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JP3733349B2 - Airflow classifier - Google Patents
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JP3733349B2 - Airflow classifier - Google Patents

Airflow classifier Download PDF

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Publication number
JP3733349B2
JP3733349B2 JP2002286489A JP2002286489A JP3733349B2 JP 3733349 B2 JP3733349 B2 JP 3733349B2 JP 2002286489 A JP2002286489 A JP 2002286489A JP 2002286489 A JP2002286489 A JP 2002286489A JP 3733349 B2 JP3733349 B2 JP 3733349B2
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Japan
Prior art keywords
classification
powder
rotor
chamber
casing
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JP2002286489A
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Japanese (ja)
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JP2004121915A (en
Inventor
克二 板倉
信司 藤本
貫太郎 金子
光雄 宮地
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Kurimoto Ltd
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Kurimoto Ltd
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Description

【0001】
【発明の属する技術分野】
この発明は、空気流でもって、粉体を複数の分級物、特に、平均粒径が4〜10μm程度の粉体を3つの分級物に分級する気流式分級機に関する。
【0002】
【従来の技術】
気流式分級機により、ガラス、炭化珪素、カラートナーなどの粉体を分級して各種の工業原料とする際、いわゆる粗粉は勿論のこと微粉も除いた所要範囲内の粒径のものが要求される。例えば、炭化珪素や窒化珪素は、樹脂に混ぜて研磨材として使用されるが、微粉が混じっていると研磨性能が落ち、トナーは、熱で溶かして、紙に付着させるが、微粉が混じっていると、微紛が先に溶け、文字が不鮮明になるからである。
【0003】
このため、それらの粉体を、上記所要範囲内の粒径の中粉、それより大径の粗粉、それより小径の微粉に分級して、その中粉を製品とする。その分級手段として、最も単純な方法は、気流式分級機を2台、直列に配置して、最初の分級機で、粉体を粗粉とそれ以外の粉体とに分級し、次の分級機で、それ以外の粉体を中粉と微粉に分級するものである。
【0004】
一般に、気流分級は、回転する分級羽根に空気流とともに粉体を送り込み、その分級羽根で粉体を跳ね飛ばして分級するものであり、質量が高い粉体程、分級効率(精度)は高い。このため、例えば、粗粉、中粉、微粉とに分級する場合、後者側になるほど、分級精度は低くなる。また、粉体と空気流の割合(固気比)は、粉体量が少ない程、分級羽根によって跳ね飛ばされ易いため、分級精度は高い。すなわち、固気比は小さい程、分級精度は高くなる。
【0005】
このことから、上記2台の分級機を使用する方法は、分級精度が良く、しかも分級点の変更が容易であるが、2台用いるので設置スペースが大きくなると言う問題がある。このため、1台の分級機に複数の分級ロータを設け、粉体を、3種類に分級することが提案されている。
【0006】
例えば、図6に示すように、2分割可能なケーシング23、24内に、分級ロータ25、26を上下に設けて、粉体入口27よりケーシング内に粉体aを導入すると、この粉体aの内、微粉a3 は上の分級ロータ25内を通過し、中粉a2 は下の分級ロータ26内を通過し、両分級ロータ25、26内を通過しなかった粗粉a1 は、ケーシング24の下方の出口短管28から排出させている(特許文献1参照)。
【0007】
【特許文献】
特開2001−293438号公報
【0008】
【発明が解決しようとする課題】
しかしながら、上記従来技術は、最初に、固気比が高く、分級精度が悪い、上段の分級室(分級ロータ25)で、一番細かな(軽い)微粉a3 を除去するため、分級精度が悪いものとなっている。また、上段の分級ロータ25により微粉a3 が除かれた粉体は、下段の分級ロータ26によりさらに分級されるが、上下段の分級ロータ25、26の外側は連通しており、その粉体濃度や粒度分布は、両分級ロータ25、26に互いに影響する。このため、微粉a3 を上段の分級ロータ25で、中粉を下段の分級ロータ26で、確実に分離することができず、分級精度が悪い。
【0009】
この発明は、一のケーシング内で、粗粉、中粉、微粉というように、粗い粉体から細かい粉体に順々に分級し得るようにすることを課題とする。
【0010】
【課題を解決するための手段】
上記課題を達成するために、この発明は、ケーシング内に、複数の分級ロータを設け、その各分級ロータに順々に粉体原料を通過させ、その通過する順の分級ロータにより、粗い粉体から細かい粉体に順々に分級するようにしたのである。
【0011】
具体的には、両端閉塞の円筒状ケーシング内に、複数の分級ロータをその回転軸心が前記ケーシングの筒軸上として順々に設け、各分級ロータ間は仕切壁により仕切って前記ケーシング内に複数の分級室を形成し、前記ケーシングの一端に原料投入口、他端に吸気口をそれぞれ設けるとともに、各分級ロータに臨むケーシング側面には粉体排出口を設け、前記仕切壁には、前記原料投入口側の前段の分級室内の分級ロータ内と次段の分級室を連通する孔を形成し、前記原料投入口から原料をケーシング内に送り込むとともに、前記吸気口から吸気して、原料投入口、分級室、分級ロータ内、次段の分級室、分級ロータ内・・・吸気口という空気流れを形成して、その空気流れに沿って、各分級ロータにより順々に細かい粉体を分級するようにしたのである。
【0012】
その分級度調整は、分級ロータの回転数の制御で行ない、その各分級ロータを個別の駆動機で回転させたり、変速機を介して一つの駆動機で回転させて、その回転数を制御する。
【0013】
各分級室には、従来と同様に、分級用2次空気を送り込むことが好ましく、例えば、上記分級ロータ周りのケーシング壁全周に分級用2次空気室を形成し、その2次空気室と分級ロータとを、2次空気室の周壁全周に等間隔に設けた孔で連通し、この各孔から分級ロータに向って2次空気を送り込むようにする。
【0014】
また、上記仕切壁の前後の分級室を連通する孔周囲から前段の分級ロータの外側に向けて2次空気を噴出するようにすることもできる(実施形態の噴出口10a、環状スリット16参照)。このようにすれば、その噴出空気が前後の分級室間のエアーカーテンや粉体の粗細ゾーン分離の役目を果して、シール効果を発揮する。
【0015】
さらに、分級ロータにそのロータと共回りする分散羽根を設けて、分級前の粉体を分散するようにすれば、分級効果が増す。このとき、分級ロータが、対の平行に隔てた円板間に、その周りに放射状に分級羽根を設けたものであれば、その円板の表面に前記分散羽根を設ける。
【0016】
上記構成の分級機にあっては、分級ロータが複数あるため、最低3段階の分級を行うことができ、その3段階(粗粉、中粉、微粉)の場合には、上記分級室は2室となり、前段の分級室で粗粉を分級し、後段の分級室で中粉を分級し、吸気口から吸気とともに微粉を取出すこととなる。
【0017】
【実施の形態】
図1及び図2に一実施形態を示し、その図において、1はケーシングで、環状の仕切板2a、2bにより、上部分級室1a、下部分級室1b並びに微粉排出室1cに区分されている。ケーシング1内には2個の分級ロータ3a、3bが上下に設けられ、それぞれがケーシング1外に設けられたモータ4a、4bにより回転する。また、上部分級室1aには、粉体供給口12が設けられている。両ロータ3の回転方向は逆方向でも良いが、同一方向が望ましい。
【0018】
各分級ロータ3a、3bは、平行に隔てられた天板5と底板6及び両者に挟まれた周方向放射状の複数の分級羽根7を備えており、回転軸8によりモータ4a、4bに連結されている。また、底板6には、粉体を通過させる貫通孔20が形成されており、その外縁部が前記仕切板2の貫通孔21内縁部に近接して回転する。
【0019】
仕切板2a、2bにはシールエアー用の環状路10が形成されており、この環状路10を介しその周囲等間隔に設けた複数の噴出口10aを通じて空気bを噴出し、仕切板2a、2bと底板6との隙間からの粉体の侵入を防止している。一般に、粗粉a1 は分級羽根7で跳ね飛ばされるので、孔20、21を介して下部の分級室1bへ移動しないが、仕切板2a、2bと底板6との隙間からショートパスして侵入する恐れがある。しかし、この噴出口10aからの空気bの噴出によりそのショートパスが防止される。
【0020】
両分級室1a、1b内には環状仕切壁9が設けられ、この仕切壁9とケーシング1内面とで形成される環状空間を2次空気導入室11a、11bとしている。この2次空気導入室11a、11bに空気導入口15及び粉体出口管13a、13bが設けられ、微粉排出室1cには微粉出口管13cが設けられている。環状仕切壁9の分級羽根7と対峙する位置には複数の縦スリット(孔)14が周囲等間隔に形成され、このスリット14から2次空気bが分級室1a、1b全周に均一に導入される。このため、導入空気bはスリット14から分級ロータ3a、3bに対して均等に噴出する。これにより、分級ロータ3a、3bの周囲の気流の乱れが少なく、分級精度がよい。
【0021】
つぎに、作用について説明すると、微粉出口管13cに接続された排風機Fを起動し、粉体供給口12より空気とともに粉体aを導入する。その粉体aの内、粗粉a1 は、上部分級室1aにおいて、高速で回転する分級羽根7aに跳ね飛ばされ、仕切壁9の内側を回転し、仕切壁9に形成された大きな開口17及び筒状導出路17aを通って、粗粉出口管13aから排出される。
【0022】
上部分級室1aの分級羽根7aを通過した中粉a2 と微粉a3 は、分級ロータ3aの底板6の孔20及び仕切板2aの孔21を通って、下部分級室1bへ移送される。その下部分級室1bにおいて、中粉a2 は、分級羽根7bに跳ね飛ばされて開口17、導出路17aを通って中粉出口管13bから排出される。分級羽根7bを通過した微粉a3 は、微粉排出室1cに入り、空気とともに、微粉出口管13cから排出され、捕集機30で捕捉される。
【0023】
この分級においては、粗粉a1 を最初に分離したので、下部分級室1bの固気比が下がり、微粉a3 の分級精度がよい。また、下部分級室1bに粗粉a1 がないので、粉体a2 が分散しやすく分級精度が向上する。さらに、粗粉a1 、中粉a2 が分散されて、分級されることより、この粗粉a1 等に基づく、気流式分級機の摩耗が軽減される。また、仕切板2aにより分級室1a、1bを仕切ったので、各分級室1a、1bの粉体濃度を調整しやすい。また、上下の分級室1a、1bが直接つながっていないため、粗粉a1 が下部分級室7bに混入する恐れはない。
【0024】
図3乃至図5に他の実施形態を示し、この実施形態は、まず、分級ロータの底板6の外縁と、仕切板2a、2bの内縁との隙間(環状スリット16)から2次空気bを噴出するものである。この2次空気bは、シール空気としても作用する。一般に、分級室では、分級ロータ周辺の空気流速が大きく、ケーシング1の仕切壁9に近づくほど流速が低下する。すなわち、分級ロータ3周辺では細かい粉体が多く、分級ロータ3から離れた仕切壁9周辺では粗い粉体が多い。このため、両者の中間の環状スリット16から2次空気を導入すれば、細かな粉体ゾーンと粗い粉体のゾーンとに分かれやすくなり、分級ロータ内に入る粉体は細かな粉体だけとなりやすい。このとき、図5に示すように、環状スリット16の位置L2は、L1の約半分(40〜60%)程度が望ましく、中央位置に近づけば、細かな粉体のゾーンと粗い粉体のゾーンとにより分かれやすくなる。
【0025】
さらに、分級ロータに分散羽根18を設けており、対向する分散羽根18にあっては、上下の分散ロータ3a、3bの相対速度効果により、微粉a3 の凝集を防止する。このとき、分級室1a、1bへの2次空気bの導入は主として環状スリット16より行ない、縦スリット14からは補助的に行う。なお、縦スリット14からの2次空気bの導入は行なわなくてもよい。
【0026】
各実施形態は、分級ロータ3a、3bが2段のものであったが、3段以上のものでも、この発明を採用し得ることは勿論である。
【0027】
【発明の効果】
この発明は、以上のようにして、一のケーシング内で粗い粉体から細かい粉体に順々に分級するようにしたので、分級精度の高いものとなる。
【図面の簡単な説明】
【図1】一実施形態の概略断面図
【図2】同切断平面図
【図3】他の実施形態の概略断面図
【図4】同実施形態の切断平面図
【図5】同要部拡大切断正面図
【図6】従来例の概略断面図
【符号の説明】
1 ケーシング
1a 上部分級室
1b 下部分級室
1c 微粉排出室
2a、2b 仕切板
3a、3b 分級ロータ
4a、4b モータ
5 天板
6 底板
7、7a、7b 分級羽根
8 回転軸
9 仕切壁
10 環状路
11a、11b 2次空気導入室
12 粉体供給口
13a 粗粉出口管
13b 中粉出口管
13c 微粉出口管
14 スリット(孔)
15 二次空気導入口
16 環状スリット
18 分散羽根
20、21 貫通孔
a 原料
1 粗紛
2 中粉
3 微粉
b 空気
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an airflow classifier that classifies powder into a plurality of classified products, in particular, a powder having an average particle size of about 4 to 10 μm into three classified products by air flow.
[0002]
[Prior art]
When powders such as glass, silicon carbide, and color toner are classified into various industrial raw materials using an airflow classifier, they must have a particle size within the required range excluding fine powder as well as so-called coarse powder. Is done. For example, silicon carbide or silicon nitride is mixed with resin and used as an abrasive. However, if fine powder is mixed, the polishing performance is lowered, and the toner is melted by heat and adheres to paper, but the fine powder is mixed. If it is, the fine powder will melt first, and the letters will become unclear.
[0003]
For this reason, those powders are classified into medium powder having a particle size within the above-mentioned required range, coarse powder having a larger diameter, and fine powder having a smaller diameter than that, and the medium powder is used as a product. As the classification method, the simplest method is to arrange two airflow classifiers in series and classify the powder into coarse powder and other powders with the first classifier, and then classify the next classifier. The other powder is classified into medium powder and fine powder.
[0004]
In general, airflow classification is a method in which powder is sent together with an air stream to a rotating classification blade, and the powder is spun off by the classification blade, and the classification efficiency (accuracy) is higher as the powder has a higher mass. For this reason, for example, when classifying into coarse powder, medium powder, and fine powder, the classification accuracy decreases as the latter side is reached. Moreover, since the ratio (solid-gas ratio) between the powder and the air flow is more likely to be splashed off by the classification blade as the amount of the powder is smaller, the classification accuracy is higher. That is, the smaller the solid-gas ratio, the higher the classification accuracy.
[0005]
For this reason, the method using the above two classifiers has good classification accuracy and can easily change the classification point, but there is a problem that the installation space becomes large because two classifiers are used. For this reason, it has been proposed to provide a plurality of classification rotors in one classifier and classify the powder into three types.
[0006]
For example, as shown in FIG. 6, when classifying rotors 25 and 26 are provided vertically in casings 23 and 24 that can be divided into two parts, and powder a is introduced into the casing from powder inlet 27, this powder a Among these, the fine powder a 3 passes through the upper classification rotor 25, the medium powder a 2 passes through the lower classification rotor 26, and the coarse powder a 1 that does not pass through both the classification rotors 25, 26 is The gas is discharged from the outlet short pipe 28 below the casing 24 (see Patent Document 1).
[0007]
[Patent Literature]
Japanese Patent Laid-Open No. 2001-293438
[Problems to be solved by the invention]
However, the above prior art first removes the finest (lighter) fine powder a 3 in the upper classification chamber (classification rotor 25), which has a high solid-gas ratio and poor classification accuracy. It is bad. The powder from which the fine powder a 3 has been removed by the upper classification rotor 25 is further classified by the lower classification rotor 26, but the outer sides of the upper and lower classification rotors 25, 26 are in communication with each other. The concentration and the particle size distribution affect each of the classification rotors 25 and 26. For this reason, the fine powder a 3 cannot be reliably separated by the upper classification rotor 25 and the middle powder by the lower classification rotor 26, and the classification accuracy is poor.
[0009]
This invention makes it a subject to be able to classify from coarse powder to fine powder in order, such as coarse powder, medium powder, and fine powder, in one casing.
[0010]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, the present invention provides a plurality of classification rotors in a casing, allows powder raw materials to pass through each of the classification rotors one after another, and the coarse powders are obtained by the classification rotors in the passing order. In order to classify from fine powder to fine powder.
[0011]
Specifically, a plurality of classifying rotors are provided in order in a cylindrical casing closed at both ends, with the rotational axis centered on the cylindrical axis of the casing, and each classifying rotor is partitioned by a partition wall in the casing. A plurality of classification chambers are formed, a raw material input port is provided at one end of the casing, an intake port is provided at the other end, a powder discharge port is provided on the side of the casing facing each classification rotor, and the partition wall Forms a hole that connects the classification rotor in the previous classification chamber on the raw material input side to the classification chamber in the next stage, and feeds the raw material into the casing from the raw material input port, and sucks in the air from the intake port to input the raw material. Mouth, classification chamber, classification rotor, next-stage classification chamber, classification rotor, air flow is formed as an intake port, and fine powder is classified in order by each classification rotor along the air flow. Like Than it was.
[0012]
The classification degree adjustment is performed by controlling the rotation speed of the classification rotor, and each classification rotor is rotated by an individual driving machine or rotated by one driving machine via a transmission to control the rotation speed. .
[0013]
As in the past, it is preferable to send secondary air for classification into each classification chamber. For example, a secondary air chamber for classification is formed around the entire casing wall around the classification rotor. The classification rotor communicates with the entire circumference of the peripheral wall of the secondary air chamber through holes provided at equal intervals, and secondary air is sent from each hole toward the classification rotor.
[0014]
Further, secondary air can be ejected from the periphery of the hole communicating with the classification chambers before and after the partition wall toward the outside of the previous classification rotor (see the ejection port 10a and the annular slit 16 in the embodiment). . In this way, the blown air plays the role of separating the air curtain between the front and rear classification chambers and the coarse and fine zones of the powder, and exhibits a sealing effect.
[0015]
Furthermore, if the classifying rotor is provided with dispersing blades that rotate together with the rotor to disperse the powder before classification, the classification effect is increased. At this time, if the classifying rotor is such that classifying blades are provided radially between a pair of parallelly spaced discs, the dispersing blades are provided on the surface of the disc.
[0016]
In the classifier having the above-described configuration, since there are a plurality of classifying rotors, classification can be performed at least in three stages. In the case of the three stages (coarse powder, medium powder, fine powder), the classification chamber has 2 The coarse powder is classified in the preceding classification chamber, the medium powder is classified in the subsequent classification chamber, and the fine powder is taken out together with the intake air from the intake port.
[0017]
Embodiment
1 and 2 show an embodiment, in which 1 is a casing, which is divided into an upper partial chamber 1a, a lower partial chamber 1b, and a fine powder discharge chamber 1c by annular partition plates 2a and 2b. Yes. In the casing 1, two classification rotors 3a and 3b are provided up and down, and each is rotated by motors 4a and 4b provided outside the casing 1. In addition, a powder supply port 12 is provided in the upper partial chamber 1a. The rotational directions of both rotors 3 may be opposite, but the same direction is desirable.
[0018]
Each of the classification rotors 3a and 3b includes a top plate 5 and a bottom plate 6 which are separated in parallel, and a plurality of circumferential radial blades 7 sandwiched therebetween, and are connected to the motors 4a and 4b by a rotating shaft 8. ing. Further, the bottom plate 6 is formed with a through-hole 20 through which powder passes, and the outer edge portion thereof rotates close to the inner edge portion of the through-hole 21 of the partition plate 2.
[0019]
An annular passage 10 for sealing air is formed in the partition plates 2a and 2b, and air b is ejected through the annular passage 10 through a plurality of jet outlets 10a provided at equal intervals around the annular passage 10 and the partition plates 2a and 2b. Intrusion of powder from the gap between the base plate 6 and the bottom plate 6 is prevented. In general, since the coarse powder a 1 is splashed by the classification blade 7, it does not move to the lower classification chamber 1 b through the holes 20 and 21, but enters through a short path from the gap between the partition plates 2 a and 2 b and the bottom plate 6. There is a fear. However, the short path is prevented by the ejection of the air b from the ejection port 10a.
[0020]
An annular partition wall 9 is provided in both the classification chambers 1a and 1b, and an annular space formed by the partition wall 9 and the inner surface of the casing 1 is used as secondary air introduction chambers 11a and 11b. The secondary air introduction chambers 11a and 11b are provided with an air inlet 15 and powder outlet pipes 13a and 13b, and the fine powder discharge chamber 1c is provided with a fine powder outlet pipe 13c. A plurality of vertical slits (holes) 14 are formed at equal intervals around the annular partition wall 9 at the position facing the classifying blades 7, and the secondary air b is uniformly introduced into the entire circumference of the classifying chambers 1a and 1b from the slits 14. Is done. For this reason, the introduction air b is uniformly ejected from the slit 14 to the classification rotors 3a and 3b. Thereby, there is little disturbance of the air current around the classification rotors 3a and 3b, and the classification accuracy is good.
[0021]
Next, the operation will be described. The air exhaust device F connected to the fine powder outlet pipe 13c is started, and the powder a is introduced together with air from the powder supply port 12. Of the powder a, the coarse powder a 1 is splashed by the classification blade 7a that rotates at a high speed in the upper partial chamber 1a, rotates inside the partition wall 9, and has a large opening formed in the partition wall 9. 17 and the cylindrical lead-out path 17a are discharged from the coarse powder outlet pipe 13a.
[0022]
The intermediate powder a 2 and fine powder a 3 that have passed through the classification blade 7a of the upper partial chamber 1a are transferred to the lower partial chamber 1b through the hole 20 of the bottom plate 6 and the hole 21 of the partition plate 2a of the classification rotor 3a. The In its lower part classifying chamber 1b, the medium powder a 2, which classifying blades 7b bouncing skipped in the opening 17, is discharged from the intermediate powder outlet tube 13b through the outlet passage 17a. The fine powder a 3 that has passed through the classification blade 7 b enters the fine powder discharge chamber 1 c, is discharged from the fine powder outlet pipe 13 c together with air, and is captured by the collector 30.
[0023]
In this classification, since the coarse powder a 1 is first separated, the solid-gas ratio in the lower partial classification chamber 1b is lowered, and the classification accuracy of the fine powder a 3 is good. Further, since there is no coarse a 1 on the lower portion classifying chamber 1b, the powder a 2 is improved dispersibility easily classified accuracy. Further, since the coarse powder a 1 and the medium powder a 2 are dispersed and classified, wear of the airflow classifier based on the coarse powder a 1 and the like is reduced. Moreover, since the classification chambers 1a and 1b are partitioned by the partition plate 2a, it is easy to adjust the powder concentration in each of the classification chambers 1a and 1b. Further, since the upper and lower classification chambers 1a and 1b are not directly connected, there is no possibility that the coarse powder a 1 is mixed into the lower partial classification chamber 7b.
[0024]
3 to 5 show another embodiment. In this embodiment, first, the secondary air b is drawn from the gap (annular slit 16) between the outer edge of the bottom plate 6 of the classification rotor and the inner edges of the partition plates 2a and 2b. It is a eruption. This secondary air b also acts as sealing air. In general, in the classification chamber, the air flow velocity around the classification rotor is large, and the flow velocity decreases as it approaches the partition wall 9 of the casing 1. That is, there are many fine powders around the classification rotor 3, and there are many coarse powders around the partition wall 9 away from the classification rotor 3. For this reason, if secondary air is introduced from the annular slit 16 between the two, it becomes easy to separate into a fine powder zone and a coarse powder zone, and only fine powder enters the classification rotor. Cheap. At this time, as shown in FIG. 5, the position L2 of the annular slit 16 is desirably about half (40 to 60%) of L1, and if close to the center position, a fine powder zone and a coarse powder zone It becomes easier to separate.
[0025]
Furthermore, it has established a dispersion blade 18 in the classifying rotor, in the opposite dispersion blade 18, the upper and lower dispersion rotor 3a, the relative velocity effect of 3b, to prevent aggregation of fine powder a 3. At this time, the secondary air b is introduced into the classification chambers 1a and 1b mainly through the annular slit 16 and supplementarily through the vertical slit 14. It is not necessary to introduce the secondary air b from the vertical slit 14.
[0026]
In each embodiment, the classifying rotors 3a and 3b have two stages, but it is needless to say that the present invention can be adopted even with three or more stages.
[0027]
【The invention's effect】
According to the present invention, as described above, classification is performed in order from coarse powder to fine powder in one casing, so that the classification accuracy is high.
[Brief description of the drawings]
FIG. 1 is a schematic cross-sectional view of one embodiment. FIG. 2 is a plan view of the same. FIG. 3 is a schematic cross-sectional view of another embodiment. Cut front view [Fig. 6] Schematic sectional view of conventional example [Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Casing 1a Upper partial chamber 1b Lower partial chamber 1c Fine powder discharge chamber 2a, 2b Partition plate 3a, 3b Classification rotor 4a, 4b Motor 5 Top plate 6 Bottom plate 7, 7a, 7b Classification blade 8 Rotating shaft 9 Partition wall 10 Ring Paths 11a, 11b Secondary air introduction chamber 12 Powder supply port 13a Coarse powder outlet pipe 13b Medium powder outlet pipe 13c Fine powder outlet pipe 14 Slit (hole)
15 Secondary air inlet 16 Annular slit 18 Dispersion blade 20, 21 Through hole a Raw material a 1 Coarse powder a 2 Medium powder a 3 Fine powder b Air

Claims (6)

両端閉塞で筒軸が上下方向の円筒状ケーシング(1)内に、複数の分級ロータ(3a、3b)をその回転軸心が前記ケーシング(1)の筒軸上になるように上下方向に順々に設け、各分級ロータ間は仕切壁(2)により仕切って前記ケーシング(1)内に複数の分級室(1a、1b)を形成し、前記ケーシング(1)の一端に、前記最上段の分級室(1a)に連通する原料投入口(12)、他端に最下段の分級室に連通する吸気口(13c)をそれぞれ設けるとともに、分級ロータ(3a、3b)に臨むケーシング(1)側面には粉体排出口(13a、13b)をそれぞれ設け、前記仕切壁(2)には、前記原料投入口(12)側の前段の分級室(1a)内の分級ロータ(3a)内と次段の分級室(1b)を連通する孔(20、21)を形成し、前記原料投入口(12)から原料(a)をケーシング(1)内に送り込むとともに、前記吸気口(13c)から吸気して、原料投入口(12)、分級室(1a)、分級ロータ(3a)内、次段の分級室(1b)・・・最後に吸気口(13c)という空気流れを形成して、その空気流れに沿って、粗い粉体から細かい粉体の順でこれらを取出して分級する気流式分級機。A plurality of classifying rotors (3a, 3b) are arranged in the vertical direction so that the rotation axis is on the cylindrical axis of the casing (1) in the cylindrical casing (1) with both ends closed and the cylindrical axis in the vertical direction. Each classification rotor is partitioned by a partition wall (2) to form a plurality of classification chambers (1a, 1b) in the casing (1), and one end of the casing (1) A raw material input port (12) communicating with the classification chamber (1a), an intake port (13c) communicating with the lowermost classification chamber at the other end, and a casing (1) facing each classification rotor (3a, 3b) Powder discharge ports (13a, 13b) are provided on the side surfaces, respectively , and the partition wall (2) includes an inside of a classification rotor (3a) in a previous classification chamber (1a) on the raw material input port (12) side. Form holes (20, 21) that communicate with the next-stage classification chamber (1b) Then, the raw material (a) is fed into the casing (1) from the raw material inlet (12), and sucked from the inlet (13c), and then the raw material inlet (12), the classification chamber (1a), the classification rotor (3a) In the next classification chamber (1b) ... Finally, an air flow called an inlet (13c) is formed, and these are arranged in the order of coarse powder to fine powder along the air flow. Airflow classifier that takes out and classifies. 上記分級ロータ(3a、3b)周りに環状仕切壁(9)を設け、この環状仕切壁(9)と上記ケーシング(1)の内面とで形成される環状空間により分級用2次空気室を形成し、その2次空気室と分級ロータとを、前記環状仕切壁(9)全周に等間隔に設けた孔(14)で連通し、この各孔(14)から分級ロータに向って2次空気を送り込むようにしたことを特徴とする請求項1に記載の気流式分級機。  An annular partition wall (9) is provided around the classification rotor (3a, 3b), and a secondary air chamber for classification is formed by an annular space formed by the annular partition wall (9) and the inner surface of the casing (1). The secondary air chamber and the classification rotor communicate with each other through holes (14) provided at equal intervals on the entire circumference of the annular partition wall (9), and the secondary air chambers are directed from the holes (14) toward the classification rotor. 2. The airflow classifier according to claim 1, wherein air is fed. 前段の分級室(1a)内の分級ロータ(3a)内と次段の分級室(1b)を連通する孔(20、21)の周囲から前段の分級ロータ(3a)の外側に向けて2次空気を噴出するようにしたことを特徴とする請求項1又は2に記載の気流式分級機。Secondary from the circumference of the holes (20 , 21 ) communicating the classification rotor (3a) in the previous classification chamber (1a) and the classification chamber (1b) in the next stage toward the outside of the classification rotor (3a) in the previous stage The airflow classifier according to claim 1 or 2, wherein air is jetted out. 分級ロータの外面にそのロータと共回りする分散羽根(18)を設け、この分散羽根(18)により、前記分級ロータ内に入る粉体を分散するようにしたことを特徴とする請求項1乃至3のいずれかに記載の気流式分級機。  Dispersion blades (18) co-rotating with the rotor are provided on the outer surface of the classification rotor, and the powder entering the classification rotor is dispersed by the dispersion blades (18). 4. The airflow classifier according to any one of 3. 上記分級ロータは、対の平行に隔てた円板(5、6)の間において放射状に延びる分級羽根(7)を有するものであり、その円板(5、6)の外側表面に上記分散羽根(18)を設けたことを特徴とする請求項4に記載の気流式分級機。  The classifying rotor has classifying blades (7) extending radially between a pair of parallelly separated discs (5, 6), and the dispersing blades are arranged on the outer surface of the discs (5, 6). The airflow classifier according to claim 4, further comprising (18). 上記分級室を2室(1a、1b)とし、前段の分級室(1a)の粉体排出口(13a)から粗粉(a)を取出し、後段の分級室(1b)の粉体排出口(13b)から中粉(a)を取出し、吸気口(13c)から吸気とともに微粉(a)を取出すようにしたことを特徴とする請求項1乃至5のいずれかに記載の気流式分級機。The classification chambers are two chambers (1a, 1b), the coarse powder (a 1 ) is taken out from the powder discharge port (13a) of the previous classification chamber (1a), and the powder discharge port of the subsequent classification chamber (1b). The airflow type classification according to any one of claims 1 to 5, wherein medium powder (a 2 ) is taken out from (13b), and fine powder (a 3 ) is taken out together with intake air from an air inlet (13c). Machine.
JP2002286489A 2002-09-30 2002-09-30 Airflow classifier Expired - Fee Related JP3733349B2 (en)

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