JPH01275715A - Vacuum degassing treatment of molten steel by rh type degassing device - Google Patents
Vacuum degassing treatment of molten steel by rh type degassing deviceInfo
- Publication number
- JPH01275715A JPH01275715A JP10249788A JP10249788A JPH01275715A JP H01275715 A JPH01275715 A JP H01275715A JP 10249788 A JP10249788 A JP 10249788A JP 10249788 A JP10249788 A JP 10249788A JP H01275715 A JPH01275715 A JP H01275715A
- Authority
- JP
- Japan
- Prior art keywords
- molten steel
- gas
- pipe
- downcomer
- degassing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 45
- 239000010959 steel Substances 0.000 title claims abstract description 45
- 238000007872 degassing Methods 0.000 title claims abstract description 24
- 238000009849 vacuum degassing Methods 0.000 title claims description 12
- 239000007789 gas Substances 0.000 claims abstract description 43
- 239000002893 slag Substances 0.000 claims abstract description 24
- 238000007664 blowing Methods 0.000 claims abstract description 15
- 239000011261 inert gas Substances 0.000 claims abstract description 14
- 238000000034 method Methods 0.000 claims abstract description 9
- 230000001174 ascending effect Effects 0.000 claims description 4
- 238000007654 immersion Methods 0.000 abstract description 13
- 230000003749 cleanliness Effects 0.000 abstract description 3
- 239000011819 refractory material Substances 0.000 abstract description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 229910052786 argon Inorganic materials 0.000 description 6
- 230000000630 rising effect Effects 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treatment Of Steel In Its Molten State (AREA)
Abstract
Description
〈産業上の利用分野〉
本発明は溶鋼の真空脱ガス処理方法、特にRH式脱ガス
装置の上昇側浸漬管や下降側浸漬管の周辺部に取鍋内の
スラグ巻込みを防止することを目的としたRH式脱ガス
装置による溶鋼の真空脱ガス処理方法に関するものであ
る。
〈従来の技術〉
RH式脱ガス装置は第2図に示すように脱ガス槽1の下
端に設けた上昇側浸漬管10(以下上昇管と称す)およ
び下降側浸漬管11(以下下降管と称す)を取鍋2内の
溶鋼12に浸漬し、脱ガス槽1内を減圧することにより
溶f@12を吸い上げ、ガス吹込み系統3aから供給さ
れる不活性ガスは上昇管10に設けたガス吹込口3より
吹込まれる。
上昇管10内に吹込まれた不活性ガスのガス浮上刃を利
用して溶w412を上昇させて脱ガス槽1に導き、ガス
供給口を備えていない下降管11より下降させて溶鋼1
2を循環して脱ガス処理を行うものである。
したがって、単位時間当たりに脱ガス槽1内を通過する
溶鋼量(以下環流量と称す)が脱ガス処理に要する時間
すなわち脱ガス処理能力に与える影響が大きいため、溶
鋼の真空脱ガス処理二一ズの増大に伴い溶鋼環流量を増
加して脱ガス反応速度を上昇することが図られて来た。
従来から環流量の増大には環流用吹込みガス流量の増大
および浸漬管の内径の拡大が有効であるとされている0
例えば特開昭51−6103号公報に開示されているよ
うに上昇管下端部の水平断面中心近傍に設けたガス吹込
口より上昇管内鉛直方向に不活性ガスを吹込んで吹込ガ
ス量を増加させ環流量の増大を達成している。
〈発明が解決しようとする課題〉
しかしながら環流量の増大に伴って上昇管10への溶鋼
12の上昇あるいは下降管からの溶鋼12の下降による
流速が必然的に増大し、取鍋2内のスラグ4が溶鋼12
内に巻込まれる現象が観察され、特に上昇管10側に比
較して下降管11側の外周近傍に白抜矢印で示すような
溶鋼12の下降流が生じこの下降流にスラグ4が吸い込
まれ易い。
このようなスラグ巻込み防止策として従来、下降管11
の直径を大きくして下降する溶鋼流速の減少を図る手段
や下降管11の長さを増加して溶鋼12内への浸漬深さ
h(第2図参照)を増加してスラグ4の巻込みを防止す
る手段が採られて来たがいずれも下降管11の耐火物コ
ストが増加し経済的でないという難点があった。
本発明は上記従来の問題点を解消し環流量の増大に伴っ
て溶鋼流速が大きくなっても取鍋内スラグの巻込みが防
止できるようにしたRH式肌脱ガス装置よる溶鋼の真空
脱ガス処理方法を提供することを目的とするものである
。
く課題を解決するための手段〉
本発明者は上昇管と下降管のうち特にスラグ巻込みの著
しい下降管からの溶鋼下降流による取鍋スラグ巻込み現
象について研究を重ねた。
第4図に水モデル実験による下降管11′近傍の流れの
様子を示している。下降管11′内を矢印方向に流下す
る水12′の流速が大きくなるとこれに伴い容器(図示
略)に収納した水12′の表面近傍に白抜矢印で示す流
れが生じて疑似スラグ4′の一部がこの流れに巻込まれ
下降管11’の外周に沿い下方に導かれることが判明し
た。
上記疑似スラグ4′の巻込みが水流の条件によって生じ
ること、すなわち下降管11′の外周に吸いよせられる
流れのときに生じ逆に下降管11′の外周から離れる流
れのときには生じないことを見出した。
そこで水モデル実験によって第3図に示すように下降管
11′の下部に外向きにガス吹出ロア′を設け、ガス供
給系統5a′から供給されるアルゴンガスを吹き出させ
アルゴンガスの上昇による浮力を利用して第4図に示す
ような下降管11′の外周近傍に生じる下向きの流れを
低減させるかあるいは第3図に示すように逆に上昇させ
ることができることをit認した。
上記のような一連の水モデル実験を重ねた結果、下降管
の外周側に不活性ガスを吹出すことにより下降管外周部
の負圧領域を解消し得るとの知見を得、本発明を達成す
るに至ったものである。
本発明は脱ガス槽の下端に上昇側浸漬管および下降側浸
漬管を備えたRH式肌脱ガス装置よる溶鋼の真空脱ガス
処理方法において、上記の上昇側浸漬管の下部外周およ
び下降側浸漬管の下部外周のいずれか一方または両方に
複数個のガス吹出口を円周方向に配列して外向きに設け
、上記ガス吹出口から不活性ガスを吹出すことによって
環流する溶鋼流に取鍋内溶鋼上のスラグ巻込みを防止し
つつ真空脱ガス処理することを特徴としたものである。
本発明の構成を第1図に基づいて下降管11側にガス吹
出口3を設けたものについて説明する。なお、図中上記
第2図のものと同じものは同一符号を付して説明のN畦
化を図ることにする。
第1図において下降管11の下部外周に複数個のガス吹
出ロアを円周方向に配列して外向きに設け、ガス供給系
統5および下降管11の耐火物中に埋設したガス通路6
を通してガス吹出ロアから不活性ガスを溶鋼12中に吹
出すようになっている。
〈作 用〉
本発明は前記の手段により下降管11の下部外周から外
向きに不活性ガスを吹出すので下降管ll内を流下する
溶鋼12の流速が大きくても下降管11の外周に吸い寄
せられて生じる下向き流れを不活性ガスの浮力を利用し
て阻止し、下降管11周辺の溶鋼流れを白抜矢印のごと
くむしろ上向きに変えるものであり、これによって取鍋
2内のスラグ4の巻込みを防止するのである。
なお、第1図では下降管11にだけガス吹出ロアを設け
るものについて説明したが、上昇管10側の溶鋼上昇に
伴う吸い寄せ流によってスラグ巻込みが生ずるときには
上界管10に同様にしてガス吹出ロアを設けるのが好ま
しい、また設備条件や操業条件によっては逆に上昇管1
0側にのみガス吹出ロアを設けることもできる。
〈実施例〉
以下に本発明の好適な一実施例を図面に基づいて説明す
る。
第1図に示すRH式肌脱ガス装置おいて、脱ガス槽1の
下端にそれぞれ内径550鴫φの上昇管10および下降
管11を取鍋2中の容量200 tonの溶鋼(化学成
分C: 0.04%、 Si : 0.01%、 Mn
: Q、20%。
A1: 0.040%)中に溶鋼12への浸漬深さ40
0mmとして浸漬したのち減圧して溶鋼12を脱ガス槽
1内に吸引した。
そして上昇管10に設けた環流用のガス吹込口3から1
500 f 7分のアルゴンガスを吹込んで溶鋼12を
環流させると共に下降管11に設けたスラグ巻込み防止
用のガス吹出ロアから2004!/分のアルゴンガスを
吹込みつつ真空脱ガス処理した。また比較のため同条件
で下降管11のスラグ巻込用のガス吹出ロアからの不活
性ガス量を零とした真空脱ガス処理を行ワた。
第5図は、上記の処理条件下で真空脱ガス処理したとき
のRHHガス処理時間と取鍋2中の溶鋼酸素<Industrial Field of Application> The present invention relates to a method for vacuum degassing treatment of molten steel, and particularly to a method for preventing slag from being entrained in a ladle around the ascending side immersion pipe and the descending side immersion pipe of an RH degassing device. The present invention relates to a method for vacuum degassing treatment of molten steel using an RH type degassing apparatus. <Prior art> As shown in FIG. 2, the RH type degassing device has a rising side immersion pipe 10 (hereinafter referred to as the rising pipe) and a descending side immersion pipe 11 (hereinafter referred to as the downcomer pipe) provided at the lower end of the degassing tank 1. ) immersed in the molten steel 12 in the ladle 2 and sucked up the molten steel 12 by reducing the pressure in the degassing tank 1, and the inert gas supplied from the gas injection system 3a was provided in the riser pipe 10. The gas is blown in from the gas blowing port 3. The molten w412 is raised using a gas flotation blade of inert gas blown into the riser pipe 10 and guided to the degassing tank 1, and then lowered through the downcomer pipe 11 which is not equipped with a gas supply port to remove the molten steel 1.
2 is circulated to perform degassing treatment. Therefore, the amount of molten steel that passes through the degassing tank 1 per unit time (hereinafter referred to as the recirculation flow rate) has a large effect on the time required for degassing treatment, that is, on the degassing treatment capacity. As the amount of gas increases, efforts have been made to increase the degassing reaction rate by increasing the flow rate of molten steel. It has been believed that increasing the flow rate of the recirculation gas and increasing the inner diameter of the immersion pipe are effective ways to increase the recirculation flow rate.
For example, as disclosed in Japanese Unexamined Patent Publication No. 51-6103, an inert gas is blown vertically into the riser pipe from a gas inlet provided near the center of the horizontal section at the lower end of the riser pipe to increase the amount of blown gas. An increase in flow rate has been achieved. <Problems to be Solved by the Invention> However, as the recirculation flow rate increases, the flow velocity due to the rise of the molten steel 12 into the riser pipe 10 or the fall of the molten steel 12 from the downfall pipe inevitably increases, and the slag in the ladle 2 increases. 4 is molten steel 12
In particular, a downward flow of molten steel 12 as shown by the white arrow occurs near the outer periphery on the downcomer pipe 11 side compared to the riser pipe 10 side, and the slag 4 is easily sucked into this downward flow. . Conventionally, as a measure to prevent such slag entrainment, the downcomer pipe 11
The diameter of the descending pipe 11 is increased to increase the immersion depth h (see Fig. 2) into the molten steel 12, thereby entraining the slag 4. Although measures have been taken to prevent this, all of them have the disadvantage that they increase the cost of the refractory material for the downcomer pipe 11 and are not economical. The present invention solves the above-mentioned conventional problems and is capable of vacuum degassing of molten steel using an RH type skin degassing device that prevents slag from being caught in the ladle even when the molten steel flow velocity increases with an increase in the recirculation flow rate. The purpose is to provide a processing method. Means for Solving the Problems> The present inventor has conducted extensive research on the ladle slag entrainment phenomenon caused by the downward flow of molten steel from the downcomer pipe, where slag entrainment is particularly significant among the riser pipe and the downcomer pipe. FIG. 4 shows the state of the flow near the downcomer pipe 11' in a water model experiment. When the flow velocity of the water 12' flowing down in the direction of the arrow in the downcomer pipe 11' increases, a flow shown by a white arrow is generated near the surface of the water 12' stored in a container (not shown), causing pseudo slag 4'. It was found that a portion of the water was caught in this flow and guided downward along the outer periphery of the downcomer pipe 11'. It was discovered that the entrainment of the pseudo slag 4' occurs depending on the conditions of the water flow, that is, it occurs when the flow is sucked up to the outer periphery of the downcomer pipe 11', but does not occur when the flow leaves the outer periphery of the downcomer pipe 11'. Ta. Therefore, in a water model experiment, as shown in FIG. 3, a gas blowing lower 'is provided outward at the bottom of the downcomer pipe 11', and the argon gas supplied from the gas supply system 5a' is blown out to reduce the buoyancy caused by the rise of the argon gas. It has been found that the downward flow generated near the outer periphery of the downcomer pipe 11' can be reduced as shown in FIG. 4, or can be made to rise as shown in FIG. 3. As a result of a series of water model experiments as described above, we found that the negative pressure region around the outer circumference of the downcomer pipe can be eliminated by blowing inert gas toward the outer circumference of the downcomer pipe, and the present invention was achieved. This is what I came to do. The present invention provides a method for vacuum degassing treatment of molten steel using an RH type skin degassing device equipped with an ascending side immersion pipe and a descending side immersion pipe at the lower end of the degassing tank. A plurality of gas outlets are arranged in the circumferential direction on one or both of the outer peripheries of the lower part of the pipe and are provided facing outward, and inert gas is blown out from the gas outlets to direct the circulating molten steel into the ladle. This method is characterized by performing vacuum degassing treatment while preventing slag entrainment on the internally molten steel. The structure of the present invention will be described based on FIG. 1 with a gas outlet 3 provided on the downcomer pipe 11 side. Components in the figure that are the same as those in FIG. 2 above are given the same reference numerals to facilitate explanation. In FIG. 1, a plurality of gas blowing lowers are arranged circumferentially on the outer periphery of the lower part of the downcomer pipe 11 and are provided facing outward, and a gas passage 6 is buried in the gas supply system 5 and the refractory material of the downcomer pipe 11.
Inert gas is blown into the molten steel 12 from the gas blowing lower through the gas blowing lower. <Function> The present invention blows inert gas outward from the lower outer periphery of the downcomer pipe 11 by the above-described means, so that even if the flow velocity of the molten steel 12 flowing down in the downcomer pipe 11 is high, it is attracted to the outer periphery of the downcomer pipe 11. The buoyancy of the inert gas is used to block the downward flow of molten steel around the downcomer pipe 11, rather than turning it upward as shown by the white arrow. This prevents crowding. In addition, in FIG. 1, a case in which a gas blowing lower is provided only in the descending pipe 11 has been explained, but when slag entrainment occurs due to the suction flow accompanying the rise of molten steel on the rising pipe 10 side, the gas blowing lower is provided in the upper pipe 10 in the same way. It is preferable to install a lower pipe, and depending on the equipment and operating conditions, it is preferable to install a lower pipe.
It is also possible to provide a gas blowing lower only on the 0 side. <Embodiment> A preferred embodiment of the present invention will be described below based on the drawings. In the RH type skin degassing apparatus shown in FIG. 1, a rising pipe 10 and a descending pipe 11 each having an inner diameter of 550 φ are placed at the lower end of a degassing tank 1, and a molten steel (chemical composition C: 0.04%, Si: 0.01%, Mn
: Q, 20%. A1: Immersion depth 40 in molten steel 12 (0.040%)
After being immersed at a depth of 0 mm, the pressure was reduced and the molten steel 12 was sucked into the degassing tank 1. Then, gas inlets 3 to 1 for circulation provided in the riser pipe 10
500 f 7 minutes of argon gas is blown in to circulate the molten steel 12 and from the gas blowing lower installed in the downcomer pipe 11 to prevent slag entrainment.2004! Vacuum degassing was performed while blowing argon gas at a rate of 1/2 min. For comparison, a vacuum degassing process was carried out under the same conditions with the amount of inert gas from the gas blowing lower for slag entrainment in the downcomer pipe 11 being zero. Figure 5 shows the RHH gas treatment time and the molten steel oxygen in ladle 2 when performing vacuum degassing treatment under the above treatment conditions.
〔0〕との
関係をプロットしたものである。
第5図から明らかなように、スラグ巻込防止用のアルゴ
ンガス量を零とした場合には溶鋼〔0]の減少速度は遅
(、また到達This is a plot of the relationship with [0]. As is clear from Figure 5, when the amount of argon gas to prevent slag entrainment is reduced to zero, the rate of decrease of molten steel [0] is slow (and
〔0〕の濃度が高い。
これは取鍋スラグの巻込みによる溶鋼の再酸化現象が生
じているためである。
これに対して、取鍋゛スラグ巻込み防止用のアルゴンガ
スを2001/分吹込んだ場合にはスラグ巻込みがない
ため脱酸速度は増加し、到達酸素濃度The concentration of [0] is high. This is because the molten steel is reoxidized due to the inclusion of ladle slag. On the other hand, when argon gas to prevent slag entrainment is blown into the ladle at 2001/min, there is no slag entrainment, so the deoxidation rate increases, and the oxygen concentration reached
〔0〕も減少して
いることが判る。
〈発明の効果〉
以上説明したように浸漬管の外部外周から外向きに不活
性ガスを吹込んで取鍋スラグを溶鋼中に巻込むのを阻止
することができるので、溶鋼の清浄度向上を目指す脱ガ
ス処理に有効であり、容易に高清浄度溶鋼を得ることが
出来る。It can be seen that [0] is also decreasing. <Effects of the Invention> As explained above, it is possible to prevent ladle slag from being drawn into molten steel by blowing inert gas outward from the outer periphery of the immersion tube, which aims to improve the cleanliness of molten steel. It is effective for degassing treatment and can easily obtain highly clean molten steel.
第1図は本発明の好適な一実施例を示す断面図、第2図
は従来例を示す断面図、第3図および第4図は水モデル
実験例を示す部分断面図、第5図は溶鋼中の酸素(0)
とRHH理時間の関係を示すグラフである。
l・・・脱ガス槽、 2・・・取 鍋、3・・
・環流用ガス吹出口、 4・・・取鍋スラグ、5・・
・ガス供給系統、 6・・・ガス通路、7・・・ス
ラグ巻込防止用ガス吹出口、10・・・上昇側浸漬管、
11・・・下降側浸漬管、12・・・溶 鋼。
特許出願人 川崎製鉄株式会社
第1図
第2図
第3図
第4図
第5図
RH処理時間FIG. 1 is a sectional view showing a preferred embodiment of the present invention, FIG. 2 is a sectional view showing a conventional example, FIGS. 3 and 4 are partial sectional views showing a water model experiment example, and FIG. Oxygen in molten steel (0)
It is a graph showing the relationship between RHH processing time and RHH processing time. l... degassing tank, 2... ladle, 3...
・Recirculation gas outlet, 4... Ladle slag, 5...
・Gas supply system, 6... Gas passage, 7... Gas outlet for preventing slag entrainment, 10... Rising side immersion pipe,
11... Descending side immersion pipe, 12... Molten steel. Patent applicant: Kawasaki Steel Corporation Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 RH processing time
Claims (1)
えたRH式脱ガス装置による溶鋼の真空脱ガス処理方法
において、上記の上昇側浸漬管の下部外周および下降側
浸漬管の下部外周のいずれか一方または両方に複数個の
ガス吹出口を円周方向に配列して外向きに設け、上記ガ
ス吹出口から不活性ガスを吹出すことによって環流する
溶鋼流に取鍋内溶鋼上のスラグ巻込みを防止しつつ真空
脱ガス処理することを特徴とするRH式脱ガス装置によ
る溶鋼の真空脱ガス処理方法。In a method for vacuum degassing treatment of molten steel using an RH type degassing device equipped with an ascending dip tube and a descending dip tube at the lower end of the degassing tank, the lower outer periphery of the ascending dip tube and the lower outer circumference of the descending dip tube are A plurality of gas outlets are arranged circumferentially and facing outward in one or both of the gas outlets, and by blowing out inert gas from the gas outlets, the circulating molten steel flow is exposed to the surface of the molten steel in the ladle. A method for vacuum degassing treatment of molten steel using an RH type degassing device, characterized in that vacuum degassing treatment is performed while preventing slag entrainment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10249788A JPH01275715A (en) | 1988-04-27 | 1988-04-27 | Vacuum degassing treatment of molten steel by rh type degassing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10249788A JPH01275715A (en) | 1988-04-27 | 1988-04-27 | Vacuum degassing treatment of molten steel by rh type degassing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01275715A true JPH01275715A (en) | 1989-11-06 |
Family
ID=14329050
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10249788A Pending JPH01275715A (en) | 1988-04-27 | 1988-04-27 | Vacuum degassing treatment of molten steel by rh type degassing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01275715A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0649526A (en) * | 1992-07-31 | 1994-02-22 | Kurosaki Refract Co Ltd | Immersion pipe for treating molten steel and method for preventing sticking to immersion pipe |
WO2011023337A1 (en) * | 2009-08-28 | 2011-03-03 | Sms Siemag Aktiengesellschaft | Device for degassing molten steel with an improved discharge nozzle |
-
1988
- 1988-04-27 JP JP10249788A patent/JPH01275715A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0649526A (en) * | 1992-07-31 | 1994-02-22 | Kurosaki Refract Co Ltd | Immersion pipe for treating molten steel and method for preventing sticking to immersion pipe |
WO2011023337A1 (en) * | 2009-08-28 | 2011-03-03 | Sms Siemag Aktiengesellschaft | Device for degassing molten steel with an improved discharge nozzle |
RU2473704C1 (en) * | 2009-08-28 | 2013-01-27 | Смс Зимаг Акциенгезелльшафт | Device for degassing steel melt furnished with perfected exhaust sleeve |
US9181602B2 (en) | 2009-08-28 | 2015-11-10 | Sms Group Gmbh | Device for degassing molten steel with an improved discharge nozzle |
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