JPH11172309A - Smelting reduction apparatus - Google Patents
Smelting reduction apparatusInfo
- Publication number
- JPH11172309A JPH11172309A JP33428297A JP33428297A JPH11172309A JP H11172309 A JPH11172309 A JP H11172309A JP 33428297 A JP33428297 A JP 33428297A JP 33428297 A JP33428297 A JP 33428297A JP H11172309 A JPH11172309 A JP H11172309A
- Authority
- JP
- Japan
- Prior art keywords
- reduction furnace
- smelting reduction
- ore
- wind box
- furnace
- 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 Of Iron (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
- Furnace Details (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、落鉱の排出経路を
改良した溶融還元装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a smelting reduction apparatus having an improved ore dropping path.
【0002】[0002]
【従来の技術】従来の技術として特開平4−63216
号公報がある。この技術は、図2に示すように、予備還
元炉1の風箱1a 底部と溶融還元炉2の頂部とを管路3
で連結し、予備還元炉1から溶融還元炉2への鉱石の供
給を、予備還元炉分散板1a からの落鉱によって行な
う。落鉱量の調整は、予備還元炉の上部に取付けた排ガ
ス管4に取付けた排ガスダンパ5の開度の調整によって
行なう。即ち、ダンパ開度大とすると予備還元炉内圧力
が低下し、分散板ノズル内ガス流速が大となり、落鉱量
が減少する。逆に、ダンパ開度を小とすると、予備還元
炉内圧力が高くなり、分散板ノズル内ガス流速が小くな
り、落鉱量が増大する。2. Description of the Related Art As a prior art, Japanese Patent Laid-Open Publication No.
There is an official gazette. In this technique, as shown in FIG. 2, the bottom of the wind box 1a of the preliminary reduction furnace 1 and the top of the
The ore is supplied from the preliminary reduction furnace 1 to the smelting reduction furnace 2 by dropping the ore from the preliminary reduction furnace dispersion plate 1a. The amount of ore fall is adjusted by adjusting the opening of the exhaust gas damper 5 attached to the exhaust gas pipe 4 attached to the upper part of the preliminary reduction furnace. That is, when the opening degree of the damper is increased, the pressure in the preliminary reduction furnace decreases, the gas flow velocity in the dispersion plate nozzle increases, and the amount of ore drop decreases. Conversely, when the damper opening is reduced, the pressure in the preliminary reduction furnace increases, the gas flow velocity in the dispersion plate nozzle decreases, and the amount of ore drop increases.
【0003】しかし、ノズル内ガス流速を調節して落鉱
量を制御しようとすると、予備還元流動層内のガス流速
も変化してしまう問題がある。一般に、予備還元炉にお
いて鉱石の安定した流動化状況を実現するためには、層
内ガス流速の適正範囲が存在するが、上述のように落鉱
量を制御するためにノズル内ガス流速を変更すると、層
内ガス流速も変化してしまう。このため、従来技術では
流動層内の良好な流動化状況を安定して形成することは
困難である。[0003] However, there is a problem that the gas flow rate in the pre-reduction fluidized bed also changes if the amount of ore drop is controlled by adjusting the gas flow rate in the nozzle. Generally, there is an appropriate range of gas flow rate in the bed to realize stable ore fluidization of ore in the preliminary reduction furnace, but the gas flow rate in the nozzle is changed to control the amount of ore drop as described above. Then, the gas flow velocity in the layer also changes. For this reason, it is difficult to stably form a favorable fluidized state in the fluidized bed with the conventional technology.
【0004】例えば、流動層内ガス流速が適正範囲を超
えて大きくなると、微粒鉱石の大部分がフリーボードか
ら炉外へ排出され、流動層が形成されない。その結果、
所定の還元性能が得られない。さらに、鉱石の紛化が助
長され、サイクロンなどの集塵装置を通過する、いわゆ
るダストロスが増大する。[0004] For example, when the gas flow velocity in the fluidized bed exceeds a proper range, most of the fine ore is discharged from the freeboard to the outside of the furnace, and the fluidized bed is not formed. as a result,
The predetermined reduction performance cannot be obtained. Further, ore liquefaction is promoted, and so-called dust loss that passes through a dust collecting device such as a cyclone increases.
【0005】また逆に、流動層内ガス流速が適正範囲を
外れて小さくなると、鉱石の流動化が不活発となり、鉱
石の不動領域が発生し、炉内での鉱石がスティッキング
が発生し、その結果、所定の還元性能が得られない。Conversely, when the gas flow rate in the fluidized bed is out of the proper range and becomes small, the fluidization of the ore becomes inactive, an immobile area of the ore is generated, and the ore sticks in the furnace. As a result, predetermined reduction performance cannot be obtained.
【0006】しかも、この方法では、溶融還元炉への鉱
石供給量を、ダンパ開度によって調整するため、応答
性、精度の面で溶融還元炉への供給量制御は難しい。さ
らにまた、溶融還元炉のシャットダウン時、予備還元炉
内の層内滞留鉱石が全量溶融還元炉へ落下供給されるた
め、溶融還元炉内の溶鉄温度が低下し、極端な場合は、
炉内で溶鉄が凝固してしまい、再立ち上げが難しい状況
が生じる。Further, in this method, since the amount of ore supplied to the smelting reduction furnace is adjusted by the damper opening, it is difficult to control the amount of ore supplied to the smelting reduction furnace in terms of responsiveness and accuracy. Furthermore, at the time of shutting down the smelting reduction furnace, since all the ore retained in the layer in the preliminary reduction furnace is dropped and supplied to the smelting reduction furnace, the temperature of the molten iron in the smelting reduction furnace decreases, and in extreme cases,
The molten iron solidifies in the furnace, which makes it difficult to restart.
【0007】[0007]
【発明が解決しようとする課題】本発明は上記事情に鑑
みてなされたもので、その目的とするところは、流動内
の良好な流動化状況を安定して形成し、所定の還元性能
が得られ、ダストロスの増大を防ぎ、しかも溶融還元炉
への供給量制御が容易で、さらにまた溶融還元炉のシャ
ットダウン時に再立ち上げが容易な溶融還元装置を提供
する。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and an object of the present invention is to stably form a good fluidization state in a flow and obtain a predetermined reduction performance. Thus, it is possible to provide a smelting reduction apparatus that can prevent an increase in dust loss, can easily control the supply amount to the smelting reduction furnace, and can easily restart when the smelting reduction furnace is shut down.
【0008】[0008]
【課題を解決するための手段】即ち、本発明は、(1)
分散板を介して下部に風箱、上部に流動層を形成した予
備還元炉と、予備還元炉の流動層で予備還元された鉱石
が装入される溶融還元炉と、この溶融還元炉の上部から
予備還元炉の風箱内に接続した排ガスダクトとを具備し
た溶融還元装置において、前記風箱の底部と前記溶融還
元炉上部との間に落鉱系管路を接続し、この管路に、流
動層から分散板を通って風箱内に落鉱された鉱石を溶融
還元炉へ切り出す切出し手段を装着したことを特徴とす
る溶融還元装置、(2)前記風箱は、排ガスダクトの取
付位置より下部の容積が、鉱石の流動層内滞留量容積以
上であることを特徴とする(1)に記載の溶融還元装
置、(3)前記風箱は底部に、溶融還元炉の操業停止時
に風箱内滞留鉱石を系外に排出する落鉱系外排出系管路
を接続したことを特徴とする(1)又は(2)に記載の
溶融還元装置である。That is, the present invention provides (1)
A pre-reduction furnace with a wind box at the bottom and a fluidized bed at the top via a dispersion plate, a smelting reduction furnace into which the ore pre-reduced in the fluidized bed of the pre-reduction furnace is charged, and an upper part of the smelting reduction furnace In the smelting reduction apparatus having an exhaust gas duct connected to the inside of the wind box of the preliminary reduction furnace, a fallen pipe is connected between the bottom of the wind box and the top of the smelting reduction furnace. A smelting reduction device equipped with a cutting means for cutting ore dropped from the fluidized bed into a wind box through a dispersion plate into a smelting reduction furnace; (2) the wind box is provided with an exhaust gas duct; The smelting reduction device according to (1), wherein the volume below the position is equal to or more than the volume of ore retained in the fluidized bed, (3) the wind box is at the bottom, when the operation of the smelting reduction furnace is stopped. It is specially connected to a fallen pipe discharge system that discharges ore retained in the wind box to the outside of the system. A smelting reduction apparatus according to (1) or (2) and.
【0009】[0009]
【発明の実施の形態】以下、図1を参照して本発明の溶
融還元装置の実施の形態を説明する。この装置は、溶融
還元炉10と、予備還元炉20とを備えている。溶融還
元炉は、頂部から内部に向けて酸素ランス11を装入し、
溶融還元により炉内にメタル層12とスラグ層13とを
形成する。予備還元炉は、分散板21を介して、その上部
に流動層22を、下部に風箱23を形成している。さら
に、予備還元炉の風箱側部と溶融還元炉の頂部との間に
は排ガスダクト30が接続され、溶融還元炉で発生した
排ガスを風箱に導入し、分散板を通して流動層に吹込む
ようになっている。前記風箱は、排ガスダクトの取付位
置より下部の風箱容積が鉱石の流動層内滞留量以上とな
っているのが望ましい。また、予備還元炉の上側部には
原料鉱石の装入管31が取付けられ、上部にはサイクロ
ン32が装着されている。サイクロン底部には溶融還元
炉頂部との間に微粒系配管33が接続され、この微粒系
配管に切出し装置34が取付けられている。また、予備
還元炉の流動層の位置から溶融還元炉上側部に粗粒系配
管35が接続され、ここに切出し装置36が装着されて
いる。次に、風箱底部と溶融還元炉上側部との間に落鉱
系配管37が接続され、ここに切出し装置38が装着さ
れている。さらに、風箱底部に落鉱系外排出系配管39
が接続され、ここに落鉱系外排出系開閉弁42が装着さ
れている。前記排ガスダクト30には排ガス流量計40
が装着され、この流量計の流量検知信号により溶融還元
炉のシャットダウンを検出し、このシャットダウン検出
信号により、前記落鉱系開閉弁41が閉じられ、他方、
落鉱系外排出系開閉弁42が開くようになっている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a smelting reduction apparatus according to the present invention will be described below with reference to FIG. This apparatus includes a smelting reduction furnace 10 and a preliminary reduction furnace 20. The smelting reduction furnace is charged with an oxygen lance 11 from the top toward the inside,
A metal layer 12 and a slag layer 13 are formed in the furnace by smelting reduction. The pre-reduction furnace has a fluidized bed 22 formed at an upper portion thereof and a wind box 23 formed at a lower portion thereof via a dispersion plate 21. Further, an exhaust gas duct 30 is connected between the wind box side of the preliminary reduction furnace and the top of the smelting reduction furnace, so that the exhaust gas generated in the smelting reduction furnace is introduced into the wind box and blown into the fluidized bed through the dispersion plate. Has become. In the wind box, the volume of the wind box below the mounting position of the exhaust gas duct is desirably equal to or more than the amount of ore retained in the fluidized bed. A raw ore charging pipe 31 is attached to the upper part of the preliminary reduction furnace, and a cyclone 32 is attached to the upper part. A fine particle pipe 33 is connected to the bottom of the cyclone and the top of the smelting reduction furnace, and a cutout device 34 is attached to the fine particle pipe. A coarse-grained piping 35 is connected from the position of the fluidized bed of the preliminary reduction furnace to the upper part of the smelting reduction furnace, and a cutout device 36 is mounted here. Next, an ore dropping pipe 37 is connected between the bottom of the wind box and the upper part of the smelting reduction furnace, and a cutout device 38 is mounted here. Further, a pipe 39 outside the dropping system is installed at the bottom of the wind box.
Is connected, and a non-mineralized discharge system on-off valve 42 is mounted here. An exhaust gas flow meter 40 is provided in the exhaust gas duct 30.
Is attached, a shutdown of the smelting reduction furnace is detected by a flow rate detection signal of the flow meter, and the downfall opening / closing valve 41 is closed by the shutdown detection signal.
The off-mineral discharge system open / close valve 42 is opened.
【0010】以上のように、この装置は、予備還元炉か
ら溶融還元炉への鉱石供給は、粗粒系、微粒系および落
鉱系の3系統を備えている。粗粒系と微粒系の供給は各
切り出し装置34,36によって定量的に行なわれる。
落鉱系は、風箱へ落ちた鉱石を切り出し装置38によっ
て、落鉱量だけ定量的に切り出す。As described above, this apparatus is provided with three systems of ore supply from the pre-reduction furnace to the smelting reduction furnace: coarse-grain system, fine-grain system, and ore drop system. The supply of the coarse-grained system and the fine-grained system is quantitatively performed by the respective cutting devices 34 and 36.
In the falling ore system, the ore that has fallen into the wind box is quantitatively cut out by the cutting device 38 by the amount of ore fall.
【0011】落鉱を定量的に切出すことによって、溶融
還元炉への鉱石供給の高精度化、高応答性が図れる。ま
た、層内ガス流速は変更しないため、良好な流動層内流
動化状況を安定して実現可能である。The ore supply to the smelting reduction furnace can be performed with high precision and high responsiveness by quantitatively cutting out ore droppings. Further, since the gas flow rate in the bed is not changed, a good fluidized state in the fluidized bed can be stably realized.
【0012】次に、溶融還元炉のシャットダウン時、落
鉱系開閉弁41が閉じられ、層内滞留鉱石が全量ダクト
下の風箱内に堆積される。従って、これによって、シャ
ットダウン時の溶融還元炉内の鉱石流れ込み防止がで
き、しかも排ガスダクト30の、落鉱鉱石による閉塞防止
が実現し、溶融還元炉の安定操業が可能となる。Next, when the smelting reduction furnace is shut down, the ore dropping on-off valve 41 is closed, and the ore accumulated in the formation is entirely deposited in the wind box below the duct. Therefore, it is possible to prevent ore from flowing into the smelting reduction furnace at the time of shutdown, and also to prevent the exhaust gas duct 30 from being clogged by falling ore, thereby enabling stable operation of the smelting reduction furnace.
【0013】さらに、溶融還元炉のシャットダウンと連
動して、落鉱系外排出系開閉弁42が開放され、一時的
に落鉱鉱石を系外に排出する。これによって風箱23の縮
小化が図られ、予備還元炉のコンパクト化が可能にな
る。Further, in conjunction with the shutdown of the smelting reduction furnace, the off-mineralized discharge system on-off valve 42 is opened, and the ore-mineralized ore is temporarily discharged outside the system. As a result, the size of the wind box 23 is reduced, and the size of the preliminary reduction furnace can be reduced.
【0014】[0014]
【実施例】図1に示す装置において、 生産量:3000t/d 、 流動層炉径:7.2m 流動層炉高:分散板上7m 炉内鉱石滞留量:56t 風箱容積(ダクト下):120m3 の予備還元炉構成とし、予備還元炉への給鉱量に対して
所定の割合(例えば2%)で落鉱するので、この落鉱量
と等しくなるように落鉱系の切出し量を設定した。ま
た、落鉱切出しのタイミングは、予備還元炉への給鉱開
始時に開始し、予備還元炉に鉱石滞留量がなくなつた時
に終了した。[Example] In the apparatus shown in FIG. 1, production volume: 3000 t / d, fluidized bed furnace diameter: 7.2 m, fluidized bed furnace height: 7 m above the dispersion plate, ore retention in the furnace: 56 t, wind box volume (under the duct): The pre-reduction furnace is composed of 120 m 3 , and the ore is dropped at a predetermined ratio (for example, 2%) with respect to the amount of ore supplied to the pre-reduction furnace. Set. The timing of ore dropping was started at the start of ore supply to the pre-reduction furnace, and ended when the amount of ore stagnant in the pre-reduction furnace was exhausted.
【0015】しかして、上記の操業条件で操業を行った
結果、流動内の良好な流動化状況を安定して形成し、所
定の還元性能が得られることが認められた。さらに、ダ
ストロスの増大を防ぎ、しかも溶融還元炉への供給量制
御が容易で、さらにまた溶融還元炉のシャットダウン時
に再立ち上げが容易であることが確認された。Thus, as a result of operating under the above operating conditions, it was confirmed that a favorable fluidization state in the flow was formed stably, and a predetermined reducing performance was obtained. Furthermore, it was confirmed that an increase in dust loss was prevented, the supply amount to the smelting reduction furnace was easily controlled, and further, the smelting reduction furnace was easily restarted when shutting down.
【0016】[0016]
【発明の効果】以上のように本発明によれば、落鉱量を
制御するのにノズル内ガス流速を調整することがないの
で、流動層内の良好な流動化状況を安定して形成するこ
とができる。その結果、所定の還元性能が得られ、かつ
ダストロスの増大を阻止することができる。更に、落鉱
量の供給量制御を直接行うことができるため、その応答
性及び精度を向上することができる。更に、溶融還元炉
のシャットダウン時には、落鉱を系外に排出するため、
再立ち上げが容易となるなど顕著な効果を発揮する。As described above, according to the present invention, since the gas flow rate in the nozzle is not adjusted for controlling the amount of ore dropping, a good fluidized state in the fluidized bed is stably formed. be able to. As a result, a predetermined reduction performance can be obtained, and an increase in dust loss can be prevented. Further, since the supply control of the ore dropping amount can be directly performed, the responsiveness and accuracy thereof can be improved. Furthermore, when shutting down the smelting reduction furnace, the ore drop is discharged outside the system,
It has a remarkable effect such as easy restart.
【図1】本発明の溶融還元炉の概略説明図。FIG. 1 is a schematic explanatory view of a smelting reduction furnace of the present invention.
【図2】特開平4-63216 号に記載された溶融還元炉の概
略説明図。FIG. 2 is a schematic explanatory view of a smelting reduction furnace described in JP-A-4-63216.
10... 溶融還元炉、11... 酸素ランス、12... メタル
層、13... スラグ層、11... 予備還元炉、21... 分散
板、22... 流動層、23... 風箱、 30...排ガスダクト、
31... 原料鉱石の装入管、32... サイクロン、33... 微
粒系配管、34...出し装置、35... 粗粒系配管、36...
切出し装置、37... 落鉱系配管、38... 切出し装置、3
9... 落鉱系外排出系配管、40... 排ガス流量計、41...
落鉱系開閉弁、42... 落鉱系外排出系開閉弁10 ... Smelting reduction furnace, 11 ... Oxygen lance, 12 ... Metal layer, 13 ... Slag layer, 11 ... Pre-reduction furnace, 21 ... Dispersion plate, 22 ... Fluidized bed , 23 ... wind box, 30 ... exhaust gas duct,
31 ... Raw material ore charging pipe, 32 ... cyclone, 33 ... fine-grained piping, 34 ... dispensing device, 35 ... coarse-grained piping, 36 ...
Cutting device, 37 ... Plumbing pipe, 38 ... Cutting device, 3
9 ... Exhaust pipes outside the dropping system, 40 ...
Dropping-type on-off valve, 42 ...
───────────────────────────────────────────────────── フロントページの続き (72)発明者 関口 毅 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 渡部 雅之 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 (72)発明者 岩崎 克博 東京都千代田区丸の内一丁目1番2号 日 本鋼管株式会社内 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takeshi Sekiguchi 1-1-2 Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Co., Ltd. (72) Inventor Masayuki Watanabe 1-2-1, Marunouchi, Chiyoda-ku, Tokyo Sun (72) Inventor Katsuhiro Iwasaki 1-2-1 Marunouchi, Chiyoda-ku, Tokyo Nihon Kokan Co., Ltd.
Claims (3)
層を形成した予備還元炉と、予備還元炉の流動層で予備
還元された鉱石が装入される溶融還元炉と、この溶融還
元炉の上部から予備還元炉の風箱内に接続した排ガスダ
クトとを具備した溶融還元装置において、 前記風箱の底部と前記溶融還元炉上部との間に落鉱系管
路を接続し、この管路に、流動層から分散板を通って風
箱内に落鉱された鉱石を溶融還元炉へ切り出す切出し手
段を装着したことを特徴とする溶融還元装置。1. A pre-reduction furnace having a wind box at the lower part and a fluidized bed formed at the upper part via a dispersion plate, a smelting reduction furnace into which the ore pre-reduced by the fluidized bed of the pre-reduction furnace is charged. In a smelting reduction apparatus comprising an exhaust gas duct connected from the upper part of the smelting reduction furnace to the wind box of the preliminary reduction furnace, a fallen pipe is connected between the bottom part of the wind box and the upper part of the smelting reduction furnace. A smelting reduction apparatus, characterized in that a cut-out means for cutting ore dropped from a fluidized bed through a dispersion plate into a wind box into a smelting reduction furnace is attached to the conduit.
り下部の容積が、鉱石の流動層内滞留量容積以上である
ことを特徴とする請求項1に記載の溶融還元装置。2. The smelting reduction apparatus according to claim 1, wherein a volume of the wind box below a mounting position of an exhaust gas duct is equal to or more than a volume of ore retained in a fluidized bed.
止時に風箱内滞留鉱石を系外に排出する落鉱系外排出系
管路を接続したことを特徴とする請求項1または2に記
載の溶融還元装置。3. A discharge system outside the ore dropping system for discharging ore retained in the wind box outside the system when the operation of the smelting reduction furnace is stopped is connected to the bottom of the wind box. 3. The smelting reduction device according to 2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33428297A JPH11172309A (en) | 1997-12-04 | 1997-12-04 | Smelting reduction apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33428297A JPH11172309A (en) | 1997-12-04 | 1997-12-04 | Smelting reduction apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11172309A true JPH11172309A (en) | 1999-06-29 |
Family
ID=18275603
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33428297A Pending JPH11172309A (en) | 1997-12-04 | 1997-12-04 | Smelting reduction apparatus |
Country Status (1)
Country | Link |
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JP (1) | JPH11172309A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100360109B1 (en) * | 2000-12-19 | 2002-11-07 | 주식회사 포스코 | fludized bed type Smelting reduction apparatus and method for recycling fines |
KR100391914B1 (en) * | 2001-08-28 | 2003-07-16 | 주식회사 포스코 | Process for coal based ironmaking to reduce loss of fine ore |
KR100435443B1 (en) * | 2001-08-09 | 2004-06-10 | 주식회사 포스코 | Byproduct sludge recycling apparatus in ironmaking system |
KR100568342B1 (en) * | 2001-10-17 | 2006-04-05 | 주식회사 포스코 | An apparatus for recycking incompletely-reduced fine iron ore and, a method for recycling and treating at emergency the incompletely-reduced fine iron ore by using the same apparatus in a fluidized-bed reduction process |
KR101009019B1 (en) | 2003-12-29 | 2011-01-17 | 주식회사 포스코 | Sludge ejection device of fluidized reduction furnace |
-
1997
- 1997-12-04 JP JP33428297A patent/JPH11172309A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100360109B1 (en) * | 2000-12-19 | 2002-11-07 | 주식회사 포스코 | fludized bed type Smelting reduction apparatus and method for recycling fines |
KR100435443B1 (en) * | 2001-08-09 | 2004-06-10 | 주식회사 포스코 | Byproduct sludge recycling apparatus in ironmaking system |
KR100391914B1 (en) * | 2001-08-28 | 2003-07-16 | 주식회사 포스코 | Process for coal based ironmaking to reduce loss of fine ore |
KR100568342B1 (en) * | 2001-10-17 | 2006-04-05 | 주식회사 포스코 | An apparatus for recycking incompletely-reduced fine iron ore and, a method for recycling and treating at emergency the incompletely-reduced fine iron ore by using the same apparatus in a fluidized-bed reduction process |
KR101009019B1 (en) | 2003-12-29 | 2011-01-17 | 주식회사 포스코 | Sludge ejection device of fluidized reduction furnace |
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