JPH09157719A - Smelting reduction apparatus of iron - Google Patents
Smelting reduction apparatus of ironInfo
- Publication number
- JPH09157719A JPH09157719A JP31446095A JP31446095A JPH09157719A JP H09157719 A JPH09157719 A JP H09157719A JP 31446095 A JP31446095 A JP 31446095A JP 31446095 A JP31446095 A JP 31446095A JP H09157719 A JPH09157719 A JP H09157719A
- Authority
- JP
- Japan
- Prior art keywords
- reduction furnace
- smelting reduction
- furnace
- ore
- smelting
- 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
Links
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- Manufacture And Refinement Of Metals (AREA)
- Manufacture Of Iron (AREA)
- Furnace Details (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は鉄の溶融還元装置に
関するものである。TECHNICAL FIELD The present invention relates to an iron smelting reduction apparatus.
【0002】[0002]
【従来の技術】鉄鉱石の溶融還元法は粒度の細かい、鉄
鉱石、石炭、副原料等の原料を直接溶融還元装置に投入
できるので、焼結工場およびコ−クス工場が不要とな
り、高炉製鉄法に比べて経済的であり、両工場で発生し
ていた環境問題も解決できる優れた製鉄法となってい
る。2. Description of the Related Art In the smelting reduction method of iron ore, raw materials such as iron ore, coal, and auxiliary raw materials having a fine grain size can be directly charged into a smelting reduction apparatus, so that a sinter plant and a coke plant are not required, and blast furnace steelmaking This is an excellent steelmaking method that is more economical than the law and can solve the environmental problems that have occurred at both plants.
【0003】鉄鉱石の溶融還元法は、溶融還元炉を用い
鉄鉱石を溶融状態で還元して、銑鉄を得る方法である。
溶融還元炉は反応が速やかで生産性を弾力的に調整でき
る一方、エネルギー利用率が低いので、これに予備還元
炉を併設して溶融還元装置が構成されることが多い。The smelting reduction method of iron ore is a method of obtaining pig iron by reducing iron ore in a molten state using a smelting reduction furnace.
While the smelting reduction furnace has a quick reaction and can adjust the productivity elastically, it has a low energy utilization rate, so that a smelting reduction apparatus is often constructed with a preliminary reduction furnace.
【0004】予備還元炉には、溶融還元炉で発生するC
Oを主体とする高温ガスが、還元用ガスとして導入され
る。予備還元炉内の鉄鉱石は固体状態で予備還元、且つ
予熱され、溶融還元炉に装入される。予備還元炉として
は、粒状、粉状の鉄鉱石の還元に適した流動層式が採用
されるのが一般的であり、従来の溶融還元装置は、鉄浴
式の溶融還元炉と流動層式の予備還元炉より構成され、
操業時には溶融還元炉から高温の還元性ガスが発生し、
高温の還元性ガスは管路を通じて溶融還元炉の上部から
予備還元炉の下部に導入され、予備還元炉で鉄鉱石の予
熱と予備還元が行われる。In the preliminary reduction furnace, C generated in the smelting reduction furnace is used.
A high temperature gas containing O as a main component is introduced as a reducing gas. The iron ore in the pre-reduction furnace is pre-reduced and pre-heated in the solid state, and charged into the smelting reduction furnace. As a preliminary reduction furnace, a fluidized bed type that is suitable for the reduction of granular or powdery iron ore is generally adopted.The conventional smelting reduction apparatus is an iron bath type smelting reduction furnace and a fluidized bed type. It consists of a preliminary reduction furnace of
During operation, high-temperature reducing gas is generated from the smelting reduction furnace,
The high-temperature reducing gas is introduced from the upper part of the smelting reduction furnace to the lower part of the pre-reduction furnace through a pipe, and the pre-reduction furnace preheats and pre-reduces the iron ore.
【0005】これらの従来の溶融還元装置の一例とし
て、特開平4−63216号公報で開示された装置を図
2に示す。この装置は予備還元炉1と溶融還元炉11が
管路21により直結されており、管路21が溶融還元炉
11から予備還元炉1への還元性ガスの通路と、予備還
元炉1から溶融還元炉11への予熱・予備還元された鉱
石の通路を兼ねていて、管路21の途中にダスト回収装
置を持たない溶融還元装置であり、溶融還元炉11から
の高温の発生ガスを温度を低下させることなく、予備還
元炉1において有効に利用できるようになっている。As an example of these conventional smelting reduction apparatuses, the apparatus disclosed in Japanese Patent Laid-Open No. 4-63216 is shown in FIG. In this apparatus, the pre-reduction furnace 1 and the smelting reduction furnace 11 are directly connected by a pipe line 21, and the pipe line 21 connects the reducing gas passage from the smelting reduction furnace 11 to the pre-reduction furnace 1 and melts it from the pre-reduction furnace 1. It is a smelting reduction apparatus that also serves as a passage for ore that has been preheated / preliminarily reduced to the reduction furnace 11, and does not have a dust recovery device in the middle of the pipeline 21. It can be effectively used in the preliminary reduction furnace 1 without lowering it.
【0006】この溶融還元装置においては、予備還元炉
1の流動層室4に鉄鉱石投入管を通じて投入された鉄鉱
石は、分散板2上で予熱・予備還元される。操業時には
分散板2より落鉱が発生するが、これらの落鉱は風箱3
に滞留することなく直ちに管路21を通じて溶融還元炉
11に落下する構造となっているので、落鉱は風箱3に
長時間溜まることがなく、風箱内で落鉱が固着すること
がない。In this smelting reduction apparatus, the iron ore charged into the fluidized bed chamber 4 of the preliminary reduction furnace 1 through the iron ore charging pipe is preheated and preliminarily reduced on the dispersion plate 2. During operation, falling slag is generated from the dispersion plate 2.
Because the structure is such that it does not stay in the smelting furnace and immediately falls into the smelting reduction furnace 11 through the pipe line 21, the falling ore does not accumulate in the wind box 3 for a long time, and the falling ore does not stick in the wind box. .
【0007】[0007]
【発明が解決しようとする課題】しかしながら、特開平
4−63216号公報で開示された溶融還元装置では、
排ガス顕熱の損失は少ないが、操業条件によって落鉱が
増加した場合には、溶融還元炉の操業に以下のような悪
影響を及ぼすことがある。However, in the smelting reduction apparatus disclosed in Japanese Patent Laid-Open No. 4-63216,
Although the loss of sensible heat of exhaust gas is small, if the falling mine increases due to operating conditions, the operation of the smelting reduction furnace may be adversely affected as follows.
【0008】この溶融還元装置では、予備還元炉下流
側、即ち排ガス管6の後にダンパー27を設け、そのダ
ンパ27の開度を調整して、分散板2を通過する溶融還
元炉11からの発生ガスの流速を調整している。分散板
2での発生ガス流速の調整により、予熱・予備還元され
た鉄鉱石の溶融還元炉11への装入量を調整している。
このため分散板2上へ投入された鉄鉱石が一時的に増加
した場合、または溶融還元炉11の操業において送酸量
の低下や送酸停止により、溶融還元炉11からの発生ガ
ス量が急激に減少して分散板2を通過するガス流速が急
激に低下した場合には、短時間に鉱石装入量が増加する
事態、所謂、落鉱が発生する。In this smelting reduction apparatus, a damper 27 is provided on the downstream side of the preliminary reduction furnace, that is, after the exhaust gas pipe 6, the opening degree of the damper 27 is adjusted, and the smelting reduction furnace 11 passing through the dispersion plate 2 is generated. The gas flow rate is adjusted. The amount of preheated / pre-reduced iron ore charged into the smelting reduction furnace 11 is adjusted by adjusting the flow rate of the generated gas in the dispersion plate 2.
Therefore, when the amount of iron ore put on the dispersion plate 2 is temporarily increased, or when the smelting reduction furnace 11 is in operation, the amount of oxygen fed is reduced or stopped. When the flow velocity of the gas passing through the dispersion plate 2 is rapidly reduced, the situation in which the ore charging amount increases in a short time, so-called falling mine occurs.
【0009】このような緊急時に予備還元炉1への鉱石
装入量を制御することは極めて困難であり、予熱・予備
還元の不充分な鉄鉱石の落鉱が発生した場合や、溶融還
元炉11の溶銑温度が低い場合には、落鉱によって溶銑
温度がさらに低下して炉況は悪化する。最悪の場合は熱
不足により溶融還元炉11の操業が不可能になる場合が
あった。It is extremely difficult to control the amount of ore charged in the preliminary reduction furnace 1 in such an emergency, and when iron ore falling occurs due to insufficient preheating and preliminary reduction, or in the smelting reduction furnace. When the hot metal temperature of No. 11 is low, the hot metal temperature further decreases due to falling rock, and the furnace condition deteriorates. In the worst case, the operation of the smelting reduction furnace 11 may become impossible due to insufficient heat.
【0010】また、この溶融還元装置では、溶融還元炉
から発生するダストの分離装置を持たないために、溶融
還元炉11に投入した原料量(特に炭材)に対しダスト
としてロスする量が把握できないので、操業時の重要な
指針の一つである投入成分の炉内残存量を知ることがで
きず、従って、溶融還元炉内は高反応性条件下であるた
め常に迅速な操業アクションを必要とするにもかかわら
ず、溶融還元炉内の製錬反応状態が全く把握できない。Further, since this smelting reduction apparatus does not have a separating device for the dust generated from the smelting reduction furnace, the amount of dust lost with respect to the amount of raw material (particularly carbonaceous material) charged into the smelting reduction furnace 11 is grasped. Since it is not possible to know the remaining amount of the input components in the furnace, which is one of the important guidelines during operation, it is necessary to always take prompt operation action because the inside of the smelting reduction furnace is under highly reactive conditions. However, the smelting reaction state in the smelting reduction furnace cannot be grasped at all.
【0011】さらに、溶融還元炉へ投入される鉄鉱石が
予備還元炉の分散板上で流動化している間に鉄鉱石と発
生ダストが接触するために、投入される鉄鉱石の表面に
発生ダストが付着し鉄鉱石と還元用ガスとの接触が妨げ
られ、鉄鉱石の予熱・予備還元が遅れて不充分となるこ
とがあった。Furthermore, since the iron ore charged to the smelting reduction furnace contacts the generated dust while the iron ore is fluidized on the dispersion plate of the preliminary reduction furnace, the generated dust on the surface of the charged iron ore. Sometimes adhered to the iron ore and prevented the contact between the iron ore and the reducing gas, and the preheating / pre-reduction of the iron ore was delayed and became insufficient.
【0012】本発明は、このような課題を解決するする
ためになされたものであって、溶融還元炉からの発生ガ
ス顕熱を予備還元炉において有効に利用でき、かつ操業
中の落鉱の悪影響を解消し、落鉱およびダストの発生量
および性状を充分に把握することができる溶融還元装置
を提供するものである。The present invention has been made in order to solve such a problem, and the sensible heat of the gas generated from the smelting reduction furnace can be effectively used in the preliminary reduction furnace, and the slag produced during operation It is intended to provide a smelting reduction apparatus capable of eliminating adverse effects and sufficiently grasping the amount and properties of falling mine and dust.
【0013】[0013]
【課題を解決するための手段】本発明の鉄の溶融還元装
置は、溶融還元炉と、その発生ガスを還元用ガスとして
下部の風箱から導入して分散板上の鉄鉱石に接触させた
後に上方の排ガス管より排出する流動層式予備還元炉
と、溶融還元炉と予備還元炉の風箱側壁部を繋ぎ発生ガ
スを導入する管路と、流動層下部より予備還元された鉄
鉱石を溶融還元炉の炉口に排出する予備還元鉱石の排出
管と、風箱底部の排出孔を介して発生ガスのダストと分
散板からの落鉱とを集めて分別回収する回収装置とから
なることを特徴とする鉄鉱石の溶融還元装置である。In the iron smelting reduction apparatus of the present invention, a smelting reduction furnace and its generated gas are introduced as a reducing gas from a lower wind box and brought into contact with iron ore on a dispersion plate. Later, a fluidized bed type pre-reduction furnace that discharges from the upper exhaust gas pipe, a pipeline that connects the smelting reduction furnace and the side wall of the wind box of the pre-reduction furnace, and introduces the generated gas, and the iron ore that is pre-reduced from the lower part of the fluidized bed It consists of a discharge pipe for preliminary reduced ore discharged to the furnace mouth of the smelting reduction furnace, and a recovery device for collecting and separately collecting dust of generated gas and falling ore from the dispersion plate through the discharge hole at the bottom of the wind box. Is a smelting reduction apparatus for iron ore.
【0014】溶融還元炉と予備還元炉の風箱とを管路で
直接繋ぐので、溶融還元炉からの発生ガス顕熱を予備還
元炉において有効に利用できる。更に、風箱にて発生ガ
スが保持しているダストと予備還元炉の分散板からの落
鉱とを集めて、このダストと落鉱とを排出する排出孔
と、排出孔より排出されたダストと落鉱とを回収する回
収装置とを設けているので、分散板上へ投入された鉄鉱
石が一時的に増加したり、または溶融還元炉の操業にお
いて送酸ダウンや送酸停止により溶融還元炉からの発生
ガス量が急激に減少して、分散板ノズルでのガス流速が
急激に低下しても、発生ガスを導入する管路が風箱側壁
部に開口しているので、鉄鉱石は直接溶融還元炉に落下
せず、回収装置で回収できる。Since the smelting reduction furnace and the air box of the preliminary reduction furnace are directly connected by the pipe line, the sensible heat of the gas generated from the smelting reduction furnace can be effectively used in the preliminary reduction furnace. Further, the dust held by the generated gas in the wind box and the falling ore from the dispersion plate of the preliminary reduction furnace are collected, and the discharge hole for discharging the dust and the falling ore and the dust discharged from the discharge hole. Since a recovery device is installed to recover the iron ore and the iron ore, the iron ore put on the dispersion plate temporarily increases, or the smelting reduction is performed by stopping or stopping the acid transfer during the operation of the smelting reduction furnace. Even if the amount of gas generated from the furnace sharply decreases and the gas flow velocity at the dispersion plate nozzle sharply decreases, the pipe for introducing the generated gas opens at the side wall of the wind box, so iron ore It can be recovered by a recovery device without falling directly to the smelting reduction furnace.
【0015】したがって溶融還元炉の操業を乱すことな
く、また落鉱およびダストの発生量が正確に把握できる
ので、安定した操業ができる。Therefore, the operation of the smelting reduction furnace is not disturbed, and the amount of falling ore and dust generated can be accurately grasped, so that stable operation can be performed.
【0016】[0016]
【発明の実施の形態】以下、本発明の詳細を図面に基い
て説明する。図1に本発明による溶融還元装置の概要断
面図を示す。DESCRIPTION OF THE PREFERRED EMBODIMENTS The details of the present invention will be described below with reference to the drawings. FIG. 1 shows a schematic sectional view of a smelting reduction apparatus according to the present invention.
【0017】予備還元炉1は、分散板2と風箱3と流動
層室4と排ガス管6とより構成され、流動層室4には鉄
鉱石の投入管5が配置されている。流動層室4で予熱・
予備還元された鉄鉱石は予備還元鉱石の排出管7より排
出される。この予備還元炉1の予備還元鉱石の排出管7
は、溶融還元炉11の予熱・予備還元された鉄鉱石の投
入管16と配管で接続されている。風箱3の下部には、
落鉱およびダストを排出する排出孔8が配置されてい
る。排出孔8には排出用配管9が接続され、排出用配管
9は更に回収装置10に接続されている。回収装置10
は、主に落鉱を回収する落鉱回収タンク10aと、主に
発生ガス中のダストを回収するダスト回収タンク10b
から構成されている。排出用配管9には、付着防止用の
パ−ジ配管22と付着検知器23を少なくとも一箇以上
設置する。The preliminary reduction furnace 1 is composed of a dispersion plate 2, a wind box 3, a fluidized bed chamber 4 and an exhaust gas pipe 6, and an iron ore charging pipe 5 is arranged in the fluidized bed chamber 4. Preheating in fluidized bed chamber 4
The pre-reduced iron ore is discharged from the pre-reduced ore discharge pipe 7. Preliminary reduction ore discharge pipe 7 of this preliminary reduction furnace 1
Is connected by a pipe to a preheating / pre-reduction iron ore charging pipe 16 of the smelting reduction furnace 11. At the bottom of the wind box 3,
A discharge hole 8 for discharging falling rocks and dust is arranged. A discharge pipe 9 is connected to the discharge hole 8, and the discharge pipe 9 is further connected to a recovery device 10. Recovery device 10
Is a rock fall recovery tank 10a that mainly collects rock fall, and a dust recovery tank 10b that mainly collects dust in the generated gas.
It is composed of In the discharge pipe 9, at least one or more adhering prevention purge pipes 22 and adhering detectors 23 are installed.
【0018】溶融還元炉11は炉体12とフ−ド13か
ら構成され、炉体12の底には鉄浴14が溜められ、炉
体12は炉体支持装置15によって支持され、鉄浴14
を攪拌するガス吹込み管19などが接続されている。フ
−ド13には還元された鉄鉱石の投入管16、石炭およ
び副原料の投入管17、酸素吹込み用ランス18、ダス
ト吹込み管20、および管路21などが接続されてい
る。The smelting reduction furnace 11 is composed of a furnace body 12 and a hood 13. An iron bath 14 is stored in the bottom of the furnace body 12, and the furnace body 12 is supported by a furnace body supporting device 15, and the iron bath 14 is
A gas blowing pipe 19 for stirring the gas is connected. Connected to the hood 13 are a reduced iron ore charging pipe 16, a coal and auxiliary raw material charging pipe 17, an oxygen blowing lance 18, a dust blowing pipe 20, and a pipeline 21.
【0019】そして炉体12は、フ−ド13、管路21
を介して、予備還元炉1の風箱3の側壁に繋がってい
る。The furnace body 12 includes a hood 13 and a conduit 21.
Is connected to the side wall of the wind box 3 of the preliminary reduction furnace 1.
【0020】管路21は発生ガス中のダストが通過する
ため、管路21内の水平部下面や曲り部などのダストが
堆積しやすい箇所には、付着防止用のパ−ジ配管22と
付着検知器23を少なくとも1箇所以上に設置する。な
お付着検知器23としては圧力計あるいは温度計を使用
する。Since dust in the generated gas passes through the pipe 21, the purge pipe 22 for preventing adhesion is attached to a portion such as the lower surface of the horizontal portion or the bent portion in the pipe 21 where dust is likely to accumulate. The detectors 23 are installed in at least one place. A pressure gauge or a thermometer is used as the adhesion detector 23.
【0021】管路21に付着せずに通過する発生ガス中
のダストは、予備還元炉1の風箱3に入った途端に発生
ガスの流速が大きく低下するため、ダストの大半が風箱
3内の下部の排出用配管9の方向へ自然落下して回収さ
れる。なお管路21と予備還元炉1の風箱3の接合部で
は、例えば堰24を設けたり、あるいは接合部の管路2
1の内径をその他の部分より縮小あるいは拡大するなど
して、発生ガスの流れを強制的に変更してダストをより
回収し易くしても良い。The dust in the generated gas that passes without adhering to the pipe 21 has a large decrease in the flow velocity of the generated gas as soon as it enters the wind box 3 of the preliminary reduction furnace 1, so most of the dust is in the wind box. It is naturally dropped in the direction of the discharge pipe 9 in the lower part of the inside 3 and collected. In addition, for example, a weir 24 is provided at the joint between the pipe 21 and the wind box 3 of the preliminary reduction furnace 1, or the pipe 2 at the joint is formed.
The flow of the generated gas may be forcibly changed by making the inner diameter of 1 smaller or larger than that of the other portion to make it easier to collect dust.
【0022】予備還元炉1の風箱3下部に回収されたダ
ストは排出用配管9を通じて風箱3の外部へ排出され
る。図1では風箱3からの排出用配管9を1本とし、落
鉱とダストを同じ排出用配管9より排出できるようにす
ることで装置のコンパクト化を図っている。The dust collected in the lower part of the wind box 3 of the preliminary reduction furnace 1 is discharged to the outside of the wind box 3 through the discharge pipe 9. In FIG. 1, the number of discharge pipes 9 from the wind box 3 is one, and the falling mine and the dust can be discharged from the same discharge pipe 9 to make the apparatus compact.
【0023】通常の操業中においては、分散板2での発
生ガスの流速が充分に確保されているために分散板2か
らの落鉱がほとんど無いので、落鉱回収タンク10a上
のバルブ25を閉じ、ダスト回収タンク10b上のバル
ブ26を開にして、風箱3で回収されたダストを排出用
配管9を通じてダスト回収タンク10bの方へ流れるよ
うにして回収する。ダスト回収タンク10bに回収した
ダストは発生量や成分値を測定した後、ダスト吹込み管
20により溶融還元炉11へ投入する。During normal operation, since the flow velocity of the gas generated in the dispersion plate 2 is sufficiently secured, there is almost no falling mine from the dispersion plate 2, so the valve 25 on the falling mine recovery tank 10a is set. Close and open the valve 26 on the dust recovery tank 10b to collect the dust collected in the wind box 3 through the discharge pipe 9 toward the dust recovery tank 10b. The amount of dust collected in the dust collection tank 10b and the component value are measured, and then the dust is introduced into the smelting reduction furnace 11 through the dust blowing pipe 20.
【0024】溶融還元炉11で異常が発生した場合、あ
るいは溶融還元炉11の操業立上げや操業停止する場合
には、落鉱が多量に発生するので、バルブ25を開にし
て、バルブ26を閉にすることにより、落鉱とダストの
混合したものを落鉱回収タンク10aに回収する。そし
て溶融還元炉11の操業状況が回復あるいは安定するま
では、溶融還元炉11へはダストを投入せずに系外へ排
出するようにして溶融還元炉11の操業を維持する。溶
融還元炉11の操業が回復あるいは安定したら、ダスト
回収タンク10bにてダストの回収を再開する。When an abnormality occurs in the smelting reduction furnace 11, or when the operation of the smelting reduction furnace 11 is started or stopped, a large amount of mine ore is generated, so valve 25 is opened and valve 26 is opened. By closing, a mixture of fallen rock and dust is collected in the fallen rock collection tank 10a. Then, until the operation status of the smelting reduction furnace 11 is recovered or stabilized, the operation of the smelting reduction furnace 11 is maintained by discharging the dust to the outside of the system without introducing the dust into the smelting reduction furnace 11. When the operation of the smelting reduction furnace 11 is restored or stabilized, the dust recovery is resumed in the dust recovery tank 10b.
【0025】[0025]
【発明の効果】本発明によれば、溶融還元炉からの発生
ガスの顕熱を予備還元炉で有効に利用でき、ダスト及び
落鉱の発生量と炉内残存量を正確に把握できるので、操
業条件の変動による操業の立上り、操業停止のような場
合でも、回収装置を使用することにより溶融還元炉への
悪影響を完全に解消でき、安定した操業が得られる。According to the present invention, the sensible heat of the gas generated from the smelting reduction furnace can be effectively utilized in the preliminary reduction furnace, and the generation amount of dust and falling mine and the remaining amount in the furnace can be accurately grasped. Even when the start-up or stop of the operation due to fluctuations in the operating conditions, the adverse effect on the smelting reduction furnace can be completely eliminated by using the recovery device, and stable operation can be obtained.
【図1】本発明の溶融還元装置の概略断面図である。FIG. 1 is a schematic sectional view of a smelting reduction apparatus of the present invention.
【図2】従来の溶融還元装置の概略断面図である。FIG. 2 is a schematic sectional view of a conventional smelting reduction apparatus.
1 予備還元炉 2 分散板 3 風箱 4 流動層室 5 鉄鉱石の投入管 6 排ガス管 7 予備還元鉱石の排出管 8 排出孔 9 排出用配管 10 回収装置 11 溶融還元炉 12 炉体 13 フ−ド 14 鉄浴(溶鉄) 21 管路 1 Pre-reduction furnace 2 Dispersion plate 3 Air box 4 Fluidized bed chamber 5 Iron ore input pipe 6 Exhaust gas pipe 7 Pre-reduction ore discharge pipe 8 Discharge hole 9 Discharge pipe 10 Recovery device 11 Melt reduction furnace 12 Furnace body 13 Fu- Do 14 Iron bath (molten iron) 21 Pipeline
Claims (1)
スとして下部の風箱から導入して分散板上の鉄鉱石に接
触させた後に上方の排ガス管より排出する流動層式予備
還元炉と、溶融還元炉と予備還元炉の風箱側壁部を繋ぎ
発生ガスを導入する管路と、流動層下部より予備還元さ
れた鉄鉱石を溶融還元炉の炉口に排出する予備還元鉱石
の排出管と、風箱底部の排出孔を介して発生ガスのダス
トと分散板からの落鉱とを集めて分別回収する回収装置
とからなることを特徴とする鉄鉱石の溶融還元装置。1. A smelting reduction furnace and a fluidized bed type pre-reduction furnace in which the generated gas is introduced as a reducing gas from a lower wind box to contact with iron ore on a dispersion plate and then discharged from an upper exhaust gas pipe. And a pipe line that connects the smelting reduction furnace and the side wall of the wind box of the preliminary reduction furnace to introduce the generated gas, and discharges the pre-reduced iron ore from the lower part of the fluidized bed to the throat of the smelting reduction furnace. An iron ore smelting reduction apparatus comprising a pipe and a recovery device for collecting and separately collecting dust of generated gas and falling ore from a dispersion plate through a discharge hole at the bottom of a wind box.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31446095A JP3292012B2 (en) | 1995-12-01 | 1995-12-01 | Iron smelting reduction equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31446095A JP3292012B2 (en) | 1995-12-01 | 1995-12-01 | Iron smelting reduction equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH09157719A true JPH09157719A (en) | 1997-06-17 |
JP3292012B2 JP3292012B2 (en) | 2002-06-17 |
Family
ID=18053614
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31446095A Expired - Fee Related JP3292012B2 (en) | 1995-12-01 | 1995-12-01 | Iron smelting reduction equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3292012B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
-
1995
- 1995-12-01 JP JP31446095A patent/JP3292012B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Also Published As
Publication number | Publication date |
---|---|
JP3292012B2 (en) | 2002-06-17 |
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