JPH0432510A - Method for raising temperature of molten steel in ladle with oxygen blowing - Google Patents

Method for raising temperature of molten steel in ladle with oxygen blowing

Info

Publication number
JPH0432510A
JPH0432510A JP13716890A JP13716890A JPH0432510A JP H0432510 A JPH0432510 A JP H0432510A JP 13716890 A JP13716890 A JP 13716890A JP 13716890 A JP13716890 A JP 13716890A JP H0432510 A JPH0432510 A JP H0432510A
Authority
JP
Japan
Prior art keywords
molten steel
molten
steel
ladle
oxygen
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.)
Granted
Application number
JP13716890A
Other languages
Japanese (ja)
Other versions
JPH07103415B2 (en
Inventor
Mutsuo Nakajima
中嶋 睦生
Masatomo Sasagawa
笹川 正智
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 JP2137168A priority Critical patent/JPH07103415B2/en
Publication of JPH0432510A publication Critical patent/JPH0432510A/en
Publication of JPH07103415B2 publication Critical patent/JPH07103415B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To prevent erosion of refractory and clogging of a nozzle for casting caused by produced slag from the refractory material by beforehand adjusting Si content in molten steel to high and adding the specific small quantity of Al at the time of raising temp. of molten Si killed steel with oxygen blowing. CONSTITUTION:At the time of continuously cast after charging the Si killed steel 1 already refined with a ladle 2, the temp. of molten steel is raised to the temp. being suitable to casting. For this purpose, inert gas is blown from a bubbling lance 6 and after removing the molten slag 7 floated with rising bubble, a submerged tube 4 is lowered to the position having no molten slag 7 and the tip part is submerged into the molten slag 7. Fe-Si is charged from a charging tube 5 in the submerged tube 4 to adjust Si content in the molten steel 1 at higher than the aimed value. Successively, O2 gas is supplied onto the molten steel surface from a lance 3 and during this period, Al is added into the molten steel 1 at 10-5O% of the theoretical oxidation with supplied oxygen quantity. The temp. of molten Si killed steel 1 is raised with oxidation of Al and Si and also the molten slag composed of 3Al2O3.2SiO2 is generated, and the erosion of the lining refractory of submerged tube 4 and the clogging of nozzle for continuous casting can be prevented.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は精錬炉から出鋼され、脱酸精製された後の取鍋
内容鋼を吹酸して昇熱する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method of blowing acid into steel in a ladle after it has been tapped from a refining furnace and deoxidized and refined to raise its temperature.

(従来の技術) 一般に転炉、電気炉等の精錬炉から連続鋳造工程におい
ては温度、成分及び溶鋼の供給タイミングを配慮した操
業が必要である。
(Prior Art) Generally, in continuous casting processes from refining furnaces such as converters and electric furnaces, it is necessary to operate with consideration to temperature, composition, and timing of supply of molten steel.

しかし、実操業では精錬炉の吹止め温度のバラツキ、出
鋼のタイミング不良、添加合金の歩留り変動等により連
続鋳造が不可能となる。
However, in actual operation, continuous casting becomes impossible due to variations in the blow-off temperature of the refining furnace, poor timing of tapping, and fluctuations in the yield of additive alloys.

従って、例えば特開昭53−149826号公報、ある
いは特開昭59−、13331’ 4号公報に示すよう
に取鍋内容鋼の上層面に浸漬管を浸漬す合金、81等の
可燃物を添加しつつ吹酸することにより溶鋼を昇熱する
方法が提案されている。
Therefore, for example, as shown in JP-A-53-149826 or JP-A-59-13331'4, a combustible material such as alloy 81 is added to the upper surface of the steel in the ladle. A method has been proposed in which the temperature of molten steel is raised by blowing acid at the same time.

(発明が解決しようとよする課題) しかしながら、前述の取鍋固溶鋼の吹酸昇熱方法では以
下の問題点がある。
(Problems to be Solved by the Invention) However, the above-described method for heating solid solution steel in a ladle with acid blowing has the following problems.

まず、Siキルド鋼の昇熱には発熱材としてFeSi合
金を使用し、上吹酸素で酸化させて、その酸化発熱によ
り取鍋的溶鋼を昇熱する方法が一般的である。この方法
では浸漬管の内張耐火物が激しく溶損され、通常作業に
耐え難い。
First, a common method for heating Si-killed steel is to use an FeSi alloy as a heat generating material, oxidize it with top-blown oxygen, and use the heat generated by the oxidation to heat up molten steel in a ladle. In this method, the refractory lining of the immersion pipe is severely eroded and cannot withstand normal work.

これを解決し、浸漬管耐火物の溶損を防ぐ方法として酸
化生成物の溶融点の高い発熱材を使用する方法が最も効
果がある。即ち、酸化生成物が固形化すると耐火物と反
応しないためである。
The most effective method to solve this problem and prevent melting loss of the immersion pipe refractories is to use a heat generating material whose oxidation product has a high melting point. That is, this is because the oxidation product does not react with the refractory once solidified.

この条件に合致する発熱材はAQであり、この酸化物の
l!、O,はその溶融点が2000℃以上と高く、通常
の操業では浸漬管内で固形化しており、全く浸漬管の溶
損はない。
A heat generating material that meets this condition is AQ, and this oxide l! , O, has a high melting point of 2000° C. or higher, and during normal operation, it solidifies inside the immersion tube, and there is no melting loss of the immersion tube.

この様にAffを溶鋼の昇熱用発熱剤として使用するこ
とは操業上極めて有利である。
The use of Aff as a heating agent for raising the temperature of molten steel in this way is extremely advantageous in terms of operation.

しかし、Siキルト鋼に発熱剤としてA(を使用すると
少量のA(が酸化出来ずに溶鋼内に残留することになる
。Siキルト鋼は大部分か、現在ビレット又はブルーム
CCで生産されているか、タンデイツシュノズルは比較
的小径であるため、溶鋼内に少量のAQ、が残留すると
、このAQによりノズル閉塞が発生し鋳込が不可能とな
る。これが一般のSiキルト鋼には発熱剤としてAQを
使用出来ない理由である。
However, if A is used as a heating agent in Si quilted steel, a small amount of A cannot be oxidized and remains in the molten steel. Since the tandate nozzle has a relatively small diameter, if a small amount of AQ remains in the molten steel, this AQ will clog the nozzle and make casting impossible. This is the reason why AQ cannot be used as

又、Fe−Si合金で溶鋼を昇熱する方法では前述の如
く浸漬管が激しく溶損する欠点に加え、溶鋼中のMnが
酸化除去される大きな欠点も有している。Mnも酸化発
熱に寄与するが、その発熱量はSi、AQに比して1/
6であり効率的とは言い難い。又、Mnの酸化除去分は
F e−M n合金し で補充芯なければならず、大きなコストアップとなり好
ましくない。
In addition, the method of heating molten steel using an Fe-Si alloy has the disadvantage that the immersion tube is severely damaged by erosion as described above, and also has the major disadvantage that Mn in the molten steel is removed by oxidation. Mn also contributes to oxidation heat generation, but its calorific value is 1/1 compared to Si and AQ.
6, which can hardly be called efficient. Further, the amount of Mn removed by oxidation must be replaced by a Fe--Mn alloy, which is undesirable as it increases the cost significantly.

多量のMnが酸化除去される理由としてはMnの酸化強
度が81の酸化強度よりも若干劣るけれとも酷似してい
るためである。
The reason why a large amount of Mn is removed by oxidation is that the oxidation strength of Mn is very similar to that of 81, although it is slightly inferior to that of 81.

本発明はこれ等従来の取鍋内容鋼の吹酸昇熱方法の欠点
である吹酸昇熱時の耐火物の溶損を防止するとともに有
価元素の損失を抑制し、しかも高速昇熱の実現と鋳造時
のノズル閉塞のない昇熱方法を提供することにある。
The present invention prevents the erosion of the refractory during heating with blown acid, which is a drawback of the conventional heating method for heating steel in a ladle with blown acid, suppresses the loss of valuable elements, and realizes high-speed heating. Another object of the present invention is to provide a heating method that does not cause nozzle clogging during casting.

(課題を解決するための手段) 本発明は取鍋内の溶鋼に不活性ガスを吹き込み溶鋼を撹
拌するとともに、溶鋼上部に浸漬管を浸漬し、該浸漬管
内に発熱剤を添加し酸素を吹き付けて取鍋内の溶鋼を昇
熱する方法において、S】キルド鋼の溶鋼に酸素を吹き
付ける際に取鍋内の溶鋼のSi成分を目標値よりも予め
高く調整した後、酸素を吹き付けると同時にアルミもし
くは合金を添加するとともに、この添加される純アルミ
壜が酸素で理論的に燃焼する量の10%から50%を連
続投入することを特徴とする取鍋内容鋼の吹酸昇熱方法
である。
(Means for Solving the Problems) The present invention involves blowing inert gas into molten steel in a ladle to stir the molten steel, and immersing an immersion tube in the upper part of the molten steel, adding a heat generating agent into the immersion tube, and blowing oxygen into the molten steel. In the method of raising the temperature of molten steel in a ladle, the Si content of the molten steel in the ladle is adjusted to be higher than the target value beforehand when spraying oxygen to the molten steel of killed steel. Alternatively, it is a blown acid heating method for steel in a ladle, which is characterized by adding an alloy and continuously adding 10% to 50% of the amount that the added pure aluminum bottle would theoretically burn with oxygen. .

以下本発明によるSjキルドII (S i = 0.
10%以上)の溶鋼の昇熱方法について図に基づいて述
へる。
Hereinafter, Sj Killed II (S i = 0.
10% or more) of molten steel will be described based on the diagram.

本発明で使用する溶鋼の昇熱設備は第1図に示す如く溶
Illの上面に浸漬管4を設置して実施される。浸漬管
4の」1方には発熱付投入管及び排煙吸引管5が浸漬管
4の上下昇降に追従する構造体で接続されている。又浸
漬管4とは独立して昇降化 する」−吹酸素ランス3が′を置されている。取鍋底部
から溶鋼lを撹拌する目的でバブリングランス6が設置
されている。
The molten steel heating equipment used in the present invention is implemented by installing an immersion pipe 4 on the upper surface of the molten steel as shown in FIG. A heating input pipe and an exhaust gas suction pipe 5 are connected to one side of the dipping tube 4 by a structure that follows the up and down movement of the dipping tube 4. Also, a blown oxygen lance 3 is placed which is raised and lowered independently of the dip tube 4. A bubbling lance 6 is installed for the purpose of stirring the molten steel l from the bottom of the ladle.

1−述の昇熱設備を使用して実際の昇熱作業方法を述へ
る。
1- An actual heating work method using the heating equipment described above will be described.

浸漬管4を溶鋼内に浸漬するに先立ち、バブリングラン
ス6を下降させ、浸漬管4下方の取鍋溶鋼」−面に浮遊
したスラグ7を排除する。その後浸漬管4を下降させ溶
91内に浸漬させる。
Prior to immersing the immersion tube 4 into molten steel, the bubbling lance 6 is lowered to remove the slag 7 floating on the surface of the ladle molten steel below the immersion tube 4. Thereafter, the immersion tube 4 is lowered and immersed in the melt 91.

この状態で浸漬管4内にFe−Si合金鉄等のSl系合
金鉄を投入し、取鍋固溶1i+の81成分をその目標値
よりも高目に調整する。
In this state, a Sl-based ferroalloy such as Fe-Si ferroalloy is introduced into the dipping tube 4, and the 81 component of the ladle solid solution 1i+ is adjusted to be higher than its target value.

その後送酸するが、この期間中AQ、を供給酸素量で理
論的に酸化するAQ量の10%〜50%相当量のAff
を送酸中に連続して供給する。この際同時期にSi系合
金を浸漬管4内に少量供給しても良いが、投入されたA
Cを完全に浸漬管4内で酸化燃焼させ、溶鋼中に残留さ
せないためにはSi系合金鉄は供給しない方が望ましい
。又投入された八(を浸漬管4内で効果的に酸化させる
ためには浸漬管4内の溶鋼の撹拌状況が極めて重要であ
り、種々の水モデルテストと実操業の結果から浸漬管4
の浸漬深さは200mm以上、撹拌ガス量は溶鋼1 t
on当たりINρ/分、以下が好ましい。
After that, oxygen is supplied, but during this period, AQ is supplied in an amount equivalent to 10% to 50% of the amount of AQ that theoretically oxidizes with the amount of supplied oxygen.
is continuously supplied during oxygen supply. At this time, a small amount of Si-based alloy may be supplied into the immersion tube 4 at the same time, but the
In order to completely oxidize and burn C in the immersion tube 4 and prevent it from remaining in the molten steel, it is preferable not to supply Si-based alloy iron. In addition, in order to effectively oxidize the molten steel in the immersion tube 4, the stirring condition of the molten steel in the immersion tube 4 is extremely important, and based on the results of various water model tests and actual operations,
The immersion depth is 200 mm or more, and the amount of stirring gas is 1 t of molten steel.
INρ/min per ON, preferably less than or equal to INρ/min.

この方法で吹酸昇熱する場合、浸漬管4の内部では先ず
八ρが酸化される又、lを酸化した残余の酸素は溶鋼中
のSiを同時に酸化する。
When heating with blown acid using this method, 8ρ is first oxidized inside the immersion tube 4, and the remaining oxygen after oxidizing 1 simultaneously oxidizes Si in the molten steel.

このように本発明は浸漬管耐火物の溶損機構に着目した
結果、酸化生成物の高溶融点化が効果的であると考え八
〇とSiの同時酸化による3i、O。
As described above, the present invention focused on the erosion mechanism of immersion pipe refractories and found that raising the melting point of the oxidation product is effective in reducing 3i and O through the simultaneous oxidation of 80 and Si.

2 S i Oyの複塩生成物を造るようにしたもので
ある。
2 S i Oy double salt product is produced.

この3A(1203’ 2S io、+;i第2図の如
く、高温の融点を有しており、通常操業では浸漬管内で
固形化している。又送酸中の鋼中Mnの酸化を防ぐため
には酸化能力がMnより著しく高いlが最も優れており
少量のACを送酸点に供給することにより、Mnの酸化
に優先してAQが酸化することになる。そのためMnの
酸化が抑制される。
As shown in Figure 2, this 3A (1203' 2S io, +; The oxidizing ability of 1 is significantly higher than that of Mn, and by supplying a small amount of AC to the oxygen supply point, AQ oxidizes in preference to Mn oxidation.Therefore, the oxidation of Mn is suppressed. .

ここで投入されるAg量が理論的酸化量に対し10%よ
り少ないと高速昇熱が行ない得す、しかも溶鋼中Siが
先行酸化されてスラグ中のSin。
If the amount of Ag introduced here is less than 10% of the theoretical oxidation amount, high-speed heating can be achieved, and moreover, Si in the molten steel is oxidized in advance and Si in the slag.

濃度が上昇して耐火物の溶損が急激に進行する。The concentration increases and the erosion of refractories progresses rapidly.

また、AQ量が50%より多いと浸漬管内に添加された
八ぐが溶鋼中に残留し、鋳造時のノズル閉塞を生じる。
Furthermore, if the AQ amount is more than 50%, the octane added to the immersion tube remains in the molten steel, causing nozzle blockage during casting.

このように、前記の条件に加味して、該A12をその時
々の所要比となるように連続投入することにより、AQ
あるいはAQ金合金本来の高速昇熱を行なわしめるとと
もに、耐火物の損耗を抑制し、且つA(による鋳造阻害
を防止し効果的なS]キルト鋼の昇熱方法を確立てきた
In this way, by taking into account the above conditions and continuously adding the A12 to the required ratio at each time, the AQ
Alternatively, we have established a heating method for S quilt steel that is effective in achieving the high-speed heating inherent to AQ gold alloys, suppressing wear on the refractories, and preventing casting inhibition caused by A.

(実施例) 次にSlの含有量が0.15%の81キルト鋼にあらか
しめ余分のSiを付加した後に本発明の昇熱方法を適用
した場合を従来法及び比較例と対比して表1に示す。
(Example) Next, the case where the heating method of the present invention is applied after tempering and adding extra Si to 81 quilt steel with a Sl content of 0.15% is shown in comparison with the conventional method and a comparative example. Shown in 1.

表1の昇熱条件は送酸速度を4000 Nm3/lIr
にした時の比較であり、Fe−5iで昇熱する従来法は
Siを酸化させるに要する酸素の量がAQのそれより大
きいため昇熱速度が小さくなっている。
The heating conditions in Table 1 are as follows: The oxygen delivery rate is 4000 Nm3/lIr.
This is a comparison when the conventional method uses Fe-5i to raise the temperature, and since the amount of oxygen required to oxidize Si is larger than that of AQ, the heating rate is lower.

浸漬管耐火物の溶損量は送酸中に少量のA(を使用し、
AQとSiの両者を同時に酸化させる本発明法の場合、
従来法に比して極めて小さく著しく改善されていること
が解ける。
The amount of erosion of immersion pipe refractories is measured by using a small amount of A (
In the case of the present invention method in which both AQ and Si are oxidized at the same time,
It can be seen that this is a very small and significant improvement compared to the conventional method.

又鋼中Mnの減少量も従来法に比して小さく M n系
合金の節約となるものである。
Furthermore, the reduction in Mn in the steel is smaller than in the conventional method, resulting in savings in Mn-based alloys.

この様にSiキルト鋼の効果的な昇熱方法を提供するも
のであり、小径ノズルタンデイツシュを有するCCにと
っては極めて有用な取鍋内容鋼昇熱法である。
In this way, this method provides an effective heating method for Si quilt steel, and is an extremely useful method for heating steel in a ladle for CCs having small-diameter nozzle tundishes.

表    1 本発明法^法人e使用量を酸素で理論的に燃焼する量の
0.1とした。
Table 1 Method of the Invention The amount used was set at 0.1 of the theoretical combustion amount with oxygen.

B法二Aa使用量を酸素で理論的に燃焼する量の05と
した。
B Method 2 The amount of Aa used was set to 0.05, which is the amount that can be theoretically burned with oxygen.

比較例   ・へa使用量を酸素で理論的に燃焼する量
の06とした。
Comparative Example - The amount of a used was set to 06, which is the amount that can be theoretically burned with oxygen.

*^C使用量を増量した場合の操業可否を確認するため
^e使用量を酸素で理論的に燃焼する量の(L、Sとし
た確認試験を行ったところ、昇温量、浸漬管耐火物溶損
量について極めて良好な結果が得られたが、溶鋼中残留
T、八へ量がo、ooa%とたかくなり、小径タンデイ
シュノズルではノズル閉塞が発生して通常操業には適用
出来ないことが判明した。
*In order to confirm whether operation is possible when the amount of C used is increased, a confirmation test was conducted using the amount of e used that was theoretically combustible with oxygen (L, S). Very good results were obtained regarding the amount of material corrosion loss, but the amount of residual T, 8, in the molten steel was as high as 0,00%, and nozzle clogging occurred with the small-diameter tundish nozzle, making it unsuitable for normal operation. It turns out there isn't.

(発明の効果) 以上述べた如く、本発明の昇熱方法はSiキルド鯛特有
の鋳造時におけるノズル閉塞が全く生じることなく溶鋼
の高速昇熱が実現でき、かつ耐火物の溶損を防止し得る
もので、極めて優れた溶鋼の吹酸昇熱方法である。
(Effects of the Invention) As described above, the heating method of the present invention can achieve high-speed heating of molten steel without causing any nozzle clogging during casting, which is unique to Si-killed sea bream, and prevents melting of refractories. This is an extremely excellent method for heating molten steel by blowing acid.

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

第1図は本発明で使用する取鍋内容鋼昇熱装置の概略図
、第2図はS i Ot−αAL03の溶融点図、第3
図(a) (b)は鋳造時のノズル閉塞と鋳片ピンホー
ルの発生指数の比較を示す図である。 l・・・・・溶鋼 2・・・・・取鍋 上吹酸素ランス 浸漬管 全熱材投入管及び排煙吸引管 バブリングランス スラグ 出 願 人 新日本製鐵株式会社 I&3図 (α) 1N2図 5IOrjAl+O+
Figure 1 is a schematic diagram of the ladle content steel heating device used in the present invention, Figure 2 is the melting point diagram of S i Ot-αAL03, and Figure 3 is a diagram of the melting point of S i Ot-αAL03.
Figures (a) and (b) are diagrams showing a comparison of the nozzle blockage during casting and the occurrence index of slab pinholes. l... Molten steel 2... Ladle top-blown oxygen lance immersion tube Total heating material input pipe and flue gas suction pipe bubbling lance slag Applicant Nippon Steel Corporation Figure I & 3 (α) Figure 1N2 5IOrjAl+O+

Claims (1)

【特許請求の範囲】[Claims] 取鍋内の溶鋼に不活性ガスを吹き込み溶鋼を撹拌すると
ともに、溶鋼上部に浸漬管を浸漬し、該浸漬管内に発熱
剤を添加し酸素を吹き付けて取鍋内の溶鋼を昇熱する方
法において、Siキルド鋼の溶鋼に酸素を吹き付ける際
に取鍋内の溶鋼のSi成分を目標値よりも予め高く調整
した後、酸素を吹き付けると同時にアルミもしくはアル
ミ合金を添加するとともに、この添加される純アルミ量
が酸素で理論的に燃焼する量の10%から50%を連続
投入することを特徴とする取鍋内容鋼の吹酸昇熱方法。
In a method in which inert gas is blown into the molten steel in the ladle to stir the molten steel, a dipping tube is immersed above the molten steel, a heating agent is added to the dipping tube, and oxygen is blown to raise the temperature of the molten steel in the ladle. When blowing oxygen to molten steel of Si-killed steel, after adjusting the Si content of the molten steel in the ladle to be higher than the target value, at the same time as blowing oxygen, aluminum or aluminum alloy is added, and the added pure A blowing acid heating method for steel in a ladle, characterized by continuously adding 10% to 50% of the amount of aluminum theoretically combustible with oxygen.
JP2137168A 1990-05-29 1990-05-29 Heating method of molten acid in molten steel in ladle Expired - Lifetime JPH07103415B2 (en)

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Application Number Priority Date Filing Date Title
JP2137168A JPH07103415B2 (en) 1990-05-29 1990-05-29 Heating method of molten acid in molten steel in ladle

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Application Number Priority Date Filing Date Title
JP2137168A JPH07103415B2 (en) 1990-05-29 1990-05-29 Heating method of molten acid in molten steel in ladle

Publications (2)

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JPH0432510A true JPH0432510A (en) 1992-02-04
JPH07103415B2 JPH07103415B2 (en) 1995-11-08

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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS594485A (en) * 1982-06-29 1984-01-11 Saburo Nishimura Separation of waste composite plastic material
JPS61235506A (en) * 1985-04-09 1986-10-20 Nippon Steel Corp Heating up method for molten steel in ladle

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS594485A (en) * 1982-06-29 1984-01-11 Saburo Nishimura Separation of waste composite plastic material
JPS61235506A (en) * 1985-04-09 1986-10-20 Nippon Steel Corp Heating up method for molten steel in ladle

Also Published As

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JPH07103415B2 (en) 1995-11-08

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