JPH0285311A - Smelting reduction method of iron ore and scrap - Google Patents

Smelting reduction method of iron ore and scrap

Info

Publication number
JPH0285311A
JPH0285311A JP63235938A JP23593888A JPH0285311A JP H0285311 A JPH0285311 A JP H0285311A JP 63235938 A JP63235938 A JP 63235938A JP 23593888 A JP23593888 A JP 23593888A JP H0285311 A JPH0285311 A JP H0285311A
Authority
JP
Japan
Prior art keywords
iron
iron ore
molten
pulverized coal
melting
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
JP63235938A
Other languages
Japanese (ja)
Other versions
JP2782070B2 (en
Inventor
Motoaki Hirao
平尾 元亮
Keizo Nakamura
恵造 中村
Toshiyuki Takeuchi
利行 竹内
Shunpei Nozoe
野添 浚平
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.)
Kawasaki Heavy Industries Ltd
Original Assignee
Kawasaki Heavy 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 Kawasaki Heavy Industries Ltd filed Critical Kawasaki Heavy Industries Ltd
Priority to JP23593888A priority Critical patent/JP2782070B2/en
Publication of JPH0285311A publication Critical patent/JPH0285311A/en
Application granted granted Critical
Publication of JP2782070B2 publication Critical patent/JP2782070B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Manufacture Of Iron (AREA)

Abstract

PURPOSE:To continuously smelt iron ore, etc., with small scale equipment at good efficiency and to obtain a large quantity of molten iron by blowing finely powdered iron ore, iron-containing dust, etc., into a circular flow type reaction furnace, in which blows fine coal powder and air and is partially burnt at high load. CONSTITUTION:The air or O2 sent under pressurizing through feeding hole 3, is blown into the circular flow type reaction furnace 1 from a tangent line direction together with the fine coal powder and the finely powdered iron ore and iron-containing dust or mill scale conveyed through conveying hole 2. Then, the fine coal powder is partially burnt at high load while circularly moving and also the iron ore and the above dust, etc., are reduced with high temp. partial combustion gas and melted together with ash content in the fine coal powder, and the molten iron 4 and the molten ash are stored in the furnace 1 bottom. By this method, smelting reduction can be continuously executed to the iron ore, etc., with the small scale equipment, such as the above furnace 1, at good efficiency. Further, the above molten iron 4 and the melting ash are introduced into a refining furnace 5 connected with the furnace 1 and refined, and the molten steel 7 can be obtd.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、鉄鉱石及びスクラップの溶融還元方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for melting and reducing iron ore and scrap.

[従来の技術とその課B] 従来より鉄鉱石を溶融還元する方法は種々あるが、いず
れも大規模な設備を必要とした。この為、近時小規模な
設備で鉄鉱石を溶融還元する方法が望まれている。また
従来よりスクラップは鉄源としてリサイクルの為、電気
炉、転炉等の再生手段により溶融していたが、エネルギ
ーコストが高く且つ大量処理が困難であるので、低コス
トで大量処理が可能な溶融還元方法が望まれている。
[Prior art and its section B] There have been various methods for melting and reducing iron ore, but all of them required large-scale equipment. For this reason, a method of melting and reducing iron ore using small-scale equipment has recently been desired. In addition, conventionally, scrap has been melted using recycling means such as electric furnaces and converters in order to be recycled as an iron source, but since the energy cost is high and it is difficult to process in large quantities, melting, which can be processed in large quantities at low cost, has been used. A reduction method is desired.

ところで、従来より旋回流式反応炉内に微粉炭と空気と
を共に吹込み、高負荷部分燃焼させて大半の灰を溶融除
去する方法が知られている。
Incidentally, a method is conventionally known in which pulverized coal and air are injected together into a swirling flow reactor, and most of the ash is melted and removed by high-load partial combustion.

[発明の目的] 本発明は上記実情に鑑みなされたもので、旋回流式反応
炉を利用して鉄鉱石を溶融還元し、旋回流式反応炉に続
いて設けた溶融炉でスクラップを溶融する方法を提供す
ることを目的とするものである。
[Object of the Invention] The present invention was made in view of the above circumstances, and involves melting and reducing iron ore using a swirling flow reactor, and melting scrap in a melting furnace provided following the swirling flow reactor. The purpose is to provide a method.

[課題を解決するための手段] 上記課題を解決するための本発明の1つは、旋回流式反
応炉内に、微粉炭と、微粉化した鉄鉱石及び鉄分を含む
ダスト又はミルスケールと、空気又は酸素とを共に接線
方向から吹込み、還元雰囲気にて微粉炭を部分燃焼させ
ることにより鉄鉱石を溶融還元し、溶鉄を得ることを特
徴とする鉄鉱石の溶融還元方法である。
[Means for Solving the Problems] One of the present inventions for solving the above problems is to provide pulverized coal and dust or mill scale containing pulverized iron ore and iron in a swirling flow reactor, This is an iron ore melting and reducing method characterized by melting and reducing iron ore to obtain molten iron by partially burning pulverized coal in a reducing atmosphere by blowing air or oxygen together in a tangential direction.

本発明の他の1つは、旋回流式反応炉内に、微粉炭と、
微粉化した鉄鉱石及び鉄分を含むダスト又はミルスケー
ルと、空気又は酸素とを共に接線方向から吹込み、還元
雰囲気にて微粉炭を部分燃焼させることにより鉄鉱石を
溶融還元し、溶鉄を得、然る後前記旋回流式反応炉に続
く溶融炉に溶鉄および溶融灰を導き、酸素と微粉炭又は
チャー等の還元剤とフラックス剤による溶鉄の精錬を行
うことを特徴とする鉄鉱石の溶融還元方法である。
Another aspect of the present invention is that pulverized coal is contained in a swirling flow reactor,
Pulverized iron ore and dust or mill scale containing iron are tangentially blown in with air or oxygen, and the pulverized coal is partially combusted in a reducing atmosphere to melt and reduce the iron ore to obtain molten iron. Thereafter, the molten iron and molten ash are introduced into a melting furnace following the swirling flow reactor, and the molten iron is refined using oxygen, a reducing agent such as pulverized coal or char, and a fluxing agent. It's a method.

本発明のさらに他の1つは、旋回流式反応炉内に、微粉
炭と、微粉化した鉄鉱石及び鉄分を含むダスト又はミル
スケールと、空気又は酸素とを共に接線方向から吹込み
、還元雰囲気にて微粉炭を部分燃焼させることにより鉄
鉱石を溶融還元し、溶鉄を得、前記旋回流式反応炉に続
く溶融炉に溶鉄および溶融灰を導き、溶融炉にスクラッ
プを投入すると共に酸素と微粉炭又はチャー等の還元剤
とフラックス剤を吹込みスクラップ溶融を行うことを特
徴とする鉄鉱石及びスクラップの溶融還元方法である。
Yet another aspect of the present invention is to tangentially inject pulverized coal, dust or mill scale containing pulverized iron ore and iron, and air or oxygen into a swirling flow reactor to reduce the Iron ore is melted and reduced by partially burning pulverized coal in an atmosphere to obtain molten iron, molten iron and molten ash are introduced into a melting furnace following the swirling flow reactor, and scrap is introduced into the melting furnace, and oxygen and This is a method for melting and reducing iron ore and scrap, which is characterized by melting scrap by injecting a reducing agent such as pulverized coal or char and a fluxing agent.

[作 用] 上記の如く本発明の1つである鉄鉱石の溶融還元方法は
、旋回流式反応炉内に、微粉炭と微粉化した鉄鉱石及び
鉄分を含むダスト又はミルスケールと空気又は酸素とを
共に接線方向から吹込んで、微粉炭を高負荷部分燃焼さ
せると共に鉄鉱石を高温の部分燃焼ガスにより還元し、
且つ微粉炭中の灰分と共に溶融し、溶鉄を得るのである
から、小規模な設備で鉄鉱石を連続的に効率良く溶融し
て、溶鉄を大量に得ることが可能である。また鉄鉱石等
の溶融を微粉炭の燃焼による高温の部分燃焼ガスにより
行うのであるからエネルギーコストを低減できる。
[Function] As described above, the method for melting and reducing iron ore, which is one of the aspects of the present invention, includes pulverized coal, pulverized iron ore, dust or mill scale containing iron, and air or oxygen in a swirling flow reactor. is injected from the tangential direction, pulverized coal is partially combusted under high load, and iron ore is reduced by high-temperature partially combusted gas.
In addition, since the iron ore is melted together with the ash in the pulverized coal to obtain molten iron, iron ore can be continuously and efficiently melted using small-scale equipment to obtain a large amount of molten iron. Furthermore, since iron ore and the like are melted using high-temperature partially combusted gas from combustion of pulverized coal, energy costs can be reduced.

また本発明の他の1つである鉄鉱石の溶融還元方法は、
前記の溶融方法により溶鉄を得た後、前記旋回流式反応
炉に続く溶融炉に溶鉄と溶融灰を導き、酸素と微粉炭又
はチャー等の還元剤とフラックス剤による精錬を行うの
であるから、小規模な設備で溶鋼を効率良く得ることが
できる。しかも溶鉄工程と溶鋼工程が直結しているので
、溶鉄の運搬が無く、溶鋼の生産性が良いものである。
Another aspect of the present invention, a method for melting and reducing iron ore, is as follows:
After obtaining molten iron by the above-mentioned melting method, the molten iron and molten ash are introduced into a melting furnace following the swirling flow reactor, and refined using oxygen, a reducing agent such as pulverized coal or char, and a fluxing agent. Molten steel can be obtained efficiently with small-scale equipment. Moreover, since the molten iron process and the molten steel process are directly connected, there is no transportation of molten iron, and the productivity of molten steel is good.

さらに本発明の他の1つである鉄鉱石及びスクラップの
溶融還元方法は、前記の溶融還元方法により溶鉄を得た
後、前記旋回流式反応炉に続く溶融炉に溶鉄および溶融
灰を導き、溶融炉にスクラップと微粉炭又はチャー等の
還元剤とフラックス剤を投入してスクラップ溶融を行う
のであるから、溶鉄の温度を旋回流式反応炉への微粉炭
投入量と溶融炉への酸素と微粉炭又はチャー等の還元剤
の吹込量の調整によって制御することにより、スクラッ
プの溶融量を容易に調整でき、スクラップ率の高い溶鉄
を得ることができる。
Furthermore, another method of melting and reducing iron ore and scrap according to the present invention includes obtaining molten iron by the above-mentioned smelting-reduction method, and then leading the molten iron and molten ash to a melting furnace following the swirling flow reactor. Scrap melting is carried out by charging scrap, a reducing agent such as pulverized coal or char, and a fluxing agent into the melting furnace, so the temperature of the molten iron is determined by the amount of pulverized coal input into the swirling flow reactor and the amount of oxygen into the melting furnace. By controlling by adjusting the amount of injected reducing agent such as pulverized coal or char, the amount of melted scrap can be easily adjusted and molten iron with a high scrap rate can be obtained.

[実施例] 本発明の1つである鉄鉱石の溶融還元方法の一実施例を
第1図によって説明する。旋回流式反応炉1内に搬送口
2を通して搬送されてきた微粉炭と微粉化した鉄鉱石及
び鉄分を含むダスト又はミルスケールが接線方向から投
入され、且つ送入口3を通して圧送されてきた空気又は
酸素も接線方向から吹込まれると、微粉炭が旋回運動し
乍ら高負荷部分燃焼せしめられると共に鉄鉱石及び鉄分
を含むダスト又はミルスケールが高温の部分燃焼ガスに
より還元され、且つ微粉炭中の灰分と共に溶融され、旋
回流式反応炉1の底に溶鉄4と溶融灰が溜まる。
[Example] An example of a method for melting and reducing iron ore, which is one aspect of the present invention, will be described with reference to FIG. Pulverized coal, pulverized iron ore, and dust or mill scale containing iron are tangentially fed into the swirling flow reactor 1 through the transfer port 2, and air or mill scale is fed under pressure through the feed port 3. When oxygen is also blown in from the tangential direction, the pulverized coal undergoes high-load partial combustion while rotating, and the dust or mill scale containing iron ore and iron is reduced by the high-temperature partial combustion gas, and the pulverized coal is The molten iron 4 and molten ash are melted together with the ash, and the molten iron 4 and molten ash accumulate at the bottom of the swirling flow reactor 1.

この時の燃焼反応は次の通りである。The combustion reaction at this time is as follows.

2G+ 0□−e−2GO+ 58400KcafFe
203+3[:→2Fe +3GO−147にcaRこ
うして鉄鉱石等は旋回流式反応炉1という小規模な設備
で連続的に効率良く溶融還元され、溶鉄4が大量に得ら
れる。また鉄鉱石等の溶融を微粉炭の部分燃焼による高
温の部分燃焼ガスにより行うのでエネルギーコストが低
いものである。
2G+ 0□-e-2GO+ 58400KcafFe
203+3[:→2Fe +3GO-147 caR In this way, iron ore and the like are continuously and efficiently melted and reduced in a small-scale facility called the swirling flow reactor 1, and a large amount of molten iron 4 is obtained. Furthermore, since iron ore and the like are melted using high-temperature partial combustion gas produced by partial combustion of pulverized coal, energy costs are low.

次に本発明の他の1つである鉄鉱石の溶解還元方法の一
実施例を第1図によって説明する。この実施例は溶鉄4
を得るまで前記実施例と全く同じであるので、その説明
を省略する。旋回流式反応炉1の底に溜まった溶鉄4お
よび溶融灰は旋回流式反応炉1に接続された溶融炉5に
導き、酸素吹込ランス6より酸素と微粉炭又はチャー等
の還元剤とフラックス剤を吹き込んで精錬を行い、溶鋼
7を得る。
Next, an embodiment of a method for dissolving and reducing iron ore, which is another aspect of the present invention, will be described with reference to FIG. This example is molten iron 4
Since the process is exactly the same as the previous embodiment until obtaining , the explanation thereof will be omitted. The molten iron 4 and molten ash accumulated at the bottom of the swirling flow reactor 1 are led to the melting furnace 5 connected to the swirling flow reactor 1, and are fed with oxygen, a reducing agent such as pulverized coal or char, and flux through an oxygen injection lance 6. The molten steel 7 is obtained by injecting a refining agent and refining.

この時の反応は次の通りである。The reaction at this time is as follows.

Fe2O3+ 5G+ 02  2Fe + 500 
+ 58253にCaZかくして小規模な設備で溶鋼7
を効率良く得ることができる。しかも溶鉄4を得る工程
と溶鋼7を得る工程が直結しているので、溶鉄4の運搬
が無く、溶w47の生産性が良いものである。
Fe2O3+ 5G+ 02 2Fe + 500
+ 58253 CaZ Thus molten steel 7 with small-scale equipment
can be obtained efficiently. Moreover, since the process of obtaining the molten iron 4 and the process of obtaining the molten steel 7 are directly connected, there is no need to transport the molten iron 4, and the productivity of the molten w47 is good.

前記溶鋼7は溶融炉5の底に設けた取出口8より取出し
て鍋9に入れて搬送し、溶鋼7上に浮く溶融灰7aはス
ラグとして溶融炉5の側壁に設けた排出口10より排出
してスラグ鍋11に入れて搬送する。
The molten steel 7 is taken out from an outlet 8 provided at the bottom of the melting furnace 5, placed in a pot 9, and transported, and the molten ash 7a floating on the molten steel 7 is discharged as slag from an outlet 10 provided at the side wall of the melting furnace 5. The slag is placed in a slag pot 11 and transported.

尚、酸素吹錬を行わない先の実施例の場合は、溶鉄4を
溶融炉5の底の取出口8より取出して鍋9に入れて搬送
する。
In the case of the previous embodiment in which oxygen blowing is not performed, the molten iron 4 is taken out from the outlet 8 at the bottom of the melting furnace 5, placed in a ladle 9, and transported.

高温の燃焼ガスは溶融炉5の炉頂に設けたダクト12の
途中の吸引送風機13の運転により吸引されて冷却装置
14により冷却され、集塵装置15により集塵され、吸
引送風機13を経由して脱硫装置16に入って脱硫され
た後回示せぬガス放散筒を通って頂部で燃焼されて大気
中に放散される。
The high-temperature combustion gas is sucked in by the operation of the suction blower 13 in the middle of the duct 12 installed at the top of the melting furnace 5, cooled by the cooling device 14, collected by the dust collector 15, and passed through the suction blower 13. After entering the desulfurization device 16 and being desulfurized, it passes through a gas dissipation tube (not shown) and is burned at the top and dissipated into the atmosphere.

次いで本発明のさらに他の1つである鉄鉱石及びスクラ
ップの溶融還元方法の一実施例を第2図によって説明す
る。この実施例も溶鉄4を得るまでは前記実施例と全く
同じであるので、その説明を省略する。旋回流式反応炉
1の底に溜まった溶鉄4と溶融灰は溶融炉5に導き、溶
融炉5の炉頂部に設けたダクト兼用のスクラップ投入筒
17の上端のスクラップ貯槽18よりスクラップ19を
一定量切り出してスクラップ投入筒17を通して溶融炉
5内に供給し、溶鉄4中に混入して溶融する。このスク
ラップ19の溶融において、溶鉄4の温度を旋回流式反
応炉1への微粉炭没入量と溶融炉への酸素吹込ランス6
からの酸素吹込量の調整によって制御することにより、
スクラップ19の溶融量が容易に調整され、スクラップ
率の高い溶鉄4を得ることができる。
Next, an embodiment of a method for melting and reducing iron ore and scrap, which is still another aspect of the present invention, will be described with reference to FIG. This example is also exactly the same as the previous example until the molten iron 4 is obtained, so the explanation thereof will be omitted. The molten iron 4 and molten ash accumulated at the bottom of the swirling flow reactor 1 are led to the melting furnace 5, and a certain amount of scrap 19 is collected from the scrap storage tank 18 at the upper end of the scrap input tube 17, which is installed at the top of the melting furnace 5 and also serves as a duct. The scrap metal is cut out and fed into the melting furnace 5 through the scrap input tube 17, where it is mixed into the molten iron 4 and melted. In melting this scrap 19, the temperature of the molten iron 4 is determined by the amount of pulverized coal immersed into the swirling flow reactor 1 and the oxygen injection lance 6 into the melting furnace.
By controlling by adjusting the amount of oxygen blown from
The amount of melted scrap 19 can be easily adjusted, and molten iron 4 with a high scrap rate can be obtained.

モして溶鉄4は溶融炉5の底の取出口8より取出して鍋
9に入れて搬送し、溶鉄4上に浮く溶融灰8はスラグと
して溶融炉5の側壁の排出口i。
The molten iron 4 is taken out from the outlet 8 at the bottom of the melting furnace 5, placed in a pot 9, and transported, and the molten ash 8 floating on the molten iron 4 is transferred as slag to the outlet i at the side wall of the melting furnace 5.

より排出してスラグ鍋11に入れて搬送する。The slag is then discharged, placed in a slag pot 11, and transported.

高温の燃焼ガスはスクラップ投入筒17の上部で分岐さ
れたダクト17′の途中の吸引送風機13の運転により
吸引されて冷却装置14により冷却され、集塵装置15
により集塵され、吸引送風機13を経由、して脱硫装置
16に入って脱硫された後、図示せぬガス放散筒を通っ
て頂部で燃焼されて大気中に放散される。
The high-temperature combustion gas is sucked in by the operation of the suction blower 13 in the middle of the duct 17' branched at the upper part of the scrap input tube 17, cooled by the cooling device 14, and then passed through the dust collector 15.
After passing through the suction blower 13 and entering the desulfurization device 16 to be desulfurized, it passes through a gas dissipation cylinder (not shown) and is burned at the top and dissipated into the atmosphere.

[発明の効果] 以上の説明で判るように本発明の鉄鉱石の溶融還元方法
によれば、旋回流式反応炉という小規模な設備で鉄鉱石
を連続的に効率良く溶融して、溶鉄を大量に得ることが
可能であり、また鉄鉱石等の溶融が微粉炭の燃焼により
高温の燃焼ガスにより行われるのでエネルギーコストを
低減できる。
[Effects of the Invention] As can be seen from the above explanation, according to the method for melting and reducing iron ore of the present invention, iron ore can be continuously and efficiently melted in a small-scale facility called a swirling flow reactor, and molten iron can be produced. It can be obtained in large quantities, and energy costs can be reduced because iron ore and the like are melted using high-temperature combustion gas through combustion of pulverized coal.

また本発明の他の鉄鉱石の溶融還元方法は、旋回流式反
応炉で得た溶鉄を旋回流式反応炉に続く溶融炉に導いて
酸素による精錬を行うのであるから、小規模な設備で溶
鋼を効率良く得ることができ、しかも溶鉄を得る工程と
溶鋼を得る工程とが直結しているので、溶鉄の運搬が無
く、溶鋼の生性は、旋回流式反応炉で得た溶鉄を溶融炉
に導き、溶融炉にスクラップを投入してスクラップ溶融
を行うのであるから、溶鉄の温度を制御することにより
、スクラップの溶融量を容易に調整でき、スクラップ率
の高い溶鉄を得ることができるものである。
In addition, in another iron ore smelting reduction method of the present invention, molten iron obtained in a swirling flow reactor is led to a melting furnace following the swirling flow reactor and refining with oxygen, so it requires small-scale equipment. Molten steel can be obtained efficiently, and since the process of obtaining molten iron and the process of obtaining molten steel are directly connected, there is no need to transport the molten steel, and the greenness of the molten steel is reduced by transferring the molten iron obtained in the swirling flow reactor to the melting furnace. Therefore, by controlling the temperature of the molten iron, the amount of molten scrap can be easily adjusted and molten iron with a high scrap rate can be obtained. be.

1・・・旋回流式反応炉、2・・・搬送口、3・・・送
入口、    4・・・溶鉄、5・・・溶融炉、   
  6・・・酸素吹込ランス、7・・・溶鋼、    
 7a・・・溶融灰、8・・・取出口、     9・
・・鍋、10・・・排出口、    11・・・スラグ
鍋、12・・・ダクト、    13・・・吸引送風機
、14・・・冷却装置、   15・・・集應装置、1
6・・・脱硫装置、 17・・・ダクト兼用のスクラップ投入間、17′・・
・ダクト、   18・・・スクラップ貯槽、19・・
・スクラップ。
1... Swirling flow reactor, 2... Transfer port, 3... Inlet port, 4... Molten iron, 5... Melting furnace,
6... Oxygen injection lance, 7... Molten steel,
7a...Melted ash, 8...Outlet, 9.
... pot, 10 ... discharge port, 11 ... slag pot, 12 ... duct, 13 ... suction blower, 14 ... cooling device, 15 ... slag collecting device, 1
6...Desulfurization equipment, 17...Duct also doubles as scrap input, 17'...
・Duct, 18... Scrap storage tank, 19...
·scrap.

Claims (1)

【特許請求の範囲】 1)旋回流式反応炉内に、微粉炭と、微粉化した鉄鉱石
及び鉄分を含むダスト又はミルスケールと、空気又は酸
素とを共に接線方向から吹込み、還元雰囲気にて微粉炭
を部分燃焼させることにより鉄鉱石を溶融還元し、溶鉄
を得ることを特徴とする鉄鉱石の溶融還元方法。 2)旋回流式反応炉内に、微粉炭と、微粉化した鉄鉱石
及び鉄分を含むダスト又はミルスケールと、空気又は酸
素とを共に接線方向から吹込み、還元雰囲気にて微粉炭
を部分燃焼させることにより鉄鉱石を溶融還元し、溶鉄
を得、然る後前記旋回流式反応炉に続く溶融炉に溶鉄お
よび溶融灰を導き、酸素と微粉炭又はチャー等の還元剤
とフラックス剤による溶鉄の精錬を行うことを特徴とす
る鉄鉱石の溶融還元方法。 3)旋回流式反応炉内に、微粉炭と、微粉化した鉄鉱石
及び鉄分を含むダスト又はミルスケールと、空気又は酸
素とを共に接線方向から吹込み、還元雰囲気にて微粉炭
を部分燃焼させることにより鉄鉱石を溶融還元し、溶鉄
を得、前記旋回流式反応炉に続く溶融炉に溶鉄および溶
融灰を導き、溶融炉にスクラップを投入すると共に酸素
と微粉炭又はチャー等の還元剤とフラックス剤を吹込み
スクラップ溶融を行うことを特徴とする鉄鉱石及びスク
ラップの溶融還元方法。
[Claims] 1) Pulverized coal, dust or mill scale containing pulverized iron ore and iron, and air or oxygen are tangentially blown into a swirling flow reactor to create a reducing atmosphere. A method for melting and reducing iron ore, which comprises partially burning pulverized coal to obtain molten iron. 2) Pulverized coal, pulverized iron ore and iron-containing dust or mill scale, and air or oxygen are tangentially blown into a swirling flow reactor, and the pulverized coal is partially combusted in a reducing atmosphere. The iron ore is melted and reduced to obtain molten iron, and then the molten iron and molten ash are introduced into the melting furnace following the swirling flow reactor, and the molten iron is melted with oxygen, a reducing agent such as pulverized coal or char, and a fluxing agent. A method for melting and reducing iron ore, which comprises refining iron ore. 3) Pulverized coal, pulverized iron ore and iron-containing dust or mill scale, and air or oxygen are tangentially blown into a swirling flow reactor, and the pulverized coal is partially combusted in a reducing atmosphere. The iron ore is smelted and reduced to obtain molten iron, the molten iron and molten ash are introduced into a melting furnace following the swirling flow reactor, and scrap is introduced into the melting furnace, and oxygen and a reducing agent such as pulverized coal or char are added to the melting furnace. A method for melting and reducing iron ore and scrap, which comprises blowing in a fluxing agent and melting the scrap.
JP23593888A 1988-09-20 1988-09-20 Smelting reduction method of iron ore and scrap Expired - Lifetime JP2782070B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23593888A JP2782070B2 (en) 1988-09-20 1988-09-20 Smelting reduction method of iron ore and scrap

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23593888A JP2782070B2 (en) 1988-09-20 1988-09-20 Smelting reduction method of iron ore and scrap

Publications (2)

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JPH0285311A true JPH0285311A (en) 1990-03-26
JP2782070B2 JP2782070B2 (en) 1998-07-30

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Country Link
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61159491A (en) * 1985-01-07 1986-07-19 Sumitomo Metal Ind Ltd Method and apparatus for gasifying coal involving production of molten iron
JPS62284005A (en) * 1986-05-30 1987-12-09 Nippon Kokan Kk <Nkk> Melting reduction furnace
JPS6342314A (en) * 1986-07-23 1988-02-23 クレツクネル−フムボルト−ドイツ・アクチエンゲゼルシヤフト Method and apparatus for producing pig iron
JPH01195213A (en) * 1988-01-29 1989-08-07 Nippon Steel Corp Method for supplying raw powdery material into iron bath type melting and reducing furnace

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61159491A (en) * 1985-01-07 1986-07-19 Sumitomo Metal Ind Ltd Method and apparatus for gasifying coal involving production of molten iron
JPS62284005A (en) * 1986-05-30 1987-12-09 Nippon Kokan Kk <Nkk> Melting reduction furnace
JPS6342314A (en) * 1986-07-23 1988-02-23 クレツクネル−フムボルト−ドイツ・アクチエンゲゼルシヤフト Method and apparatus for producing pig iron
JPH01195213A (en) * 1988-01-29 1989-08-07 Nippon Steel Corp Method for supplying raw powdery material into iron bath type melting and reducing furnace

Also Published As

Publication number Publication date
JP2782070B2 (en) 1998-07-30

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