JPS6224488B2 - - Google Patents

Info

Publication number
JPS6224488B2
JPS6224488B2 JP16431784A JP16431784A JPS6224488B2 JP S6224488 B2 JPS6224488 B2 JP S6224488B2 JP 16431784 A JP16431784 A JP 16431784A JP 16431784 A JP16431784 A JP 16431784A JP S6224488 B2 JPS6224488 B2 JP S6224488B2
Authority
JP
Japan
Prior art keywords
purge gas
furnace
hole
gas
converter
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
JP16431784A
Other languages
Japanese (ja)
Other versions
JPS6144117A (en
Inventor
Tooru Yoshida
Yutaka Narita
Keiji Arima
Jujiro Ueda
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 JP16431784A priority Critical patent/JPS6144117A/en
Publication of JPS6144117A publication Critical patent/JPS6144117A/en
Publication of JPS6224488B2 publication Critical patent/JPS6224488B2/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
    • C21C5/42Constructional features of converters
    • C21C5/46Details or accessories
    • C21C5/4653Tapholes; Opening or plugging thereof
    • 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
    • C21C5/4693Skull removal; Cleaning of the converter mouth

Landscapes

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

Description

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

産業上の利用分野 転炉炉壁に貫通孔を設け、炉内を観測すると共
に、必要な添加物を吹込むことは、転炉操業上き
わめて有効な方法である。 本発明はこの炉壁貫通孔の閉塞防止に関するも
のである。 従来の技術 転炉操業の目的は、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、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、種々の問題が生ずる。 これに反し、滓化不良の場合は、脱燐作用等が
低下し、所望の品質を得ることができない。 したがつて、滓化を充分行わせながらスロツピ
ングを生じさせない操業方法がとられるべきで、
そのためには炉内の状況を時々刻々に的確に把
え、臨機に滓化促進又は抑制のための添加物を吹
込むことが望ましい。 出願人は以上の目的を達成するため、転炉炉壁
に貫通孔を設けて炉内光を観測する装置(特開昭
60−228929)および、貫通孔からスロツピング抑
制材を吹込む装置(特開昭60−245715)(特開昭
60−245716)を特許出願した。 これら装置を有効に機能させるためには貫通孔
の閉塞を防止する必要があり、閉塞防止方法につ
いても既に特許出願(特開昭60−228930)(特開
昭60−234911)した。 これらは何れも貫通孔に吹込むパージガス中に
酸素を混入するものであつた。 発明が解決しようとする問題点 上述のパージガスに酸素を混入する方法はきわ
めて有効な方法であるが、酸素濃度を過度に高め
ると内張り煉瓦まで溶失損傷させるおそれがあ
り、また酸素吹込みにより一酸化炭素を主成分と
する炉内ガスが燃焼し、回収ガスの量が低下する
と共にその品質も劣化する。 本発明は、これらの欠点を極力抑えたパージガ
スに酸素を混合する改良された方法を提供するも
のである。 問題点を解決するための手段・作用 本発明の構成は、転炉側壁に設けられた添加物
吹込みおよび炉内観測用の貫通孔閉塞防止方法に
おいて、該貫通孔に装置された添加物吹込プロー
ブ、および光検出端に酸素ガスを含むパージガス
吹込装置を付設し、前記光検出端によるスラグフ
オーミング検出状況に応じて、前記パージガス中
の酸素濃度を変更し、前記貫通孔の閉塞防止を行
うことを特徴とする転炉側壁貫通孔の閉塞防止方
法である。 本発明の方法を実施する装置の一例を図示し、
図によつて本発明方法を説明する。 第1図は本法の全容を示す説明図である。本図
においては、炉内観測用光検出端を内蔵してなる
添加物吹込プローブを、転炉側壁に設けられた貫
通孔に設備するごとく例示したものである。 第1図において添加物吹込装置の一部である添
加物吹込プローブ6の中には、光検出装置の一構
成要素である光検出プローブ62が内蔵かれ、光
検出プローブ62は、第3図に示すごとく光検出
端61を内蔵し、その先端には観測窓63がチツ
プ64によつて装着されている。 光検出端は、光導体例えば石英系光フアイバー
の如く、高温物体から放射される放射光を低損失
で伝送する導体から成り、その後端にはコネクタ
9を介して光電変換素子10が結合され、さらに
演算装置11、判定装置12と連結される。 本発明におけるスラグフオーミング検出状況
は、上述の光検出端61から判定装置12までの
一連の装置で得られるもので、その概要について
説明する。 転炉操業中、炉内の滓化がある程度進行して、
スラグ上部のガスの温度がスラグの温度よりも高
くなると、このガス雰囲気の発する光とスラグの
発する光の、波長と強度の関係は明らかな差異を
示す。 この事実から、炉内光を把えて光電変換し、3
種の波長域B(青)、G(緑)、R(赤)に分別
し、受光しなかつたときの黒も含めて8色の色別
面積信号として映像を処理し、色別面積の大きさ
と、その面積の変化の大きさをそれぞれ2値化信
号として取り出す。 これらの中、スラグのフオーミング状態と最も
相関の高い色又は色の組合せを多数の実績から求
め、以後はその色又はその色の組合せに絞つて一
定の基準を設定し、観測値をこの基準と比較する
ことによつて、炉内状況特にスロツピングの発生
の可能性を予知することができる。 発明者の経験によれば、上記の相関の高い色又
は色の組合せは黄;黄と赤;黄と白であつて、黄
色系色彩のみで充分の判定成功率が得られた。 以上の説明をブロツク図であらわせば、第2図
のようで、第1図の演算装置として括つた部分を
より詳細に示したものである。光検出端で把えら
れた炉内光の映像は、光電変換素子例えばITVカ
メラによつて光電変換映像信号として波長別分別
装置21に入力する。ここで炉内光は全波長域を
B(青)、G(緑)、R(赤)に分別され、波長域
毎の映像信号(R・G・B信号)として取出さ
れ、適当なスレシヨルドレベルで2値化回路22
で2値化されて面積演算回路23に入力する。 面積演算回路では例えば黄色面積の場合2値化
R信号、2値化G信号、2値化B信号をカウント
パルス0.134μsecにのせ、一定のリセツトパルス
間のパルス×2値化信号からR・Gon、Boffのパ
ルス数をカウントして、黄色面積値として出力さ
れる。 このようにして得られた面積信号を2系統に別
け、一系統はそのまま適当なスレシヨルドレベル
で2値化回路24で2値化して判定装置に入力
し、他の一系統は面積信号の時間的変化の大きさ
をとり出すために高域透過フイルター25、正値
化回路26を通して2値化回路27で2値化して
判定装置12に入力する。 判定装置ではこれら2つの2値化信号の組合せ
により、例えば第1表のごとくスロツピング発生
の可能性を判定し、可能性の無、小、中、大に応
じてそれぞれアラーム無、1次アラーム、2次ア
ラーム、3次アラームを発する。
Industrial Application Fields Providing a through hole in the converter wall to observe the inside of the furnace and inject necessary additives is an extremely effective method for operating a converter. The present invention relates to prevention of blockage of the furnace wall through-hole. Conventional technology The purpose of converter operation is to reduce the carbon contained in the molten metal using oxygen supplied during converter blowing, and to turn the slag-forming agent introduced into the furnace into sludge, thereby reducing the generated molten slag. The purpose is to cause dephosphorization, desulfurization, etc. to occur through the reaction between the molten metal and the molten metal. In this case, the slagging state of the slag is a major factor that determines the operational results.If the slag slag progresses excessively, it will promote the forming state of the slag and eventually cause an abnormal reaction in which the slag overflows outside the furnace, that is, slopping. Various problems arise, such as a decrease in work efficiency, a decrease in iron yield, a deterioration of the work 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 the desired quality. Therefore, it is necessary to adopt an operating method that does not cause slopping while allowing sufficient slag formation.
For this purpose, it is desirable to accurately grasp the situation inside the furnace from time to time and inject additives to promote or suppress slag formation as needed. In order to achieve the above objectives, the applicant has developed a device for observing light inside the converter furnace by providing a through hole in the converter wall.
60-228929) and a device for injecting a slopping suppressing material from a through hole (Japanese Patent Application Laid-Open No. 60-245715)
60-245716) was applied for a patent. In order for these devices to function effectively, it is necessary to prevent the through holes from being blocked, and a patent application has already been filed for a method for preventing blockage (Japanese Patent Laid-Open No. 60-228930) (Japanese Patent Laid-Open No. 60-234911). All of these methods mixed oxygen into the purge gas blown into the through holes. Problems to be Solved by the Invention Although the above-mentioned method of mixing oxygen into the purge gas is an extremely effective method, if the oxygen concentration is increased excessively, there is a risk that even the lining bricks will be melted and damaged. The gas in the furnace whose main component is carbon oxide is combusted, and the amount of recovered gas decreases, as well as its quality. The present invention provides an improved method of mixing oxygen into purge gas that minimizes these drawbacks. Means and Effects for Solving the Problems The structure of the present invention provides a method for preventing blockage of a through hole provided in the side wall of a converter for injecting additives and observing inside the furnace. A purge gas blowing device containing oxygen gas is attached to the probe and the photodetection end, and the oxygen concentration in the purge gas is changed depending on the state of slag forming detected by the photodetection end to prevent the through hole from being blocked. This is a method for preventing blockage of a through hole in a converter side wall. illustrating an example of an apparatus for carrying out the method of the invention,
The method of the present invention will be explained with the aid of figures. FIG. 1 is an explanatory diagram showing the entire outline of this method. In this figure, an additive injection probe having a built-in optical detection end for inside the furnace is illustrated as being installed in a through hole provided in the side wall of the converter. The additive injection probe 6, which is a part of the additive injection device in FIG. 1, has a built-in photodetection probe 62, which is a component of the photodetection device. As shown, a light detection end 61 is built in, and an observation window 63 is attached to the tip of the light detection end 61 by a chip 64. The photodetection end is made of a conductor, such as a quartz optical fiber, that transmits synchrotron radiation emitted from a high-temperature object with low loss, and a photoelectric conversion element 10 is coupled to the rear end via a connector 9. Furthermore, it is connected to an arithmetic device 11 and a determination device 12 . The slug forming detection situation in the present invention is obtained by a series of devices from the above-mentioned photodetection end 61 to the determination device 12, and its outline will be explained. During converter operation, slag formation inside the furnace progresses to some extent,
When the temperature of the gas above the slag becomes higher than the temperature of the slag, there is a clear difference in the wavelength and intensity relationship between the light emitted by the gas atmosphere and the light emitted by the slag. From this fact, we can understand the light inside the furnace and convert it into electricity, 3
Separates the species into wavelength ranges B (blue), G (green), and R (red), processes the image as area signals for each color in 8 colors, including black when no light is received, and calculates the size of the area for each color. and the magnitude of the change in area are respectively extracted as binary signals. Among these, the color or color combination that has the highest correlation with the slag forming state is determined from a large number of results, and from then on, a certain standard is set for that color or color combination, and the observed values are based on this standard. By comparison, it is possible to predict the situation inside the furnace, especially the possibility of slopping occurring. According to the inventor's experience, the above-mentioned highly correlated colors or combinations of colors are yellow; yellow and red; and yellow and white, and a sufficient determination success rate was obtained only with yellow colors. If the above explanation were to be expressed in a block diagram, it would be as shown in FIG. 2, which shows in more detail the portions grouped together as the arithmetic unit in FIG. 1. The image of the light inside the furnace captured by the photodetection end is input to the wavelength separation device 21 as a photoelectric conversion image signal by a photoelectric conversion element, for example, an ITV camera. Here, the entire wavelength range of the light inside the furnace is divided into B (blue), G (green), and R (red), which are extracted as video signals (R, G, and B signals) for each wavelength range, and are divided into appropriate thresholds. Binarization circuit 22 at the field level
It is binarized and input to the area calculation circuit 23. In the area calculation circuit, for example, in the case of a yellow area, the binarized R signal, the binarized G signal, and the binarized B signal are placed on a count pulse of 0.134 μsec, and R・Gon is calculated from the pulse between constant reset pulses x the binarized signal. , the number of Boff pulses is counted and output as a yellow area value. The area signal obtained in this way is divided into two systems, one system is binarized as it is by the binarization circuit 24 at an appropriate threshold level and input to the determination device, and the other system is the area signal. In order to extract the magnitude of the temporal change, the signal passes through a high-pass filter 25 and a positive value conversion circuit 26, is converted into a binary value by a binarization circuit 27, and is input to the determination device 12. The determination device uses a combination of these two binary signals to determine the possibility of slopping occurring, for example, as shown in Table 1, and depending on whether the possibility is non-existent, low, medium, or high, it will issue no alarm, primary alarm, or a primary alarm, respectively. Issues secondary and tertiary alarms.

【表】 しかして実際には、判断時の転炉の操業状況も
考慮する必要がある。例えば吹錬初期では炉内ガ
ス温度も低いから炉内光は黄色系に偏るし、鉱石
投入、副材投入、溶銑中のシリコン量等も炉内光
変化の要因で、これらの情報も必要である。 これらをまとめて吹錬条件28として図示し
た。 このようにして炉況を観測し、得られる情報か
らたとえばスラグ量を増大する必要のある場合は
砂鉄粉、焼結鉱粉、スケール粉、鉄マンガン鉱粉
などの酸化材の装入が好ましく、スラグのフオー
ミングを抑制する必要のある場合は、コークス
粉、石炭粉などの炭素源を含む環元剤の装入が好
ましい。 これら添加剤のうち特にスロツピング抑制に有
効な環元剤などは、迅速に装入してしかも速かに
反応させるために、粒度は5mm以下好ましくは3
mm以下の粉状とし、キヤリヤーガスで気流輸送
し、吹込ノズルから炉内に吹込む方法が極めてよ
いことが判明した。 第1図には、上述の炉内観測と添加物吹込みの
装置を連動させるごとく設備した例を示した。す
なわち判定装置12から、例えば第1表の判断に
従つて3次アラームが発せられた場合、吹込制御
装置13が作動し、止弁31を開いて不活性ガス
源30からの不活性ガスを給粉タンク70に送り
給粉タンクを加圧すると共に、キヤリヤーガス配
管系50の流量調節装置53および給粉タンクの
出口弁71を調整して、必要量の添加物をキヤリ
ヤーガスと共に添加物入口68から添加物吹込ノ
ズル69に送りこむようにしたものである。 ここでキヤリヤーガスは、前述の添加物と常温
で反応することなく、炉内に吹込まれた場合に炉
内内容物とも容易には反応することなく、且つ目
標とする鋼成分に影響を与えないガスが好まし
く、CO2,Ar,N2などの不活性ガスが用いられ
る。 添加物吹込ノズルおよび光検出端は、貫通孔内
に装置されるため特にその先端部分は高温にさら
され損耗のおそれがあるため冷却する必要があ
る。また光検出端の先端にとりつけられた観測窓
の粉塵付着も防止する必要がある。これらの必要
を満すため、通常一定量の不活性ガスをブローし
ておく。以下このガスをパージガスと称するが、
パージガスは3系統に分けられ導入される。 パージガス配管系41は止弁、減圧弁、流量調
節装置、止弁等通常の配管設備を備え、パージガ
ス入口66に導かれ、光検出プローブ62内の空
隙65を通つて、光検出プローブを冷却後チツプ
64に設けられたパージガス出口67より観測窓
63の粉塵付着を防止しつつ、炉内に放出され
る。 パージガス配管系42は、パージガス配管系4
1と同様の設備を備え、パージガスは添加物吹込
プローブ6のパージガス入口692より添加物吹
込ノズル69とその外筒との間の空隙691を通
り、吹込ノズルおよび外筒を冷却して炉内に放出
される。 他の一つのパージガス配管系は、キヤリヤーガ
ス配管系50であつて、添加物吹込み時以外であ
つても、一定量の不活性ガスを添加物吹込ノズル
に流しておく。 以上述べたパージガスにより、光検出プローブ
および添加物吹込ノズルは保護されるが、このパ
ージガスの冷却効果により貫通孔の閉塞はむしろ
促進される。貫通孔閉塞の原因は吹錬中の炉内内
容物の貫通孔への付着、あるいは既往の吹錬時の
スラグ等のたれかけによるものであつて、発明者
の経験によれば、たとえパージガスの貫通孔出口
の吐出速度を22m/sec程度にしても、速度上昇
による効果は認められたが閉塞を防止することは
できなかつた。 パージガスについて種々検討の結果、パージガ
ス中に酸素を混入することが閉塞防止上有効で、
混合ガス中のO2濃度が30〜45%程度が好ましい
ことは、既に本出願人が前記した特許(特開昭60
−228930)で明らかにしたところである。これを
第1図および第3図の例示で説明すれば、パージ
ガス配管系42にO2ガス配管系55を結合し、
O2含有ガスはパージガス入口692より添加物
吹込プローブに供給され、先端開口部693より
噴出されるごとく構成される。 しかしてO2の含有率は、パージガス配管系4
1および50の流量は一定にできるから、パージ
ガス配管系42の流量調節装置58と、O2ガス
配管系の流量調節装置57の流量比率を比率設定
器56で設定して、全パージガス量に対する酸素
添加量を調整できる。 本例では、添加物吹込プローブの最も外側にあ
る空隙691の先端開口部693よりO2含有パ
ージガスが噴出し、その先端部で燃焼することか
ら、スラグや添加物の付着を効率的に防止でき、
光導体や観測窓を全く損傷することはない。 しかしながらO2の添加は、転炉側壁レンガを
損傷させるおそれがあり、また炉内で発生する
CO主成分のガスを燃焼させてその価値を低下さ
せるものであるから、O2の添加量を必要最小限
に止めるべく種々検討を加えた。その結果貫通孔
の閉塞は、滓化が正常な場合10〜15%の酸素濃度
で予防できること、およびフオーミング状態が進
行して前述の1次アラーム、2次アラーム、3次
アラームの発信があつた場合に、それぞれに対応
した酸素濃度に変更することにより防止できるこ
とが明らかになつた。変更すべき酸素濃度は、ア
ラームの次数が多くなるほど高くなり、その絶体
値については判定基準、炉容および貫通孔の位
置、寸法等により異るので、一概に規定は困難で
あるが、一例を後述の実施例で示す。 以上の知見から第1図の如く、スラグフオーミ
ング状況検出の判定装置12の判定を比率制御装
置14に入力し、比率設定器56を制御すること
により本法を実施することができる。 なお上述の説明においては、一つの貫通孔に添
加物吹込ノズルおよび光検出端を装置した例を示
したが、これに限定するものでなく、例えば複数
個の貫通孔に添加物吹込ノズルおよび光検出端を
別個に装置しても、この方法は実施できるもので
ある。 実施例 170t/CHの上底吹転炉の炉底から約4mの高
さの転炉側壁に直径約15cmの貫通孔を設け、第1
図および第3図の如き装置により、上述のアラー
ムの区分毎にパージガス量と添加酸素ガス量を変
えて、試験回数に対する貫通孔閉塞回数を求め
た。 この結果を第2表に示す。 本実施例では、アラーム発信のない時はパージ
ガス中の酸素ガス濃度は10〜15%、1次アラーム
発信時は25〜35%、2次アラーム発信時は45〜55
%、3次アラーム発信時は55〜65%、パージガス
量は約200〜300Nm3/Hが好適である。
[Table] However, in reality, it is also necessary to consider the operational status of the converter at the time of judgment. For example, in the early stages of blowing, the gas temperature inside the furnace is low, so the light inside the furnace is biased toward yellowish colors, and the input of ore, the addition of auxiliary materials, the amount of silicon in the hot metal, etc. are also factors that cause the light inside the furnace to change, so information on these is also necessary. be. These are collectively illustrated as blowing conditions 28. Observing the furnace condition in this way, and using the information obtained, for example, if it is necessary to increase the amount of slag, it is preferable to charge oxidizing materials such as iron sand powder, sintered ore powder, scale powder, ferromanganese ore powder, etc. If it is necessary to suppress slag forming, it is preferable to charge a ring agent containing a carbon source such as coke powder or coal powder. Among these additives, in order to charge the ring agent which is particularly effective in suppressing slopping and cause a rapid reaction, the particle size should be 5 mm or less, preferably 3 mm.
It has been found that it is extremely effective to form the powder into a powder of less than mm in size, transport it in an air stream using a carrier gas, and blow it into the furnace through a blowing nozzle. FIG. 1 shows an example in which the above-mentioned furnace observation and additive injection devices are installed in conjunction with each other. That is, when the determination device 12 issues a tertiary alarm according to the determination in Table 1, for example, the blow control device 13 is activated and the stop valve 31 is opened to supply inert gas from the inert gas source 30. In addition to pressurizing the powder feeding tank 70, the flow rate regulator 53 of the carrier gas piping system 50 and the outlet valve 71 of the powder feeding tank are adjusted to supply the necessary amount of additives together with the carrier gas from the additive inlet 68. It is designed to be fed into a blow nozzle 69. Here, the carrier gas is a gas that does not react with the aforementioned additives at room temperature, does not easily react with the contents of the furnace when blown into the furnace, and does not affect the target steel composition. is preferable, and an inert gas such as CO 2 , Ar, or N 2 is used. Since the additive injection nozzle and the photodetection end are installed in the through hole, their tips in particular are exposed to high temperatures and are likely to be worn out, so they must be cooled. It is also necessary to prevent dust from adhering to the observation window attached to the tip of the light detection end. To meet these needs, a certain amount of inert gas is usually blown. This gas is hereinafter referred to as purge gas,
The purge gas is divided into three systems and introduced. The purge gas piping system 41 is equipped with normal piping equipment such as a stop valve, a pressure reducing valve, a flow rate adjustment device, a stop valve, etc., and is led to a purge gas inlet 66, passes through a gap 65 in the photodetection probe 62, and cools the photodetection probe. The purge gas is discharged into the furnace through a purge gas outlet 67 provided in the chip 64 while preventing dust from adhering to the observation window 63. The purge gas piping system 42 is the purge gas piping system 4
1, the purge gas passes from the purge gas inlet 692 of the additive injection probe 6 through the gap 691 between the additive injection nozzle 69 and its outer cylinder, cools the injection nozzle and the outer cylinder, and enters the furnace. released. Another purge gas piping system is a carrier gas piping system 50 in which a fixed amount of inert gas is allowed to flow through the additive injection nozzle even when the additive is not being blown into the system. Although the photodetection probe and the additive injection nozzle are protected by the purge gas described above, the cooling effect of this purge gas actually accelerates the clogging of the through holes. The cause of through-hole blockage is the adhesion of the contents of the furnace to the through-hole during blowing, or the hanging of slag, etc. during past blowing.According to the inventor's experience, even if the purge gas is Even when the discharge speed at the outlet of the through hole was set to about 22 m/sec, the effect of increasing the speed was observed, but clogging could not be prevented. As a result of various studies regarding purge gas, we found that mixing oxygen into purge gas is effective in preventing blockages.
The fact that the O 2 concentration in the mixed gas is preferably about 30 to 45% has already been disclosed in the above-mentioned patent by the applicant
−228930). To explain this using the examples shown in FIGS. 1 and 3, an O 2 gas piping system 55 is connected to the purge gas piping system 42,
The O 2 -containing gas is supplied to the additive injection probe from the purge gas inlet 692 and is configured to be ejected from the tip opening 693 . Therefore, the content of O 2 in the purge gas piping system 4
Since the flow rates of 1 and 50 can be kept constant, the flow ratio of the flow rate regulator 58 of the purge gas piping system 42 and the flow rate regulator 57 of the O 2 gas piping system is set by the ratio setting device 56, so that the amount of oxygen relative to the total purge gas amount is The amount added can be adjusted. In this example, the O 2 -containing purge gas is ejected from the tip opening 693 of the outermost cavity 691 of the additive injection probe and is combusted at the tip, which effectively prevents the adhesion of slag and additives. ,
There is no damage to the light guide or observation window. However, the addition of O 2 may damage the converter side wall bricks, and the
Since the gas, whose main component is CO, is combusted and its value is reduced, various studies were conducted to reduce the amount of O 2 added to the necessary minimum. The results showed that blockage of the through hole can be prevented with an oxygen concentration of 10 to 15% when slag formation is normal, and that the forming state progresses and the above-mentioned primary, secondary, and tertiary alarms are transmitted. It has become clear that in some cases, this can be prevented by changing the oxygen concentration to suit each case. The oxygen concentration that should be changed increases as the number of alarms increases, and its absolute value varies depending on the judgment criteria, the position and dimensions of the furnace volume and through holes, etc., so it is difficult to make a general rule, but here is an example. will be shown in Examples below. Based on the above knowledge, as shown in FIG. 1, the present method can be implemented by inputting the judgment of the judgment device 12 for detecting a slug forming situation to the ratio control device 14 and controlling the ratio setting device 56. In the above explanation, an example was shown in which an additive injection nozzle and a light detection end were installed in one through hole, but the invention is not limited to this. This method can also be implemented even if the detection end is provided as a separate device. Example A through hole with a diameter of approximately 15 cm is provided in the side wall of the converter at a height of approximately 4 m from the bottom of the 170 t/CH top-bottom blowing converter.
Using the apparatus shown in Fig. 3 and Fig. 3, the number of times the through hole was blocked with respect to the number of tests was determined by changing the amount of purge gas and the amount of added oxygen gas for each of the above-mentioned alarm categories. The results are shown in Table 2. In this example, the oxygen gas concentration in the purge gas is 10 to 15% when no alarm is issued, 25 to 35% when the primary alarm is issued, and 45 to 55% when the secondary alarm is issued.
%, 55 to 65% when the tertiary alarm is issued, and a purge gas amount of approximately 200 to 300 Nm 3 /H.

【表】【table】

【表】 発明の効果 以上詳細に述べたように、転炉操業上きわめて
有用な炉内観測および添加物吹込み用貫通孔を転
炉側壁に設けて操業するに際し、本法を適用すれ
ば、炉内の内張耐火物を損傷することなく、また
回収すべき炉内ガスの品質を劣化させることなく
貫通孔の閉塞を防止できる。したがつて転炉の操
業管理ならびに回収ガス原単位向上に大きく貢献
するものである。
[Table] Effects of the invention As described in detail above, if this method is applied when operating a converter with through-holes for inside observation and additive injection, which are extremely useful in the operation of the converter, provided in the side wall of the converter, Blockage of the through hole can be prevented without damaging the refractory lining inside the furnace and without degrading the quality of the furnace gas to be recovered. Therefore, it greatly contributes to the operational management of converters and to improving the recovery gas consumption rate.

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

第1図は、本法の全容を示す説明図、第2図は
光検出装置のブロツク図、第3図は添加物吹込プ
ローブの一例を示す図である。 6……添加物吹込プローブ、9……コネクタ、
10……光電変換素子、11……演算装置、12
……判定装置、13……吹込制御装置、14……
比率制御装置、21……波長別分別装置、22…
…2値化回路、23……面積演算装置、24……
2値化回路、25……高域透過フイルター、26
……正値化回路、27……2値化回路、28……
吹錬条件、30……不活性ガス源、31……止
弁、41……パージガス配管系、42……パージ
ガス配管系、50……キヤリヤーガス配管系、5
1……止弁、52……減圧弁、53……流量調節
装置、54……止弁、55……O2ガス配管系、
56……比率設定器、57……流量調節弁、58
……流量調節弁、61……光検出端、62……光
検出プローブ、63……観測窓、64……チツ
プ、65……空隙、66……パージガス入口、6
7……パージガス出口、68……添加物入口、6
9……添加物吹込ノズル、691……空隙、69
2……パージガス入口、693……先端開口部、
70……給粉タンク、71……出口弁、72……
受入タンク。
FIG. 1 is an explanatory diagram showing the entire process of this method, FIG. 2 is a block diagram of a photodetecting device, and FIG. 3 is a diagram showing an example of an additive injection probe. 6...Additive injection probe, 9...Connector,
10...Photoelectric conversion element, 11...Arithmetic device, 12
...Determination device, 13...Blowing control device, 14...
Ratio control device, 21... Wavelength separation device, 22...
... Binarization circuit, 23 ... Area calculation device, 24 ...
Binarization circuit, 25... High-pass transmission filter, 26
... Positive value conversion circuit, 27 ... Binarization circuit, 28 ...
Blowing conditions, 30... Inert gas source, 31... Stop valve, 41... Purge gas piping system, 42... Purge gas piping system, 50... Carrier gas piping system, 5
1... Stop valve, 52... Pressure reducing valve, 53... Flow rate adjustment device, 54... Stop valve, 55... O 2 gas piping system,
56...Ratio setter, 57...Flow rate control valve, 58
...flow control valve, 61 ... light detection end, 62 ... light detection probe, 63 ... observation window, 64 ... chip, 65 ... gap, 66 ... purge gas inlet, 6
7...Purge gas outlet, 68...Additive inlet, 6
9...Additive injection nozzle, 691...Void, 69
2...Purge gas inlet, 693...Tip opening,
70...Powder feeding tank, 71...Outlet valve, 72...
receiving tank.

Claims (1)

【特許請求の範囲】[Claims] 1 転炉側壁に設けられた添加物吹込みおよび炉
内観測用の貫通孔閉塞防止方法において、該貫通
孔に装置された添加物吹込プローブ、および光検
出端に酸素ガスを含むパージガス吹込装置を付設
し、前記光検出端によるスラグフオーミング検出
状況に応じて、前記パージガス中の酸素濃度を変
更し、前記貫通孔の閉塞防止を行うことを特徴と
する転炉側壁貫通孔の閉塞防止方法。
1. A method for preventing blockage of a through hole for injecting additives and observing inside the furnace provided on the side wall of a converter, which includes an additive injecting probe installed in the through hole and a purge gas injecting device containing oxygen gas at the photodetection end. A method for preventing blockage of a converter side wall through-hole, the method further comprising: changing the oxygen concentration in the purge gas depending on the state of slag forming detected by the light detection end to prevent the through-hole from clogging.
JP16431784A 1984-08-07 1984-08-07 Method for preventing clogging of through-hole of converter side wall Granted JPS6144117A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16431784A JPS6144117A (en) 1984-08-07 1984-08-07 Method for preventing clogging of through-hole of converter side wall

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16431784A JPS6144117A (en) 1984-08-07 1984-08-07 Method for preventing clogging of through-hole of converter side wall

Publications (2)

Publication Number Publication Date
JPS6144117A JPS6144117A (en) 1986-03-03
JPS6224488B2 true JPS6224488B2 (en) 1987-05-28

Family

ID=15790850

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16431784A Granted JPS6144117A (en) 1984-08-07 1984-08-07 Method for preventing clogging of through-hole of converter side wall

Country Status (1)

Country Link
JP (1) JPS6144117A (en)

Also Published As

Publication number Publication date
JPS6144117A (en) 1986-03-03

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