JPH02267213A - Method for vacuum-decarbonizing molten steel - Google Patents
Method for vacuum-decarbonizing molten steelInfo
- Publication number
- JPH02267213A JPH02267213A JP8643289A JP8643289A JPH02267213A JP H02267213 A JPH02267213 A JP H02267213A JP 8643289 A JP8643289 A JP 8643289A JP 8643289 A JP8643289 A JP 8643289A JP H02267213 A JPH02267213 A JP H02267213A
- Authority
- JP
- Japan
- Prior art keywords
- molten steel
- vacuum
- decarburization
- tuyeres
- decarbonizing
- 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 39
- 239000010959 steel Substances 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 17
- 238000007664 blowing Methods 0.000 claims abstract description 14
- 239000011261 inert gas Substances 0.000 claims abstract description 9
- 238000005261 decarburization Methods 0.000 claims description 27
- 238000007654 immersion Methods 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 8
- 229910052799 carbon Inorganic materials 0.000 abstract description 8
- 238000005262 decarbonization Methods 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 8
- 230000007423 decrease Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 238000009849 vacuum degassing Methods 0.000 description 5
- 238000003756 stirring Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 239000006104 solid solution Substances 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000009489 vacuum treatment Methods 0.000 description 1
Landscapes
- Treatment Of Steel In Its Molten State (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
この発明は、R1−1真空脱ガス装置により溶鋼を脱炭
する方法に係り、特に極低炭素域(C<80pan)で
の脱炭速度を上昇させて脱炭限界値を低下させる真空脱
炭方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a method for decarburizing molten steel using an R1-1 vacuum degassing device, particularly for increasing the decarburization rate in the extremely low carbon range (C<80pan). The present invention relates to a vacuum decarburization method for lowering the decarburization limit value.
従来の技術
溶鋼の真空処理には、一般にDH設備、RH股備が利用
されている。Conventional Technology Generally, DH equipment and RH equipment are used for vacuum processing of molten steel.
DH設備では取鍋固溶鋼に1本の浸漬管を有する真空槽
を浸漬し、槽内を減圧して溶鋼を吸い上げ、ざらに真空
槽自体を上下運動させることにより溶鋼流動を生じさせ
て脱ガスを促進させる方法で真空処理が行なわれる。In DH equipment, a vacuum tank with one immersion tube is immersed in a ladle of solid solution steel, the pressure inside the tank is reduced to suck up the molten steel, and the vacuum tank itself is roughly moved up and down to create a flow of molten steel and degas it. Vacuum treatment is performed in a manner that promotes.
これに対し、R1−1設備では2本の浸漬管を有する真
空槽を溶鋼内に浸漬し、槽内を減圧して溶鋼を吸い上げ
るとともに、2本の浸漬管のうち溶鋼を吸い上げる方を
上昇管、他方を溶鋼下降管として機能させ、取鍋と真空
槽の間で溶鋼を循環させて真空脱ガス処理が行なわれる
。On the other hand, in the R1-1 equipment, a vacuum tank with two immersion tubes is immersed in molten steel, the pressure inside the tank is reduced and the molten steel is sucked up, and the one of the two immersion tubes that sucks up the molten steel is connected to the riser tube. , the other is made to function as a molten steel downcomer pipe, and molten steel is circulated between the ladle and the vacuum tank to perform vacuum degassing treatment.
このRH真空脱ガス処理においては、上昇管より不活性
ガスを吹込み、そのガスの浮力を利用して溶鋼の環流を
補助するのが一般的で必る(特開昭55−161023
号公報稔照)。In this RH vacuum degassing process, it is common and necessary to blow inert gas from the riser pipe and use the buoyancy of the gas to assist the circulation of the molten steel (Japanese Patent Laid-Open No. 55-161023
Publication No. Minoru).
ところで最近、深絞り用鋼板、電!i鋼板等の極低炭素
鋼に対して、深絞り値、伸びの向上を目的とした超極低
炭素鋼化の要求が高まってきている。By the way, recently, steel sheets for deep drawing, electric! There is an increasing demand for ultra-low carbon steels such as i-steel plates to improve deep drawing value and elongation.
しかし、現状のCV−RH−CCプロセスでのRH脱炭
限界は平均15ppm程度でおり、050ppm程度か
らの脱炭速度は急激に低下することから、処理時間の延
長は避けられない。However, the RH decarburization limit in the current CV-RH-CC process is about 15 ppm on average, and the decarburization rate rapidly decreases from about 0.5 ppm, so an extension of the processing time is unavoidable.
この極低炭素域での脱炭速度の低下原因は、反応界面積
の低下が主たるものであり、反応界面積を十分確保すれ
ば平行値に近いC値が得られ、脱炭速度の向上がはから
れる。The main cause of the decrease in the decarburization rate in this extremely low carbon region is the decrease in the reaction interface area.If the reaction interface area is secured sufficiently, a C value close to the parallel value can be obtained, and the decarburization rate can be improved. It can be measured.
しかし、RH設備で実施されている上昇管からの不活性
ガスの吹込み方法では、溶鋼の環流効果は得られても、
真空槽内の溶鋼撹拌効果が少ないため反応界面積を十分
に確保し得ない。また、この方法は細い浸漬管にガスを
吹込むため、臨界ガス量以上にガスを吹込むと吹抜けを
起し、溶鋼循環速度が制約を受けるという問題もある。However, with the method of injecting inert gas from the riser pipe implemented in RH equipment, although the molten steel circulation effect can be obtained,
Since the molten steel stirring effect in the vacuum chamber is low, a sufficient reaction interface area cannot be secured. Furthermore, since this method blows gas into a narrow immersion tube, there is also the problem that blow-by occurs when gas is blown in an amount exceeding a critical gas amount, and the molten steel circulation speed is restricted.
なお、特開昭56−44711号公報には、真空槽の浴
面下に設けた羽口または煉瓦よりCO2ガスを吹込む方
法が開示されているが、この方法はCO2ガスを吹込む
ことによって吸熱反応を起し真空槽の耐火物寿命の延長
をはかることを目的としたものであり、真空槽内での溶
鋼撹拌を目的としたものではないため、脱炭効率の向上
効果はほとんど得られない。Note that Japanese Patent Application Laid-open No. 56-44711 discloses a method of blowing CO2 gas through tuyeres or bricks provided below the bath surface of a vacuum tank; The purpose is to cause an endothermic reaction and extend the life of the refractories in the vacuum chamber, and it is not intended to stir molten steel in the vacuum chamber, so it has little effect on improving decarburization efficiency. do not have.
発明が解決しようとする課題
この発明は、RH真空脱ガス設備による溶鋼の脱炭方法
において、極低炭素域での脱炭速度の低下原因でおる反
応界面積の低下の問題を解決し、極低炭素域での脱炭速
度を上昇させて脱炭限界値を低下させ得る溶鋼の真空脱
炭方法を提案しようとするものである。Problems to be Solved by the Invention The present invention solves the problem of a decrease in the reaction interface area, which is the cause of the decrease in the decarburization rate in the extremely low carbon range, in a method for decarburizing molten steel using RH vacuum degassing equipment, and This paper attempts to propose a vacuum decarburization method for molten steel that can increase the decarburization rate in the low carbon region and lower the decarburization limit value.
課題を解決するための手段
この発明に係る溶鋼の真空脱炭方法は、RH真空槽の溶
鋼浸漬部に横吹羽口を設け、溶鋼脱炭中に前記羽口より
Ar、 N2等の不活性ガスを溶鋼中に吹込むことに
より、極低炭素域(C<aoppm)における脱炭限界
値を低下させることを要旨とするものである。Means for Solving the Problems In the vacuum decarburization method of molten steel according to the present invention, a horizontal blowing tuyere is provided in the molten steel immersion part of the RH vacuum tank, and an inert gas such as Ar or N2 is injected from the tuyere during decarburization of the molten steel. The purpose is to lower the decarburization limit value in the ultra-low carbon range (C<aoppm) by injecting C into molten steel.
作 用
R)−f真空槽の溶鋼浸漬部に設けた横吹羽口よりAr
、 N2等の不活性ガスを溶鋼脱炭中に吹込むことに
より、該真空槽内の溶鋼が撹拌され、その結果反応界面
積が十分に確保され、IIR炭速度の上昇がはかられる
。Effect R)-f Ar
By injecting an inert gas such as , N2, etc. into molten steel decarburization, the molten steel in the vacuum chamber is agitated, and as a result, a sufficient reaction interface area is ensured and the IIR coal velocity is increased.
実 施 例
第1図および第2図はこの発明方法を実施するためのR
H真空槽を示す概略図であり、第1図は正面図、第2図
は平面図で、(1)は真空槽、(2)上昇管、(3)は
下降管、(4)は不活性ガス吹込み用横吹き羽口である
。Embodiment FIGS. 1 and 2 show R for carrying out the method of this invention.
FIG. 1 is a schematic diagram showing a vacuum chamber; FIG. 1 is a front view, and FIG. 2 is a plan view, in which (1) is a vacuum chamber, (2) is an ascending pipe, (3) is a downcomer pipe, and (4) is a free pipe. This is a side blowing tuyere for active gas injection.
すなわち、この発明方法を実施する場合は、真空槽(1
)の側壁に横吹き羽口(4)を槽内溶鋼(5)の浴面下
に位@するごとく設置する。この横吹き羽口は、真空槽
の周壁に例えば4個、あるいは3個適当間隔をおいて設
置すればよい。勿論、羽口の個数は限定されるものでは
ないが、真空槽内の溶鋼の撹拌効果を高めるためには複
数個等間隔に設置するのが好ましい。That is, when carrying out the method of this invention, a vacuum chamber (1
) A horizontal blowing tuyere (4) is installed on the side wall of the tank so that it is below the bath surface of the molten steel (5) in the tank. For example, four or three horizontal blowing tuyeres may be installed at appropriate intervals on the peripheral wall of the vacuum chamber. Of course, the number of tuyeres is not limited, but in order to enhance the effect of stirring the molten steel in the vacuum chamber, it is preferable to install a plurality of tuyere at equal intervals.
上記真空槽(1)において、溶鋼脱炭中に横吹き羽口(
4)からAr、 N2等の不活性ガスを吹込むと、真
空槽内の溶1i11(5)が撹拌され反応界面積が増加
し脱炭速度が上昇する。In the vacuum chamber (1), the side blowing tuyere (
When an inert gas such as Ar or N2 is blown from step 4), the solution 1i11(5) in the vacuum chamber is stirred, the reaction interfacial area increases, and the decarburization rate increases.
次に、RH真空ll?:lガス装置の真空槽に第1図に
示すごとく横吹き羽口を4個設置し、脱炭中にこの4個
の羽口からトータル533Kg/皿のA、を吹込んだ結
果を第2図に示す。Next, RH vacuum ll? :L Four horizontal blowing tuyeres were installed in the vacuum chamber of the gas equipment as shown in Figure 1, and a total of 533 kg/dish of A was blown from these four tuyeres during decarburization. As shown in the figure.
なお比較のため、横吹き羽口からArガスを吹込まずに
脱炭した結果(従来例)を第3図に示す。For comparison, FIG. 3 shows the results of decarburization (conventional example) without blowing Ar gas through the side blowing tuyere.
第2図および第3図より明らかなごとり1.真空槽の側
壁よりkを吹込むことによって、極低炭素域での脱炭速
度の低下は僅かであり、到達Cも10pplT1以下と
、Ar吹込みを行なわない従来に比べ低下している。As is clear from Figures 2 and 3, 1. By injecting K from the side wall of the vacuum chamber, the decarburization rate decreases only slightly in the extremely low carbon range, and the achieved C is less than 10 pplT1, which is lower than in the conventional case where Ar is not injected.
また、到IPcoは従来0.03atmで必ったのが、
槽内Ar撹拌によりO,Olatmまで低下している。In addition, IPco was previously required to be 0.03 atm, but
Due to Ar agitation in the tank, the temperature has decreased to O, Olatm.
槽内真空度から計算されるPCQ O,004atmよ
りはまだ高位にあるものの、さらに羽口数を増加して槽
内強撹拌を実施することによりPcoを低下することが
でき、到達Cの低下、脱炭速度の向上がはかられる。Although it is still higher than PCQ O,004atm calculated from the vacuum degree in the tank, by increasing the number of tuyeres and performing strong stirring in the tank, Pco can be lowered, reducing the amount of C reached and eliminating The charcoal speed will be improved.
発明の詳細
な説明したごとく、この発明方法によれば、RH真空脱
ガス設備の真空槽の側壁に設けた横吹き羽口より不活性
ガスを吹込むことによって、真空槽固溶allを撹拌す
ることができるので、反応界面積を十分に確保すること
ができ、極低炭素域での脱炭速度を上昇できる結果、脱
炭限界値を低下することができ、超極低炭素鋼の製造に
大なる効果を奏するものである。As described in detail of the invention, according to the method of this invention, the solid solution in the vacuum tank is stirred by blowing inert gas through the side blowing tuyere provided on the side wall of the vacuum tank of the RH vacuum degassing equipment. As a result, it is possible to secure a sufficient reaction interface area, increase the decarburization rate in the ultra-low carbon range, and lower the decarburization limit value, making it suitable for the production of ultra-low carbon steel. It has great effects.
第1図はこの発明方法を実/Jf!iするためのR]−
1真空槽を示す概略平面図、第2図は同上真空槽の概略
平面図、第3図はこの発明の実施例における脱炭状況を
示す図、第4図は同じ〈従来の脱炭状況を示す図である
。
1・・・真空槽 2・・・上昇管3・・
・下降管 4・・・横吹き羽口5・・・
溶鋼
代理人 弁理士 押田良久帰琵]
第3図
時
間(min)
第1図
第2図
第4図
間(min)Figure 1 shows the method of this invention in practice/Jf! R for i]-
1 is a schematic plan view showing a vacuum chamber, FIG. 2 is a schematic plan view of the same vacuum chamber, FIG. 3 is a view showing a decarburization situation in an embodiment of the present invention, and FIG. 4 is a diagram showing the same (conventional decarburization situation) FIG. 1...Vacuum chamber 2...Rising pipe 3...
・Downcomer pipe 4...Side blowing tuyere 5...
Molten Steel Agent Patent Attorney Yoshihisa Oshida Figure 3 Time (min) Figure 1 Figure 2 Figure 4 Time (min)
Claims (1)
に前記羽口よりAr、N_2等の不活性ガスを溶鋼中に
吹込むことにより、極低炭素域(C<80ppm)にお
ける脱炭限界値を低下させることを特徴とする溶鋼の真
空脱炭方法。A horizontal blowing tuyere is provided in the molten steel immersion part of the RH vacuum tank, and inert gases such as Ar and N_2 are blown into the molten steel through the tuyere during decarburization of the molten steel. A vacuum decarburization method for molten steel characterized by lowering the decarburization limit value.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8643289A JPH02267213A (en) | 1989-04-05 | 1989-04-05 | Method for vacuum-decarbonizing molten steel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8643289A JPH02267213A (en) | 1989-04-05 | 1989-04-05 | Method for vacuum-decarbonizing molten steel |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02267213A true JPH02267213A (en) | 1990-11-01 |
Family
ID=13886747
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8643289A Pending JPH02267213A (en) | 1989-04-05 | 1989-04-05 | Method for vacuum-decarbonizing molten steel |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02267213A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994029488A1 (en) * | 1993-06-04 | 1994-12-22 | Nippon Steel Corporation | Method of manufacturing low carbon molten steel by vacuum degasification and decarbonization |
-
1989
- 1989-04-05 JP JP8643289A patent/JPH02267213A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1994029488A1 (en) * | 1993-06-04 | 1994-12-22 | Nippon Steel Corporation | Method of manufacturing low carbon molten steel by vacuum degasification and decarbonization |
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