JPH01180915A - Dephosphorizing and molten slag separating method at tapping from converter - Google Patents

Dephosphorizing and molten slag separating method at tapping from converter

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Publication number
JPH01180915A
JPH01180915A JP556888A JP556888A JPH01180915A JP H01180915 A JPH01180915 A JP H01180915A JP 556888 A JP556888 A JP 556888A JP 556888 A JP556888 A JP 556888A JP H01180915 A JPH01180915 A JP H01180915A
Authority
JP
Japan
Prior art keywords
molten steel
converter
slag
tapping
ladle
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
Application number
JP556888A
Other languages
Japanese (ja)
Inventor
Shinichi Maeda
眞一 前田
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP556888A priority Critical patent/JPH01180915A/en
Publication of JPH01180915A publication Critical patent/JPH01180915A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To easily dephosphorize a molten steel and to prevent intrusion of molten slag into the molten steel in a ladle during tapping by blowing a dephosphorizing agent by an inert gas from the outside circumferential part of a tap hole into a converter at the time of discharging the molten steel from the converter into the ladle. CONSTITUTION:A hole 7 for discharging the molten steel 3 and a hole 8 for blowing the dephosphorizing agent are provided on the tap hole 2 of the converter. The molten steel 3 is discharged from the molten steel outflow hole 7 of the tap hole 2 into the ladle 5 by tilting the converter 1a and the powdery dephosphorizing agent is simultaneously blown by the inert gas such as N2 or Ar as a carrier gas from the blowing hole 8 into the molten steel 3 into the converter. The molten steel 3 in the converter is dephosphorized by such blowing of the dephosphorizing agent and the molten steel 21 in the upper part of the tap hole 2 is built up by the blowing of the carrier gas, by which the intrusion of the molten slag 4 into the molten steel 3 and the eventual intrusion into the ladle 5 are prevented even just before the end of the tapping. Rephosphorization of the molten steel from the molten slag in the ladle 5 is prevented and the low phosphorus content steel is easily obtd.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、転炉からの出鋼過程において、転炉内での脱
燐を更に補強的に行なうと共に、併せて脱燐処理後の分
離溶鋼中への溶滓の混入を可及的に防止する方法に関す
るものである。
[Detailed Description of the Invention] [Industrial Field of Application] The present invention is directed to further reinforcing dephosphorization in the converter during the process of tapping steel from the converter, and also to perform separation after the dephosphorization treatment. This invention relates to a method of preventing molten slag from entering molten steel as much as possible.

[従来の技術] 溶銑中には燐や硫黄等の不純物が多量に含まれているが
、これらは脱燐や脱硫に代表される精錬反応によって除
去されたり、或は組成コントロールのなされた溶滓(以
下スラグと呼ぶこともある)を生成させて適正な含有量
となる様に調、整されている。いずれにせよこの様な精
錬並びに成分調整(以下精錬で代表する)のなされた後
の溶銑は取鍋等に移し替えられてその後の処理に付され
る。
[Prior art] Hot metal contains a large amount of impurities such as phosphorus and sulfur, but these can be removed through refining reactions such as dephosphorization and desulfurization, or slags with controlled composition can be removed. (hereinafter sometimes referred to as slag) is generated and adjusted to have an appropriate content. In any case, the hot metal after such refining and component adjustment (hereinafter referred to as refining) is transferred to a ladle or the like and subjected to subsequent treatment.

そして最近の脱燐処理は、溶銑を転炉に穆し替える前の
段階で行なうという所謂溶銑予備処理によって行なわれ
ており、転炉ては専ら脱炭と昇温を行っているのである
が、転炉における吹錬時間の40%を占める出鋼時間を
有効に活用するという観点から、近年転炉出鋼時の転炉
内における脱燐方法か報告されるに至フている(「鉄と
鋼J86−31033参照)。この技術は出鋼中の転炉
4口からインジェクションランスを装入し、該ランスを
介して脱燐剤を吹き込み、これにょって脱燐効果を高め
ると共に出鋼時における復燐現象を抑制しようとするも
のである。
Recently, dephosphorization has been carried out by so-called hot metal pretreatment, which is carried out before the hot metal is sifted into the converter, and the converter mainly performs decarburization and temperature raising. From the perspective of making effective use of the tapping time, which accounts for 40% of the blowing time in the converter, in recent years there have been reports on methods for dephosphorization in the converter during tapping. (Refer to Steel J86-31033).In this technology, injection lances are inserted into the four ports of the converter during tapping, and a dephosphorizing agent is injected through the lances, thereby increasing the dephosphorizing effect and reducing the The aim is to suppress the rephosphorization phenomenon.

しかしなから当該技術は出鋼開始直後にランスを炉口か
ら転炉内に装入して脱燐処理を行ない、出鋼終了前に該
ランスを抜き取るという方法であるのて、その操作か繁
雑となり迅速性に欠けるという問題かあった。
However, this technique involves inserting a lance into the converter through the furnace opening immediately after the start of steel tapping to perform dephosphorization treatment, and then removing the lance before the end of steel tapping, which makes the operation complicated. There was a problem with the lack of speed.

一方精錬(吹錬)終了時にはスラグは溶鋼を覆う状態で
浮遊しており、精錬後のスラグは既に無用の物質であり
、以後の工程を考慮すればむしろ極めて有害な物質であ
るから、精錬後に溶鋼とスラグを分離することは極めて
重要な作業である。
On the other hand, at the end of refining (blowing), slag is floating covering the molten steel, and the slag after refining is already a useless substance, and if you consider the subsequent process, it is actually an extremely harmful substance, so after refining, Separating molten steel and slag is an extremely important task.

即ちスラグの分離か不十分て取鍋の中の溶鋼中にスラグ
が混入すると、精錬過程でスラグ中に分離除去されてい
た不純物か脱酸剤による還元作用等を受けて溶鋼中に復
帰(復燐、復硫等)するという問題があり、例えはギル
ド鋼における復燐現象は鋼の品質に重大な影響を与える
。又溶鋼を取鍋等に取出した後の工程で例えは脱酸等の
溶鋼処理を行なうには溶鋼表面を還元性:囲気に保つ必
要かあって、この様な要求からしても酸化性であるスラ
グを溶鋼中に混入させることは決して好ましいことては
ない。しかしながら溶鋼及びスラグは何れも高温である
為流動性か高く、溶鋼取出時に両者を完全に分離するこ
とは極めて困難なこととされている。
In other words, if slag is mixed into the molten steel in the ladle due to insufficient slag separation, impurities that were separated and removed from the slag during the refining process may return to the molten steel due to the reducing action of the deoxidizing agent. For example, the phenomenon of rephosphorization in guild steel has a serious effect on the quality of the steel. In addition, in the process after molten steel is taken out into a ladle, etc., in order to perform molten steel treatment such as deoxidation, it is necessary to maintain the molten steel surface in a reducing atmosphere. It is never desirable to mix some slag into molten steel. However, both molten steel and slag have high fluidity due to their high temperatures, and it is extremely difficult to completely separate the two when taking out the molten steel.

第2図及び第3図は従来の溶鋼取出し作業状態を示す概
略説明図てあり、図中1は転炉、2は溶鋼排出口、3は
溶鋼14はスラグ、5は取鍋を夫々示している。まず第
2図において、転炉1の底部側には精錬された溶鋼3が
あって、その溶鋼3の表面上にはこれを被覆する様にス
ラグ4が浮遊している。そして溶鋼3の取出しに際して
は、第2図の状態から転炉傾動装置(図示せず)によっ
て転炉1が傾動されて第3図に示した状態とされ、下層
の溶鋼3は溶鋼排出口2を通って流出され、取鍋5等に
移し替えられる。尚出鋼に先立って転炉を反対方向に傾
動させ、注き口10からスラグ4のみを排出させ、しか
る後第3図に示す如く反転させて溶鋼を取出すことは古
くより行なわれているか、この場合においても最初の傾
動でスラグ4を完全に排出てきる訳ではないのて、量の
多少はあるか第3図において溶鋼3の上にスラグ4か浮
上している状況は同じである。
Figures 2 and 3 are schematic explanatory diagrams showing the conventional molten steel extraction work state, and in the figures, 1 indicates a converter, 2 indicates a molten steel discharge port, 3 indicates molten steel 14, slag, and 5 indicates a ladle, respectively. There is. First, in FIG. 2, there is refined molten steel 3 at the bottom side of the converter 1, and slag 4 is floating on the surface of the molten steel 3 so as to cover it. When taking out the molten steel 3, the converter 1 is tilted from the state shown in FIG. 2 by a converter tilting device (not shown) to the state shown in FIG. It flows out through a ladle 5 and is transferred to a ladle 5 or the like. It has been practiced for a long time to tilt the converter in the opposite direction prior to tapping the steel, to discharge only the slag 4 from the spout 10, and then turn it around as shown in Fig. 3 to take out the molten steel. Even in this case, since the slag 4 is not completely discharged by the first tilting, the situation is the same as that of the slag 4 floating on top of the molten steel 3 in some amount in FIG. 3.

第2図及び第3図に示した様な溶鋼の取出し作業は、換
言ずれば溶鋼3とスラグ4の分離作業とも言える。その
目的を達成する為には溶W43が流出し終った時点若し
くはスラグ4の流出開始時点を確実に把握して出鋼口2
を塞ぐ方法、或は転炉1を第2図の如く立て起こし、続
いて流出してくるスラグ4が取鍋5内に混入するのを防
止する方法等が知られているが、後者の方法はスラグ混
入防止の確実性や作業の安全性といった観点から見て問
題かある。
In other words, the work of removing molten steel as shown in FIGS. 2 and 3 can be said to be the work of separating molten steel 3 and slag 4. In order to achieve this purpose, it is necessary to accurately grasp the point at which the molten W43 has finished flowing out or the point at which the slag 4 has started flowing out, and then
There are two known methods: one is to block the converter 1, as shown in Figure 2, and the other is to prevent the slag 4 that flows out from entering the ladle 5, but the latter method However, there are problems from the viewpoint of ensuring the prevention of slag contamination and work safety.

一方前者の様な方法としては、従来からスライディング
ノズル方式、スラグホール方式、投射機方式2工アージ
エツト方式、サイフオン方式、ストッパ一方式等の各種
のスラグカット方法か知られており、これらの方法のほ
とんどはスラグを機械的に遮断してスラグの取鍋内への
混入を防ごうとするものである。
On the other hand, as for the former method, various slag cutting methods have been known, such as the sliding nozzle method, slag hole method, projector method, two-piece arget method, siphon method, and one-stopper method. Most of the methods attempt to prevent slag from entering the ladle by mechanically blocking the slag.

しかしながらこれらの従来方法ては、スラグの取鍋への
混入量を成る程度は減少できるものの十分と言える程で
はなく、スラグ混入量を更に少なくすることか望まれて
いる。又取鍋内の溶鋼中に多量のスラグが混入してしま
った場合には、これらのスラグをスラグトラッカー等を
用いて除去する作業が必要となる。従ってこれらの設備
及びその保守作業か必要なことは勿論のこと、スラグの
混入量か多ければ多い程スラグ除去作業が繁雑となるは
かりでなく、除去作業時間か長くなることによる溶鋼の
温度低下(熱エネルギーの損失)、スラグトラッカー等
による溶鋼の共流用による鉄歩留りの低下、或は取鍋耐
大物の溶損という弊害等も生じる。
However, although these conventional methods can reduce the amount of slag mixed into the ladle, it is not sufficient, and it is desired to further reduce the amount of slag mixed into the ladle. Furthermore, if a large amount of slag gets mixed into the molten steel in the ladle, it is necessary to remove the slag using a slag tracker or the like. Therefore, it goes without saying that these facilities and their maintenance work are necessary, and the greater the amount of slag mixed in, the more complicated the slag removal work. Loss of thermal energy), reduction in iron yield due to co-diversion of molten steel by a slag tracker, etc., or melting damage to large ladle-resistant materials, etc., also occur.

[発明が解決しようとする課題] 本発明は上述した様な転炉出鋼時における技術的課題、
即ち脱燐処理作業が繁雑であること及び溶鋼・溶滓分離
が極めて困難である等という問題を解決する為になされ
たものであって、その目的とするところは、上記趣旨か
ら明らかな様に転炉での出鋼過程における転炉内での脱
燐を迅速に行なうと共に、併せて溶鋼と溶滓の分離を確
実に達成てきる方法を提供する点にある。
[Problems to be solved by the invention] The present invention solves the above-mentioned technical problems at the time of steel tapping in a converter,
In other words, this was done to solve the problems that dephosphorization processing is complicated and separation of molten steel and slag is extremely difficult, and as is clear from the above purpose, The object of the present invention is to provide a method that can rapidly dephosphorize in a converter during the steel tapping process in the converter, and also reliably separate molten steel and slag.

[課題を解決する為の手段] 上記目的を達成し得た本発明とは、溶鋼上に溶滓か存在
している転炉の溶鋼排出口から、溶鋼を排出して溶鋼と
溶滓の分離を行なうに当たり、前記溶鋼排出口には溶鋼
排出孔及び脱燐剤・キャリアカス混合物吹込孔を有する
脱燐剤供給部材を取付け、出鋼中は前記脱燐剤供給部材
を介して脱燐剤をキャリアガスによって供給し、出鋼完
了直前時期はキャリアガスのみを供給し、溶滓の排出を
防止しつつ溶鋼を排出することによって脱燐並びに溶鋼
・溶滓分離を行なう点に要旨を有する転炉出鋼時の脱燐
及び溶滓分離方法である。
[Means for Solving the Problems] The present invention that achieves the above object is a method of separating molten steel and slag by discharging molten steel from the molten steel discharge port of a converter where slag is present on the molten steel. In doing this, a dephosphorizing agent supply member having a molten steel discharge hole and a dephosphorizing agent/carrier cass mixture injection hole is attached to the molten steel discharge port, and during tapping, the dephosphorizing agent is supplied through the dephosphorizing agent supply member. A converter that dephosphorizes and separates molten steel and slag by supplying carrier gas and only supplying carrier gas immediately before the completion of tapping, and discharging molten steel while preventing the discharge of slag. This is a method for dephosphorization and slag separation during tapping.

[作用] 本発明の作用を図面を参照しつつ説明する。[Effect] The operation of the present invention will be explained with reference to the drawings.

第1図は本発明方法を実施する為に構成される転炉の概
略説明図てあり、その基本的な構成は第3図に示した従
来技術と類似し、対応する部分には同一の参照符号を付
すことによって重複説明を避ける。尚第1図に示した転
炉1aの状態は出鋼時を示しており、この状態に至るま
で及び転炉出鋼時の基本的動作は第2図及び第3図に関
連して既に述べた通りである。
FIG. 1 is a schematic explanatory diagram of a converter configured to carry out the method of the present invention, and its basic configuration is similar to that of the prior art shown in FIG. By adding symbols, duplicate explanations can be avoided. The state of the converter 1a shown in Fig. 1 shows the state of steel tapping, and the basic operations up to this state and during the tapping of the converter have already been described in connection with Figs. 2 and 3. That's right.

転炉1aにおいては、その溶鋼排出口2に大略筒状の脱
燐剤供給部材6が取付けられており、該脱燐剤供給部材
6には第4図(拡大断面図)に示す様に溶鋼排出孔7及
び脱燐剤・キャリアガス混合物吹込孔8(以下単に吹込
孔と呼ぶ)が形成されている。そして出鋼中は溶鋼排出
孔7を介して溶@3が取鍋5内に排出されると共に、吹
込孔8を介して脱燐剤がキャリアガスによって転炉la
内の溶鋼3に供給される。又出鋼完了直前時期即ち脱燐
剤を供給し終ってから出鋼が完了するまでにおいては、
前記吹込孔8を介してキャリアカスのみが引続き供給さ
れる。尚脱燐剤・キャリアガス混合物又はキャリアガス
単独が供給される機構は例えは第1図にも示した様に、
圧力供給ライン11、論理制御器(PLC)12.脱燐
剤貯留タンク13.キャリアガス供給ライン14.制御
器(RC)15.及び電磁弁V、、V2を設はルコとに
よって、その流量か調整されっつ吹込孔8に連通するラ
イン20を介して供給される。又このとき用いられるキ
ャリアガスとしては、Ar。
In the converter 1a, a roughly cylindrical dephosphorizing agent supply member 6 is attached to the molten steel discharge port 2, and the molten steel is supplied to the dephosphorizing agent supplying member 6 as shown in FIG. 4 (enlarged sectional view). A discharge hole 7 and a dephosphorizing agent/carrier gas mixture blowing hole 8 (hereinafter simply referred to as a blowing hole) are formed. During tapping, the molten @3 is discharged into the ladle 5 through the molten steel discharge hole 7, and the dephosphorizing agent is introduced into the converter la by the carrier gas through the blowing hole 8.
It is supplied to the molten steel 3 inside. In addition, in the period immediately before the completion of steel tapping, that is, after the dephosphorization agent has been supplied and until the steel tapping is completed,
Only carrier waste is subsequently supplied via the blowing hole 8. The mechanism by which the dephosphorizing agent/carrier gas mixture or the carrier gas alone is supplied is, for example, as shown in Figure 1.
Pressure supply line 11, logic controller (PLC) 12. Dephosphorizing agent storage tank 13. Carrier gas supply line 14. Controller (RC)15. The flow rate is regulated by the solenoid valves V, , V2 and supplied via a line 20 communicating with the blow hole 8. Further, the carrier gas used at this time is Ar.

N2等の不活性カスである。It is inert scum such as N2.

この様に脱燐剤・キャリアガス混合物又はキャリアカス
単独を脱燐剤供給部材6を介して供給することによって
、転炉出鋼中において転炉内における脱燐剤供給部材6
付近の溶鋼3にはバブリング現象か生し、スラグ4を押
しのける様にして裸湯21が露出するので、出鋼中は勿
論のこと出鋼終了まぎわ(溶鋼が少なくなった時)にお
いてもスラグが取鍋内へ混入することが最小限となる。
By supplying the dephosphorizing agent/carrier gas mixture or the carrier gas alone through the dephosphorizing agent supplying member 6 in this way, the dephosphorizing agent supplying member 6 in the converter during steel tapping from the converter.
A bubbling phenomenon occurs in the molten steel 3 in the vicinity, pushing away the slag 4 and exposing the bare hot water 21, so that the slag is removed not only during tapping but also near the end of tapping (when the molten steel is low). Contamination into the ladle is minimized.

そればかりか脱燐剤を供給する構成も従来技術で述べた
様なランス等を設けない簡単な構成であるので、出鋼時
における脱燐処理も迅速に達成される。尚最終的(出鋼
終了時)には前述した様なスラグカット方法を適用し、
溶鋼に引続いて流出してくるスラグを遮断する必要があ
るが、本発明の場合には少なくとも出鋼終了直前までは
スラグ混入か確実に防がれ、又出鋼終了時のスラグの混
入が多少あるとしても従来方法に比へてスラグ混入量を
大幅に低減することができる。
Moreover, since the structure for supplying the dephosphorizing agent is simple and does not require a lance or the like as described in the prior art, the dephosphorization process at the time of tapping can be accomplished quickly. In addition, in the final stage (at the end of steel tapping), the slag cutting method as described above is applied,
It is necessary to block the slag that flows out following the molten steel, but in the case of the present invention, it is possible to reliably prevent slag from entering at least until immediately before the end of tapping, and also to prevent slag from entering at the end of tapping. Even if there is some amount, the amount of slag mixed in can be significantly reduced compared to the conventional method.

[実施例] 本発明者らは、第1図に示した転炉1aを用いて脱燐及
びスラグ分離を行ない各種の項目(後記第1表参照)に
ついて調査し、本発明方法の効果について確認した。尚
比較の為第2図及び第3図に関連して述べた様な従来法
についても同様の調査を行なった。
[Example] The present inventors performed dephosphorization and slag separation using the converter 1a shown in Fig. 1, investigated various items (see Table 1 below), and confirmed the effects of the method of the present invention. did. For comparison, a similar investigation was also conducted regarding the conventional method described in connection with FIGS. 2 and 3.

その結果を第1表に示すが、この結果から明らかな様に
、本発明方法によれば出鋼工程中に脱燐の効果が得られ
ると共に、取鍋内への混入スラグ量を確実に低減できる
ことが理解される。
The results are shown in Table 1, and as is clear from the results, the method of the present invention not only achieves the effect of dephosphorization during the steel tapping process, but also reliably reduces the amount of slag mixed into the ladle. Understand what is possible.

第   1   表 [発明の効果] 以上述へた如く本発明によれは、既述の構成に従って操
業を行なうことによって、出鋼中の脱燐か従来よりも容
易となり、しかも溶鋼と溶滓の分離か確実に達成されて
取鍋内への流出スラグ量を低減することかできるので、
鉄歩留りの向上、復燐防止、取鍋寿命の延長等の多くの
効果か得られた。
Table 1 [Effects of the Invention] As described above, according to the present invention, by operating according to the configuration described above, dephosphorization during tapping is easier than before, and separation of molten steel and slag is possible. This can be achieved reliably and reduce the amount of slag flowing into the ladle.
Many effects were obtained, including improved iron yield, prevention of rephosphorization, and extended ladle life.

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

第1図は本発明を実施する為に構成される転炉の概略説
明図、第2図及び第3図は従来の溶鋼取出し作業を示す
概略説明図、第4図は脱燐剤供給部材6の拡大断面図で
ある。 1.1a・・・転炉     2・・・溶鋼排出口3・
・・溶鋼      4・・・スラグ5・・・取鍋  
    6・・・脱燐剤供給部材7・・・溶鋼排出孔
FIG. 1 is a schematic explanatory diagram of a converter configured to carry out the present invention, FIGS. 2 and 3 are schematic explanatory diagrams showing conventional molten steel extraction work, and FIG. 4 is a dephosphorizing agent supply member 6. FIG. 1.1a... Converter 2... Molten steel outlet 3.
... Molten steel 4 ... Slag 5 ... Ladle
6... Dephosphorizing agent supply member 7... Molten steel discharge hole

Claims (1)

【特許請求の範囲】[Claims] 溶鋼上に溶滓が存在している転炉の溶鋼排出口から、溶
鋼を排出して溶鋼と溶滓の分離を行なうに当たり、前記
溶鋼排出口には溶鋼排出孔及び脱燐剤・キャリアガス混
合物吹込孔を有する脱燐剤供給部材を取付け、出鋼中は
前記脱燐剤供給部材を介して脱燐剤をキャリアガスによ
って供給し、出鋼完了直前時期はキャリアガスのみを供
給し、溶滓の排出を防止しつつ溶鋼を排出することによ
って脱燐並びに溶鋼・溶滓分離を行なうことを特徴とす
る転炉出鋼時の脱燐及び溶滓分離方法。
When discharging molten steel from the molten steel discharge port of the converter where molten steel exists on the molten steel and separating the molten steel and slag, the molten steel discharge port is equipped with a molten steel discharge hole and a dephosphorizing agent/carrier gas mixture. A dephosphorizing agent supply member having a blowing hole is installed, and during tapping, the dephosphorizing agent is supplied with a carrier gas through the dephosphorizing agent supplying member, and just before the completion of tapping, only the carrier gas is supplied, and the slag is A method for dephosphorization and separation of molten slag during tapping from a converter, characterized in that dephosphorization and separation of molten steel and slag are performed by discharging molten steel while preventing the discharge of molten steel.
JP556888A 1988-01-13 1988-01-13 Dephosphorizing and molten slag separating method at tapping from converter Pending JPH01180915A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP556888A JPH01180915A (en) 1988-01-13 1988-01-13 Dephosphorizing and molten slag separating method at tapping from converter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP556888A JPH01180915A (en) 1988-01-13 1988-01-13 Dephosphorizing and molten slag separating method at tapping from converter

Publications (1)

Publication Number Publication Date
JPH01180915A true JPH01180915A (en) 1989-07-18

Family

ID=11614816

Family Applications (1)

Application Number Title Priority Date Filing Date
JP556888A Pending JPH01180915A (en) 1988-01-13 1988-01-13 Dephosphorizing and molten slag separating method at tapping from converter

Country Status (1)

Country Link
JP (1) JPH01180915A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109880965A (en) * 2019-04-24 2019-06-14 东北大学 The device and method that a kind of converter taphole top powder dephosphorization realizes pushing off the slag simultaneously
CN113832286A (en) * 2021-09-17 2021-12-24 东北大学 Device and method for powder injection dephosphorization and slag blocking at converter steel tapping hole and composite dephosphorization agent

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109880965A (en) * 2019-04-24 2019-06-14 东北大学 The device and method that a kind of converter taphole top powder dephosphorization realizes pushing off the slag simultaneously
CN113832286A (en) * 2021-09-17 2021-12-24 东北大学 Device and method for powder injection dephosphorization and slag blocking at converter steel tapping hole and composite dephosphorization agent

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