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JPH0314514B2 - - Google Patents

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Publication number
JPH0314514B2
JPH0314514B2 JP4143486A JP4143486A JPH0314514B2 JP H0314514 B2 JPH0314514 B2 JP H0314514B2 JP 4143486 A JP4143486 A JP 4143486A JP 4143486 A JP4143486 A JP 4143486A JP H0314514 B2 JPH0314514 B2 JP H0314514B2
Authority
JP
Japan
Prior art keywords
raw material
classification
section
powder
classifier
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
Application number
JP4143486A
Other languages
Japanese (ja)
Other versions
JPS62201679A (en
Inventor
Masakazu Hosono
Yoshihiko Sumya
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.)
Sumitomo Cement Co Ltd
Original Assignee
Sumitomo Cement Co Ltd
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 Sumitomo Cement Co Ltd filed Critical Sumitomo Cement Co Ltd
Priority to JP4143486A priority Critical patent/JPS62201679A/en
Publication of JPS62201679A publication Critical patent/JPS62201679A/en
Publication of JPH0314514B2 publication Critical patent/JPH0314514B2/ja
Granted legal-status Critical Current

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  • Combined Means For Separation Of Solids (AREA)
  • Centrifugal Separators (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は粉末原料を粗粉と微粉とに分離する分
級装置の改良に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an improvement in a classification device for separating powder raw materials into coarse powder and fine powder.

〔従来の技術〕[Conventional technology]

従来より、セメント等の粉末原料を気流に乗
せ、遠心力と求心力とを同時に作用させ、所望の
粒径域で粉末原料の選別を行なう分級装置が一般
に使用されている。このような粉末原料の分級装
置にあつては、一般に、複数の分級羽根が設けら
れた回転体から成る分級部において、分級部下方
に設けられた原料導入部から導入された粉末原料
を遠心力により粗粉を外周方向へ放出させると共
に、上記分級羽根間を経由して機外へ排出される
空気流の抗力による求心力により微粉を収集し、
粉末原料を微粉と粗粉とに分離選別し、微粉は該
分級部上方に設けられた微粉排出部から次工程へ
送り出すこととしている。
BACKGROUND ART Conventionally, a classification apparatus has been generally used that carries powder raw materials such as cement in an air stream, applies centrifugal force and centripetal force simultaneously, and sorts the powder raw materials in a desired particle size range. In such a powder raw material classification device, the powder raw material introduced from the raw material introduction section provided below the classification section is generally subjected to centrifugal force in the classification section, which is made up of a rotating body equipped with a plurality of classification blades. The coarse powder is discharged toward the outer circumference, and the fine powder is collected by the centripetal force caused by the drag force of the air flow discharged to the outside of the machine via the classification blades.
The powder raw material is separated and sorted into fine powder and coarse powder, and the fine powder is sent to the next process from a fine powder discharge section provided above the classification section.

〔従来技術の問題点〕[Problems with conventional technology]

しかしながら、このような従来の粉末原料の分
級装置にあつては、分級域における遠心力の方が
求心力よりも強く、外周方向に放出された粗粒
と、前段階における粉砕工程で分散され上昇気流
に乗つた粉末原料とが、回転体外周部において衝
突、混合を繰り返し、回転体外周部の含塵濃度が
著しく上昇するとともに粉末原料の再凝集を誘発
する場合もあつた。また、回転体内部において
も、遠心力と求心力とが粉末原料に連続して作用
するため、遠心力と求心力とのバランスがとれた
粒径の粒子が回転体内部に停滞してしまうことと
なる。従つて、回転体内部の含塵濃度の上昇、粉
末原料の再凝集が発生し、一方で、分級羽根へ粉
末原料が付着し易いものであつた。その結果、粗
粉粒子に付着した微粉粒子が粗粉中に混入した
り、粗粉粒子が微粉中へ混じり込む場合もあり、
特に、粉末原料が数μm単位の微粉の場合、高精
度な分級ができない、という欠点があつた。さら
に、回転体を回転させるための動力及び微粉を機
外へ排出させるための排風機の動力も無駄に消費
されてしまう、という欠点をも有していた。
However, in such conventional powder raw material classification equipment, the centrifugal force in the classification zone is stronger than the centripetal force, and the coarse particles released in the outer circumferential direction and the upward air flow dispersed in the crushing process in the previous stage The powder raw materials riding on the rotor repeatedly collide and mix on the outer periphery of the rotor, and the dust concentration on the outer periphery of the rotor increases markedly, and in some cases, the powder raw materials may re-agglomerate. Furthermore, since centrifugal force and centripetal force act continuously on the powder raw material inside the rotating body, particles with a particle size that balances centrifugal force and centripetal force become stagnant inside the rotating body. . Therefore, the dust concentration inside the rotating body increases and the powder raw material re-agglomerates, while the powder raw material tends to adhere to the classification blades. As a result, fine powder particles attached to coarse powder particles may be mixed into the coarse powder, or coarse powder particles may be mixed into the fine powder.
In particular, when the powder raw material is a fine powder on the order of several μm, there is a drawback that highly accurate classification cannot be performed. Furthermore, it also has the disadvantage that the power for rotating the rotating body and the power for the exhaust fan for discharging the fine powder to the outside of the machine are wasted.

そこで、本発明の技術的課題は、数μm単位の
分級域での分級であつても、高精度かつ効率良く
行なうことができる粉末原料の分級装置を提供す
ることにある。
Therefore, a technical object of the present invention is to provide a powder raw material classification apparatus that can perform classification with high precision and efficiency even in a classification range of several μm.

〔上記問題点解決のための技術的手段〕[Technical means for solving the above problems]

かかる技術的課題解決のため本発明にあつては
上記分級部を、複数の所定径の孔部が開設され、
垂直方向に所定間隔を置いて配置された複数の円
盤状の整流板と夫々の整流板の間に回転中心から
円周方向へ放射状に設けられた複数の分級羽根と
を有する分級機により構成する一方、該分級羽根
車の下方には整流板に開設された孔部の直下に開
口する原料導入パイプを設ける一方、上記原料導
入パイプ開口部を除き、上記分級部を原料導入部
から隔絶して包囲する粗粉収集排出部を設けたも
のである。
In order to solve this technical problem, in the present invention, the above-mentioned classification section is provided with a plurality of holes of a predetermined diameter,
A classifier having a plurality of disc-shaped rectifier plates arranged at predetermined intervals in the vertical direction and a plurality of classification blades provided radially in the circumferential direction from the center of rotation between the respective rectifier plates; Below the classification impeller, a raw material introduction pipe is provided that opens directly below the hole formed in the rectifier plate, while the classification section is isolated from and surrounded by the raw material introduction section, except for the raw material introduction pipe opening. It is equipped with a coarse powder collection and discharge section.

〔作用〕[Effect]

従つて、本発明に係る粉末原料の分級装置にあ
つては、上記分級部内に導入された粉末原料に
は、該分級部を構成する各整流板の間で遠心力と
求心力とが働き、粗粉は遠心力により分級部外周
方向へと放出され、供給される粉末原料と混合す
ることなく該分級部を包囲する粗粉収集排出部か
ら粗粉排出口へと向うと共に、微粉は求心力によ
り分級部の回転中心部に設けられた空隙部から微
粉排出口へと向うものである。
Therefore, in the powder raw material classification device according to the present invention, centrifugal force and centripetal force act on the powder raw material introduced into the classification section between the rectifying plates that constitute the classification section, and the coarse powder is The fine powder is discharged toward the outer periphery of the classification section by centrifugal force, and flows from the coarse powder collection/discharge section that surrounds the classification section to the coarse powder discharge port without mixing with the supplied powder raw material. The fine powder is directed from a gap provided at the center of rotation to the fine powder discharge port.

〔実施例〕〔Example〕

以下、添付図面に示す実施例に基づき本発明を
詳細に説明する。
Hereinafter, the present invention will be described in detail based on embodiments shown in the accompanying drawings.

第1図に示すように、本実施例に係る粉末原料
の分級装置1にあつては、分級部2と、該分級部
2下方に設けられた断面截頭円錐台状の原料導入
部3と、該分級部2の上方に設けられた微粉排出
部4とが設けられている。そして、上記分級部2
は、略短円筒状に形成された大型のフアンから成
る分級機20により構成されている。本実施例に
あつては、この分級機20は、第1図、第2図、
第3図及び第4図に示すように、垂直方向に所定
等間隔を置いて配置された4枚の円盤状の整流板
5,6,7,8と、該4枚の整流板5,6,7,
8の間に回転中心から円周方向へ放射状に設けら
れると共に反回転方向に所定の角度をもつて装着
された複数枚の分級羽根9とから成る。そして、
上記整流板5,6,7,8には、夫々径の異なる
円形の孔部10,11,12が開設されている。
これらの孔部10,11,12は、第3図及び第
4図に示すように、最下段の整流板5に開設され
ている孔部10が最も大径であり、中段下方の整
流板6に開設されている孔部11は中径であり、
そして中段上方の整流板7の孔部12は小径に形
成されており、第2図に示すように、最上段の整
流板8には孔部は開設されていない。また、該分
級機20の回転中心部には円筒状の空隙部13が
形成されており、該空隙部13の上方には微粉排
出部4が設けられている。一方、粗粉収集排出部
14は該分級部2を包囲して設けられており、こ
の粗粉収集排出部14は原料導入部3内に設けら
れたコーン部15とパイプ部16とから成り、該
パイプ部16の端部に設けられた粗粉排出口17
はロータリーバルブ18によりエアロツクされて
いる。また、分級機20の下方において上記コー
ン部15には、最下段の整流板の孔部10と同一
数の原料導入パイプ19が設けられ、これらの原
料導入パイプ19は該複数の孔部10の直下に開
口するように形成されており、これらの原料導入
パイプ19は、原料導入部3と分級部2との間を
結ぶものである。
As shown in FIG. 1, the powder raw material classification device 1 according to the present embodiment includes a classification section 2, and a material introduction section 3 with a truncated conical cross section provided below the classification section 2. , and a fine powder discharge section 4 provided above the classification section 2. And the above classification section 2
The classifier 20 is composed of a large fan formed into a substantially short cylindrical shape. In this embodiment, this classifier 20 is shown in FIGS.
As shown in FIGS. 3 and 4, four disc-shaped current plates 5, 6, 7, and 8 are arranged at predetermined equal intervals in the vertical direction; ,7,
8 and a plurality of classification blades 9 provided radially in the circumferential direction from the rotation center and attached at a predetermined angle in the counter-rotation direction. and,
Circular holes 10, 11, and 12 having different diameters are formed in the current plates 5, 6, 7, and 8, respectively.
As shown in FIGS. 3 and 4, these holes 10, 11, and 12 have the largest diameter in the hole 10 opened in the lowermost rectifying plate 5, and in the lower middle rectifying plate 6. The hole 11 opened in is of medium diameter,
The holes 12 of the upper middle rectifying plate 7 are formed to have a small diameter, and as shown in FIG. 2, no holes are formed in the uppermost rectifying plate 8. Further, a cylindrical cavity 13 is formed in the rotational center of the classifier 20, and a fine powder discharge part 4 is provided above the cavity 13. On the other hand, the coarse powder collecting and discharging section 14 is provided surrounding the classification section 2, and this coarse powder collecting and discharging section 14 consists of a cone section 15 and a pipe section 16 provided in the raw material introduction section 3, A coarse powder outlet 17 provided at the end of the pipe portion 16
is airlocked by a rotary valve 18. In addition, the cone section 15 below the classifier 20 is provided with the same number of raw material introduction pipes 19 as the holes 10 of the lowermost straightening plate, and these raw material introduction pipes 19 are connected to the plurality of holes 10. These raw material introduction pipes 19 are formed to open directly below, and connect between the raw material introduction section 3 and the classification section 2.

そして、上記粗粉収集排出部14は原料導入パ
イプ開口部25を除き、上記分級部2をコーン部
15及びパイプ部16により原料導入部3から隔
絶して包囲するように形成されている。
The coarse powder collecting and discharging section 14 is formed so as to surround the classifying section 2 separated from the raw material introducing section 3 by the cone section 15 and the pipe section 16, except for the raw material introducing pipe opening 25.

尚、図中符号21は分級機20を回転駆動する
モータ、22は該モータの駆動力を分級機20へ
伝達するシヤフトである。また、図示されていな
いが、原料導入部3の下方に開設された原料導入
口23にはエジエクタ等の原料供給装置が接続さ
れ、原料導入部3内へ気流に乗せて原料粉末を供
給するものである。また、微粉排出部4の先端部
の微粉排出孔24にはバツグフイルタ等の補集器
を介して図示外の風車が連結されるものである。
In the figure, reference numeral 21 is a motor that rotationally drives the classifier 20, and 22 is a shaft that transmits the driving force of the motor to the classifier 20. Although not shown, a raw material supply device such as an ejector is connected to the raw material introduction port 23 opened below the raw material introduction part 3, and supplies the raw material powder into the raw material introduction part 3 on an air flow. It is. Further, a windmill (not shown) is connected to the fine powder discharge hole 24 at the tip of the fine powder discharge portion 4 via a collector such as a bag filter.

従つて、本実施例に係る粉末原料の分級装置に
あつては、エジエクタ等の原料供給装置により原
料導入部3内へ気流と共に供給された原料粉末2
6は、原料導入パイプ19及び整流板5に開設さ
れた孔部10を介して分級機20内へ導入され
る。この場合、粉末原料26に対しては、該分級
機20内において分級機20の回転に伴なう遠心
力(第1図中二点鎖線で示す方向に働く力)と、
分級機20の中心部へ向う気流による求心力(第
1図中一点鎖線で示す方向に働く力)とが働く。
従つて、求心力の方が大きく作用する微粉粒子
は、第1図中実線で示すように、分級機20の中
心部に気流と共に吸引され、微粉排出孔24から
分級装置1外へ出て、前記図示外の補集器により
気体と分離して補集されるものである。
Therefore, in the powder raw material classification device according to the present embodiment, the raw material powder 2 supplied with the airflow into the raw material introduction section 3 by the raw material supply device such as the ejector
6 is introduced into the classifier 20 via the raw material introduction pipe 19 and the hole 10 formed in the rectifier plate 5. In this case, the powder raw material 26 is subjected to centrifugal force within the classifier 20 due to the rotation of the classifier 20 (force acting in the direction indicated by the two-dot chain line in FIG. 1),
A centripetal force (a force acting in the direction indicated by the dashed line in FIG. 1) is exerted by the airflow toward the center of the classifier 20.
Therefore, the fine particles on which the centripetal force acts more strongly are sucked into the center of the classifier 20 together with the airflow, as shown by the solid line in FIG. It is collected separately from gas by a collector not shown.

一方、遠心力の方が大きく作用する粗粉粒子
は、第1図中破線で示すように、分級機20の外
周方向へ放出され、粗粉収集排出部14を形成す
るコーン部15上に落下し、パイプ部16を滑落
して粗粉排出口17から装置外部へ排出される。
この場合、分級機20外方へ放出された粗粉粒子
と粉末原料を含んだ上昇気流とは上記コーン部1
5及びパイプ部16により隔離されているため、
従来のように、粗粉粒子と粉末原料とが衝突、混
合を繰り返すことはない。また、本実施例に係る
粉末原料の分級装置1にあつては、原料導入パイ
プ19及び整流板5に複数開設された孔部10を
介して断続的に分級機20へと供給されるもので
あるため、従来とは異なり、分級機20の中心方
向に吸引される気流の流れも断続的なものとな
る。従つて、分級機20内においては、遠心力は
常に粉末原料に作用しているが、分級機20内に
おいて該遠心力と求心力とがつり合う粒径域は存
在しない。
On the other hand, coarse particles on which the centrifugal force acts more strongly are discharged toward the outer periphery of the classifier 20, as shown by the broken line in FIG. Then, it slides down the pipe section 16 and is discharged from the coarse powder outlet 17 to the outside of the apparatus.
In this case, the upward airflow containing the coarse powder particles and powder raw materials discharged to the outside of the classifier 20 is the cone portion 1
5 and the pipe section 16,
Unlike the conventional method, the coarse powder particles and the powder raw material do not repeatedly collide and mix. In addition, in the powder raw material classification device 1 according to the present embodiment, the raw material is intermittently supplied to the classifier 20 through the raw material introduction pipe 19 and the plurality of holes 10 formed in the current plate 5. Therefore, unlike the conventional case, the airflow sucked toward the center of the classifier 20 is also intermittent. Therefore, although centrifugal force is always acting on the powder raw material in the classifier 20, there is no particle size range in the classifier 20 where the centrifugal force and the centripetal force are balanced.

〔発明の効果〕〔Effect of the invention〕

本発明にあつては、分級機により分離された粗
粉粒子と供給された粉末原料とが混合することが
ないと共に、従来のように、分級機内部において
遠心力と求心力とがつり合う粒径域の粒子が存在
しなくなるため、分級機外周部における含塵濃度
の上昇及び粉末原料の再凝集を防止することがで
き、また、粉末原料の分級羽根への付着をも防止
できる。従つて、本発明に係る粉末原料の分級装
置にあつては、数μm単位の分級域での分級であ
つても、高精度かつ効率良く行うことができる。
In the present invention, the coarse powder particles separated by the classifier and the supplied powder raw material do not mix, and unlike the conventional classifier, the particle size range where centrifugal force and centripetal force are balanced is achieved. Since these particles no longer exist, it is possible to prevent an increase in the dust concentration in the outer periphery of the classifier and the re-agglomeration of the powder raw material, and it is also possible to prevent the powder raw material from adhering to the classification blades. Therefore, in the powder raw material classification apparatus according to the present invention, even classification in a classification range of several μm can be performed with high precision and efficiency.

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

第1図は本発明に係る粉末原料の分級装置の一
実施例を示す断面図、第2図は上段の整流板位置
における第1図の−線断面図、第3図は中段
の整流板を示す第1図の−線断面図、第4図
は下段の整流板位置における第1図の−線断
面図である。 1……粉末原料の分級装置、2……分級部、3
……原料導入部、4……微粉排出部、5,6,
7,8……整流板、9……分級羽根、10,1
1,12……孔部、14……粗粉収集排出部、1
9……原料導入パイプ、20……分級機、25…
…原料導入パイプ開口部。
Fig. 1 is a sectional view showing an embodiment of the powder raw material classification device according to the present invention, Fig. 2 is a sectional view taken along the line - - of Fig. 1 at the position of the upper rectifying plate, and Fig. 3 is a sectional view showing the middle rectifying plate. 1, and FIG. 4 is a sectional view taken along the line - 1 in FIG. 1 at the position of the lower rectifier plate. 1... Powder raw material classification device, 2... Classification section, 3
...raw material introduction section, 4...fine powder discharge section, 5, 6,
7, 8... Current plate, 9... Classifying blade, 10, 1
1, 12... Hole section, 14... Coarse powder collection and discharge section, 1
9... Raw material introduction pipe, 20... Classifier, 25...
...raw material introduction pipe opening.

Claims (1)

【特許請求の範囲】[Claims] 1 分級部と、該分級部下方に設けられた原料導
入部と、該分級部上方に設けられた微粉排出部
と、該分級部に設けられた回転体を駆動する回転
駆動部とを有し、粉末原料を粗粉と微粉とに分離
する粉末原料の分級装置において、上記分級部
を、複数の所定径の孔部が開設され、垂直方向に
所定間隔を置いて配置された複数の円盤状の整流
板と夫々の整流板の間の回転中心から円周方向へ
放射状に設けられた複数の分級羽根とを有する分
級機により構成すると共に、該分級機の下方には
整流板に開設された孔部の直下に開口する原料導
入パイプを設ける一方、上記原料導入パイプ開口
部を除き、上記分級部を原料導入部から隔絶して
包囲する粗粉収集排出部を設けたことを特徴とす
る粉末原料の分級装置。
1 Comprising a classification section, a raw material introduction section provided below the classification section, a fine powder discharge section provided above the classification section, and a rotation drive section that drives a rotating body provided in the classification section. In a powder raw material classification device that separates powder raw materials into coarse powder and fine powder, the classification section is formed by a plurality of disc-shaped holes having a plurality of predetermined diameters and arranged at predetermined intervals in the vertical direction. The classifier has a current plate and a plurality of classification blades provided radially in the circumferential direction from the center of rotation between each current plate, and below the classifier there are holes formed in the current plate. A raw material introduction pipe that opens directly below the raw material introduction pipe is provided, and a coarse powder collection and discharge part that surrounds and isolates the classification part from the raw material introduction part except for the opening of the raw material introduction pipe is provided. Classifying device.
JP4143486A 1986-02-28 1986-02-28 Apparatus for classifying powdery raw material Granted JPS62201679A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4143486A JPS62201679A (en) 1986-02-28 1986-02-28 Apparatus for classifying powdery raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4143486A JPS62201679A (en) 1986-02-28 1986-02-28 Apparatus for classifying powdery raw material

Publications (2)

Publication Number Publication Date
JPS62201679A JPS62201679A (en) 1987-09-05
JPH0314514B2 true JPH0314514B2 (en) 1991-02-26

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JP4143486A Granted JPS62201679A (en) 1986-02-28 1986-02-28 Apparatus for classifying powdery raw material

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JP6713540B2 (en) 2016-08-09 2020-06-24 貢 院去 Classifier

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JPS62201679A (en) 1987-09-05

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