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JPH0468363B2 - - Google Patents
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JPH0468363B2 - - Google Patents

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Publication number
JPH0468363B2
JPH0468363B2 JP9112984A JP9112984A JPH0468363B2 JP H0468363 B2 JPH0468363 B2 JP H0468363B2 JP 9112984 A JP9112984 A JP 9112984A JP 9112984 A JP9112984 A JP 9112984A JP H0468363 B2 JPH0468363 B2 JP H0468363B2
Authority
JP
Japan
Prior art keywords
slag
blowing
oxygen
furnace
slopping
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.)
Expired
Application number
JP9112984A
Other languages
Japanese (ja)
Other versions
JPS60234911A (en
Inventor
Tooru Yoshida
Yutaka Narita
Jujiro Ueda
Keiji Arima
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 JP9112984A priority Critical patent/JPS60234911A/en
Publication of JPS60234911A publication Critical patent/JPS60234911A/en
Publication of JPH0468363B2 publication Critical patent/JPH0468363B2/ja
Granted legal-status Critical Current

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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
    • C21C5/30Regulating or controlling the blowing
    • C21C5/32Blowing from above

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

産業上の利用分野 本発明は転炉を用いた鉄鋼精錬の操業方法に関
するものである。 発明の目的 上吹もしくは上底吹転炉操業方法の目的は、転
炉吹錬中に供給される酸素により、溶湯中に含ま
れる炭素を低減すると共に、炉内に投入する造滓
剤を滓化させて、生成した溶融スラグと溶湯との
反応により、脱燐・脱硫等の作用を営ませること
にある。 この場合、スラグの滓化状態が転炉操業の成果
を左右する大きな因子で、滓化が過度に進むと、
スラグのフオーミング状態を助長し、遂にはスラ
グが炉外に溢流する異常反応すなわちスロツピン
グを生じ、作業効率の低下、鉄歩留の低下、作業
環境の悪化、装置の損傷など種々の問題を生ず
る。 これに反し、滓化不良の場合は、脱燐作用等が
低下し、所望の品質の鋼を得ることができない。 したがつてスラグを過剰に形成する方向で吹錬
を行い、且つスロツピングが起らないように制御
するのが望ましい。しかし脱炭反応が旺盛に起る
吹錬中期をすぎれば、脱炭のために消費されない
酸素が次第に増加してスラグ中(FeO)の増加と
なり、これが溶湯中のMnと反応して酸化マンガ
ンを形成し、マンガン含量の減少をきたすので、
この時期にはスラグ中酸素量を低減するか、ある
いは、滓化量そのものを低減し、Mn富化の操作
ができることが望ましい。 本発明は上述の所望の操業を可能にする方法を
提供するものである。 発明の構成・作用 本発明の構成は、 1 上吹もしくは上底吹転炉操業方法において、
吹錬の初期から中期にかけて、常にスラグが過
滓化状況を示すように吹錬し、スロツピングを
予知もしくは検出した際に、フオーミング調整
操作を実施することを特徴とする転炉操業方
法、及び 2 上吹もしくは上底吹転炉操業方法において、
吹錬の初期から中期にかけて、常にスラグが過
滓化状況を示すように吹錬し、スロツピングを
予知もしくは検出した際に、フオーミング調整
操作を実施し、吹錬末期では、スラグ中酸素量
もしくはスラグ滓化状況を指標としてMn富化
操作を実施することを特徴とする転炉操業方
法、 である。 前述の如く、転炉操業の最大の目的の一つは脱
炭である。ランスから吹込まれる酸素ジエツト
は、溶湯面と衝突して速かに溶湯に吸収され、溶
湯中のCと反応してCO又はCO2ガスとして炉口
から排出される。 しかして実際の炉内での脱炭反応の速度−
dc/dtは次のように変化する。すなわち、吹錬開
始後早い時期は、溶湯中のSiの濃度がまだ高く、
溶湯温度もまだ低いため、脱炭の反応速度は徐々
に上昇する。反応がある程度進み、溶湯の温度が
上昇すると、供給される酸素のほぼ100%が脱炭
に消費され、反応速度も一定になる。その後溶湯
中のCの濃度が減少し、溶湯中のCの、酸素ジエ
ツトと溶湯との衝突面への拡散が律速となると、
反応速度は次第に低下する。 したがつて反応速度の経時変化を供給する酸素
をベースに考えて−dc/dO2すなわち脱炭素効率
としても、時間当りの酸素流量を一定とすれば全
く同じ形の脱炭効率の経時変化を示すグラフとな
り、模式的に第1図の如く画かれ、反応速度一定
のところの−dC/dO2は通常1.08Kg/Nm3前後と
なる。 このグラフのフラツトな線の時間帯を吹錬の中
期、その前後をそれぞれ吹錬初期および吹錬末期
と定義する。勿論、実際の吹錬中の−dC/dO2
変化は第1図のように単純なものではないが、そ
の傾向は、ほぼ第1図に代表されると考えてよ
い。 吹錬初期および吹錬中期においては、吹込まれ
る酸素により、溶湯中のSiはSiO2に酸化され、
これが炉内に投入される造滓剤たとえば生石灰と
反応して滓化を進行させ、また酸素と溶湯の反応
あるいは媒溶剤によるスラグ中(FeO)の生成と
合俟つて脱燐の作用などを行うので、この時間は
スラグの生成が過剰傾向にあることが望ましい。 このためには、例えばランス高さを高くして上
吹酸素ジエツトをソフトブローにし、スラグ中の
酸素ポテンシヤルが増加するような吹錬操作を行
えばよい。 ところで本発明で称するスラグ過滓化状況と
は、前述したようにスラグの生成が過剰傾向にあ
る状態であり、スラグ中の酸素ポテンシヤルが高
めに推移し、前記生石灰等の造滓剤の滓化を過剰
に促進し、炉内のスラグを大量に存在せしめる吹
錬状況を意味している。 而して過滓化状況にあるか否かは、吹錬中にお
ける炉内残留酸素量で把握することが可能であ
る。例えば前記炉内残留酸素量を指標とし、過去
の実績等よりその時間的な変化の限界を吹錬時間
との関連でパターン化して予め設定して過滓化状
況の判断基準とすることができる。即ち操業中に
おける前記炉内残留酸素量の時間的変化を検出
し、前記許容限界パターンと比較することによつ
て過滓化状況にあるか否かを決定することができ
る。つまり前記許容限界パターン以下の時間的変
化であれば滓化が充分促進されていない状態であ
り、許容限界パターン以上であれば過滓化状況に
あると判定できる。 吹錬中における炉内残留酸素量の時間的変化
は、例えば特開昭57−29519号に示されるように
排ガスの流量及び組成、送酸素量、溶鋼の温度及
び炭素含有量等を計算し、演算処理することによ
つて容易に検出することが可能である。 またこの過滓化状況にあるか否かは、スラグレ
ベルを測定することによつても決定することがで
きる。即ちスラグ中の酸素ポテンシヤルが高めに
推移し、過滓化状況にあると言うことは、スラグ
が過剰に形成されている状態である。従つて前述
の残留酸素量の時間的変化の許容限界パターンと
同様に当該吹錬時のスラグレベルパターンを予め
設定して判断基準とする共に、吹錬中におけるス
ラグレベルを後述する種々の手段で直接的に検出
し、前記設定パターンと比較することによつて炉
内が過滓化状況にあるか、あるいは過滓化状況に
達していないかを決定することができる。 しかしこのようなスラグの過滓化状況の吹錬は
常にスロツピングの危険を伴う。したがつてスロ
ツピングの予知もしくは検出がきわめて重要な技
術となる。 従来スラグレベルを検知しようとする試みは
種々なされていて、音響測定法(特開昭54−
33790号)、振動測定法(特開昭54−114414号)、
炉内圧測定法(特開昭55−104417号)、マイクロ
波測定法(特開昭57−140812号)、炉体表面温度
測定法(特開昭58−48615号)などが提案されて
いる。 音響測定法は吹錬中に炉内より発生する音響の
周波数および強度の変化を把えてスラグレベルを
推定してスロツピング発生を予知しようとするも
のであり、振動測定法は吹錬中のランスの振動の
変化、波形の推移を把えてスラグレベル又はスラ
グの状態を推定してスロツピング発生を予知しよ
うとするものであり、炉内圧測定法は吹錬中の炉
口排ガス噴出圧の変動を把えてスロツピング発生
を予知しようとするものであり、マイクロ波測定
法は吹錬中に炉内にマイクロ波を直接投射して
FMレーダーの原理によりスラグレベルを直接測
定してスロツピング発生を予知しようとするもの
であり、炉体表面温度測定法は炉体の上部および
下部の放射エネルギーを温度として把え、その温
度変化、ピーク値などからスロツピングの発生と
その量を検知しようとするものである。 これらに対し本出願人は先に転炉炉壁の非浸漬
部に設けられた貫通孔に炉内光測定器を装着し、
炉内光の強度または波長変化もしくはその双方を
観測してフオーミングレベルを検知し、スロツピ
ングの予知および滓化不良の検知を行う方法を特
許出願(特願昭58−37872号)し、その後さらに
炉内光を光検出装置で検出し、得られた色彩信号
の中から主として黄色系色彩の占める割合及びそ
の割合の変動を抽出してスロツピング発生を検出
する方法を特許出願しているが、これらの方法
は、炉内の状況、特にスラグレベルを直接且つ迅
速にできる。 而して前述したように予め設定されたスラグレ
ベルパターンと検出されたスラグレベルを比較す
れば過滓化状況にあるか否かが決定でき、さらに
過滓化状況にあつてもそれが異常に高くなりスロ
ツピング発生の危険性が高くなるレベルを設定し
ておくことによつて、スロツピングの発生を正確
に予知、あるいは検出することが可能となる。 スロツピングの予知もしくは検出した際とるべ
きフオーミング調整操作については、従来種々の
方法が提案されている。 例えば、スロツピング抑制剤の投入、底吹流量
の増加、ランス高さの低下、送酸流量の低減、副
原料の投入等があり、何れも有効であるが、優先
順位としては、前記記載の順が好ましい。またス
ロツピングの予知もしくは検出した際に、吹錬ス
タート前に、上述の底吹流量の増加以下のフオー
ミング調整操作が予め予定されていた場合は、そ
の予定操作を優先するとよい。 しかして吹錬末期においては、前述のごとくス
ラグ中(FeO)が次第に増加して溶湯中Mnと反
応してMnOとなつてスラグ中に移行するか、あ
るいは溶湯中のMnと、スラグ中のMnOとFeOの
平衡関係によつて、スラグ中(FeO)の増加に伴
つてMnが減少する変化がおこるので、これらを
防止してMnの富化を図ることは、貴重なMnを
有効に利用することになり価値のある操作であ
る。 この場合は、スラグ中(FeO)を減少させるこ
とを目標にするか、スラグのフオーミングした容
量そのものを減少させることを目標にするか2つ
の方法がある。 スラグ中(FeO)と密接な関係のある吹錬操作
上の指標はスラグ中酸素量であつて、これは吹錬
酸素流量、排ガス流量、排ガス成分、転炉にチヤ
ージする溶銑の量及び成分、副原料の投入銘柄
(組成・成分)、副原料の投入速度等より求められ
る。したがつて予め吹錬前に特に吹錬末期にMn
富化の目標値を考慮したスラグ中酸素量の時間的
変化の許容限界をパターン化し、操業中逐次算出
されるスラグ中酸素量が予め定めた許容限界内に
入るごとく吹錬操作を行えばよい。 しかしてそのような操作の例としては、上吹酸
素ジエツトの調整がある。これは上吹ジエツトの
撹拌力を変えてスラグ−メタル間の撹拌状態およ
び諸反応のバランスを変化させ、スラグ中の酸素
ポテンシヤルを制御するもので、ランス高さを高
くしてソフトブローにするとスラグ中(FeO)の
増加、ランス高さを低くしてハードブローにする
とスラグ中(FeO)の減少に結びつく。 他の例として底吹ガスの調整がある。これは底
吹ガスの流量を変えてガスによる撹拌力を変化さ
せ、スラグ−メタル間の撹拌状態および諸反応の
バランスを変え、スラグ中酸素ポテンシヤルを制
御するもので、ガス流量を上げると、強撹拌とな
りスラグ中(FeO)の減少、ガス流量を下げる
と、スラグ中(FeO)の増加に結びつく。 スラグのフオーミングした容量そのものを減少
させようとする場合は、前述の炉内光を光検出装
置で検出して炉内のスラグレベルの測定を行い、
予めMn富化の目標値を考慮したスラグレベルの
時間的変化をパターン化したものを指標として、
前述のフオーミングの調整操作と同様の操作によ
つて、スラグレベルの低下すなわちスラグのフオ
ーミングした容量の低減を図ることができる。 以上のような方法により、本発明の目的を達す
ることができるがさらに実施例を述べて説明す
る。 実施例 1 170Tの上底吹転炉を用い、スロツピング予知
もしくは検知方法には前述の光検出装置を用い次
の通りに行つた。すなわち炉口下垂直距離で2.5
mの転炉側壁に貫通孔を設け、光フアイバーを内
蔵したプローブを貫通孔に臨ませて炉内光映像を
把え、光電変換装置としてCCDカメラを用いて
光電変換し、18.7m sec中に把えた映像中の黄
色系色彩の占める面積の割合すなわち面積率を求
め、スレシヨルドレベル50%で2値化して面積率
の2値化信号を得る。この面積率の時間的変化を
知るため高域透過フイルター・遮断周波数5Hzを
通し、正値化し、スレシヨルドレベル50%で2値
化して面積率の変化量の2値化信号を得る。これ
らを組合せ第1表のごとくスロツピングの可能性
を判定し、スロツピングの可能性有の時点でスロ
ツピング抑制操作を行つた。 吹錬初期および吹錬中期には、スラグ過形成吹
錬を行うため、基準パターンのランス高さより
200mm高くし、送酸量は全吹錬操作中一定を基準
とした。上述のスロツピングの可能性有と判定さ
れた時点では第2表の優先順位で表中のフオーミ
ング調整操作を行つた。但し、スロツピング予知
もしくは検出した際に、吹錬スタート前にあらか
じめフオーミング操作と同等のNo.2〜No.5の操作
が予定されている時は、それを優先させた。 このような操業を25回、従来法を25回行い、ス
ラグ中(T−Fe)%、吹止[P]×10-3%、吹止
[Mn]×10-2%の平均値並びにばらつきを計算し
て第3表に示した。 実施例 2 170Tの上底吹転炉を用い、スロツピング予知
もしくは検知方法は実施例1と同様とし、吹錬初
期と吹錬中期はスラグ過形成吹錬を吹錬末期は
Mn富化吹錬を行つた。 吹錬初期および吹錬中期は、ランス高さを基準
+200mm、送酸流量は基準量とし、吹錬末期はラ
ンス高さ基準−100mm、送酸流量は基準量、底吹
ガス流量は基準+300Nm3/Hrとした。 スロツピングの可能性有と判定された時点の操
作は実施例1と同一とした。 このような操業を21回行い、実施例1と同様の
表としてその結果を第4表に示した。 実施例 3 170Tの上底吹転炉を用い、スロツピング予知
もしくは検知方法は実施例1と同様とし、吹錬初
期と吹錬中期はスラグ過形成吹錬を、吹錬末期は
Mn富化吹錬を行つた。 ランス高さは吹錬初期および吹錬中期は、基準
+200mm、吹錬後期は基準にもどし、送酸流量は
吹錬全期間基準通りとし、底吹ガス流量は吹錬初
期および中期は基準通り、吹錬後期に基準+
300Nm3CO2/Hrとした。 従来の多くの操業実績を参考にして吹錬酸素流
量、排ガス流量、排ガス成分、転炉にチヤージす
る溶洗の量及び成分、副原料の投入銘柄(組成・
成分)、副原料の投入速度等より予めスラグ中酸
素量の経時変化の許容限界値を第2図に示すよう
に作成し、操業の基準とした。 操業中は、逐次算出されるスラグ中酸素量を許
容限界値のパターンと対比させたが、吹錬初期お
よび吹錬中期は、スラグ過形成吹錬のため上限値
あるいはこれを超える変化を示し、前述のスロツ
ピング予知または検知の判定があつた時点(第2
図中XおよびY)で、実施例1と同様なフオーミ
ング調整操作を行つた。 吹錬後期には、前述のスラグ中酸素量が増加す
るパターンになるが、増加傾向を示す時点(第2
図中Z)で鉄マンガン鉱石を0.9トン投入してス
ラグの冷却とMnの増加を図つた。 このような操業を18回行い、実施例1と同様の
表としてその結果を第5表に示した。 なお全実施例を通じてスロツピング発生吹錬比
率を計算すると、従来法の28%に対し、3%の低
率を示した。
INDUSTRIAL APPLICATION FIELD The present invention relates to a method of operating steel refining using a converter. Purpose of the Invention The purpose of the top-blown or top-bottom blown converter operating method is to reduce the carbon contained in the molten metal by oxygen supplied during converter blowing, and to reduce the slag-forming agent introduced into the furnace. The purpose is to cause dephosphorization, desulfurization, etc. to occur through the reaction between the molten slag and the molten metal. In this case, the state of slag slag is a major factor that determines the results of converter operation, and if slag progresses excessively,
This promotes the forming state of slag and eventually causes an abnormal reaction in which slag overflows outside the furnace, i.e., slopping, which causes various problems such as decreased work efficiency, decreased iron yield, deterioration of the working environment, and damage to equipment. . On the other hand, in the case of poor slag formation, the dephosphorization effect and the like deteriorate, making it impossible to obtain steel of desired quality. Therefore, it is desirable to carry out blowing in such a way that excessive slag is formed, and to control the blowing so that sloping does not occur. However, after the middle stage of blowing, when the decarburization reaction actively occurs, the oxygen that is not consumed for decarburization gradually increases, resulting in an increase in FeO in the slag, which reacts with Mn in the molten metal to produce manganese oxide. formation, resulting in a decrease in manganese content,
At this stage, it is desirable to be able to reduce the amount of oxygen in the slag or reduce the amount of slag itself to enrich the slag with Mn. The present invention provides a method that enables the above-mentioned desired operation. Structure and operation of the invention The structure of the present invention is as follows: 1. In a top-blowing or top-bottom blowing converter operating method,
2. A converter operating method, characterized in that blowing is carried out so that the slag always shows a superslag state from the early to middle stages of blowing, and that a forming adjustment operation is carried out when sloping is predicted or detected; and 2. In the top-blown or top-bottom blown converter operating method,
From the early to middle stages of blowing, the slag is always blown so that it shows a state of excessive slag, and when sloping is predicted or detected, forming adjustment operations are carried out, and at the end of the blowing, the amount of oxygen in the slag or A converter operating method characterized by carrying out a Mn enrichment operation using the slag formation status as an indicator. As mentioned above, one of the most important objectives of converter operation is decarburization. The oxygen jet blown from the lance collides with the molten metal surface, is quickly absorbed by the molten metal, reacts with C in the molten metal, and is discharged from the furnace mouth as CO or CO 2 gas. However, the rate of decarburization reaction in the actual furnace -
dc/dt changes as follows. In other words, early after the start of blowing, the concentration of Si in the molten metal is still high.
Since the molten metal temperature is still low, the decarburization reaction rate gradually increases. When the reaction progresses to a certain extent and the temperature of the molten metal rises, almost 100% of the supplied oxygen is consumed for decarburization, and the reaction rate becomes constant. After that, the concentration of C in the molten metal decreases, and when the diffusion of C in the molten metal to the collision surface between the oxygen jet and the molten metal becomes rate-determining,
The reaction rate gradually decreases. Therefore, considering the change in reaction rate over time based on the supply of oxygen - dc/dO 2 , or decarbonization efficiency, if the oxygen flow rate per hour is constant, then the change in decarburization efficiency in exactly the same way over time can be calculated as follows: The graph is schematically drawn as shown in Figure 1, and -dC/dO 2 at a constant reaction rate is usually around 1.08 Kg/Nm 3 . The time period of the flat line in this graph is defined as the middle period of blowing, and the periods before and after that are defined as the early and final stages of blowing, respectively. Of course, the change in -dC/dO 2 during actual blowing is not as simple as shown in FIG. 1, but the tendency can be considered to be roughly represented by FIG. 1. In the early and middle stages of blowing, Si in the molten metal is oxidized to SiO 2 by the injected oxygen.
This reacts with a slag-forming agent, such as quicklime, which is introduced into the furnace, to advance slag formation, and together with the reaction between oxygen and molten metal or the generation of (FeO) in the slag by a solvent, dephosphorization is performed. Therefore, it is desirable that slag generation tends to be excessive during this time. For this purpose, for example, the lance height may be increased, the top-blown oxygen jet may be soft-blown, and a blowing operation may be performed to increase the oxygen potential in the slag. Incidentally, the slag slag formation referred to in the present invention is a state in which slag production tends to be excessive as described above, and the oxygen potential in the slag remains high, causing slag formation of the slag-forming agent such as quicklime. This refers to a blowing situation that promotes excessive slag and causes a large amount of slag to exist in the furnace. Therefore, it is possible to determine whether or not there is excessive slagging by checking the amount of oxygen remaining in the furnace during blowing. For example, using the amount of residual oxygen in the furnace as an index, the limit of its temporal change can be patterned and preset in relation to the blowing time based on past results, etc., and can be used as a criterion for determining the excessive slag situation. . That is, by detecting the temporal change in the amount of residual oxygen in the furnace during operation and comparing it with the permissible limit pattern, it is possible to determine whether or not an excessive sludge condition exists. In other words, if the temporal change is below the permissible limit pattern, it can be determined that slag formation is not sufficiently promoted, and if it is above the permissible limit pattern, it can be determined that there is an excessive sludge formation situation. Temporal changes in the amount of residual oxygen in the furnace during blowing can be determined by calculating the flow rate and composition of exhaust gas, the amount of oxygen supplied, the temperature of molten steel, the carbon content, etc., as shown in JP-A No. 57-29519, for example. It can be easily detected by performing arithmetic processing. Further, whether or not the slag is present can also be determined by measuring the slag level. That is, when the oxygen potential in the slag becomes high and the slag becomes excessively slag, it means that an excessive amount of slag is formed. Therefore, similar to the above-mentioned permissible limit pattern of temporal change in residual oxygen amount, the slag level pattern during blowing is set in advance and used as a judgment criterion, and the slag level during blowing can be determined by various means described below. By directly detecting it and comparing it with the set pattern, it can be determined whether the inside of the furnace is in an over-slagging state or not reaching an over-slagging state. However, such blowing with excessive slag always involves the risk of slopping. Therefore, prediction or detection of sloping becomes an extremely important technique. Various attempts have been made to detect the slag level in the past, including the acoustic measurement method
33790), Vibration measurement method (Japanese Patent Application Laid-Open No. 114414/1983),
A method for measuring furnace internal pressure (Japanese Patent Application Laid-Open No. 104417-1982), a microwave measurement method (Japanese Patent Application Laid-open No. 140812-1982), a method for measuring the surface temperature of a furnace body (Japanese Patent Application Laid-open No. 48615-1987), etc. have been proposed. The acoustic measurement method attempts to predict the occurrence of sloping by estimating the slag level by ascertaining changes in the frequency and intensity of the sound generated from inside the furnace during blowing, while the vibration measurement method attempts to predict the occurrence of slopping. This method attempts to predict the occurrence of slopping by estimating the slag level or state by understanding vibration changes and waveform transitions, while the furnace pressure measurement method attempts to predict the occurrence of slopping by understanding changes in the furnace exhaust gas injection pressure during blowing. This method attempts to predict the occurrence of slopping, and the microwave measurement method involves directly projecting microwaves into the furnace during blowing.
This method uses the principle of FM radar to directly measure the slag level and predict the occurrence of slopping.The furnace surface temperature measurement method captures the radiant energy at the top and bottom of the furnace body as temperature, and measures temperature changes and peaks. It attempts to detect the occurrence and amount of sloping from values etc. In response to these, the present applicant first installed an in-furnace light measuring device in a through hole provided in the non-immersed part of the converter wall,
We applied for a patent (Japanese Patent Application No. 37872/1983) for a method for predicting slopping and detecting poor slag formation by observing the intensity and/or wavelength changes of the light in the furnace to detect the forming level. A patent application has been filed for a method for detecting the occurrence of slopping by detecting the light inside the furnace with a light detection device and extracting the proportion of mainly yellowish colors and the fluctuations in that proportion from the obtained color signal. This method can directly and quickly check the situation inside the furnace, especially the slag level. As mentioned above, by comparing the preset slag level pattern and the detected slag level, it is possible to determine whether or not there is excessive slag, and even if there is excessive slag, it is possible to determine whether the slag level is abnormal or not. By setting a level at which the risk of slopping increases, it is possible to accurately predict or detect the occurrence of sloping. Various methods have been proposed in the past for forming adjustment operations to be performed when sloping is predicted or detected. For example, adding a slopping inhibitor, increasing the flow rate of bottom blowing, lowering the lance height, reducing the flow rate of oxygen supply, and adding auxiliary materials are all effective, but the order of priority is as follows: is preferred. Further, when slopping is predicted or detected, if a forming adjustment operation less than the above-mentioned increase in bottom blowing amount is scheduled in advance before the start of blowing, that scheduled operation may be given priority. However, at the final stage of blowing, as mentioned above, FeO in the slag gradually increases and reacts with Mn in the molten metal to become MnO and transfers to the slag, or Mn in the molten metal and MnO in the slag Due to the equilibrium relationship between FeO and FeO, changes occur in which Mn decreases as FeO in the slag increases. Preventing these changes and enriching Mn will make effective use of valuable Mn. This is a valuable operation. In this case, there are two methods: either aiming to reduce the FeO in the slag, or aiming to reduce the formed capacity of the slag itself. The indicator for blowing operations that is closely related to FeO in the slag is the amount of oxygen in the slag, which includes the blowing oxygen flow rate, exhaust gas flow rate, exhaust gas composition, the amount and composition of hot metal charged to the converter, It is determined from the input brand (composition/ingredients) of auxiliary raw materials, input speed of auxiliary raw materials, etc. Therefore, before blowing, especially at the end of blowing, Mn
The permissible limit for the temporal change in the amount of oxygen in the slag should be patterned in consideration of the target enrichment value, and the blowing operation should be performed so that the amount of oxygen in the slag, which is calculated sequentially during operation, falls within the predetermined permissible limit. . Thus, an example of such manipulation is the adjustment of top blown oxygen jets. This is to control the oxygen potential in the slag by changing the stirring power of the top blowing jet to change the stirring state between the slag and metal and the balance of various reactions. Increase in FeO in the slag, and lowering the lance height to create a harder blow will lead to a decrease in FeO in the slag. Another example is the adjustment of bottom blow gas. This is to change the stirring force of the gas by changing the flow rate of the bottom blowing gas, changing the stirring state between the slag and metal and the balance of various reactions, and controlling the oxygen potential in the slag. Stirring results in a decrease in FeO in the slag, and lowering the gas flow rate leads to an increase in FeO in the slag. When attempting to reduce the volume of slag formed, the slag level inside the furnace is measured by detecting the aforementioned light inside the furnace with a photodetector.
Using a pattern of temporal changes in slag level that takes into account the target value of Mn enrichment in advance, as an indicator,
By performing an operation similar to the above-described forming adjustment operation, it is possible to lower the slag level, that is, reduce the formed capacity of the slug. Although the object of the present invention can be achieved by the method described above, further examples will be described and explained. Example 1 A 170T top-bottom blowing converter was used, and the above-mentioned photodetector was used to predict or detect sloping as follows. In other words, the vertical distance below the furnace mouth is 2.5
A through-hole was made in the side wall of the converter of m, and a probe with a built-in optical fiber was placed facing the through-hole to capture the optical image inside the furnace, and a CCD camera was used as a photoelectric conversion device to perform photoelectric conversion. The proportion of the area occupied by the yellowish color in the captured image, that is, the area ratio, is determined and binarized at a threshold level of 50% to obtain a binary signal of the area ratio. In order to know the temporal change in this area ratio, it is passed through a high-pass filter with a cutoff frequency of 5 Hz, converted into a positive value, and then binarized at a threshold level of 50% to obtain a binary signal of the amount of change in area ratio. By combining these, the possibility of sloping was determined as shown in Table 1, and a sloping suppression operation was performed when there was a possibility of sloping. In the early and middle stages of blowing, the lance height of the standard pattern is
The height was set at 200 mm, and the amount of oxygen supplied was kept constant during the entire blowing operation. At the time when it was determined that there was a possibility of slopping, the forming adjustment operations listed in Table 2 were performed in accordance with the priority order shown in Table 2. However, when slopping was predicted or detected, if operations No. 2 to No. 5, which are equivalent to forming operations, were scheduled before the start of blowing, priority was given to them. This kind of operation was carried out 25 times, and the conventional method was carried out 25 times, and the average values and variations of (T-Fe)% in the slag, blow-off [P] x 10 -3 %, blow-off [Mn] x 10 -2 % were determined. was calculated and shown in Table 3. Example 2 A 170T top-bottom blowing converter was used, and the slopping prediction or detection method was the same as in Example 1, with slag overforming blowing at the beginning and middle of blowing, and slag overforming blowing at the end of blowing.
Mn enrichment blowing was performed. In the early and middle stages of blowing, the lance height is the standard +200mm, the oxygen supply flow rate is the standard amount, at the end of the blowing, the lance height is -100mm, the oxygen supply flow rate is the standard amount, and the bottom blowing gas flow rate is the standard +300Nm 3 /Hr. The operations at the time when it was determined that there was a possibility of slopping were the same as in Example 1. Such operation was carried out 21 times, and the results are shown in Table 4, which is the same table as in Example 1. Example 3 A 170T top-bottom blowing converter was used, and the slopping prediction or detection method was the same as in Example 1, with slag overforming blowing being performed during the early and middle stages of blowing, and slag overforming during the final stage of blowing.
Mn enrichment blowing was performed. The lance height was set to the standard +200 mm during the early and middle stages of blowing, and returned to the standard during the late stage of blowing.The flow rate of oxygen was set to the standard throughout the entire blowing period, and the flow rate of bottom blowing gas was the same as the standard during the early and middle stages of blowing. Standard + in the latter half of blowing training
The pressure was set at 300Nm 3 CO 2 /Hr. Based on many past operating results, we determined the blowing oxygen flow rate, exhaust gas flow rate, exhaust gas components, the amount and composition of melt cleaning charged to the converter, and the brands of auxiliary raw materials (composition and composition).
As shown in Fig. 2, the permissible limit value for the change in oxygen content in the slag over time was prepared in advance from the input rate of auxiliary raw materials, etc., and was used as a standard for operation. During operation, the sequentially calculated oxygen content in the slag was compared with the pattern of the allowable limit value, but in the early and middle stages of blowing, due to slag hyperformation blowing, the oxygen content in the slag showed changes that were at or above the upper limit value. At the time when the above-mentioned sloping prediction or detection is determined (second
At points X and Y in the figure, forming adjustment operations similar to those in Example 1 were performed. In the later stages of blowing, the aforementioned pattern of increasing oxygen content in the slag occurs;
At Z) in the figure, 0.9 tons of ferromanganese ore was added to cool the slag and increase Mn. Such operation was carried out 18 times, and the results are shown in Table 5, which is the same table as in Example 1. When the blowing ratio of slopping occurrence was calculated for all the examples, it was found to be 3% lower than 28% for the conventional method.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

【表】 発明の効果 以上詳述したように本発明の操業方法を採用す
れば、転炉の操業は安定し、出鋼品質のばらつき
は少く、さらにMn富化操作を実施すれば吹錬後
の合金鉄の添加量を減少させることが可能で、製
鋼技術上の価値は極めて大きい。
[Table] Effects of the Invention As detailed above, if the operating method of the present invention is adopted, the operation of the converter will be stable, the variation in the quality of tapped steel will be small, and if the Mn enrichment operation is performed, the It is possible to reduce the amount of ferroalloy added, which is extremely valuable in terms of steelmaking technology.

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

第1図は脱炭酸素効率の経時変化を模式的に示
す図、第2図は本発明のMn富化操業方法の一例
を示す図である。
FIG. 1 is a diagram schematically showing the change over time in the decarburization oxygen efficiency, and FIG. 2 is a diagram showing an example of the Mn-enriching operation method of the present invention.

Claims (1)

【特許請求の範囲】 1 上吹もしくは上底吹転炉操業方法において、
吹錬の初期から中期にかけて、常にスラグが過滓
化状況を示すように吹錬し、スロツピングを予知
もしくは検出した際に、フオーミング調整操作を
実施することを特徴とする転炉操業方法。 2 上吹もしくは上底吹転炉操業方法において、
吹錬の初期から中期にかけて、常にスラグが過滓
化状況を示すように吹錬し、スロツピングを予知
もしくは検出した際に、フオーミング調整操作を
実施し、吹錬末期では、スラグ中酸素量もしくは
スラグ滓化状況を指標としてMn富化操作を実施
することを特徴とする転炉操業方法。
[Claims] 1. In a top-blowing or top-bottom blowing converter operating method,
A converter operating method characterized by blowing so that the slag always shows a slag condition from the early to middle stages of blowing, and performing a forming adjustment operation when slopping is predicted or detected. 2. In the top-blowing or top-bottom blowing converter operating method,
From the early to middle stages of blowing, the slag is always blown so that it shows a state of excessive slag, and when sloping is predicted or detected, forming adjustment operations are carried out, and at the end of the blowing, the amount of oxygen in the slag or A converter operating method characterized by carrying out Mn enrichment operation using the slag status as an indicator.
JP9112984A 1984-05-09 1984-05-09 Operating method of converter Granted JPS60234911A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9112984A JPS60234911A (en) 1984-05-09 1984-05-09 Operating method of converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9112984A JPS60234911A (en) 1984-05-09 1984-05-09 Operating method of converter

Publications (2)

Publication Number Publication Date
JPS60234911A JPS60234911A (en) 1985-11-21
JPH0468363B2 true JPH0468363B2 (en) 1992-11-02

Family

ID=14017922

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9112984A Granted JPS60234911A (en) 1984-05-09 1984-05-09 Operating method of converter

Country Status (1)

Country Link
JP (1) JPS60234911A (en)

Also Published As

Publication number Publication date
JPS60234911A (en) 1985-11-21

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