JPS59173170A - Air classifier - Google Patents

Air classifier

Info

Publication number
JPS59173170A
JPS59173170A JP4757683A JP4757683A JPS59173170A JP S59173170 A JPS59173170 A JP S59173170A JP 4757683 A JP4757683 A JP 4757683A JP 4757683 A JP4757683 A JP 4757683A JP S59173170 A JPS59173170 A JP S59173170A
Authority
JP
Japan
Prior art keywords
powder
classification
chamber
air
dispersion
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
JP4757683A
Other languages
Japanese (ja)
Inventor
順二 山形
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP4757683A priority Critical patent/JPS59173170A/en
Publication of JPS59173170A publication Critical patent/JPS59173170A/en
Pending legal-status Critical Current

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  • Combined Means For Separation Of Solids (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 この発明は、セメントプラントなどの粉砕工程、に用い
る空気分級機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an air classifier used in a crushing process in a cement plant or the like.

一般にセメントプラン、トなどの粉砕工程は、t=1図
のように原料Aを粉砕機lに供給して粉砕した後入粉と
して空気分級機2に送り、回転中の精粉Bを分離し、こ
れを精粉室3に送り製品を得る。 この精粉室3から排
出される空気中には、精粉Bが相当含まれているので、
パックフィルタ4により回転し、これを前記製品に加え
る。
Generally, in the crushing process of cement plant, etc., raw material A is supplied to the crusher 1 as shown in the figure t=1, and after being crushed, it is sent to the air classifier 2 as an incoming powder, and the rotating refined powder B is separated. , this is sent to the milling room 3 to obtain a product. The air discharged from this fine powder chamber 3 contains a considerable amount of fine powder B, so
The pack filter 4 rotates and adds it to the product.

一方前記入粉中の粗粉Cは戻粉として粉砕機1に送られ
原料Aと共に再び粉砕される。
On the other hand, the coarse powder C in the powder input is sent to the crusher 1 as a return powder and is crushed again together with the raw material A.

従来、この種の空気分級機は分級室下部に空気入口を有
する空気室を設け、該分級室上部に精粉室を連通させ、
該分級室、中央部に入粉を分散させる分散板と分級用の
分級羽根を回転自在に設けている。
Conventionally, this type of air classifier has an air chamber with an air inlet at the bottom of the classification chamber, and a fine powder chamber is communicated with the top of the classification chamber.
A dispersion plate for dispersing incoming powder and a classification blade for classification are rotatably provided in the central part of the classification chamber.

回転中の分散板に投入された入粉は遠心力により分級室
内に散布され、分級室内を上昇する分級空気および回転
中の分散羽根により精粉と戻粉に分離され、精粉は精粉
室に収容され、一方戻り粉は、分級室内P旋回しながら
落下し、空気入口、付近で、再び分離される。ところで
前記戻粉は、層状となって分級室ケーシング内面を落下
するため、戻粉から分離される精粉は、少量である。従
って戻粉中の精粉の多くは、戻粉として粉砕機に送られ
る。
The incoming powder fed into the rotating dispersion plate is dispersed into the classification chamber by centrifugal force, and is separated into fine powder and returned powder by the classification air rising in the classification chamber and the rotating dispersion blade, and the fine powder is returned to the fine powder chamber. On the other hand, the returned powder falls while rotating inside the classification chamber P, and is separated again near the air inlet. By the way, since the returned powder forms a layer and falls down the inner surface of the classification chamber casing, the amount of fine powder separated from the returned powder is small. Therefore, most of the refined powder in the returned powder is sent to the grinder as returned powder.

ちなみに、この分級機では、回転中の精粉の30%前後
が戻粉として粉砕機に戻される。
Incidentally, in this classifier, approximately 30% of the rotating refined powder is returned to the pulverizer as returned powder.

本発明は上記の点に鑑み、戻粉中の精粉を多量に回収せ
しめ、空気分級機の性能を大巾に向よさせると共に粉砕
工程の消費動力を軽減することを目的とする◇ 本発明は分級機下部に空気入口を有する空気室を設け、
該分級室上部に精粉室を連通せしめ、該分級室中央部に
入粉を分散する分散板と、分級用の分級羽根を回゛転自
在に設け、前記分散板より下部の分級室内面に戻粉2分
散させる分散ベーンを設け、該分散ベーンの端縁にエア
吹き出しスリットを形成したことを特徴とする空気分級
機である。
In view of the above points, it is an object of the present invention to recover a large amount of refined powder in returned powder, greatly improve the performance of an air classifier, and reduce power consumption in the crushing process.◇ This invention has an air chamber with an air inlet at the bottom of the classifier,
A fine powder chamber is connected to the upper part of the classification chamber, and a dispersion plate for dispersing the incoming powder and a classification blade for classification are rotatably provided in the center of the classification chamber, and a part of the inner surface of the classification chamber below the dispersion plate is provided. This air classifier is characterized in that a dispersion vane for dispersing the returned powder is provided, and an air blowing slit is formed at the edge of the dispersion vane.

以下本発明の実施例を図面により説明すると、才2図に
おいて5は空気分級機本体であり、該本体5の上部に分
級室6を形成し、該分級室下部に空気室7を形成し、更
に分級室上部に精粉室8と連通する精粉通路9を設ける
。 前記空気室7に空気入口10を形成し、該′空気室
7の上部に案内羽根11を設ける。前記分級室中央部に
入粉を分散する分散板12を回転自在に設け、該分散板
几に分級用の分級羽根13t−固定する。
Embodiments of the present invention will be described below with reference to the drawings. In Figure 2, 5 is an air classifier main body, a classification chamber 6 is formed in the upper part of the main body 5, an air chamber 7 is formed in the lower part of the classification chamber, Further, a fine powder passage 9 communicating with the fine powder chamber 8 is provided in the upper part of the classification chamber. An air inlet 10 is formed in the air chamber 7, and a guide vane 11 is provided above the air chamber 7. A dispersion plate 12 for dispersing incoming powder is rotatably provided in the center of the classification chamber, and a classification blade 13t for classification is fixed to the dispersion plate box.

前記分級室60ケーシング6aは、その下部が逆円錐状
に形成され、該ケーシング6&下部内面に戻粉を分散さ
せる分散ベーン14を設け、該分散ベーン14の端縁に
エア吹き出しスリット15を形成する。
The lower part of the casing 6a of the classification chamber 60 is formed into an inverted conical shape, and a dispersion vane 14 for dispersing the returned powder is provided on the inner surface of the casing 6 and the lower part, and an air blowing slit 15 is formed at the edge of the dispersion vane 14. .

前記分散ベーン14は矛3図の様に円周方向に一定間隔
をおいて配設すると共に、分級室内を矢印几方向(分級
羽根の回転方向)に旋(ロ)する旋回流が、該分散ベー
ン14に衝突して斜上方に流れるよう傾斜をつける。
The dispersion vanes 14 are disposed at regular intervals in the circumferential direction as shown in Figure 3, and the swirling flow that swirls in the direction of the arrow (rotation direction of the classification vanes) within the classification chamber is dispersed. It is sloped so that it collides with the vane 14 and flows obliquely upward.

前記スリット15は、分散ベーン14の上部端縁および
側部端縁に形成し、圧縮空気口16から分散ベーン14
に送られる圧縮空気を斜上方および分級室中心方向(例
えば水平方向)に吹き出させる0゛ 次に、本実施例の作動について&朋すると、原料供給口
17から回転中の分散板計上に供給された入粉は、遠心
力により分級室内に散布される。
The slit 15 is formed at the upper edge and side edge of the dispersion vane 14, and the slit 15 is formed at the upper edge and the side edge of the dispersion vane 14, and the slit 15 is formed at the upper edge and the side edge of the dispersion vane 14.
The compressed air is blown out obliquely upward and toward the center of the classification chamber (for example, in the horizontal direction). The incoming powder is dispersed into the classification chamber by centrifugal force.

一方分級室6内では分級羽根13が回転していると共に
、空気入[1]0より空気室7に入り案内羽根11によ
りガイドされ、矢印a方向に旋回しなからL#7する分
級空気が発生しているO附記分級室内に散布された入粉
は、前記分級羽根J3と分級空気により軽い精粉と重い
戻粉に分離される。
On the other hand, in the classification chamber 6, the classification blade 13 is rotating, and the classified air enters the air chamber 7 from the air inlet [1] 0, is guided by the guide blade 11, and rotates in the direction of arrow a, then moves to L#7. The generated powder scattered in the classification chamber marked with O is separated into light fine powder and heavy returned powder by the classification blade J3 and the classification air.

この精粉は、分級空気に乗り精粉通路9を通り精粉室8
に収容され、一方戻粉は、分級室内面を旋1i1JL、
ながら層状となって、オ・4図に示す様に矢1:lJd
、方向にすべり落ち、分散ベーン14に衝突して、くだ
かれる。
This fine powder rides on the classified air and passes through the fine powder passage 9 into the fine powder room 8.
On the other hand, the returned powder is rotated around the inside of the classification chamber.
As shown in Fig. 4, arrow 1:lJd
, it slides down in the direction of , collides with the dispersion vane 14, and is crushed.

このくだかれた戻粉(B+C)は分級室内を分級羽根の
回転方向と同方向に旋回流に乗って分散ベーン14の端
縁から円周方向(矢印(11L方回)、に飛び出す。 
この際、戻粉< B+C)は、エア吹き出しスリット1
5から、斜上方(矢印e+)および分級室中心方向(例
えば水平方向)(矢印eヨ方向)に吹き出す圧縮エア°
と直交し、分級室6因に拡散されて、ntl記分級空気
(矢印f・方向)により再び洗われ、戻粉中の精粉Bが
分離される。
This broken back powder (B+C) flies out from the edge of the dispersion vane 14 in the circumferential direction (arrow (11L direction)) in the classification chamber in a swirling flow in the same direction as the rotation direction of the classification blade.
At this time, the returned powder < B + C) is removed from the air blowing slit 1.
5, compressed air is blown out diagonally upward (arrow e+) and toward the center of the classification chamber (for example horizontally) (arrow e yo direction).
It is perpendicular to , and is diffused into the classification chamber 6 and washed again by the classification air (direction of arrow f) to separate fine powder B in the returned powder.

この精粉Bは、分級空気(矢印f方向)に乗り精粉室8
に収容され、一方戻粉Cは粉砕機に戻され再び粉砕され
る。
This fine powder B rides on the classified air (in the direction of arrow f) to the fine powder chamber 8.
On the other hand, the returned powder C is returned to the pulverizer and pulverized again.

本発明は分散板より下部の分級室内面に、分散ベーンを
設け、数分散さ−ンの端縁にエア吹き出しスリットを形
成したので分級室内面を層状となって落下する戻粉を分
散ベーンでくだいて分散させ、更に、この分散した戻粉
を、エア吹き出しスリットより吹き出す圧縮エアと直交
させて拡散させることができる。従って戻粉は分級夜気
により、よく洗れるので、戻粉中の精粉を多量に回収で
き、空気分級機の分級機能を大巾に同上させると共に、
戻粉の循環量が下がり粉砕工程の消費動力を軽減するこ
とができる。
In the present invention, a dispersion vane is provided on the inside of the classification chamber below the dispersion plate, and an air blowing slit is formed at the edge of the several dispersion tube. The powder can be crushed and dispersed, and further, the dispersed returned powder can be spread perpendicularly to the compressed air blown out from the air blowing slit. Therefore, the returned powder can be washed well by the classified night air, so a large amount of fine powder in the returned powder can be recovered, and the classification function of the air classifier can be greatly improved.
The amount of recycled powder is reduced, and the power consumption in the crushing process can be reduced.

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

71図は、従来の空気分級機を用いたセメンゝ−Pvロ
Y1−チャート、第2図は、本発明の実施例を示す縦断
面図、1・3図は矛2図のm−m線断面図、矛4肉は本
発明の実施例で戻粉の分離状態を示す図である。 6・・・分級室 7・・・空気室 8−・・精粉室 10・・・空気入口 12・・・分散板 13−・・分級羽根 14・・・分散ベーン 15・・・エア吹き出しスリット 代理人升埋士 斎 藤   侑 外2名 @ 1 図 第 3w1 1日 112図 7 6 14  図 日 14  ′:゛、 11 −〇
Figure 71 is a cement-Pvro Y1 chart using a conventional air classifier, Figure 2 is a longitudinal sectional view showing an embodiment of the present invention, Figures 1 and 3 are the m-m line of Figure 2. The cross-sectional view and the 4th cross section are diagrams showing the separated state of the returned powder in an embodiment of the present invention. 6...Classifying chamber 7...Air chamber 8-...Powder chamber 10...Air inlet 12...Dispersion plate 13-...Classifying blade 14...Dispersion vane 15...Air blowing slit Representative masu filler Saifuji Yugai 2 people @ 1 Figure 3w1 1st 112 Figure 7 6 14 Figure 14 ′:゛, 11 -〇

Claims (1)

【特許請求の範囲】[Claims] 分級室下部に空気入口を有する空気室を設は該分級室上
部に精粉室を連通せしめ、該分級室中央部に入粉を分散
する分散板と分級用の分級羽根を回転自在に設け、前記
分散板より下部の分級室内面に戻粉を分散させる分散ベ
ーンを設け、該分散ベーンの端縁にエア吹き出しスリッ
トを形成したことを特徴とする空気分級機。
An air chamber with an air inlet is provided in the lower part of the classification chamber, and a fine powder chamber is communicated with the upper part of the classification chamber, and a dispersion plate for dispersing incoming powder and a classification blade for classification are rotatably provided in the center of the classification chamber. An air classifier characterized in that a dispersion vane for dispersing returned powder is provided on the inner surface of the classification chamber below the dispersion plate, and an air blowing slit is formed at an edge of the dispersion vane.
JP4757683A 1983-03-22 1983-03-22 Air classifier Pending JPS59173170A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4757683A JPS59173170A (en) 1983-03-22 1983-03-22 Air classifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4757683A JPS59173170A (en) 1983-03-22 1983-03-22 Air classifier

Publications (1)

Publication Number Publication Date
JPS59173170A true JPS59173170A (en) 1984-10-01

Family

ID=12779067

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4757683A Pending JPS59173170A (en) 1983-03-22 1983-03-22 Air classifier

Country Status (1)

Country Link
JP (1) JPS59173170A (en)

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