JPH05285410A - Grinder - Google Patents

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Publication number
JPH05285410A
JPH05285410A JP11309892A JP11309892A JPH05285410A JP H05285410 A JPH05285410 A JP H05285410A JP 11309892 A JP11309892 A JP 11309892A JP 11309892 A JP11309892 A JP 11309892A JP H05285410 A JPH05285410 A JP H05285410A
Authority
JP
Japan
Prior art keywords
air
casing
powder
hopper
coarse 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.)
Pending
Application number
JP11309892A
Other languages
Japanese (ja)
Inventor
Satoru Tominaga
哲 富永
Kiyoshi Sasahara
喜代司 笹原
Shingo Mukai
新悟 向井
Nobuya Hatta
暢哉 八田
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 JP11309892A priority Critical patent/JPH05285410A/en
Publication of JPH05285410A publication Critical patent/JPH05285410A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To drastically enhance operation efficiency and to enhance the production capacity of the whole crusher body by constituting a sorting machine of a casing, a takeout hopper of coarse powder and middle powder, a charging chute and a movable damper which is arranged in the boundary part and tiltable in the flow direction of classification air. CONSTITUTION:A sorting machine 39 is equipped with a casing 40, a takeout hopper 15 of coarse powder and a takeout hopper 46 of middle powder respectively described below. The casing 40 is provided with an air introducing port 42 in one side and an air discharge port 43 in the other side so that the flow of classification air 41 flowing in the transverse direction is formed in the inside. The takeout hopper 45 of coarse powder and the takeout hopper 46 of middle powder are provided side by side in order toward an air discharge port 43 side from an air intoroduciton port 42 side in the lower part of the casing 40. A charging chute 50 is provided in the upper part of the casing 40 so that the ground material 5 supplied from a preliminary grinder falls and is supplied on the takeout hopper 45 near to the boundary part 53 of both hoppers 45, 46 while holding the necessary classification space. A movable damper 54 tiltable in the flow direction of a classification air 41 is provided in the boundary part 53.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はセメント製造等に使用す
る粉砕装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a crushing device used for cement production.

【0002】[0002]

【従来の技術】近年、微粉砕性能が優れた本粉砕機によ
る粉砕工程の前段階として粉砕能力の高い予備粉砕機に
より予め原料を粗粉砕するようにした2段粉砕方式の粉
砕装置の開発が進められている。
2. Description of the Related Art In recent years, as a pre-stage of the crushing process by the fine crusher having excellent fine crushing performance, a two-stage crushing system crushing device has been developed in which a preliminary crusher having a high crushing ability is used to roughly crush raw materials. It is being advanced.

【0003】図5は上記粉砕装置の一例を示すもので、
原料ホッパ1からの原料2をベルトフィーダ3を介して
ローラミル4(予備粉砕機)に導入して粗粉砕を行い、
該粗粉砕した粉砕物5をフィーダ6及びバケットエレベ
ータ7等を介して選別機8にかけ、該選別機8により選
別された粗粉9を前記ローラミル4に再び戻し、又、前
記選別機8により選別された中粉11をボールミル13
(本粉砕機)に導入して微粉砕するようにし、更に前記
ボールミル13で微粉砕された粉砕物5’を、バケット
エレベータ14及びエアスライド15等を介して分級機
16に導き、該分級機16により精粉(微粉)17と細
粉18とに分級し、該細粉18をエアスライド19を介
して前記ボールミル13に戻し、又、前記精粉17をエ
アスライド37を介して製品として取り出すようになっ
ている。
FIG. 5 shows an example of the above crushing device.
Raw material 2 from raw material hopper 1 is introduced into roller mill 4 (preliminary crusher) through belt feeder 3 to perform coarse crushing,
The coarsely crushed pulverized product 5 is applied to a sorting machine 8 via a feeder 6 and a bucket elevator 7, etc., and the coarse powder 9 sorted by the sorting machine 8 is returned to the roller mill 4 again and sorted by the sorting machine 8. Ball mill 13
It is introduced into (main crusher) to be finely crushed, and the crushed product 5 ′ finely crushed by the ball mill 13 is guided to a classifier 16 via a bucket elevator 14 and an air slide 15, and the classifier The fine powder (fine powder) 17 and the fine powder 18 are classified by 16 and the fine powder 18 is returned to the ball mill 13 through an air slide 19 and the fine powder 17 is taken out as a product through an air slide 37. It is like this.

【0004】尚、前記ローラミル4及び選別機8内に漂
う細粉30は、吸引ファン10により吸引排出しバグフ
ィルタ12で捕集してボールミル13に導入するように
してある。
The fine powder 30 floating in the roller mill 4 and the sorter 8 is sucked and discharged by the suction fan 10, collected by the bag filter 12, and introduced into the ball mill 13.

【0005】更に、前記ボールミル13内に漂う細粉3
0’は吸引ファン31により吸引排出してサイクロン3
2で分級し、該分級した前記細粉30’中の精粉17を
バグファン33により吸引してバグフィルタ34で捕集
すると共に、精粉17を分離した残りの細粉30’は前
記したバケットエレベータ14に導くようにしてある。
Further, fine powder 3 floating in the ball mill 13
0'is sucked and discharged by the suction fan 31 and the cyclone 3
The fine powder 17 in the fine powder 30 ′ classified in step 2 is sucked by the bag fan 33 and collected by the bag filter 34, and the fine powder 30 ′ remaining after separating the fine powder 17 is as described above. It leads to the bucket elevator 14.

【0006】又、前記分級機16の分級エア35は循環
ファン36により循環されるようになっているが、この
分級エア35の一部を前記バグフィルタ34に導くこと
により該分級エア35に同伴して流れる精粉17を捕集
し得るようにしてある。
The classifying air 35 of the classifier 16 is circulated by a circulation fan 36. A part of the classifying air 35 is guided to the bag filter 34 so that the classifying air 35 is entrained in the classifying air 35. The flowing fine powder 17 is collected.

【0007】上記した如き粉砕装置においては、従来、
選別機8として多段篩が用いられていた。
In the crushing apparatus as described above, conventionally,
A multi-stage sieve was used as the sorter 8.

【0008】前記多段篩の一例を図6を参照して以下に
説明する。
An example of the multi-stage screen will be described below with reference to FIG.

【0009】架台20に振動容器21が防振支持体22
及び伸縮継手23を介し振動を吸収されるように支承さ
れており、前記振動容器21には、篩目の大きさが異な
るスクリーン24a〜24eが複数段(五段)に、上段
から下段に行くにつれ篩目の大きさが小さくなるように
傾斜して配設されており、更に前記振動容器21の下側
部に振動発生装置(例えば偏心ホィールを回転して振動
を生ぜしめるユーラスモータ装置)25が取付けられて
いて該振動発生装置25により振動容器21が振動する
ようになっている。図中26は粉砕物投入口、27は粉
砕物衝突板、28は中粉取出しシュート、29は粗粉取
出しシュートを示す。
A vibration container 21 is mounted on a pedestal 20 and an anti-vibration support 22 is provided.
Further, the vibration container 21 is supported so as to absorb vibrations, and the vibrating container 21 has screens 24a to 24e having different sieve mesh sizes in a plurality of stages (five stages) from the upper stage to the lower stage. It is arranged so as to be inclined so that the size of the sieve mesh becomes smaller, and further, a vibration generator (for example, a eurus motor device for causing vibration by rotating an eccentric wheel) 25 on the lower side of the vibration container 21. Is attached, and the vibration container 21 is vibrated by the vibration generator 25. In the figure, 26 is a crushed material input port, 27 is a crushed material collision plate, 28 is a medium powder extraction chute, and 29 is a coarse powder extraction chute.

【0010】ローラミル4(図5参照)からの粉砕物5
の篩分けに際し、振動発生装置25により振動容器と一
体に各スクリーン24a〜24eを振動せしめ、次いで
粉砕物投入口26から前記ローラミル4からの粉砕物5
を投入すると、該粉砕物5は粉砕物衝突板27に衝突し
て分散し、第一段(最上段)のスクリーン24aで多段
篩分けされ、該スクリーン24aの篩目を通過しない粉
砕物5(粗粉)はスクリーン24aの傾斜下端から落下
して粗粉取出しシュート29に至る。他方、前記第一段
のスクリーン24aの篩目を通過して第二段のスクリー
ン24bに落下した粉砕物5は、該第二段のスクリーン
24bにより前記第一段のスクリーン24aの場合と同
様に多段篩分けされる。このようにして一番篩目の大き
い(粗い)第一段(最上段)のスクリーン24aから一
番篩目の小さい(細かい)第五段(最下段)のスクリー
ン24eにわたり順次篩分けされ、中粉11は中粉取出
しシュート28から又粗粉9は粗粉取出しシュート29
から夫々取り出される。
Ground material 5 from roller mill 4 (see FIG. 5)
At the time of sieving, the screens 24a to 24e are vibrated integrally with the vibrating container by the vibration generator 25, and then the pulverized material 5 from the roller mill 4 is fed from the pulverized material input port 26.
Then, the pulverized material 5 collides with the pulverized material collision plate 27 and is dispersed, and is multi-stage sieved by the screen 24a of the first stage (uppermost stage), and the pulverized material 5 (which does not pass through the sieve mesh of the screen 24a) The coarse powder falls from the lower inclined end of the screen 24a and reaches the coarse powder take-out chute 29. On the other hand, the crushed material 5 that has passed through the sieve mesh of the first-stage screen 24a and dropped to the second-stage screen 24b is the same as the case of the first-stage screen 24a by the second-stage screen 24b. Multi-stage screened. In this way, the first screen (a) with the largest (coarse) screen 24a to the fifth (the lowest) screen 24e with a smallest (fine) screen is screened, The powder 11 is from the medium powder extraction chute 28, and the coarse powder 9 is the coarse powder extraction chute 29.
Are taken out from each.

【0011】[0011]

【発明が解決しようとする課題】しかしながら、前記多
段篩はスクリーン24a〜24eの摩耗の進行が早く、
該スクリーン24a〜24eのメンテナンスの頻度が高
い為、粉砕装置の運転を前記メンテナンスの度に停止し
なければならなくなって連続運転を阻害してしまう問題
があった。
However, in the multistage sieve, the abrasion of the screens 24a to 24e progresses rapidly,
Since the screens 24a to 24e are frequently maintained, there has been a problem that the operation of the crusher must be stopped each time the maintenance is performed, which impedes continuous operation.

【0012】又、多段篩には処理能力が低いという欠点
があり、粉砕装置全体の生産能力が前記多段篩の処理能
力によって制約をうける問題があった。
Further, the multi-stage sieve has a drawback that it has a low processing capacity, and there is a problem that the production capacity of the entire pulverizer is restricted by the processing capacity of the multi-stage sieve.

【0013】更に、前記多段篩では分割粒径の限界が約
2mm程度と大きく、これ以下の分割粒径に設定するこ
とができなかった。
Further, in the above-mentioned multi-stage sieve, the limit of the divided particle size is as large as about 2 mm, and it has not been possible to set the divided particle size smaller than this.

【0014】本発明は斯かる実情に鑑みてなしたもの
で、上述した全ての問題を解決し得る選別機を備えた粉
砕装置を提供することを目的としている。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a crusher equipped with a sorting machine that can solve all the problems described above.

【0015】[0015]

【課題を解決するための手段】本発明は、予備粉砕機に
て粗粉砕された粉砕物を選別機により粗粉と中粉とに選
別し、該選別された粗粉を前記予備粉砕機に戻して再粉
砕し、前記選別された中粉を本粉砕機に導入して微粉砕
するようにした粉砕装置において、前記選別機を、内部
に横方向に流れる分級エアの流れが形成されるよう一側
にエア導入口を他側にエア排気口を夫々有するケーシン
グと、該ケーシングの下部に前記エア導入口側からエア
排気口側に向け順に並設した粗粉取出しホッパ及び中粉
取出しホッパと、該両ホッパの境界部に近い粗粉取出し
ホッパ上に前記予備粉砕機からの粉砕物が所要の分級空
間を隔てて落下供給されるよう前記ケーシング上部に配
設した投入シュートと、前記境界部に配設した分級エア
の流れ方向に傾動可能な可動ダンパとにより構成したこ
とを特徴とするものである。
According to the present invention, a crushed product roughly crushed by a preliminary crusher is sorted into a coarse powder and an intermediate powder by a sorter, and the sorted coarse powder is fed to the preliminary crusher. In a pulverizer that returns and re-pulverizes, and introduces the selected intermediate powder into the main pulverizer to finely pulverize, in the pulverizer, a flow of classification air that flows laterally inside is formed. A casing having an air inlet on one side and an air outlet on the other side, and a coarse powder extracting hopper and a medium powder extracting hopper arranged in parallel at the lower part of the casing from the air introducing port side toward the air exhaust port side. , A charging chute arranged on the upper part of the casing so that the pulverized material from the preliminary pulverizer is dropped and supplied across the required classification space onto the coarse powder extraction hopper near the boundary between the two hoppers, and the boundary. Tilts in the direction of classification air flow It is characterized in that constructed in accordance with the capacity movable damper.

【0016】[0016]

【作用】従って本発明では、エア導入口から空気を導入
してケーシング内に横方向に流れる分級エアの流れを形
成し、投入シュートの上部に、予備粉砕機にて粗粉砕し
た粉砕物を供給すると、該粉砕物は前記分級エアの流れ
に交差するようケーシング内に落下し、投入シュートと
境界部との間の分級空間を落下する間に前記粉砕物中の
中粉以下の粒度の粉粒体が前記分級エアの流れに乗って
下流側に運び去られ、分級エアの流れに乗れない重量の
大きな粗粉のみが重力により粗粉取出しホッパに落下し
て分離され、ローラミルに戻される。
Therefore, according to the present invention, air is introduced from the air introduction port to form a flow of classified air flowing in the lateral direction in the casing, and the crushed material coarsely crushed by the preliminary crusher is supplied to the upper part of the charging chute. Then, the pulverized product falls into the casing so as to intersect with the flow of the classification air, and while falling in the classification space between the charging chute and the boundary, the pulverized product has a particle size of not more than the intermediate powder. The body is carried to the downstream side along with the flow of the classification air, and only the coarse powder having a large weight that cannot ride on the flow of the classification air is dropped by the coarse powder into the hopper to be separated and returned to the roller mill.

【0017】一方、下流側に運び去られた粉粒体のうち
比較的粒度の大きな中粉は中粉取出しホッパ上方を移動
する間に重力により落下して中粉取出しホッパに回収さ
れ、ボールミルに導入される。
On the other hand, among the granular materials carried to the downstream side, the intermediate powder having a relatively large particle size falls due to gravity while moving above the intermediate powder extraction hopper and is collected in the intermediate powder extraction hopper, and is then stored in the ball mill. be introduced.

【0018】又、前記粗粉及び中粉を分離された残りの
粉粒体は、分級エアに浮遊されたままエア排気口から外
部に排出されて分級機等を経た後に回収される。
The remaining granular material from which the coarse powder and the intermediate powder have been separated is discharged from the air exhaust port to the outside while being suspended in the classification air, and recovered after passing through the classifier and the like.

【0019】[0019]

【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。
Embodiments of the present invention will be described below with reference to the drawings.

【0020】図1〜図3は本発明の一実施例であり、図
中図5と同一の符号を付した部分は同一物を表わしてい
る。
1 to 3 show an embodiment of the present invention, in which the same reference numerals as in FIG. 5 represent the same parts.

【0021】前記した図5の粉砕装置と略同様に構成さ
れた粉砕装置38において、ローラミル4(予備粉砕
機)とボールミル13(本粉砕機)との間に、従来の多
段篩に換えて図1及び図2に示すような空気分級式の選
別機39を設ける。
In the crushing device 38 having substantially the same structure as that of the crushing device shown in FIG. 5, a conventional multistage sieve is used between the roller mill 4 (preliminary crusher) and the ball mill 13 (main crusher). An air classification type sorting machine 39 as shown in FIG. 1 and FIG. 2 is provided.

【0022】尚、従来の多段篩に換えて前記選別機39
を採用した以外の構成は、図5の粉砕装置と略同様であ
るので説明を省略する。
It should be noted that instead of the conventional multistage sieve, the sorting machine 39
Since the configuration other than the above is similar to that of the crushing device of FIG. 5, the description thereof is omitted.

【0023】以下、前記選別機39について詳細に説明
する。
The sorting machine 39 will be described in detail below.

【0024】図中40は前記選別機39のケーシングを
示し、該ケーシング40は内部に横方向(図1における
左右方向)に流れる分級エア41の流れが形成されるよ
う一側(図1中左側)にエア導入口42を他側(図1中
右側)にエア排気口43を夫々有しており、該エア排気
口43は吸引ファン44を介して分級機16に接続され
ている。
Reference numeral 40 in the drawing denotes a casing of the sorter 39, and the casing 40 has one side (the left side in FIG. 1) so that a flow of classification air 41 flowing in the lateral direction (left and right direction in FIG. 1) is formed therein. ) Has an air inlet 42 on the other side (on the right side in FIG. 1), and the air outlet 43 is connected to the classifier 16 via a suction fan 44.

【0025】更に、前記ケーシング40の下部には前記
エア導入口42側からエア排気口43側に向け順に粗粉
取出しホッパ45と中粉取出しホッパ46とが並設され
ており、該両ホッパ45,46の下端部には交互に開閉
する二重のフラップを備えたエアロックダンパ47,4
8が夫々設けられていて、粗粉取出しホッパ45のエア
ロックダンパ47から排出される粗粉9がローラミル4
に戻され、中粉取出しホッパ46から排出される中粉1
1がボールミル13に導入されるようになっている。
Further, in the lower part of the casing 40, a coarse powder extraction hopper 45 and a medium powder extraction hopper 46 are arranged in parallel in this order from the air introduction port 42 side toward the air exhaust port 43 side. Airlock dampers 47, 4 with double flaps that open and close alternately at the lower ends of
8 is provided for each of the roller mill 4 and the coarse powder 9 discharged from the air lock damper 47 of the coarse powder extraction hopper 45.
Powder 1 returned to the factory and discharged from the powder hopper 46
1 is introduced into the ball mill 13.

【0026】又、前記ケーシング40上部には、前記粗
粉取出しホッパ45と中粉取出しホッパ46の境界部に
近い粗粉取出しホッパ45上にローラミル4からの粉砕
物5が所要の分級空間49を隔てて落下供給されるよう
に傾斜させた投入シュート50が配設されている。
In the upper part of the casing 40, a crushed material 5 from the roller mill 4 is provided with a required classification space 49 on the coarse powder extraction hopper 45 near the boundary between the coarse powder extraction hopper 45 and the intermediate powder extraction hopper 46. An injecting chute 50 that is inclined so as to be dropped and supplied is provided.

【0027】前記投入シュート50は、図2に示す如く
下方向きに末広がりの形状で形成され、その滑落面51
には逆V字形の分散板52が千鳥状に取り付けられてお
り、上部から供給された粉砕物5が投入シュート50内
を滑落する間にケーシング40の前後方向(図2におけ
る左右方向)に均等に分散されるようになっている。
As shown in FIG. 2, the charging chute 50 is formed in a downward diverging shape and has a sliding surface 51.
Inverted V-shaped dispersion plates 52 are attached in a zigzag manner, and while the pulverized material 5 supplied from above slides down in the charging chute 50, it is even in the front-back direction of the casing 40 (left-right direction in FIG. 2). It is supposed to be distributed in.

【0028】又、前記粗粉取出しホッパ45と中粉取出
しホッパ46の境界部53には、前記分級エア41の流
れ方向に傾動可能な可動ダンパ54が配設されており、
該可動ダンパ54の傾動位置を調整することにより分割
粒径を調整し得るようにしてある。
A movable damper 54 which is tiltable in the flow direction of the classification air 41 is disposed at the boundary 53 between the coarse powder extraction hopper 45 and the intermediate powder extraction hopper 46.
The divided particle size can be adjusted by adjusting the tilting position of the movable damper 54.

【0029】而して、前記吸引ファン44を駆動するこ
とによりエア導入口42から空気を吸引してケーシング
40内に横方向に流れる分級エア41の流れを形成し、
投入シュート50の上部に、ローラミル4にて粗粉砕さ
れた粉砕物5を供給すると、該粉砕物5は前記投入シュ
ート50の滑落面51を滑落する間に分散板52により
ケーシング40前後方向に均等に分散されて前記分級エ
ア41の流れに交差するようケーシング40内に落下
し、投入シュート50と境界部53との間の分級空間4
9で前記粉砕物5中の中粉11以下の粒度の粉粒体が前
記分級エア41の流れに乗って下流側(図1中右側)に
運び去られ、分級エア41の流れに乗れない重量の大き
な粗粉9のみが重力により粗粉取出しホッパ45に落下
して分離され、エアロックダンパ47から排出されてロ
ーラミル4に戻される。
Then, by driving the suction fan 44, air is sucked from the air inlet 42 to form a flow of the classified air 41 flowing in the casing 40 in the lateral direction,
When the crushed material 5 roughly crushed by the roller mill 4 is supplied to the upper part of the charging chute 50, the crushed material 5 is evenly distributed in the front-rear direction of the casing 40 by the dispersion plate 52 while sliding on the sliding surface 51 of the charging chute 50. And falls into the casing 40 so as to intersect the flow of the classification air 41, and the classification space 4 between the charging chute 50 and the boundary portion 53
At 9, the powder particles having a particle size of 11 or less in the pulverized material 5 are carried along the flow of the classification air 41 to the downstream side (right side in FIG. 1) and are not carried in the flow of the classification air 41. Only the coarse powder 9 having a large size falls by gravity into the coarse powder extraction hopper 45, is separated, is discharged from the air lock damper 47, and is returned to the roller mill 4.

【0030】一方、下流側に運び去られた粉粒体のうち
比較的粒度の大きな中粉11は中粉取出しホッパ46上
方を移動する間に重力により落下して中粉取出しホッパ
46に回収され、エアロックダンパ48から排出されて
ボールミル13に導入される。
On the other hand, among the powder particles carried to the downstream side, the intermediate powder 11 having a relatively large particle size is dropped by gravity while moving above the intermediate powder extraction hopper 46, and is recovered by the intermediate powder extraction hopper 46. , Is discharged from the air lock damper 48 and introduced into the ball mill 13.

【0031】又、前記粗粉9及び中粉11を分離された
残りの粉粒体は、分級エア41に浮遊されたままエア排
気口43から分級機16に導かれて該分級機16にて細
粉18と精粉17とに分級され、前記細粉18はボール
ミル13に導入されて微粉砕され、前記精粉17は製品
として回収される。
The remaining granular material from which the coarse powder 9 and the intermediate powder 11 are separated is guided to the classifier 16 from the air exhaust port 43 while being suspended in the classifying air 41, and the classifier 16 is used. The fine powder 18 and the fine powder 17 are classified, the fine powder 18 is introduced into the ball mill 13 and finely pulverized, and the fine powder 17 is recovered as a product.

【0032】従って上記実施例によれば、従来の多段篩
の如くメンテナンス頻度の高いスクリーンを用いること
がない為、粉砕装置38の運転を選別機39のメンテナ
ンス作業の為に停止する頻度が著しく低減され、運転効
率を大幅に向上することができる。
Therefore, according to the above-mentioned embodiment, since a screen having a high maintenance frequency unlike the conventional multi-stage sieve is not used, the frequency of stopping the operation of the crushing device 38 for the maintenance work of the sorting machine 39 is remarkably reduced. Therefore, the operation efficiency can be significantly improved.

【0033】又、従来の如く多段篩にかけて粉砕物5を
篩分けする場合と比較して選別機39の処理能力を大幅
に向上することができるので、粉砕装置38の生産能力
を従来より向上することができる。
Further, as compared with the conventional case where the pulverized material 5 is sieved by multistage sieving, the processing capacity of the sorter 39 can be greatly improved, so that the production capacity of the pulverizer 38 is improved as compared with the conventional case. be able to.

【0034】更に、従来の多段篩では、スクリーンの篩
目の製作上の限界から分割点を粒径2mm以下に設定す
ることができなかったが、空気分級式の選別機39を採
用したことにより、必要に応じて分割点を粒径2mm以
下に設定することが可能となる。
Further, in the conventional multi-stage sieve, it was not possible to set the dividing point to a particle size of 2 mm or less due to the limitation of the screen mesh of the screen, but by adopting the air classifying sorter 39. It is possible to set the dividing point to a particle size of 2 mm or less as necessary.

【0035】図4は本発明の他の実施例を示すもので、
選別機のエア排気口43を吸引ファン44を介してサイ
クロン32に接続した例であり、この実施例の場合も前
述した図1〜図3の実施例と同様の効果を奏することが
できる。
FIG. 4 shows another embodiment of the present invention.
This is an example in which the air exhaust port 43 of the sorter is connected to the cyclone 32 via the suction fan 44, and in the case of this embodiment as well, the same effects as those of the embodiments of FIGS. 1 to 3 described above can be obtained.

【0036】尚、本発明の粉砕装置は、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。
The crushing apparatus of the present invention is not limited to the above-mentioned embodiments, and it goes without saying that various modifications can be made without departing from the gist of the present invention.

【0037】[0037]

【発明の効果】以上説明したように、本発明の粉砕装置
によれば、下記の如き種々の優れた効果を奏し得る。
As described above, according to the crushing device of the present invention, various excellent effects as described below can be obtained.

【0038】(I)従来の多段篩の如くメンテナンス頻
度の高いスクリーンを用いることがない為、粉砕装置の
運転を選別機のメンテナンス作業の為に停止する頻度が
著しく低減され、運転効率を大幅に向上することができ
る。
(I) Since a screen with high maintenance frequency unlike the conventional multi-stage sieve is not used, the frequency of stopping the operation of the crushing device for the maintenance work of the sorting machine is remarkably reduced, and the operation efficiency is greatly improved. Can be improved.

【0039】(II)従来の如く多段篩にかけて粉砕物
を篩分けする場合と比較して選別機の処理能力を大幅に
向上することができるので、粉砕装置全体の生産能力を
従来より向上することができる。
(II) Since the processing capacity of the sorting machine can be greatly improved as compared with the conventional case where the pulverized material is sieved by multistage sieving, the production capacity of the entire pulverizing apparatus can be improved as compared with the conventional case. You can

【0040】(III)従来の多段篩では、スクリーン
の篩目の製作上の限界から分割点を粒径2mm以下に設
定することができなかったが、空気分級式の選別機を採
用したことにより、必要に応じて分割点を粒径2mm以
下に設定することが可能となる。
(III) In the conventional multi-stage sieve, it was not possible to set the dividing point to a particle size of 2 mm or less due to the limitation of the screen mesh of the screen, but by using the air classification type sorting machine, It is possible to set the dividing point to a particle size of 2 mm or less as necessary.

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

【図1】本発明の一実施例における選別機の断面図であ
る。
FIG. 1 is a sectional view of a sorting machine according to an embodiment of the present invention.

【図2】図1のII−II方向の矢視図である。FIG. 2 is a view taken along line II-II in FIG.

【図3】本発明の一実施例の系統図である。FIG. 3 is a system diagram of an embodiment of the present invention.

【図4】本発明の他の実施例を示す系統図である。FIG. 4 is a system diagram showing another embodiment of the present invention.

【図5】従来の粉砕装置の概略図である。FIG. 5 is a schematic view of a conventional crushing device.

【図6】図5の選別機である多段篩の一例を示す側面図
である。
FIG. 6 is a side view showing an example of a multi-stage sieve which is the sorting machine of FIG.

【符号の説明】[Explanation of symbols]

4 ローラミル(予備粉砕機) 5 粉砕物 9 粗粉 11 中粉 13 ボールミル(本粉砕機) 38 粉砕装置 39 選別機 40 ケーシング 41 分級エア 42 エア導入口 43 エア排気口 45 粗粉取出しホッパ 46 中粉取出しホッパ 49 分級空間 50 投入シュート 53 境界部 54 可動ダンパ 4 Roller Mill (Preliminary Crusher) 5 Crushed Material 9 Coarse Powder 11 Medium Powder 13 Ball Mill (Main Crusher) 38 Crusher 39 Sorter 40 Casing 41 Classification Air 42 Air Inlet 43 Air Exhaust Port 45 Coarse Powder Extraction Hopper 46 Medium Powder Extraction hopper 49 Classification space 50 Input chute 53 Boundary 54 Movable damper

───────────────────────────────────────────────────── フロントページの続き (72)発明者 八田 暢哉 東京都江東区豊洲三丁目2番16号 石川島 播磨重工業株式会社豊洲総合事務所内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Nobuya Hatta 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawajima Harima Heavy Industries Co., Ltd. Toyosu General Office

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 予備粉砕機にて粗粉砕された粉砕物を選
別機により粗粉と中粉とに選別し、該選別された粗粉を
前記予備粉砕機に戻して再粉砕し、前記選別された中粉
を本粉砕機に導入して微粉砕するようにした粉砕装置に
おいて、前記選別機を、内部に横方向に流れる分級エア
の流れが形成されるよう一側にエア導入口を他側にエア
排気口を夫々有するケーシングと、該ケーシングの下部
に前記エア導入口側からエア排気口側に向け順に並設し
た粗粉取出しホッパ及び中粉取出しホッパと、該両ホッ
パの境界部に近い粗粉取出しホッパ上に前記予備粉砕機
からの粉砕物が所要の分級空間を隔てて落下供給される
よう前記ケーシング上部に配設した投入シュートと、前
記境界部に配設した分級エアの流れ方向に傾動可能な可
動ダンパとにより構成したことを特徴とする粉砕装置。
1. A crushed product coarsely crushed by a preliminary crusher is sorted into a coarse powder and a medium powder by a sorter, and the sorted coarse powder is returned to the preliminary crusher and re-milled to perform the sorting. In the crushing device configured to introduce the fine powder into the main crusher and finely pulverize it, the sorting machine is provided with an air inlet on one side so that a flow of classification air flowing in the lateral direction is formed inside. A casing having an air exhaust port on each side, a coarse powder extraction hopper and a medium powder extraction hopper arranged in parallel at the lower part of the casing in order from the air introduction port side to the air exhaust port side, and at the boundary between both hoppers. A charging chute disposed on the upper part of the casing so that the pulverized material from the preliminary pulverizer is dropped and supplied across a required classification space on a near coarse powder extraction hopper, and a flow of classification air disposed at the boundary portion. A movable damper that can tilt in any direction A crushing device characterized by being made.
JP11309892A 1992-04-06 1992-04-06 Grinder Pending JPH05285410A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11309892A JPH05285410A (en) 1992-04-06 1992-04-06 Grinder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11309892A JPH05285410A (en) 1992-04-06 1992-04-06 Grinder

Publications (1)

Publication Number Publication Date
JPH05285410A true JPH05285410A (en) 1993-11-02

Family

ID=14603435

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11309892A Pending JPH05285410A (en) 1992-04-06 1992-04-06 Grinder

Country Status (1)

Country Link
JP (1) JPH05285410A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5529248A (en) * 1993-10-15 1996-06-25 Kawasaki Jukogyo Kabushiki Kaisha Method and apparatus for grinding material particles
JP2000070859A (en) * 1998-08-27 2000-03-07 Wacker Chemie Gmbh Air screening for polysilicon
KR100936872B1 (en) * 2002-12-26 2010-01-14 주식회사 포스코 A hopper dispersible the blast furnace return fine for the sintering process

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5529248A (en) * 1993-10-15 1996-06-25 Kawasaki Jukogyo Kabushiki Kaisha Method and apparatus for grinding material particles
JP2000070859A (en) * 1998-08-27 2000-03-07 Wacker Chemie Gmbh Air screening for polysilicon
KR100936872B1 (en) * 2002-12-26 2010-01-14 주식회사 포스코 A hopper dispersible the blast furnace return fine for the sintering process

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