Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS625969B2 - - Google Patents
[go: Go Back, main page]

JPS625969B2 - - Google Patents

Info

Publication number
JPS625969B2
JPS625969B2 JP8129483A JP8129483A JPS625969B2 JP S625969 B2 JPS625969 B2 JP S625969B2 JP 8129483 A JP8129483 A JP 8129483A JP 8129483 A JP8129483 A JP 8129483A JP S625969 B2 JPS625969 B2 JP S625969B2
Authority
JP
Japan
Prior art keywords
powder
slopping
blowing
gas
tuyere
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
JP8129483A
Other languages
Japanese (ja)
Other versions
JPS59205410A (en
Inventor
Keiji Arima
Jujiro Ueda
Shoichi Osada
Yukinori Shigeyama
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 JP8129483A priority Critical patent/JPS59205410A/en
Publication of JPS59205410A publication Critical patent/JPS59205410A/en
Publication of JPS625969B2 publication Critical patent/JPS625969B2/ja
Granted 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
    • C21C5/30Regulating or controlling the blowing
    • C21C5/35Blowing from above and through the bath

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]

本発明は転炉操業方法に関し、炉内発生スロツ
ピングを効果的に抑制し吹錬を安定化させること
により効率的な転炉操業を可能ならしめる方法を
提供するものである。 周知の如く転炉では、溶湯中に吹込まれた酸素
が溶湯中の不純物を酸化し精錬反応を促進する。
この精錬中に、溶湯中の鉄も一部酸化され、酸化
鉄としてスラグ中に混入する。ところがスラグ中
に混入する前記酸化鉄が多くなり過ぎると過滓に
なり、スラグがフオーミングし、炉口からあふれ
出る云わゆるスロツピング現象が発生する。該ス
ロツピングは、例えば、溶銑配合比、スラグ塩基
度等の操業条件、あるいはその他の多くの要因に
よつて発生し、操業上の大きな問題となつてい
た。 上記スロツピングの抑制策として、例えば、ス
ロツピング発生時に炉上バンカーから塊状の抑制
剤を投入する方法、また底吹ノズルから吹錬ガ
ス、キヤリヤーガスと共に抑制剤粉を吹込む方法
等が提案されている。 而して本発明者らはこれらの方法を実際の転炉
に適用して次の知見を得た。 まず、炉上バンカーから塊状抑制剤を投入する
方法では抑制剤の投入時期が遅れてスロツピング
の抑制をできないことがあり、かつ、その粒度に
よつてスロツピング抑制効果が大きく変化するの
で、十分な抑制効果が得られないことがあるとい
う欠点がある。即ち、炉上バンカーは通常転炉よ
り離れた位置に設備されており、スロツピングを
検知してから抑制剤を秤量し投入するのでは炉内
に投入されるまでに相当時間がかかり迅速なアク
シヨンがとれないと云う問題があつた。又、抑制
剤の粒度が細か過ぎると投入された抑制剤はスラ
グフオーミング面上に拡がつて浮遊しスロツピン
グ抑制効果は小さくなる。逆に大きくなると、抑
制剤は、スラグ・メタル界面に沈み、前記抑制効
果が小さくなるうえに未溶解の抑制剤の精錬反応
におよぼす影響が、無視できなくなり、品質に悪
影響をおよぼす。さらに塊状の抑制剤では、一定
大きさ、形状の塊はないのでその反応にばらつき
があり、従つてスロツピング抑制効果も変動す
る。 一方、底吹ノズルより粉末の抑制剤を吹込む方
法として例えば特公昭57―5809の石灰石粉と炭素
粉の吹込み、特開昭49―129617の炭素吹込み等が
提案されている。しかしながら、これらの方法は
底吹による、低〔P〕鋼溶製、熱源添加、安価な
副材使用による省コストを狙つた底吹操業法であ
り、スロツピング抑制の効果を期待できるもので
なかつた。 即ち、底吹きのため、前記粉末は、溶鋼中へ吹
込まれるため溶鋼反応を介してのスラグ―メタル
反応となり直接、スラグ性状を抑制するものとは
なり得ないためと思はれる。又、底吹ノズルから
の粉体ふき込みは設備費が高いという欠点と、羽
口が常に溶鋼に接していることもあり、羽口管理
が極めて困難であるという問題を抱えている。 本発明は、前記従来法における欠点、問題点を
解決するために種々実験研究を重ねた結果なされ
たもので、スロツピング現象が検知された際に簡
単な操作で、迅速に、かつ確実にスロツピングを
抑制し、吹錬を安定化させることを可能ならしめ
る転炉操業方法であり、その要旨は転炉炉壁の通
常操業時には溶鋼に浸漬しない位置に羽口を設
け、該羽口より閉塞防止用ガスを吹込み羽口閉塞
を防止すると共にスロツピング現象を検知した
際、前記閉塞防止用ガスをキヤリヤーガスとして
石灰石粉、生石灰粉、石炭粉、コークス粉のうち
の1もしくは2以上の粉体を吹込み転炉内発生ス
ロツピングを抑制し、吹錬を安定化させることを
特徴とする、転炉操業方法である。 以下、実施例に基づき本発明を詳述する。 第1図は、本発明方法を上吹転炉に適用した一
実施例の構造図で、1は転炉、2は内張レンガ、
3は上吹ランス、4は、炉壁5に設けられた羽口
である。該羽口4は、炉壁5の通常操業時には溶
鋼6に浸漬しない位置に設けられている。7は前
記羽口4に後述する閉塞防止用ガスを供給するガ
ス供給装置であり、流量調整装置8および供給管
9を介して羽口4に連接されている。10は後述
するスロツピング抑制剤としての粉体を貯留し、
かつ、前記供給管9に供給する粉体圧送装置であ
り、フイーダー等の粉体供給装置11を介して前
記ガス供給装置7と羽口4との間の供給管9に接
続されている。 而して本発明においては通常の正常な操業状態
では羽口4より炉内圧より若干高い程度の必要最
小限のガスを連続的に炉内へ噴出させ羽口4の閉
塞を防止する。 該閉塞防止用ガスとしては、アルゴン(Ar)、
二酸化炭素(CO2)、チツ素(N2)等が使用でき、
鋼に与える品質影響、価格、取扱いの容易さ等を
考慮して適宜選定すればよい。例えば第1表は前
記ガスの価格指数であり、価格面からはN2,CO2
が有利である。
The present invention relates to a converter operating method, and provides a method that enables efficient converter operation by effectively suppressing slopping occurring in the furnace and stabilizing blowing. As is well known, in a converter, oxygen blown into the molten metal oxidizes impurities in the molten metal and promotes the refining reaction.
During this refining, some iron in the molten metal is also oxidized and mixed into the slag as iron oxide. However, if too much iron oxide is mixed into the slag, it becomes slag, forming the slag, and causing a so-called slopping phenomenon in which the slag overflows from the furnace mouth. This sloping occurs due to operating conditions such as the hot metal blending ratio, slag basicity, and many other factors, and has become a major operational problem. As methods for suppressing the above-mentioned slopping, for example, methods have been proposed, such as a method of injecting a block of inhibitor from an above-furnace bunker when sloping occurs, and a method of blowing inhibitor powder together with blowing gas and carrier gas from a bottom blowing nozzle. The present inventors applied these methods to an actual converter and obtained the following findings. First, with the method of introducing bulk inhibitor from the above-furnace bunker, the timing of introducing the inhibitor is delayed and sloping may not be suppressed.Also, the sloping suppressing effect varies greatly depending on the particle size, so sufficient suppression cannot be achieved. The drawback is that it may not be effective. In other words, the above-furnace bunker is usually installed at a distance from the converter, and if the inhibitor is weighed and introduced after detecting slopping, it will take a considerable amount of time to introduce it into the furnace, making quick action impossible. There was a problem that I couldn't get it. Furthermore, if the particle size of the inhibitor is too fine, the introduced inhibitor will spread and float on the slag forming surface, reducing the slopping inhibiting effect. On the other hand, if it becomes too large, the inhibitor sinks to the slag-metal interface, reducing the inhibitory effect, and the influence of the undissolved inhibitor on the refining reaction cannot be ignored, adversely affecting quality. Furthermore, in the case of block-like inhibitors, there are no lumps of a fixed size and shape, so the reaction varies, and therefore the slopping suppressing effect also varies. On the other hand, as a method of blowing a powdered inhibitor through a bottom blowing nozzle, for example, blowing of limestone powder and carbon powder in Japanese Patent Publication No. 57-5809, carbon injection in Japanese Patent Application Laid-open No. 129617-1974, etc. has been proposed. However, these methods are bottom-blowing operation methods that aim to save costs by melting low [P] steel, adding a heat source, and using inexpensive auxiliary materials, and cannot be expected to be effective in suppressing slopping. . That is, it is thought that this is because the powder is blown into the molten steel due to bottom blowing, so a slag-metal reaction occurs through the molten steel reaction, and it cannot directly suppress the slag properties. In addition, powder blowing from a bottom blowing nozzle has the drawback of high equipment costs and the fact that the tuyere is always in contact with molten steel, making it extremely difficult to manage the tuyere. The present invention was made as a result of various experimental studies to solve the drawbacks and problems of the conventional methods, and it is possible to quickly and reliably perform slopping with simple operations when a slopping phenomenon is detected. This is a converter operating method that makes it possible to suppress blowing and stabilize blowing.The gist of this is that a tuyere is installed on the converter wall at a position where it is not immersed in molten steel during normal operation, and from the tuyere, blowing is made possible to prevent blockage. Gas is injected to prevent tuyere clogging, and when a slopping phenomenon is detected, one or more powders of limestone powder, quicklime powder, coal powder, and coke powder are injected using the anti-clogging gas as a carrier gas. This is a converter operating method characterized by suppressing slopping occurring in the converter and stabilizing blowing. Hereinafter, the present invention will be explained in detail based on Examples. FIG. 1 is a structural diagram of an embodiment in which the method of the present invention is applied to a top-blown converter, where 1 is a converter, 2 is a lining brick,
3 is a top blowing lance, and 4 is a tuyere provided on the furnace wall 5. The tuyere 4 is provided at a position where the furnace wall 5 is not immersed in the molten steel 6 during normal operation. Reference numeral 7 denotes a gas supply device for supplying an anti-occlusion gas to the tuyere 4, which will be described later, and is connected to the tuyere 4 via a flow rate adjustment device 8 and a supply pipe 9. 10 stores powder as a slopping suppressant, which will be described later;
It is also a powder feeding device for supplying powder to the supply pipe 9, and is connected to the supply pipe 9 between the gas supply device 7 and the tuyere 4 via a powder supply device 11 such as a feeder. Accordingly, in the present invention, under normal operating conditions, the minimum necessary gas at a level slightly higher than the furnace internal pressure is continuously ejected from the tuyere 4 into the furnace to prevent the tuyere 4 from clogging. The gas for preventing blockage includes argon (Ar),
Carbon dioxide (CO 2 ), nitrogen (N 2 ), etc. can be used.
It may be selected as appropriate, taking into consideration the quality impact on steel, price, ease of handling, etc. For example, Table 1 shows the price index of the gas mentioned above, and from the price point of view, N 2 , CO 2
is advantageous.

【表】 一方、N2は吹上溶鋼中の〔N〕レベルを若干
高める恐れがある。本発明者等の経験では普通炭
素鋼に対してはN2吹込みで前記〔N〕レベルが
高まることによる品質に与える悪影響はほとんど
無視できる程度であつたが、前記普通炭素鋼以外
の高級鋼では前記〔N〕レベルの高まりが品質に
悪影響を与える可能性があり、CO2あるいはAr
を用いることが好ましかつた。 さて、前記操業(吹錬)中にスロツピング現象
が検知されたならば、粉体供給装置11を駆動
し、粉体圧送装置10からの粉体を供給管9に供
給し、前記閉塞防止用ガスをキヤリヤーガスとし
て炉内へ吹込む。 粉体としてはスラグ中の過剰な酸化鉄と反応し
てガスを生成するか、あるいは、それ自体が熱分
解してガスを発生することによつてスロツピング
を抑制する機能を有する石灰石粉、生石灰粉、石
炭粉、コークス粉を単味で、あるいはそれらの2
以上を適宜な割合いで組合せて用いる。 本発明においては、前記粉体が第1図に示すよ
うにフオーミング形成層12中に直接吹込まれる
ことからそれが極く微粉子のものであつてもフオ
ーミング形成層外に飛散することなく、吹込まれ
た全粒子がフオーミング形成層中に分散してフオ
ーミング形成層12のスラグと直接反応する。こ
のため前記粉体の機能が充分発揮でき、短時間で
スロツピングを抑制できる。 粉体の種類および供給量は炉容や製造される鋼
種およびスロツピングの程度等によつて決定すれ
ばよく、該供給量に応じてキヤリヤーガスとして
の前記ガスの吹込量、吹込圧等を決定し、流量調
整装置8を調整すればよい。 ところでスロツピング現象の検知には公知の方
法を適用することができる。例えば、オペレータ
ーが自分の眼で炉口フレーム等の観察を行い過去
の経験より判断し、検出する方法、吹錬中の吹錬
反応の1つとしてスラグの滓化状態を物理的、化
学的、もしくは目視的な手法により定量的定性的
に推定し、これをオペレーターガイドとして出力
されたデーターをもつてオペレーターが判断し、
検出する方法、吹錬中の滓化状況を炉内の音響レ
ベル、炉体の振動あるいは、ランス振動によつて
推定し、該滓化状況より、検知する方法、吹錬中
炉内のスラグ中酸素量を排ガス情報を用いて推定
し、該スラグ中酸素量より検知する方法等を適用
することができる。 又、前記吹錬パラメータとスロツピングとの関
係を例えば演算装置に記憶せしめると共に吹錬時
の検出値を前記演算装置に入力し、自動的にスロ
ツピング発生を判断し予知することも可能であ
る。本発明では実際にスロツピングが発生したこ
とを検出した場合は勿論のこと、前記吹錬パラメ
ータよりスロツピング発生を予知し、該予知情報
から粉体を吹込むよう制御することも可能であ
る。本発明において、スロツピング現象を検知す
ることは、前記スロツピングの予知までを含めて
云うものである。 次に本発明の具体的実施例について説明する。 実施例 1 180屯上底吹転炉において低炭Alキルド鋼を製
造する際に本発明方法を実施した。本実施例では
羽口4を通常操業時には溶鋼に浸漬しない位置の
炉壁に(本実施例では炉口より6mの位置)1個
設けた。該羽口4からはその閉塞を防止するため
常時120Nm3/Hr/個のCO2ガスを吹込んだ。 スロツピングの検知は、排ガス情報を用いて炉
内残留酸素量を計算し、スラグの滓化状態を推定
し、該スラグ滓化状態よりスロツピング発生を検
知する下記の方法で行つた。 先づ前記炉内残留酸素量とスロツピング発生と
の関係を調査した。第2図はその結果を示す図表
である。図において横軸は吹錬を開始してからの
時間を、縦軸はスラグ中の残留酸素量を示し、多
くの操業においてスロツピング発生を炉口観察で
検出しその時の残留酸素量と時間とを測定しプロ
ツトしてある。この図表から破線Zより残留酸素
量が高くなる側では、スロツピング発生率が急激
に高まることが確認された。 そこで、本実施例においては、吹錬中における
前記炉内残留酸素量の変動を追跡調査しスロツピ
ング現象の発生を監視したところ、第3図に示す
X点で残留酸素量が破線Zより高くなりスロツピ
ングの発生が検知された。 このため直ちに羽口4より前記閉塞防止用の
CO2ガスをキヤリヤーガスとして石灰石粉を130
Kg/mm/個の流量で吹込んだ。石灰石粉はその粒
度が3mm以下の粉体を用い、CO2ガスの流量を
600Nm3/Hrに増加させ、前記炉内へ吹込まれる
石灰石粉のキヤリヤーガスとしての機能を発揮さ
せた。 石灰石粉の吹込みを開始して1分後には前記炉
内残留酸素量が第3図に示すY点まで減少したた
めスロツピングが抑制されたものと判断し、石灰
石粉の吹込みを中止した。これに伴ない羽口4か
らのCO2ガスの吹込量を120Nm3/Hrにもどし
た。 実施例 2 実施例1と同様に180屯上底吹転炉において低
炭Alキルド鋼を製造する際にスロツピング抑制
用粉体の種類とスロツピング抑制効果を調査し
た。第2表は、粉体の種類とスロツピング抑制の
成功率との関係を従来法と比較して示したもので
ある。
[Table] On the other hand, N 2 may slightly increase the [N] level in blown up molten steel. In the experience of the present inventors, for ordinary carbon steel, the adverse effect on quality due to the increase in the [N] level due to N 2 injection was almost negligible, but for high-grade steels other than the ordinary carbon steel. In this case, the increase in [N] level mentioned above may have a negative effect on quality, and CO 2 or Ar
It was preferable to use Now, if a slopping phenomenon is detected during the operation (blowing), the powder supply device 11 is driven, the powder from the powder pumping device 10 is supplied to the supply pipe 9, and the blockage prevention gas is is blown into the furnace as a carrier gas. As a powder, limestone powder or quicklime powder has the function of suppressing sloping by reacting with excess iron oxide in slag to generate gas, or by thermally decomposing itself and generating gas. , coal powder, coke powder alone, or two of them.
The above methods are used in combination at an appropriate ratio. In the present invention, as the powder is directly blown into the forming layer 12 as shown in FIG. 1, even if the powder is extremely fine, it will not scatter outside the forming layer. All of the injected particles are dispersed in the forming layer and react directly with the slag of the forming layer 12. Therefore, the functions of the powder can be fully exhibited, and slopping can be suppressed in a short time. The type and amount of powder to be supplied may be determined depending on the furnace capacity, the type of steel to be manufactured, the degree of slopping, etc., and the amount and pressure of the gas blown as a carrier gas are determined according to the amount of supply. The flow rate adjustment device 8 may be adjusted. By the way, known methods can be applied to detect the sloping phenomenon. For example, there is a method in which an operator observes the furnace mouth frame with his own eyes and makes a judgment based on past experience, and a method in which the slag state of slag is detected physically, chemically, as one of the blowing reactions during blowing. Alternatively, it can be estimated quantitatively and qualitatively using a visual method, and then the operator can make a judgment using the output data as an operator guide.
A method of detecting slag formation during blowing, a method of estimating the slag formation state from the sound level in the furnace, vibrations of the furnace body, or lance vibration, and detecting it from the slag formation state; A method of estimating the amount of oxygen using exhaust gas information and detecting the amount of oxygen in the slag can be applied. It is also possible to automatically determine and predict the occurrence of slopping by storing the relationship between the blowing parameters and slopping in, for example, a computing device and inputting the detected values during blowing into the computing device. In the present invention, it is possible not only to detect the actual occurrence of sloping, but also to predict the occurrence of sloping from the blowing parameters and control the blowing of powder based on the predicted information. In the present invention, detecting a sloping phenomenon includes even predicting the sloping. Next, specific examples of the present invention will be described. Example 1 The method of the present invention was carried out in producing low carbon Al killed steel in a 180 ton top-bottom blowing converter. In this example, one tuyere 4 was provided on the furnace wall at a position that is not immersed in molten steel during normal operation (in this example, at a position 6 m from the furnace mouth). 120 Nm 3 /Hr/piece of CO 2 gas was constantly blown into the tuyere 4 to prevent clogging. Slopping was detected by the method described below, in which the amount of residual oxygen in the furnace was calculated using exhaust gas information, the state of slag sludge was estimated, and the occurrence of sloping was detected from the slag slag state. First, the relationship between the amount of residual oxygen in the furnace and the occurrence of slopping was investigated. Figure 2 is a chart showing the results. In the figure, the horizontal axis shows the time since the start of blowing, and the vertical axis shows the amount of residual oxygen in the slag.In many operations, the occurrence of slopping is detected by observation at the furnace mouth, and the amount of residual oxygen and time at that time are calculated. It has been measured and plotted. From this chart, it was confirmed that on the side where the amount of residual oxygen is higher than the broken line Z, the slopping occurrence rate increases rapidly. Therefore, in this example, when we tracked the fluctuations in the amount of residual oxygen in the furnace during blowing and monitored the occurrence of the slopping phenomenon, we found that the amount of residual oxygen became higher than the broken line Z at point X shown in FIG. An occurrence of slopping has been detected. For this reason, the above-mentioned blockage prevention valve is immediately opened from the tuyere 4.
130 limestone powder with CO2 gas as carrier gas
It was injected at a flow rate of Kg/mm/piece. Use limestone powder with a particle size of 3 mm or less, and adjust the flow rate of CO 2 gas.
The pressure was increased to 600 Nm 3 /Hr to allow the limestone powder blown into the furnace to function as a carrier gas. One minute after starting the injection of limestone powder, the amount of residual oxygen in the furnace decreased to point Y shown in FIG. 3, so it was judged that slopping had been suppressed, and the injection of limestone powder was stopped. Along with this, the amount of CO 2 gas blown from the tuyere 4 was returned to 120 Nm 3 /Hr. Example 2 Similar to Example 1, the type of powder for suppressing sloping and the effect of suppressing slopping were investigated when producing low carbon Al killed steel in a 180 ton top-bottom blowing converter. Table 2 shows the relationship between the type of powder and the success rate of slopping suppression in comparison with the conventional method.

【表】 第2表の従来法はスロツピングが検出された際
に炉口より塊状の生石灰(粒度15〜30mm)を300
Kg/回、投入した実施例である。又本発明法では
CO2ガスをキヤリヤーガスとしてスロツピング検
出の際に各種の粉体(粒度3mm以下)をそれぞれ
130Kg/mm/個吹込み、そのときのCO2ガス量を
600Nm3/Hrとした。 スロツピング抑制成功の判断基準はスロツピン
グが検知され、粉体(従来法では塊生石灰)の吹
込みを開始してから1分以内にスロツピングが完
全に抑制されたか否かによつて判断し、1分以内
に完全に抑制されたときを成功とした。該第2表
から本発明方法によるときには、スロツピング抑
制の成功率は従来法に比べて極めて高いことが明
らかである。 さて第4図に、前記複数のガスおよび粉体を選
択し、吹込むことを可能ならしめる本発明方法を
適用可能な転炉の他の実施例の構造図を示す。こ
の図において、70a,70b,70cはそれぞ
れ異なつた種類のガスを供給するガス供給装置で
あり、切替弁13a,13b,13cおよび流量
調整装置80a,80b,80cを介して供給管
9に接続されている。而して切替弁13a,13
b,13cを切替制御することにより任意のガス
を吹込むことができる。又、10a,10b,1
0cは粉体圧送装置であり、各々の粉体圧送装置
10a,10b,10cに貯留された粉体は、粉
体供給装置11a,11b,11cによつて必要
な粉体が単味で、あるいは、適宜な割合で混合せ
しめられ供給管9に送給される。 本発明方法では粉体を、鋼の品質に悪影響を与
えないキヤリヤーガスと共にフオーミング形成層
中に吹込むことから、反応性は高いけれども従来
その使用が極めて困難であつた微粉子の粉体を使
用できる利点がある。加えてスロツピングが検出
された時点で直ちに前記抑制剤としての粉体をフ
オーミング形成層中に直接吹込むことが可能であ
り、このため極めて短時間に、かつ高い率で確実
にスロツピングを抑制することができる効果があ
る。そこで安定した吹錬ができる。 以上のように本発明の実用的効果は非常に大で
ある。
[Table] In the conventional method shown in Table 2, when slopping is detected, 300 lumps of quicklime (particle size 15 to 30 mm) are poured from the furnace mouth.
This is an example in which Kg/time was introduced. Also, in the method of the present invention
Various powders (particle size 3 mm or less) are used for slopping detection using CO 2 gas as a carrier gas.
Inject 130Kg/mm/piece, and calculate the amount of CO 2 gas at that time.
It was set to 600Nm 3 /Hr. The criterion for success in suppressing slopping is whether or not sloping is completely suppressed within 1 minute after sloping is detected and injection of powder (in the conventional method, lump quicklime) is started. Success was defined as complete suppression within a certain period of time. From Table 2, it is clear that when the method of the present invention is used, the success rate of suppressing slopping is extremely high compared to the conventional method. Now, FIG. 4 shows a structural diagram of another embodiment of a converter to which the method of the present invention, which makes it possible to select and inject the plurality of gases and powders, is applicable. In this figure, 70a, 70b, 70c are gas supply devices that supply different types of gas, respectively, and are connected to the supply pipe 9 via switching valves 13a, 13b, 13c and flow rate adjustment devices 80a, 80b, 80c. ing. Therefore, the switching valves 13a, 13
Any desired gas can be blown by controlling b and 13c. Also, 10a, 10b, 1
0c is a powder feeding device, and the powder stored in each of the powder feeding devices 10a, 10b, 10c is fed by the powder feeding devices 11a, 11b, 11c, so that the necessary powder can be delivered as a single powder, or , mixed in an appropriate ratio and fed to the supply pipe 9. In the method of the present invention, the powder is blown into the forming layer together with a carrier gas that does not adversely affect the quality of the steel, so it is possible to use fine powder, which is highly reactive but has been extremely difficult to use in the past. There are advantages. In addition, it is possible to directly inject the powder as the suppressor into the forming layer as soon as sloping is detected, which makes it possible to reliably suppress sloping in an extremely short period of time and at a high rate. It has the effect of Stable blowing can be done there. As described above, the practical effects of the present invention are very large.

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

第1図は、本発明方法が適用できる上吹転炉の
一実施例を示す構造図、第2図は炉内残留酸素量
とスロツピングの発生との関係を示す図表、第3
図は、吹錬中の炉内残留酸素量の追跡調査結果の
一例を示す図表、第4図は、本発明方法が適用で
きる上吹転炉の他の実施例を示す構造図である。 1:転炉、2:内張レンガ、3:上吹ランス、
4:羽口、5:炉壁、6:溶鋼、7,70a,7
0b,70c:ガス供給装置、8,80a,80
b,80c:流量調整装置、9:供給管、10,
10a〜10c:粉体圧送装置、11,11a〜
11c:粉体供給装置、12:フオーミング形成
層、13a〜13c:切替弁。
Fig. 1 is a structural diagram showing an example of a top-blown converter to which the method of the present invention can be applied, Fig. 2 is a diagram showing the relationship between the amount of residual oxygen in the furnace and the occurrence of slopping, and Fig. 3 is a diagram showing the relationship between the amount of residual oxygen in the furnace and the occurrence of slopping.
The figure is a chart showing an example of the results of a follow-up investigation of the amount of residual oxygen in the furnace during blowing, and FIG. 4 is a structural diagram showing another embodiment of a top-blowing converter to which the method of the present invention can be applied. 1: converter, 2: lining brick, 3: top-blown lance,
4: Tuyere, 5: Furnace wall, 6: Molten steel, 7, 70a, 7
0b, 70c: Gas supply device, 8, 80a, 80
b, 80c: flow rate adjustment device, 9: supply pipe, 10,
10a-10c: Powder feeding device, 11, 11a-
11c: powder supply device, 12: forming layer, 13a to 13c: switching valve.

Claims (1)

【特許請求の範囲】[Claims] 1 転炉炉壁の通常操業時には溶鋼に浸漬しない
位置に羽口を設け、該羽口より閉塞防止用ガスを
吹込み羽口閉塞を防止すると共にスロツピング現
象を検知した際、前記閉塞防止用ガスをキヤリヤ
ーガスとして石灰石粉、生石灰粉、石炭粉、コー
クス粉のうちの1もしくは2以上の粉体を吹込み
転炉内発生スロツピングを抑制し、吹錬を安定化
させることを特徴とする、転炉操業方法。
1. A tuyere is provided on the converter wall at a position where it is not immersed in molten steel during normal operation, and an anti-occlusion gas is blown through the tuyere to prevent clogging of the tuyere, and when a slopping phenomenon is detected, the anti-occlusion gas is A converter characterized in that one or more of limestone powder, quicklime powder, coal powder, and coke powder is injected as a carrier gas to suppress slopping occurring in the converter and stabilize blowing. Operating method.
JP8129483A 1983-05-10 1983-05-10 Operating process of converter Granted JPS59205410A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8129483A JPS59205410A (en) 1983-05-10 1983-05-10 Operating process of converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8129483A JPS59205410A (en) 1983-05-10 1983-05-10 Operating process of converter

Publications (2)

Publication Number Publication Date
JPS59205410A JPS59205410A (en) 1984-11-21
JPS625969B2 true JPS625969B2 (en) 1987-02-07

Family

ID=13742359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8129483A Granted JPS59205410A (en) 1983-05-10 1983-05-10 Operating process of converter

Country Status (1)

Country Link
JP (1) JPS59205410A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100340501B1 (en) * 1997-10-09 2002-10-25 주식회사 포스코 A Method for Preventing Slopping Phenomina in Converter by Injection of Cokes and a Apparatus therefor
CN100343397C (en) * 2003-09-17 2007-10-17 首钢总公司 Process for producing steel containing alumium low carbon low ilicon by small square blank continuous caster
WO2009003364A1 (en) * 2007-07-03 2009-01-08 Northeastern University A manufacture process of steel in converter with top, bottom and side lances
CN111500815B (en) * 2020-05-28 2021-06-11 北京科技大学 Bottom blowing O2-CO2Dynamic control method for steelmaking process of CaO converter

Also Published As

Publication number Publication date
JPS59205410A (en) 1984-11-21

Similar Documents

Publication Publication Date Title
CN101818231B (en) Control method for preventing splash during refining ferrochromium alloy with argon oxygen
EP2331715B1 (en) Low cost making of a low carbon, low sulfur, and low nitrogen steel using conventional steelmaking equipment
CN113661257A (en) Splash prediction method of converter, operation method of converter, and splash prediction system of converter
JP2015092026A (en) Hot metal pretreatment method
JPS625969B2 (en)
US6793708B1 (en) Slag composition
JP3164976B2 (en) Method for predicting slopping in a converter and its prevention
EP0996749B1 (en) Method for controlling a smelting reduction process
US4891064A (en) Method of melting cold material including iron
GB1597597A (en) Preparation of low-carbon low-nitrogen steels in the basic oxygen process
JP5289906B2 (en) Forming suppression method in dephosphorization process
JP2654587B2 (en) Carbon material injection method to control slag forming
JP2800537B2 (en) Prediction method of molten steel and slag spouting scale in refining process
JP3665600B2 (en) Hot metal dephosphorization method
JP7852660B2 (en) Pre-treatment method for molten iron
KR100225249B1 (en) Remaining slag control method of of slopping control
JP3529641B2 (en) Hot metal dephosphorization treatment method
JP4025713B2 (en) Dephosphorization method of hot metal
JP2671063B2 (en) Slag forming prevention method
JP2654586B2 (en) Carbon material injection method to control slag forming
JP2000160222A (en) How to deal with slag forming during hot metal pretreatment
RU2125099C1 (en) Method of steel melting in converter
JPS62196314A (en) Operating method for converter
JPS6372811A (en) How to prevent slopping
JPS62205221A (en) Method for degassing and dephosphorizing molten steel