JPH0456083B2 - - Google Patents

Info

Publication number
JPH0456083B2
JPH0456083B2 JP59132784A JP13278484A JPH0456083B2 JP H0456083 B2 JPH0456083 B2 JP H0456083B2 JP 59132784 A JP59132784 A JP 59132784A JP 13278484 A JP13278484 A JP 13278484A JP H0456083 B2 JPH0456083 B2 JP H0456083B2
Authority
JP
Japan
Prior art keywords
gas
blowing
amount
molten steel
decarburization
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 - Lifetime
Application number
JP59132784A
Other languages
Japanese (ja)
Other versions
JPS6112812A (en
Inventor
Minoru Ishikawa
Koji Ieda
Norimasa Mochizuki
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
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP13278484A priority Critical patent/JPS6112812A/en
Publication of JPS6112812A publication Critical patent/JPS6112812A/en
Publication of JPH0456083B2 publication Critical patent/JPH0456083B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/005Manufacture of stainless steel

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Steel In Its Molten State (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 この発明は、AOD炉、転炉等によりステンレ
ス鋼の精錬(脱炭)を行なう方法に関する。 従来技術とその問題点 AOD炉、転炉等によるステンレス鋼の精錬は、
酸素ガスとアルゴン等の不活性ガスを大気圧下で
鋼浴中に吹き込んで行なわれるが、底吹きAOD
法の場合、底吹き羽口を介してO2,Arガスを吹
き込むため吹き込み流量に限界があり、精錬時間
が長くかかる。また、底吹き羽口と上吹きランス
による上下吹きAOD法の場合、純酸素上吹き、
アルゴン、酸素ガス底吹きでは、精錬時間は短か
いが、Crの酸化損失が大きい。また、アルゴン、
酸素の混合ガス上吹き、アルゴン、酸素の混合ガ
ス底吹きでは、Cr酸化損失の問題は解消される
が、上吹き混合ガスの酸素ガスとアルゴンガスの
混合比制御範囲が狭く、高価なアルゴンガスを大
量に使用する必要がある。さらに、酸素ガスと不
活性ガスを一定割合で吹き込む精錬においては、
大量のガスを強く吹き込むと溶鋼中のCrが酸化
されて歩留りが悪化し、Crの酸化を防止するた
めに少ない量で弱く吹き込むと精錬に長時間かか
るという問題があつた。 発明の目的 この発明は、従来の前記問題点に鑑みなされた
もので、Crの酸化を防止して鋼への酸化歩留り
を上げるとともに、脱炭時間の短縮がはかられる
ステンレス鋼の脱炭方法を提案することを目的と
するものである。 発明の構成 すなわちこの発明は、酸素ガスと共に不活性ガ
スを大気圧下で鋼浴中に吹き込んでステンレス鋼
の脱炭を行なう方法において、上吹きランスをダ
ブルフロー型とし、中心孔を酸素ガスと不活性ガ
スの混合ガス用とし、中心孔周囲の側孔を酸素ガ
ス用とし、溶鋼中の炭素含有量に応じて、酸素ガ
ス量/不活性ガス量の値αを下記表の範囲に調整
して吹き込むことを特徴とするものである。
INDUSTRIAL APPLICATION FIELD This invention relates to a method for refining (decarburizing) stainless steel using an AOD furnace, a converter, or the like. Conventional technology and its problems Stainless steel refining using AOD furnace, converter, etc.
This is done by blowing oxygen gas and inert gas such as argon into the steel bath under atmospheric pressure, but bottom blowing AOD
In the case of this method, since O 2 and Ar gas are blown through the bottom blowing tuyere, there is a limit to the blowing flow rate and the refining time is long. In addition, in the case of the top-bottom blowing AOD method using bottom-blowing tuyeres and top-blowing lances, pure oxygen top-blowing,
With argon or oxygen gas bottom blowing, the refining time is short, but the oxidation loss of Cr is large. Also, argon,
Top blowing of a mixed gas of oxygen, bottom blowing of a mixed gas of argon and oxygen solves the problem of Cr oxidation loss, but the control range of the mixture ratio of oxygen gas and argon gas in the top blowing mixed gas is narrow, and expensive argon gas is used. need to be used in large quantities. Furthermore, in refining where oxygen gas and inert gas are injected at a certain ratio,
If a large amount of gas is strongly blown into the molten steel, the Cr in the molten steel will be oxidized and the yield will deteriorate, and if a small amount of gas is blown into the molten steel weakly to prevent oxidation, refining will take a long time. Purpose of the Invention The present invention was made in view of the above-mentioned conventional problems, and is a method for decarburizing stainless steel that prevents oxidation of Cr, increases the oxidation yield of steel, and shortens decarburization time. The purpose is to propose the following. Structure of the Invention In other words, the present invention provides a method for decarburizing stainless steel by blowing an inert gas together with oxygen gas into a steel bath under atmospheric pressure. The hole is for mixed gas of inert gas, and the side hole around the center hole is for oxygen gas, and the value α of oxygen gas amount/inert gas amount is adjusted to the range shown in the table below according to the carbon content in the molten steel. It is characterized by being blown into the air.

【表】 以下、この発明方法について詳細に説明する。
ここでは、この発明方法を実施する設備として
AOD炉を例にとり説明する。 第1図はAOD炉による脱炭方法を、第2図は
AOD炉の精錬に使用するダブルフロー型上吹き
ランスをそれぞれ示す。 AOD炉1は底部の側壁に、炉内に貯えられた
溶鋼2にO2ガスと不活性ガス(以下「Arガス」
で代表する)を吹込むための羽口3が設けられ、
上部には精錬用上吹きランス4が昇降可能に設置
されている。そして、精錬中は前記上吹きランス
4を炉内まで降下させてO2ガス5、またはO2
スとArガスの混合ガス6を吹き込むとともに羽
口3からもO2ガスとArガスの混合ガス6を吹き
込み、AOD炉1の上方を覆う排ガス吸引カバー
7にて排ガスを吸引しながら精錬を行なつてい
る。 この発明では、前記の精錬用上吹きランス4
を、第2図に示すダブルフロー型のランス14に
替えて精錬することを特徴とする。このダブルフ
ロー型上吹きランス14は、中心孔14−1とそ
の周囲に多孔14−2が配設されたもので、中心
孔14−1からO2ガスとArガスの混合ガス6を
流し、その外側の多孔14−2よりO2ガス5の
みを流すようにしている。このようにランスの中
心孔をO2ガスとArガスの混合ガス用とし、その
周囲の多孔をO2ガス用とすることにより、溶鋼
2の炭素量に応じてO2ガス量、Arガス量および
〔O2ガス量/Arガス量〕値が調整可能となり、脱
炭精錬の効率化がはかられる。 さらに、このダブルフロー型ランスは、中心孔
からO2ガスとArガスの混合ガスを噴射するため、
Arガスによる酸素ポテンシヤルの希釈によつて
Crの酸化損失が抑制されると共に、中心孔から
垂直に吹き付けられる混合ガスジエツトは、中心
周囲の側孔からの酸素ガスジエツトに包囲されて
溶鋼中に深く浸入するから、溶鋼中の脱炭反応お
よびCrの酸化防止に有効に作用する。また、中
心孔周囲の側孔からの酸素ガスジエツトは、炉内
に有効に拡散するため、通常の脱炭吹錬および二
次燃焼に有効に作用する。 第3図は横軸に溶鋼中の炭素含有量(wt%)
を、縦軸に精錬中におけるCr酸化損失量(Kg/
T−st)をとり、溶鋼中に吹き込むO2ガスとAr
ガスの割合〔O2ガス量/Arガス量=α〕の値を
変化させて溶鋼中の炭素含有量とCr酸化損失量
の関係を示したものである。なお、この結果は
SUS430の場合である。 すなわち、炭素含有量の多い溶鋼では酸素ガス
吹き込み量が多くてもCr酸化損失量は少ないが、
炭素含有量が少なくなるにつれてCr酸化損失量
が増加する傾向にあるため、炭素含有量の少ない
溶鋼の場合はO2ガス量の割合を少なくしなけれ
ばならない。従つて、O2ガス吹き込みによる脱
炭反応は周知の通り、 2C+O2→2CO であるから、溶鋼中に炭素含有量の多い精錬初期
においては、O2ガス吹き込み量を多くし、溶鋼
中でのCO分圧(Pco)を下げ、O2分圧を高める
程脱炭反応が急速に進行し、脱炭精錬時間が短縮
することになる。 この発明はかかる知見より、ステンレス鋼の脱
炭に際し、溶鋼中の炭素含有量が多い場合はO2
ガス吹き込み量を極力多くして脱炭時間を短縮
し、溶鋼中の炭素含有量が低下するにしたがつて
O2ガス吹き込み量を低下させるとともにArガス
吹き込み量を増加して溶鋼の攪拌を十分に行ない
ながらCr酸化損失量の低減をはかる方法である。 すなわち、この発明は第3図の結果より、溶鋼
中の炭素量に応じて〔O2ガス量/Arガス量〕値
を前記第1表に示す範囲(第3図斜線部)で調整
して脱炭する方法であり、そのガス量調整を容易
にするために第2図に示すダブルフロー型の上吹
きランスを使用し、該ランスの中心孔14−1か
らO2ガスとArガスの混合ガス6を、その外側の
多孔14−2よりO2ガス5をそれぞれ吹き込む
こととしたのである。また、このダブルフロー型
ランスによれば、〔O2ガス流量/Arガス流量〕の
値の広い調整範囲を得ることができる。 この発明において、溶鋼中の炭素含有量に応じ
て〔O2ガス流量/Arガス流量〕を前記第1表の
範囲に調整する理由は、各範囲の上限値以上では
O2ガス流量を上昇させても脱炭速度はほとんど
上昇しないだけでなく溶鋼中のCrが酸化し損失
量が増加するためであり、また下限値以下では溶
鋼中のCrの酸化は低下するが、脱炭反応が遅く、
脱炭処理時間が延長して処理能率の悪化を招くか
らである。 実施例 SUS430系のステンレス鋼の脱炭を90トンAOD
炉で行なう際、第2表に示す初期成分(高炭素フ
エロクロム添加前溶鋼成分)の溶鋼60トンを
AOD炉に貯え、炉底部の羽口からO2ガスとArガ
スの混合ガスを吹き込みながら、第2図に示す上
吹きランスを使用してO2ガスとArガスを吹き込
んだ。その際、推定される含有炭素量に応じて前
記O2ガスとArガスの吹き込み割合〔O2ガス流
量/Arガス流量〕を調整した。その時の溶鋼中
炭素含有量と〔O2ガス流量/Arガス流量〕の関
係を第3表に示す。なお、高炭素フエロクロムの
投入は、炉上ホツパーより吹錬を行ないながら吹
錬初期に投入した。 本実施例における脱炭後溶鋼成分等結果を第4
表に、脱炭の経緯を第4図に示す。なお、第4表
には第3表に示す従来法で脱炭した場合の結果を
併せて示した。 第4表の結果より、従来法に比べてCr酸化損
失が少なくなることにより還元用フエロシリコン
も少なくてすみ、また脱炭時間も大巾に短縮され
ることがわかる。
[Table] The method of this invention will be explained in detail below.
Here, as equipment for carrying out the method of this invention,
This will be explained using an AOD furnace as an example. Figure 1 shows the decarburization method using an AOD furnace, and Figure 2 shows the decarburization method using an AOD furnace.
The double-flow type top-blowing lances used for refining in AOD furnaces are shown. The AOD furnace 1 is equipped with O 2 gas and inert gas (hereinafter referred to as "Ar gas") on the side wall of the bottom of the molten steel 2 stored in the furnace.
A tuyere 3 is provided for blowing in (represented by ),
A top blowing lance 4 for refining is installed in the upper part so as to be movable up and down. During refining, the upper blowing lance 4 is lowered into the furnace and O 2 gas 5 or a mixed gas 6 of O 2 gas and Ar gas is blown into the furnace, and a mixed gas of O 2 gas and Ar gas is also blown from the tuyere 3. 6 is blown into the AOD furnace 1, and refining is performed while sucking the exhaust gas with an exhaust gas suction cover 7 that covers the upper part of the AOD furnace 1. In this invention, the above-mentioned top blowing lance for refining 4
It is characterized in that the refining process is performed by replacing the lance 14 with a double flow type lance 14 shown in FIG. This double flow type top-blowing lance 14 has a center hole 14-1 and a plurality of holes 14-2 arranged around the center hole 14-1, and a mixed gas 6 of O 2 gas and Ar gas flows through the center hole 14-1. Only the O 2 gas 5 is allowed to flow through the outer holes 14-2. In this way, by using the center hole of the lance for a mixed gas of O 2 gas and Ar gas, and using the surrounding porous holes for O 2 gas, the amount of O 2 gas and Ar gas amount can be reduced depending on the carbon content of the molten steel 2. and [O 2 gas amount/Ar gas amount] values can be adjusted, improving the efficiency of decarburization refining. Furthermore, this double flow lance injects a mixture of O 2 gas and Ar gas from the center hole.
By diluting the oxygen potential with Ar gas
The oxidation loss of Cr is suppressed, and the mixed gas jet blown vertically from the center hole penetrates deeply into the molten steel surrounded by the oxygen gas jet from the side holes around the center, which reduces the decarburization reaction and Cr in the molten steel. Effective in preventing oxidation. In addition, the oxygen gas jet from the side holes around the center hole is effectively diffused into the furnace, so it acts effectively on normal decarburization blowing and secondary combustion. In Figure 3, the horizontal axis shows the carbon content (wt%) in molten steel.
The vertical axis shows the amount of Cr oxidation loss (Kg/
T-st) and inject O2 gas and Ar into the molten steel.
The figure shows the relationship between the carbon content in molten steel and the amount of Cr oxidation loss by varying the gas ratio [O 2 gas amount/Ar gas amount = α]. Furthermore, this result is
This is the case of SUS430. In other words, in molten steel with a high carbon content, the amount of Cr oxidation loss is small even if the amount of oxygen gas blown is large, but
Since the amount of Cr oxidation loss tends to increase as the carbon content decreases, in the case of molten steel with a low carbon content, the ratio of the amount of O 2 gas must be reduced. Therefore, as is well known , the decarburization reaction due to O 2 gas injection is 2C + O 2 → 2CO. The lower the CO partial pressure (Pco) and the higher the O 2 partial pressure, the more rapidly the decarburization reaction will proceed and the decarburization refining time will be shortened. Based on this knowledge, this invention is based on the knowledge that when decarburizing stainless steel, if the carbon content in molten steel is high, O 2
By increasing the gas injection amount as much as possible to shorten the decarburization time and reduce the carbon content in the molten steel.
This method aims to reduce the amount of Cr oxidation loss while sufficiently stirring the molten steel by decreasing the amount of O 2 gas blown and increasing the amount of Ar gas blown. That is, based on the results shown in Fig. 3, the present invention adjusts the [O 2 gas amount/Ar gas amount] value within the range shown in Table 1 (hatched area in Fig. 3) according to the carbon content in molten steel. This is a method of decarburizing, and in order to easily adjust the gas amount, a double flow type top blowing lance shown in Fig. 2 is used, and O 2 gas and Ar gas are mixed from the center hole 14-1 of the lance. It was decided to blow in the gas 6 and the O2 gas 5 through the outer holes 14-2. Moreover, according to this double flow type lance, a wide adjustment range of the value of [O 2 gas flow rate/Ar gas flow rate] can be obtained. In this invention, the reason why [O 2 gas flow rate/Ar gas flow rate] is adjusted to the range shown in Table 1 according to the carbon content in molten steel is that if the upper limit of each range is exceeded,
This is because increasing the O 2 gas flow rate not only hardly increases the decarburization rate but also oxidizes the Cr in the molten steel and increases the amount of loss.Also, below the lower limit, the oxidation of Cr in the molten steel decreases. , the decarburization reaction is slow;
This is because the decarburization treatment time is extended, resulting in deterioration of treatment efficiency. Example: Decarburization of SUS430 series stainless steel by 90 tons AOD
When processing in a furnace, 60 tons of molten steel with the initial composition shown in Table 2 (molten steel composition before high carbon ferrochrome addition) is
The mixture was stored in an AOD furnace, and while a mixed gas of O 2 gas and Ar gas was blown in from the tuyeres at the bottom of the furnace, O 2 gas and Ar gas were blown in using the top blowing lance shown in Figure 2. At that time, the blowing ratio of the O 2 gas and Ar gas [O 2 gas flow rate/Ar gas flow rate] was adjusted according to the estimated carbon content. Table 3 shows the relationship between the carbon content in the molten steel and [O 2 gas flow rate/Ar gas flow rate] at that time. Note that high carbon ferrochrome was introduced from the hopper above the furnace at the beginning of blowing while blowing was being carried out. The results of the molten steel composition after decarburization in this example are shown in the fourth table.
The table shows the history of decarbonization in Figure 4. Table 4 also shows the results of decarburization using the conventional method shown in Table 3. From the results in Table 4, it can be seen that compared to the conventional method, the oxidation loss of Cr is reduced, so less ferrosilicon is needed for reduction, and the decarburization time is also greatly shortened.

【表】【table】

【表】【table】

【表】【table】

【表】 発明の効果 以上説明したごとく、この発明方法によれば、
Cr酸化損失を増加させることなく送酸速度を上
昇させることができるので、脱炭時間の短縮がは
かられ、かつ巾広い不活性ガス比の選択が可能で
あるためCr酸化損失を最少限に抑えることがで
き、ステンレス鋼の精錬に多大な効果を奏するも
のである。
[Table] Effects of the invention As explained above, according to the method of this invention,
Since the oxygen delivery rate can be increased without increasing Cr oxidation loss, decarburization time can be shortened, and a wide range of inert gas ratios can be selected, minimizing Cr oxidation loss. This has a great effect on the refining of stainless steel.

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

第1図はAOD炉による脱炭方法を示す説明図、
第2図はこの発明方法を実施するための上吹きラ
ンスの構造を示す縦断面図、第3図は同上ランス
を用い〔O2ガス量/Arガス量〕の値を変化させ
て脱炭したときの溶鋼中炭素含有量とCr酸化損
失量の関係を示す図表、第4図はこの発明の実施
例における脱炭の経緯を示す図表である。 1……AOD炉、2……溶鋼、3……羽口、4
……ランス、5……O2ガス、6……混合ガス、
14……ダブルフロー型ランス。
Figure 1 is an explanatory diagram showing the decarburization method using an AOD furnace.
Figure 2 is a vertical cross-sectional view showing the structure of a top blowing lance for carrying out the method of this invention, and Figure 3 shows decarburization using the same lance and varying the value of [ O2 gas amount/Ar gas amount]. FIG. 4 is a chart showing the relationship between the carbon content in molten steel and the amount of Cr oxidation loss. 1...AOD furnace, 2...molten steel, 3...tuyere, 4
... Lance, 5 ... O 2 gas, 6 ... Mixed gas,
14...Double flow type lance.

Claims (1)

【特許請求の範囲】 1 酸素ガスと共に不活性ガスを大気圧下で鋼浴
中に吹き込んでステンレス鋼の脱炭を行なう方法
において、上吹きランスをダブルフロー型とし、
中心孔を酸素ガスと不活性ガスの混合ガス用と
し、中心孔周囲の側孔を酸素ガス用とし、溶鋼中
の炭素含有量[C]に応じて、酸素ガス量/不活
性ガス量の値αを下記表の範囲に調整して吹き込
むことを特徴とするステンレス鋼の脱炭方法。 【表】
[Claims] 1. In a method for decarburizing stainless steel by blowing inert gas together with oxygen gas into a steel bath under atmospheric pressure, the top blowing lance is of a double flow type,
The center hole is used for a mixed gas of oxygen gas and inert gas, and the side holes around the center hole are used for oxygen gas, and the value of oxygen gas amount / inert gas amount is determined according to the carbon content [C] in molten steel. A method for decarburizing stainless steel, which is characterized by adjusting α to the range shown in the table below and blowing into the stainless steel. 【table】
JP13278484A 1984-06-27 1984-06-27 Method for decarburizing stainless steel Granted JPS6112812A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13278484A JPS6112812A (en) 1984-06-27 1984-06-27 Method for decarburizing stainless steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13278484A JPS6112812A (en) 1984-06-27 1984-06-27 Method for decarburizing stainless steel

Publications (2)

Publication Number Publication Date
JPS6112812A JPS6112812A (en) 1986-01-21
JPH0456083B2 true JPH0456083B2 (en) 1992-09-07

Family

ID=15089461

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13278484A Granted JPS6112812A (en) 1984-06-27 1984-06-27 Method for decarburizing stainless steel

Country Status (1)

Country Link
JP (1) JPS6112812A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2674186C1 (en) * 2017-11-13 2018-12-05 Публичное акционерное общество "Северсталь" (ПАО "Северсталь") Procedure for melting steel in converter
RU2764455C1 (en) * 2021-05-06 2022-01-17 Публичное акционерное общество «Северсталь» (ПАО «Северсталь») Method for steel smelting in a converter

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JP2615728B2 (en) * 1987-12-26 1997-06-04 日本鋼管株式会社 Decarburization method for Cr-containing pig iron
JPH04362115A (en) * 1991-06-06 1992-12-15 Nippon Steel Corp Decarburizing method for molten steel
DE102006056672A1 (en) * 2006-11-30 2008-06-05 Sms Demag Ag Method and apparatus for stainless steel production without electrical energy supply based on pig iron

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US4529442A (en) * 1984-04-26 1985-07-16 Allegheny Ludlum Steel Corporation Method for producing steel in a top oxygen blown vessel

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2674186C1 (en) * 2017-11-13 2018-12-05 Публичное акционерное общество "Северсталь" (ПАО "Северсталь") Procedure for melting steel in converter
RU2764455C1 (en) * 2021-05-06 2022-01-17 Публичное акционерное общество «Северсталь» (ПАО «Северсталь») Method for steel smelting in a converter

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