JPH0574681U - Multi-stage classifier - Google Patents

Multi-stage classifier

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Publication number
JPH0574681U
JPH0574681U JP2181092U JP2181092U JPH0574681U JP H0574681 U JPH0574681 U JP H0574681U JP 2181092 U JP2181092 U JP 2181092U JP 2181092 U JP2181092 U JP 2181092U JP H0574681 U JPH0574681 U JP H0574681U
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JP
Japan
Prior art keywords
classifier
raw material
air conduit
coarse
air
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
JP2181092U
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Japanese (ja)
Inventor
貞隆 坂本
哲 富永
喜代司 笹原
新悟 向井
暢哉 八田
Original Assignee
大阪セメント株式会社
石川島播磨重工業株式会社
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Priority to JP2181092U priority Critical patent/JPH0574681U/en
Publication of JPH0574681U publication Critical patent/JPH0574681U/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【目的】 粒度分布の広い原料を大量にしかも精度良く
多段に分級できるようにする。 【構成】 回転する分級羽根4の外周から混合気流5が
導入され、分級羽根4を通り抜ける精粉6と分級羽根4
を通ることなく落下する粗粉7とに分級するようにした
回転式分級機1と、該回転式分級機1に接続した空気導
管9を備え、該空気導管9内の空気流10に対して交差
する方向に原料14を落下供給するよう空気導管9の途
中上側に原料供給口13を設けると共に、前記空気導管
9における前記原料供給口13の下方位置に粗粒分離ホ
ッパ16,17を設けた重力式分級機26とを備える。
(57) [Summary] [Purpose] To enable large-scale and accurate multi-stage classification of raw materials with a wide particle size distribution. [Composition] A mixed airflow 5 is introduced from the outer periphery of the rotating classification blade 4, and the fine powder 6 and the classification blade 4 passing through the classification blade 4 are introduced.
The rotary classifier 1 is designed to classify into the coarse powder 7 that falls without passing through, and the air conduit 9 connected to the rotary classifier 1 is provided, with respect to the air flow 10 in the air conduit 9. A raw material supply port 13 is provided in the middle of the air conduit 9 so that the raw material 14 is dropped and supplied in the intersecting direction, and coarse particle separation hoppers 16 and 17 are provided below the raw material supply port 13 in the air conduit 9. And a gravity classifier 26.

Description

【考案の詳細な説明】[Detailed description of the device]

【0001】[0001]

【産業上の利用分野】[Industrial applications]

本考案は、原料を多段階に精度良く分級することができる多段分級機に関する ものである。 The present invention relates to a multi-stage classifier capable of accurately classifying raw materials in multiple stages.

【0002】[0002]

【従来の技術】[Prior Art]

粒度分布範囲の広い原料を、所要の粒度毎に分級する際、従来は機械式多段篩 (モーゲンセン多段篩)で実施することが一般に行われてきた。この機械式多段 篩は、金属製コイルを使用した篩目を振動させて、該篩目上に原料を供給するこ とにより分級を行うようにしており、従って分級したい粒度に応じたメッシュの 複数の篩目を備えるようにしている。 When classifying raw materials having a wide particle size distribution into desired particle sizes, it has been customary in the past to use a mechanical multi-stage sieve (Mogensen multi-stage sieve). This mechanical multi-stage sieve is designed to perform classification by vibrating the sieve mesh using a metal coil and supplying the raw material onto the sieve mesh. Therefore, a plurality of meshes corresponding to the particle size to be classified are selected. It has a sieve mesh.

【0003】[0003]

【考案が解決しようとする課題】[Problems to be solved by the device]

しかし、上記したような従来の機械式多段篩に於いては、篩目の摩耗が激しく メンテナンスが大変であり、又篩目が目詰りを起こしやすいために大容量の分級 に適しておらず、更に篩目の大きさに機械的な制限があるために分級できる最小 粒径に限度がある、等の問題を有していた。 However, in the conventional mechanical multi-stage sieve as described above, the mesh of the sieve is severe and the maintenance is difficult, and the mesh of the sieve is apt to be clogged, so that it is not suitable for the classification of a large volume. Further, there was a problem that there was a limit to the minimum particle size that could be classified due to mechanical restrictions on the size of the sieve mesh.

【0004】 又、回転する分級羽根の外周から原料の混合気流を導入し、分級羽根を通り抜 ける微粉と分級羽根を通ることなく落下する粗粉とに分級するようにした回転式 分級機が実施されているが、粒度を3段階以上に分級するようなことは困難であ り、又回転式分級機は比較的粉体のような粒子が細かいものの分級に適している が、粗粒を含むような粒度分布の広い原料の分級を行う際には粒子の衝突等によ る飛びはねにより粗粒が微粉に混入して分級精度が低下する、等の問題を有して いた。In addition, a rotary classifier that introduces a mixed air flow of raw materials from the outer circumference of a rotating classifying blade to classify it into fine powder that passes through the classifying blade and coarse powder that falls without passing through the classifying blade is provided. Although it has been implemented, it is difficult to classify the particle size in three or more steps, and the rotary classifier is suitable for classifying fine particles such as powder, but coarse particles are used. When classifying a raw material having a wide particle size distribution such as that containing coarse particles into fine powder due to splashing due to collision of particles, there is a problem that the classification accuracy decreases.

【0005】 本考案は、上記従来の問題点に鑑みてなしたもので、粒度分布の広い原料を大 量にしかも精度良く多段に分級することができる多段分級機を提供することを目 的とする。The present invention has been made in view of the above conventional problems, and an object of the present invention is to provide a multi-stage classifier capable of classifying a large amount of a raw material having a wide particle size distribution with high precision in multiple stages. To do.

【0006】[0006]

【課題を解決するための手段】[Means for Solving the Problems]

本考案は、回転する分級羽根の外周から混合気流が導入され、分級羽根を通り 抜ける微粉と分級羽根を通ることなく落下する粗粉とに分級するようにした回転 式分級機と、該回転式分級機に接続した空気導管を備え、該空気導管内の空気流 に対して交差する方向に原料を落下供給するよう空気導管の途中上側に原料供給 口を設けると共に、前記空気導管における前記原料供給口の下方位置に粗粒分離 ホッパを設けた重力式分級機とを備えたことを特徴とする多段分級機及び重力式 分級機の空気導管を、所要の下り勾配の角度を有して前記回転式分級機の分級羽 根の外周に接続していることを特徴とする多段分級機、に係るものである。 The present invention is directed to a rotary classifier in which a mixed airflow is introduced from the outer circumference of a rotating classifying blade to classify it into fine powder passing through the classifying blade and coarse powder falling without passing through the classifying blade, and the rotary classifier. An air conduit connected to the classifier is provided, and a raw material supply port is provided on the upper side of the air conduit so that the raw material drops and is supplied in a direction intersecting with the air flow in the air conduit, and the raw material supply in the air conduit is performed. The multi-stage classifier and the air duct of the gravity classifier, which are equipped with a gravity classifier equipped with a coarse-grain separation hopper at a position below the mouth, are rotated at the required downward gradient angle. The present invention relates to a multi-stage classifier, which is characterized in that it is connected to the outer circumference of a classifying blade of a type classifier.

【0007】[0007]

【作用】[Action]

本考案では、重力式分級機の原料供給口から空気導管内の空気流に交差するよ うに原料を供給すると、供給された原料中の微粉や粗粉は空気導管内の空気流に 乗って下流側に運び去られ、前記空気流に乗らない重量が大きい粗粒のみが重力 により粗粒分離ホッパに落下して分離される。 In the present invention, when the raw material is supplied from the raw material supply port of the gravity classifier so as to intersect with the air flow in the air conduit, the fine powder and coarse powder in the supplied raw material ride on the air flow in the air conduit to the downstream side. Only the coarse particles that are carried away to the side and do not ride on the air flow are dropped into the coarse particle separation hopper by gravity and separated.

【0008】 粗粒が分離された微粉と粗粉の混合気流は、空気導管から回転式分級機の分級 羽根に外周から接線方向に導入され、分級羽根を通り抜ける微粉と分級羽根を通 ることなく落下する粗粉とに精度良く分級される。A mixed air stream of fine powder and coarse powder from which coarse particles have been separated is introduced tangentially from the outer periphery into the classification blade of a rotary classifier from an air conduit and passes through the classification blade without passing through the fine powder and the classification blade. It is accurately classified into the falling coarse powder.

【0009】[0009]

【実施例】【Example】

以下本考案の実施例を図面を参照しつつ説明する。 Embodiments of the present invention will be described below with reference to the drawings.

【0010】 図1及び図2は本考案の多段分級機の一例を示すもので、セメント原料等のよ うに粉砕された原料から製品としての微粉と、ボールミル(二次粉砕機)などに より再び粉砕を必要とする粗粒と、粗粒専用の粉砕機(一次粉砕機)により再び 粉砕を必要とする粗粒等に多段階にしかも精度良く分級する必要のある場合に適 したものである。FIG. 1 and FIG. 2 show an example of the multi-stage classifier of the present invention, in which fine powder as a product from raw materials such as cement raw material and a ball mill (secondary pulverizer) are used again. It is suitable for the case where it is necessary to classify coarse particles that need to be crushed and coarse particles that need to be crushed again by a crusher for exclusive use of coarse particles (primary crusher) in multiple stages and with high precision.

【0011】 即ち、1は駆動モータ2により減速機3を介して鉛直軸心を中心に回転する分 級羽根4と固定の整流羽根4’を備えた回転式分級機であり、回転する分級羽根 4及び整流羽根4’の外周から混合気流5を導入し、分級羽根4を通り抜ける微 粉6と分級羽根4を通ることなく落下する粗粉7とに分級するようになっている 。That is, 1 is a rotary classifier equipped with a classifying blade 4 which is rotated around a vertical axis by a drive motor 2 via a speed reducer 3 and a fixed rectifying blade 4 ′. The mixed air flow 5 is introduced from the outer circumference of the rectifying blade 4 and the rectifying blade 4 ', and is classified into fine powder 6 passing through the classifying blade 4 and coarse powder 7 falling without passing through the classifying blade 4.

【0012】 前記回転式分級機1に、重力式分級機26を接続配置する。A gravitational classifier 26 is connected to the rotary classifier 1.

【0013】 即ち、一端に空気導入口8を有し且つ底部に粗粉7が堆積しないように所要の 下り勾配の角度αを有した空気導管9の他端を前記回転式分級機1の分級羽根4 の外周に接線方向から接続する。前記空気導管9の空気導入口8の後部位置に、 空気導管9内の空気流10が均一に安定するように整流する整流板11を設け、 又空気導管9が接線方向に接続されている回転式分級機1の底部には粗粉7が堆 積しないように所要の角度βを有した傾斜面12を形成する。That is, the other end of the air conduit 9 having an air inlet 8 at one end and a required downward slope angle α so that coarse powder 7 does not accumulate at the bottom is classified by the rotary classifier 1. It is tangentially connected to the outer circumference of the blade 4. At the rear position of the air introduction port 8 of the air conduit 9, there is provided a rectifying plate 11 for rectifying the air flow 10 in the air conduit 9 so as to be uniformly stabilized, and the air conduit 9 is tangentially connected to the rotary member. An inclined surface 12 having a required angle β is formed on the bottom of the type classifier 1 so that the coarse powder 7 is not deposited.

【0014】 更に、空気導管9の途中における上側に原料供給口13を形成し、且つ該原料 供給口13からの原料14が前記空気導管9内の空気流10に対して交差する方 向に落下供給されるようにした原料分散板15を設ける。該原料分散板15は、 空気導管9の空気導入口8側と原料分散板15との成す角度γが略90度或いは 90度以上になるように設けられている。Further, a raw material supply port 13 is formed on the upper side in the middle of the air conduit 9, and a raw material 14 from the raw material supply port 13 falls in a direction intersecting with the air flow 10 in the air conduit 9. The raw material dispersion plate 15 is provided so as to be supplied. The raw material dispersion plate 15 is provided so that an angle γ formed between the air introduction port 8 side of the air conduit 9 and the raw material dispersion plate 15 is approximately 90 degrees or 90 degrees or more.

【0015】 更に、前記空気流整流導管9における前記原料供給口13の下方位置に、粗粒 分離ホッパ16を設ける。図示の場合、前記粗粒分離ホッパ16の更に回転式分 級機1側に別の粗粒分離ホッパ17を設けて粒度の異なる2種類の粗粒18を分 離することができるようにしており、且つ2つの粗粒分離ホッパ16,17の間 には分離する粒度を変えられるようにした調整板19を設けている。この調整板 19は固定をしたり、或いは設置を省略することもできる。Further, a coarse grain separation hopper 16 is provided below the raw material supply port 13 in the air flow rectifying conduit 9. In the case shown in the figure, another coarse particle separating hopper 17 is provided on the rotary classifier 1 side of the coarse particle separating hopper 16 so that two kinds of coarse particles 18 having different particle sizes can be separated. Further, an adjusting plate 19 is provided between the two coarse-grain separating hoppers 16 and 17 so that the grain size for separation can be changed. The adjusting plate 19 may be fixed or may be omitted.

【0016】 又、前記回転式分級機1の傾斜面12の下側には、粗粉回収ホッパ20を設け ていると共に、前記分級羽根4の内側上部には、微粉捕集機21と吸引ファン2 2からなる微粉捕集装置23を吸引管24を介して接続している。図中25は原 料供給口13、粗粒分離ホッパ16,17及び粗粉回収ホッパ20に設けたエア ロックフィーダを示す。A coarse powder recovery hopper 20 is provided below the inclined surface 12 of the rotary classifier 1, and a fine powder collector 21 and a suction fan are provided above the inside of the classifying blade 4. A fine powder collector 23 composed of 22 is connected via a suction pipe 24. Reference numeral 25 in the drawing denotes an air lock feeder provided in the raw material supply port 13, the coarse particle separating hoppers 16 and 17, and the coarse powder collecting hopper 20.

【0017】 次に作用を説明する。Next, the operation will be described.

【0018】 微粉捕集装置23の吸引ファン22を駆動すると、回転式分級機1を介して空 気導管9の空気導入口8から空気が吸引され、空気導管9内に安定した空気流1 0が形成される。When the suction fan 22 of the fine powder collecting device 23 is driven, air is sucked from the air introduction port 8 of the air conduit 9 via the rotary classifier 1, and a stable air flow 10 is supplied into the air conduit 9. Is formed.

【0019】 重力式分級機26の原料供給口13から原料14を供給すると、原料14は原 料分散板15の角度γにより、空気導管9内の空気流10に交差するように供給 され、原料14中の微粉や粗粉は空気導管9内の空気流10に乗って下流側に運 び去られ、前記空気流10に乗れない重量が大きい粗粒18のみが重力により粗 粒分離ホッパ16に落下して分離され、エアロックフィーダ25を介して外部に 取り出される。又比較的粒度の小さい粗粒18は下流側の粗粒分離ホッパ17に より分離される。図示の場合、2つの粗粒分離ホッパ16,17により粒度が異 なる粗粒18を分離することができ、且つ上記2つの粗粒分離ホッパ16,17 の間に設けた調整板19の角度を変えることにより、分離する粒度を調節するこ とができる。When the raw material 14 is supplied from the raw material supply port 13 of the gravity type classifier 26, the raw material 14 is supplied by the angle γ of the raw material dispersion plate 15 so as to intersect the air flow 10 in the air conduit 9, and the raw material 14 is supplied. The fine powder and coarse powder in 14 are carried on the air flow 10 in the air conduit 9 and carried away to the downstream side, and only the coarse particles 18 having a large weight that cannot be carried on the air flow 10 are transferred to the coarse particle separation hopper 16 by gravity. It is dropped, separated, and taken out to the outside via the airlock feeder 25. The coarse particles 18 having a relatively small particle size are separated by the coarse particle separating hopper 17 on the downstream side. In the case shown in the figure, the coarse particles 18 having different particle sizes can be separated by the two coarse particle separating hoppers 16 and 17, and the angle of the adjusting plate 19 provided between the two coarse particle separating hoppers 16 and 17 can be adjusted. By changing it, it is possible to control the particle size to be separated.

【0020】 粗粒18が分離された微粉と粗粉の混合気流5は、空気導管9から回転式分級 機1の分級羽根4の外周に接線方向から導かれ、分級羽根4を通り抜ける微粉6 と分級羽根4を通ることなく落下する粗粉7とに精度良く分級され、分級羽根4 を通り抜けた微粉6は微粉捕集装置23の微粉捕集機21により回収され、また 分級羽根4により弾かれて通過できなかった粗粉7は傾斜面12を介して粗粉回 収ホッパ20に落下し、エアロックフィーダ25を介して外部に取り出される。The mixed air flow 5 of fine powder and coarse powder from which the coarse particles 18 are separated is introduced from the air conduit 9 to the outer periphery of the classification blade 4 of the rotary classifier 1 in the tangential direction, and passes through the classification blade 4 and the fine powder 6 The fine powder 6 that has been accurately classified into the coarse powder 7 that does not pass through the classification blade 4 and has passed through the classification blade 4 is recovered by the fine powder collector 21 of the fine powder collecting device 23 and repelled by the classification blade 4. The coarse powder 7 that cannot pass through the inclined surface 12 falls into the coarse powder collecting hopper 20 and is taken out through the air lock feeder 25.

【0021】 上記したように、空気導管9を流れる空気流10により粗粒18を重力差によ り分離するようにしているので、先ず粗粒18を安定して精度良く分離すること ができ、続いて粗粒18が分離された微粉6及び粗粉7のみを流度が小さいもの の分級に優れている回転式分級機1に導いて分級するようにしているので、全体 的に精度の良い分級を行うことができると共に、粒度に応じて優れた分級機能を 発揮する装置を用いて分級を行うようにしたことにより、装置の処理能力を増大 させることができる。As described above, since the coarse particles 18 are separated by the gravity difference by the air flow 10 flowing through the air conduit 9, first, the coarse particles 18 can be stably and accurately separated. Subsequently, since only the fine powder 6 and the coarse powder 7 from which the coarse particles 18 are separated are guided to the rotary classifier 1 which has a small flow rate but is excellent in classification, the overall accuracy is high. Since the classification can be performed and the classification is performed using an apparatus that exhibits an excellent classification function depending on the particle size, the processing capacity of the apparatus can be increased.

【0022】 尚、本考案は上記実施例にのみ限定されるものではなく、回転式分級機と重力 式分級機とを水平に接続したり、相互間に接続管を介在させて接続するようにし ても良いこと、原料供給口の設置位置、粗粒分離ホッパの設置位置及び設置数、 並びに空気導管及び原料分散板の傾斜角度等は種々変更し得ること、その他本考 案の要旨を逸脱しない範囲内において種々変更を加え得ること等は勿論である。The present invention is not limited to the above-mentioned embodiment, and the rotary classifier and the gravity classifier may be connected horizontally, or connected by interposing a connecting pipe between them. It is also possible to change the installation position of the raw material supply port, the installation position and number of the coarse grain separation hopper, the inclination angle of the air conduit and the raw material dispersion plate, etc., and other points not departing from the gist of the present proposal. It goes without saying that various changes can be made within the range.

【0023】[0023]

【考案の効果】[Effect of the device]

本考案の多段分級機によれば、空気流中に原料を供給して先ず粗粒を重力差に よって分離し、続いて粗粒が分離された微粉及び粗粉のみを回転式分級機に導い て微粉と粗粉とに分級するようにしているので、原料を粒度に応じて優れた分級 機能を発揮する装置により段階的に分級することができ、精度の高い多段分級を 可能にすると共に、装置の分級能力を増大することができる優れた効果を奏し得 る。 According to the multi-stage classifier of the present invention, the raw material is supplied into the air flow to first separate the coarse particles by the difference in gravity, and then only the fine particles and the coarse particles from which the coarse particles are separated are guided to the rotary classifier. Since it classifies the material into fine powder and coarse powder, the raw material can be classified in stages by a device that exhibits an excellent classification function according to the particle size, enabling highly accurate multistage classification and The excellent effect that the classification ability of the device can be increased can be obtained.

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

【図1】本考案の一実施例を示す部分切断正面図であ
る。
FIG. 1 is a partially cut front view showing an embodiment of the present invention.

【図2】図1の平面図である。FIG. 2 is a plan view of FIG.

【符号の説明】[Explanation of symbols]

1 回転式分級機 4 分級羽根 5 混合気流 6 微粉 7 粗粉 9 空気導管 10 空気流 13 原料供給口 14 原料 16 粗粒分離ホッパ 17 粗粒分離ホッパ 26 重力式分級機 α 下り勾配の角度 1 rotary classifier 4 classifying blade 5 mixed air flow 6 fine powder 7 coarse powder 9 air conduit 10 air flow 13 raw material supply port 14 raw material 16 coarse particle separation hopper 17 coarse particle separation hopper 26 gravity classifier α angle of descending gradient

───────────────────────────────────────────────────── フロントページの続き (72)考案者 笹原 喜代司 東京都江東区豊洲三丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 (72)考案者 向井 新悟 東京都江東区豊洲三丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 (72)考案者 八田 暢哉 東京都江東区豊洲三丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kiyoji Sasahara 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawajima Harima Heavy Industries, Ltd. Toyosu General Office (72) Inventor Shingo Mukai 3-2 Toyosu, Koto-ku, Tokyo No. 16 Ishikawajima Harima Heavy Industries Co., Ltd. Toyosu General Office (72) Inventor Nobuya Hatta 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawajima Harima Heavy Industries Co., Ltd. Toyosu General Office

Claims (2)

【実用新案登録請求の範囲】[Scope of utility model registration request] 【請求項1】 回転する分級羽根の外周から混合気流が
導入され、分級羽根を通り抜ける微粉と分級羽根を通る
ことなく落下する粗粉とに分級するようにした回転式分
級機と、該回転式分級機に接続した空気導管を備え、該
空気導管内の空気流に対して交差する方向に原料を落下
供給するよう空気導管の途中上側に原料供給口を設ける
と共に、前記空気導管における前記原料供給口の下方位
置に粗粒分離ホッパを設けた重力式分級機とを備えたこ
とを特徴とする多段分級機。
1. A rotary classifier in which a mixed air stream is introduced from the outer periphery of a rotating classifying blade to classify fine powder passing through the classifying blade and coarse powder falling without passing through the classifying blade, and the rotary classifier. An air conduit connected to the classifier is provided, and a raw material supply port is provided in the middle of the air conduit so as to drop and supply the raw material in a direction intersecting the air flow in the air conduit, and the raw material supply in the air conduit. A multi-stage classifier characterized by comprising a gravity type classifier having a coarse-grain separating hopper at a position below the mouth.
【請求項2】 重力式分級機の空気導管を、所要の下り
勾配の角度を有して前記回転式分級機の分級羽根の外周
に接続している請求項1の多段分級機。
2. The multi-stage classifier according to claim 1, wherein the air pipe of the gravity classifier is connected to the outer periphery of the classifying blades of the rotary classifier with a required downward slope angle.
JP2181092U 1992-03-11 1992-03-11 Multi-stage classifier Pending JPH0574681U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2181092U JPH0574681U (en) 1992-03-11 1992-03-11 Multi-stage classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2181092U JPH0574681U (en) 1992-03-11 1992-03-11 Multi-stage classifier

Publications (1)

Publication Number Publication Date
JPH0574681U true JPH0574681U (en) 1993-10-12

Family

ID=12065417

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2181092U Pending JPH0574681U (en) 1992-03-11 1992-03-11 Multi-stage classifier

Country Status (1)

Country Link
JP (1) JPH0574681U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000070859A (en) * 1998-08-27 2000-03-07 Wacker Chemie Gmbh Air screening for polysilicon
JP2006320850A (en) * 2005-05-19 2006-11-30 Kubota Corp Wind separator
KR100766908B1 (en) * 2006-06-09 2007-10-17 한용환 A sorting plant for gathering of particle from waste
JP2009508680A (en) * 2005-09-23 2009-03-05 ポリシウス アクチェンゲゼルシャフト Equipment for classifying input materials
WO2013079416A1 (en) * 2011-11-28 2013-06-06 Maschinenfabrik Köppern Gmbh & Co. Kg Device for sifting granular material

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000070859A (en) * 1998-08-27 2000-03-07 Wacker Chemie Gmbh Air screening for polysilicon
JP2006320850A (en) * 2005-05-19 2006-11-30 Kubota Corp Wind separator
JP4698286B2 (en) * 2005-05-19 2011-06-08 株式会社クボタ Wind sorter
JP2009508680A (en) * 2005-09-23 2009-03-05 ポリシウス アクチェンゲゼルシャフト Equipment for classifying input materials
KR100766908B1 (en) * 2006-06-09 2007-10-17 한용환 A sorting plant for gathering of particle from waste
WO2013079416A1 (en) * 2011-11-28 2013-06-06 Maschinenfabrik Köppern Gmbh & Co. Kg Device for sifting granular material
EP2785472B1 (en) 2011-11-28 2016-07-20 Maschinenfabrik Köppern GmbH. & Co. KG Device for classifying grainy products

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