JPH07265802A - Powder classifier and its operation - Google Patents

Powder classifier and its operation

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Publication number
JPH07265802A
JPH07265802A JP6313394A JP6313394A JPH07265802A JP H07265802 A JPH07265802 A JP H07265802A JP 6313394 A JP6313394 A JP 6313394A JP 6313394 A JP6313394 A JP 6313394A JP H07265802 A JPH07265802 A JP H07265802A
Authority
JP
Japan
Prior art keywords
powder
air
classification
amount
rotor
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.)
Granted
Application number
JP6313394A
Other languages
Japanese (ja)
Other versions
JP3485624B2 (en
Inventor
Shoji Yamada
昌治 山田
Hiroshi Hatano
拓 波田野
Satoshi Akiyama
聡 秋山
Takahiro Ichikawa
孝博 市川
Yukiyoshi Yamada
幸良 山田
Toru Hikosaka
徹 彦坂
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.)
Nisshin Engineering Co Ltd
Nisshin Seifun Group Inc
Original Assignee
Nisshin Engineering Co Ltd
Nisshin Seifun Group Inc
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 Nisshin Engineering Co Ltd, Nisshin Seifun Group Inc filed Critical Nisshin Engineering Co Ltd
Priority to JP06313394A priority Critical patent/JP3485624B2/en
Publication of JPH07265802A publication Critical patent/JPH07265802A/en
Application granted granted Critical
Publication of JP3485624B2 publication Critical patent/JP3485624B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To provide a powder classifier capable of efficiently and precisely classifying powders even when the classification point is changed. CONSTITUTION:A casing 1 is provided with a powder inlet 3 at the center of the upper face and an air inlet 10 on the outer side wall periphery, and a classification rotor 4 having an air circulating cavity extending from the circumference toward the axial center is provided and made rotatable by a vertical rotating shaft 8. Further, a throttling plate 9 is detachably fixed in the powder inlet to adjust the amt. of air from the powder inlet. Consequently, the ratio of the amt. of air from the powder inlet to that from the air inlet is appropriately set, and classification is performed under optimum conditions.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は空気流を利用した粉体分
級機および空気量を調整する粉体分級機の運転法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a powder classifier using an air flow and a method of operating a powder classifier for adjusting the amount of air.

【0002】[0002]

【従来の技術】粉体分級機は、様々な粒径を含む粉粒体
から所定の粒径で粉体を選り分けるのに用いるもので、
多くの分級方法が知られているが、その内の一つに、分
級ロータを用いた粉体分級機がある。この分級ロータを
用いた粉体分級機は、分級羽根を有する分級ロータをケ
ーシング内で高速で回転させ、分級ロータの上部から投
入した粉体に分級ロータの回転によって遠心力を生じさ
せるとともに分級ロータの周縁から中心に向って空気を
導入させ、分級ロータによる遠心力を大きく受ける粒径
の大きな粉体は分級ロータの外方に流出し、一方遠心力
より空気流による作用を大きく受ける粒径の小さな粉体
は空気とともに中心方向に移動させて粉体を分級するも
のである。
2. Description of the Related Art A powder classifier is used for selecting powders having a predetermined particle size from powder particles having various particle sizes.
Many classification methods are known, and one of them is a powder classifier using a classification rotor. A powder classifier using this classifying rotor rotates a classifying rotor having classifying blades at high speed in a casing to generate centrifugal force by rotating the classifying rotor on the powder charged from the upper part of the classifying rotor and at the same time, classifying rotor. Air is introduced from the periphery of the class toward the center, and powder with a large particle size that is largely subjected to centrifugal force by the classification rotor flows out of the classification rotor, while particle size that is greatly affected by the air flow due to centrifugal force The small powder is moved along with air toward the center to classify the powder.

【0003】[0003]

【発明が解決しようとする課題】この型式の粉体分級機
では、分級に用いる空気は空気導入口を経由して分級円
板の外周より流入するようになっているが、実際は他の
部分すなわち被分級粉体の投入開口部からも入ってきて
おり、粉体とともに分級円板に流入する。この二つの空
気量の合計が分級作用のための空気ということになる。
一般に空気分級機では、外周より流入する空気量のみで
分級作用をさせた方がよいように思われるが、種々の経
験から、この形式の分級機では粉体投入口からの空気量
もある程度必要であり、2つの空気量の比率を適当に選
ぶことにより、分級効率が高くなることがわかった。
In this type of powder classifier, the air used for classification flows from the outer circumference of the classifying disk through the air inlet, but in reality, other parts, namely, The powder to be classified also enters from the charging opening and flows into the classification disk together with the powder. The sum of these two amounts of air is the air for classification.
Generally, in an air classifier, it seems that it is better to perform the classification action only with the amount of air flowing in from the outer periphery, but from various experiences, this type of classifier also requires some amount of air from the powder inlet. Therefore, it was found that the classification efficiency is increased by appropriately selecting the ratio of the two air amounts.

【0004】また一方では、この形式の分級機でも、粉
体に作用する遠心力と空気流との均衡によって粉体を分
級するため、分級の仕様例えば時間当たりの処理量や分
級点等は設計の段階からある程度定められてしまい、使
用者が必要に応じて回転数等を変更して分級点を変更で
きるものの、このようにして分級点を変更した場合に
は、分級ロータによる遠心力と空気流の抗力との均衡が
変化してしまい、効率や分級精度の低下が生ずることが
ある。
On the other hand, even in this type of classifier, since the powder is classified by the balance between the centrifugal force acting on the powder and the air flow, the specifications of classification, such as the throughput per unit time and the classification point, are designed. However, if the user changes the number of rotations, etc., the classification point can be changed, but if the classification point is changed in this way, the centrifugal force and air from the classification rotor The equilibrium with the drag force of the flow may change, resulting in a decrease in efficiency and classification accuracy.

【0005】本発明は上記の点に鑑みてなされたもの
で、このような場合でも精度を低下させずに分級点を変
更できる粉体分級機を提供するばかりでなく、分級機の
分級精度も向上させる運転法を提供することにある。
The present invention has been made in view of the above points, and not only provides a powder classifier that can change the classification point without lowering the accuracy even in such a case, but also has a classification accuracy of the classifier. It is to provide an improved driving method.

【0006】[0006]

【課題を解決するための手段】本発明は上記の目的を達
成するために、ケーシングの上面中央に形成した粉体投
入口からの空気流入量と、ケーシングの側方に形成した
空気導入口からの空気導入量との比率を好ましい比率に
調整する運転法である。その比率の調整のためには、粉
体投入口に空気量調整装置を取り付けたり、又絞り板も
しくは調整弁を取り付けることにより行なう。
In order to achieve the above object, the present invention uses an air inflow amount from a powder charging port formed at the center of the upper surface of a casing and an air introducing port formed at the side of the casing. The operating method is to adjust the ratio with the amount of air introduced into the device to a preferable ratio. To adjust the ratio, an air amount adjusting device, a diaphragm plate or an adjusting valve is attached to the powder charging port.

【0007】空気導入口からの空気量Q2 と粉体投入口
から入ってくる空気量Q1 との比率Q1/Q2 を0.02
〜0.14に保つことにより最も分級効率が高くなる。
この種の分級機においては機内に導入された粉体が同時
に導入される空気により分散作用を受け、より単粒子に
近くなるため、Q1 がある程度必要であり、極端に少な
くなると分散作用ができなくなる。一方、Q1 は余り大
きくなると本来の空気導入口より入ってくる空気流との
合流による乱れが大きくなり、分級場の空気流が乱され
設計通りの力が粒子に及ばず、結果として分級精度が低
下する。
The ratio Q 1 / Q 2 between the air amount Q 2 from the air inlet and the air amount Q 1 coming from the powder inlet is 0.02.
The classification efficiency becomes highest by keeping it at 0.14.
In this type of classifier, the powder introduced into the machine is subjected to a dispersing action by the air introduced at the same time and becomes closer to a single particle, so that Q 1 is required to some extent, and when it is extremely small, the dispersing action can occur. Disappear. On the other hand, if Q 1 becomes too large, the turbulence due to the merging with the airflow that comes in from the original air inlet will increase, and the airflow in the classification field will be disturbed and the force as designed will not reach the particles, resulting in classification accuracy. Is reduced.

【0008】このような比率を実現するために、前述の
ように粉体の投入口へ絞り板を取り付けたり、調整弁を
付けてもよいが、設計時において粉体投入口からの空気
量と空気導入口からの空気量との関係を上述の範囲に納
めておいてもよい。
In order to achieve such a ratio, a diaphragm plate or a regulating valve may be attached to the powder inlet as described above. The relationship with the amount of air from the air inlet may be set within the above range.

【0009】[0009]

【作用】粉体分級機の粉体投入口からの空気量と空気導
入口からの空気量の比率を適当に選ぶことにより分級精
度が向上する。分級ロータの回転数等を変更して分級点
を変更すると、分級ロータによる遠心力と空気導入口か
らの空気の抗力との関係が変化してしまい、設計仕様通
りの分級精度が得られなくなることがあるが、このよう
な場合にも粉体投入口からケーシング内に流入する空気
量と空気導入口からの空気導入量との比率を適宜に設定
することによって分級精度を低下させず高い効率で分級
ができる。
[Function] The classification accuracy is improved by appropriately selecting the ratio of the amount of air from the powder inlet to the amount of air from the air inlet of the powder classifier. If the classification point is changed by changing the rotation speed of the classification rotor, etc., the relationship between the centrifugal force of the classification rotor and the drag force of the air from the air inlet will change, and the classification accuracy as designed will not be obtained. However, even in such a case, by appropriately setting the ratio of the amount of air flowing into the casing from the powder inlet and the amount of air introduced from the air inlet, it is possible to achieve high efficiency without lowering the classification accuracy. Can classify.

【0010】[0010]

【実施例】本発明の粉体分級機及びその運転法の一実施
例を図面に基づいて説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the powder classifier and its operating method of the present invention will be described with reference to the drawings.

【0011】図1は、本発明による粉体分級機の一実施
例を示す縦断面図である。粉体分級機1は、全体を覆う
ケーシング2と、ケーシング2内に設けられた分級ロー
タ4、バランスロータ6及びこれらを回転させる回転軸
8等から構成されている。
FIG. 1 is a vertical sectional view showing an embodiment of a powder classifier according to the present invention. The powder classifier 1 includes a casing 2 that covers the entire body, a classifying rotor 4 provided in the casing 2, a balance rotor 6, a rotating shaft 8 that rotates these, and the like.

【0012】ケーシング2は、全体が円形で、上面中心
部に粉体供給装置(図示せず)と連結される粉体投入口
3を有し、周側部に空気導入口10、粗粉取出口12及
び渦巻ケーシング14を備えている。粉体投入口3に
は、粉体投入管5が連結してあり、この粉体投入管5か
ら粉体が空気とともに粉体分級機1内に投入される。粉
体投入管5には、絞り取付部7が設けられ、絞り板9が
取り付け可能になっている(図には説明上取り付けた状
態で示してある。)。回転軸8はケーシング2の中心に
設けられ、軸受け30によって回転自在に支持され、下
端にはプーリ33が取り付けてあり、図示しない駆動モ
ータに連結して回転駆動される。
The casing 2 has a circular shape as a whole, has a powder feeding port 3 connected to a powder feeding device (not shown) at the center of the upper surface, and has an air introducing port 10 and a coarse powder removing device on the peripheral side. An outlet 12 and a spiral casing 14 are provided. A powder feeding pipe 5 is connected to the powder feeding port 3, and the powder is fed into the powder classifier 1 together with air from the powder feeding pipe 5. The powder feeding pipe 5 is provided with a diaphragm mounting portion 7 so that a diaphragm plate 9 can be mounted (in the figure, it is shown in a mounted state). The rotating shaft 8 is provided at the center of the casing 2, is rotatably supported by a bearing 30, and has a pulley 33 attached to the lower end thereof, and is rotationally driven by being connected to a drive motor (not shown).

【0013】分級ロータ4は、回転軸8に一体に取り付
けられ、内部には円周部から軸心部下方に連通する空洞
部16が形成されており、この空洞部16内の開放周縁
部には、半径方向に放射状に延びる分級羽根18が複数
設けられ、分級室24が形成されている。又分級ロータ
4の上板19には、分級羽根18の半径方向ほぼ中央に
位置して粉体を落下させる開口20が外周に沿ってリン
グ状に形成してある。
The classification rotor 4 is integrally attached to the rotary shaft 8 and has a cavity 16 formed therein, which communicates from the circumferential portion to the lower portion of the shaft center. The cavity 16 has an open peripheral edge portion. Is provided with a plurality of classification blades 18 extending radially in a radial direction, and a classification chamber 24 is formed. In addition, on the upper plate 19 of the classification rotor 4, an opening 20 is formed in a ring shape along the outer periphery, which is located substantially in the center of the classification blade 18 in the radial direction and through which the powder falls.

【0014】又分級ロータ4の分級羽根18と対向する
下面には複数の補助羽根22が等間隔に配列されてお
り、分級ロータ4が回転したときこの補助羽根22によ
り空気に回転方向の流れを与え、旋回した状態で空気が
分級室24の方向へ導入されるようにしてある。又分級
ロータ4の外周囲にはケーシング2との間に空所26が
形成してあり、粗粉取出口12がこの空所26と連通し
て形成されている。
A plurality of auxiliary blades 22 are arranged at equal intervals on the lower surface of the classification rotor 4 facing the classification blades 18. When the classification rotor 4 rotates, the auxiliary blades 22 cause air to flow in the direction of rotation. Air is introduced in the direction of the classification chamber 24 in a given and swirled state. A space 26 is formed between the casing 2 and the outer periphery of the classification rotor 4, and the coarse powder outlet 12 is formed in communication with the space 26.

【0015】分級ロータ4の上板19とケーシング2の
上板17との間には、空所32が形成され、粉体投入口
3と分級ロータ4のリング状の開口20とを連通させて
いる。この空所32には、分級ロータ4の上板19の中
央部側に軸心部から外周方向に伸びる多数の粉体分散羽
根34が放射状に設けられ、かつこの分散羽根34の半
径方向の終端と開口20との間の分級ロータ4の上板1
9上面を平坦にして、この平坦面とこれに対向するケー
シング2の内面間において粉体を二次分散させるように
なっている。
A space 32 is formed between the upper plate 19 of the classification rotor 4 and the upper plate 17 of the casing 2 to connect the powder charging port 3 and the ring-shaped opening 20 of the classification rotor 4 to each other. There is. In this space 32, a large number of powder dispersion blades 34 extending from the axial center to the outer peripheral direction are radially provided on the center side of the upper plate 19 of the classification rotor 4, and the dispersion blades 34 have radial ends. Upper plate 1 of the classification rotor 4 between the opening 20 and the opening 20
9 The upper surface is made flat, and the powder is secondarily dispersed between this flat surface and the inner surface of the casing 2 facing it.

【0016】バランスロータ6は、分級ロータ4と配置
状態が対称となるように取り付けられており、分級ロー
タ4とほぼ同様に円周部から軸心部に連通する空洞部4
2を有し、空胴部42が分級ロータ4の空胴部16と連
通するようにして分級ロータ4及び回転軸8に一体に固
着されている。バランスロータ6の開口周縁部の空胴部
42内には多数の羽根44が放射状に設けられ、さらに
このバランスロータ6の開口外周囲にはこれを包囲する
ようにした渦巻ケーシング14がケーシング2に一体か
つ気密に取り付けられている。この渦巻ケーシング14
は、図示しないサイクロン、バッグフィルタなどの補集
装置、およびファン、ブロワーなどと連結されている。
The balance rotor 6 is mounted so as to be symmetrical with respect to the classification rotor 4 in arrangement, and the cavity portion 4 communicating from the circumferential portion to the axial center portion is almost the same as the classification rotor 4.
2, and the cavity portion 42 is integrally fixed to the classification rotor 4 and the rotary shaft 8 so as to communicate with the cavity portion 16 of the classification rotor 4. A large number of blades 44 are radially provided in the cavity 42 at the peripheral edge of the opening of the balance rotor 6, and the casing 2 is provided with a spiral casing 14 surrounding the outer periphery of the balance rotor 6 opening. It is integrally and airtightly attached. This spiral casing 14
Is connected to a collection device such as a cyclone and a bag filter (not shown), and a fan and a blower.

【0017】次に、このように構成された粉体分級機1
の運転法を説明する。
Next, the powder classifier 1 configured as described above
I will explain how to drive.

【0018】まず、分級ロータ4およびバランスロータ
6を図示しないモータにより所望の速度で回転させ、外
部に連結されたブロアーで粉体分級機1内部に負圧の空
気流を生じさせる。これによって、ケーシング2の空気
導入口10から空気が吸引され、この吸引によって流入
された空気は補助羽根22によって回転方向の流れに変
換され、旋回した状態で空所26から分級室24に入
り、分級室24で分級羽根18に沿った半径方向の流れ
となる。分級室24に入った空気は、バランスロータ6
を通過し、渦巻ケーシング14を介して吸引される。こ
のときの空気の流れを図1に矢印で示す。
First, the classification rotor 4 and the balance rotor 6 are rotated at a desired speed by a motor (not shown), and a negative pressure air flow is generated inside the powder classifier 1 by a blower connected to the outside. As a result, air is sucked from the air introduction port 10 of the casing 2, and the air introduced by this suction is converted into a flow in the rotational direction by the auxiliary blades 22 and swirls into the classification chamber 24 from the void 26, In the classification chamber 24, the flow is in the radial direction along the classification blade 18. The air that has entered the classification chamber 24 is the balance rotor 6
And is sucked through the spiral casing 14. The flow of air at this time is shown by an arrow in FIG.

【0019】この状態で粉体投入口3から空気とともに
投入された粉体原料は空気流に乗り、各分散羽根34間
を通過する間に分級ロータ4の軸心を中心とする放射方
向にほぼ均一に分散され、粉体の一次分散が行われる。
そして分散羽根34の終端から出た粉体は分級ロータ4
の回転に伴い分散羽根34の配列円のほぼ接線方向に放
射され、二次分散される。
In this state, the powder raw material charged with the air from the powder charging port 3 rides on the air flow, and while passing between the dispersion blades 34, the powder raw material is almost radiated about the axis of the classification rotor 4 in the radial direction. The powder is uniformly dispersed, and the powder is primarily dispersed.
The powder coming out from the end of the dispersion blade 34 is the classification rotor 4
With the rotation of, the light is radiated almost in the tangential direction of the array circle of the dispersion blades 34 and is secondarily dispersed.

【0020】十分に分散された粉体はリング状の粉体導
入用の開口20を通して分級室24に供給され、ここで
粉体の各粒子は分級ロータ4の回転による遠心力と半径
方向に流れる空気による抗力を受ける。これらの粒子の
うち遠心力>抗力の関係が成り立つ粗い粒子は分級ロー
タ4の外周囲の空所26内に飛ばされ、粗粉取出口12
からロータリーバルブなどを用いてエアシールした状態
で粉体分級機1の外に取り出される。また遠心力<抗力
の関係が成り立つ細かい粒子は半径方向の空気流に乗っ
た状態でバランスロータ6、渦巻ケーシング14を介し
て粉体分級機1の外に空気輸送され、サイクロン、バッ
グフィルタなどの捕集装置により捕集される。
The sufficiently dispersed powder is supplied to the classification chamber 24 through the ring-shaped powder introduction opening 20, where each particle of the powder flows in the radial direction along with the centrifugal force generated by the rotation of the classification rotor 4. Receives drag due to air. Of these particles, the coarse particles satisfying the relationship of centrifugal force> drag force are blown into the space 26 around the outer periphery of the classification rotor 4, and the coarse powder outlet 12
Is taken out of the powder classifier 1 while being air-sealed using a rotary valve or the like. Further, fine particles for which the relationship of centrifugal force <drag is established are pneumatically transported to the outside of the powder classifier 1 through the balance rotor 6 and the spiral casing 14 while being carried on the air flow in the radial direction, and are then transferred to the cyclone, bag filter, etc. It is collected by a collector.

【0021】ここで、例えば分級ロータ4の回転数を変
更することにより分級点を変更すると、回転数による遠
心力と空気流とのバランスが変化して、分級効率が低下
することがある。そこで、絞り板9を図に示すように粉
体投入管5に取り付ける。絞り板9を取り付けることに
より、粉体投入口3を通過する空気量と空気導入口10
からの空気導入量との比率を最適な値に変更して、遠心
力と空気の抗力とを分級点に適合した値に設定すること
ができ、分級点を変更した場合にも、分級精度を低下さ
せることなく分級できる。
Here, if the classification point is changed by changing the rotation speed of the classification rotor 4, for example, the balance between the centrifugal force and the air flow due to the rotation speed may change, and the classification efficiency may decrease. Therefore, the diaphragm plate 9 is attached to the powder feeding pipe 5 as shown in the figure. By attaching the diaphragm plate 9, the amount of air passing through the powder charging port 3 and the air introducing port 10
It is possible to change the ratio of the amount of air introduced from the to the optimum value, and set the centrifugal force and the drag force of air to values that match the classification points.Even when the classification points are changed, the classification accuracy is improved. Classification is possible without lowering.

【0022】尚、予め粉体投入口3の径を太く設定し空
気量を調整手段、もしくは絞り板9等により絞って使用
するようにしておくと、分級点の変更により空気量を増
加させる場合に調整手段を調整したり、絞り板を取り外
すなど対応が容易である。又、空気量を増大させるため
には、粉体導入口の径を増加させるだけではなく、分級
ロータ4の上板19とケーシング2との間隔を増加させ
るようにしてもよい。このようにした上で、粉体投入管
5の空気流入量のみを絞り板9等により制限することは
有効である。また、調整手段は通常の空気流通量を調整
できる可変式の空気調整手段でよい。
If the diameter of the powder charging port 3 is set to be thick and the amount of air is narrowed down by the adjusting means, the diaphragm plate 9 or the like, the amount of air is increased by changing the classification point. It is easy to adjust the adjustment means or remove the diaphragm plate. Further, in order to increase the amount of air, not only the diameter of the powder introduction port may be increased, but also the distance between the upper plate 19 of the classification rotor 4 and the casing 2 may be increased. After doing so, it is effective to limit only the air inflow amount of the powder feeding pipe 5 by the diaphragm plate 9 or the like. Further, the adjusting means may be a variable air adjusting means capable of adjusting the normal air flow rate.

【0023】更に、絞り板9は中心に通過孔が設けられ
ているため、粉体を分級ロータ4の中心に投入させるこ
とができ、分級ロータ4の上面での粉体の分散をより確
実にする効果もある。
Further, since the diaphragm plate 9 is provided with the passage hole at the center thereof, the powder can be introduced into the center of the classification rotor 4, and the dispersion of the powder on the upper surface of the classification rotor 4 can be more surely performed. There is also an effect to do.

【0024】(実験例)実験は、分級ロータの径が10
00mmの本発明にかかる遠心式粉体分級機を用いて、
回転数700rpm、総空気量120m3 /分、粉体の
供給量6t/時の条件で行なった。実験結果を図2及び
図3に示す。尚、総空気量とは、粉体投入口3からの空
気流入量と空気導入口10からの空気量の和であり、空
気量比とは、粉体投入口3から流入された空気量の空気
導入口10からの空気導入量に対する比率をいう。又、
図3のD25は、積算して25%の粉体が分離される粒子
径であり、D75は積算して75%の粉体が分離される粒
子径をいう。分級精度指数κは、D25をD75で割った値
で、この値が1に近い程分級精度が鋭いことを示す。図
2は図3の結果をグラフにしたもので、空気量比に対す
る分級精度指数κの変化を示す。このグラフから粉体投
入口3の空気量を制限して空気量比を低下させると、分
級精度指数κが向上することがよくわかる。
(Experimental example) In the experiment, the diameter of the classification rotor was 10
Using a centrifugal powder classifier according to the present invention of 00 mm,
The rotation speed was 700 rpm, the total air amount was 120 m 3 / min, and the powder supply amount was 6 t / hour. The experimental results are shown in FIGS. 2 and 3. The total air amount is the sum of the air inflow amount from the powder feeding port 3 and the air amount from the air introducing port 10, and the air amount ratio is the air amount flowing from the powder feeding port 3. It refers to the ratio to the amount of air introduced from the air inlet 10. or,
D 25 in FIG. 3 is a particle size at which 25% of powder is integrated and separated, and D 75 is a particle size at which 75% of powder is integrated and separated. The classification accuracy index κ is a value obtained by dividing D 25 by D 75 , and the closer the value is to 1, the sharper the classification accuracy is. FIG. 2 is a graph showing the results of FIG. 3, and shows the change of the classification accuracy index κ with respect to the air amount ratio. It is clear from this graph that the classification accuracy index κ improves when the air amount in the powder inlet 3 is limited and the air amount ratio is reduced.

【0025】一方、図4は、上記実験例に用いたと同様
な粉体分級機について、回転数を3600rpm、総空
気量62m3 /分、粉体の供給量250kg/時の条件
で分級したときの図2と同じ関係を示す。図4からわか
るように、空気量比がある値を超えると分級精度指数κ
が低下する。これは、粉体投入口3からの空気量を過剰
に制限すると、分級ロータ4の上面での粉体の分散に悪
影響を及ぼし、又遠心力と空気の抗力との関係にも悪影
響を及ぼしているためと思われる。
On the other hand, FIG. 4 shows a case where a powder classifier similar to that used in the above experimental example is classified under the conditions of a rotation speed of 3600 rpm, a total air amount of 62 m 3 / min, and a powder supply amount of 250 kg / hour. 2 shows the same relationship as in FIG. As can be seen from FIG. 4, when the air amount ratio exceeds a certain value, the classification accuracy index κ
Is reduced. This is because if the amount of air from the powder charging port 3 is excessively limited, it adversely affects the dispersion of the powder on the upper surface of the classification rotor 4 and also the relationship between the centrifugal force and the drag force of air. It seems to be because.

【0026】[0026]

【発明の効果】本発明の粉体分級機及びその運転法によ
れば、粉体投入口から流入する空気量と空気導入口から
の空気の導入量との比率を調整することにより、最適な
運転状態で分級を行なうことができる。更に、空気量比
を0.02〜0.14に設定することにより分級精度を
より高めることができる。
According to the powder classifier and the method of operating the same of the present invention, the optimum ratio can be obtained by adjusting the ratio of the amount of air flowing in from the powder inlet and the amount of air introduced from the air inlet. It is possible to perform classification in the operating state. Furthermore, by setting the air amount ratio to 0.02 to 0.14, the classification accuracy can be further improved.

【0027】又、分級機の空気量比を適宜に変更するこ
とができることとしたので、分級点を変更した場合にお
いても、かかる空気量の比率を、変更した分級点に適合
した値に設定することにより最適な分級状態を形成で
き、分級精度が低下せず、変更した分級点においても高
い効率で分級を行なわせることができる。
Further, since the air quantity ratio of the classifier can be changed appropriately, even when the classification point is changed, the air quantity ratio is set to a value suitable for the changed classification point. As a result, the optimum classification state can be formed, the classification accuracy does not decrease, and classification can be performed with high efficiency even at the changed classification point.

【0028】粉体投入口に接続した粉体投入管に空気調
整手段を設けたことにより、粉体投入口から流入される
空気量を容易に変更することができる。更に、絞り板を
取り付け、又取り外すことができるので、簡易に空気量
を調整することができ、しかも安価にできる。更に、粉
体を分級ロータの中心に投入でき、分散を確実にでき
る。
By providing the air adjusting means in the powder feeding pipe connected to the powder feeding port, the amount of air flowing in from the powder feeding port can be easily changed. Furthermore, since the diaphragm plate can be attached or detached, the amount of air can be easily adjusted and the cost can be reduced. Further, the powder can be put in the center of the classification rotor, and the dispersion can be ensured.

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

【図1】本発明による粉体分級機の断面図である。FIG. 1 is a sectional view of a powder classifier according to the present invention.

【図2】本発明による粉体分級機を用いた実験結果を示
すグラフである。
FIG. 2 is a graph showing experimental results using the powder classifier according to the present invention.

【図3】本発明による粉体分級機を用いた実験結果を示
す表である。
FIG. 3 is a table showing experimental results using the powder classifier according to the present invention.

【図4】本発明による粉体分級機を用いた実験結果を示
すグラフである。
FIG. 4 is a graph showing the experimental results using the powder classifier according to the present invention.

【符号の説明】[Explanation of symbols]

1 分級機 2 ケーシング 3 粉体投入口 4 分級ロータ 5 粉体投入管 6 バランスロータ 7 絞り取付部 8 回転軸 9 絞り板 10 空気導入口 12 粗粉取出口 14 渦巻ケーシング 16 空洞部 18 分級羽根 20 開口 1 Classifier 2 Casing 3 Powder charging port 4 Classification rotor 5 Powder charging pipe 6 Balance rotor 7 Restrictor mounting part 8 Rotating shaft 9 Throttling plate 10 Air inlet 12 Coarse powder outlet 14 Vortex casing 16 Cavity 18 Classifying blade 20 Opening

───────────────────────────────────────────────────── フロントページの続き (72)発明者 秋山 聡 埼玉県入間郡大井町鶴ケ岡5丁目3番1号 日清製粉株式会社生産技術研究所 (72)発明者 市川 孝博 埼玉県入間郡大井町鶴ケ岡5丁目3番1号 日清製粉株式会社生産技術研究所 (72)発明者 山田 幸良 埼玉県入間郡大井町鶴ケ岡5丁目3番1号 日清製粉株式会社生産技術研究所 (72)発明者 彦坂 徹 東京都中央区日本橋小網町18番4号 日清 エンジニアリング株式会社内 ─────────────────────────────────────────────────── ─── Continuation of front page (72) Inventor Satoshi Akiyama 5-3-1, Tsurugaoka, Oi-cho, Iruma-gun, Saitama Nisshin Seifun Co., Ltd. (72) Takahiro Ichikawa Tsurugaoka, Oi-cho, Iruma-gun, Saitama 5-3-1 Nisshin Seifun Co., Ltd. Production Technology Research Institute (72) Inventor Yukiyoshi Yamada Tsurugaoka, Oi-cho, Iruma-gun, Saitama 5-3-1 Nisshin Seifun Co., Ltd. (72) Inventor Hikosaka Tohru Nisshin Engineering Co., Ltd. 18-4 Koamimachi, Nihonbashi, Chuo-ku, Tokyo

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 上面中央に粉体投入口を、外側壁周囲に
空気導入口をそれぞれ有するケーシング内に、同径の円
板を2枚平行において円周部から軸中心方向に空気流通
空胴部とした分級ロータを垂直回転軸により回転可能に
設け、かつ前記分級ロータの空胴部内の分級室円周部に
複数の分級羽根を形成するとともに、該分級羽根間の上
部円板に粉体投入開口を設けてなる粉体分級機におい
て、前記粉体投入口からの空気流入量と前記空気導入口
からの空気量との比率を調整して運転することを特徴と
する前記粉体分級機の運転法。
1. An air flow cavity in which two powder disks having the same diameter are parallel to each other in the axial direction from the circumference to the axial center in a casing having a powder inlet in the center of the upper surface and an air inlet around the outer wall. A classification rotor having a vertical section is rotatably provided by a vertical rotation shaft, and a plurality of classification blades are formed on the circumference of the classification chamber in the cavity of the classification rotor, and a powder is formed on the upper disc between the classification blades. In the powder classifier provided with a charging opening, the powder classifying apparatus is operated by adjusting a ratio of an air inflow amount from the powder charging port and an air amount from the air introducing port. Driving method.
【請求項2】 前記空気導入口からの空気量に対する前
記粉体投入口からの空気流入量の空気量比を0.02〜
0.14にしたことを特徴とする請求項1に記載の粉体
分級機の運転法。
2. The air amount ratio of the air inflow amount from the powder charging port to the air amount from the air introducing port is 0.02 to 0.02.
The method for operating the powder classifier according to claim 1, wherein the method is 0.14.
【請求項3】 上面中央に粉体投入口を、外側壁周囲に
空気導入口をそれぞれ有するケーシング内に、同径の円
板を2枚平行において円周部から軸中心方向に空気流通
空胴部とした分級ロータを垂直回転軸により回転可能に
設け、かつ前記分級ロータの空胴部内の分級室円周部に
複数の分級羽根を形成するとともに、該分級羽根間の上
部円板に粉体投入開口を設けてなる粉体分級機におい
て、前記粉体投入口に空気流入量を調整する調整手段を
設けたことを特徴とする粉体分級機。
3. An air circulation cavity in which two powder disks having the same diameter are parallel to each other in the axial center direction from a circumferential portion in a casing having a powder charging opening at the center of the upper surface and an air introducing opening around the outer wall. A classification rotor having a vertical section is rotatably provided by a vertical rotation shaft, and a plurality of classification blades are formed on the circumference of the classification chamber in the cavity of the classification rotor, and a powder is formed on the upper disc between the classification blades. A powder classifier having a charging opening, wherein the powder charging port is provided with adjusting means for adjusting an air inflow amount.
【請求項4】 前記調整手段が絞り板であることを特徴
とする請求項3に記載の粉体分級機。
4. The powder classifier according to claim 3, wherein the adjusting means is a diaphragm plate.
【請求項5】 前記調整手段が可変式の空気量調整弁で
あることを特徴とする請求項3に記載の粉体分級機。
5. The powder classifier according to claim 3, wherein the adjusting means is a variable air amount adjusting valve.
JP06313394A 1994-03-31 1994-03-31 Powder classifier and its operation method Expired - Fee Related JP3485624B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP06313394A JP3485624B2 (en) 1994-03-31 1994-03-31 Powder classifier and its operation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP06313394A JP3485624B2 (en) 1994-03-31 1994-03-31 Powder classifier and its operation method

Publications (2)

Publication Number Publication Date
JPH07265802A true JPH07265802A (en) 1995-10-17
JP3485624B2 JP3485624B2 (en) 2004-01-13

Family

ID=13220473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP06313394A Expired - Fee Related JP3485624B2 (en) 1994-03-31 1994-03-31 Powder classifier and its operation method

Country Status (1)

Country Link
JP (1) JP3485624B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107626587A (en) * 2017-11-09 2018-01-26 宜兴市华井科技有限公司 A kind of silicon nitride grading wheel

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107626587A (en) * 2017-11-09 2018-01-26 宜兴市华井科技有限公司 A kind of silicon nitride grading wheel
CN107626587B (en) * 2017-11-09 2024-02-06 宜兴市华井科技有限公司 Silicon nitride classifying wheel

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