JPS61279636A - Charging apparatus of sintered ore cooling machine - Google Patents
Charging apparatus of sintered ore cooling machineInfo
- Publication number
- JPS61279636A JPS61279636A JP12060685A JP12060685A JPS61279636A JP S61279636 A JPS61279636 A JP S61279636A JP 12060685 A JP12060685 A JP 12060685A JP 12060685 A JP12060685 A JP 12060685A JP S61279636 A JPS61279636 A JP S61279636A
- Authority
- JP
- Japan
- Prior art keywords
- sintered ore
- cooler
- chute
- stone box
- sintering machine
- 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
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は焼結鉱冷却機の焼結鉱装入装置に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a sintered ore charging device for a sintered ore cooler.
従来の焼結鉱冷却機(以下クーラと略す)への高温焼結
鉱の装入装置の概略を第2図に示す。FIG. 2 schematically shows a conventional device for charging high-temperature sintered ore into a sintered ore cooler (hereinafter referred to as cooler).
焼結機1から排出された焼結鉱2はシュータ12を介し
てクラッシャー3で大塊のものは破砕され、しかる後ス
トーンボックス4(焼結鉱が落下したときの粉化を防止
する為、クッションとなるべくこの中には焼結鉱が充満
している)に落下し、更忙シエータ5に落下してクーラ
6中へ装入される。大部分の焼結鉱はシュータ12を通
って供給されるが、一部の焼結鉱はシュー ・り1
2の位置では焼結機から排出されず焼結鉱 □fと
なって直接シュータ5を介して供給される為、どpして
も2系列のシュータが必要となシ、その為シュータ12
の位置で排出された焼結鉱 2.2′は落下距離が
大きくなり、落下時の衝撃 ・時で破壊されて粉化
し易くなシ、焼結鉱の歩留 □りが低下する要因と
なっていた。The sintered ore 2 discharged from the sintering machine 1 passes through a chute 12 and is crushed by a crusher 3 in large chunks, and is then transferred to a stone box 4 (to prevent the sintered ore from pulverizing when it falls). The sintered ore is filled with sintered ore to form a cushion. Most of the sintered ore is fed through the chute 12, but some of the sintered ore is fed through the chute 12.
In position 2, the sintered ore is not discharged from the sintering machine but is supplied as sintered ore □f directly through the shooter 5, so two series of chutes are required in any case.
The sintered ore discharged at the position 2.2' has a longer falling distance and is less likely to be broken and powdered by impact and time when falling, which is a factor in reducing the yield of sintered ore. was.
なお第2図に示したクー26は、この中に冷却用のガス
7(一般に空気)を吹込んで焼結鉱を冷却すると共に、
と九によシ得られた高温ガ □ス8を回収ガスダク
ト9で回収する排熱回収型 □クーラの例であるが
、排熱回収しないクーラに 於いても上記事情は全
く同様である0
〔発明が解決しようとする問題点〕
しかし′ながら、従来技術においては下記のよ □
うな欠点があった。The cooler 26 shown in FIG. 2 cools the sintered ore by blowing cooling gas 7 (generally air) into it, and
This is an example of an exhaust heat recovery type □ cooler in which the high temperature gas □ gas 8 obtained by the above is recovered in the recovery gas duct 9, but the above situation is exactly the same for a cooler that does not recover exhaust heat. [Problems to be Solved by the Invention] However, in the prior art, the following □
There were some drawbacks.
(1) 前述の第2図に於いて大部分の焼結鉱はシュ
ータ12を介してクーラへ供給されるが、焼結鉱の落下
距離が大きくなる為に落下時の衝撃で焼結鉱が破壊され
所定粒径以下の焼結鉱の割合が増加し歩留りが低下する
。(1) In the above-mentioned Figure 2, most of the sintered ore is supplied to the cooler via the chute 12, but since the falling distance of the sintered ore becomes large, the sintered ore is damaged by the impact when it falls. The proportion of sintered ore that is destroyed and has a particle size smaller than a predetermined size increases, and the yield decreases.
(2) クーラ中への焼結鉱の落下位置を制御できず
、その為一般にクーラ内の焼結鉱の山の形状は第3図の
如く中央部分が高くて両端が低い形状となシ、その為冷
却ガスの通過距離H1に比較してHlが小さくなシかつ
、両側壁近傍に存在する粒子のサイズがホツベ中央部付
近に存在する粒子のサイズよりも大きくなる為に壁近傍
の充てん率が小さくなって(見かけ上のB、が更に小さ
くなって)′、冷却ガスの一部は圧損の小さい上部へ逃
げる為に焼結鉱の冷却効率が低下するとともに熱回収効
率も低下する。(2) It is not possible to control the position of the sintered ore falling into the cooler, and as a result, the shape of the pile of sintered ore in the cooler is generally high in the center and low at both ends, as shown in Figure 3. Therefore, Hl is smaller than the passage distance H1 of the cooling gas, and since the size of particles near both side walls is larger than the size of particles near the center of the hopper, the filling ratio near the walls is reduced. becomes small (apparent B becomes even smaller)', and part of the cooling gas escapes to the upper part where the pressure drop is small, resulting in a decrease in cooling efficiency of the sintered ore and a decrease in heat recovery efficiency.
本発明は従来技術における上述したような欠点を解消し
た焼結鉱冷却機の装入装置を提供しようとするものであ
る。The present invention aims to provide a charging device for a sintered ore cooler that eliminates the above-mentioned drawbacks of the prior art.
C問題点を解決するための手段〕
すなわち、本発明は焼結鉱冷却機の装入装置−に於いて
、焼結機から離脱した焼結鉱を上部と下部のシュータ−
l)為ら冷却機へ供給すべく2系列のシュータとすると
共に上部のシュータカラ落下する焼結鉱の軌跡上に冷却
機の半径方向に移動可能なストーンボックスを設置した
ことを特徴とする焼結鉱冷却機の装入装置である。Means for Solving Problem C] That is, the present invention provides a charging device for a sintered ore cooler, in which the sintered ore separated from the sintering machine is transferred to the upper and lower shooters.
l) A sintering device characterized in that two series of chutes are used to supply the sinter to the cooler, and a stone box movable in the radial direction of the cooler is installed on the trajectory of the sinter falling from the upper chute. This is a charging device for a condensate cooler.
本発明の一実施態様の概略図を第1図忙示す0□
第1図において第2図と同一のものには第2図 i
と同一符号を付している。
:第1図における特徴部分は、シュータ5以外 □
に新たにシュータ−0を設置した点と、シュー □
ター0から落下した焼結鉱の衝撃を弱める為にストーン
ボックス4に加えストーンボックス4′を設置した点と
、更にクーラ中の焼結鉱の山の形状を制御する目的で該
ストーンボックス4′ヲ:シリンダー等の駆動手段にて
クーラの半径方向 へに移動することができる機構
とした点である。A schematic diagram of an embodiment of the present invention is shown in Figure 1.0 □ In Figure 1, the same parts as Figure 2 are shown in Figure 2.
The same reference numerals are given.
: Characteristic parts in Figure 1 are other than shooter 5 □
The new shooter 0 has been installed in , and the shooter □
In addition to the stone box 4, a stone box 4' was installed in order to weaken the impact of the sintered ore that fell from the cooler 0, and the stone box 4' was installed for the purpose of controlling the shape of the pile of sintered ore in the cooler. (2) The mechanism is such that it can be moved in the radial direction of the cooler using a driving means such as a cylinder.
シュータ10の設置によ如焼結鉱の落下距離(第2図に
おいてストーンボックス4からシュータ5への落下距離
)が小さくなり、落下衝撃による焼結鉱の破壊(粉化)
が減少し、その為焼結鉱の歩留シが向上する0
また、移動可能なストーンボックス4′の設置によシク
ーラ内の焼結鉱の山の形状をたとえば第4図に示す如く
制御できる為に焼結鉱の冷却効率が向上しかつ回収熱量
も増大する0本発明の実施例の概略は第1図に示したと
おシである。また7 00 ton/’hの焼結鉱を処
理する排熱回収型クーラに本発明を適用した場合の処理
後の焼結鉱の粒度分布を従来法と対比して第5図に、ま
たこの時の熱回収結果を第1表に示す0
〔発明の効果〕
実施例の項に記載のとおシ。焼結鉱の粒径が6vna以
下のものを返鉱すると、第5図より従来法の歩留は90
%であるのに対して本発明では歩留り95q6となり5
チ向上する0また第1表に示した如く回収熱量は約18
チ向上する。By installing the chute 10, the falling distance of the sintered ore (the falling distance from the stone box 4 to the chute 5 in Fig. 2) becomes smaller, and the sintered ore is destroyed (pulverized) due to the impact of the fall.
is reduced, thereby improving the yield of sintered ore.In addition, by installing a movable stone box 4', the shape of the pile of sintered ore in the shaker can be controlled as shown in Fig. 4, for example. Therefore, the cooling efficiency of the sintered ore is improved and the amount of recovered heat is also increased.An outline of an embodiment of the present invention is shown in FIG. In addition, the particle size distribution of sintered ore after treatment when the present invention is applied to an exhaust heat recovery type cooler that processes sintered ore at a rate of 700 tons/'h is shown in Figure 5 in comparison with the conventional method. Table 1 shows the heat recovery results at 0 [Effects of the Invention] As described in the Examples section. When returning sintered ore with a grain size of 6vna or less, the yield of the conventional method is 90% as shown in Figure 5.
%, whereas in the present invention, the yield is 95q6, which is 5
Also, as shown in Table 1, the amount of recovered heat is approximately 18%.
Improve your skills.
第1図は本発明の一実施例を説明する概略図、第2図は
従来の焼結鉱冷却機の装入装置を説明する概略図、第3
図及び第4図はそれぞれ従来法、本発明に於けるクーラ
中の焼結の山の形状の一実施例の模式図、第5図は従来
法及び本発明に於ける冷却後の焼結鉱の粒度分布の測定
結果例を示す図表である0
復代理人 内 1) 明
復代理人 萩 原 亮 −
復代理人 安 西 篤 夫
第1図
第4図Fig. 1 is a schematic diagram illustrating an embodiment of the present invention, Fig. 2 is a schematic diagram illustrating a charging device for a conventional sintered ore cooler, and Fig. 3 is a schematic diagram illustrating a charging device for a conventional sintered ore cooler.
4 and 4 are schematic diagrams of an example of the shape of sintered ridges in the cooler in the conventional method and the present invention, respectively, and FIG. 5 is a schematic diagram of the sintered ore after cooling in the conventional method and the present invention. This is a chart showing an example of the measurement results of particle size distribution.
Claims (1)
焼結鉱を上部と下部のシュータから冷却機へ供給すベく
2系列のシュータとすると共に上部のシュータから落下
する焼結鉱の軌跡上に冷却機の半径方向に移動可能なス
トーンボックスを設置したことを特徴とする焼結鉱冷却
機の装入装置。In the charging device of the sintered ore cooler, two series of chutes are used to supply the sintered ore separated from the sintering machine to the cooler from the upper and lower chutes, and the sintered ore that falls from the upper chute is used. A charging device for a sintered ore cooler, characterized in that a stone box movable in the radial direction of the cooler is installed on the trajectory of the condensate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12060685A JPS61279636A (en) | 1985-06-05 | 1985-06-05 | Charging apparatus of sintered ore cooling machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12060685A JPS61279636A (en) | 1985-06-05 | 1985-06-05 | Charging apparatus of sintered ore cooling machine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61279636A true JPS61279636A (en) | 1986-12-10 |
Family
ID=14790409
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12060685A Pending JPS61279636A (en) | 1985-06-05 | 1985-06-05 | Charging apparatus of sintered ore cooling machine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61279636A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100617258B1 (en) * | 1999-11-24 | 2006-08-29 | 주식회사 포스코 | Discharging apparatus of sintered ore decreasing returned fine and controlling method thereof |
KR100851159B1 (en) | 2007-01-16 | 2008-08-08 | 주식회사 포스코 | System for discharging and crushing sintered ores having drop impact alleviating function |
JP2012251203A (en) * | 2011-06-02 | 2012-12-20 | Nippon Steel & Sumitomo Metal Corp | Method for cooling sintered ore, method and device for sorting out sintered ore |
KR101235756B1 (en) | 2010-12-03 | 2013-02-21 | 주식회사 포스코 | Cooling system for sintered mineral |
-
1985
- 1985-06-05 JP JP12060685A patent/JPS61279636A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100617258B1 (en) * | 1999-11-24 | 2006-08-29 | 주식회사 포스코 | Discharging apparatus of sintered ore decreasing returned fine and controlling method thereof |
KR100851159B1 (en) | 2007-01-16 | 2008-08-08 | 주식회사 포스코 | System for discharging and crushing sintered ores having drop impact alleviating function |
KR101235756B1 (en) | 2010-12-03 | 2013-02-21 | 주식회사 포스코 | Cooling system for sintered mineral |
JP2012251203A (en) * | 2011-06-02 | 2012-12-20 | Nippon Steel & Sumitomo Metal Corp | Method for cooling sintered ore, method and device for sorting out sintered ore |
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