JPH10317029A - Smelting reduction furnace for iron raw material - Google Patents

Smelting reduction furnace for iron raw material

Info

Publication number
JPH10317029A
JPH10317029A JP13264497A JP13264497A JPH10317029A JP H10317029 A JPH10317029 A JP H10317029A JP 13264497 A JP13264497 A JP 13264497A JP 13264497 A JP13264497 A JP 13264497A JP H10317029 A JPH10317029 A JP H10317029A
Authority
JP
Japan
Prior art keywords
slag
iron
reaction vessel
smelting reduction
raw material
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.)
Withdrawn
Application number
JP13264497A
Other languages
Japanese (ja)
Inventor
Shinji Shima
真司 嶋
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP13264497A priority Critical patent/JPH10317029A/en
Publication of JPH10317029A publication Critical patent/JPH10317029A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a smelting reduction furnace, in which the heat load on the furnace wall is reduced and while preventing the reoxidation of reduced metallic iron, the improvement of productivity and lowering of the unit requirement of solid carbon are realized. SOLUTION: In the smelting reduction furnace for iron raw material arranging plural lower tuyeres 4 and upper tuyeres 5 at both sides of the lower part and the upper part of a reaction vessel, respectively and a molten iron pool part and a slag pool part at the lower part of the reaction vessel 1, plural projections 14 or grooves 15 forming horizontal steps on the wall surface at the intervals at the upper part from the lower tuyeres 4 in molten slag part of the water-cooling furnace wall 13 in the reaction vessel 1.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、鉄原料と炭材とを
溶融還元するスラグ浴に投入し、そこに酸素又は酸素富
化空気を吹き込むことによって溶融状態の鉄又は銑鉄を
直接製造する鉄原料の溶融還元炉に関する。
[0001] The present invention relates to an iron for directly producing molten iron or pig iron by putting an iron raw material and a carbonaceous material into a slag bath for smelting reduction, and blowing oxygen or oxygen-enriched air into the slag bath. The present invention relates to a smelting reduction furnace for raw materials.

【0002】[0002]

【従来の技術】鉄鉱石の溶融還元法は、反応容器、反応
容器とサイフォン口で連通する溶銑溜まり及びスラグ溜
まりとで構成した溶融還元炉の反応容器内に鉄原料、炭
材及び造滓剤を投入し、還元反応を進めるために反応容
器の側壁に設けられた下部羽口から吹き込んだ酸素又は
酸素富化空気によってスラグ浴を撹拌し鉄原料、炭材及
び造滓剤をスラグ浴中に混合させて鉄原料を還元し、生
成した鉄又は銑鉄とスラグとを分離することにより、溶
融状態の鉄又は銑鉄を直接製造する方法である。
2. Description of the Related Art In the smelting reduction method of iron ore, an iron raw material, a carbonaceous material and a slag-making agent are placed in a reaction vessel of a smelting reduction furnace comprising a reaction vessel, a hot metal reservoir and a slag reservoir communicating with the reaction vessel at a siphon opening. The slag bath is stirred by oxygen or oxygen-enriched air blown from the lower tuyere provided on the side wall of the reaction vessel to advance the reduction reaction, and the iron raw material, the carbonaceous material and the slag-making agent are introduced into the slag bath. This is a method for directly producing molten iron or pig iron by mixing and reducing the iron raw material and separating the produced iron or pig iron from slag.

【0003】図4は従来の溶融還元炉で、図4−(a)
は正断面図、図4−(b)は側断面図であり、反応容器
1の上部には、鉄原料、炭材、造滓材等の原料を反応容
器1内に投入するための原料投入孔2と、反応容器1内
で発生したガスを排出するガス排出口3が設けられ、ガ
ス排出口3は排ガスの熱を回収するボイラーに接続され
ている。
FIG. 4 shows a conventional smelting reduction furnace, and FIG.
Is a front cross-sectional view, and FIG. 4- (b) is a side cross-sectional view. In the upper part of the reaction vessel 1, a raw material input for charging a raw material such as an iron raw material, a carbon material, and a slag-making material into the reaction container 1 is performed. A hole 2 and a gas outlet 3 for discharging gas generated in the reaction vessel 1 are provided, and the gas outlet 3 is connected to a boiler for recovering heat of exhaust gas.

【0004】反応容器1の下部及び上部の両側にはそれ
ぞれ複数の下部羽口4及び上部羽口5が設けられ、下部
羽口4から酸素富化空気、上部羽口5から酸素がそれぞ
れ反応容器1内へ吹き込まれる。
A plurality of lower tuyeres 4 and upper tuyeres 5 are provided on both lower and upper sides of the reaction vessel 1, respectively. Oxygen-enriched air is supplied from the lower tuyeres 4 and oxygen is supplied from the upper tuyeres 5 respectively. It is blown into 1.

【0005】反応容器1の下部の外側の左右には、一方
の側に反応容器1とサイフォン口6aで連通している溶
銑溜まり7が設けられ、溶銑溜まり7には溶銑8を出銑
するための出銑口9が設けられている。他方の側には反
応容器1とサイフォン口6bで連通しているスラグ溜ま
り10が設けられ、スラグ溜まり10にはスラグ11を
出滓するための出滓口12が設けられている。
[0005] On the left and right outside of the lower portion of the reaction vessel 1, a hot metal pool 7 is provided on one side thereof, which communicates with the reaction vessel 1 through a siphon port 6a. Tap hole 9 is provided. On the other side, a slag reservoir 10 communicating with the reaction vessel 1 at the siphon port 6b is provided, and the slag reservoir 10 is provided with a slag outlet 12 for discharging the slag 11.

【0006】上記の溶融還元炉を用いた鉄又は銑鉄の製
造プロセスについて説明すると、原料投入孔2から鉄原
料、石炭あるいはコークス等の炭材及び造滓剤等の原料
が連続的に反応容器1内に投入される。
The process for producing iron or pig iron using the above-described smelting reduction furnace will be described. Iron raw materials, carbon materials such as coal or coke, and raw materials such as slag-making agents are continuously supplied from a raw material charging hole 2 to a reaction vessel 1. It is thrown in.

【0007】反応容器1内には、原料が溶解されて14
00〜1500°Cのスラグ浴11aが形成されてお
り、スラグ浴11aには下部羽口4を通して酸素富化空
気が吹き込まれ、スラグ浴11aを撹拌するとともに、
投入された石炭の一部を燃焼させてスラグ浴11aに熱
を供給する。投入された原料は、スラグ浴11aに巻き
込まれ溶融され、さらにスラグ中の酸化鉄は石炭により
還元される。
[0007] In the reaction vessel 1, 14
A slag bath 11a of 00 to 1500 ° C. is formed, and oxygen-enriched air is blown into the slag bath 11a through the lower tuyere 4 to stir the slag bath 11a,
A part of the input coal is burned to supply heat to the slag bath 11a. The charged raw material is caught and melted in the slag bath 11a, and the iron oxide in the slag is reduced by the coal.

【0008】スラグ浴11aから出るガス(COガス)
には上部羽口5から酸素を吹き込んで1500〜180
0°Cの二次燃焼熱を生成し、二次燃焼熱を効率よくス
ラグ浴11aに伝達することができる。
Gas (CO gas) emitted from the slag bath 11a
Oxygen from upper tuyere 5 to 1500-180
The secondary combustion heat of 0 ° C. is generated, and the secondary combustion heat can be efficiently transmitted to the slag bath 11a.

【0009】下部羽口4の下には、動きの穏やかなスラ
グ層があり、ここで鉄又は銑鉄の小滴とスラグ11とが
分離され、鉄又は銑鉄8はサイフォン口6aを経て溶銑
溜まり7から出銑口9を通って炉外に排出され、スラグ
11はサイフォン口6bを経てスラグ溜まり10から出
滓口12を通って炉外に排出される。スラグ下方から酸
素を吹き込むと、スラグ内でカーボンを燃焼するためス
ラグへの着熱効率が高く攪拌効果も大きいという特徴を
持っている。
Below the lower tuyere 4 there is a slag layer with a gentle movement where the iron or pig iron droplets and the slag 11 are separated, and the iron or pig iron 8 passes through the siphon port 6a and the molten iron pool 7 The slag 11 is discharged out of the furnace through the tap hole 9 and the slag 11 is discharged from the slag reservoir 10 through the tap hole 12 through the siphon port 6b. When oxygen is blown from below the slag, carbon is combusted in the slag, so that the slag has a high heat transfer efficiency to the slag and a large stirring effect.

【0010】[0010]

【発明が解決しようとする課題】しかしながら、スラグ
中に巻き込まれている固体カーボンが下部羽口から吹き
込まれた酸素で燃焼して発生した高温ガスが炉壁の熱負
荷を増大させるので、これを避けるために酸素を含む吹
込みガスを下部羽口から高速で吐出し、炉壁から遠ざけ
る必要があった。その結果として、ガスは炉中央部まて
吹き込まれて酸化域が広がって固体カーボンの滞留する
還元域の形成が妨げられ、さらに生成された金属鉄の多
くは沈降途中に下方の酸化域通過時に再酸化され、生産
速度が上がらないという欠点を有していた。
However, the high-temperature gas generated by burning the solid carbon entrained in the slag with oxygen blown from the lower tuyere increases the heat load on the furnace wall. To avoid this, it was necessary to discharge the blowing gas containing oxygen at a high speed from the lower tuyere and keep it away from the furnace wall. As a result, the gas is blown up to the center of the furnace and the oxidation zone expands, preventing the formation of a reduction zone in which solid carbon stays.Moreover, most of the metallic iron generated during the sedimentation passes through the oxidation zone below. It had the disadvantage that it was reoxidized and the production rate did not increase.

【0011】また、炉内のスラグ全体がフォーミング
し、固体カーボンの滞留が妨げられ、還元域が形成され
にくいという欠点も有していた。
Further, there is also a disadvantage that the entire slag in the furnace is formed, the stagnation of solid carbon is prevented, and a reduction zone is hardly formed.

【0012】本発明は、炉壁の熱負荷を軽減するととも
に、還元された金属鉄の再酸化を防止して生産性の向上
及び固体カーボン原単位低減を実現する溶融還元炉を提
供するものである。
The present invention provides a smelting reduction furnace which reduces the heat load on the furnace wall, prevents reoxidation of reduced metallic iron, and improves the productivity and reduces the solid carbon unit consumption. is there.

【0013】[0013]

【課題を解決するための手段】本発明の鉄原料の溶融還
元炉は、反応容器の下部及び上部の両側にそれぞれ複数
の下部羽口及び上部羽口が設けられ、反応容器の下部
に、溶銑溜まりと、スラグ溜まりが設けられている鉄原
料の溶融還元炉において、反応容器の水冷炉壁にスラグ
浴部分で下部羽口より上方に間隔をおいて壁面に水平段
差を形成する複数の突起又は溝を形成したことを特徴と
する。
A smelting reduction furnace for an iron raw material according to the present invention is provided with a plurality of lower tuyeres and upper tuyeres on both sides of a lower part and an upper part of a reaction vessel, respectively. In the slag reservoir, a slag reservoir is provided in the smelting reduction furnace of the iron raw material, and a plurality of protrusions or a plurality of protrusions forming a horizontal step on the wall surface at a distance above the lower tuyere in the slag bath portion on the water cooling furnace wall of the reaction vessel. A feature is that a groove is formed.

【0014】[0014]

【発明の実施の形態】図1は本発明の溶融還元炉の正断
面図である。本発明において、反応容器の水冷炉壁を除
く、溶融還元炉本体を構成する反応容器、溶銑溜まり及
びスラグ溜まりの構造、羽口の配置は、前述の「従来の
技術」で図4により説明した溶融還元炉の本体と同じ構
造となっており、同一部分は同一符号で表し、その説明
は省略する。
FIG. 1 is a front sectional view of a smelting reduction furnace according to the present invention. In the present invention, the structure of the reaction vessel, the hot metal pool and the slag chamber, and the arrangement of the tuyere constituting the smelting reduction furnace main body, excluding the water-cooled furnace wall of the reaction vessel, have been described with reference to FIG. It has the same structure as the main body of the smelting reduction furnace, and the same parts are denoted by the same reference numerals, and description thereof is omitted.

【0015】反応容器1の水冷炉壁13には、スラグ浴
部分で下部羽口4より上方に間隔をおいて壁面に水平段
差を形成する複数の突起14又は溝15を形成する。突
起14又は溝15は、反応容器全周に設けることが好ま
しい。水冷炉壁13は、熱伝導率のよい材料、例えば、
銅系の金属で形成することが好ましい。
A plurality of protrusions 14 or grooves 15 are formed on the wall of the water-cooled furnace 13 of the reaction vessel 1 at intervals above the lower tuyere 4 in the slag bath portion to form horizontal steps on the wall surface. The projection 14 or the groove 15 is preferably provided on the entire circumference of the reaction vessel. The water-cooled furnace wall 13 is made of a material having good heat conductivity, for example,
It is preferable to use a copper-based metal.

【0016】図2−(a)、図2−(b)及び図3−
(a)は本発明の水冷炉壁の各種実施例を示す縦断面図
で、図3−(b)及び図3−(c)は水冷エレメントの
斜視図である。
FIG. 2A, FIG. 2B and FIG.
(A) is a longitudinal sectional view showing various embodiments of a water-cooling furnace wall of the present invention, and FIGS. 3- (b) and 3- (c) are perspective views of a water-cooling element.

【0017】図2−(a)は、水平段差を形成する突起
14又は溝15を一体に成形し、突起14に冷却水路1
6を設けた水冷炉壁13の例である。
FIG. 2A shows that the projection 14 or the groove 15 forming the horizontal step is formed integrally, and the cooling water channel 1 is formed on the projection 14.
6 is an example of a water-cooled furnace wall 13 provided with a water-cooled furnace wall 6.

【0018】図2−(b)及び図3−(a)は、冷却水
路16を有する水冷エレメント17a,17bを組み合
わせて水平段差を形成する突起14を形成した例であ
る。水冷エレメントは、図3−(b)及び図3−(c)
に示すように、冷却水路16を有する銅製のバーからな
る。
FIG. 2B and FIG. 3A show an example in which a projection 14 for forming a horizontal step is formed by combining water cooling elements 17a and 17b having a cooling water passage 16. The water-cooling element is shown in FIG. 3- (b) and FIG. 3- (c)
As shown in FIG. 3, the bar is made of copper and has a cooling water passage 16.

【0019】本発明の溶融還元炉による鉄原料の溶融還
元プロセスについて説明する。
The smelting reduction process of the iron raw material by the smelting reduction furnace of the present invention will be described.

【0020】本発明の溶融還元炉による鉄原料の溶融還
元は、反応容器での鉄又は銑鉄、及びスラグの生成過程
は、前述の「従来の技術」で説明した製造プロセスと同
じであり、スラグ浴で還元されて生成した銑鉄はサイフ
ォン口を経て溶銑溜まりに溜まり、スラグはサイフォン
口を経てスラグ溜まりに溜まる。
In the smelting reduction of the iron raw material by the smelting reduction furnace of the present invention, the production process of iron or pig iron and slag in the reaction vessel is the same as the production process described in the aforementioned “prior art”. Pig iron produced by the reduction in the bath accumulates in the molten iron pool through the siphon opening, and slag accumulates in the slag reservoir through the siphon opening.

【0021】図1において、鉄原料は固体カーボンによ
り還元域18で還元されてスラグ浴中を金属鉄流れ19
となって沈降していく。スラグ浴11aには下部羽口4
を通して酸素富化空気が吹き込まれ、スラグ浴11a中
の微量の固体カーボンを2次燃焼させてスラグ浴11a
に熱を供給し、未燃酸素を含むガス20は上昇する。
In FIG. 1, an iron raw material is reduced in a reduction zone 18 by solid carbon, and a metallic iron stream 19 flows through a slag bath.
It sinks down. Lower tuyere 4 for slag bath 11a
Oxygen-enriched air is blown through the slag bath 11a to cause secondary combustion of a small amount of solid carbon in the slag bath 11a to perform secondary combustion.
And the gas 20 containing unburned oxygen rises.

【0022】水冷炉壁13の水平段差を形成する突起1
4または溝15は、接触する溶融スラグ流れ21の自由
流動を妨げるため、ガス−水冷炉壁間の伝熱量を低下さ
せ、また、炉壁に接触する溶融スラグ流れ21の流動を
妨げて炉壁の熱負荷を軽減するため炉壁近傍のみを撹拌
し還元域18を溶融スラグ浴中央に形成することが可能
となり、還元された金属鉄の再酸化を防止できる。
The protrusion 1 forming the horizontal step of the water-cooled furnace wall 13
The groove 4 or the groove 15 prevents the free flow of the molten slag stream 21 in contact therewith, so that the amount of heat transfer between the gas-water cooled furnace walls is reduced, and the flow of the molten slag stream 21 in contact with the furnace walls is prevented. In order to reduce the heat load, only the vicinity of the furnace wall is agitated, and the reduction zone 18 can be formed at the center of the molten slag bath, so that reoxidation of the reduced metallic iron can be prevented.

【0023】[0023]

【発明の効果】水冷壁の水平段差を形成する突起または
溝により炉壁の熱負荷が軽減するため、水冷壁からの奪
熱量が低減し、プロセスの熱効率が向上し、石炭原単位
低減を実現できる。
The heat load on the furnace wall is reduced by the projections or grooves forming the horizontal steps of the water cooling wall, so the amount of heat taken from the water cooling wall is reduced, the thermal efficiency of the process is improved, and the unit consumption of coal is reduced. it can.

【0024】本発明は、還元された金属鉄の再酸化が防
止できるので、生産性が向上し、また、金属鉄の再酸化
によって失われるカーボンが減少し、石炭原単位低減を
実現できる。
According to the present invention, since reoxidation of reduced metallic iron can be prevented, productivity is improved, and carbon lost due to reoxidation of metallic iron is reduced, and a reduction in unit consumption of coal can be realized.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の溶融還元炉の正断面図である。FIG. 1 is a front sectional view of a smelting reduction furnace of the present invention.

【図2】本発明の水冷炉壁の実施例を示す縦断面図であ
る。
FIG. 2 is a longitudinal sectional view showing an embodiment of a water-cooled furnace wall of the present invention.

【図3】図3−(a)は本発明の水冷炉壁の実施例を示
す縦断面図及び図3−(b)及び図3−(c)は水冷エ
レメントの斜視図である。
FIG. 3A is a longitudinal sectional view showing an embodiment of a water-cooling furnace wall according to the present invention, and FIGS. 3B and 3C are perspective views of a water-cooling element.

【図4】従来の溶融還元炉で、図4−(a)は正断面
図、図4−(b)は側断面図である。
4 (a) is a front sectional view and FIG. 4- (b) is a side sectional view of a conventional smelting reduction furnace.

【符号の説明】[Explanation of symbols]

1 反応容器 2 原料投入孔 3 ガス排出口 4 下部羽口 5 上部羽口 6a,6b サイフォン口 7 溶銑溜まり 8 溶銑 9 出銑口 10 スラグ溜まり 11 スラグ 11a スラグ浴 12 出滓口 13 水冷炉壁 14 突起 15 溝 16 冷却水路 17a,17b 水冷エレメント 18 還元域 19 金属鉄流れ 20 未燃酸素を含むガス 21 溶融スラグ流れ DESCRIPTION OF SYMBOLS 1 Reaction container 2 Raw material input hole 3 Gas discharge port 4 Lower tuyere 5 Upper tuyere 6a, 6b Siphon port 7 Hot metal pool 8 Hot metal 9 Tap hole 10 Slag pool 11 Slag 11a Slag bath 12 Tap hole 13 Water cooling furnace wall 14 Projection 15 Groove 16 Cooling channel 17a, 17b Water cooling element 18 Reduction zone 19 Metal iron flow 20 Gas containing unburned oxygen 21 Molten slag flow

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 反応容器の下部及び上部の両側にそれぞ
れ複数の下部羽口及び上部羽口が設けられ、反応容器の
下部に、溶銑溜まりと、スラグ溜まりが設けられている
鉄原料の溶融還元炉において、反応容器の水冷炉壁にス
ラグ浴部分で下部羽口より上方に間隔をおいて壁面に水
平段差を形成する複数の突起又は溝を形成したことを特
徴とする鉄原料の溶融還元炉。
1. A smelting reduction method for an iron raw material in which a plurality of lower tuyeres and upper tuyeres are provided on both sides of a lower part and an upper part of a reaction vessel, respectively, and a molten iron pool and a slag pool are provided at a lower part of the reaction vessel. A smelting reduction furnace for an iron raw material, wherein a plurality of projections or grooves are formed on a wall of a water-cooled furnace of a reaction vessel at a distance above the lower tuyere at a slag bath portion to form a horizontal step on the wall. .
JP13264497A 1997-05-22 1997-05-22 Smelting reduction furnace for iron raw material Withdrawn JPH10317029A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13264497A JPH10317029A (en) 1997-05-22 1997-05-22 Smelting reduction furnace for iron raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13264497A JPH10317029A (en) 1997-05-22 1997-05-22 Smelting reduction furnace for iron raw material

Publications (1)

Publication Number Publication Date
JPH10317029A true JPH10317029A (en) 1998-12-02

Family

ID=15086151

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13264497A Withdrawn JPH10317029A (en) 1997-05-22 1997-05-22 Smelting reduction furnace for iron raw material

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107649090A (en) * 2017-10-30 2018-02-02 蔡素真 A kind of multipurpose chemical industry stirred autoclave

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107649090A (en) * 2017-10-30 2018-02-02 蔡素真 A kind of multipurpose chemical industry stirred autoclave

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