JPS6331260B2 - - Google Patents
Info
- Publication number
- JPS6331260B2 JPS6331260B2 JP58085073A JP8507383A JPS6331260B2 JP S6331260 B2 JPS6331260 B2 JP S6331260B2 JP 58085073 A JP58085073 A JP 58085073A JP 8507383 A JP8507383 A JP 8507383A JP S6331260 B2 JPS6331260 B2 JP S6331260B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- tower
- crusher
- crushed
- circular column
- 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
Landscapes
- Crushing And Grinding (AREA)
Description
【発明の詳細な説明】
本発明は乾式の塔式粉砕機(タワーミル)の改
良に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a dry tower mill.
乾式の塔式粉砕機は例えば特公昭39−5584号
「乾式塔式摩砕粉砕機」にも開示された公知の粉
砕機である。この粉砕機は第1図、第2図に示す
ように、閉鎖円塔1内の中心に軸があり、この軸
にスクリユー3が取り付けられており、ギヤード
モータ4によりスクリユー3を内容物を持ち上げ
る向きに回転させる。給鉱はロータリーバルブ5
によつて粉砕機内に定量供給する。粉砕は、給鉱
物同士で行わせることもあるが、通常は鋼球など
の粉砕媒体を粉砕機内に充填しておき、給鉱され
た被粉砕物は粉砕媒体とともに、スクリユー3に
よつて持ち上げられ、壁に沿つて落下し、この
間、粉砕媒体と被粉砕物との摺り合わせによる磨
砕作用により粉砕される。以下この粉砕された産
物を粉末という。 The dry tower type pulverizer is a known pulverizer disclosed, for example, in Japanese Patent Publication No. 39-5584 ``Dry Tower Type Grinding Mill''. As shown in Figures 1 and 2, this crusher has a shaft at the center of a closed circular column 1, and a screw 3 is attached to this shaft, and a geared motor 4 lifts the contents of the screw 3. Rotate it in the same direction. Ore feeding is rotary valve 5
Quantitatively supplied into the crusher by Although pulverization is sometimes carried out using feed minerals, usually a crushing medium such as steel balls is filled in the crusher, and the fed material to be crushed is lifted up by the screw 3 together with the crushing medium. , it falls along the wall, and during this time it is crushed by the grinding action of the grinding medium and the object to be crushed. Hereinafter, this pulverized product will be referred to as powder.
従来の塔式粉砕機では粉末を粉砕機外に排出す
る手段は全て通風を利用するものであつた。すな
わち第1図の粉砕機においては、送風機6による
粉砕機内の上昇気流に同伴されて上方から排出さ
れ、サイクロン2で捕集される。気流は送風機6
から再び粉砕機に至り循環する。第2図の粉砕機
にあつては粉末は粉砕機下部からスリツトを経て
送風機6からの気流に抽かれて粉砕機外に排出さ
れ、バグフイルタ7で捕集される。以上の従来の
塔式粉砕機では、被粉砕物が粉砕媒体の隙間に充
填する充填量あるいは充填密度等によつて粉砕機
内の通風抵抗が大きく変動する結果、被粉砕物の
供給量が一定であつても粉末の排出量が一定せ
ず、時として充填量の異常増加のため連続運転を
不能としたり、あるいは排出用送風機動力に異常
変動を惹起したりする欠点があつた。 In conventional tower-type pulverizers, all means for discharging powder out of the pulverizer utilize ventilation. That is, in the crusher shown in FIG. 1, the particles are discharged from above along with the upward air flow inside the crusher caused by the blower 6, and are collected by the cyclone 2. Airflow is by blower 6
Then it goes to the crusher again and is circulated. In the pulverizer shown in FIG. 2, the powder passes through a slit from the bottom of the pulverizer, is extracted by the airflow from the blower 6, is discharged outside the pulverizer, and is collected by a bag filter 7. In the above-mentioned conventional tower type crusher, the ventilation resistance inside the crusher varies greatly depending on the filling amount or packing density of the material to be crushed into the gaps between the crushing media, and as a result, the supply amount of the material to be crushed is not constant. However, the amount of powder discharged was not constant, and sometimes continuous operation was impossible due to an abnormal increase in the filling amount, or the power of the exhaust blower caused abnormal fluctuations.
本発明者らはこれらの欠点を改善すべく研究を
重ね第3図に示す通風を利用しない不部抜き出し
型の粉砕機を開発した。 The inventors of the present invention have conducted extensive research in order to improve these drawbacks and have developed a part-extracting type crusher that does not utilize ventilation, as shown in Fig. 3.
本発明は、閉鎖円塔内の粉砕媒体の隙間に充填
された被粉砕物の充填量を一定に保つことを目的
として、粉末を通風によることなく内塔下部より
機械的に抜き出すこととし、かつ粉末の抜き出し
量を任意に制御し得るようにしたことにある。 The present invention aims to keep the amount of material to be crushed filled in the gap between the crushing media in a closed circular column constant, by mechanically extracting the powder from the lower part of the inner column without using ventilation, and The objective is to be able to arbitrarily control the amount of powder extracted.
次に本発明を図面により説明する。第3図は本
発明の実施例を模式的に示す一部断面側面図であ
る。閉鎖円塔1内に上方に向つて推進力を生ずる
スクリユー3があり、ギヤードモータ4によつて
回転駆動され、円塔1内には必要により鋼球など
の粉砕媒体が充填されており、給鉱はロータリー
バルブ5を経て定量供給される。 Next, the present invention will be explained with reference to the drawings. FIG. 3 is a partially sectional side view schematically showing an embodiment of the present invention. There is a screw 3 in the closed circular column 1 that generates an upward propulsive force, and it is rotationally driven by a geared motor 4. The circular column 1 is filled with grinding media such as steel balls as necessary. The ore is supplied in a constant quantity through a rotary valve 5.
被粉砕物は粉砕媒体により磨砕されて粉末とな
り逐次下部に移行する。本発明は閉鎖円塔1の下
端横部に粉末の下部抜き出し口9を設け、この抜
き出し口9に抜き出し量を任意に制御可能な輸送
機10または回転バルブ11を設ける。輸送機1
0または回転バルブ11は例えば回転速度を任意
に調整可能な可変速モータ等によつて駆動するも
ので、輸送機11としてはスクリユーコンベヤ等
が適し、中でも気密性の高いいわゆる鉄砲スクリ
ユーコンベヤ、またはスクリユーピツチが先行き
漸減する漸変ピツチ型スクリユーコンベヤが最適
である。第3図aはスクリユーコンベヤ10を備
えた例、第3図bは回転バルブ11を備え別途の
輸送機13によつて送出する例を示した。第3図
cは粉末抜き出し口9と輸送機10あるいは回転
バルブ11とを接続する密閉ダクト12の内面を
シユートとして機能するよう傾斜角度を極力大き
く取つた例を示す。従来の通風による下部抜き出
し方式の塔式粉砕機は粉末の排出は送風機による
空気の吹き込みあるいは吸い出しによつていたの
でダクト内に粉末が堆積するという問題はなかつ
たが、本発明では空気輸送の方法を用いずに円塔
から密閉ダクトで粉末を機械的に直接抜き出す方
式とした結果、このダクト内での粉末の停滞ある
いは最悪の場合は閉塞という現象が生ずる場合が
ある。この現象は例えば粉末の粒度構成が広い範
囲に亘る場合に粉体の流動性が著しく阻害された
結果引き起こされるものである。このような場合
には、ダクト12を45度以上の傾斜とすれば、流
動性よく抜き出すことができ好ましい。 The material to be crushed is ground by the crushing medium and turned into powder, which gradually moves to the lower part. In the present invention, a lower powder outlet 9 is provided at the side of the lower end of the closed circular column 1, and this outlet 9 is provided with a transporter 10 or a rotary valve 11 that can arbitrarily control the amount of powder extracted. Transport aircraft 1
The rotary valve 11 is driven by, for example, a variable speed motor whose rotational speed can be adjusted arbitrarily, and a screw conveyor or the like is suitable as the transport device 11, and among them, a so-called gun screw conveyor with high airtightness, Alternatively, a gradual pitch type screw conveyor in which the screw pitch gradually decreases in the future is optimal. 3a shows an example equipped with a screw conveyor 10, and FIG. 3b shows an example equipped with a rotary valve 11 and sent out by a separate transporter 13. FIG. 3c shows an example in which the inclination angle is set as large as possible so that the inner surface of the sealed duct 12 connecting the powder outlet 9 and the transporter 10 or the rotary valve 11 functions as a chute. In conventional tower-type crushers that use ventilation to extract powder from the bottom, the powder is discharged by blowing in or sucking out air using a blower, so there was no problem of powder accumulating in the duct, but the present invention eliminates the problem of powder accumulation in the duct. As a result of using a system in which the powder is directly mechanically extracted from the circular tower through a closed duct without using any other method, the phenomenon of powder stagnation or, in the worst case, blockage, may occur in this duct. This phenomenon is caused, for example, as a result of the fluidity of the powder being significantly inhibited when the particle size structure of the powder is over a wide range. In such a case, it is preferable to make the duct 12 slope at an angle of 45 degrees or more so that the material can be extracted with good fluidity.
次に第3図cに示す本発明の実施例について効
果を説明する。この実施例の主なる仕様は次の通
り
円 塔 内径:1170mmφ
高さ:3500mmH
スクリユー 直径: 900mmφ
スリツトの目 : 20mm
粉砕媒体 : 27mmφ鋼球
抜き出し口ダクト傾斜:45゜
抜き出し装置:可変速モータ駆動鉄砲スクリユー
コンベヤ
被粉砕物 :高炉スラグ
被粉砕物給鉱量 :1.7t/h
以上の仕様の塔式粉砕機を用いて機械的抜き出
し装置により粉末を抜き出しつつ運転したとこ
ろ、粉末の排出は円滑で、全くトラブルがなく、
抜き出し量ならびに塔内被粉砕物レベル(高さ)
を種々変化させて運転した結果、一定運転状態の
維持が容易であり、また粉砕能力において従来の
風力を利用する抜き出し装置を備えた粉砕機に対
し、最大約70%の能力増加が可能となつた。 Next, the effects of the embodiment of the present invention shown in FIG. 3c will be explained. The main specifications of this example are as follows: Round tower Inner diameter: 1170mmφ Height: 3500mmH Screw diameter: 900mmφ Slit size: 20mm Grinding medium: 27mmφ Steel ball extraction port duct inclination: 45° Extraction device: Variable speed motor-driven gun Screw conveyor Materials to be crushed: Blast furnace slag Materials to be crushed Feed amount: 1.7 t/h When operating a tower-type crusher with specifications of 1.7 t/h or more while extracting powder using a mechanical extraction device, the powder was discharged smoothly. , no trouble at all,
Amount of extraction and level (height) of crushed material in the tower
As a result of operating the machine with various changes, it was found that it was easy to maintain a constant operating state, and the crushing capacity could be increased by up to 70% compared to a conventional crusher equipped with a wind-powered extractor. Ta.
第1図、第2図は乾式の塔式粉砕機の一部断面
側面図であり、何れも被粉砕物を気流式で排出す
るもの。第3図a,b,cは本発明に基づく下部
抜き出し式塔式粉砕機の実施例の一部断面側面図
を示す。
1……閉鎖円塔、2……サイクロン、3……ス
クリユー、4……ギヤードモータ、5……給鉱用
ロータリーバルブ、6……送風機、7……バグフ
イルタ、9……粉末抜き出し口、10……輸送機
(スクリユーコンベヤ)、11……回転バルブ、1
2……ダクト(シユート)、13……輸送機。
Figures 1 and 2 are partially sectional side views of a dry tower type crusher, both of which discharge the material to be crushed using an air stream. Figures 3a, b and c show partially sectional side views of an embodiment of a bottom drawer tower crusher according to the invention. 1... Closed circular tower, 2... Cyclone, 3... Screw, 4... Geared motor, 5... Rotary valve for ore feeding, 6... Blower, 7... Bag filter, 9... Powder extraction port, 10 ... Transport machine (screw conveyor), 11 ... Rotary valve, 1
2... Duct (chute), 13... Transport aircraft.
Claims (1)
り付けたスクリユーと該円塔下部に被粉砕物抜き
出し装置を設けてなる塔式粉砕機において、閉鎖
円塔の下端横部に被粉砕物の抜き出し口を設け、
該抜き出し口に抜き出し量を任意に制御可能な機
械的抜き出し装置を設けたことを特徴とする塔式
粉砕機。1. In a tower-type crusher consisting of a closed circular column, a shaft that rotates at the center, a screw attached to the shaft, and a device for extracting the crushed material at the bottom of the circular column, the crushed material is placed on the side of the lower end of the closed circular column. Provide an outlet for the
A tower-type crusher characterized in that the extraction port is provided with a mechanical extraction device that can arbitrarily control the extraction amount.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8507383A JPS59213451A (en) | 1983-05-17 | 1983-05-17 | Tower type crusher provided with mechanical withdrawing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8507383A JPS59213451A (en) | 1983-05-17 | 1983-05-17 | Tower type crusher provided with mechanical withdrawing apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59213451A JPS59213451A (en) | 1984-12-03 |
| JPS6331260B2 true JPS6331260B2 (en) | 1988-06-23 |
Family
ID=13848440
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8507383A Granted JPS59213451A (en) | 1983-05-17 | 1983-05-17 | Tower type crusher provided with mechanical withdrawing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59213451A (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3601376A (en) * | 1970-06-04 | 1971-08-24 | Kennedy Van Saun Co | Process and apparatus for preheating limestone and the like |
| CA948170A (en) * | 1970-11-10 | 1974-05-28 | Kalman Gabor | Comminuting device |
| US4337031A (en) * | 1981-02-02 | 1982-06-29 | Kennedy Van Saun Corporation | Preheating apparatus |
-
1983
- 1983-05-17 JP JP8507383A patent/JPS59213451A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59213451A (en) | 1984-12-03 |
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