JPS6324100Y2 - - Google Patents

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Publication number
JPS6324100Y2
JPS6324100Y2 JP7473983U JP7473983U JPS6324100Y2 JP S6324100 Y2 JPS6324100 Y2 JP S6324100Y2 JP 7473983 U JP7473983 U JP 7473983U JP 7473983 U JP7473983 U JP 7473983U JP S6324100 Y2 JPS6324100 Y2 JP S6324100Y2
Authority
JP
Japan
Prior art keywords
slag
collision plate
molten slag
gutter
rotating roll
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
JP7473983U
Other languages
Japanese (ja)
Other versions
JPS60336U (en
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 filed Critical
Priority to JP1983074739U priority Critical patent/JPS60336U/en
Publication of JPS60336U publication Critical patent/JPS60336U/en
Application granted granted Critical
Publication of JPS6324100Y2 publication Critical patent/JPS6324100Y2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/024Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/02Physical or chemical treatment of slags
    • C21B2400/022Methods of cooling or quenching molten slag
    • C21B2400/026Methods of cooling or quenching molten slag using air, inert gases or removable conductive bodies
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/052Apparatus features including rotating parts
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/052Apparatus features including rotating parts
    • C21B2400/056Drums whereby slag is poured on or in between
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B2400/00Treatment of slags originating from iron or steel processes
    • C21B2400/05Apparatus features
    • C21B2400/066Receptacle features where the slag is treated
    • C21B2400/072Tanks to collect the slag, e.g. water tank
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

Landscapes

  • Glanulating (AREA)
  • Manufacture Of Iron (AREA)

Description

【考案の詳細な説明】 本考案は水砕スラグ製造装置に係り、特に回転
ロールと衝突板を効果的に組合わせた水砕スラグ
製造装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a granulated slag manufacturing device, and more particularly to a granulated slag manufacturing device that effectively combines a rotating roll and a collision plate.

高炉等より排出する溶融スラグを水砕化するに
一般に次の2方法が行なわれている。
The following two methods are generally used to pulverize molten slag discharged from a blast furnace or the like.

(イ) 溶融スラグを圧力水のみによつて分散、急冷
する方法。
(a) A method in which molten slag is dispersed and rapidly cooled using only pressurized water.

(ロ) 溶融スラグを一旦機械的に分散、飛散せしめ
た後冷却水によつて冷却する方法。
(b) A method in which molten slag is once mechanically dispersed and scattered, and then cooled with cooling water.

通常の水砕スラグは従来(イ)の方法で製造されて
来た。すなわち、スラグ樋にて吹製函まで誘導さ
れた溶融スラグに圧力水を噴射して水砕し、この
水砕スラグを撹拌槽によつて受け、スラリーの形
で脱水槽に送り、脱水、乾燥等の工程を経て製造
されるものである。
Ordinary granulated slag has been produced by the conventional method (a). That is, molten slag guided to a blown box in a slag gutter is pulverized by injecting pressure water, and this granulated slag is received by a stirring tank and sent to a dehydration tank in the form of slurry, where it is dehydrated and dried. It is manufactured through the following steps.

しかし、この方法は溶融スラグを高圧水のみで
分散急冷するために4〜5Kg/cm2Gの高圧、かつ
大量の冷却水を要し、高炉等より供給されるスラ
グ量の変動に呼応するには大量のエルギーを必要
とする欠点がある。
However, this method requires a high pressure of 4 to 5 kg/cm 2 G and a large amount of cooling water to rapidly cool the molten slag by dispersing it only with high-pressure water. has the disadvantage of requiring a large amount of energy.

次に(ロ)の従来法としては第1図に示す如き方法
が公知である。すなわち、スラグ樋2によつて誘
導されて来た溶融スラグ4を、スラグ樋2の下方
に設けた回転ロール6に衝突させて分散、飛散さ
せ、この分散された溶融スラグ4Aを直接冷却水
8を貯留する水槽10に落下させるか、もしくは
飛散する溶融スラグ4Aの上部から雨水状に冷却
水8を散布する方法である。しかし、この方法は
溶融スラグの分散効果が十分でなく、また供給ス
ラグ量の変動に対応できない欠点がある。
Next, as a conventional method (b), a method as shown in FIG. 1 is known. That is, the molten slag 4 guided by the slag gutter 2 collides with the rotating roll 6 provided below the slag gutter 2 to be dispersed and scattered, and the dispersed molten slag 4A is directly supplied to the cooling water 8. In this method, the cooling water 8 is dropped into a water tank 10 for storing the molten slag, or the cooling water 8 is sprayed in the form of rainwater from above the scattered molten slag 4A. However, this method has the disadvantage that the dispersion effect of molten slag is insufficient and that it cannot respond to fluctuations in the amount of slag supplied.

更に水砕スラグ成品は、その品質上の要件とし
て高ガラス化度を要求されるものと、これを要求
されない単なる砂状のみで満足するものがある
が、上記従来法によるものはいずれもスラグ成品
の品質の制御が甚だ困難であり、供給する溶融ス
ラグ温度を制御して高密度化成品を得る方法その
他が開示されているが、大量生産方式として実用
化が極めて困難である。
Furthermore, some granulated slag products require a high degree of vitrification as a quality requirement, while others do not require this and are satisfied with a mere sand-like quality. It is extremely difficult to control the quality of the molten slag, and although methods for obtaining high-density chemical products by controlling the temperature of the molten slag to be supplied have been disclosed, it is extremely difficult to put it into practical use as a mass production system.

従つて、水砕スラグ成品の品質は、その製造装
置の特異性によつて決定され、更に水砕化処理に
おいては溶融スラグの分散、求冷技術が極めて肝
要であつて、この技術によつて製造原価のみなら
ず成品の品質まで左右されると言つても過言では
ない。
Therefore, the quality of granulated slag products is determined by the specificity of the manufacturing equipment, and in addition, dispersion of molten slag and cooling technology are extremely important in the granulation process. It is no exaggeration to say that not only the manufacturing cost but also the quality of the finished product is affected.

本考案の目的は、水砕スラグ製造における上記
従来技術の欠点を解消し、溶融スラグの分散、飛
散効果を最大とすると共に、スラグ供給量の変化
にも対応することができ、かつスラグ成品の品質
も制御可能な効果的な水砕スラグ製造置を提供す
るにある。
The purpose of the present invention is to eliminate the drawbacks of the above-mentioned conventional techniques in the production of granulated slag, to maximize the dispersion and scattering effect of molten slag, to be able to respond to changes in the amount of slag supplied, and to improve the quality of slag products. The aim is to provide an effective granulated slag manufacturing equipment that can also control quality.

本考案の要旨とするところは次の如くである。 The gist of the present invention is as follows.

すなわち、高炉より排出された溶融スラグを誘
導するスラグ樋と、前記スラグ樋端より流下する
溶融スラグを衝突させて飛散させる回転ロール
と、を有して成る水砕スラグ製造装置において、
前記回転ロールの前方に該回転ロールからの距離
を可変に前後進自在ならびに衝突角度可変に傾動
自在に配設され前記飛散溶融スラグを更に衝突さ
せ急冷固化させる衝突板と、前記衝突板の上部に
設けられ該衝突板の飛散溶融スラグ衝突面に冷却
水を流下させる冷却水供給ノズルと、前記回転ロ
ールおよび衝突板の下方に設けられ前記細粒固化
スラグを水流にて押流す吹製樋と、を有すること
を特徴とする水砕スラグ製造装置である。
That is, in a granulated slag production apparatus comprising a slag gutter that guides molten slag discharged from a blast furnace, and a rotating roll that causes the molten slag flowing down from the end of the slag gutter to collide and scatter,
A collision plate is disposed in front of the rotating roll so as to be able to move forward and backward with a variable distance from the rotating roll and to be tiltable with a variable collision angle, and further collides the scattered molten slag to rapidly cool and solidify it; a cooling water supply nozzle that is provided and causes cooling water to flow down onto the collision surface of the scattered molten slag of the collision plate; and a blowing gutter that is provided below the rotating roll and the collision plate that forces the fine solidified slag away with a water stream; This is a granulated slag manufacturing apparatus characterized by having the following.

本考案の実施例を第2,3,4図を参照して説
明する。スラグ樋2によつて誘導されて来た溶融
スラグ4は樋端より下方に設けられた回転ロール
6の上に流下し、回転ロール6の回動力を受けて
前方へ飛散し、分散されて粒状溶融スラグ4Aと
なる。回転ロール6の前方には内面に冷却水8を
流した濡れ壁状の衝突板10が設けられているの
で、飛散した粒状溶融スラグ4Aは、この衝突板
10に衝突して急冷され粒状固化スラグ4Bとな
つて下方に設けられた吹製樋12上に落下する。
An embodiment of the present invention will be described with reference to FIGS. 2, 3, and 4. The molten slag 4 guided by the slag gutter 2 flows down onto the rotating roll 6 provided below the gutter end, receives the rotational force of the rotating roll 6, scatters forward, and is dispersed into granular molten slag. The result is slag 4A. In front of the rotating roll 6, there is provided a collision plate 10 in the form of a wetted wall with cooling water 8 flowing on its inner surface, so that the scattered granular molten slag 4A collides with this collision plate 10 and is rapidly cooled and turned into granular solidified slag. 4B and falls onto the blowing gutter 12 provided below.

衝突板10は前後進および傾動自在に設けられ
ており、次の如く構成されている。すなわち、第
3〜4図に示す如く、衝突板本体10Aの上部に
は左右は2個の支持ローラ10Bが取付けられて
いて、この支持ローラ10Bは衝突板10の両端
に水平に設けられたガイドレール13上を前後進
可能に移動できるようになつている。すなわち、
衝突板本体10Aの上部両側にブラケツト7Cが
取付けられ、ブラケツト7Cには軸7Dを介して
ピストンロツド14が連結されており、ガイドレ
ール13に固定されたアクチユエーター16の作
動により、ピストンロツド14が前後進し、従つ
て衝突板10が前後進可能の如く構成されてい
る。アクチユエーター16は衝突板10の両側に
それぞれ1台宛設けられているが、中央部に1台
だけ設置することもできる。
The collision plate 10 is provided so as to be movable forward and backward and tiltable, and is constructed as follows. That is, as shown in FIGS. 3 and 4, two support rollers 10B are installed on the left and right sides of the upper part of the collision plate main body 10A, and these support rollers 10B are connected to guides provided horizontally at both ends of the collision plate 10. It is designed to be able to move forward and backward on the rails 13. That is,
Brackets 7C are attached to both sides of the upper part of the collision plate main body 10A, and a piston rod 14 is connected to the bracket 7C via a shaft 7D.By the operation of an actuator 16 fixed to the guide rail 13, the piston rod 14 is moved back and forth. Therefore, the collision plate 10 is configured to be able to move forward and backward. One actuator 16 is provided on each side of the collision plate 10, but only one actuator 16 may be provided in the center.

衝突板本体10Aの下部中央には第4図に示す
如く傾動支持ブラケツト7Eが取付けられてお
り、傾動支持ブラケツト7Eにはシヤツクル7F
を介して傾動用ワイヤーロープ18が連結されて
おり、シープ19を介して図示されていないが、
ウインチ等の駆動装置によつてワイヤーロープ1
8を巻取り、もしくは巻戻すことにより衝突板本
体10Aの傾動角度θを調節できるようになつて
いる。
As shown in FIG. 4, a tilting support bracket 7E is attached to the center of the lower part of the collision plate main body 10A, and a shank 7F is attached to the tilting support bracket 7E.
Although not shown, a tilting wire rope 18 is connected via a sheep 19.
Wire rope 1 by a drive device such as a winch
The tilting angle θ of the collision plate main body 10A can be adjusted by winding or unwinding the collision plate 8.

上記衝突板10の前後進ならびに傾動角度の調
整はその他の構成もとることができる。
Other configurations may be used to adjust the forward and backward movement of the collision plate 10 and the tilt angle.

また、衝突板本体10Aの内側面上部には、冷
却水ノズル20が取付けられ、冷却水ホース2
2、バルブ24を介して供給される冷却水8を冷
却水ノズル20から衝突板本体10Aの内側面に
沿わせて流下させるようになつている。その結
果、回転ロール6に衝突して前方に分散飛散した
粒状溶融スラグ4Aは、更に冷却水8が流下する
衝突板本体10Aに衝突して急冷固化し、粒状固
化スラグ4Bとなつて下方に設けられた吹製樋1
2上に落下する。吹製樋12の後方には押水ノズ
ル26が設けられていて、吹製樋12の全面に押
水を流しているので、落下した粒状固化スラグ4
Bは押流されて下流に設けられた槽中に集められ
る。
Further, a cooling water nozzle 20 is attached to the upper part of the inner surface of the collision plate main body 10A, and a cooling water hose 2
2. The cooling water 8 supplied via the valve 24 is made to flow down from the cooling water nozzle 20 along the inner surface of the collision plate main body 10A. As a result, the granular molten slag 4A that collides with the rotating roll 6 and is dispersed and scattered forward further collides with the collision plate main body 10A through which the cooling water 8 flows and rapidly cools and solidifies, becoming granular solidified slag 4B and disposed below. Blown gutter 1
2 falls on top. A water push nozzle 26 is provided at the rear of the blowing gutter 12, and since the water is poured over the entire surface of the blowing gutter 12, the fallen granular solidified slag 4 is removed.
B is swept away and collected in a tank provided downstream.

上記本考案の構成と作用について記載したが、
本考案による水砕スラグ製造に際しては、水砕ス
ラグの品質を任意に制御できることが、本考案の
特徴の一つである。すなわち、本考案者が第2図
に示す如く、スラグ樋2より流下する溶融スラグ
4が回転ロール6に衝突し分散飛散して更に冷却
水8が内側面を流れる衝突板10に衝突して急冷
固化する際の回転ロール6への最初の衝突点から
衝突板10の頂部で測定した衝突板10までの距
離をaとして水砕した場合と、次に衝突板10を
移動して回転ロール6からの距離を(a+b)と
して水砕した時を比較すると、水砕スラグ成品4
Bの品質性状が異なることを見出した。すなわ
ち、衝突板10の距離aの場合の如く、短時間の
飛行後、衝突板10の冷却水8と接触した場合に
はガラス質の高いセメント用に適する成品を得、
飛距離が(a+b)と長い場合にはガラス質が低
下するが緻密な硬質水砕スラグ成品が得られるこ
とが判明した。
Although the structure and operation of the present invention have been described above,
When producing granulated slag according to the present invention, one of the features of the present invention is that the quality of the granulated slag can be controlled arbitrarily. That is, as shown in FIG. 2 by the present inventor, the molten slag 4 flowing down from the slag gutter 2 collides with the rotating roll 6 and is dispersed, and the cooling water 8 collides with the collision plate 10 flowing on the inner surface and is rapidly cooled. The distance from the first collision point to the rotating roll 6 during solidification to the collision plate 10 measured at the top of the collision plate 10 is set as a, and the collision plate 10 is then moved and the collision plate 10 is moved from the rotating roll 6. When comparing the results when granulated with the distance of (a+b), granulated slag product 4
It was found that the quality characteristics of B were different. That is, when the collision plate 10 comes into contact with the cooling water 8 after a short flight, as in the case of the distance a of the collision plate 10, a product suitable for cement with high glass quality is obtained.
It has been found that when the flying distance is as long as (a+b), a dense hard granulated slag product can be obtained although the glass quality is reduced.

この飛散溶融スラグ4Aの飛距離の差による水
砕スラグ成品の品質の相異理由は次の如く考えら
れる。すなわち、飛距離が長く(a+b)の場合
には、分散溶融スラグ4Aが、衝突板10の冷却
水10による冷却作用の前に空気中で徐冷された
後、衝突板10の冷却水8により急冷されるのに
対し、飛距離が短くaの場合には空気による冷却
がほとんどなくして直ちに衝突板10の冷却水8
によつて急冷される結果に因るものと考えられ
る。かくの如く本考案による水砕スラグ成品の品
質性状は、回転ロール6に衝突した分散溶融スラ
グ4Aの飛行距離に依存するので、この特性を利
用して水砕スラグ成品の品質制御が可能である。
その実施例を次に記載する。
The reason for the difference in the quality of the granulated slag products due to the difference in flying distance of the scattered molten slag 4A is considered to be as follows. That is, when the flying distance is long (a+b), the dispersed molten slag 4A is gradually cooled in the air before being cooled by the cooling water 10 of the collision plate 10, and then is cooled by the cooling water 8 of the collision plate 10. On the other hand, in the case of a short flight distance, the cooling water 8 of the collision plate 10 is immediately cooled with almost no air cooling.
This is thought to be due to the rapid cooling caused by the process. As described above, the quality of the granulated slag product according to the present invention depends on the flight distance of the dispersed molten slag 4A that collided with the rotating roll 6, so it is possible to control the quality of the granulated slag product using this characteristic. .
Examples thereof are described below.

すなわち、第2図に示した回転ロール6から衝
突板10までの距離a=500mmとして水砕スラグ
4Bを製造したところ単位容積重量Kg/にて
1.0の成品を得た。衝突板10までの距離を長く
し(a+b)=1500mmとしたところ単位容積重量
Kg/にて1.2の成品が得られた。前者はセメン
ト用として適当であり、後者は更に粒度調整を行
うことによつて単位容積重量が1.5とすすことが
でき、この種の緻密な水砕スラグ成品はコンクリ
ート用細骨材として合格し得るものである。
That is, when granulated slag 4B was manufactured with the distance a from the rotating roll 6 to the collision plate 10 shown in FIG. 2 = 500 mm, the unit volume weight was Kg/.
I got a product of 1.0. When the distance to the collision plate 10 is increased to (a + b) = 1500 mm, the unit volume weight is
A product of 1.2 kg/kg was obtained. The former is suitable for use in cement, and the latter can be made to have a unit volume weight of 1.5 by further adjusting the particle size, and this type of dense granulated slag product can pass as fine aggregate for concrete. It is something.

かくの如く、同一装置を使用し、衝突板10の
位置を換えることによつて異種の品質の水砕スラ
グ成品の製造が可能である。
As described above, by using the same apparatus and changing the position of the collision plate 10, it is possible to produce granulated slag products of different qualities.

上記実施例より明らかな如く、本考案はスラグ
樋2の下方に回転ロール6を設け、流下する溶融
スラグ4を回転ロール6に衝突させることにより
分散飛散せしめ、この飛散溶融スラグ4Aを更に
前方に設けた前後進および傾動自在の濡れ壁式の
衝突板10に衝突させることにより急冷固化さ
せ、下方の吹製樋12に落下した粒状固化スラグ
成品を吹製樋12の後方に設けた押水ノズル26
からの流水により押し流し槽中に集める構成とし
たので次の如き効果を収めることができた。
As is clear from the above embodiment, the present invention provides a rotating roll 6 below the slag gutter 2, and causes the flowing molten slag 4 to collide with the rotating roll 6 to disperse and scatter the scattered molten slag 4A further forward. The granular solidified slag product is rapidly cooled and solidified by colliding with a wet wall-type collision plate 10 that can freely move back and forth and tilt, and falls into the blowing gutter 12 below.
By using a structure in which the water is washed away and collected in a tank by flowing water, the following effects can be achieved.

(イ) 溶融スラグの細粒化は回転ロールにて行な
い、その後冷却水を流した衝突板によつて急冷
する方法をとつたので従来の水砕スラグ製造装
置の如く大量の処理水を要せず、使用エネルギ
ーも極めて少くてすますことができる。
(b) The molten slag is made fine by rotating rolls and then rapidly cooled by a collision plate through which cooling water is flowed, so a large amount of treated water is not required as in conventional granulated slag production equipment. Moreover, the amount of energy used can be extremely reduced.

(ロ) 回転ロールの回転数および衝突板の角度を調
整することにより、溶融スラグの供給量の変動
に対応することができるので大量生産も可能で
ある。
(b) By adjusting the rotation speed of the rotary roll and the angle of the collision plate, it is possible to respond to fluctuations in the amount of molten slag supplied, making mass production possible.

(ハ) 回転ロールから衝突板までの距離を調整する
ことにより水砕スラグ成品の品質の制御が可能
である。
(c) The quality of the granulated slag product can be controlled by adjusting the distance from the rotating roll to the collision plate.

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

第1図は回転ロールを利用する従来の水砕スラ
グ製造装置を示す断面図、第2図は本考案による
水砕スラグ製造装置の大要および衝突板の設置位
置変更の効果を説明する断面図、第3図は本考案
における衝突板の前後進および傾動機構の実施例
を示す断面図、第4図は第3図の−線矢視衝
突板の正面図である。 2……スラグ樋、4……溶融スラグ、4A……
細粒化溶融スラグ、4B……細粒化固化スラグ、
6……回転ロール、8……冷却水、10……衝突
板、12……吹製樋、13……ガイドレール、1
4……ピストンロツド、16……アクチユエータ
ー、18……ワイヤロープ。
Fig. 1 is a sectional view showing a conventional granulated slag manufacturing apparatus using rotating rolls, and Fig. 2 is a sectional view illustrating an overview of the granulated slag manufacturing apparatus according to the present invention and the effect of changing the installation position of the collision plate. , FIG. 3 is a sectional view showing an embodiment of the forward and backward movement and tilting mechanism of the collision plate in the present invention, and FIG. 4 is a front view of the collision plate as viewed from the - line arrow in FIG. 3. 2... Slag gutter, 4... Molten slag, 4A...
Fine-grained molten slag, 4B... fine-grained solidified slag,
6...Rotating roll, 8...Cooling water, 10...Collision plate, 12...Blown gutter, 13...Guide rail, 1
4... Piston rod, 16... Actuator, 18... Wire rope.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 高炉より排出された溶融スラグを誘導するスラ
グ樋と、前記スラグ樋端より流下する溶融スラグ
を衝突させて飛散させる回転ロールと、を有して
成る水砕スラグ製造装置において、前記回転ロー
ルの前方に該回転ロールからの距離を可変に前後
進自在ならびに衝突角度可変に傾動自在に配設さ
れ前記飛散溶融スラグを更に衝突させ急冷固化さ
せる衝突板と、前記衝突板の上部に設けられ該衝
突板の飛散溶融スラグ衝突面に冷却水を流下させ
る冷却水供給ノズルと、前記回転ロールおよび衝
突板の下方に設けられ前記細粒固化スラグを水流
にて押流す吹製樋と、を有することを特徴とする
水砕スラグ製造装置。
A granulated slag manufacturing apparatus comprising: a slag gutter that guides molten slag discharged from a blast furnace; and a rotating roll that causes the molten slag flowing down from the end of the slag gutter to collide and scatter. a collision plate which is arranged so as to be able to move forward and backward with a variable distance from the rotating roll and to be tiltable with a variable collision angle, for further colliding the scattered molten slag to rapidly cool and solidify it; It is characterized by having a cooling water supply nozzle that causes cooling water to flow down onto the collision surface of the scattered molten slag, and a blowing gutter that is provided below the rotating roll and the collision plate and that forces the fine solidified slag away with a water stream. Granulated slag manufacturing equipment.
JP1983074739U 1983-05-19 1983-05-19 Granulated slag production equipment Granted JPS60336U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1983074739U JPS60336U (en) 1983-05-19 1983-05-19 Granulated slag production equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1983074739U JPS60336U (en) 1983-05-19 1983-05-19 Granulated slag production equipment

Publications (2)

Publication Number Publication Date
JPS60336U JPS60336U (en) 1985-01-05
JPS6324100Y2 true JPS6324100Y2 (en) 1988-07-01

Family

ID=30204822

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1983074739U Granted JPS60336U (en) 1983-05-19 1983-05-19 Granulated slag production equipment

Country Status (1)

Country Link
JP (1) JPS60336U (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5313631A (en) * 1976-07-23 1978-02-07 Nippon Steel Corp Blast furnace slag granulation method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS567836Y2 (en) * 1977-06-10 1981-02-20

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5313631A (en) * 1976-07-23 1978-02-07 Nippon Steel Corp Blast furnace slag granulation method

Also Published As

Publication number Publication date
JPS60336U (en) 1985-01-05

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