JPS62780Y2 - - Google Patents
Info
- Publication number
- JPS62780Y2 JPS62780Y2 JP12606482U JP12606482U JPS62780Y2 JP S62780 Y2 JPS62780 Y2 JP S62780Y2 JP 12606482 U JP12606482 U JP 12606482U JP 12606482 U JP12606482 U JP 12606482U JP S62780 Y2 JPS62780 Y2 JP S62780Y2
- Authority
- JP
- Japan
- Prior art keywords
- classification
- powder
- dispersion plate
- blades
- blade
- 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.)
- Expired
Links
- 239000006185 dispersion Substances 0.000 claims description 14
- 230000007423 decrease Effects 0.000 claims description 7
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 239000000843 powder Substances 0.000 description 30
- 239000002245 particle Substances 0.000 description 10
- 239000011362 coarse particle Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Landscapes
- Combined Means For Separation Of Solids (AREA)
Description
【考案の詳細な説明】 本考案は、空気分級機の改良に関する。[Detailed explanation of the idea] The present invention relates to improvements in air classifiers.
粉体の分散板と分級羽根と施回上昇気流とによ
り分級する空気分級機には種々の形式のものがあ
るが、ここではサイクロンセパレータを例として
説明する。第1図において1が分級室、2が分級
室1のケーシング、3が粉体供給管、4が粉体供
給口、8は粉体供給管3下端部の粉体の通路であ
る。また6が減速機付モータ、7が同モータ6に
より駆動される駆動軸、9が同駆動軸7の下端に
固定した分散板10が同分散板9上に固定した分
級羽根、11が含塵ガス排出管、12がサイクロ
ン、13がガス排出口、14が精粉排出口、15
が循環フアン、16が循環ガス取入口、17a,
17bがベーン、18がリングベルト、19が外
側ケーシング、20が粗粉排出口である。 There are various types of air classifiers that classify powder using a powder dispersion plate, classification blades, and swirling upward air current, but here, a cyclone separator will be explained as an example. In FIG. 1, 1 is a classification chamber, 2 is a casing of the classification chamber 1, 3 is a powder supply pipe, 4 is a powder supply port, and 8 is a powder passage at the lower end of the powder supply pipe 3. Further, 6 is a motor with a reducer, 7 is a drive shaft driven by the motor 6, 9 is a dispersion plate 10 fixed to the lower end of the drive shaft 7, is a classification blade fixed on the dispersion plate 9, and 11 is a dust-containing blade. Gas discharge pipe, 12 cyclone, 13 gas discharge port, 14 fine powder discharge port, 15
is a circulation fan, 16 is a circulation gas intake port, 17a,
17b is a vane, 18 is a ring belt, 19 is an outer casing, and 20 is a coarse powder discharge port.
上記サイクロンセパレータの分級機構について
説明すると、粉砕機の排出粉等のある粒径範囲を
もつた粉体は、供給口4より分級機内に供給さ
れ、粉体供給管3、通路8を経て、モータ6によ
り回転している分散板9上に落ちる。粉体は分散
板9より遠心力を受けて外壁方向へ飛散し、循環
フアン15により生じた分級室1内を上昇する気
流中に散布される。この際比較的大きい粒子は、
大きい遠心力のために分級室ケーシング2まで飛
ばされ衝突して重力の作用で落下し、分級され
る。一方、残りの粒子は上昇気流に乗つて上昇
し、分散板9を介して回転している分級羽根10
により打撃され、慣性力及び更に強い遠心力を受
けて外壁方向に向う。このとき旋回上昇流の粉体
に与える抗力と、分級羽根10の粉体に与える外
壁方向への遠心力とのつり合いで、微粉と粗粉に
分級され、微粉は気流とともに含塵ガス排出管1
1を通つてサイクロン12に導かれて補集され精
粉となる。気流はガス排出管13より出て、循環
フアン15を介して循環ガス取入口16より再び
分級機内に入る。また、分級された粗粉は、分級
室1のケーシング2を伝つて下降し、さらにベー
ン17a,17bリングベルト18を通り、粗粉
排出口20に導かれる。この時、ベーン部を下降
する粗粉は、ベーンをすり抜けた旋回気流により
再分散され、粗粒に付着していた微粉は再び噴き
上げられる。これにより粗粉への微粉の混入を少
くすることができる。 To explain the classification mechanism of the above-mentioned cyclone separator, powder having a certain particle size range, such as powder discharged from a crusher, is supplied into the classifier from the supply port 4, passes through the powder supply pipe 3 and the passage 8, and is transferred to the motor. 6, it falls onto the rotating dispersion plate 9. The powder is dispersed toward the outer wall by the centrifugal force from the dispersion plate 9, and is dispersed in the airflow generated by the circulation fan 15 and rising inside the classification chamber 1. At this time, relatively large particles are
Due to the large centrifugal force, it is blown up to the classification chamber casing 2, collides with it, falls under the action of gravity, and is classified. On the other hand, the remaining particles rise on the updraft and pass through the dispersion plate 9 to the rotating classification blade 10.
The object is struck by the object, receives inertial force and stronger centrifugal force, and moves toward the outer wall. At this time, the drag force exerted on the powder by the swirling upward flow and the centrifugal force exerted on the powder in the direction of the outer wall by the classification blades 10 are balanced, and the powder is classified into fine powder and coarse powder.
1 and is led to a cyclone 12 where it is collected and turned into fine powder. The airflow exits from the gas exhaust pipe 13, passes through the circulation fan 15, and enters the classifier again through the circulation gas intake port 16. Further, the classified coarse powder descends through the casing 2 of the classification chamber 1, further passes through the vanes 17a, 17b and the ring belt 18, and is guided to the coarse powder discharge port 20. At this time, the coarse powder descending through the vane portion is redispersed by the swirling airflow that has passed through the vane, and the fine powder adhering to the coarse particles is blown up again. This makes it possible to reduce the amount of fine powder mixed into coarse powder.
ただ、このような半径方向にある程度長さを持
つ分級羽根を有した分級機では、分級羽根の半径
方向の位置によつて周速度が異なるために、粒子
の受ける慣性力及び遠心力が、その半径方向によ
つて異なつてくるので、分離粒径を一定にするこ
とは望めない。特に分級羽根の取付部に近いとこ
ろでは、粒子の受ける慣性力、遠心力とも小さく
なるので、粗粒の精粉側へすり抜けがある。した
がつて精粉への粗粉の迷い込みはある程度避けら
れないという欠点があつた。 However, in such a classifier that has classification blades with a certain length in the radial direction, the circumferential speed differs depending on the radial position of the classification blade, so the inertial force and centrifugal force that particles are subjected to are Since it varies depending on the radial direction, it is not possible to make the separated particle size constant. Particularly near the attachment part of the classification blade, both the inertial force and the centrifugal force exerted on the particles are small, so that the coarse particles slip through to the fine powder side. Therefore, there was a drawback that the introduction of coarse powder into fine powder was unavoidable to some extent.
本考案は、前記分級羽根の欠点を改良するた
め、新規な分級羽根を提供し、分級効率の高い空
気分級機を得ることを目的として提案されたもの
で、分散板周縁部に、放射方向に延びる長尺の分
級羽根と、短尺の分級羽根とを交互に取付け、該
短尺の分級羽根を、その高さが外方に向つて減少
するように形成してなることを特徴とする空気分
級機に係るものである。 The present invention was proposed for the purpose of providing a new classification blade and obtaining an air classifier with high classification efficiency in order to improve the drawbacks of the classification blade. An air classifier characterized in that elongated classification blades and short classification blades are attached alternately, and the short classification blades are formed so that their height decreases outward. This is related to.
以下、第2図乃至第4図に示す実施例により、
本考案につき具体的に説明する。 Hereinafter, according to the embodiments shown in FIGS. 2 to 4,
The present invention will be explained in detail.
それらの図において、24は分散板(第1図の
分散板9に相当する部材)21は該分散板24の
周縁部に等間隔毎に、放射方向に延びるように取
付けられた長尺の分級羽根、22は相隣る長尺の
分級羽根21の間に、分散板24の周縁部に放射
方向に延びるように装着された短尺の分級羽根
で、長尺の分級羽根21と短尺の分級羽根22と
は、分散板24の周縁部に、交互に取付けらてい
る。また、各短尺の分級羽根22の高さhは、外
方に向つて減少するよう形成されている。(第4
図参照)なお、図中23は供給粉体の分散板24
への出口、25は分散板24の駆動軸をそれぞれ
示す。 In those figures, 24 is a dispersion plate (a member corresponding to the dispersion plate 9 in FIG. 1), and 21 is a long classifier attached to the periphery of the dispersion plate 24 at equal intervals so as to extend in the radial direction. The blades 22 are short classification blades attached to the peripheral edge of the dispersion plate 24 so as to extend in the radial direction between adjacent long classification blades 21, and the long classification blades 21 and the short classification blades 22 are attached alternately to the peripheral edge of the dispersion plate 24. Further, the height h of each short classification blade 22 is formed to decrease toward the outside. (4th
(See figure) In the figure, 23 is a dispersion plate 24 for the supplied powder.
25 indicates the drive shaft of the distribution plate 24, respectively.
本考案の空気分級機の分級羽根の一実施例は上
記のように構成されており、空気分級機の主な作
用は、第1図に示す従来の空気分級機とほぼ同様
で、気流に乗つて上昇した粒子は、分級羽根2
1,22によつて打撃され、慣性力及び遠心力を
受けて分級されるが、この時の分級羽根への粒子
の衝突は、分級羽根の高さ及び分級羽根の周速度
に依存し、両者とも大きい程衝突効率は大きい。
本考案では、外周方向に高さの減少する短尺の分
級羽根22が、従来形成の長尺の分級羽根21の
間に取付けられているため、中心側での衝突効率
が増大し、中心側での周速度の減少に伴なう衝突
効率の低下を打消す。この作用により、分級羽根
取付部に近い所でも、衝突効率が増加し、粗粒の
すり抜けが低減される。さらに分級羽根全体での
衝突効率が均一化され、従つて粒子の慣性力の受
け方が均一化され、分離粒径が一定に近づけられ
る。これらの作用により、本考案によれば、粗粉
の精粉側への迷い込みが低減されるとともに、分
級効率が向上するという実用的効果を挙げること
ができる。 One embodiment of the classification blade of the air classifier of the present invention is constructed as described above, and the main action of the air classifier is almost the same as that of the conventional air classifier shown in Fig. 1. The particles that have risen are transported to the classification blade 2
1 and 22, and are classified by receiving inertial force and centrifugal force, but the collision of particles with the classification blade at this time depends on the height of the classification blade and the circumferential speed of the classification blade, and both The larger both are, the higher the collision efficiency is.
In the present invention, the short classification blades 22 whose height decreases in the outer circumferential direction are installed between the conventionally formed long classification blades 21, so that the collision efficiency on the center side increases, and the collision efficiency on the center side increases. This counteracts the decrease in collision efficiency caused by a decrease in circumferential speed. Due to this effect, the collision efficiency is increased even in the vicinity of the classification blade attachment part, and the passage of coarse particles is reduced. Furthermore, the collision efficiency over the entire classification blade is made uniform, so that the inertial force of the particles is made uniform, and the separated particle size is brought to a constant value. Due to these effects, according to the present invention, it is possible to achieve the practical effects of reducing the straying of coarse powder into the fine powder side and improving the classification efficiency.
第1図は従来の空気分級機の略示的縦断面図、
第2図乃至第4図は、本考案の一実施例の概略説
明図で、第2図は平面図、第3図は第2図のA−
A線断面図、第4図は第2図のB−B線断面図で
ある。
21:長尺の分級羽根、22:短尺で外方に向
つて高さが減少する分級羽根、24:分散板、2
5:駆動軸。
Figure 1 is a schematic longitudinal cross-sectional view of a conventional air classifier;
2 to 4 are schematic explanatory diagrams of one embodiment of the present invention, where FIG. 2 is a plan view and FIG. 3 is a
FIG. 4 is a sectional view taken along line A--B in FIG. 2. 21: Long classification blade, 22: Short classification blade whose height decreases toward the outside, 24: Dispersion plate, 2
5: Drive shaft.
Claims (1)
羽根と、短尺の分級羽根とを交互に取付け、該短
尺の分級羽根を、その高さが外方に向つて減少す
るように形成してなることを特徴とする空気分級
機。 Long classification blades extending in the radial direction and short classification blades are attached alternately to the peripheral edge of the dispersion plate, and the short classification blades are formed so that their heights decrease toward the outside. An air classifier that is characterized by
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12606482U JPS5931475U (en) | 1982-08-23 | 1982-08-23 | air classifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12606482U JPS5931475U (en) | 1982-08-23 | 1982-08-23 | air classifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5931475U JPS5931475U (en) | 1984-02-27 |
| JPS62780Y2 true JPS62780Y2 (en) | 1987-01-09 |
Family
ID=30286782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12606482U Granted JPS5931475U (en) | 1982-08-23 | 1982-08-23 | air classifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5931475U (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0319969Y2 (en) * | 1986-09-02 | 1991-04-26 |
-
1982
- 1982-08-23 JP JP12606482U patent/JPS5931475U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5931475U (en) | 1984-02-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP0122608B1 (en) | Micropulverizer | |
| US4523990A (en) | Particulate classifying apparatus | |
| JPS62780Y2 (en) | ||
| JPS594477A (en) | Powder classifier | |
| JP2002119920A (en) | Airflow classifier | |
| JPH08173909A (en) | Classifier | |
| JPS5843271A (en) | Method and device for classifying granular substance | |
| KR970020201A (en) | Air classifier with dual classifier | |
| KR100235291B1 (en) | Air separator and method | |
| JPS6140390Y2 (en) | ||
| JPH0222060Y2 (en) | ||
| JP2672566B2 (en) | Air classifier | |
| KR940002840B1 (en) | Powder classifier | |
| GB1200996A (en) | Improvements in or relating to air separators for powders and granular materials | |
| JP3448716B2 (en) | Eddy current air classifier | |
| JPH07185467A (en) | Classifier | |
| JPS6044031B2 (en) | Structure of classification impeller for powder classification equipment | |
| JPH0811222B2 (en) | Powder classifier | |
| JP3083769B2 (en) | Collision type air crusher | |
| JPH0659464B2 (en) | Free vortex centrifugal classifier for vertical mill | |
| JPS5814956A (en) | Classifier for crusher | |
| JPS5839821Y2 (en) | air classifier | |
| JPH11216426A (en) | Airflow classifier | |
| JPS5867316A (en) | Air separator | |
| JPS5839820Y2 (en) | Wind classifier |