JPH01116018A - Converter steelmaking method - Google Patents
Converter steelmaking methodInfo
- Publication number
- JPH01116018A JPH01116018A JP27166587A JP27166587A JPH01116018A JP H01116018 A JPH01116018 A JP H01116018A JP 27166587 A JP27166587 A JP 27166587A JP 27166587 A JP27166587 A JP 27166587A JP H01116018 A JPH01116018 A JP H01116018A
- Authority
- JP
- Japan
- Prior art keywords
- slag
- converter
- briquettes
- powder
- molten steel
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C2300/00—Process aspects
- C21C2300/02—Foam creation
Landscapes
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
この発明は、転炉吹錬時においてスラグ及び溶鋼が噴出
することを防止する転炉製鋼法に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a converter steel manufacturing method that prevents slag and molten steel from spewing out during converter blowing.
[従来技術]
転炉の製鋼作業において、吹錬中は転炉の炉口から鉄を
含有するスラグが噴出することがある。[Prior Art] In steelmaking operations using a converter, slag containing iron may be ejected from the furnace mouth of the converter during blowing.
このようなスラグの噴出は、操業上及び設備上多くのト
ラブルを誘発し且つ出鋼歩留を低下させる。そこで、転
炉炉口からスラグ及び溶鋼の噴出を防止するために次の
ような方法が取られていた。Such spouting of slag causes many operational and equipment problems and reduces the yield of steel tapping. Therefore, the following methods have been used to prevent slag and molten steel from spewing out from the converter mouth.
■吹錬中において、転炉内の溶鋼表面からのランスの高
さ、及びランスからの送酸流量を制御することによって
、スラグの噴出を防止する。■During blowing, slag is prevented from blowing out by controlling the height of the lance above the molten steel surface in the converter and the flow rate of oxygen sent from the lance.
■スラグの噴出が発生した場合、または、転炉内に挿入
された例えば光フアイバースコープ内蔵プローブ等の検
知器によってスラグの噴出が予知される場合、転炉内の
溶鋼上に小粒の生ドロマイト又はオガライト(おが屑の
成形品)の噴出鎮静剤を投入することによって、物理的
にスラグの噴出を防止する。■If slag eruption occurs, or if it is predicted by a detector such as a probe with a built-in optical fiber scope inserted into the converter, small particles of raw dolomite or Slag eruption is physically prevented by adding a blowout suppressant of sawdust (molded sawdust).
■上述のようにスラグの噴出が発生した場合またはスラ
グの噴出が予知される場合に、転炉内の溶鋼上にキャリ
ヤガスによって粉コークスを吹き込み、この粉コークス
によりスラグ中の酸化物に還元剤と反応させて鎮静化す
ることにより、スラグ及び溶鋼の噴出を防止している。■As mentioned above, when slag eruption occurs or is predicted, coke powder is blown onto the molten steel in the converter using a carrier gas, and the coke powder is used to convert the oxides in the slag into reducing agents. This prevents slag and molten steel from spewing out by reacting with and calming down the molten steel.
〈文献二 鉄と鋼 1985.8−1045.1046
) 。<Reference 2 Iron and Steel 1985.8-1045.1046
).
[発明が解決しようとする問題点〕
しかしながら、上桁した■〜■の方法には、次のような
問題がある。■ランス高さ及びランスからの送酸流量の
制御は、その操作者及び吹錬条件等によって大きな影響
を受ける。従って、スラグの噴出を適確に制御すること
は極めて困難である。■小粒の生ドロマイト又はオガラ
イトのような噴出鎮静剤の投入は、投入時に一時的な効
果はあっても長続きせず、噴出が再発する場合が多い、
そεで噴出鎮静剤の投入を連続的に行うと、噴出鎮静剤
による溶鋼の抜熱が大きくなり、吹錬時の熱ロスが多大
となる。しかも、噴出鎮静剤の溶融によりスラグ量が多
くなる結果、8鋼歩留が低下する。[Problems to be Solved by the Invention] However, the methods (■ to ■) with upper digits have the following problems. ■The control of the lance height and the oxygen flow rate from the lance is greatly influenced by the operator, blowing conditions, etc. Therefore, it is extremely difficult to accurately control the ejection of slag. ■The injection of eruption sedatives such as small grains of raw dolomite or ogalite may have a temporary effect at the time of injection, but it does not last long, and eruptions often occur again.
If the eruption sedative is continuously added at that ε, the amount of heat removed from the molten steel by the eruption sedative increases, resulting in a large amount of heat loss during blowing. Furthermore, the amount of slag increases due to the melting of the blowout suppressant, resulting in a decrease in the yield of 8 steel.
■粉コークスの吹き込みは吹き込むための特別な設備を
要するため、設備費及びランニングコストが上昇する。■Blowing coke powder requires special equipment for blowing, which increases equipment costs and running costs.
又、キャリヤガスによって、溶鋼中に窒素が混入する恐
れがある。この発明はかかる事情に鑑みてなされたもの
であって、転炉吹錬時において炉口より噴出するスラグ
と溶鋼を確実に防止できる方法を提供することにある。Furthermore, there is a risk that nitrogen may be mixed into the molten steel due to the carrier gas. The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a method that can reliably prevent slag and molten steel from spewing out from the furnace mouth during converter blowing.
[問題点を解決するための手段]
この発明に係る転炉製鋼法は、鉄分を含んだ転炉粉状ダ
ストに石炭粉、コークス粉を一種以上混合した材料に、
前記材料にピッチ系バインダーでスラグと溶鋼の比重の
間になるようなブリケットにし、前記ブリケットを転炉
炉口上より投入することを特徴とする。[Means for Solving the Problems] The converter steel manufacturing method according to the present invention includes a material in which a converter powder dust containing iron is mixed with one or more types of coal powder and coke powder.
The method is characterized in that the material is made into briquettes using a pitch-based binder to have a specific gravity between that of slag and molten steel, and the briquettes are charged from above the converter mouth.
[作用、]
この発明における転炉製鋼法は、鉄分を含んだ転炉粉状
ダストに石炭粉、コークス粉を一種以上混合した材料に
、前記材料にピッチ系バインダーでスラグと溶鋼の比重
の間になるようなブリケットにし、前記ブリケットを転
炉炉口上より投入するので、ブリケットがスラグ内を通
過する時にスラグの熱により瞬時に揮発性成分が揮発し
、その部分のスラグを冷却し、同時にブリケットが瞬時
に微粉状に崩壊し、スラグ中のFeOと反応してco2
又はCOとなりスラグ中からガスとなって抜けるので、
スラグが鎮静し泡立ちを防止できるので、スラグと溶鋼
が転炉炉口より噴出することが防止できる。[Function] The converter steel manufacturing method according to the present invention includes a material in which a converter powder dust containing iron is mixed with one or more types of coal powder and coke powder, and a pitch-based binder is added to the material to form a material with a specific gravity between that of slag and molten steel. The briquettes are charged from above the converter mouth, so when the briquettes pass through the slag, the volatile components are instantly volatilized by the heat of the slag, cooling the slag in that area, and at the same time discharging the briquettes. instantly disintegrates into fine powder, reacts with FeO in the slag, and produces CO2.
Or it becomes CO and escapes from the slag as a gas.
Since the slag is calmed down and bubbling can be prevented, slag and molten steel can be prevented from spewing out from the converter mouth.
[発明の実施例]
以下に添付図面を参照して、この発明の一実施例につい
て説明する。第1図本発明の実施例を示す概要図である
。1は転炉、2は酸素ランス、3はホッパー、4はシュ
ート、5は溶鋼、6はスラグ、7はブリケットである。[Embodiment of the Invention] An embodiment of the invention will be described below with reference to the accompanying drawings. FIG. 1 is a schematic diagram showing an embodiment of the present invention. 1 is a converter, 2 is an oxygen lance, 3 is a hopper, 4 is a chute, 5 is a molten steel, 6 is a slag, and 7 is a briquette.
転炉1の上部に開口部には、溶銑5に酸素を吹き込む酸
素ランス2が上下自在に移動できるように配設されてい
る。転炉1の上方にはブリケット7を貯蔵するホッパー
3が配設され、前記ホッパー3の下方にブリケット7を
転炉1に投入するシュート4が配設されている0次にこ
の実施例の動作について説明する。An oxygen lance 2 for blowing oxygen into the hot metal 5 is disposed in an opening at the top of the converter 1 so as to be able to move vertically. A hopper 3 for storing briquettes 7 is disposed above the converter 1, and a chute 4 for charging the briquettes 7 into the converter 1 is disposed below the hopper 3.Operation of this embodiment I will explain about it.
溶銑を転炉1内に装入した後、媒溶剤として、焼石灰、
スケール、蛍石等を転炉の上部のホッパー(図示せず)
から投入する。溶銑に酸素ランス2から酸素ガスを吹き
つけ吹錬を開始する。吹錬の初期は、溶銑中の炭素と酸
素とが反応して一酸化炭素ガスが発生し、溶銑5が脱炭
される。一方投入された媒溶剤は、溶銑が脱炭される時
の発熱反応によって、媒溶剤が溶解され溶銑の上にスラ
グ6となって浮上する。そしてこのスラグ6は溶銑の燐
、硫黄等を吸収して溶銑の燐、硫黄等を低減させる。吹
錬中の脱炭反応の過程で吹込酸素と溶銑中の炭素とのア
ンバランスにより、スラグ6中にFeOが多くなるとス
ラグ6中が泡立ち、転炉1の炉口まで膨張する。その膨
張の程度が急激の場合には吹錬中の溶鋼5とスラグ6が
一緒に、転炉1の炉口から系外に噴出される。これを防
止するために、転炉内に挿入された例えば光フアイバー
スコープ内蔵プローブ等の検知器によってスラグの噴出
を予知し、その信号によって転炉1の上方にはブリケッ
ト7を貯蔵するホッパー3のバルブ(図示せず〉を開に
してブリケット7をシュート4を通って、転炉1内に投
入する。そうするとブリケット7がスラグ内を通過する
時にスラグの熱により瞬時に揮発性成分が揮発しその部
分のスラグ6を冷却し、同時にブリケット7が瞬時に微
粉状に崩壊し、スラグ6中のFeOと反応してCO2又
はCOとなりスラグ6中から抜けるので、スラグ6が鎮
静し泡立ちを防止できるので、スラグ6と5溶鋼が転炉
炉口より噴出することが防止できる。After charging hot metal into the converter 1, burnt lime,
Scale, fluorite, etc. are placed in the hopper at the top of the converter (not shown).
Insert from. Oxygen gas is blown onto the hot metal from oxygen lance 2 to start blowing. At the beginning of blowing, carbon in the hot metal reacts with oxygen to generate carbon monoxide gas, and the hot metal 5 is decarburized. On the other hand, the introduced solvent is dissolved by an exothermic reaction when the hot metal is decarburized and floats as slag 6 on top of the hot metal. This slag 6 absorbs phosphorus, sulfur, etc. of the hot metal, thereby reducing the phosphorus, sulfur, etc. of the hot metal. When FeO increases in the slag 6 due to an imbalance between blown oxygen and carbon in the hot metal during the decarburization reaction during blowing, the slag 6 bubbles and expands to the mouth of the converter 1. If the degree of expansion is rapid, the molten steel 5 and slag 6 during blowing are ejected from the furnace mouth of the converter 1 to the outside of the system. In order to prevent this, a detector inserted into the converter, such as a probe with a built-in optical fiber scope, predicts the ejection of slag, and in response to the signal, a hopper 3 for storing briquettes 7 is installed above the converter 1. A valve (not shown) is opened and the briquettes 7 are introduced into the converter 1 through the chute 4. Then, when the briquettes 7 pass through the slag, the volatile components are instantly vaporized by the heat of the slag. At the same time, the slag 6 is cooled, and at the same time, the briquettes 7 instantly disintegrate into fine powder, react with FeO in the slag 6, become CO2 or CO, and escape from the slag 6, which calms the slag 6 and prevents foaming. , molten steel slags 6 and 5 can be prevented from spewing out from the converter mouth.
なおブリケット7をスラグ6と溶鋼5の比重の間になる
ようにした理由はブリケット7がスラグ6層を通過する
ときに反応しきれない場合はブリケット7がスラグ6と
溶鋼5の境に浮遊しているのでそこで反応させるためで
ある。第1表はブリケットを製造するための石炭、コー
クス、転炉粉状ダスト、ピッチ系バインダー、ブリケッ
トの一実施例の成分表を示す。The reason why the specific gravity of the briquettes 7 is between that of the slag 6 and the molten steel 5 is that if the briquettes 7 cannot fully react when passing through the slag 6 layer, the briquettes 7 will float on the boundary between the slag 6 and the molten steel 5. This is because the reaction occurs there. Table 1 shows a list of ingredients of coal, coke, converter powder dust, pitch binder, and one example of briquettes for producing briquettes.
第1表
石炭、コークス、転炉粉状ダストの粒度は0.05〜0
.4mmで、ピッチ系バインダーを装入原料の3〜5%
添加する。造粒方法はデスクペレタイザーで行う。粒径
は10〜70mmである。Table 1 Particle size of coal, coke, and converter powder dust is 0.05 to 0.
.. 4mm, pitch-based binder is charged at 3-5% of the raw material.
Added. The granulation method is performed using a desk pelletizer. The particle size is 10-70 mm.
第2図は転炉粉状ダストと石炭又はコークスの比(嵩比
重の比)とブリケットの転炉投入からスラグの泡立ちを
防止するまでの時間を示すグラフ図である。この図から
明らかなように転炉粉状ダストと石炭又はコークスの比
(嵩比重の比)が2:1〜3:1(2,9〜3.2)の
範囲が最も短期間にスラグの泡立ちを防止できる。転炉
粉状ダストと石炭又はコークスの比(嵩比重の比)が2
:1(2,9>以下のブリゲットの場合はスラグ層の上
部のみで反応し、転炉粉状ダストと石炭又はコークスの
比(嵩比重の比)が3=1(3,2)以上のブリケット
の場合はスラグ層の下部のみで反応する。転炉粉状ダス
トと石炭又はコークスの比(嵩比重の比)が2:1〜3
:1(2,9〜3.2〉の範囲のブリゲットの場合はス
ラグ層に均一に分散し、反応するので短期間にスラグの
泡立ちを防止できる。第3図は石炭又はコークスの粒度
とブリケットの転炉投入からスラグの泡立ちを防止する
までの時間を示すグラフ図である。この図から明らかな
ようにブリケット中の石炭又はコークスの粒度が小さい
はどスラグ層でブリケットが瞬時に微粉状に崩壊し、ブ
リケット中のカーボンがスラグ6中のFeOと瞬時に反
応する。このためブリケット中の石炭又はコークスの粒
度が小さいほど良い、コークス粉より石炭粉のブリケッ
ト方がスラグの泡立ちを防止するまでの時間が短いのは
コークス粉より石炭粉のブリケット方がブリゲット中の
揮発分が多いためにブリケットが瞬時に微粉状に崩壊し
やすいからである。又、石炭又はコークスの粒度が0.
3mm超になるとスラグの泡立ちを防止するまでの時間
が20秒以上になり前記ブリケットを転炉炉口上より投
入すると、吹錬中のスラグと溶鋼が共に炉口より噴出す
るので石炭又はコークスの粒度が0.3mm以下にする
のが好ましい、即ち、鉄分を含んだ転炉粉状ダストに石
炭粉、コークス粉を一種以上混合した材料に、前記材料
にピッチ系バインダーでスラグと溶鋼の比重の間になる
ようなブリケットにし、前記ブリケットを転炉炉口上よ
り投入すると、吹錬中のスラグと溶鋼が共に炉口より防
止することができる。FIG. 2 is a graph showing the ratio of converter powder dust to coal or coke (ratio of bulk specific gravity) and the time from when briquettes are introduced into the converter to when the bubbling of slag is prevented. As is clear from this figure, when the ratio of converter powder dust to coal or coke (ratio of bulk specific gravity) is in the range of 2:1 to 3:1 (2.9 to 3.2), slag is removed in the shortest period of time. Can prevent foaming. The ratio of converter powder dust to coal or coke (ratio of bulk specific gravity) is 2
If the brigett is less than 1 (2,9), the reaction occurs only in the upper part of the slag layer, and the ratio of converter powder dust to coal or coke (ratio of bulk specific gravity) is 3 = 1 (3,2) or more. In the case of briquettes, the reaction occurs only at the bottom of the slag layer.The ratio of converter powder dust to coal or coke (ratio of bulk specific gravity) is 2:1 to 3.
:1 (2.9 to 3.2) briquettes are uniformly dispersed in the slag layer and react, so slag bubbling can be prevented in a short period of time. Figure 3 shows the particle size of coal or coke and briquettes. This is a graph showing the time taken from the time the slag is introduced into the converter to the time when the slag is prevented from foaming.As is clear from this figure, when the particle size of the coal or coke in the briquettes is small, the briquettes instantly turn into fine powder in the slag layer. The carbon in the briquettes instantly reacts with the FeO in the slag 6.For this reason, the smaller the particle size of the coal or coke in the briquettes, the better; coal powder briquettes are better than coke powder until the slag foaming is prevented. The reason why the time is shorter is that coal powder briquettes have more volatile content than coke powder, so the briquettes are more likely to disintegrate into fine powder instantly.Also, when the particle size of coal or coke is 0.
If it exceeds 3 mm, it will take more than 20 seconds to prevent the slag from bubbling, and when the briquettes are introduced from above the converter mouth, both the slag and molten steel during blowing will be ejected from the furnace mouth, so the grain size of the coal or coke will increase. is preferably 0.3 mm or less. In other words, the material is a mixture of converter powder dust containing iron and one or more types of coal powder and coke powder, and a pitch-based binder is added to the material so that the specific gravity is between that of slag and molten steel. By making the briquettes into such a shape that the briquettes are introduced from above the converter mouth, both the slag and molten steel during blowing can be prevented from entering the furnace mouth.
[発明の効果コ
以上のように、この発明によればブリケットを投入する
ことよって吹錬中にスラグと溶鋼が共に炉口より噴出す
ることを防止することができるので、能率の良い吹錬作
業ができる。[Effects of the Invention] As described above, according to the present invention, by introducing briquettes, it is possible to prevent both slag and molten steel from spewing out from the furnace mouth during blowing, resulting in efficient blowing work. Can be done.
第1図本発明の実施例を示す概要図、第2図は転炉粉状
ダストと石炭又はコークスの比(嵩比重の比)とブリケ
ットの転炉投入からスラグの泡立ちを防止するまでの時
間を示すグラフ図、第3図は石炭又はコークスの粒度と
ブリケットの転炉投入からスラグの泡立ちを防止するま
での時間を示すグラフ図である。
1・・・転炉、2・・・酸素ランス、3・・・ホッパー
、4・・・シュート、5・・・溶鋼、6・・・スラグ、
7・・・ブリケット。Figure 1 is a schematic diagram showing an embodiment of the present invention. Figure 2 is a diagram showing the ratio of powdered dust in the converter to coal or coke (ratio of bulk specific gravity) and the time from when briquettes are introduced into the converter to when the bubbling of slag is prevented. FIG. 3 is a graph showing the particle size of coal or coke and the time from when briquettes are introduced into the converter to when slag foaming is prevented. 1... Converter, 2... Oxygen lance, 3... Hopper, 4... Chute, 5... Molten steel, 6... Slag,
7...briquettes.
Claims (1)
一種以上混合した材料に、前記材料にピッチ系バインダ
ーでスラグと溶鋼の比重の間になるようなブリケットに
し、前記ブリケットを転炉炉口上より投入することを特
徴とする転炉製鋼法。A material made by mixing converter powder dust containing iron with one or more types of coal powder and coke powder is made into briquettes using a pitch-based binder to have a specific gravity between that of slag and molten steel, and the briquettes are then transferred to a converter furnace. A converter steel manufacturing method characterized by charging from the top.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27166587A JPH01116018A (en) | 1987-10-29 | 1987-10-29 | Converter steelmaking method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP27166587A JPH01116018A (en) | 1987-10-29 | 1987-10-29 | Converter steelmaking method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH01116018A true JPH01116018A (en) | 1989-05-09 |
Family
ID=17503181
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP27166587A Pending JPH01116018A (en) | 1987-10-29 | 1987-10-29 | Converter steelmaking method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01116018A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05125424A (en) * | 1991-11-08 | 1993-05-21 | Nippon Steel Corp | Slug foaming suppression method |
| US5833735A (en) * | 1993-07-20 | 1998-11-10 | Maschinenfabrik Koppern Gmbh & Co. Kg | Method of making steel |
| WO2011089027A1 (en) * | 2010-01-19 | 2011-07-28 | Sms Siemag Ag | Method for foamed slag generation of a non-corrosive melt in a converter |
| CN102162020A (en) * | 2010-02-23 | 2011-08-24 | 宝山钢铁股份有限公司 | Foaming agent for electrosmelting of stainless steel and using method thereof |
| WO2011113632A1 (en) * | 2010-03-17 | 2011-09-22 | Sms Siemag Ag | Briquette for producing a foamed slag effect in eaf technology in stainless steel production |
-
1987
- 1987-10-29 JP JP27166587A patent/JPH01116018A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05125424A (en) * | 1991-11-08 | 1993-05-21 | Nippon Steel Corp | Slug foaming suppression method |
| US5833735A (en) * | 1993-07-20 | 1998-11-10 | Maschinenfabrik Koppern Gmbh & Co. Kg | Method of making steel |
| WO2011089027A1 (en) * | 2010-01-19 | 2011-07-28 | Sms Siemag Ag | Method for foamed slag generation of a non-corrosive melt in a converter |
| CN102791888A (en) * | 2010-01-19 | 2012-11-21 | Sms西马格股份公司 | Method for foamed slag generation of a non-corrosive melt in a converter |
| US8747518B2 (en) | 2010-01-19 | 2014-06-10 | Sms Siemag Aktiengesellschaft | Method for foamed slag generation of a non-corrosive melt in a converter |
| KR101507398B1 (en) * | 2010-01-19 | 2015-03-31 | 에스엠에스 지마크 악티엔게젤샤프트 | Method for foamed slag generation of a non-corrosive melt in a converter |
| CN102162020A (en) * | 2010-02-23 | 2011-08-24 | 宝山钢铁股份有限公司 | Foaming agent for electrosmelting of stainless steel and using method thereof |
| WO2011113632A1 (en) * | 2010-03-17 | 2011-09-22 | Sms Siemag Ag | Briquette for producing a foamed slag effect in eaf technology in stainless steel production |
| US20130192422A1 (en) * | 2010-03-17 | 2013-08-01 | Johann Reichel | Briquette for producing a foamed slag effect in eaf technology in stainless steel production |
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