JPS61153163A - Electrostatically classifying apparatus of powdery granular body - Google Patents

Electrostatically classifying apparatus of powdery granular body

Info

Publication number
JPS61153163A
JPS61153163A JP28142384A JP28142384A JPS61153163A JP S61153163 A JPS61153163 A JP S61153163A JP 28142384 A JP28142384 A JP 28142384A JP 28142384 A JP28142384 A JP 28142384A JP S61153163 A JPS61153163 A JP S61153163A
Authority
JP
Japan
Prior art keywords
sieves
electrodes
sieve
particle size
pair
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
JP28142384A
Other languages
Japanese (ja)
Inventor
Kazuhiro Tsuruta
鶴田 和博
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.)
Fuji Electric Co Ltd
Original Assignee
Fuji Electric 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 Fuji Electric Co Ltd filed Critical Fuji Electric Co Ltd
Priority to JP28142384A priority Critical patent/JPS61153163A/en
Publication of JPS61153163A publication Critical patent/JPS61153163A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To classify the powder granular bodies efficiently without the clogging by making a pair of opposed sieves both electrodes, providing the electrode plates to the backs of the electrodes and spraying the electrically-conductive particles between both the electrodes. CONSTITUTION:A pair of sieves 11, 12 provided with the meshes wherein the powdery and granular bodies having the prescribed particle size and below are passed therethrough are opposed in the up-and-down direction and made to both electrodes. The electrode plates 15, 16 are arranged in the backs of the sieves 11, 12 of both the electrodes via the insulators 13, 14. The electrically-conductive particles 17 having the particle size larger than the prescribed particle size are sprayed between a pair of electrodes 11-15, 12-16 respectively. The sieve 11 and the electrode plate 16 are grounded and the sieve 12 and the electrode plate 15 are connected with an anode side of a high-voltage DC power source 22. When the powdery granular bodies 18 are introduced from a channel 21, these are sent between the sieves 11, 12 by means of the air current of a suction fan 26 and classified. In this case, since the sieves are always beaten by the electrically-conductive particles, the efficient classification is performed without clogging.

Description

【発明の詳細な説明】 (発明の属する技術分野) この発明は、粒度の異なる導電性粒子からなる粉粒体を
帯電させクーロン力を利用してふるいを通過させて所定
粒度の粉粒体を得る静電分級装置に関する。
Detailed Description of the Invention (Technical Field to which the Invention Pertains) The present invention is directed to charging powder and granules made of conductive particles with different particle sizes and passing them through a sieve using Coulomb force to obtain powder and granules of a predetermined particle size. The present invention relates to an electrostatic classifier.

(従来技術とその問題点) この種の装置はたとえば炭化珪素からなる研摩材粒子の
粒度を分類し、所望あらさの砥石をつくる際に用いられ
、第3図に示すような静電選別装置が知られている。こ
の装置は、所定粒度以下の粒度を通過せしめる大きさの
網目を有する、形が平板状に形成され水平におかれた金
属製のふ4い1を上部電極とし、これと上下方向に対向
して平行におかれた平板状の下部電極2との間に、モー
タ3によってベルト駆動されるローラ4と、所定粒度の
粒子が採集された後に残る粉粒体を溜める貯溜容器5側
に支承されたローラ6、との間に渡されたエンドレスの
誘電体ベルト8を前記下部電極2に近接して走らせ、サ
ンプルボックス7から誘電体ベルト8上に供給された導
電性粉粒体が前記両電極1.2の間を通過するときに、
まずこの粉粒体を下部電極2と同極性に帯電させ、この
帯電した粉粒体をクーロン力により反対極性を有する上
部電極1に向かって飛翔させ、このときの飛翔速度と空
気吸引ファン9により矢印方向に吸引される空気流とを
利用して、上部電極を構成するふるいの網目を通過させ
ようとするものである。ふるいに衝突し網目を通過する
ことができなかった粉粒体は、こんどは上部電極の極性
に帯電されてベルト方向へ吸引され、ここで再び反対極
性に帯電され、以下前記の過程を繰り返しながらバグフ
ィルタlOに収容される。従って両電極1,2の間を通
過した誘電体ベルト上には、所定粒度以下の粒子が除去
された、粒度の大きい粉粒体や、混在する絶縁性粒子が
残留し、これが貯溜容器5に収容される。
(Prior art and its problems) This type of device is used, for example, to classify the particle size of abrasive particles made of silicon carbide to produce a grindstone with a desired roughness. Are known. This device uses a metal screen 1, which is formed in a flat plate shape and placed horizontally and has a mesh size that allows particles of a particle size below a predetermined size to pass therethrough, as an upper electrode, and is vertically opposed to this. A roller 4 driven by a belt by a motor 3 is supported between a flat lower electrode 2 placed in parallel with a roller 4 and a storage container 5 for storing powder and granules remaining after particles of a predetermined size are collected. An endless dielectric belt 8 passed between the lower electrode 2 and the lower electrode 2 is run close to the lower electrode 2, and the conductive powder supplied from the sample box 7 onto the dielectric belt 8 is applied to both the electrodes. When passing between 1.2,
First, this granular material is charged with the same polarity as the lower electrode 2, and this charged granular material is caused to fly toward the upper electrode 1 having the opposite polarity by Coulomb force, and the flying speed and air suction fan 9 at this time are The purpose is to use the airflow sucked in the direction of the arrow to pass through the mesh of the sieve that constitutes the upper electrode. The powder that collided with the sieve and could not pass through the mesh is now charged with the polarity of the upper electrode and attracted towards the belt, where it is charged with the opposite polarity again, and the above process is repeated. It is accommodated in the bag filter IO. Therefore, on the dielectric belt that has passed between the electrodes 1 and 2, particles with a predetermined particle size or less have been removed, and large powder particles and mixed insulating particles remain. be accommodated.

しかしながら、このような装置では、分級される所定粒
度を細かくすると、網目を構成する金属線の太さは、そ
の機械的強度と製造の難易との両面からさほど細くでき
ないことから、ふるいの全面積に占める網目の全面積の
割合すなわち開口率が小さくなって分級作業の効率が低
下するのみならず、目づまりを生じやすくなり、分級さ
れる所定粒度が数ミクロン程度になると、このような方
法ではもはや分級不能となる。
However, in such devices, when the predetermined particle size to be classified is made finer, the thickness of the metal wires that make up the mesh cannot be made very thin due to both mechanical strength and manufacturing difficulty, so the total area of the sieve is reduced. The percentage of the total area of the mesh, that is, the aperture ratio, decreases, which not only reduces the efficiency of the classification work, but also causes clogging, and when the predetermined particle size to be classified is a few microns, it is no longer possible to use this method. It becomes impossible to classify.

そこで、このような微粉を分級する装置として、超音波
を用いたふるい振とう機がある。このふるい振とう機は
、ここには特に図示しないが、所定の大きさに網目が構
成されたふるいに分級される粉粒体を入れ、これを水が
張られた容器中に浸漬させ、ふるいを固定した状態で容
器に超音波振動を与え、水を介して被分級粉粒体を振動
させながら所定粒度以下の粉粒体を取り出すものである
Therefore, as a device for classifying such fine powder, there is a sieve shaker using ultrasonic waves. Although this sieve shaker is not particularly shown here, the powder to be classified is placed in a sieve with a mesh of a predetermined size, immersed in a container filled with water, and the sieve is passed through the sieve. Ultrasonic vibration is applied to the container in a fixed state, and while the powder to be classified is vibrated through water, powder with a predetermined particle size or less is taken out.

しかしながら、このような方法で取り出された粉粒体は
湿っているから、乾燥状態で使用するものにあっては、
分級作業に対して乾燥工程が余分に追加されることとな
り、所望の粉粒体を得るのにコストが上昇する。
However, since the powder extracted by this method is wet, if it is used in a dry state,
An extra drying step is added to the classification work, which increases the cost to obtain the desired powder or granular material.

(発明の目的) この発明は、分級方法が乾式であって、粒度が細かい微
粉に対しても目づまりがなく効率よく分級することので
きる静電分級装置を提供することを目的とする。
(Objective of the Invention) An object of the present invention is to provide an electrostatic classifier that uses a dry classification method and can efficiently classify fine powder without clogging.

(発明の要点) この発明は、粒度の異なる導電性粒子からなる粉粒体を
帯電させクーロン力を利用してふるいを通過させて所定
粒度の粉粒体を得る静電分級装置として、水平に置かれ
上下方向に対向させた1対のふるいを両電極とし、該両
電極のそれぞれの電極の背後に電極板を配置してさらに
それぞれ1対の電極を構成し、該それぞれ1対の電極の
間に前記所定粒度より大きい粒度を有する導電性粒子を
撒布するとともに前記1対のふるいの間に前記分級され
る粉粒体が導入されるように構成することにより、前記
の目的を達成しようとするものである。すなわち、第2
図に示されるように、所定粒度以下の粉粒体を通過せし
める網目を備えた1対のふるい11.12を上下方向に
対向させて両電極を構成し、□陰極側が接地された高圧
直流電源22の陽極側をふるい12と接続し、ふるい1
1を接地する。この両電極を構成するそれぞれのふるい
11.12の背後には、絶縁物13.14を介して電極
板15.16が配置されてそれぞれ1対の電極11−1
5.12−16が構成され、該それぞれ1対の電極の間
には、前記所定の粒度より大きい粒度を有する導電性粒
子が撒布されている。電極板15は相手方電極11とは
反対極性の陽極に接続され、電極板16も相手方電極1
2とは反対極性の大地電位に接続されているから、前記
粒度の大きい導電性粒子は、ふるい11..12の網目
を通過することなく、電極11.15および12.16
の間でそれぞれ往復運動をしながらふるい11.12を
叩く。
(Summary of the Invention) The present invention is an electrostatic classification device that charges powder and granules made of conductive particles of different particle sizes and passes them through a sieve using Coulomb force to obtain powder and granules of a predetermined particle size. A pair of sieves placed and facing each other in the vertical direction are used as both electrodes, and an electrode plate is arranged behind each of the two electrodes to further constitute a pair of electrodes, and each of the pair of electrodes is The above object is achieved by dispersing conductive particles having a particle size larger than the predetermined particle size between the sieves and introducing the classified powder between the pair of sieves. It is something to do. That is, the second
As shown in the figure, a pair of sieves 11 and 12 each having a mesh that allows powder particles of a predetermined particle size or less to pass through are vertically opposed to form both electrodes, and a high-voltage DC power supply with the cathode side grounded. Connect the anode side of 22 to sieve 12,
1 is grounded. Behind each of the sieves 11.12 constituting both electrodes, an electrode plate 15.16 is arranged with an insulator 13.14 in between, and each pair of electrodes 11-1
5.12-16 are constructed, and conductive particles having a particle size larger than the predetermined particle size are sprinkled between each pair of electrodes. The electrode plate 15 is connected to an anode having a polarity opposite to that of the other electrode 11, and the electrode plate 16 is also connected to the other electrode 1.
2, the large conductive particles are connected to the ground potential of opposite polarity to sieve 11. .. electrodes 11.15 and 12.16 without passing through the mesh of 12.
The sieves 11 and 12 are hit while reciprocating between the sieves 11 and 12.

一方、ふるい11.12の間に外部から導入された被分
級粉粒体中の前記ふるい11.12の網目より小さい粉
粒体は、第3図に示された従来例と同一の分級原理によ
り、ふるいの網目を通過してその背後にある電極空間A
、Bに入る。この電極空間には図示されないバグフィル
タへ向かう空気流が存在しているから、所定粒度の粉粒
体がバグフィルタに収容されるとともに、ふるいの網目
より粒度が大きい粗粒は、図の19のように、この分級
装置から排出される。
On the other hand, the powder particles smaller than the mesh of the sieve 11.12 in the powder particles introduced from the outside between the sieves 11.12 are classified according to the same classification principle as in the conventional example shown in FIG. , the electrode space A that passes through the sieve mesh and is behind it.
, enters B. In this electrode space, there is an air flow heading towards the bag filter (not shown), so powder particles with a predetermined particle size are accommodated in the bag filter, and coarse particles with a particle size larger than the mesh of the sieve are As such, it is discharged from this classification device.

ところで、ふるい11.12は、それぞれ背後にある電
極15.16との間に撒布された大粒度の導電性粒子に
よって叩かれているから、分級される粒度が細かい微粉
の場合にも、ふるいの網目のまわりに堆積して目づまり
の原因となる微粉はふるい12においては常時叩き落さ
れ、また、下方のふるい11に堆積した微粉は容易に上
方のふるい12に向かって飛翔し、ふるいの網目の大き
さは常に本来の大きさを保つ。このため、時間の経過と
ともに分級効率が低下することなく、常に初期の分級効
率を維持することができる。
By the way, the sieves 11 and 12 are beaten by large conductive particles that are spread between them and the electrodes 15 and 16 behind them, so even when the particles to be classified are fine, the sieves are The fine powder that accumulates around the mesh and causes clogging is constantly knocked off by the sieve 12, and the fine powder that accumulates on the lower sieve 11 easily flies toward the upper sieve 12, and the fine powder that accumulates around the mesh of the sieve causes clogging. The size always remains the original size. Therefore, the initial classification efficiency can always be maintained without the classification efficiency decreasing over time.

(発明の実施例)      ′ 第1図に、本発明に基づく静電分級装置の実施例を示す
。図からみられるように、水平に置かれ上下方向に小間
隔をもって対向配置された1対のふるい11.12の間
に形成される空間は、分級される粉粒体18が導入され
るチャンネル21の側壁を構成する絶縁板211?によ
って側方が閉鎖されている。チャンネル21はこの絶縁
板211?と上、下の絶縁板21αとによってその導入
口が形成され、同じく絶縁板21Cと上、下の絶縁板2
1A とによってその吐出口が形成されている。
(Embodiment of the Invention) ' Fig. 1 shows an embodiment of an electrostatic classifier based on the present invention. As can be seen from the figure, the space formed between the pair of sieves 11 and 12, which are placed horizontally and opposed to each other with a small interval in the vertical direction, is the space formed between the channels 21 into which the granular material 18 to be classified is introduced. Insulating plate 211 forming the side wall? The sides are closed by. Channel 21 is this insulating plate 211? The inlet is formed by the upper and lower insulating plates 21α, and the insulating plate 21C and the upper and lower insulating plates 2
The discharge port is formed by 1A.

対向する1対のふるい11.12のそれぞれの背後には
電極板15.16が配され、ふるい11と電極板15.
ふるい12と電極板16との間にある空間A、 B (
第2図参照)はそれぞれ13,210および14.21
’でとり囲まれ、各電極空間A、  Bはダクト 24
α、24Aを介してバグフィルタ室25と連絡されてい
る。バブフィルタ室25には吸引ファンz6が取り付け
られ、チャンネル21の粉粒体導入口から1対のふるい
11.12によって形成された空間と、それぞれのふる
い背後の電極空間A、Bとを通ってバグフィルタ室25
へ向かう空気流を生せしめる。
Electrode plates 15.16 are arranged behind each of the pair of opposing sieves 11.12, and the sieve 11 and the electrode plate 15.16 are arranged behind each other.
Spaces A and B between the sieve 12 and the electrode plate 16 (
(see Figure 2) are 13,210 and 14.21, respectively.
', and each electrode space A, B is a duct 24
It is connected to the bag filter room 25 via α and 24A. A suction fan z6 is attached to the bub filter chamber 25, and the suction fan z6 passes from the powder introduction port of the channel 21 through the space formed by the pair of sieves 11 and 12 and the electrode spaces A and B behind each sieve. Bag filter room 25
Creates an air flow towards.

このように構成された静電分級装置のふるい11と電極
板16とは接地され、ふるい12と電極板15は高圧直
流電源z2の陽極側に接続される。
The sieve 11 and electrode plate 16 of the electrostatic classifier thus configured are grounded, and the sieve 12 and electrode plate 15 are connected to the anode side of the high voltage DC power supply z2.

この状態で粉粒体18を空気流23とともにチャンネル
21の導入口から導入すると、吸引7アン26が生ずる
空気流によって、粉粒体18は1対のふるい11.12
の間へ送り込まれ、ここですでに述べた分級原理によっ
て分級され、所定粒度以下の粉粒は電極空間A、Bへ入
り、さらに空気流によりバグフィルタ室25へ送り込ま
れる。また、電極空間A、B内に撒布された大粒度の導
電性粒子は、該分級装置の運転中は常時ふるい11.1
2を叩いているから、ふるいの網目の大きさは常にその
本来の大きさを保ち、時間が経過しても初期の分級効率
を維持することができる。
When the granular material 18 is introduced from the inlet of the channel 21 together with the air flow 23 in this state, the granular material 18 is passed through the pair of sieves 11 and 12 by the air flow generated by the suction 7 amp 26.
Powder particles having a predetermined particle size or less enter the electrode spaces A and B, and are further sent into the bag filter chamber 25 by the air flow. In addition, the large conductive particles scattered in the electrode spaces A and B are constantly filtered through the sieve 11.1 during the operation of the classification device.
2, the mesh size of the sieve always maintains its original size, and the initial classification efficiency can be maintained even over time.

このようにして所定粒度以下の粉粒が分級された後の、
より大きい粒度の粉粒は、図の19のようにチャンネル
21の吐出口から吐き出され、図示されない貯溜容器に
収容される。
After the powder grains with a predetermined particle size or less are classified in this way,
Powder grains having a larger particle size are discharged from the outlet of the channel 21 as shown in 19 in the figure, and are stored in a storage container (not shown).

また、第1図に示された実施例において、上。Also, in the embodiment shown in FIG.

下1対のふるいの対向する網目のピッチを、第2図に示
されるように半ピッチづつずらせると、クーロン力によ
り相手方のふるいに向かって飛翔する所定粒度以下の粉
粒は、1対のふるいの間隔が小さく、シかもこの1対の
ふるいには高電圧が印加されていることから、ふるいの
面に垂直に飛翔し、相手方のふるいの網目を容易に通過
することができるようになり、一定時間内に分級可能な
粉粒体の量が増加する。
When the pitch of the opposing meshes of the lower pair of sieves is shifted by half a pitch as shown in Fig. 2, particles of a predetermined particle size or less that fly toward the other sieve due to Coulomb force are Because the distance between the sieves is small and a high voltage is applied to this pair of sieves, the particles fly perpendicular to the sieve surface and can easily pass through the mesh of the other sieve. , the amount of powder that can be classified within a certain period of time increases.

(発明の効果) 以上に述べたように、本発明によれば、(1)水平に置
かれ上下方向に対向させた1対のふるいを両電極として
いるから、被分級粉粒体を上、下両方向に分級すること
ができ、分級効率が高い。
(Effects of the Invention) As described above, according to the present invention, (1) since a pair of sieves placed horizontally and facing each other in the vertical direction are used as both electrodes, the granular material to be classified is It can be classified in both downward directions and has high classification efficiency.

(2)1対のふるいのそれぞれの背後に電極空間を形成
し、この電極空間内に粒度の大゛きい金属粒子を撒布し
、この空間を構成する両電極間に直流高電圧を印加して
、分級装置の運転中は常時ふるいを叩くようにしたので
、分級される粒子の粒度が細かい場合にも目づまりがな
く、ふるいの網目の大きさは常に本来の大きさを保ち、
時間の経過とともに分級効率が低下することなく、常に
初期の分級効率が維持される。
(2) An electrode space is formed behind each of a pair of sieves, large metal particles are scattered in this electrode space, and a high DC voltage is applied between the two electrodes that make up this space. Since the sieve is constantly tapped during operation of the classification device, there is no clogging even when the particles to be classified are fine, and the sieve mesh size always maintains its original size.
The initial classification efficiency is always maintained without decreasing the classification efficiency over time.

(3)本発明の静電分級装置は乾式であるから、超音波
を用いる湿式の振とり機の場合のように粉粒体の乾燥工
程を必要とせず、粒度の小さい微粉を粒度の大きい粗粒
と同等のコストで得ることができる。
(3) Since the electrostatic classifier of the present invention is a dry type, there is no need for a drying process for powder and granules unlike in the case of a wet shaker that uses ultrasonic waves, and it can separate fine powder with a small particle size into coarse particles with a large particle size. It can be obtained at the same cost as grain.

などの効果が得られるほか、前記1対のふるいの対向す
る網目のピッチを半ピッチづつずらせることにより、分
級される粉粒の網目の通過が容易になり、一定時間内に
分級可能な粉粒体の量が増え、分級効率を向上させるこ
とができるという付加的効果が得られる。
In addition to the effects of The additional effect is that the amount of granules increases and the classification efficiency can be improved.

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

第1図は本発明に基づく静電分級装置の構成の実施例を
示す斜視図、第2図は本発明による分級効率の向上を説
明する分級原理図、第3図は従来の静電分級装置の構成
を示す斜視図である。 1:ふるい、2:電極、h士暑甫==;ll、12゜ふ
るい、15.16 :電極板、17:導電性粒子、1a
:粉粒体、21:チャンネル。表し祠11←第1図
Fig. 1 is a perspective view showing an example of the configuration of an electrostatic classifier based on the present invention, Fig. 2 is a classification principle diagram explaining the improvement in classification efficiency according to the present invention, and Fig. 3 is a conventional electrostatic classifier. FIG. 1: Sieve, 2: Electrode, 12° sieve, 15.16: Electrode plate, 17: Conductive particles, 1a
: Powder, 21: Channel. Expression Shrine 11←Figure 1

Claims (1)

【特許請求の範囲】 1)粒度の異なる導電性粒子からなる粉粒体を帯電させ
クーロン力を利用してふるいを通過させて所定粒度の粉
粒体を得る静電分級装置であつて、水平に置かれ上下方
向に対向させた1対のふるいを両電極とし、該両電極の
それぞれの電極の背後に電極板を配置してさらにそれぞ
れ1対の電極を構成し、該それぞれ1対の電極の間に前
記所定粒度より大きい粒度を有する導電性粒子を撒布す
るとともに前記1対のふるいの間に前記分級される粉粒
体が導入されるように構成されたことを特徴とする粉粒
体の静電分級装置。 2)特許請求の範囲第1項記載の静電分級装置において
、両電極を構成する1対のふるいの1方のふるいの目の
ピッチと他方のふるいの目のピッチとが互に半ピッチず
れるように配されたことを特徴とする粉粒体の静電分級
装置。
[Scope of Claims] 1) An electrostatic classifier that obtains powder or granular material of a predetermined particle size by charging powder or granular material made of conductive particles with different particle sizes and passing it through a sieve using Coulomb force, which A pair of sieves placed on the screen and facing each other in the vertical direction are used as both electrodes, and an electrode plate is arranged behind each electrode of the two electrodes to further form a pair of electrodes. A granular material characterized in that it is configured such that conductive particles having a particle size larger than the predetermined particle size are spread between the two sieves, and the classified granular material is introduced between the pair of sieves. electrostatic classifier. 2) In the electrostatic classification device according to claim 1, the pitch of the meshes of one sieve and the pitch of the meshes of the other sieve of a pair of sieves forming both electrodes are shifted by half a pitch from each other. An electrostatic classification device for powder and granular materials characterized by being arranged as follows.
JP28142384A 1984-12-25 1984-12-25 Electrostatically classifying apparatus of powdery granular body Pending JPS61153163A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28142384A JPS61153163A (en) 1984-12-25 1984-12-25 Electrostatically classifying apparatus of powdery granular body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28142384A JPS61153163A (en) 1984-12-25 1984-12-25 Electrostatically classifying apparatus of powdery granular body

Publications (1)

Publication Number Publication Date
JPS61153163A true JPS61153163A (en) 1986-07-11

Family

ID=17638953

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28142384A Pending JPS61153163A (en) 1984-12-25 1984-12-25 Electrostatically classifying apparatus of powdery granular body

Country Status (1)

Country Link
JP (1) JPS61153163A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006015298A (en) * 2004-07-05 2006-01-19 Kawasaki Heavy Ind Ltd Electrostatic separation device of particulate
KR100609816B1 (en) * 2004-05-27 2006-08-08 신한기연주식회사 Dedusting device
JP2007155992A (en) * 2005-12-02 2007-06-21 Ricoh Co Ltd Recovered toner classifier and image forming apparatus
JP2008104954A (en) * 2006-10-25 2008-05-08 Institute Of Physical & Chemical Research Fine particle classifier

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100609816B1 (en) * 2004-05-27 2006-08-08 신한기연주식회사 Dedusting device
JP2006015298A (en) * 2004-07-05 2006-01-19 Kawasaki Heavy Ind Ltd Electrostatic separation device of particulate
JP2007155992A (en) * 2005-12-02 2007-06-21 Ricoh Co Ltd Recovered toner classifier and image forming apparatus
JP2008104954A (en) * 2006-10-25 2008-05-08 Institute Of Physical & Chemical Research Fine particle classifier

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