置の半径方向の空気流速、ρ
p は分級する粉体の密度を各々示す。
[Formula 1] Here, V t is the peripheral speed of the rotor blade, μ is the viscosity of air, r is the radius of the rotor blade, V r is the air velocity in the radial direction at the position of r, ρ
p indicates the density of the powder to be classified.

【0007】気流分級機内に投入された上記被分級原料
Wが、上記式1において表される分離限界粒子のストー
クス径(=Dpc)で、正確に粗粉Aと微粉Bとに分級さ
れるためには、上記旋回流による遠心力と、空気流の粘
性力とが作用する分級室103内に、被分級原料Wがい
かに分散した状態で投入されるかが非常に重要な問題と
なる。
The raw material W to be classified introduced into the air stream classifier is accurately classified into the coarse powder A and the fine powder B by the Stokes diameter (= D pc ) of the separation limit particles represented by the above formula 1. In order to do so, it is a very important problem how the raw material W to be classified is dispersed in the classifying chamber 103 where the centrifugal force due to the swirling flow and the viscous force of the air flow act.

【0008】即ち、被分級原料Wが、万一凝集した状態
で上記分級室103内に投入されると、該凝集粒子は、
本来微粉Bに属する粒径の粉体を含む物であっても、分
級室103内においては粗粉Aとしての分級操作を受
け、分級後の粗粉A中には多くの微粉Bが含まれること
となり、気流分級機の分級精度が著しく低下する。
That is, if the raw material W to be classified is introduced into the classification chamber 103 in the state of being aggregated, the aggregated particles are
Even if the powder contains the powder having the particle diameter originally belonging to the fine powder B, it undergoes the classification operation as the coarse powder A in the classification chamber 103, and the coarse powder A after classification contains a large amount of the fine powder B. As a result, the classification accuracy of the airflow classifier is significantly reduced.

【0009】そのため気流分級機においては、被分級原
料Wを一次粒に解きほぐして分級室103内に投入する
上記分散板102の作用が非常に重要となるが、上記し
た従来より使用されている気流分級機は、該回転式分散
板102と、ケーシング105内に旋回流を形成する上
記回転翼104とが、同一の駆動モーター109によっ
て回転する回転軸110に固定されたものであるため、
分級する粉体の性状、特に凝集性状に応じて上記分散板
102の回転数を独自に変更することはできず、近年の
粒子径のより小さい粉体、或いは凝集し易い性状を有す
る粉体の分級ニーズには、十分には応え得る装置となっ
ていなかった。
Therefore, in the air stream classifier, the function of the dispersion plate 102 for unraveling the raw material W to be classified into primary particles and introducing it into the classifying chamber 103 is very important. In the classifier, the rotary dispersion plate 102 and the rotary blades 104 that form a swirl flow in the casing 105 are fixed to a rotary shaft 110 that is rotated by the same drive motor 109.
The number of revolutions of the dispersion plate 102 cannot be independently changed according to the properties of the powder to be classified, particularly the agglomeration property, and the powder having a smaller particle size in recent years or the powder having the property of easily aggregating is used. It was not a device that could sufficiently meet the classification needs.

【0010】本発明は、上述した従来技術が有する課題
に鑑み成されたものであって、その目的は、分級する粉
体の凝集性状等に合わせて、その分散板の回転数を容易
に変更できる気流分級機を提供することにある。
The present invention has been made in view of the problems of the above-mentioned prior art, and its object is to easily change the rotational speed of the dispersion plate according to the agglomeration property of the powder to be classified. It is to provide an airflow classifier that can.

【0011】[0011]

【課題を解決するための手段】本発明は、上記目的を達
成するため、ケーシング内に投入された被分級原料を分
散させる回転式分散板と、前記ケーシング内に旋回流を
形成する回転翼とを、各々別駆動の回転体とした。
In order to achieve the above object, the present invention provides a rotary dispersion plate for dispersing a material to be classified put in a casing, and a rotary blade for forming a swirling flow in the casing. Were separately driven rotating bodies.

【0012】[0012]

【作用】上記した本発明にかかる気流分級機によれば、
被分級原料を分散させる回転式分散板と、被分級原料の
カット径に影響を与える回転翼とを各々別駆動のものと
したため、分級する粉体の性状、例えば石灰石粒子のよ
うに粒子間の付着力が強く、凝集が発生し易い粉体を分
級する場合においては、回転式分散板の回転数を独自に
上げることにより、凝集した粉体を十分に解きほぐした
状態で分級にかけることが可能となり、また、逆に樹脂
系の粒子のように、帯電による凝集を引き起こし易い粉
体を分級する場合においては、ケーシング内に分級のた
めの旋回流を形成する回転翼の回転数を確保した状態
で、回転式分散板の回転数のみを落とし、粉体の帯電を
極力抑えた状態で分級にかける操作も可能となることか
ら、種々の異なる性状の粉体を、高い分級精度で分級で
きる装置となる。
According to the airflow classifier according to the present invention described above,
Since the rotary dispersion plate for dispersing the material to be classified and the rotating blades that affect the cut diameter of the material to be classified are driven separately, the property of the powder to be classified, for example, between particles like limestone particles When classifying powders that have strong adhesion and are prone to agglomeration, the rotation speed of the rotary dispersion plate can be increased independently to allow the agglomerated powders to be thoroughly disentangled before classification. On the contrary, in the case of classifying powder such as resin-based particles that easily causes agglomeration due to electrification, a state in which the rotational speed of the rotary blade that forms a swirling flow for classification in the casing is secured. It is also possible to classify powders of various different properties with high classification accuracy, since it is possible to perform classification while reducing the number of rotations of the rotary dispersion plate and suppressing charging of powders as much as possible. Becomes

【0013】[0013]

【実施例】以下、本発明の実施例を挙げ、本発明を詳細
に説明する。
The present invention will be described in detail below with reference to examples of the present invention.

【0014】ここで、図1は本発明にかかる気流分級機
の一実施例を示した概念的な断面図であって、図中1は
円筒状に形成したケーシング、2は該ケーシング1内に
収納されたホッパである。
Here, FIG. 1 is a conceptual cross-sectional view showing an embodiment of an air classifier according to the present invention, in which 1 is a cylindrical casing and 2 is a casing 1. It is a stored hopper.

【0015】上記ケーシング1の天井部1aには、該天
井部1aの中心を回転自在に貫通して垂下された中空シ
ャフト3、及び該中空シャフト3内に回転可能の挿入さ
れたシャフト4が設けられ、前記中空シャフト3の下端
には、シュート5より投入された被分級原料Wを分散さ
せる円盤状の分散板6が固着され、該中空シャフト3の
下端より下方に突出した上記シャフト4の下端には、ケ
ーシング1内に旋回流を形成する回転翼7が固着されて
いる。
The ceiling portion 1a of the casing 1 is provided with a hollow shaft 3 rotatably penetrating the center of the ceiling portion 1a and a shaft 4 rotatably inserted in the hollow shaft 3. At the lower end of the hollow shaft 3, a disc-shaped dispersion plate 6 for dispersing the raw material W to be classified introduced from the chute 5 is fixed, and the lower end of the shaft 4 protruding below the lower end of the hollow shaft 3. A rotary blade 7 that forms a swirling flow in the casing 1 is fixed to the.

【0016】また、上記中空シャフト3の上端には、プ
ーリ8が固着され、該プーリ8に巻掛けられた無端ベル
ト9によって、駆動モータ10の回転が中空シャフト3
に伝達され、該中空シャフト3の下端に固着された上記
分散板6が回転する。また該中空シャフト3の上端より
更に上方に突出した状態で存在する上記シャフト4の上
端にも、プーリ11が固着され、該プーリ11に巻掛け
られた無端ベルト12によって、上記とは異なる駆動モ
ータ13の回転がシャフト4に伝達され、該シャフト4
に固着された上記回転翼7が回転する。
A pulley 8 is fixed to the upper end of the hollow shaft 3, and the endless belt 9 wound around the pulley 8 causes the rotation of the drive motor 10 to rotate.
And the dispersion plate 6 fixed to the lower end of the hollow shaft 3 is rotated. Further, a pulley 11 is fixed to the upper end of the shaft 4 which is present so as to project further upward from the upper end of the hollow shaft 3, and an endless belt 12 wound around the pulley 11 causes a drive motor different from the above. The rotation of 13 is transmitted to the shaft 4, and the shaft 4
The rotary blade 7 fixed to the rotor rotates.

【0017】さらに、ケーシング1内に旋回流を形成す
る上記回転翼6の内側中心付近には、図示したように吸
引ブロアー14に連通するダクト15が開口し、該吸引
ブロアー14を稼働させることにより、ケーシング1内
に旋回しながら回転翼6の間隙を通ってダクト15内に
流れ込む空気の流れを形成する。
Further, as shown in the drawing, a duct 15 communicating with the suction blower 14 is opened near the inner center of the rotary blade 6 forming a swirl flow in the casing 1, and the suction blower 14 is operated. , Forms a flow of air flowing into the duct 15 through the gap of the rotary blades 6 while swirling into the casing 1.

【0018】上記のように構成された本発明にかかる気
流分級機は、次のように操作される。
The airflow classifier according to the present invention constructed as described above is operated as follows.

【0019】先ず、分級する粉体の種類、及び分級のカ
ット径から上記分散板6の回転数、ケーシング1内に旋
回流を形成する回転翼7の回転数、及び吸引ブロアー1
4の回転数を各々決定する。この際、本発明にかかる気
流分級機は、上述したように分散板6と、回転翼7とが
各々独立した軸3,4、及び駆動装置10,13によっ
て回転するように構成されているため、各々の回転数を
分級する粉体の種類に応じて最適なものに設定すること
ができる。
First, based on the type of powder to be classified and the cut diameter of classification, the number of revolutions of the dispersion plate 6, the number of revolutions of the rotor blades 7 forming a swirling flow in the casing 1, and the suction blower 1
Each of the four rotation speeds is determined. At this time, since the airflow classifier according to the present invention is configured such that the dispersion plate 6 and the rotary vanes 7 are rotated by the independent shafts 3 and 4 and the drive devices 10 and 13 as described above. , The number of revolutions can be set to an optimum one according to the type of powder to be classified.

【0020】次に、決定された各々の回転数で分散板
6、回転翼7、及び吸引ブロアー14を回転させ、ケー
シング1内に形成される空気流が安定したところで、上
記シュート5より該ケーシング1内に被分級原料Wを投
入する。
Next, the dispersion plate 6, the rotary blades 7, and the suction blower 14 are rotated at the determined respective rotation speeds, and when the air flow formed in the casing 1 is stabilized, the casing 5 is discharged from the chute 5. The raw material W to be classified is put into 1.

【0021】投入された被分級原料Wは、駆動モータ1
0によって回転する分散板6により効率的に一次粒に解
きほぐされ、外周方向に飛散しながら遠心力と、空気流
の粘性力とが作用する分級室16に落下する。
The raw material W to be classified is fed into the drive motor 1
The particles are efficiently disentangled into primary particles by the dispersion plate 6 rotating by 0, and fall into the classification chamber 16 where the centrifugal force and the viscous force of the air flow act while scattering in the outer peripheral direction.

【0022】分級室16に落下した上記被分級原料W
は、駆動モータ13によって回転する回転翼7の作用に
よりケーシング1内に形成される旋回流による遠心力
と、吸引ブロアー14の作用によって旋回しながら中心
に向かう空気流の粘性力との釣合いから分級が行われ、
粗粉Aは、上記遠心力が勝ってホッパー2内を旋回しな
がら下降し、下方の粗粉出口17より排出されると共
に、微粉Bは、空気流の粘性力が勝り、該空気流に乗っ
て回転翼7の間隙を通ってダクト15内に入り、図示し
ない捕集装置で回収される。
The material W to be classified which has fallen into the classification chamber 16
Is classified based on the balance between the centrifugal force due to the swirling flow formed in the casing 1 by the action of the rotating blades 7 rotated by the drive motor 13 and the viscous force of the air flow toward the center while swirling by the action of the suction blower 14. Is done
The coarse powder A descends while swirling in the hopper 2 due to the above centrifugal force, and is discharged from the coarse powder outlet 17 at the lower side, while the fine powder B has a viscous force of the air flow and rides on the air flow. Through the gap between the rotary blades 7 into the duct 15 and is collected by a collecting device (not shown).

【0023】上記構造の装置を用いて、粒子間の付着力
が強く、凝集が発生し易いという性状を有する石灰石粒
子について、3μmの分離限界粒子のストークス径で、
分級試験を行った。その分級試験の結果を、図2にTr
omp曲線として示す。
Using the apparatus having the above structure, with respect to limestone particles having a property that the adhesion between particles is strong and agglomeration easily occurs, the Stokes diameter of the separation limit particle of 3 μm,
A classification test was conducted. The result of the classification test is shown in FIG.
Shown as an omp curve.

【0024】なお、図2中(a)のTromp曲線は、
前記した式1から見出される分離限界粒子のストークス
径と、回転翼7及び吸引ブロアー14の関係から、3μ
mが分離限界粒子のストークス径となる回転翼7、及び
吸引ブロアー14の回転数を算出し、該回転翼7の回転
数と同一の回転数で、上記分散板6を回転させた場合、
即ち分散板6と、回転翼7との同一の駆動手段によって
回転させられていた従来の気流分級機を想定して、石灰
石粒子を3μmをカット径として分級した場合の結果で
ある。
The Tromp curve in FIG. 2A is
From the relationship between the Stokes diameter of the separation limit particles found from the above equation 1 and the rotor 7 and the suction blower 14, 3 μ
When the number of rotations of the rotary blade 7 and the suction blower 14 in which m is the Stokes diameter of the separation limit particles are calculated and the dispersion plate 6 is rotated at the same number of rotations as the rotary blade 7,
That is, it is a result when limestone particles are classified with a cut diameter of 3 μm, assuming a conventional airflow classifier that is rotated by the same drive means of the dispersion plate 6 and the rotary blade 7.

【0025】これに対し、図2中(b)のTromp曲
線は、上記式1より算出した回転翼7の回転数に関係な
く、分散板6の回転数を被分級原料である石灰石粒子が
最も効率的に一次粒に解きほぐされる回転数に設定し、
石灰石粒子を3μmをカット径として分級した場合の結
果である。
On the other hand, in the Tromp curve of FIG. 2B, the rotational speed of the dispersion plate 6 is the highest for the limestone particles as the material to be classified, regardless of the rotational speed of the rotary blade 7 calculated from the above equation 1. Set the number of revolutions to efficiently loosen the primary particles,
It is a result when limestone particles are classified with a cut diameter of 3 μm.

【0026】図2に示した(a),(b)のTromp
曲線から、分散板6と回転翼7とを各々別駆動のものと
し、分散板6の回転数を被分級原料が最も効率的に一次
粒に解きほぐされる回転数に設定し、被分級原料の分級
を行うと、その分級精度は飛躍的に向上することが判明
する。
Tromps (a) and (b) shown in FIG.
From the curve, the dispersion plate 6 and the rotary blade 7 are driven separately, and the rotation speed of the dispersion plate 6 is set to the rotation speed at which the classified raw material is most efficiently disentangled into primary particles. It is found that the classification accuracy is dramatically improved when the classification is performed.

【0027】以上、本発明の一実施例に付き説明した
が、本発明は既述の実施例に限定されるものではなく、
本発明の技術的思想に基づいて各種の変形及び変更が可
能である。
The embodiment of the present invention has been described above. However, the present invention is not limited to the above-mentioned embodiment,
Various modifications and changes can be made based on the technical idea of the present invention.

【0028】特に、上記実施例において説明した気流分
級機の構造は、その一例を示したに過ぎず、回転式分散
板と回転翼との両者を有する全ての気流分級機におい
て、本発明にかかる思想、即ち回転式分散板と回転翼と
を各々別駆動のものとすることは、全て本願発明に包含
される。
In particular, the structure of the airflow classifier described in the above embodiments is merely an example, and the present invention is applicable to all the airflow classifiers having both the rotary dispersion plate and the rotary blades. The idea, that is, the rotary dispersion plate and the rotary blade are separately driven, is included in the present invention.

【0029】[0029]

【発明の効果】以上、説明した本発明にかかる気流分級
機によれば、分級する粉体の性状に合わせてその回転式
分散板の回転数を任意に変更できるため、性状の異なる
種々の粉体を高い分級精度で分級できる装置となる。
As described above, according to the air stream classifier according to the present invention, the rotational speed of the rotary dispersion plate can be arbitrarily changed according to the property of the powder to be classified, and thus various powders having different properties can be obtained. The device can classify the body with high accuracy.

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

【図1】本発明にかかる気流分級機の一実施例を示した
概念的な縦断面図である。
FIG. 1 is a conceptual vertical cross-sectional view showing an embodiment of an airflow classifier according to the present invention.

【図2】Tromp曲線を示した図である。FIG. 2 is a diagram showing a Tromp curve.

【図3】従来から使用されている気流分級機の一例を示
した概念的な縦断面図である。
FIG. 3 is a conceptual vertical cross-sectional view showing an example of an airflow classifier that has been conventionally used.

【符号の説明】[Explanation of symbols]

1 ケーシング 2 ホッパ 3 中空シャフト 4 シャフト 5 シュート 6 分散板 7 回転翼 8 プーリ 9 無端ベルト 10 駆動モータ 11 プーリ 12 無端ベルト 13 駆動モータ 14 吸引ブロアー 15 ダクト 16 分級室 17 粗粉出口 1 Casing 2 Hopper 3 Hollow shaft 4 Shaft 5 Chute 6 Dispersion plate 7 Rotor blade 8 Pulley 9 Endless belt 10 Drive motor 11 Pulley 12 Endless belt 13 Drive motor 14 Suction blower 15 Duct 16 Classification chamber 17 Coarse powder outlet

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ケーシング内に投入された被分級原料を
分散させる回転式分散板と、前記ケーシング内に旋回流
を形成する回転翼とを、各々別駆動のものとしたことを
特徴とする気流分級機。
1. An air flow characterized in that a rotary dispersion plate for dispersing the classified raw material charged in a casing and a rotary blade for forming a swirling flow in the casing are driven separately. Classifier.
JP18722493A 1993-06-30 1993-06-30 Air classifier Pending JPH0716539A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18722493A JPH0716539A (en) 1993-06-30 1993-06-30 Air classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18722493A JPH0716539A (en) 1993-06-30 1993-06-30 Air classifier

Publications (1)

Publication Number Publication Date
JPH0716539A true JPH0716539A (en) 1995-01-20

Family

ID=16202244

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18722493A Pending JPH0716539A (en) 1993-06-30 1993-06-30 Air classifier

Country Status (1)

Country Link
JP (1) JPH0716539A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2754475A1 (en) * 1995-04-14 1998-04-17 Ishikawahima Harima Jukogyo Ka Classifier for cement mfr installation
JP2007117825A (en) * 2005-10-26 2007-05-17 Ube Machinery Corporation Ltd Classifier

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2754475A1 (en) * 1995-04-14 1998-04-17 Ishikawahima Harima Jukogyo Ka Classifier for cement mfr installation
JP2007117825A (en) * 2005-10-26 2007-05-17 Ube Machinery Corporation Ltd Classifier
JP4614132B2 (en) * 2005-10-26 2011-01-19 宇部興産機械株式会社 Classification device

Similar Documents

Publication Publication Date Title
US3040888A (en) Classifier for pulverized substances
JPH08281213A (en) Classifier
JP4614132B2 (en) Classification device
JP3517692B2 (en) Airflow classifier
JPH0716539A (en) Air classifier
US8083071B2 (en) Rotating cone classifier
JP2002119920A (en) Air flow type classifier
JPH105696A (en) Powder classifier
JP3482669B2 (en) Classifier
JP2597794B2 (en) Method and apparatus for classifying powder raw materials
JP3341088B2 (en) Eddy current air classifier
JPH0780413A (en) Air classifier
JP2000157934A (en) Pneumatic classifier
KR940002840B1 (en) Powdered-body sorter
JPH11216426A (en) Air classifier
JPH0810706A (en) Pneumatic sorter
JPH07155698A (en) Vortex air classifier
JP4026051B2 (en) Classifier
SU1546181A1 (en) Rotary classifier
Weigel et al. Development of an air classifier for the classification of crushed aggregates
JP3448716B2 (en) Eddy current air classifier
JP3485624B2 (en) Powder classifier and its operation method
JPH0259076A (en) Apparatus for classifying particulate material
JPS5953115B2 (en) Powder classification device
JP2004121915A (en) Air flow type classifier