JPS6119307B2 - - Google Patents

Info

Publication number
JPS6119307B2
JPS6119307B2 JP9558081A JP9558081A JPS6119307B2 JP S6119307 B2 JPS6119307 B2 JP S6119307B2 JP 9558081 A JP9558081 A JP 9558081A JP 9558081 A JP9558081 A JP 9558081A JP S6119307 B2 JPS6119307 B2 JP S6119307B2
Authority
JP
Japan
Prior art keywords
crushed
rotating container
fixed cover
container
casing
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
JP9558081A
Other languages
Japanese (ja)
Other versions
JPS57209649A (en
Inventor
Toyomi Nishida
Takeshi Suzuki
Taku Hatamori
Sei Terada
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy Industries 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP9558081A priority Critical patent/JPS57209649A/en
Priority to US06/389,145 priority patent/US4504020A/en
Priority to DE19823222890 priority patent/DE3222890A1/en
Priority to FR8210724A priority patent/FR2507925B1/en
Priority to DE19828217579U priority patent/DE8217579U1/en
Priority to DK275182A priority patent/DK275182A/en
Priority to GB08217959A priority patent/GB2100618B/en
Publication of JPS57209649A publication Critical patent/JPS57209649A/en
Publication of JPS6119307B2 publication Critical patent/JPS6119307B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明はセメント原料やクリンカー等の微粉砕
を行う円錐形ボールミルの改良に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a conical ball mill for finely pulverizing cement raw materials, clinker, etc.

円錐形ボールミルには、例えば西独国特許第
1607562号に記載されているようなものがある。
それは、第1図に示すようにほゞ逆円錐台形状の
回転容器1とこの回転容器1の上部を覆う如く配
置された固定カバー2とからなり、回転容器1内
の多数の粉砕媒体3が回転容器1の回転により遠
心力を受け、回転容器1の側壁1a上を上昇し固
定カバー2に達すると、その粉砕媒体3の有する
慣性力でもつて固定カバー2の内面の案内羽根4
に沿つて内方向に移動すると共に落下し、固定カ
バー2の上部に設けられた被粉砕物投入シユート
5から供給された回転容器1内の被粉砕物6を粉
砕する装置である。
For conical ball mills, for example, West German patent no.
There is something like the one described in No. 1607562.
As shown in FIG. 1, it consists of a rotating container 1 having an approximately inverted truncated cone shape and a fixed cover 2 placed to cover the upper part of the rotating container 1. When the rotating container 1 receives a centrifugal force due to its rotation and rises above the side wall 1a of the rotating container 1 and reaches the fixed cover 2, the inertial force of the grinding medium 3 causes the guide vanes 4 on the inner surface of the fixed cover 2 to move upward.
This device moves inward along the rotary container 1 and falls down to crush the crushed material 6 in the rotary container 1, which is supplied from the crushed material input chute 5 provided at the top of the fixed cover 2.

この種粉砕装置は被粉砕物6を空気流7に乗せ
て固定カバー2の中央部に接続されたダクト8よ
り機外へ排出するもので、回転容器1の回転を許
容するために固定カバー2との間に間隙9を設け
る必要がある反面、被粉砕物6がこの間隙9から
機外へ飛び出すのを防止するためにできるだけそ
の間隙を小さくしなければならない。
This type of crusher carries the material to be crushed 6 in an air flow 7 and discharges it outside the machine through a duct 8 connected to the center of a fixed cover 2.In order to allow rotation of the rotating container 1, the fixed cover 2 While it is necessary to provide a gap 9 between the two, the gap must be made as small as possible to prevent the material to be crushed 6 from flying out of the machine through the gap 9.

しかし粉砕を行なうに必要な回転速度では、容
器内の被粉砕物に加わる遠心力がかなり大きく、
上述のシール部の隙間を小さくすると、この間隙
9の近傍の被粉砕物6には機外へ飛び出そうとす
る大きな遠心力が作用しているので、間隙9に被
粉砕物6が付着したり、粉砕媒体であるスチール
ボールの破片その他の異物が噛み込むなどのため
に安定した連続運転ができないという欠点があ
る。一方、隙間を大きくすると、大量の空気をこ
こから吸引しなければ粒子の飛び出しを防止でき
ないので、大きな圧力損失を招くことになる。こ
のように、被粉砕物は上部の固定カバーから誘引
空気と共に排出されるが、間隙9のシール部が問
題となるのである。
However, at the rotational speed required for pulverization, the centrifugal force exerted on the material to be pulverized in the container is quite large.
When the above-mentioned seal gap is made small, a large centrifugal force is acting on the object 6 to be crushed near the gap 9 so that it tends to fly out of the machine, so the object 6 to be crushed does not stick to the gap 9. However, there is a drawback that stable continuous operation cannot be performed because fragments of the steel balls used as the grinding medium and other foreign objects get caught. On the other hand, if the gap is made large, particles cannot be prevented from flying out unless a large amount of air is sucked through the gap, resulting in a large pressure loss. In this way, the material to be crushed is discharged from the upper fixed cover together with the induced air, but the sealing portion of the gap 9 poses a problem.

また被粉砕物6を空気流7に乗せて上方へ排出
させるためには、風量の大きい圧力の高い送風機
が必要となり省エネルギーの観点からも好ましく
ない。
Further, in order to carry the material 6 to be crushed in the air flow 7 and discharge it upward, a blower with a large air volume and high pressure is required, which is not preferable from the viewpoint of energy saving.

本発明は上述の問題点の解決を図るためになさ
れたもので、回転容器と固定カバーとの間隙を従
来の装置に較べ大きくし、かつ被粉砕物の機外へ
の排出を少ない動力でもつて可能にする円錐形ボ
ールミルを提供することを目的とし、その特徴と
するところは、回転容器と固定カバーの間隙を粉
砕媒体径より小さく被粉砕物径より大きくする程
度に設け、前記回転容器の傾斜側壁に被粉砕物排
出用スリツトを穿設すると共に、上記回転容器と
固定カバー全体を包囲するケーシングを備え、こ
のケーシングと前記回転容器の側壁との間に被粉
砕物を搬送する手段を介在させたことである。
The present invention has been made in order to solve the above-mentioned problems, and the gap between the rotating container and the fixed cover is made larger than that of conventional devices, and the material to be crushed can be discharged to the outside of the machine with less power. The purpose of the present invention is to provide a conical ball mill that enables the rotation of the rotary container and the fixed cover to have a gap smaller than the diameter of the grinding medium and larger than the diameter of the object to be crushed. A slit for discharging the material to be crushed is bored in the side wall, and a casing is provided that completely surrounds the rotating container and the fixed cover, and a means for conveying the material to be crushed is interposed between the casing and the side wall of the rotating container. That's what happened.

以下本発明を実施例に基づいて詳細に説明す
る。
The present invention will be described in detail below based on examples.

第2図は本発明の粉砕装置10の全体断面図
で、容器枠材11とそれに内張されたライナー1
2で構成されるほゞ逆円錐台形の回転容器1は、
粉砕媒体3(スチールボール、スチール製シルペ
ブ等)を内蔵していて、その底部下面に垂直に固
着され軸受14で支承された回転軸13、減速装
置15を介して電動機16で回転駆動される。
FIG. 2 is an overall sectional view of the crushing device 10 of the present invention, showing a container frame 11 and a liner 1 lined therewith.
The rotating container 1 having a substantially inverted truncated cone shape is composed of:
It has a built-in grinding medium 3 (steel balls, steel sill peb, etc.), and is rotatably driven by an electric motor 16 via a rotary shaft 13 fixed vertically to the lower surface of the bottom and supported by a bearing 14, and a speed reduction device 15.

なお、上述のライナー12には第3図に示すよ
うなスリツト17が穿設されている。そのスリツ
ト17が穿設されている傾斜壁1aの傾斜は直鎖
状であつても曲線状であつてもよい。
Incidentally, the above-mentioned liner 12 is provided with a slit 17 as shown in FIG. The slope of the inclined wall 1a in which the slit 17 is formed may be linear or curved.

回転容器1の直上には間隙9を隔てゝ固定カバ
ー2が機枠18に固定され、この間隙9は機内の
気密性を保持させるために小さくするという必要
はなく、粉砕媒体3が飛び出さない程度の寸法に
定められている。
A fixed cover 2 is fixed to the machine frame 18 directly above the rotating container 1 with a gap 9 in between, and this gap 9 does not need to be made small in order to maintain airtightness inside the machine, so that the grinding media 3 will not fly out. The dimensions are determined as follows.

上述の固定カバー2には第4図に示すように案
内羽根4が付設され、固定カバー2の中央部には
被粉砕物6を投入するシユート5と、このシユー
ト5の外周に空気吸引用のダクト8が設置されて
いる。
The above-mentioned fixed cover 2 is provided with guide vanes 4 as shown in FIG. 4, and the fixed cover 2 has a chute 5 in the center thereof into which the material to be crushed 6 is fed, and a chute 5 on the outer periphery of the chute 5 for air suction. A duct 8 is installed.

加えて、上述の回転容器1と固定カバー2の全
体を包囲するケーシング19が、前記機枠18に
貼設され、円錐形ミルは外気と隔絶されている。
第2図の実施例では、前記ケーシング19と回転
容器1の間にエアスライデイングコンベア20が
環状かつ傾斜するごとく介装されていて、その最
下位置にシユート21がケーシング19を貫通し
て設置されている。
In addition, a casing 19 that completely surrounds the rotating container 1 and the fixed cover 2 described above is attached to the machine frame 18, and the conical mill is isolated from the outside air.
In the embodiment shown in FIG. 2, an air sliding conveyor 20 is interposed between the casing 19 and the rotating container 1 in an annular and inclined manner, and a chute 21 is installed at the lowest position passing through the casing 19. has been done.

次に、本発明の粉砕装置の運転について記載す
る。
Next, the operation of the crushing apparatus of the present invention will be described.

予め粉砕媒体3が装入されている回転容器1が
電動機16で駆動されると、粉砕媒体3は遠心力
を受け回転容器1の傾斜側壁1aを上昇する。傾
斜側壁1aの上端に達した粉砕媒体3は、その保
有する慣性力により回転容器1の上部を覆うよう
に設置された固定カバー2に衝突し、固定カバー
2にとりつけられた複数の案内羽根4に誘導され
て中央部へ移動し、ついで案内羽根4から離れて
落下し回転容器1へ戻る。被粉砕物6は固定カバ
ー2の中央部に設けられたシユート5を経て回転
容器1内に供給され、回転容器1の底部で上述の
案内羽根4を離れて落下する粉砕媒体3の循環挙
動により衝撃粉砕される。さらに粉砕媒体3と共
に回転容器1の傾斜側壁1aを移動する際に粉砕
媒体3と傾斜側壁1a間、あるいは粉砕媒体3間
に挟まれることにより主として摩擦粉砕される。
When the rotating container 1 in which the grinding medium 3 is charged in advance is driven by the electric motor 16, the grinding medium 3 is moved up the inclined side wall 1a of the rotating container 1 under the influence of centrifugal force. The grinding medium 3 that has reached the upper end of the inclined side wall 1a collides with the fixed cover 2 installed to cover the upper part of the rotating container 1 due to its inertia force, and a plurality of guide vanes 4 attached to the fixed cover 2 collide with the fixed cover 2 installed to cover the upper part of the rotating container 1. The guide blade 4 moves to the center, then falls away from the guide vane 4 and returns to the rotating container 1. The material to be crushed 6 is supplied into the rotary container 1 through a chute 5 provided in the center of the fixed cover 2, and due to the circulation behavior of the crushing medium 3 that leaves the above-mentioned guide vanes 4 and falls at the bottom of the rotary container 1. Shattered by impact. Furthermore, when moving along the inclined side wall 1a of the rotary container 1 together with the grinding medium 3, it is caught between the grinding medium 3 and the inclined side wall 1a or between the grinding media 3, and is mainly subjected to friction pulverization.

ところで、被粉砕物6も粉砕媒体3と共に回転
容器1の傾斜側壁1aを上昇するが、この傾斜側
壁1aには前述の如くスリツト17が穿設されて
いるので、このスリツト17を通過しうる程度に
粉砕された被粉砕物のみが遠心力で回転容器1外
へ放出される。また傾斜側壁1aの上端に達した
被粉砕物で固定カバー2へ上昇する程度までの慣
性力のないものは、上述の間隙9を介して回転容
器1外へ放出される。
Incidentally, the object to be crushed 6 also moves up the inclined side wall 1a of the rotary container 1 together with the grinding medium 3, but since the slit 17 is bored in this inclined side wall 1a as described above, the object 6 moves up the inclined side wall 1a of the rotary container 1. Only the crushed material is discharged outside the rotating container 1 by centrifugal force. Further, objects to be crushed that have reached the upper end of the inclined side wall 1a and do not have enough inertia to rise to the fixed cover 2 are discharged to the outside of the rotary container 1 through the above-mentioned gap 9.

このように放出された被粉砕物6は、回転容器
1の外周に配置されたエアスライデイングコンベ
ア20上に落下し、図示しない送風機より圧送さ
れキヤンバス22を通過した空気23により被粉
砕物6が流動化され、傾斜した環状のエアスライ
デイングコンベア20の下端部に順次搬送されて
シユート21より機外に排出される。なお、回転
容器1とケーシング19間での搬送手段はエアス
ライデイングコンベアに限ることはなく、公知の
スクレーパーによるものであつてもよい。上述の
エアスライデイングコンベア20を採用したとき
は、図示しない集塵機や誘引送風機に連結してい
るダクト8より機内の空気を吸引すると、回転容
器1と固定カバー2に囲まれる粉砕機本体内部
と、ケーシング19とエアスライデイングコンベ
ア20に囲まれる空間は、負圧に保持され、粉塵
の機外への飛散が防止される。このときダクト8
を経て気流に乗つて排出される若干の被粉砕物
は、集塵機で捕集される。なお、回転容器1とエ
アスライデイングコンベア20との間は、回転容
器1の回転を許容する程度の間隙があれば十分で
ある。
The material to be crushed 6 thus discharged falls onto an air sliding conveyor 20 arranged around the outer periphery of the rotary container 1, and the material to be crushed 6 is crushed by the air 23 that has been force-fed by a blower (not shown) and passed through the canvas 22. The fluidized material is sequentially conveyed to the lower end of the inclined annular air sliding conveyor 20 and discharged from the machine through the chute 21. Note that the conveying means between the rotating container 1 and the casing 19 is not limited to an air sliding conveyor, and may be a known scraper. When the above-mentioned air sliding conveyor 20 is adopted, when the air inside the machine is sucked through the duct 8 connected to a dust collector or induced blower (not shown), the inside of the crusher body surrounded by the rotating container 1 and the fixed cover 2, The space surrounded by the casing 19 and the air sliding conveyor 20 is maintained at a negative pressure to prevent dust from scattering outside the machine. At this time, duct 8
Some of the crushed materials that are discharged along with the airflow are collected by a dust collector. Note that it is sufficient that there is a gap between the rotating container 1 and the air sliding conveyor 20 that allows rotation of the rotating container 1.

上述した回転容器1の傾斜側壁1aに穿設され
たスリツト17は被粉砕物6の排出に適切な形状
であればよく、第3図は円弧状のスリツトを示
す。なお、このスリツトは傾斜側壁1aの全面に
設けてもよいが、第3図の如くスリツトのないラ
イナー12aとスリツトを有するライナー12b
を交互に設けてもよい。この場合スリツトのない
ライナー12aの面では粉砕媒体3の上昇が円滑
に行われ都合がよい。
The slit 17 formed in the inclined side wall 1a of the rotary container 1 described above may have any shape as long as it is suitable for discharging the material to be crushed 6, and FIG. 3 shows an arcuate slit. Note that this slit may be provided on the entire surface of the inclined side wall 1a, but as shown in FIG.
may be provided alternately. In this case, the surface of the liner 12a without slits allows the grinding media 3 to rise smoothly, which is convenient.

次に、第5および第6図には上述した円錐形ミ
ルを適用した粉砕プラント設備の例を示す。第5
図において、シユート31を経て供給される被粉
砕物は単室チユーブミル32で粗粉砕され、エレ
ベータ33でもつてセパレータ34に搬送され
る。分級された精粉はシユート35を経て次の工
程へ、粗粉はシユート36を介し本発明の微粉砕
用粉砕装置10である円錐形ミルにシユート5か
ら投入される。
Next, FIGS. 5 and 6 show examples of crushing plant equipment to which the above-mentioned conical mill is applied. Fifth
In the figure, the material to be crushed that is supplied through a chute 31 is coarsely crushed in a single-chamber tube mill 32 and conveyed to a separator 34 by an elevator 33. The classified fine powder passes through the chute 35 to the next step, and the coarse powder passes through the chute 36 and is fed into the conical mill, which is the pulverizing device 10 for fine pulverization of the present invention, from the chute 5.

この粉砕装置10の出粉は、シユート37を介
して再びエレベーター33に投入され上述の経路
で分級される。なお、ダクト8より吸引される空
気は集塵機38で除塵されて大気に放出される
が、その時に得られる粉塵を上述のシユート35
からの精粉と共に次工程に送つてもよい。
The powder from the crushing device 10 is fed into the elevator 33 again via the chute 37 and classified through the above-mentioned route. Note that the air sucked through the duct 8 is removed by a dust collector 38 and released into the atmosphere, and the dust obtained at that time is sent to the above-mentioned chute 35.
It may be sent to the next process together with the refined powder.

このような配置にすると、粗粉砕過程を衝撃力
が支配的なチユーブミルで効率よく行ない、その
中から微粉を取り除いたあと、磨砕力が支配的な
本発明の粉砕機により微粉を生成することがで
き、システム全体の粉砕効率を向上させることが
できる。
With this arrangement, the coarse pulverization process can be efficiently carried out using a tube mill in which impact force is dominant, and after removing fine powder therefrom, fine powder can be generated by the pulverizer of the present invention in which grinding force is dominant. This can improve the grinding efficiency of the entire system.

第6図は上述と異なる設備例で、2室チユーブ
ミル39と組合せたものである。前述の例と異な
るところはセパレータ34からの戻り粉の一部が
シユート36aを介して原料投入シユート31へ
戻されることであり、微粉砕用の粉砕装置10で
ある円錐ミルの出粉を分級するセパレータ40と
そこへ搬送するエレベータ41をもう1つ設けた
ことである。このような配置にすると、2室チユ
ーブミル39の内部の被粉砕物の保有量を微粉生
成に最適のレベルに維持することができること、
および既設のチユーブミル39、セパレータ34
の粉砕能力を増強させる必要がある際の改良が比
較的簡単に行なうことができる利点がある。
FIG. 6 shows an example of equipment different from that described above, which is combined with a two-chamber tube mill 39. The difference from the above example is that a part of the returned powder from the separator 34 is returned to the raw material input chute 31 via the chute 36a, and the powder from the conical mill, which is the pulverizing device 10 for fine pulverization, is classified. This is because one more separator 40 and another elevator 41 are provided to transport the separator 40 to the separator 40. With this arrangement, the amount of material to be crushed inside the two-chamber tube mill 39 can be maintained at the optimal level for fine powder production;
and existing tube mill 39, separator 34
It has the advantage that improvements can be made relatively easily when it is necessary to increase the crushing capacity of the machine.

以上詳細に述べたように、本発明は回転容器と
固定カバーの間隙を粉砕媒体径より小さく被粉砕
物径より大きくする程度に設け、前記回転容器の
傾斜側壁に被粉砕物排出用スリツトを穿設すると
共に、上記回転容器と固定カバー全体を包囲する
ケーシングを備え、このケーシングと前記回転容
器の側壁との間に被粉砕物を搬送する手段を介在
させたので粉砕に必要な回転速度では被粉砕物に
加わる遠心力がかなり大きくなるが、シール部の
隙間を小さくすることができる。一方、粉砕され
たものはスリツトから排出されるので、大量の排
出用空気は不要となり、間隙に被粉砕物が付着し
たり、粉砕媒体であるスチールボールの破片その
他の異物が噛み込むなどのことは回避される。ま
た、その間隙から大量の空気を吸引する必要もな
く、大きな圧力損失を招くことはない。このよう
に、円錐ミルの問題点である固定カバーとの間隙
で生ずるトラブルが解消され、また粉塵の機外へ
の飛散を防止できると共に、被粉砕物の排出のた
めの動力が極めて軽減される。加えて円錐ミルの
特徴である粉砕媒体の運動性を高く保たれ、その
ための駆動動力が小さく機全体もコンパクトにな
り、微粉砕に適した衝撃力と摩擦力とを利用した
複合粉砕が可能となる。
As described in detail above, the present invention provides a gap between the rotating container and the fixed cover to an extent that is smaller than the diameter of the grinding medium and larger than the diameter of the object to be crushed, and a slit for discharging the object to be crushed is bored in the inclined side wall of the rotating container. In addition, a casing is provided that surrounds the rotating container and the fixed cover, and a means for conveying the material to be crushed is interposed between the casing and the side wall of the rotating container, so that the material cannot be crushed at the rotational speed necessary for pulverization. Although the centrifugal force applied to the pulverized material becomes considerably large, the gap between the seal parts can be reduced. On the other hand, since the pulverized material is discharged through the slit, there is no need for a large amount of exhaust air, which can prevent the pulverized material from adhering to the gap or biting of pieces of the steel balls used as the pulverizing medium or other foreign matter. is avoided. Further, there is no need to suck a large amount of air through the gap, and no large pressure loss is caused. In this way, the problems caused by the gap between the fixed cover and the conical mill are eliminated, dust is prevented from scattering outside the machine, and the power required to discharge the material to be crushed is significantly reduced. . In addition, the high mobility of the grinding media, which is a characteristic of conical mills, is maintained, and the drive power is small and the entire machine is compact, making it possible to perform complex grinding using impact force and frictional force, which are suitable for fine grinding. Become.

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

第1図は円錐ミルの従来例の要部断面図、第2
図は本発明の粉砕装置の全体断面図、第3図は第
2図の―線矢視図、第4図は第2図の―
線矢視図であり、第5図および第6図は本発明の
粉砕装置を適用したプラント設備例である。 1…回転容器、1a…傾斜側壁、2…固定カバ
ー、3…粉砕媒体、4…案内羽根、8…ダクト、
9…間隙、13…回転軸、17…スリツト、19
…ケーシング、20…エアスライデイングコンベ
ア。
Figure 1 is a sectional view of the main part of a conventional conical mill, Figure 2
The figure is an overall sectional view of the crushing device of the present invention, FIG. 3 is a view taken along the line shown in FIG. 2, and FIG. 4 is a view taken along the line shown in FIG.
5 and 6 are examples of plant equipment to which the crushing apparatus of the present invention is applied. DESCRIPTION OF SYMBOLS 1... Rotating container, 1a... Inclined side wall, 2... Fixed cover, 3... Grinding medium, 4... Guide vane, 8... Duct,
9... Gap, 13... Rotating shaft, 17... Slit, 19
...Casing, 20...Air sliding conveyor.

Claims (1)

【特許請求の範囲】 1 垂直軸回りに回転するほゞ逆円錐台形状の回
転容器と、この回転容器の上部を覆う如く配設さ
れかつ内部に案内羽根を付設した固定カバーとを
有し、粉砕媒体の循環挙動により粉砕を行う円錐
形ミルにおいて、前記回転容器と固定カバーの間
隙を粉砕媒体径より小さく被粉砕物径より大きく
する程度に設け、前記回転容器の傾斜側壁に被粉
砕物排出用スリツトを穿設すると共に、上記回転
容器と固定カバー全体を包囲するケーシングを備
え、このケーシングと前記回転容器の側壁との間
に被粉砕物を搬送する手段を介在させたことを特
徴とする粉砕装置。 2 前記被粉砕物搬送手段は傾斜した環状のエア
スライデイングコンベアであることを特徴とする
特許請求の範囲第1項記載の粉砕装置。 3 前記ケーシングのほゞ中心部にこのケーシン
グ内の圧力を大気圧よりやゝ低く保つ程度に空気
を吸引するダクトを突設させたことを特徴とする
特許請求の範囲第1項または第2項記載の粉砕装
置。 4 前記スリツトが前記回転容器の傾斜側壁の一
部に穿設されていることを特徴とする特許請求の
範囲第1項から第3項のいずれかに記載の粉砕装
置。
[Scope of Claims] 1. A rotating container having a substantially inverted truncated conical shape that rotates around a vertical axis, and a fixed cover disposed to cover the upper part of the rotating container and having guide vanes attached therein, In a conical mill that performs pulverization by the circulation behavior of a pulverizing medium, the gap between the rotating container and the fixed cover is set to be smaller than the diameter of the pulverizing medium and larger than the diameter of the object to be crushed, and the object to be crushed is discharged onto the inclined side wall of the rotating container. The present invention is characterized in that it includes a casing which is provided with a slit and which surrounds the entire rotary container and the fixed cover, and a means for conveying the material to be crushed is interposed between the casing and the side wall of the rotary container. Grinding equipment. 2. The crushing apparatus according to claim 1, wherein the means for conveying the crushed material is an inclined annular air sliding conveyor. 3. Claims 1 or 2, characterized in that a duct for sucking air is provided at substantially the center of the casing to maintain the pressure inside the casing slightly lower than atmospheric pressure. Grinding equipment as described. 4. The crushing device according to any one of claims 1 to 3, wherein the slit is formed in a part of an inclined side wall of the rotating container.
JP9558081A 1981-06-20 1981-06-20 Crusher Granted JPS57209649A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP9558081A JPS57209649A (en) 1981-06-20 1981-06-20 Crusher
US06/389,145 US4504020A (en) 1981-06-20 1982-06-16 Pulverizing mill apparatus
DE19823222890 DE3222890A1 (en) 1981-06-20 1982-06-18 POWDER MILL DEVICE
FR8210724A FR2507925B1 (en) 1981-06-20 1982-06-18 SPRAYER
DE19828217579U DE8217579U1 (en) 1981-06-20 1982-06-18 POWDER MILL DEVICE
DK275182A DK275182A (en) 1981-06-20 1982-06-18 APPLIANCES FOR PULVERIZING SOLID MATERIALS FOR EXCHANGE CEMENTS INCLUDING ABOUT A Vertical Axis Rotating Conical Container
GB08217959A GB2100618B (en) 1981-06-20 1982-06-21 Pulverizing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9558081A JPS57209649A (en) 1981-06-20 1981-06-20 Crusher

Publications (2)

Publication Number Publication Date
JPS57209649A JPS57209649A (en) 1982-12-23
JPS6119307B2 true JPS6119307B2 (en) 1986-05-16

Family

ID=14141526

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9558081A Granted JPS57209649A (en) 1981-06-20 1981-06-20 Crusher

Country Status (1)

Country Link
JP (1) JPS57209649A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6362559A (en) * 1986-09-03 1988-03-18 宇部興産株式会社 Centrifugal fluidzing crusher
US4830289A (en) * 1987-08-27 1989-05-16 Ube Industries, Ltd. Centrifugal fluidized grinding apparatus

Also Published As

Publication number Publication date
JPS57209649A (en) 1982-12-23

Similar Documents

Publication Publication Date Title
JP2666097B2 (en) Slag crushing equipment
WO2003097242A1 (en) Grinder
JPH04222646A (en) Device for treating output material from crushing device
US4504020A (en) Pulverizing mill apparatus
US4813619A (en) Disintegrator having grinding chamber with rotors including carrying disk with grinding wheels concentrically arranged thereon
CN206168550U (en) Hierarchical recycle system of cement particle
JPS6119307B2 (en)
JP3074656B2 (en) Crushing equipment
JPS604598Y2 (en) vertical mill
JP3832095B2 (en) Crusher
JPH0576793A (en) Pulverizing equipment
JP2622909B2 (en) Vertical crusher
JPH02265660A (en) Centrifugal flow crusher
US2821344A (en) Self-classifying pulverizer
JPS6043776B2 (en) Grinding equipment
JPH0331099B2 (en)
JPH0593558U (en) Preliminary crusher
JPS601804Y2 (en) vertical mill
KR870002126B1 (en) Pulverization method
JPS6327984B2 (en)
JPS6327985B2 (en)
JP2594829B2 (en) Centrifugal flow crusher
JPH0256941B2 (en)
JPH0131422B2 (en)
JPS6136457B2 (en)