JPH06306441A - Method for refining steel - Google Patents

Method for refining steel

Info

Publication number
JPH06306441A
JPH06306441A JP12090093A JP12090093A JPH06306441A JP H06306441 A JPH06306441 A JP H06306441A JP 12090093 A JP12090093 A JP 12090093A JP 12090093 A JP12090093 A JP 12090093A JP H06306441 A JPH06306441 A JP H06306441A
Authority
JP
Japan
Prior art keywords
steel
deoxidation
molten steel
gaseous hydrogen
blowing
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.)
Withdrawn
Application number
JP12090093A
Other languages
Japanese (ja)
Inventor
Tetsuo Okamoto
徹夫 岡本
Yoshisato Takesono
嘉識 竹園
Masaaki Takagi
政明 高木
Yasuhiro Kimura
泰廣 木村
Atsushi Kanekawa
淳 金川
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co 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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP12090093A priority Critical patent/JPH06306441A/en
Publication of JPH06306441A publication Critical patent/JPH06306441A/en
Withdrawn legal-status Critical Current

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  • Treatment Of Steel In Its Molten State (AREA)

Abstract

PURPOSE:To obtain a clean steel without producing Al2O3 as nonmetallic inclusion by executing deoxidation of molten steel by blowing gaseous hydrogen and adding no Al as finish deoxidation into the steel. CONSTITUTION:The gaseous hydrogen is blown into the molten steel to execute the deoxidation. In some cases, by using the other vessel to a melting furnace, the gaseous hydrogen is blown into the molten steel to execute the deoxidation. After executing the deoxidation by blowing this gaseous hydrogen, if necessary, by executing vacuum-degassing, dehydrogenation is executed. By blowing the gaseous hydrogen into the steel, oxygen in the steel is removed through the reaction H2+O2 H2O and the needed low oxygen molten steel is obtd. Therefore, Al, etc., is unnecessary to add as the finish deoxidation and the Al2O3 is not produced and the clean steel is obtd.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は鋼中の酸素を除去するた
めの鋼の精錬方法に関するものであり、更に詳しくは鋼
中にAl23 等の介在物を残留させない清浄鋼の精錬方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for refining steel for removing oxygen in steel, and more particularly to a method for refining clean steel in which inclusions such as Al 2 O 3 do not remain in the steel. It is about.

【0002】[0002]

【従来の技術】従来の鋼の脱酸方法は主としてSi ,M
n により予備脱酸を行ない仕上脱酸はAl を使用してい
た。上記Al による仕上脱酸は、4Al +3O2 →2A
l23 により進行し、生成したAl23 は溶鋼との密度
差による浮力によって浮上分離される。しかし微細なA
l23 の一部は浮上しきれず、溶鋼中に非金属介在物と
して残留することはまぬがれ得ない。鋼中に介在物を残
さない脱酸方法としてCによる脱酸が考えられるが、こ
れを真空中で行なっても到達し得る酸素レベルに限度が
あり、仕上脱酸にはAl を使用せざるを得ない。
2. Description of the Related Art Conventional deoxidizing methods for steel are mainly Si, M
Pre-deoxidation was carried out depending on n, and Al was used for final deoxidation. Finishing deoxidation with Al is 4Al + 3O 2 → 2A
The Al 2 O 3 produced by advancing with l 2 O 3 is floated and separated by the buoyancy due to the density difference with the molten steel. But fine A
A part of l 2 O 3 cannot be completely floated up, and it is inevitable that it will remain as non-metallic inclusions in the molten steel. Although deoxidation by C can be considered as a deoxidation method that does not leave inclusions in the steel, even if this is performed in vacuum, the oxygen level that can be reached is limited, and Al must be used for finish deoxidation. I don't get it.

【0003】[0003]

【発明が解決しようとする課題】Al23 として鋼中に
残留した場合には、Al23 が破壊の起点となり、部材
の寿命に重大な影響を及ぼすことは少なくない。従って
鋼中にAl23 のような非金属介在物を残留させない脱
酸方法が望まれることは言うまでもない。
If Al 2 O 3 remains in the steel as Al 2 O 3 , Al 2 O 3 often becomes the starting point of fracture, and often has a serious effect on the life of the member. Therefore, it goes without saying that a deoxidation method that does not leave nonmetallic inclusions such as Al 2 O 3 in steel is desired.

【0004】[0004]

【課題を解決するための手段】Al23 等の非金属介在
物を鋼中に残留させない脱酸方法として、本発明者等は
水素による脱酸を検討し本発明を完成した。即ち、本発
明によれば、H2 +O2 →2H2 O として溶鋼中の酸
素を除去し、したがって鋼中にはAl 等の添加が原因で
ある非金属介在物(酸化物)が残留しない。
As a deoxidizing method in which non-metallic inclusions such as Al 2 O 3 do not remain in steel, the present inventors have studied deoxidation with hydrogen and completed the present invention. That is, according to the present invention, oxygen in the molten steel is removed as H 2 + O 2 → 2H 2 O, so that nonmetallic inclusions (oxides) caused by the addition of Al or the like do not remain in the steel.

【0005】[0005]

【作用】本発明では、前記したように溶鋼中の酸素を介
在物を残さない形で除去するものであるが、この原理を
示せば下記の通りである。図1に溶鋼中の〔H〕,
〔O〕,〔2H2 O〕の平衡図を示した。図1によれば
アーク炉溶解後のH2 Oの濃度は夫々H=10ppm ,O
=100〜300ppm であり、T=1873°Kとして
次式からPH2O を求めるとおよそ0.01となる。 2log H+log O=log PH2O −8800/T−1.0
86 また取鍋精錬(LF)において、取鍋底に設けたポーラ
スプラグからアルゴンガスを送給し精錬を行なうとHは
約5ppm ,Oは40〜50ppm (A点)であるからP
H2O =0.0007となる。このPH2O =0.0007
下で溶鋼中のHを25ppm まで高めることが出来れば、
Oレベルが数ppm (B点)と言う低酸素含有の溶鋼が得
られることになる。
In the present invention, oxygen in molten steel is removed without leaving inclusions as described above. The principle of this is as follows. Fig. 1 shows [H] in molten steel,
The equilibrium diagrams of [O] and [2H 2 O] are shown. According to FIG. 1, the concentrations of H 2 O after melting in the arc furnace are H = 10 ppm and O, respectively.
= 100 to 300 ppm, and when T = 1873 ° K, P H2O is approximately 0.01 when calculated from the following equation. 2log H + log O = log PH2O- 8800 / T-1.0
86 In the ladle refining (LF), when argon gas is fed from the porous plug provided at the bottom of the ladle for refining, H is about 5 ppm and O is 40 to 50 ppm (point A).
H2O = 0.0007. This P H2O = 0.0007
If H in molten steel can be increased to 25 ppm below,
Oxygen level of several ppm (point B) means that a low oxygen content molten steel can be obtained.

【0006】図2に−〔C〕平衡図を示したが、PCO
=1は大気圧下での平衡であり、PCO=0.2は真空下
の平衡である。この場合にはC1%でようやく10ppm
を切る程度の酸素を含有する溶鋼が得られるにすぎな
い。しかし溶鋼中のCはその用途、性能により異なり、
浸炭用鋼や強靱鋼はCが0.2〜0.5%であるから真
空下でC脱酸のみではOが数十ppm 存在し、公知の手法
に従えばAl による脱酸が必要となる。軸受鋼において
はCは0.9%前後であるが、このときのOは7〜10
ppm であるからAl による仕上脱酸が必要である。Al
を使用した場合Al23 として鋼中に非金属介在物とし
て残留することは前記した通りである。また水素による
脱酸はアーク炉等通常の溶解炉で行なっても構わない
が、必要に応じて脱硫や成分調整と同時に進行させても
構わないから、取鍋精錬炉(LF)で行なうと好都合で
ある。水素による脱酸後は水素が飽和点25ppm 程度と
なるので、脱酸終了後RH,DH,流摘脱ガス等による
真空脱ガスを行なうと数ppm 以下まで低下させることが
出来る。
[0006] O 2 - showed [C] equilibrium diagram, P CO
= 1 is equilibrium under atmospheric pressure, and P CO = 0.2 is equilibrium under vacuum. In this case, C1% finally gives 10ppm
Only molten steel containing oxygen to the extent of cutting is obtained. However, C in molten steel differs depending on its application and performance,
Since carburizing steel and tough steel have C of 0.2 to 0.5%, deoxidation with Al is necessary according to the known method, if only C deoxidation under vacuum causes O of several tens of ppm. . In bearing steel, C is around 0.9%, but O at this time is 7 to 10
Since it is ppm, finishing deoxidation with Al is necessary. Al
When Al is used, Al 2 O 3 remains as non-metallic inclusions in the steel as described above. Also, deoxidation with hydrogen may be performed in an ordinary melting furnace such as an arc furnace, but it may be carried out simultaneously with desulfurization and component adjustment if necessary, so it is convenient to perform it in a ladle refining furnace (LF). Is. Since hydrogen reaches a saturation point of about 25 ppm after deoxidation with hydrogen, vacuum degassing such as RH, DH and flow degassing after completion of deoxidation can reduce it to several ppm or less.

【0007】[0007]

【実施例】図3に示す取鍋(1) に炭素を0.03%含有
する軸受鋼の溶鋼(5) 70tを充填し、デカンテーショ
ンによる脱スラグの後、アーク電極(3) を取付けた蓋
(2)を装着しCaO,CaF2 を造滓材として投入した
後、溶鋼(5) を1600℃に加熱保持するとともに該取
鍋(1) 底部に取付けたポーラスプラグ(4) を介して水素
ガス吹込みをおこなう。水素ガスの吹込み速度は200
0l/分とし、吹込み時間は70分行なった。上記水素
ガス吹込みによる脱酸効果を表1に示す。
[Example] The ladle (1) shown in FIG. 3 was filled with 70 tons of molten steel (5) of bearing steel containing 0.03% of carbon, and the arc electrode (3) was attached after deslagging by decantation. lid
After mounting (2) and introducing CaO and CaF 2 as slag material, the molten steel (5) was heated and held at 1600 ° C and hydrogen was passed through the porous plug (4) attached to the bottom of the ladle (1). Blow gas. The blowing rate of hydrogen gas is 200
The blowing time was 70 minutes. Table 1 shows the deoxidizing effect by the hydrogen gas injection.

【表1】 [Table 1]

【0008】表1によれば水素ガス吹込みのみで溶鋼中
濃度が1〜4ppm に低下し、効率的に脱酸が行なわ
れることが認められる。この後Cを投入し、C濃度を軸
受鋼(SUJ2)として所定のレベルに調整し、その後
RH脱ガスを40分行なったところ水素が1.2ppm と
なり、鋼として問題のないレベルまで低下した。
According to Table 1, it is recognized that the O concentration in the molten steel is reduced to 1 to 4 ppm only by blowing hydrogen gas, and the deoxidation is efficiently performed. After that, C was charged to adjust the C concentration to a predetermined level as the bearing steel (SUJ2), and then RH degassing was carried out for 40 minutes, and then hydrogen became 1.2 ppm, which decreased to a level at which there was no problem as steel.

【0009】[0009]

【発明の効果】したがって本発明においてはAl23
生成が防止され、かつ溶鋼中の脱酸が効率的に行なわれ
る。
Therefore, in the present invention, the formation of Al 2 O 3 is prevented, and deoxidation in molten steel is efficiently performed.

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

【図1】平衡線図[1] O - H equilibrium diagram

【図2】−〔C〕平衡線図FIG. 2 is an O- [C] equilibrium diagram.

【図3】本実施例に用いた取鍋の模式断面図FIG. 3 is a schematic cross-sectional view of a ladle used in this example.

【符号の説明】[Explanation of symbols]

1 取鍋 2 蓋 3 アーク電極 4 ポーラスプラグ 5 溶鋼 1 Ladle 2 Lid 3 Arc electrode 4 Porous plug 5 Molten steel

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】溶鋼中に水素ガスを吹込み脱酸を行なうこ
とを特徴とする鋼の精錬方法
1. A method for refining steel, which comprises degassing by injecting hydrogen gas into molten steel.
【請求項2】溶解炉とは別体の容器に溶鋼を充填し、該
溶鋼中に水素ガスを吹込み脱酸を行なうことを特徴とす
る鋼の精錬方法
2. A method for refining steel, characterized in that molten steel is filled in a container separate from the melting furnace, and hydrogen gas is blown into the molten steel for deoxidation.
【請求項3】溶鋼中に水素ガスを吹込んで脱酸を行なっ
た後、真空脱ガスを行なうことを特徴とする請求項1ま
たは請求項2に記載の鋼の精錬方法
3. The method for refining steel according to claim 1, wherein hydrogen gas is blown into the molten steel to perform deoxidation, and then vacuum degassing is performed.
JP12090093A 1993-04-23 1993-04-23 Method for refining steel Withdrawn JPH06306441A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12090093A JPH06306441A (en) 1993-04-23 1993-04-23 Method for refining steel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12090093A JPH06306441A (en) 1993-04-23 1993-04-23 Method for refining steel

Publications (1)

Publication Number Publication Date
JPH06306441A true JPH06306441A (en) 1994-11-01

Family

ID=14797782

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12090093A Withdrawn JPH06306441A (en) 1993-04-23 1993-04-23 Method for refining steel

Country Status (1)

Country Link
JP (1) JPH06306441A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109628705A (en) * 2019-02-26 2019-04-16 太原科技大学 A kind of RH method of refining of low carbon stainless steel
CN113337669A (en) * 2021-05-18 2021-09-03 北京科技大学 Method for strengthening electric furnace smelting by bottom blowing hydrogen

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109628705A (en) * 2019-02-26 2019-04-16 太原科技大学 A kind of RH method of refining of low carbon stainless steel
CN113337669A (en) * 2021-05-18 2021-09-03 北京科技大学 Method for strengthening electric furnace smelting by bottom blowing hydrogen

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Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20000704