JPH0538464A - Slag crushing equipment - Google Patents

Slag crushing equipment

Info

Publication number
JPH0538464A
JPH0538464A JP3280922A JP28092291A JPH0538464A JP H0538464 A JPH0538464 A JP H0538464A JP 3280922 A JP3280922 A JP 3280922A JP 28092291 A JP28092291 A JP 28092291A JP H0538464 A JPH0538464 A JP H0538464A
Authority
JP
Japan
Prior art keywords
slag
crushing
rotary table
separator
iron
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
JP3280922A
Other languages
Japanese (ja)
Other versions
JP2666097B2 (en
Inventor
Kazutoshi Hisaie
和利 久家
Yurio Kasai
百合夫 笠井
Kazuki Kuranari
和樹 蔵成
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.)
Ube Corp
Original Assignee
Ube 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 Ube Industries Ltd filed Critical Ube Industries Ltd
Priority to JP3280922A priority Critical patent/JP2666097B2/en
Publication of JPH0538464A publication Critical patent/JPH0538464A/en
Application granted granted Critical
Publication of JP2666097B2 publication Critical patent/JP2666097B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Disintegrating Or Milling (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Electrostatic Separation (AREA)
  • Crushing And Grinding (AREA)

Abstract

(57)【要約】 【目的】 原料スラグ中の鉄粒を粉砕中効率良く,か
つ,純度の高い状態で取り出し回収するとともに,粉砕
部の摩耗量を低減したスラグ粉砕設備を提供する。 【構成】 竪型粉砕機1とバケットエレベータ60とマ
グネットセパレータ70と鉄粒・スラグ粉分離機90と
集塵装置110とを含むスラグ粉砕設備であって,該鉄
粒・スラグ粉分離機90は内面に耐摩耗材を内張りさせ
た少なくとも1つ以上の傾斜管を備えた構成とした。
(57) [Summary] [Purpose] To provide a slag crushing facility in which the iron particles in the raw material slag are efficiently extracted during crushing and are collected in a highly pure state, and the wear amount of the crushing part is reduced. [Structure] A slag crushing equipment including a vertical crusher 1, a bucket elevator 60, a magnet separator 70, an iron particle / slag powder separator 90, and a dust collector 110, wherein the iron particle / slag powder separator 90 is At least one inclined tube having an abrasion resistant material lined on its inner surface was provided.

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,回転テーブルと粉砕ロ
ーラとの協働により,高炉スラグなどの原料を粉砕する
竪型粉砕機からなる粉砕設備であり,特に原料スラグ中
に含有する鉄粒を除去しつつ粉砕する粉砕設備に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pulverizing equipment comprising a vertical pulverizer for pulverizing a raw material such as blast furnace slag by cooperation of a rotary table and a pulverizing roller, and particularly iron particles contained in the raw slag. The present invention relates to a crushing equipment for crushing while removing the slag.

【0002】[0002]

【従来の技術】石灰石や高炉スラグ,セメント原料など
の原料を細かく粉砕し粉体とする粉砕機の一種として,
図2に示すように,回転テーブルと粉砕ローラとを備え
た竪型粉砕機1が広く用いられている。この種の粉砕機
は,円筒状ケーシング1aの下部においてモータ2Aに
より減速機2で駆動されて低速回転する円盤状の回転テ
ーブル3Aと,その上面外周部を円周方向へ等分する箇
所に油圧などで圧接されて従動回転する複数個の粉砕ロ
ーラ4とを備えている。
2. Description of the Related Art As a kind of crusher for finely crushing raw materials such as limestone, blast furnace slag, and cement raw material into powder,
As shown in FIG. 2, a vertical crusher 1 having a rotary table and a crushing roller is widely used. This type of crusher has a disk-shaped rotary table 3A which is driven by a motor 2A at a lower portion of a cylindrical casing 1a and rotates at a low speed at a lower portion of a cylindrical casing 1a, and a hydraulic pressure is applied to a portion which equally divides an outer peripheral portion of an upper surface thereof in a circumferential direction. And a plurality of crushing rollers 4 that are driven to rotate by being pressed against each other.

【0003】粉砕ローラ4はケーシング1aの下部に配
設される柱脚20の上面に積載された軸受8の軸6によ
って揺動自在に軸支されたボス5とアーム7を介して油
圧シリンダ9のピストンロッド10に連結されており,
油圧シリンダ9を作動させることにより,粉砕ローラ4
を回転テーブル3A上に押圧して原料への粉砕圧力を与
えている。3Bは回転テーブル3Aの外周縁に設けられ
原料層圧を調整するダムリング,14は回転テーブル3
A周囲のガス吹上用の環状空間通路,14Aはガスダク
ト,15はケーシング,13は羽根13Aにより粉砕さ
れた原料を分級する回転セパレータ,16はガスと共に
製品を取り出す排出口,17は原料投入シュートであ
る。
The crushing roller 4 is provided with a hydraulic cylinder 9 via a boss 5 and an arm 7 which are swingably supported by a shaft 6 of a bearing 8 mounted on the upper surface of a column base 20 arranged in the lower part of the casing 1a. Is connected to the piston rod 10 of
By operating the hydraulic cylinder 9, the crushing roller 4
Is pressed on the rotary table 3A to apply a crushing pressure to the raw material. 3B is a dam ring provided on the outer peripheral edge of the rotary table 3A for adjusting the raw material layer pressure, and 14 is a rotary table 3
An annular space passage for blowing gas around A, 14A is a gas duct, 15 is a casing, 13 is a rotary separator for classifying the raw material crushed by blades 13A, 16 is an outlet for taking out the product together with gas, and 17 is a raw material charging chute. is there.

【0004】このような竪型粉砕機において,回転テー
ブル3Aの中央部へ原料投入シュート17で供給された
原料は,回転テーブル3Aの回転によりテーブル半径方
向の遠心力を受けて回転テーブル3A上を滑るときに回
転テーブル3Aにより回転方向の力を受け,回転テーブ
ル3Aとの間で滑って回転テーブル3Aの回転数よりい
くらか遅い回転を行なう。以上2つの力,すなわち,半
径方向と回転方向の力とが合成され,原料は回転テーブ
ル3A上を渦巻状の軌跡を描いて回転テーブル3Aの外
周部へ移動する。この外周部には,ローラが圧接されて
回転しているので,渦巻線を描いた原料は粉砕ローラ4
と回転テーブル3Aとの間へローラ軸方向とある角度を
なす方向から進入して噛み込まれて粉砕される。
In such a vertical crusher, the raw material supplied to the central portion of the rotary table 3A by the raw material chute 17 is subjected to centrifugal force in the radial direction of the table due to the rotation of the rotary table 3A, so that the raw material moves on the rotary table 3A. When sliding, it receives a force in the direction of rotation by the rotary table 3A and slides between itself and the rotary table 3A to perform rotation that is somewhat slower than the rotational speed of the rotary table 3A. The above two forces, that is, the force in the radial direction and the force in the rotation direction are combined, and the raw material moves to the outer peripheral portion of the rotary table 3A in a spiral trajectory on the rotary table 3A. A roller is pressed against the outer periphery of the crushing roller 4 to rotate, so that the raw material of which the spiral is drawn is the crushing roller 4.
Between the rotating table 3A and the rotary table 3A from a direction forming an angle with the roller axis direction, and is bitten and crushed.

【0005】一方,ケーシング1aの基部にはダクトに
よって空気,あるいは熱風などのガスが導かれており,
このガスが回転テーブル3Aの外周面とケーシングの内
周面との間の環状空間通路14から吹き上がることによ
り,粉砕された微粉体はガスに同伴されてケーシング1
a内を上昇し,上部に位置するセパレータ13の羽根1
3Aにより分級作用を受け,所定粒度の製品はガスと共
に排出口16から排出され次の工程へ送られる。
On the other hand, a duct introduces air or gas such as hot air into the base of the casing 1a.
This gas is blown up from the annular space passage 14 between the outer peripheral surface of the rotary table 3A and the inner peripheral surface of the casing, so that the pulverized fine powder is entrained in the gas and the casing 1
blades 1 of the separator 13 located in the upper part of the separator 1
The product having a predetermined particle size is subjected to the classification action by 3A and is discharged together with the gas from the discharge port 16 and sent to the next step.

【0006】しかし,原料中に含有される鉄片,ボル
ト,ナット等の異物は回転テーブル3Aをオーバフロー
しても環状空間通路を上昇してくる気流よりも重力が打
ち克ってそのまま回転テーブル3Aの下方に設けた異物
排出口から機外へ排出される。また,原料中の大径粒子
も同様に上昇気流に乗ることが出来ずにそのまま異物排
出口から落下する。この落下する粒径の制御は上昇気流
の連度,すなわち,ミル通過風量によって行なうことが
できる。スラグ粉砕の場合には直径1mm〜2mmの鉄
粒が粉砕産物の中に多く混在するので比較的風量を少な
くしてこれらの粒径のものも異物排出口から排出させ
る。
However, even if foreign matter such as iron pieces, bolts and nuts contained in the raw material overflows the rotary table 3A, the gravity overcomes the air flow rising in the annular space passage and the rotary table 3A remains in that state. The foreign matter is discharged from the foreign matter discharge port provided below. In addition, large particles in the raw material cannot fall into the ascending air flow and fall directly from the foreign matter discharge port. The falling particle size can be controlled by the continuity of the ascending airflow, that is, the air volume passing through the mill. In the case of slag crushing, iron particles having a diameter of 1 mm to 2 mm are mixed in the crushed product in a large amount, so the amount of air is comparatively reduced and particles having these particle sizes are also discharged from the foreign matter discharge port.

【0007】[0007]

【発明が解決しようとする課題】竪型粉砕機でスラグを
粉砕する場合には,竪型粉砕機の異物排出口から出た粗
粒を機外のバケットエレベータを経由して竪型粉砕機へ
ニューフィードのスラグとともに再循環させて,さらに
粉砕するが,これらの再循環させるスラグの中に直径1
〜2mm程度の黒色の球状の鉄粒(主成分は酸化鉄)が
多く混入しており,竪型粉砕機内の粉砕部,すなわち,
粉砕ローラやテーブルライナの摩耗が著しく進行するば
かりでなく,運転中の発生振動の振幅値が大きく安定し
た運転を阻害していた。
When slag is crushed by a vertical crusher, coarse particles discharged from a foreign matter discharge port of the vertical crusher are passed to a vertical crusher via a bucket elevator outside the machine. It is recirculated with Newfeed slag and further crushed.
A lot of black spherical iron particles (mainly iron oxide) of about 2 mm are mixed, and the crushing part in the vertical crusher, that is,
Not only was the abrasion of the crushing rollers and table liner significantly progressed, but the amplitude value of the generated vibration during operation was large, which hindered stable operation.

【0008】一方,この鉄粒は純度が高く小粒径で,か
つ,形状がほぼ球形で粒がそろっており,これらをショ
ット・ブラスト用の鋼球として再利用することで,近年
特に需要が多くなってきた。したがって,スラグ粉中か
らこれらの鉄粒を簡便な方法で如何に効率良く,かつ,
純度の高い状態で取り出せるかが重要な課題であった。
しかしながら,これらの鉄粒が異物排出口に設置される
気密用(エヤシール用)の二重ダンパやバケットエレベ
ータを経てマグネットセパレータに至る輸送系路で,鉄
粒の周りにスラグ粉が付着し,マグネットセパレータで
捕捉されて排出される時点ではスラグ粉と鉄粒との重量
割合は50%〜50%となることもあり,ショットブラ
スト用として利用し販売するためには,再度鉄粒から微
粉スラグを除去するための分離処理を施す必要があり,
そのための設備や工程が必要となるばかりでなく,スグ
ラ粉の収率が低くなる等の不利益も生じていた。
On the other hand, the iron particles have a high purity and a small particle size, and the shape is almost spherical, and the particles are aligned, and by reusing them as steel balls for shot blasting, there is a particular demand in recent years. It's getting more and more. Therefore, how efficiently and efficiently these iron particles can be obtained from the slag powder, and
The important issue was how to take it out in a highly pure state.
However, slag powder adheres to the iron particles around the iron particles in the transportation system where these iron particles pass through the airtight (air seal) double damper installed in the foreign matter discharge port or the bucket elevator and the magnet separator. The weight ratio of the slag powder to the iron particles may be 50% to 50% at the time of being captured by the separator and discharged, and in order to use and sell it for shot blasting, fine slag powder from iron particles is again used. It is necessary to perform a separation process to remove
Not only is equipment and processes required for that purpose, but there are also disadvantages such as a low yield of sugla powder.

【0009】[0009]

【課題を解決するための手段】本発明のスラグ粉砕設備
は上記の課題を解決するため,回転テーブルの外周部上
面に複数個の回転自在な粉砕ローラを配設するととも
に,粉砕ローラを回転テーブルへ押圧する油圧シリンダ
を備え,原料投入シュートを経由して回転テーブル上へ
供給したスラグ等の原料を粉砕ローラに所定の粉砕圧力
を与えて回転テーブル上面と粉砕ローラ周面との間で粉
砕し竪型粉砕機上部の分級機で分級した精粉を空気搬送
により排出する竪型粉砕機と,竪型粉砕機の回転テーブ
ルを溢流して排出された粗粒を垂直輸送するバケットエ
レベータと,バケットエレベータの排出口の直下に設け
たマグネットセパレータと,マグネットセパレータで捕
集され排出されたスラグ含有中の鉄粒を排出する垂直管
の途中に設けられた鉄粒・スラグ粉分離機と,前記竪型
粉砕機の精粉および前記垂直管内の微粉を集塵する集塵
装置とを含むスラグ粉砕設備であって,前記鉄粒・スラ
グ粉分離機は,内面に耐摩耗材が内張りされ,かつ,少
なくとも1つ以上の傾斜管を備えた構成とした。
In order to solve the above-mentioned problems, the slag crushing equipment of the present invention is provided with a plurality of rotatable crushing rollers on the upper surface of the outer periphery of the rotary table, and the crushing rollers are provided on the rotary table. It is equipped with a hydraulic cylinder that presses the slag and other raw materials that have been supplied onto the rotary table via the raw material charging chute, and applies a predetermined pulverizing pressure to the pulverizing roller to pulverize between the upper surface of the rotating table and the peripheral surface of the pulverizing roller. A vertical crusher that discharges the fine powder classified by the classifier above the vertical crusher by air transfer, a bucket elevator that vertically transports the coarse particles discharged by overflowing the rotary table of the vertical crusher, and a bucket It was installed in the middle of the magnet separator installed directly under the elevator discharge port and the vertical pipe that discharges the iron particles contained in the slag collected and discharged by the magnet separator. What is claimed is: 1. A slag crushing facility including a grain / slag powder separator, and a dust collector that collects the fine powder of the vertical crusher and the fine powder in the vertical pipe, wherein the iron grain / slag powder separator has an inner surface. A wear resistant material is lined inside and at least one inclined pipe is provided.

【0010】[0010]

【作用】本発明の粉砕設備は,原料ホッパのスラグがコ
ンスタントフィード・ウエアを介して竪型粉砕機へ供給
され,粉砕されてミル頂部のセパレータで分級され精粉
は空気搬送されて集塵装置で回収される。一方,回転テ
ーブル上で粉砕されない鉄粒は粗粒とともに回転テーブ
ル下の異物排出口および二重ダンパを経由して,バケッ
トエレベータで垂直輸送された後,マグネットセパレー
タで原料スラグから鉄粒のみ磁力選別され,垂直管を下
方へ落下する。このとき垂直管の途中に設けた鉄粒・ス
ラグ粉分離機によってその落下する衝撃力を利用して鉄
粒の周りのスラグ粉は鉄粒から剥離し,分離機と集塵装
置とを接続した配管によってファンの吸引力によりスラ
グ微粉のみ集塵装置に回収される。一方,マグネットセ
パレータで鉄粒を除去されたスラグの粗粒はベルトコン
ベヤ等の輸送手段により再び竪型粉砕機へ供給され粉砕
される。
In the crushing equipment of the present invention, the slag of the raw material hopper is supplied to the vertical crusher through the constant feed wear, crushed and classified by the separator at the top of the mill, and the fine powder is conveyed by air to collect the dust. Will be collected at. On the other hand, iron particles that are not crushed on the rotating table are transported vertically along with coarse particles through a foreign matter discharge port under the rotating table and a double damper in a bucket elevator, and then only the iron particles are magnetically separated from the raw slag by a magnet separator. Then, the vertical pipe falls down. At this time, the slag powder around the iron particles was separated from the iron particles by using the falling impact force of the iron particle / slag powder separator installed in the middle of the vertical pipe, and the separator and dust collector were connected. Only the fine slag powder is collected in the dust collector by the suction force of the fan through the pipe. On the other hand, the coarse particles of the slag from which the iron particles have been removed by the magnet separator are again supplied to the vertical crusher by a transportation means such as a belt conveyor and crushed.

【0011】[0011]

【実施例】以下本発明の実施例について図面に基づいて
詳細に説明する。図1〜図2は本発明に係る実施例を示
し,図1はスラグ粉砕設備の全体フローシート,図2は
鉄粒・スラグ粉分離機の縦断面図,図3は鉄粒・スラグ
粉分離機の他の実施例を示す側面図である。図におい
て,1は竪型粉砕機,30は原料ホッパ,40はコンス
タントフィード・ウエア,50は二重ダンパで函体内に
一方が開状態のときもう一方が閉状態となるように作動
して外気の侵入を防ぎつつ,固体粒状物を排出できる構
成とされている。60はバケットエレベータ,70はマ
グネットセパレータ,80は垂直管,90は鉄粒・スラ
グ粉分離機,100はベルトコンベヤ,110は集塵装
置,120は吸引ファンである。なお,竪型粉砕機1の
構造は従来技術で説明したものと同じであるので省略す
る。
Embodiments of the present invention will now be described in detail with reference to the drawings. 1 and 2 show an embodiment according to the present invention, FIG. 1 is an overall flow sheet of a slag crushing equipment, FIG. 2 is a longitudinal sectional view of an iron particle / slag powder separator, and FIG. 3 is an iron particle / slag powder separator. It is a side view showing other examples of a machine. In the figure, 1 is a vertical crusher, 30 is a raw material hopper, 40 is constant feed wear, and 50 is a double damper that operates so that when one is open, the other is closed. It is configured so that solid particulate matter can be discharged while preventing the intrusion of dust. Reference numeral 60 is a bucket elevator, 70 is a magnetic separator, 80 is a vertical tube, 90 is an iron particle / slag powder separator, 100 is a belt conveyor, 110 is a dust collector, and 120 is a suction fan. Since the structure of the vertical crusher 1 is the same as that described in the conventional art, the description thereof is omitted.

【0012】鉄粒・スラグ粉分離機90は鉄粒の周囲に
付着しているスラグ粉を鉄粒から離脱させ,除去する機
能を有し,その構造は,図2に示すように,垂直管80
の途中,主として地面に近い下方に設置され,内面に耐
摩耗性の内張り材90aをコーティングした傾斜管を少
なくとも1個以上有し,この傾斜管に垂直管を接続した
ものである。鉄粒・スラグ粉分離機90内に数m以上の
落差を保持しながら落下してきた鉄粒は傾斜管の内張り
材90aに強く当たり,たとえば,図2に図示した矢印
線のように激しく屈折を繰り返しながら鉄粒・スラグ粉
分離機90内を通過する。このとき内張り材90aに当
接したときの衝撃によって分離した鉄粒表面のスラグ粉
は,吸入管90bにより吸引される空気に随伴して集塵
装置110へ配送される。なお,図3に示すように,円
管の代りに角管を用いSUS鋼板の内張り材90cを傾
斜管の斜面に沿ってスライドできる構造とし,吸入管9
0dを垂直としてもよい。
The iron particle / slag powder separator 90 has a function of separating and removing the slag powder adhering to the periphery of the iron particles from the iron particles, and its structure is as shown in FIG. 80
In the middle of the above, at least one inclined pipe, which is installed mainly below the ground and whose inner surface is coated with a wear-resistant lining material 90a, is provided, and a vertical pipe is connected to this inclined pipe. The iron particles falling into the iron particle / slag powder separator 90 while maintaining a drop of several meters or more strongly hit the lining material 90a of the inclined pipe and are severely refracted as shown by the arrow in FIG. The iron particles / slag powder separator 90 is repeatedly passed. At this time, the slag powder on the surface of the iron particles separated by the impact when it abuts the lining material 90a is delivered to the dust collector 110 along with the air sucked by the suction pipe 90b. As shown in FIG. 3, a square pipe is used instead of the circular pipe, and the lining material 90c of SUS steel plate is slidable along the slope of the inclined pipe.
0d may be vertical.

【0013】このように構成された本発明のスラグ粉砕
設備の作動について説明する。原料ホッパ30の原料ス
ラグはコンスタントフィード・ウエア40によって定量
供給され,竪型粉砕機1内へ供給される。供給された原
料スラグは回転テーブル3Aと粉砕ローラ4の相互作用
によって粉砕され,微粉は頂部のセパレータ13で分級
され,分級後の精粉は排出口より配管を経由して集塵装
置110で捕集され製品(スラグ粉)とされる。一方,
竪型粉砕機1の回転テーブル3A上の鉄粒はスラグの粗
粒(比較的大径のもの)とともに異物排出口より排出さ
れ,二重ダンパ50,バケットエレベータ60を経由し
てバケットエレベータ60の排出口の直下に配設された
マグネット・セパレータ70へ入り,磁力選別されてス
ラグ粗粒と鉄粒とに分離され,スラグ粗粒はベルトコン
ベヤ100を介して竪型粉砕機1へ再供給される。鉄粒
は垂直管80内へ落下し,垂直管80の下部に設置され
た鉄粒・スラグ粉分離機90で鉄粒表面のスラグ粉が剥
離され,集塵装置110へ空気搬送され,一方鉄粒は鉄
粒・スラグ粉分離機90の下の配管から排出される。
The operation of the slag crushing equipment of the present invention thus constructed will be described. The raw material slag of the raw material hopper 30 is supplied in a constant amount by the constant feed wear 40 and is supplied into the vertical crusher 1. The supplied raw material slag is crushed by the interaction between the rotary table 3A and the crushing roller 4, the fine powder is classified by the separator 13 at the top, and the refined powder after classification is collected by the dust collector 110 from the outlet through the pipe. Collected and made into a product (slag powder). on the other hand,
The iron particles on the rotary table 3A of the vertical crusher 1 are discharged from the foreign matter discharge port together with the coarse particles of slag (those having a relatively large diameter), and pass through the double damper 50 and the bucket elevator 60 to the bucket elevator 60. It enters the magnet separator 70 disposed immediately below the discharge port, is magnetically sorted and separated into slag coarse particles and iron particles, and the slag coarse particles are re-supplied to the vertical crusher 1 via the belt conveyor 100. It The iron particles fall into the vertical tube 80, the slag powder on the surface of the iron particles is separated by the iron particle / slag powder separator 90 installed at the lower part of the vertical tube 80, and the iron particles are conveyed to the dust collector 110 by air, while the iron particles are ironed. The particles are discharged from a pipe below the iron particle / slag powder separator 90.

【0014】このようにして得られた鉄粒は,表面のス
ラグ粉はほとんど除去された純度の高い球状で1〜2m
m程度に整粒されており,ショット・ブラスト用の鋼球
として利用価値が高い。一方,再循環されるスラグ粗粒
には鉄粒がほどんど除去されており(純度90%),従
来に多く見られたスラグ含有中の鉄粒による激しい摩耗
がほとんど消失することができる。また,鉄粒が従来持
ち去っていたスラグ粉が本発明の設備で回収できるので
収率は20〜30%向上した。
The iron particles obtained in this manner are spherical particles of high purity with slag powder on the surface almost removed, and have a diameter of 1 to 2 m.
It is sized to about m and is highly useful as a steel ball for shot blasting. On the other hand, iron particles are mostly removed from the recycled slag coarse particles (purity: 90%), and the severe wear caused by the iron particles contained in the slag, which is often found in the past, can be almost eliminated. Further, since the slag powder which iron particles have conventionally carried away can be recovered by the facility of the present invention, the yield is improved by 20 to 30%.

【0015】[0015]

【発明の効果】以上説明したように,本発明のスラグ粉
砕設備は,原料スラグからきわめて純度の高く,かつ,
円形で整粒された鉄粒を簡単な設備で効率良く回収する
ことが出来るとともに,竪型粉砕機の摩耗を低減でき,
かつ,スラグ粉の収率を向上させることができる。
As described above, the slag crushing equipment of the present invention has extremely high purity from the raw material slag, and
Circular sized iron particles can be efficiently recovered with simple equipment, and wear of the vertical crusher can be reduced,
In addition, the yield of slag powder can be improved.

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

【図1】本発明のスラグ粉砕設備の実施例を示す全体フ
ローシートである。
FIG. 1 is an overall flow sheet showing an example of slag crushing equipment of the present invention.

【図2】本発明のスラグ粉砕設備の鉄粒・スラグ粉分離
機の実施例を示す縦断面図である。
FIG. 2 is a longitudinal sectional view showing an embodiment of an iron particle / slag powder separator of the slag crushing equipment of the present invention.

【図3】本発明のスラグ粉砕設備の鉄粒・スラグ粉分離
機の他の実施例を示す側面図である。
FIG. 3 is a side view showing another embodiment of the iron particle / slag powder separator of the slag crushing equipment of the present invention.

【図4】従来の竪型粉砕機の全体縦断面図である。FIG. 4 is an overall vertical sectional view of a conventional vertical crusher.

【符号の説明】[Explanation of symbols]

1 竪型粉砕機 3A 回転テーブル 4 粉砕ローラ 30 原料ホッパ 40 コンスタントフィード・ウエア 50 二重ダンパ 60 バケットエレベータ 70 マグネットセパレータ 80 垂直管 90 鉄粒・スラグ粉分離機 90a 内張り材 90b 吸入管 90c 内張り材 90d 吸入管 100 ベルトコンベヤ 110 集塵装置 120 吸引ファン 1 Vertical Grinder 3A Rotary Table 4 Grinding Roller 30 Raw Material Hopper 40 Constant Feed Wear 50 Double Damper 60 Bucket Elevator 70 Magnet Separator 80 Vertical Pipe 90 Iron Grain / Slag Powder Separator 90a Lining Material 90b Suction Pipe 90c Lining Material 90d Suction pipe 100 Belt conveyor 110 Dust collector 120 Suction fan

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 回転テーブルの外周部上面に複数個の回
転自在な粉砕ローラを配設するとともに,粉砕ローラを
回転テーブルへ押圧する油圧シリンダを備え,原料投入
シュートを経由して回転テーブル上へ供給したスラグ等
の原料を粉砕ローラに所定の粉砕圧力を与えて回転テー
ブル上面と粉砕ローラ周面との間で粉砕し竪型粉砕機上
部の分級機で分級した精粉を空気搬送により排出する竪
型粉砕機と,竪型粉砕機の回転テーブルを溢流して排出
された粗粒を垂直輸送するバケットエレベータと,バケ
ットエレベータの排出口の直下に設けたマグネットセパ
レータと,マグネットセパレータで捕集され排出された
スラグ含有中の鉄粒を排出する垂直管の途中に設けられ
た鉄粒・スラグ粉分離機と,前記竪型粉砕機の精粉およ
び前記垂直管内の微粉を集塵する集塵装置とを含むスラ
グ粉砕設備であって,前記鉄粒・スラグ粉分離機は,内
面に耐摩耗材が内張りされ,かつ,少なくとも1つ以上
の傾斜管を備えてなるスラグ粉砕設備。
1. A rotary table is provided with a plurality of rotatable crushing rollers on an upper surface of an outer peripheral portion of the rotary table, and a hydraulic cylinder for pressing the crushing rollers against the rotary table is provided. The supplied raw materials such as slag are crushed between the upper surface of the rotary table and the peripheral surface of the crushing roller by applying a predetermined crushing pressure to the crushing roller, and the fine powder classified by the classifier above the vertical crusher is discharged by air transportation. Vertical crusher, bucket elevator that vertically transports the coarse particles discharged by overflowing the rotary table of the vertical crusher, magnet separator provided directly below the outlet of the bucket elevator, and collected by the magnetic separator An iron particle / slag powder separator installed in the middle of a vertical pipe that discharges iron particles contained in the discharged slag, a fine powder of the vertical crusher, and a fine powder in the vertical pipe. A slag crushing device including a dust collector for collecting powder, wherein the iron particle / slag powder separator is a slag having an inner surface lined with an abrasion resistant material and provided with at least one or more inclined pipes. Crushing equipment.
JP3280922A 1991-08-02 1991-08-02 Slag crushing equipment Expired - Fee Related JP2666097B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3280922A JP2666097B2 (en) 1991-08-02 1991-08-02 Slag crushing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3280922A JP2666097B2 (en) 1991-08-02 1991-08-02 Slag crushing equipment

Publications (2)

Publication Number Publication Date
JPH0538464A true JPH0538464A (en) 1993-02-19
JP2666097B2 JP2666097B2 (en) 1997-10-22

Family

ID=17631805

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3280922A Expired - Fee Related JP2666097B2 (en) 1991-08-02 1991-08-02 Slag crushing equipment

Country Status (1)

Country Link
JP (1) JP2666097B2 (en)

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