JPH0434465B2 - - Google Patents
Info
- Publication number
- JPH0434465B2 JPH0434465B2 JP26454184A JP26454184A JPH0434465B2 JP H0434465 B2 JPH0434465 B2 JP H0434465B2 JP 26454184 A JP26454184 A JP 26454184A JP 26454184 A JP26454184 A JP 26454184A JP H0434465 B2 JPH0434465 B2 JP H0434465B2
- Authority
- JP
- Japan
- Prior art keywords
- classification
- blade
- chamber
- plate
- 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.)
- Expired
Links
- 239000006185 dispersion Substances 0.000 claims description 4
- 239000004568 cement Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 239000011362 coarse particle Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Combined Means For Separation Of Solids (AREA)
Description
〔産業上の利用分野〕
本発明は粉体を効率良く分級できるエアセパレ
ータに関する。
〔従来の技術〕
エアセパレータは粉砕プラント全体の効率を向
上させるための重要な機器として、古くからセメ
ント工業、鉄鋼業、化学工業等において数多く使
用されている。しかして近年の各種設備の大型化
はこのような粉砕部門においても例外ではなく、
従つてこれに付属するエアセパレータも当然大型
化が要求されるが、旋回気流中の遠心力が粒子を
分離する原理に基づくエアセパレータは大型にな
ると分離性能が急速に悪くなるという問題がみら
れる。すなわち従来この種のエアセパレータは分
級羽根取付板に取付ける分級羽根の位置が大きく
外側にはみ出し、分級羽根の幅aに対しはみ出し
長さbの関係はb/a>0.5であり、また分級羽
根の高さcに対し、分級羽根の上辺と分級室上部
壁との間隔dの関係はd/c>1である(第3
図)。
〔発明が解決しようとする問題点〕
このため分級羽根旋回域に流入する気流は分級
羽根に対して水平に流入させることが出来ず、そ
のため、製品として回収されるべき微粉の一部が
粉砕機に戻され、再度粉砕されるべき粗粉(戻り
粉)中にまぎれこみ、分級効率を悪くしていた
(第3図中矢印)。とくにセメント工業において、
この方式は分級室を小さくせねばならないために
分級室における循環風量が減少し、粉砕量が低下
してブレーン値からみた粉砕効率が低下する等の
欠点を有している。
本発明は上記の如き欠点を解消し、分級効率の
向上をはかると共に、特にセメントの品質面から
みた粒度構成を改善できるようなエアセパレータ
を提供することを目的とする。
〔問題点を解決するための手段〕
本発明は分級効率を向上させるため分級羽根旋
回域に流入する気流をできるだけ水平になるよう
に、分級羽根と分級羽根取付板との関係位置につ
いて種々検討した結果得られたもので、分級羽根
の上辺と分級室上部壁との間隔を分級羽根の高さ
の1/10以下とし、かつ分級室上部壁から中心方向
へ水平に整流板を設けることによつてその目的を
達成し本発明を完成した。
本発明を図によつて説明する。
第1図はエアセパレータの要部、すなわち分級
室を示す図である。軸8の回転によつて分散板
2、分級羽根取付板3が回転し、投入口7より分
散板2に落下した分級すべき粉体は遠心力により
分散される。このとき粗粒は細粒に比して大きな
遠心力を受けるために分級室側壁に達し重力によ
つて側壁に沿つて沈降するが、側壁に達しない細
粒はその内の比較的粗い粒子が回転する分級羽根
4によつて分離され、粗粒と同様に側壁に沿つて
沈降する。一方粗粒が分離された細粒は上記気流
に乗り分級室上部に到り、かくして粉体は分級さ
れる。
ここで分級羽根取付板3に放射状に複数枚取付
けられている分級羽根4は、その高さcを分級室
上部壁6と分級羽根の上辺との間の間隔dとの間
にd/c<1/10になるようにする。さらに整流板
5を分級室上部壁より中心方向に水平に設ける
(第2図)。整流板5の長さは分級羽根の中心側末
端がほぼ隠れる位が好ましい。
これによつて気流が従来と比べ、水平に近く分
級羽根旋回域に流入するようになり分級効率が向
上する。
本発明のエアセパレータはサイクロン型、ステ
ータバント型等のエアセパレータに好適に採用さ
れる。
実施例
分級室径600mmのサイクロン型エアセパレータ
を用い、第1表に示された操作条件でセメントを
分級し、得られた結果を同表に示した。
[Industrial Application Field] The present invention relates to an air separator that can efficiently classify powder. [Prior Art] Air separators have been widely used in the cement industry, steel industry, chemical industry, etc. since ancient times as important equipment for improving the efficiency of the entire crushing plant. However, in recent years, the size of various equipment has increased, and this type of crushing department is no exception.
Therefore, the attached air separator is naturally required to be larger, but air separators based on the principle that centrifugal force in swirling airflow separates particles have the problem that separation performance deteriorates rapidly as they become larger. . In other words, in conventional air separators of this type, the position of the classification blade attached to the classification blade mounting plate protrudes greatly outward, and the relationship between the width a of the classification blade and the protrusion length b is b/a>0.5, and the position of the classification blade attached to the classification blade mounting plate is large. The relationship between the height c and the distance d between the upper side of the classification blade and the upper wall of the classification chamber is d/c>1 (third
figure). [Problem to be solved by the invention] For this reason, the airflow flowing into the rotating area of the classification blades cannot be made to flow horizontally to the classification blades. The particles were mixed into the coarse powder (returned powder) that was to be returned to the ground and ground again, impairing the classification efficiency (arrow in Fig. 3). Especially in the cement industry,
This method has the disadvantage that the size of the classification chamber must be made smaller, which reduces the amount of circulating air in the classification chamber, resulting in a reduction in the amount of pulverization and a reduction in the pulverization efficiency in terms of the Blaine value. SUMMARY OF THE INVENTION An object of the present invention is to provide an air separator which can eliminate the above-mentioned drawbacks, improve classification efficiency, and improve particle size structure particularly from the viewpoint of cement quality. [Means for Solving the Problems] In order to improve the classification efficiency, the present invention has made various studies on the relative position of the classification blade and the classification blade mounting plate so that the airflow flowing into the classification blade rotation area is as horizontal as possible. The results obtained show that the distance between the upper side of the classification blade and the upper wall of the classification chamber is 1/10 or less of the height of the classification blade, and that a rectifier plate is provided horizontally from the upper wall of the classification chamber toward the center. Thus, the object was achieved and the present invention was completed. The present invention will be explained using figures. FIG. 1 is a diagram showing the main part of the air separator, that is, the classification chamber. The rotation of the shaft 8 rotates the dispersion plate 2 and the classification blade attachment plate 3, and the powder to be classified that falls onto the dispersion plate 2 from the inlet 7 is dispersed by centrifugal force. At this time, the coarse particles are subjected to a larger centrifugal force than the fine particles, so they reach the side wall of the classification chamber and settle along the side wall due to gravity, but the fine particles that do not reach the side wall are relatively coarse particles. It is separated by the rotating classification blade 4 and settles along the side walls in the same way as the coarse particles. On the other hand, the fine particles from which the coarse particles have been separated ride the airflow and reach the upper part of the classification chamber, and the powder is thus classified. Here, the plurality of classification blades 4 mounted radially on the classification blade mounting plate 3 has a height c that is d/c< Make it 1/10. Further, a rectifying plate 5 is provided horizontally from the upper wall of the classification chamber toward the center (FIG. 2). The length of the current plate 5 is preferably such that the end of the classification blade on the center side is almost hidden. As a result, the airflow flows into the swirling region of the classification blades more horizontally than in the past, improving classification efficiency. The air separator of the present invention is suitably employed in cyclone type, stator bunt type, etc. air separators. Example Using a cyclone type air separator with a classification chamber diameter of 600 mm, cement was classified under the operating conditions shown in Table 1, and the obtained results are shown in the same table.
本発明により最近の大型化したエアセパレータ
に見られる分離性能の低下を克服し、分級効率の
向上、セメント等の品質面に影響する粒度構成の
改善が達成されるという利点のほか、粉砕系電力
原単位の低減等経済面での利益も大きく、工業的
に利するところ極めて大きい。
The present invention overcomes the deterioration in separation performance seen in recent large-sized air separators, improves classification efficiency, and improves the particle size structure that affects the quality of cement, etc. There are great economic benefits such as reduction in unit consumption, and the industrial benefits are extremely large.
第1図は本発明のエアセパレータの分級室の一
実施例を示す断面図であり、第2図は分級羽根取
付板に設けた分級羽根及び整流板の関係位置を示
す平面図である。第3図は従来のエアセパレータ
における分級羽根取付タの断面図である。
1……分級室、2…分散板、3……分級羽根取
付板、4……分級羽根、5……整流板、6……分
級室上部壁、7……投入口、8……軸。
FIG. 1 is a sectional view showing an embodiment of the classification chamber of the air separator of the present invention, and FIG. 2 is a plan view showing the relative positions of the classification blades and the rectifying plate provided on the classification blade mounting plate. FIG. 3 is a sectional view of a classification vane attachment in a conventional air separator. DESCRIPTION OF SYMBOLS 1... Classifying chamber, 2... Dispersion plate, 3... Classifying blade mounting plate, 4... Classifying blade, 5... Rectifying plate, 6... Classifying chamber upper wall, 7... Input port, 8... Shaft.
Claims (1)
軸と一体的に回転する分散板、分級羽根取付板お
よび分級羽根を有するエアセパレータにおいて、
該分級羽根の上辺と分級室上部壁との間隔が該分
級羽根の高さの1/10以下であり、かつ該分級室上
部壁より中心方向へ水平に整流板を設けることを
特徴とするエアセパレータ。1. In an air separator having a dispersion plate, a classification blade mounting plate, and a classification blade that rotate integrally with a vertical shaft rotatably supported at the center of the classification chamber,
The air is characterized in that the distance between the upper side of the classification blade and the upper wall of the classification chamber is 1/10 or less of the height of the classification blade, and a rectifier plate is provided horizontally from the upper wall of the classification chamber toward the center. Separator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26454184A JPS61141978A (en) | 1984-12-17 | 1984-12-17 | Air separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26454184A JPS61141978A (en) | 1984-12-17 | 1984-12-17 | Air separator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61141978A JPS61141978A (en) | 1986-06-28 |
| JPH0434465B2 true JPH0434465B2 (en) | 1992-06-08 |
Family
ID=17404695
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26454184A Granted JPS61141978A (en) | 1984-12-17 | 1984-12-17 | Air separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61141978A (en) |
-
1984
- 1984-12-17 JP JP26454184A patent/JPS61141978A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61141978A (en) | 1986-06-28 |
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