JPS6280213A - Method and apparatus for applying heat to molten metal in smelting furnace - Google Patents

Method and apparatus for applying heat to molten metal in smelting furnace

Info

Publication number
JPS6280213A
JPS6280213A JP21924385A JP21924385A JPS6280213A JP S6280213 A JPS6280213 A JP S6280213A JP 21924385 A JP21924385 A JP 21924385A JP 21924385 A JP21924385 A JP 21924385A JP S6280213 A JPS6280213 A JP S6280213A
Authority
JP
Japan
Prior art keywords
molten metal
slag
smelting furnace
tuyeres
secondary combustion
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
JP21924385A
Other languages
Japanese (ja)
Other versions
JPH0699735B2 (en
Inventor
Kenji Takahashi
謙治 高橋
Hideo Nakamura
英夫 中村
Akiya Ozeki
尾関 昭矢
Shunichi Sugiyama
峻一 杉山
Masahiro Abe
阿部 正広
Takayoshi Anzai
安斎 孝儀
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP60219243A priority Critical patent/JPH0699735B2/en
Publication of JPS6280213A publication Critical patent/JPS6280213A/en
Publication of JPH0699735B2 publication Critical patent/JPH0699735B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/42Constructional features of converters
    • C21C5/46Details or accessories
    • C21C5/48Bottoms or tuyéres of converters
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter

Abstract

PURPOSE:To apply a large quantity of heat to a molten metal and to make efficient smelting of a molten iron by obliquely blowing an oxidizing gas to the slag generated in the molten metal to burn the gaseous CO floating in the slag and swirling the slag. CONSTITUTION:The iron oxide ore and coal are charged into the smelting furnace 1 and are heated to melt. An O2 jet is further blown into the molten metal 5 from the above-mentioned tuyere 3 to stir the molten metal 5. The iron oxide is thus reduced by the coal and CO is formed. The gaseous CO is floated on the slag layer 4 in the upper layer through the molten metal 5. The gaseous CO floating on the above-mentioned slag 4 is burned by the oxidizing gas such as O2 blown from tuyeres 2-2e for secondary combustion bored to the side wall 1 of the smelting furnace. The heated slag 4 is thereby swirled and the heat is efficiently applied to the molten metal 5. Plural pieces of the above-mentioned tuyeres 2- are provided and the angle theta of inclination on the plane with the furnace center is adequately determined at 0<theta<90 deg.-180 deg./n (number of the tuyeres 2; n;>=3) or 0<theta<45 deg. (n; 2).

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は直接溶融還元炉および転炉の如き製錬炉にお
ける溶湯への熱付加方法およびその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and apparatus for adding heat to molten metal in a smelting furnace such as a direct smelting reduction furnace and a converter.

〔従来の技術〕[Conventional technology]

従来、製錬プロセスにおける酸素上吹き転炉等において
は、炉内の主反応を起させる酸素を吹き込むランス、も
しくは羽口以外に二次燃焼用の酸素を吹き込むランスま
たは羽口が設けられること 、′があり、例えば特公昭
53−35764号記載の j転炉のように、側壁に変
位可能な羽口を投げたものがある。この従来技術では溶
湯内で発生したー ・酸化炭素(CO)が溶湯上のスラ
グ中を上昇してス 5′(ゾーン)として帯留するもの
 “ を検出し、検出した一酸化炭素を基準にして側面 iの
羽口を水平方向又は前後に移動させ1羽口から :酸素
を吹込んで一酸化炭素を完全に燃焼させる。  。
Conventionally, in an oxygen top-blown converter etc. in a smelting process, a lance or tuyere is provided to blow oxygen for secondary combustion in addition to a lance or tuyere for blowing oxygen to cause the main reaction in the furnace. For example, there are converters such as the J converter described in Japanese Patent Publication No. 53-35764 that have movable tuyere mounted on the side wall. This conventional technology detects carbon oxide (CO) generated within the molten metal, which rises in the slag above the molten metal and becomes trapped as a slag (zone), and uses the detected carbon monoxide as a reference. Move the tuyere on side i horizontally or back and forth and blow in oxygen from one tuyere to completely burn out the carbon monoxide.

したがってスラグ層の上方では、−酸化炭素の燃焼によ
り高熱となるが、湯面と高熱部分との間に 、はスラグ
層が存在し、しかもスラグ層は空気な含んだ状態にある
ので、高熱は溶湯へ伝導し難い。
Therefore, above the slag layer, high heat occurs due to the combustion of carbon oxide, but there is a slag layer between the hot water surface and the high temperature area, and the slag layer contains air, so high heat does not occur. Difficult to conduct to molten metal.

また、上記従来技術以外にも二次燃焼用酸素を製錬用の
酸素吹込みランスと同一のランスに別の孔を設けて、そ
の孔から二次燃焼用酸素を吹込むものがある。しかしこ
の場合二次燃焼の領域がランスの孔の先端に限定され、
二次燃焼効率は低い。
In addition to the above-mentioned conventional techniques, there is a method in which the same lance as the oxygen injection lance for smelting is provided with another hole, and the oxygen for secondary combustion is blown through the hole. However, in this case, the area of secondary combustion is limited to the tip of the lance hole,
Secondary combustion efficiency is low.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

上記のような二次燃焼用ランスまたは羽口を設けた転炉
においては、二次燃焼用ランスまたは羽口からの酸素が
溶湯内の特定の位置あるいはスラグ上方の一酸化炭酸層
に吹込まれるので、二次燃焼によって生ずる高熱をすべ
て溶湯へ付加することb′−できないという問題があっ
た。
In a converter equipped with a secondary combustion lance or tuyere as described above, oxygen from the secondary combustion lance or tuyere is blown into a specific position within the molten metal or into the carbon monoxide layer above the slag. Therefore, there was a problem in that it was not possible to add all of the high heat generated by the secondary combustion to the molten metal.

〔問題点を解決するための手段〕[Means for solving problems]

この発明に係る!JI錬炉における溶湯への熱付加方法
は、酸化性ガスを傾斜させてスラグ層に吹込んで、スラ
グ中を浮上する一酸化炭素をスラグ層中で燃焼させろと
共に、その燃焼により高温になったスラグ層を旋回及び
循環させて、スラグ層の高熱な溶湯へ付加するものであ
る。
Regarding this invention! The method of adding heat to the molten metal in a JI smelting furnace is to inject oxidizing gas into the slag layer at an angle, and burn the carbon monoxide floating in the slag in the slag layer. The slag layer is added to the hot molten metal by swirling and circulating the layer.

またこの別の発明に係る装置は、側壁の湯面上のスラグ
層の位置に複数の二次燃焼用羽口を設け、かつ二次燃焼
用羽口は、その数n b′−n 〉3の場合は平面上に
おいて炉心と設置点とを結ぶ角度θを0〈θ〈9σ−1
80’の範囲に、またその数nが2の場合は0くθ〈4
5°の範囲になるように配設すると共に上下方向にも傾
斜させたものである。
Further, in the device according to this other invention, a plurality of secondary combustion tuyeres are provided at the position of the slag layer above the hot water surface of the side wall, and the number of secondary combustion tuyeres is n b'-n 〉3 In this case, the angle θ connecting the core and the installation point on the plane is 0〈θ〈9σ−1
80', and if the number n is 2, then θ〈4
It is disposed within a range of 5° and is also inclined in the vertical direction.

〔作用〕[Effect]

この発明においては、−酸化炭素の燃焼により溶湯の温
度よりも著しく高温になったスラグ層を二次燃焼用の酸
性ガス流及び上記CO燃焼で生じろCO,ガス流れで旋
回循環させるため熱流が溶湯の方へ向き、スラグから溶
湯への有効な熱伝導が可能となる。
In this invention, the slag layer, which has become significantly hotter than the temperature of the molten metal due to the combustion of carbon oxide, is swirled and circulated by the acidic gas flow for secondary combustion and the CO gas flow generated by the CO combustion, so that a heat flow is generated. It faces toward the molten metal, allowing effective heat transfer from the slag to the molten metal.

またこの別の発明においては、二次燃焼用の酸性ガスは
炉側壁の同じ周方向に平面上一定の範囲で傾斜し、かつ
上下方向にも傾斜した羽口からスラグ層に吹込まれるの
で、−酸化炭素を燃焼させると共にスラグ層を旋回及び
循環流にすることができる。
In this other invention, the acidic gas for secondary combustion is blown into the slag layer from the tuyere which is inclined in the same circumferential direction of the furnace side wall in a certain plane plane and is also inclined in the vertical direction. - The carbon oxide can be burned and the slag bed can be turned into a swirling and circulating flow.

〔実施例〕〔Example〕

第1図は、この発明の方法を実施する製錬炉の平断面図
である。図において(1)は製錬炉の炉壁、(2)〜(
2e)は炉壁に配設した二次燃焼用の羽口。
FIG. 1 is a plan cross-sectional view of a smelting furnace in which the method of the present invention is carried out. In the figure, (1) is the furnace wall of the smelting furnace, (2) to (
2e) is a tuyere for secondary combustion arranged on the furnace wall.

゛(3)は底吹ぎ用酸素粉体吹込用羽口である。羽口(
2)□ 〜(2e)は水平および上F方向に所定の角度
で傾斜させて配設されており、水平方向の傾斜角θは羽
口数との相対的関係により定まり、羽口数を5 nとす
ると、n 〉3の場合次式を満足する角度にまた、羽口
数がn = 2の場合は、次式を満足する′  角度に
なる。
゛(3) is a tuyere for blowing oxygen powder for bottom blowing. Tuyere (
2) □ to (2e) are arranged to be inclined at a predetermined angle in the horizontal and upper F directions, and the horizontal inclination angle θ is determined by the relative relationship with the number of tuyeres, and the number of tuyere is 5 n. Then, when n > 3, the angle satisfies the following equation, and when the number of tuyeres is n = 2, the angle satisfies the following equation.

0〈θ<45°     ・・・(2)”、 設置点と
炉心を結ぶ線に対してなン角度である。
0<θ<45°...(2)", which is the angle to the line connecting the installation point and the reactor core.

ミ ;、、よ、上記(、ン、(2)式。範囲っ傾斜’gFL
、Cい、が、1 全ての羽口(2)〜(2e)は同じ角
度である必要は□ なく、羽口(2)〜(2e)のそれ
ぞれの角度を上記(υ、(2)式の範囲内で変えてもよ
く、一部の羽口(2)〜(2e)の角度のみを変えても
よい。また羽口(2)〜(2e)の上下方向の傾斜角は
特に範囲を投げないが、交互に上下方向に傾斜させても
よく、あるいは所定の数の羽目(2)〜(2e)を組に
して上下方向に傾斜させるようにしてもよい。
Mi;,, yo, the above (, n, formula (2). Range slope 'gFL
, C, but 1 All tuyeres (2) to (2e) do not need to be at the same angle □, but each angle of tuyere (2) to (2e) can be calculated using the above equation (υ, (2)) The angles of some of the tuyeres (2) to (2e) may be changed within the range of Although they are not thrown, they may be tilted vertically alternately, or a predetermined number of stitches (2) to (2e) may be grouped and tilted vertically.

この羽口(2)〜(2e)は製錬炉の炉壁のスラグ層が
生成する位置に設けられる。製錬炉の溶湯は吹錬用酸素
ジェットまたは溶融還元時の粉体および気体の吹込み流
れてより流動しているが、湯面の高さおよびその上のス
ラグ層の厚さは一定の範囲にあるので、その範囲に羽口
(2)〜(2e)を配設すればよい。
The tuyeres (2) to (2e) are provided at positions where a slag layer is formed on the furnace wall of the smelting furnace. The molten metal in the smelting furnace is more fluid due to the oxygen jet for blowing or the blowing of powder and gas during melt reduction, but the height of the molten metal surface and the thickness of the slag layer above it are within a certain range. Therefore, the tuyeres (2) to (2e) may be arranged in that range.

以上のように構成された製錬炉により直接溶融還元によ
る製鉄また酸素底吹きによる製鋼において、溶湯にスラ
グ層の一酸化炭素の燃焼熱を付加するには、以下の方法
による。
In ironmaking by direct smelting reduction or steelmaking by oxygen bottom blowing in the smelting furnace configured as described above, the following method is used to add the combustion heat of carbon monoxide in the slag layer to the molten metal.

直接溶融還元による製鉄においては、第1図に示す製錬
炉(以下製錬炉という場合は第1図に示すものをいう)
に酸化鉄として粉状鉄鉱石を、また粉状固体還元41と
して石炭をそれぞれ羽口(3)より装入して加熱溶融す
る。そして同様に製錬炉のが 底部の羽目(3)内管からは酸素ジエツ′¥恢込まれろ
In ironmaking by direct smelting reduction, the smelting furnace shown in Figure 1 (hereinafter referred to as smelting furnace refers to the one shown in Figure 1)
Powdered iron ore as iron oxide and coal as powdered solid reduction 41 are charged through the tuyere (3) and heated and melted. And in the same way, oxygen is collected from the inner tube of the bottom panel (3) of the smelting furnace.

その結果溶融した溶湯は酸素ジエン)Kより攪拌されて
流動し、酸化鉄(Fe20s)は石炭の炭素(C)と還
元反応し、生成する一位化炭素(CO)は溶湯中を浮上
した後スラグ層を通過し、炉頂へ上昇する。そこで羽口
(2)〜(2e)よシニ欠燃焼用の酸素あるいは酸素を
含むガス等の酸化性ガスをスラグ層に吹込んでスラグ層
の一酸化炭素(CO)を燃焼させ、その燃焼熱によりス
ラグ層を高温にする。
As a result, the molten metal is stirred by oxygen (diene) K and flows, iron oxide (Fe20s) undergoes a reduction reaction with the carbon (C) of the coal, and the produced monocarbon (CO) floats up in the molten metal. It passes through the slag layer and rises to the top of the furnace. Therefore, through the tuyeres (2) to (2e), oxygen for incomplete combustion or an oxidizing gas such as a gas containing oxygen is injected into the slag layer to burn the carbon monoxide (CO) in the slag layer. Bring the slag layer to a high temperature.

一方二次燃焼用酸素あるいは酸素を含むガスは、炉壁(
1)の周方向に傾斜された羽口(2)〜(2e)から吹
込まれるので、スラグ層は炉内で旋回循環流となる。し
かもこの旋回循環流は、平面を旋回するばかりでなく、
上下、斜方向にも旋回するので。
On the other hand, the oxygen for secondary combustion or the gas containing oxygen is
Since the slag layer is blown in from the tuyeres (2) to (2e) inclined in the circumferential direction of 1), the slag layer forms a swirling circulation flow within the furnace. Moreover, this swirling circulation flow not only swirls on a plane;
It can also rotate up and down and diagonally.

溶湯の湯面とスラグ層の界面は接触面積が犬きくなシ、
より動的状態になってスラグ層の高熱は効率よく溶湯へ
伝導される。
The contact area between the molten metal surface and the slag layer is small,
The state becomes more dynamic, and the high heat in the slag layer is efficiently conducted to the molten metal.

また酸素底吹きの製錬においても、同様の操作により溶
湯へ効率よく一酸化炭素(CO)のP焼熱を付加するこ
とができろ。
Also, in oxygen bottom-blown smelting, P sintering heat of carbon monoxide (CO) can be efficiently added to the molten metal by a similar operation.

第2図は第1図に示した製錬炉の側断面図であり、二次
燃焼用羽口(2)〜(2e)からスラグ層(4)に二次
燃焼用の酸素または酸素を含むガス吹き込まれ、高熱と
なったスラグ層(4)カー循環して溶湯(4)へ熱を付
加する状態を示したものである。
FIG. 2 is a side sectional view of the smelting furnace shown in FIG. 1, in which oxygen for secondary combustion or oxygen is contained in the slag layer (4) from the tuyeres (2) to (2e) for secondary combustion. This figure shows the state in which gas is blown into the slag layer (4), which becomes extremely hot, and circulates through the car to add heat to the molten metal (4).

〔発明の効果〕〔Effect of the invention〕

この発明は以上説明したとおり、スラグ層で発生した一
酸化炭素の燃焼熱をスラグ層の旋回(でより溶湯へ付加
するようにしたので、多量の熱を必要とする直接溶融還
元製鉄における反応を効率よく行うことb′−できろと
共に、転炉による製封1においても熱効率を上昇させる
ことができろ効果がある。
As explained above, in this invention, the heat of combustion of carbon monoxide generated in the slag layer is added to the molten metal through the swirling of the slag layer, thereby reducing the reaction in direct smelting reduction steelmaking, which requires a large amount of heat. Efficiency b' - In addition to being able to perform sealing 1 using a converter, thermal efficiency can be increased, which is effective.

また、この別の発明は、製錬炉の側壁でスラグ層の位置
に一定の範囲で傾斜させた複数の二次燃焼用羽口な設け
ているので、スラグ層を効率よ(旋回させることができ
る効果があるっ
In addition, this other invention provides a plurality of secondary combustion tuyeres that are inclined within a certain range at the position of the slag layer on the side wall of the smelting furnace, so that the slag layer can be efficiently (swirled). There is an effect that can be done

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

第1図はこの発明の一実施例を示す平断面図、第2図は
その側断面図である。 図において、(1)は製錬炉の側壁、(2)〜(2e)
は二次燃焼用羽口、(3量ま02/扮体吹込用羽口、(
4)はスラグ層、(5)は溶湯である。 代理人 弁理士 佐 藤 正 年 第 1 図 2d          2〜2e ン吹入叡χ乏で層
口宵 2図
FIG. 1 is a plan sectional view showing an embodiment of the present invention, and FIG. 2 is a side sectional view thereof. In the figure, (1) is the side wall of the smelting furnace, (2) to (2e)
is a tuyere for secondary combustion,
4) is a slag layer, and (5) is a molten metal. Agent Patent Attorney Tadashi Sato Year 1 Figure 2d 2-2e

Claims (2)

【特許請求の範囲】[Claims] (1)製錬炉において溶湯中で発生し、スラグ中を浮上
する一酸化炭素ガスをスラグ中に酸化性ガスを傾斜して
吹込ことにより燃焼させると共に燃焼して昇温するスラ
グを旋回させて、スラグの熱を溶湯へ付加することを特
徴とする製錬炉における溶湯への熱付加方法。
(1) The carbon monoxide gas generated in the molten metal in the smelting furnace and floating in the slag is combusted by injecting oxidizing gas into the slag at an angle, and the slag, which burns and heats up, is swirled. , a method for adding heat to molten metal in a smelting furnace, characterized by adding heat from slag to molten metal.
(2)製錬炉において、側壁の湯面上のスラグの位置に
複数の二次燃焼用羽口を設け、かつ上記次燃焼用羽口を
、その数nがn≧3の場合は平面上において炉心と設置
点とを結ぶ線に対する角度θが0<θ<90°−180
°/nの範囲にしてその数nが2の場合は、0<θ<4
5°の範囲になるように配設すると共に上下方向にも傾
斜させたことを特徴とする製錬炉の溶湯への熱付加装置
(2) In a smelting furnace, a plurality of secondary combustion tuyeres are provided at the position of the slag above the hot water surface of the side wall, and the secondary combustion tuyere is placed on a plane when the number n is n≧3. If the angle θ with respect to the line connecting the core and the installation point is 0<θ<90°−180
If the range n is 2, then 0<θ<4
A device for adding heat to molten metal in a smelting furnace, characterized in that it is arranged within a range of 5° and is also tilted in the vertical direction.
JP60219243A 1985-10-03 1985-10-03 Method and apparatus for adding heat to molten metal in smelting furnace Expired - Fee Related JPH0699735B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60219243A JPH0699735B2 (en) 1985-10-03 1985-10-03 Method and apparatus for adding heat to molten metal in smelting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60219243A JPH0699735B2 (en) 1985-10-03 1985-10-03 Method and apparatus for adding heat to molten metal in smelting furnace

Publications (2)

Publication Number Publication Date
JPS6280213A true JPS6280213A (en) 1987-04-13
JPH0699735B2 JPH0699735B2 (en) 1994-12-07

Family

ID=16732459

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60219243A Expired - Fee Related JPH0699735B2 (en) 1985-10-03 1985-10-03 Method and apparatus for adding heat to molten metal in smelting furnace

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Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61221322A (en) * 1985-03-27 1986-10-01 Kawasaki Heavy Ind Ltd Melting and refining method for metallic raw material

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61221322A (en) * 1985-03-27 1986-10-01 Kawasaki Heavy Ind Ltd Melting and refining method for metallic raw material

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JPH0699735B2 (en) 1994-12-07

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