JPH02102768A - Classifier fitted with forcedly swirling vane - Google Patents

Classifier fitted with forcedly swirling vane

Info

Publication number
JPH02102768A
JPH02102768A JP25806588A JP25806588A JPH02102768A JP H02102768 A JPH02102768 A JP H02102768A JP 25806588 A JP25806588 A JP 25806588A JP 25806588 A JP25806588 A JP 25806588A JP H02102768 A JPH02102768 A JP H02102768A
Authority
JP
Japan
Prior art keywords
chamber
impeller
port
raw material
powder
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
JP25806588A
Other languages
Japanese (ja)
Other versions
JP2605830B2 (en
Inventor
Tsutomu Kawai
川合 勤
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 JP25806588A priority Critical patent/JP2605830B2/en
Publication of JPH02102768A publication Critical patent/JPH02102768A/en
Application granted granted Critical
Publication of JP2605830B2 publication Critical patent/JP2605830B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To improve classification efficiency by providing a rotatable swirl impeller in a casing and providing a suction port communicated with the feed port of a raw material powder. CONSTITUTION:A raw material powder supplied while being accompanied with an air flow through a feed port 3 is introduced into the feed port 3 and a feed chamber 8 of the lower layer of an impeller 4. Centrifugal force is imparted by rotation of the impeller 4 and thereby the air flow is caused and the raw material powder is accelerated and progressed to the outer peripheral direction and passed between the vanes 9 and extruded to a classification chamber 13 in the outside of the impeller 4. Coarse powder is carried farther and swirled along the outer wall of a casing 1. Fine powder is swirled inside the classification chamber 13 and raised toward a recovery chamber 7. Thereby fine powder uniform in particle size can be obtained.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明はセメントの原料であるクリンカーボイラ用微粉
炭、或いは小麦、トーモロコシ等の穀粉、石灰石、珪石
等の鉱物等の粉体を分級する強制旋回羽根付分級機に関
するものである。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention is a method for classifying pulverized coal for clinker boilers, which is a raw material for cement, or powders such as grain flour such as wheat and corn, and minerals such as limestone and silica stone. This relates to a classifier with rotating vanes.

[従来の技術] 第5図及び第6図は、従来の粉体の分級装置の一例を示
したもので、原料粉体は、側部の供給口aより空気や不
活性気体の気流に伴なわれて送入される。
[Prior Art] Figures 5 and 6 show an example of a conventional powder classification device, in which raw powder is fed through a side supply port a along with a stream of air or inert gas. It is sent to Japan.

分級装置のケーシングb的中央部には、円筒形の羽根車
Cがモータによって回転可能に配置され、該羽根車Cの
外周部には、数枚の羽根dが互に一定間隔をもち中心方
向に向うよう、即ち中心から放射状に配列されている。
A cylindrical impeller C is arranged rotatably by a motor in the center of the casing b of the classifier, and on the outer periphery of the impeller C, several blades d are spaced apart from each other at regular intervals and directed toward the center. In other words, they are arranged radially from the center.

送入された原料粉体は、該羽根車Cの回転によって、遠
心力を与えられ、又は羽IIIdに弾かれて、大きな粒
子はより外周部を、細かい粒子は内R部を旋回する。外
壁近くを旋回する大きな粒子は、旋回するに従って運動
量を失い自重により徐々に落下して下の排出口eより排
出され、細かい粒子は装置頂部「の回収口9より吸引さ
れて回収される。
The fed raw material powder is given a centrifugal force by the rotation of the impeller C, or is repelled by the blade IIId, so that larger particles swirl around the outer periphery and finer particles swirl around the inner R section. Large particles swirling near the outer wall lose momentum as they swirl and gradually fall due to their own weight and are discharged from the lower discharge port e, while fine particles are sucked and collected from the collection port 9 at the top of the device.

[発明が解決しようとする課題] しかし、上記の装置に於ては、羽根車Cの外側に原料粉
体が供給されるので、原料粉体に充分な遠心力を与える
ことが出来ず、慣性力によるtU粉と微粉の分級が完全
でなく、時には粗粉が微粉に混って頂部rより送出され
るという欠点かあった。
[Problems to be Solved by the Invention] However, in the above device, since the raw material powder is supplied to the outside of the impeller C, sufficient centrifugal force cannot be applied to the raw material powder, and the inertia There was a drawback that the classification of tU powder and fine powder by force was not perfect, and sometimes coarse powder was mixed with fine powder and sent out from the top r.

本発明は上記の欠点を解消し、精度のよい分級装置を提
供することを目的としたものである。
The present invention aims to eliminate the above-mentioned drawbacks and provide a highly accurate classification device.

[課題を解決するための手段] 本発明は底部に原料粉体供給口を有すると共に頂部に微
粉回収口を有するケーシング内に、水平に配した仕切壁
により上、下2室に仕切った旋回羽根車を回転駆動可能
に設け、各室外周に少なくとも一枚の羽根を設け、上家
の羽根は外端部か回転方向に対して下流側に位置するよ
うに傾斜させて設け、更に前記下室の下部略中央部に前
記原料粉体供給口と連通ずる吸入口を設けると共に前記
上室の上部略中央部に前記微粉回収口と連通ずる送出口
を設けたことを特徴とする強制旋回羽根付分級機にかか
るものである。
[Means for Solving the Problems] The present invention provides a swirl vane which is partitioned into two chambers, upper and lower, by a horizontally arranged partition wall in a casing which has a raw material powder supply port at the bottom and a fine powder collection port at the top. The wheel is rotatably driven, at least one blade is provided around the outer periphery of each chamber, and the upper blade is inclined so as to be located at the outer end or on the downstream side with respect to the direction of rotation, and the lower chamber A suction port communicating with the raw material powder supply port is provided at a lower center portion of the upper chamber, and a delivery port communicating with the fine powder recovery port is provided at a substantially center portion of the upper chamber. This applies to a classifier.

[作   用] 供給口と羽根車の下室とは連通しており原料粉体は、供
給口から羽根車下室(以下供給室という)内部に、直接
供給されるので、羽根が回転すると外部に供給するより
も大きな遠心力か与えられ、充分に粗粉と微粉の分離が
できる。
[Function] The supply port and the lower chamber of the impeller communicate with each other, and the raw material powder is directly supplied from the supply port into the lower chamber of the impeller (hereinafter referred to as the supply chamber), so when the impeller rotates, the outside A larger centrifugal force is applied than that supplied to the machine, and coarse powder and fine powder can be sufficiently separated.

又上室(以下回収室という)の羽根は、外端部が回転方
向に対して下流側に位置するよう(バックワード)配列
されているので、仮に粗粉が微粉に混って上昇しても羽
根に弾かれて、回収室に入ることが出来ない。
In addition, the blades in the upper chamber (hereinafter referred to as the collection chamber) are arranged so that the outer ends are located on the downstream side with respect to the rotation direction (backward), so if coarse powder mixes with fine powder and rises, However, they are not able to enter the recovery room because they are repelled by the blades.

従って、高精度の分級が行われ、粒度分布の狭い、粒径
の揃った微粉を得ることかできる。
Therefore, highly accurate classification is performed, and fine powder with a narrow particle size distribution and uniform particle size can be obtained.

[実 施 例] 以下、本発明の実施例を図面を参照しつつ説明する。[Example] Embodiments of the present invention will be described below with reference to the drawings.

第1図乃至第4図は本発明の一実施例であり、分級装置
のケーシングlの頂部中央には回収口2を、底部中央に
は原料粉体の供給口3を設ける。該ケーシングl内中央
に、円筒形の羽根車4を縦に配置し、該羽根車41部中
央にロータ軸5を設け、該軸5をケーシング1外のモー
タに回転駆動し得るよう連結する。
1 to 4 show an embodiment of the present invention, in which a recovery port 2 is provided at the center of the top of a casing 1 of a classifier, and a feed port 3 for raw material powder is provided at the center of the bottom. A cylindrical impeller 4 is arranged vertically in the center of the casing 1, a rotor shaft 5 is provided in the center of the impeller 41, and the shaft 5 is connected to a motor outside the casing 1 so as to be rotationally driven.

該羽根車4の内部で、上、下側面間の中央に仕切壁6を
水平方向に設け、該羽根1i4を等しい容積の上、下2
層の室すなわち回収室7及び供給室8に仕切る。
Inside the impeller 4, a partition wall 6 is horizontally provided at the center between the upper and lower surfaces, and the blades 1i4 are divided into upper and lower 2 parts with equal volumes.
It is divided into a layer chamber, namely a collection chamber 7 and a supply chamber 8.

該上、下に仕切った室7.8には、各々外周部に複数枚
の羽根9.9を等しい間隔に配列する。
A plurality of blades 9.9 are arranged at equal intervals on the outer periphery of each of the upper and lower partitioned chambers 7.8.

上層の回収室7の羽根9は、外端部が回転方向に対して
下流側に位置するように傾斜して(バックワード)設け
る。
The blades 9 of the upper recovery chamber 7 are provided so as to be inclined (backward) so that the outer ends thereof are located on the downstream side with respect to the rotation direction.

下層の供給室8の羽根9°は、中心から放射状に設けて
も、バックワードであってもよい。
The blades 9° of the lower supply chamber 8 may be provided radially from the center or may be provided backwards.

羽根車4の供給室8の下部中央に吸入口IOを設け、該
吸入口IOを介して直接供給室8とケーシング1底部中
央の供給口3を連通せしめる。
A suction port IO is provided at the center of the lower part of the supply chamber 8 of the impeller 4, and the supply chamber 8 is directly communicated with the supply port 3 at the center of the bottom of the casing 1 via the suction port IO.

更に回収室7の上部略中央に送出口Uを設け、該送出口
11を介して回収室7と回収口2とを連通せしめ、且ケ
ーシングl側部下方には粗粉の排出口12を設ける。
Furthermore, a delivery port U is provided approximately at the center of the upper part of the recovery chamber 7, and the collection chamber 7 and the collection port 2 are communicated through the delivery port 11, and a coarse powder discharge port 12 is provided below the casing L side. .

以下作動を説明する。The operation will be explained below.

装置の下方中央部の供給口3から原料粉体は気流に伴わ
れて供給されるが、供給口3と羽根車4下層の供給室8
は吸入口lOを介して連通しているので、直ちに供給室
8に流入する。
The raw material powder is supplied along with the airflow from the supply port 3 in the lower central part of the device.
Since it communicates through the suction port IO, it immediately flows into the supply chamber 8.

供給室8の外周部には、羽根9“が配置されているので
、羽根車4をモータで回転することにより、遠心力を与
えられ気流が起り原料粉体は加速され、気流に乗って、
外周方向に進み、羽根9°の間を通って、羽根車4の外
側の分級室」3に押出される。
Since blades 9'' are arranged on the outer periphery of the supply chamber 8, by rotating the impeller 4 with a motor, a centrifugal force is applied, an airflow is generated, the raw material powder is accelerated, and is carried on the airflow.
It advances in the outer circumferential direction, passes between the blades 9°, and is pushed out to the classification chamber 3 outside the impeller 4.

上記のように原料粉体は、羽根車4内部に供給され、羽
根9°により加速されて外部に出るので、充分に大きな
遠心力を与えられ、tU粉はより遠くまで運はれ、ケー
シングl外壁に沿って旋回する。
As mentioned above, the raw material powder is supplied to the inside of the impeller 4 and is accelerated by the blades 9° and exits to the outside, so that a sufficiently large centrifugal force is applied to the tU powder, and the tU powder is carried further, and the tU powder is transported further to the casing l. Rotate along the outer wall.

微粉は、分級室13の比較的内側を旋回し、遠心力に打
勝って、回収室7に向って上昇するが、その際、上層の
回収室7の羽根9はバックワードに配列されているので
、粒度の比較的小さいものでも、羽根9によって弾かれ
て、回収室7に入ることが出来ない。
The fine powder swirls relatively inside the classification chamber 13, overcomes the centrifugal force, and rises toward the collection chamber 7, but at this time, the blades 9 of the upper collection chamber 7 are arranged backwards. Therefore, even relatively small particles are repelled by the blades 9 and cannot enter the collection chamber 7.

非常に細かい粒子のみか、羽根9の間を通って、回収室
7に入ることが出来る。
Only very fine particles can pass between the blades 9 and enter the collection chamber 7.

細かい粒子は回収室7の送出口11より上部回収口2を
通って外部に搬送される。
The fine particles are transported to the outside from the outlet 11 of the recovery chamber 7 through the upper recovery port 2.

ill粉は、ケーシング1の外壁に沿って旋回しなから
、運動ごを失い、自重によって徐々に下降し、側部に設
けられた排出口12より排出される。
The ill powder rotates along the outer wall of the casing 1, loses its motion, gradually descends due to its own weight, and is discharged from the discharge port 12 provided on the side.

羽根9,9°の大きさ、枚数、傾斜角度及び羽根車4の
回転速度等を変えることによって、任意の狭い拉は分布
をもつ粒径のそろった粉体を得ることか可能である。
By changing the size of the blades 9, 9°, the angle of inclination, the rotational speed of the impeller 4, etc., it is possible to obtain powder having a uniform particle size distribution with any narrow blade.

以上のようにして、本発明の装置では小さい容積で効率
のよい分級を行うことができる。
As described above, the apparatus of the present invention can perform efficient classification with a small volume.

尚、本発明の強制旋回羽根付分級機は、上述の実施例に
のみ限定されるものではなく、本発明の要旨を逸脱しな
い範囲内において種々変更を加え得ることは勿論である
It should be noted that the forced swirling blade classifier of the present invention is not limited to the above-described embodiments, and it goes without saying that various changes may be made without departing from the gist of the present invention.

[発明の効果] 以上説明したように、本発明の強制旋回羽根付分級機に
よれば、下記の如き種々の優れた効果を奏し得る。
[Effects of the Invention] As explained above, according to the forced swirling blade classifier of the present invention, various excellent effects as described below can be achieved.

供給口と羽根車の供給室とは連通しているので、原料粉
体は羽根車の内部に供給され羽根車の回転によって、充
分な遠心力か与えられ粗粉と微粉の分級か充分に行われ
る。
Since the supply port and the supply chamber of the impeller are in communication, the raw material powder is supplied into the impeller, and the rotation of the impeller applies sufficient centrifugal force to sufficiently classify coarse powder and fine powder. be exposed.

更に分級後の粗粉が回収室に進入しようとしても、回収
室の羽根はバックワードに設けられているので、弾かれ
て進入することが出来ない。
Furthermore, even if the coarse powder after classification tries to enter the collection chamber, since the blades of the collection chamber are provided backwards, it will be repelled and will not be able to enter.

非常に細かい粒子のみ回収される。Only very fine particles are collected.

従って分級が完全であり粒度の揃った微粉を得ることが
出来る。
Therefore, classification is complete and fine powder with uniform particle size can be obtained.

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

第1図は本発明の一実施例の側断面図、第2図は第1図
のA−A方向矢視図、第3図は第1図のB−B方向矢視
図、第4図は第1図のD−D方向矢視図、第5図は従来
例を示す側断面図、第6図は第5図のC−C方向矢視図
である。 2は回収口、3は供給口、4は羽根車、6は仕切壁、7
は上層の室(回収室)、8は下層の室(供給室)、9は
回収室の羽根、9°は供給室の羽根、IOは吸入口、1
1は送出口、13は分級室を示す。
FIG. 1 is a side sectional view of an embodiment of the present invention, FIG. 2 is a view taken along the line A-A in FIG. 1, FIG. 3 is a view taken along line B-B in FIG. 1, and FIG. 5 is a side sectional view showing the conventional example, and FIG. 6 is a view taken along the line C--C in FIG. 5. 2 is a collection port, 3 is a supply port, 4 is an impeller, 6 is a partition wall, 7
is the upper chamber (recovery chamber), 8 is the lower chamber (supply chamber), 9 is the blade of the collection chamber, 9° is the blade of the supply chamber, IO is the suction port, 1
1 is a delivery port, and 13 is a classification chamber.

Claims (1)

【特許請求の範囲】[Claims] 1)底部に原料粉体供給口を有すると共に頂部に微粉回
収口を有するケーシング内に、水平に配した仕切壁によ
り上、下2室に仕切った旋回羽根車を回転駆動可能に設
け、各室外周に少なくとも一枚の羽根を設け、上室の羽
根は外端部が回転方向に対して下流側に位置するように
傾斜させて設け、更に前記下室の下部略中央部に前記原
料粉体供給口と連通する吸入口を設けると共に前記上室
の上部略中央部に前記微粉回収口と連通する送出口を設
けたことを特徴とする強制旋回羽根付分級機。
1) In a casing that has a raw material powder supply port at the bottom and a fine powder collection port at the top, a rotating impeller partitioned into two chambers, an upper and a lower chamber, by a horizontally arranged partition wall is provided so as to be rotatable. At least one blade is provided around the periphery, and the blade in the upper chamber is inclined so that the outer end is located on the downstream side with respect to the rotation direction, and the raw material powder is further provided in the lower center of the lower chamber. A classifier with forced swirling blades, characterized in that a suction port is provided that communicates with the supply port, and a delivery port that communicates with the fine powder recovery port is provided in the upper center of the upper chamber.
JP25806588A 1988-10-13 1988-10-13 Classifier with forced swirl vanes Expired - Lifetime JP2605830B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25806588A JP2605830B2 (en) 1988-10-13 1988-10-13 Classifier with forced swirl vanes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25806588A JP2605830B2 (en) 1988-10-13 1988-10-13 Classifier with forced swirl vanes

Publications (2)

Publication Number Publication Date
JPH02102768A true JPH02102768A (en) 1990-04-16
JP2605830B2 JP2605830B2 (en) 1997-04-30

Family

ID=17315041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25806588A Expired - Lifetime JP2605830B2 (en) 1988-10-13 1988-10-13 Classifier with forced swirl vanes

Country Status (1)

Country Link
JP (1) JP2605830B2 (en)

Also Published As

Publication number Publication date
JP2605830B2 (en) 1997-04-30

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