JPH03104814A - Ladle refining method - Google Patents
Ladle refining methodInfo
- Publication number
- JPH03104814A JPH03104814A JP24051689A JP24051689A JPH03104814A JP H03104814 A JPH03104814 A JP H03104814A JP 24051689 A JP24051689 A JP 24051689A JP 24051689 A JP24051689 A JP 24051689A JP H03104814 A JPH03104814 A JP H03104814A
- Authority
- JP
- Japan
- Prior art keywords
- molten steel
- ladle
- gas
- gaseous
- cap
- 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
- 238000000034 method Methods 0.000 title claims description 18
- 238000007670 refining Methods 0.000 title claims description 14
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 57
- 239000010959 steel Substances 0.000 claims abstract description 57
- 238000003756 stirring Methods 0.000 claims abstract description 14
- 239000002893 slag Substances 0.000 claims abstract description 10
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 32
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 16
- 239000001569 carbon dioxide Substances 0.000 claims description 7
- 239000007789 gas Substances 0.000 abstract description 47
- 238000002347 injection Methods 0.000 abstract description 5
- 239000007924 injection Substances 0.000 abstract description 5
- 238000007667 floating Methods 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 3
- 239000000463 material Substances 0.000 abstract description 3
- 238000007664 blowing Methods 0.000 abstract description 2
- 239000007792 gaseous phase Substances 0.000 abstract 2
- 239000000155 melt Substances 0.000 abstract 1
- 238000006467 substitution reaction Methods 0.000 abstract 1
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical group [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 13
- 229910052786 argon Inorganic materials 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000007872 degassing Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 229910001882 dioxygen Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 101100084040 Neurospora crassa (strain ATCC 24698 / 74-OR23-1A / CBS 708.71 / DSM 1257 / FGSC 987) ppi-1 gene Proteins 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur 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、スラグに電極を浸漬して溶鋼をサブマージ
アーク加熱しつつ、撹拌ガスを溶鋼に吹き込む取鍋精錬
方法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a ladle refining method in which an electrode is immersed in slag to submerged arc heat the molten steel and a stirring gas is blown into the molten steel.
[従来の技術]
近年、ブリキ板等の表面処理鋼板や自動車車体の外板に
低窒素鋼が使用されるようになり、この種の鋼板を迅速
かつ安定に製造する技術が要望されている。低窒素鋼板
用の薄板スラブを連続鋳造するには、転炉工程から鋳造
工程に至るまでの間に、大気中の窒素ガスによる溶鋼の
汚染、すなわち[N] ピックアップを防止し、溶鋼の
窒素含有量を抑制する必要がある。[Prior Art] In recent years, low-nitrogen steel has come to be used for surface-treated steel sheets such as tin plates and outer panels of automobile bodies, and there is a demand for technology for rapidly and stably manufacturing this type of steel sheet. In order to continuously cast thin slabs for low-nitrogen steel sheets, from the converter process to the casting process, contamination of the molten steel by nitrogen gas in the atmosphere, that is, preventing [N] pick-up, is necessary to reduce the nitrogen content of the molten steel. It is necessary to control the amount.
通常、転炉出鋼された溶鋼は、溶存酸素[0]量が高く
、硫黄[S]や燐[P]等の不純物量も高いので、鋳造
前に取鍋精錬法(LF法)により脱酸、脱硫、脱燐処理
する。Usually, molten steel tapped from a converter has a high amount of dissolved oxygen [0] and a high amount of impurities such as sulfur [S] and phosphorus [P], so it is removed by ladle refining method (LF method) before casting. Treat with acid, desulfurization, and dephosphorization.
従来の取鍋精錬方法は、取鍋に蓋を被せ、鍋内をアルゴ
ンガスで置換し、アルゴンガス雰囲気下で溶鋼をサブマ
ージアーク加熱しつつ、撹拌ガスおよび副原料を溶鋼に
インジエクションする。In the conventional ladle refining method, the ladle is covered with a lid, the inside of the ladle is replaced with argon gas, and stirring gas and auxiliary raw materials are injected into the molten steel while submerged arc heating the molten steel in an argon gas atmosphere.
[発明が解決しようとする課題]
しかしながら、従来の取鍋精錬方法においては、撹拌ガ
スのインジエクションにより取鍋内の圧力が変動し、蓋
の間隙から外気が取鍋内に侵入するので、浮上ガスによ
る溶鋼露出面が侵入外気で汚染され、[N] ピックア
ップが生じる。[Problems to be Solved by the Invention] However, in the conventional ladle refining method, the pressure inside the ladle fluctuates due to the injection of stirring gas, and outside air enters the ladle through the gap in the lid. The exposed surface of the molten steel is contaminated by the intruding outside air due to the floating gas, and [N] pickup occurs.
このため、取鍋精錬方法により低窒素鋼を製造する場合
は、下記(1)〜(3)に示すように、従来から種々の
[N] ビックアップ防止対策がなされている。For this reason, when producing low-nitrogen steel by the ladle refining method, various [N] surprise prevention measures have been conventionally taken, as shown in (1) to (3) below.
(1)不活性ガスシール法
(2)減圧処理法(V−K I P)
(3)電磁撹拌法
しかしながら、上記(1)〜(3)のいずれの方峡もラ
ンニングコスト及び設備コストが高く、丈用向ではない
。このため、取鍋精錬後に、更にRH脱ガス設備にて溶
鋼を脱窒素処理する必要がある。(1) Inert gas seal method (2) Vacuum treatment method (V-K I P) (3) Electromagnetic stirring method However, all of the above (1) to (3) have high running costs and equipment costs. , not suitable for length. Therefore, after ladle refining, it is necessary to further denitrify the molten steel using an RH degassing facility.
この発明は、かかる事情に鑑みてなされたものであって
、溶鋼の[N] ビックアップを低コストで確実に防止
することができる取鍋精錬方法を提供することを目的と
する。The present invention has been made in view of the above circumstances, and an object thereof is to provide a ladle refining method that can reliably prevent [N] surprise-up of molten steel at low cost.
[課題を解決するための手段]
この発明に係る取鍋精錬方法は、スラグに電極を浸漬し
て溶鋼をサブマージアーク加熱しつつ、撹拌ガスを溶鋼
に吹き込む取鍋精錬方法において、二酸化炭素ガスを取
鍋蓋内に供給し、溶鋼と接する気相を二酸化炭素ガス雰
囲気とすることを特徴とする。[Means for Solving the Problems] A ladle refining method according to the present invention is a ladle refining method in which electrodes are immersed in slag to submerged arc heat the molten steel and stirring gas is blown into the molten steel. It is characterized by supplying it into the ladle lid and creating a carbon dioxide gas atmosphere in the gas phase that comes into contact with the molten steel.
発明者等は、種々のガスを用いて取鍋内を置換し、[N
] ピックアップについて調べた。その結果、二酸化炭
素ガスのような酸素元素を成分に有するガスが置換ガス
に適していることが判明した。The inventors replaced the inside of the ladle with various gases and discovered that [N
] I researched the pickup. As a result, it was found that a gas containing oxygen as a component, such as carbon dioxide gas, is suitable as a replacement gas.
この場合に、酸素ガスで取鍋内雰囲気を置換することも
考えられる。しかしながら、酸素ガスは、[N] ピッ
クアップの防止効果は高いが、脱酸剤添加量が増大して
アルミナが多量に発生し、溶鋼の清浄度が低下するので
、置換ガスとしては不適である。In this case, it is also possible to replace the atmosphere inside the ladle with oxygen gas. However, although oxygen gas has a high effect of preventing [N] 2 pickup, it is not suitable as a replacement gas because the amount of deoxidizing agent added increases, a large amount of alumina is generated, and the cleanliness of molten steel decreases.
[作用]
この発明に係る取鍋精錬方注においては、撹拌ガスを溶
鋼に吹き込むと、撹拌ガスの浮上領域にてスラグが湯而
から排除され、溶鋼面が部分的に露出し、取鍋内に侵入
した大気により溶鋼が汚染されようとするが、酸化性ガ
スである二酸化炭素ガスが気相・液相界面に存在するの
で、界面における[0]濃度が高まり、侵入大気による
溶鋼の[N] ビックアップが有効に防止される。[Function] In the ladle refining method according to the present invention, when stirring gas is blown into the molten steel, slag is removed from the molten steel in the floating region of the stirring gas, the molten steel surface is partially exposed, and the inside of the ladle is removed. The molten steel tends to be contaminated by the air that has entered the atmosphere, but since carbon dioxide gas, which is an oxidizing gas, exists at the gas-liquid interface, the [0] concentration at the interface increases, and the [N ] Bick-up is effectively prevented.
?実施例]
以下、添付の図面を参照しながら、この発明の実施例に
ついて只体的に説明する。? Embodiments] Hereinafter, embodiments of the present invention will be briefly described with reference to the accompanying drawings.
未脱酸出鋼された溶鋼が取鍋に収容され、LF設備に搬
入されている。取鍋は走行台車に搭載され、走行台車の
軌条はLF設備からRH脱ガス設備および鋳造工場にそ
れぞれ延びている。取鍋内溶鋼はスラグで覆われている
。取鍋には蓋が被せられている。蓋にはガス供給管およ
びガス排気管がそれぞれ取り付けられ、取鍋内のガスが
排気される一方で、CO■ガスが鍋内に供給されるよう
になっている。CO2ガス供給管の基端側には流量調節
弁が取り付けられている。更に、添加孔が蓋に設けられ
、合金材及び副原料が鍋内に投入添加されるようになっ
ている。Undeoxidized tapped molten steel is stored in a ladle and transported to the LF equipment. The ladle is mounted on a traveling truck, and the rails of the traveling truck extend from the LF equipment to the RH degassing equipment and the foundry, respectively. The molten steel in the ladle is covered with slag. The ladle is covered with a lid. A gas supply pipe and a gas exhaust pipe are respectively attached to the lid, so that the gas in the ladle is exhausted while the CO2 gas is supplied into the ladle. A flow rate control valve is attached to the base end side of the CO2 gas supply pipe. Furthermore, an addition hole is provided in the lid, so that alloy materials and auxiliary materials can be added into the pot.
3本の電極が蓋の中央近傍を貫通し、各先端が溶鋼を覆
うスラグ層に浸漬されている。また、インジエクション
ランスが蓋の周縁近傍を貫通し、その先端部が溶鋼中に
浸漬されている。インジエクションランスの基端側はア
ルゴンガス供給源およびバウダ供給源に接続されている
。Three electrodes pass through the lid near the center, each tip immersed in the slag layer covering the molten steel. Further, an injection lance passes through the vicinity of the periphery of the lid, and its tip is immersed in the molten steel. The proximal end of the injection lance is connected to an argon gas supply source and a border supply source.
次に、低窒素鋼を取鍋精錬処理する場合について説明す
る。Next, the case of ladle refining of low nitrogen steel will be explained.
処理前の溶鋼は未脱酸状態であり、[C] 量が約40
0ppll,[0]量が約600ppm,[N]量が約
10〜15ppI1である。取鍋がLP設備に到着する
と、これに蓋を披せ、CO2ガスを供給し、取鍋内をC
O2ガス雰囲気とする。一方、添加孔から鍋内溶鋼に造
滓材および金属アルミニウムを添加し、電極に通電し、
溶鋼をサブマージアーク加熱する。これにより、溶鋼が
脱酸され、[0] ffiが約1〜5 ppmのレベル
まで低下する。The molten steel before treatment is in an undeoxidized state, and the amount of [C] is approximately 40
0 ppll, [0] amount is about 600 ppm, and [N] amount is about 10 to 15 ppI1. When the ladle arrives at the LP equipment, the lid is placed on it, CO2 gas is supplied, and the inside of the ladle is heated to C.
Create an O2 gas atmosphere. Meanwhile, slag material and metal aluminum are added to the molten steel in the pot through the addition hole, and electricity is applied to the electrode.
Submerged arc heating of molten steel. This deoxidizes the molten steel and reduces the [0]ffi to a level of about 1-5 ppm.
CO2ガス置換が完了すると、インジエクションランス
にアルゴンガスを供給し、溶鋼をガス撹拌する。撹拌ガ
スの吹き込みにより、鍋内の圧力が変動し、外気が蓋の
間隙から内部に侵入する。When CO2 gas replacement is completed, argon gas is supplied to the injection lance to gas-stir the molten steel. By blowing in stirring gas, the pressure inside the pot fluctuates, and outside air enters the pot through the gap in the lid.
ところで、撹袢ガスが浮上する領域ではスラグが排除さ
れ、場面の一部に溶鋼が露出する。この溶鋼露出面に侵
入外気が接触すると、外気に含まれる窒素ガスが溶鋼に
溶け込もうとするが、気相中にCO2ガスが存在するの
で、気液界面における[0] レベルが高まり、溶鋼へ
の[N] ビックアップが有効に阻止される。これによ
り、処理後の溶鋼は、約15ppmの[N] 量となる
。By the way, slag is removed in the region where the stirring gas floats to the surface, and molten steel is exposed in a part of the scene. When the exposed surface of the molten steel comes into contact with the intruding outside air, the nitrogen gas contained in the outside air tries to dissolve into the molten steel, but since CO2 gas exists in the gas phase, the [0] level at the gas-liquid interface increases and the molten steel [N] Bickup to [N] is effectively prevented. As a result, the molten steel after treatment has a [N] content of approximately 15 ppm.
第1図は、横軸に処理時間をとり、縦軸に[N]ピック
アップ量をとって、CO2ガス雰囲気下の処理とアルゴ
ンガス雰囲気下の処理とを比較調査したグラフ図である
。図中にて、白丸はCO2ガス雰囲気下の処理(実施例
)の結果を、黒丸はアルゴンガス雰囲気下の処理(比較
例)の結果を、それぞれ示す。図から明らかなように、
比較例では1分間当り0.2ppmの[N] ピックア
ップ量の結果を得たのに対して、実施例では1分間当り
0.01〜0.02ppI1の[N] ピックアップ量
の結果となり、促来に比べて大幅に[N] ピックアッ
プ量を低減することができた。FIG. 1 is a graph showing a comparison between processing under a CO2 gas atmosphere and processing under an argon gas atmosphere, with the horizontal axis representing the processing time and the vertical axis representing the amount of [N] picked up. In the figure, white circles indicate the results of processing under a CO2 gas atmosphere (Example), and black circles indicate the results of processing under an argon gas atmosphere (Comparative Example). As is clear from the figure,
In the comparative example, a [N] pick-up amount of 0.2 ppm per minute was obtained, whereas in the example, a [N] pick-up amount of 0.01 to 0.02 ppm per minute was obtained. It was possible to significantly reduce the amount of [N] picked up compared to the conventional method.
なお、上記実施例では、CO2ガスをI■体で鍋内の置
換ガスに用いたが、本発明はこれに限られることなく、
CO2ガスにスチームガス(H20ガス)を混合して用
いてもよい。In the above example, CO2 gas was used as the replacement gas in the pot in the form of I2, but the present invention is not limited to this.
Steam gas (H20 gas) may be mixed with CO2 gas.
[発明の効果]
この発明によれば、二酸化炭素ガスを取鍋内に供給する
という簡単な操作により、溶鋼の[N]ビックアップを
低コストで確実に防止することができる。二酸化炭素ガ
スはアルゴンガスより安価であるため、低窒素鋼の製造
コストを従来より大軸に低減することができる。[Effects of the Invention] According to the present invention, [N] surprise of molten steel can be reliably prevented at low cost by the simple operation of supplying carbon dioxide gas into the ladle. Since carbon dioxide gas is cheaper than argon gas, the manufacturing cost of low nitrogen steel can be significantly reduced compared to conventional methods.
また、後工程のRH脱ガス処理を省略することができ、
製鋼工場内における物流の簡素化も図ることができる。In addition, the post-process RH degassing treatment can be omitted,
It is also possible to simplify logistics within the steel factory.
この結果、低窒素鋼の一貫生産体制において、大幅なコ
スト低減を実現することが期待される。As a result, it is expected that significant cost reductions will be realized in the integrated production system for low nitrogen steel.
第1図はこの発明の実施例の効果を説明するためのグラ
フ図である。FIG. 1 is a graph diagram for explaining the effects of the embodiment of the present invention.
Claims (1)
しつつ、撹拌ガスを溶鋼に吹き込む取鍋精錬方法におい
て、二酸化炭素ガスを取鍋蓋内に供給し、溶鋼と接する
気相を二酸化炭素ガス雰囲気とすることを特徴とする取
鍋精錬方法。In the ladle refining method, in which stirring gas is blown into the molten steel while electrodes are immersed in slag to submerged arc heat the molten steel, carbon dioxide gas is supplied into the ladle lid and the gas phase in contact with the molten steel is made into a carbon dioxide gas atmosphere. A ladle refining method characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24051689A JPH03104814A (en) | 1989-09-19 | 1989-09-19 | Ladle refining method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24051689A JPH03104814A (en) | 1989-09-19 | 1989-09-19 | Ladle refining method |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03104814A true JPH03104814A (en) | 1991-05-01 |
Family
ID=17060688
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24051689A Pending JPH03104814A (en) | 1989-09-19 | 1989-09-19 | Ladle refining method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03104814A (en) |
-
1989
- 1989-09-19 JP JP24051689A patent/JPH03104814A/en active Pending
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