JPH11320052A - Method for controlling fluid of molten steel in continuous casting - Google Patents

Method for controlling fluid of molten steel in continuous casting

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Publication number
JPH11320052A
JPH11320052A JP13806398A JP13806398A JPH11320052A JP H11320052 A JPH11320052 A JP H11320052A JP 13806398 A JP13806398 A JP 13806398A JP 13806398 A JP13806398 A JP 13806398A JP H11320052 A JPH11320052 A JP H11320052A
Authority
JP
Japan
Prior art keywords
molten steel
flow
electromagnetic induction
meniscus
continuous casting
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Withdrawn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
JP13806398A
Other languages
Japanese (ja)
Inventor
Takehiko Fuji
健彦 藤
Hajime Hasegawa
一 長谷川
Eiichi Takeuchi
栄一 竹内
Takahiro Isono
貴宏 磯野
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 JP13806398A priority Critical patent/JPH11320052A/en
Publication of JPH11320052A publication Critical patent/JPH11320052A/en
Withdrawn legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a control method of the fluid of molten steel, with which impurity at the loose side of a slab with a bending type continuous caster is reduced. SOLUTION: An electromagnetic induction stirring device is disposed at an interval between (Lo +H/2) to (2m-H/2), (wherein, LO is the distance from a meniscus of the molten steel to a position, at which the solidified interface in the loose side becomes perpendicular, and H is the height of the electromagnetic induction stirring device). Circular flow in the horizontal direction along the solidified interface is formed in the molten steel with the electromagnetic induction stirring device, and the intensity of the circular flow is changed over into strong flow and weak flow in the following frequency (f): 1 sec<=f<=(10<3> .W/ F<1/2> ) sec. (wherein, W is casting width and F is the thrust of the electromagnetic induction stirring device). Further, instead of change-over into the strong flow and the weak flow, the circular flow can be changed over from one direction to the reverse direction.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】湾曲モールド型連続鋳造やベ
ンディング型連続鋳造においては、垂直方向に溶鋼を注
入した後、鋳片を横向きに移動させる。以下本明細書で
はこれ等を湾曲式連続鋳造と総称する。本発明はこれ等
の湾曲式連続鋳造でスラブを製造する際の連続鋳造方法
に関する。
BACKGROUND OF THE INVENTION In the continuous casting of a curved mold or a bending type, after casting molten steel in a vertical direction, a slab is moved laterally. Hereinafter, these are collectively referred to as curved continuous casting. The present invention relates to a continuous casting method for producing a slab by such curved continuous casting.

【0002】[0002]

【従来の技術】図3は従来の湾曲式連続鋳造の模式図
で、(A)は縦断面図、(B),(C)はイ−イ横断面
図である。図中1は鋳型、2は溶鋼、3は凝固シェル、
4は浸漬ノズル、5−1,5−2は電磁誘導撹拌装置、
6はフラックス、11は凝固シェルと溶鋼の界面であ
る。
2. Description of the Related Art FIG. 3 is a schematic view of a conventional curved continuous casting, in which (A) is a longitudinal sectional view, and (B) and (C) are II sectional views. In the figure, 1 is a mold, 2 is molten steel, 3 is a solidified shell,
4 is an immersion nozzle, 5-1 and 5-2 are electromagnetic induction stirrers,
6 is a flux, and 11 is an interface between the solidified shell and the molten steel.

【0003】浸漬ノズル4から供給される溶鋼2には前
工程例えばタンディッシュ内のスラグ介在物が混入し易
く、また注入に際して溶鋼を覆っているフラックス6を
巻き込み易い。また鋳造に際して浸漬ノズル4内には不
活性ガスを吹き込む事が多いため、溶鋼2はガス気泡を
含有する場合がある。これ等の介在物やフラックスやガ
ス気泡(本明細書では不純物と略記する)は浸漬ノズル
から供給される溶鋼の注入流2'に巻き込まれて溶鋼中
に潜入する。
In the molten steel 2 supplied from the immersion nozzle 4, slag inclusions in a previous process, for example, a tundish, are apt to be mixed in, and a flux 6 covering the molten steel is liable to be involved at the time of injection. Since an inert gas is often blown into the immersion nozzle 4 during casting, the molten steel 2 may contain gas bubbles. These inclusions, flux and gas bubbles (abbreviated as impurities in the present specification) are involved in the molten steel injection flow 2 ′ supplied from the immersion nozzle and infiltrate into the molten steel.

【0004】溶鋼中に潜入した不純物は溶鋼よりも軽い
ために溶鋼2中を浮上し、フラックス6に達しフラック
スに吸収されて溶鋼から除去される。図3(A)の7及
び8は不純物の例である。図3(A)のフィックスサイ
ド側の凝固シェル界面に存在する不純物8は、浮上を妨
げるものがないため溶鋼2中を浮上して除去される。し
かしルーズサイド側の凝固シェル界面に存在する不純物
7は、その上部に張り出した凝固シェル3がその上昇を
妨げる。この結果不純物7は除去されないで凝固シェル
に捕えられて、凝固完了後の鋳片の欠陥となるという問
題点がある。
The impurities infiltrated into the molten steel float in the molten steel 2 because they are lighter than the molten steel, reach the flux 6 and are absorbed by the flux and removed from the molten steel. 7A and 8 in FIG. 3A are examples of impurities. The impurities 8 existing at the solidified shell interface on the fixed side in FIG. 3A are removed by floating in the molten steel 2 because there is nothing that hinders the floating. However, the impurities 7 present at the solidified shell interface on the loose side are prevented from rising by the solidified shell 3 projecting upward. As a result, there is a problem in that the impurities 7 are not removed and are caught by the solidified shell, resulting in defects of the slab after the solidification is completed.

【0005】湾曲型連続鋳造に特定されるものではない
が、鋳造中の鋳片の長辺面を挟むようにリニアモーター
式の移動磁場を発生させる電磁誘導撹拌装置を配し、凝
固シェル内部の溶鋼に流れの強さや向きが常に変わらな
い定常旋回流を形成する技術が知られている。図3の5
−1及び5−2はこの電磁誘導撹拌装置の例である。電
磁誘導撹拌装置5−1は移動磁場を形成する事により5
−1側の溶鋼を矢印9−1方向に移動させ、電磁誘導撹
拌装置5−2は5−1が形成した移動磁場とは移動方向
が逆の移動磁場を形成する事により5−2側の溶鋼を矢
印9−2方向に移動させる。この結果、溶鋼2には図の
如く例えば左回りの定常の旋回流が形成される。
[0005] Although not limited to curved continuous casting, a linear motor type electromagnetic induction stirrer for generating a moving magnetic field of a linear motor type is provided so as to sandwich the long side surface of the slab being cast. 2. Description of the Related Art A technique for forming a steady swirling flow in which the strength and direction of a flow do not always change in molten steel is known. 3 in FIG.
-1 and 5-2 are examples of this electromagnetic induction stirrer. The electromagnetic induction stirrer 5-1 generates a moving magnetic field to generate 5
The −1 side molten steel is moved in the direction of arrow 9-1, and the electromagnetic induction stirrer 5-2 forms a moving magnetic field having a moving direction opposite to that of the moving magnetic field formed by 5-1. The molten steel is moved in the direction of arrow 9-2. As a result, a steady swirling flow, for example, counterclockwise, is formed in the molten steel 2 as shown in the figure.

【0006】本発明者等は、電磁誘導撹拌装置5−1,
5−2により未凝固溶鋼2に矢印9−1,9−2の定常
の旋回流を形成し、図3のルーズサイド側の不純物7を
この旋回流によってフィックスサイド側に移行させ、浮
上除去する試みを行なった。しかしながら本発明者等の
知見によると定常の旋回流を用いるこの方法では不純物
7はフィックスサイドに回らないで局所的に集積し、不
純物7が集積した部分が鋳片に発生するという問題点が
発生する。この理由は詳かではないが、定常の旋回流に
は局所的に流速が大きい所と例えば図3(C)の7’で
示した淀んだ所があり、不純物7はフィックスサイド側
に移動しないで、淀んだ所7’に集積するためと想考さ
れる。
The present inventors have proposed an electromagnetic induction stirrer 5-1.
A steady swirling flow of arrows 9-1 and 9-2 is formed in the unsolidified molten steel 2 by 5-2, and the impurities 7 on the loose side in FIG. 3 are transferred to the fixed side by this swirling flow and floated and removed. An attempt was made. However, according to the knowledge of the present inventors, this method using a steady swirling flow causes a problem that the impurities 7 are locally accumulated without turning to the fixed side, and a portion where the impurities 7 are accumulated is generated in a slab. I do. Although the reason for this is not clear, the steady swirling flow has a locally high flow velocity portion and a stagnant portion indicated by 7 'in FIG. 3C, for example, and the impurity 7 does not move to the fixed side. It is conceived that this is to accumulate in the stagnant place 7 '.

【0007】スラブ連続鋳造とは異なるが、特開平3−
44858号公報は、円柱または角柱ビレットを連続鋳
造で製造する際に、鋳片中心部のポロシティを伴う最終
凝固部を改善する方法として、例えば鋳型下16m〜2
7mの最終凝固部近傍に電磁誘導撹拌装置を配し、向き
が反転する旋回流を用いる事を記載している。しかしこ
の方法は最終凝固部を改善する方法であるため、電磁誘
導撹拌装置を配する場所は最終凝固部近傍の鋳型下16
〜27mであり、例えば鋳型内溶鋼のメニスカスから2
m以内の、連続鋳造装置の上方に配することはない。
Although different from slab continuous casting, Japanese Patent Application Laid-Open
No. 44858 discloses a method for improving a final solidified portion accompanied by porosity at the center of a slab when a cylindrical or prismatic billet is manufactured by continuous casting.
It describes that an electromagnetic induction stirrer is arranged near the final solidification part of 7 m, and a swirling flow whose direction is reversed is used. However, since this method is a method for improving the final solidified portion, the place where the electromagnetic induction stirrer is provided is located below the mold near the final solidified portion.
From the meniscus of the molten steel in the mold.
m above the continuous casting device.

【0008】[0008]

【発明が解決しようとする課題】本発明は、湾曲式連続
鋳造機でスラブを製造する際に、ルーズサイド側のスラ
ブの不純物を低減し、かつこれ等の欠陥の集積の発生を
低減防止する事ができる溶鋼の連続鋳造方法の提供を課
題としている。
SUMMARY OF THE INVENTION The present invention reduces the impurities in the slab on the loose side and reduces the occurrence of the accumulation of such defects when the slab is manufactured by the curved continuous casting machine. It is an object of the present invention to provide a continuous casting method for molten steel capable of performing the above-mentioned tasks.

【0009】[0009]

【課題を解決するための手段および発明の実施の形態】
図1は本発明の例の模式説明図で、(A)は縦断面、
(B),(C),(D)は横断面図である。本発明は湾
曲式連続鋳造機によるスラブ連続鋳造に関する。本発明
においては、溶鋼のメニスカス10までの距離が下記
(1)式のLとなる高さに鋳片の長辺面を挟むように配
された一対の電磁誘導撹拌装置を用いる。即ち、溶鋼の
メニスカスと電磁誘導撹拌装置の装置高さの中心までの
距離Lが、下記(1)式の範囲内となる位置に電磁誘導
撹拌装置を配する。
Means for Solving the Problems and Embodiments of the Invention
FIG. 1 is a schematic explanatory view of an example of the present invention, and FIG.
(B), (C), and (D) are cross-sectional views. The present invention relates to continuous slab casting by a curved continuous casting machine. In the present invention, a pair of electromagnetic induction stirrers arranged so as to sandwich the long side surface of the slab at a height where the distance to the meniscus 10 of the molten steel is L in the following formula (1) is used. That is, the electromagnetic induction stirrer is disposed at a position where the distance L between the meniscus of the molten steel and the center of the height of the electromagnetic induction stirrer is within the range of the following expression (1).

【0010】 L0+(H/2)<L<2−(H/2)…………(1) 図1(A)でP点より上方では、ルーズサイドの凝固シ
ェルと溶鋼の界面11は上広がりに傾斜し、P点より下
方では下広がりに傾斜し、P点で垂直になっている。
(1)式でL0はメニスカス10からP点までの距離で
ある。尚P点は計算により、あるいはブレークアウトし
た鋳片の頂部を測定する事等により、鋳造条件と関連づ
けて把握されている。また(1)式でHは電磁誘導撹拌
装置5−1あるいは5−2のそれぞれの装置の高さであ
る。
L 0 + (H / 2) <L <2- (H / 2) (1) Above point P in FIG. 1 (A), the interface 11 between the loose-side solidified shell and the molten steel Is inclined upward and downward below the point P, and downward at the point P.
In the equation (1), L 0 is the distance from the meniscus 10 to the point P. The point P is grasped in association with the casting conditions by calculation or by measuring the top of the broken-out slab. In the equation (1), H is the height of each of the electromagnetic induction stirrers 5-1 and 5-2.

【0011】P点より上方では凝固シェルの界面11近
傍に不純物があっても界面11は上広がりであるため上
昇浮上が妨げられることなく、浮上除去されて、凝固シ
ェルに把えられる事がない。このため電磁誘導撹拌装置
はL0+(H/2)よりも下方に配する。また溶鋼の注
入流2’に巻き込まれた品質管理上問題となる不純物は
メニスカスから2m下方までは溶鋼中に潜入するが、そ
れ以上深くまで潜入する事はない。このため電磁誘導撹
拌装置は2−(H/2)よりも上方に配する。
Above the point P, even if impurities are present in the vicinity of the interface 11 of the solidified shell, the interface 11 is widened, so that the rising and floating is not hindered, the floating is removed and the solidified shell is not caught by the solidified shell. . For this reason, the electromagnetic induction stirrer is disposed below L 0 + (H / 2). Further, impurities that are involved in quality control and are involved in the molten steel injection flow 2 ′ infiltrate into the molten steel up to 2 m below the meniscus, but do not infiltrate deeper. For this reason, the electromagnetic induction stirrer is disposed above 2- (H / 2).

【0012】本発明では、凝固シェル3の内部の未凝固
溶鋼2に、凝固シェルとの界面に沿って水平に流れる旋
回流9−1,9−2を形成する。この旋回流は、電磁誘
導撹拌装置5−2が形成する移動磁場の移動方向を、電
磁誘導撹拌装置5−1が形成する移動磁場の移動方向と
逆向きの移動方向となるように通電する事によって得ら
れる。
In the present invention, swirling flows 9-1 and 9-2 which flow horizontally along the interface with the solidified shell are formed in the unsolidified molten steel 2 inside the solidified shell 3. This swirling flow is energized so that the moving direction of the moving magnetic field formed by the electromagnetic induction stirrer 5-2 is opposite to the moving direction of the moving magnetic field formed by the electromagnetic induction stirrer 5-1. Obtained by

【0013】本発明では更に、この旋回流の強さを、図
1(B)の強流9−1,9−2と図1(C)の弱流9−
1’,9−2’に周期的に切り替える。この切り替え
は、電磁誘導撹拌装置5−1,5−2に流す電流値を、
高い電流値(アンペア)と低い電流値(アンペア)とに
周期的に切り替える事により行なう事ができる。
Further, in the present invention, the strength of the swirling flow is determined by comparing the strength of the swirling flow with the strong flows 9-1 and 9-2 shown in FIG. 1B and the weak flow 9--9 shown in FIG.
It is periodically switched to 1 ', 9-2'. This switching is performed by changing the current value flowing through the electromagnetic induction stirrers 5-1 and 5-2,
This can be performed by periodically switching between a high current value (ampere) and a low current value (ampere).

【0014】本発明では更に、強流と弱流に切り替える
周期f(秒)を下記(2)式の範囲内にする。
Further, in the present invention, the period f (second) for switching between the strong flow and the weak flow is set within the range of the following equation (2).

【0015】 1秒≦f≦(103・W/√F)秒…………(2) 撹拌の周期fが1秒未満では、溶鋼2の旋回移動は移動
磁場の強さの変化に追従できないで、溶鋼の流れは所望
の如くに変えられないために効果が小さい。本発明者等
は周期fを変えて電磁誘導撹拌を行い、製造した鋳片を
調査して不純物の集積の発生の有無を調査したが、周期
が(103・W/√F)秒以上で長時間過ぎる場合は鋳
片に不純物の集積が発生する事を知得した。この理由は
詳かではないが、周期が(103・W/√F)超で長く
なり過ぎると、9−1,9−2はまた9−1’,9−
2’は定常流の如くに流れて溶鋼の流れには淀む場所が
発生しこの部分に不純物が集積する事によるものと想考
される。
1 second ≦ f ≦ (10 3 · W / ΔF) seconds (2) When the stirring period f is less than 1 second, the turning movement of the molten steel 2 follows the change in the strength of the moving magnetic field. Otherwise, the flow of molten steel is less effective because it cannot be changed as desired. The present inventors performed electromagnetic induction stirring while changing the cycle f, and examined the produced slabs to determine whether or not the accumulation of impurities occurred. However, when the cycle was (10 3 · W / √F) seconds or more, It has been found that if the time is too long, accumulation of impurities occurs in the slab. The reason for this is not clear, but if the period is too long, exceeding (10 3 · W / √F), 9-1 and 9-2 will also become 9-1 'and 9-
It is thought that 2 'flows like a steady flow and a place where stagnation occurs in the flow of molten steel, and impurities accumulate in this portion.

【0016】更に本発明者等の知見によると、例えば図
1(B)の9−1,9−2の非旋回流を、9−1,9−
2とは旋回方向が反対の、図1Dの9−1”,9−2”
の向きに周期的に切り替えると不純物の低減、不純物の
集積部分の発生防止に顕著な効果が得られる。即ち本発
明はまた、電磁誘導撹拌装置を前記(1)式と同じ下記
(3)式のように配し、前記(2)式と同じ下記(4)
式の周期で、旋回流の向きを左旋回と右旋回に周期的に
切り替える方法である。尚、式(3)及び式(4)の如
くに特定する理由は、前記式(1)及び式(2)におけ
る特定理由と同様である。
Further, according to the findings of the present inventors, for example, the non-swirl flow of 9-1 and 9-2 in FIG.
2, the turning direction is opposite to that of FIG.
When the direction is periodically switched, the remarkable effects can be obtained in the reduction of impurities and the prevention of generation of an impurity accumulation portion. That is, in the present invention, the electromagnetic induction stirrer is arranged as in the following formula (3), which is the same as the formula (1), and the following formula (4), which is the same as the formula (2)
This is a method in which the direction of the swirling flow is periodically switched between left turning and right turning in the cycle of the formula. In addition, the reason for specifying as in Expressions (3) and (4) is the same as the reason for specifying in Expressions (1) and (2).

【0017】 L0+H/2<L<2−H/2………(3) 但しL:溶鋼のメニスカスと電磁誘導撹拌装置の装置高
さの中心までの距離(m) L0:溶鋼のメニスカスから凝固シェルと溶鋼の界面が
垂直になる位置まででの距離(m) H:電磁誘導撹拌装置の装置高さ(m) 1秒≦f≦(103・W/√F)秒………(4) 但しf:一方向向きの旋回流と逆方向向きの旋回流の周
期(秒) W:鋳造幅(m) F:電磁誘導撹拌装置の推力(N/m2
L 0 + H / 2 <L <2-H / 2 (3) where L: distance between the meniscus of the molten steel and the center of the height of the electromagnetic induction stirrer (m) L 0 : the molten steel Distance from meniscus to position where interface between solidified shell and molten steel is vertical (m) H: Height of electromagnetic induction stirrer (m) 1 sec ≤ f ≤ (10 3 · W / √F) sec ... … (4) where f: cycle (seconds) of the swirl flow in one direction and the swirl flow in the opposite direction W: casting width (m) F: thrust of the electromagnetic induction stirrer (N / m 2 )

【0018】[0018]

【実施例】本発明者等は、曲げ半径が10.5mの湾曲
型連続鋳造機を用いて、板幅:1000mm、板厚が2
50mmの低炭素鋼スラブを1.3m/分の鋳造速度で
連続鋳造する際に、本発明を試験した。尚浸漬ノズルは
吐出角が下向き25度の吐出孔を有する浸漬ノズルで、
内部にはノズル閉塞防止用のArガスを5L/分の割合
で吹き込んだ。電磁誘導撹拌装置は幅1500mm、高
さHが250mmのもので、装置高さの1/2の箇所が
溶鋼メニスカスから1500mm下方の位置に配されて
いる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The inventors of the present invention used a curved continuous casting machine having a bending radius of 10.5 m and a sheet width of 1000 mm and a sheet thickness of 2 mm.
The invention was tested when continuously casting a 50 mm low carbon steel slab at a casting speed of 1.3 m / min. The immersion nozzle is an immersion nozzle having a discharge hole with a discharge angle of 25 degrees downward,
Ar gas for preventing nozzle blockage was blown into the inside at a rate of 5 L / min. The electromagnetic induction stirrer has a width of 1500 mm and a height H of 250 mm, and a half of the height of the device is arranged at a position 1500 mm below the molten steel meniscus.

【0019】本発明者等は、鋳造開始から全鋳造量の約
1/4までに相当する第1鋳造期は電磁誘導撹拌は全く
行わない従来法とし、約1/4〜約1/2の第2鋳造期
は10kN/m2で図3(B)の定常の旋回流を形成し
て撹拌し、約1/2〜約3/4を鋳造する第3鋳造期は
第1図の(B)と(C)を3秒周期で切り替える本発明
を行なった。尚第3鋳造期の(B)の9−1,9−2の
推力は10kN/m2で(C)の9−1’,9−2’の
推力は5kN/m2である。また第3鋳造期後から鋳造
終了までの第4鋳造期には第1図の(B)と(D)を3
秒周期で切り替える本発明を行なった。尚第4鋳造期の
(B)の9−1,9−2と(D)の9−1”,9−2”
の推力は何れも10kN/m2である。
The present inventors assumed that the conventional method in which no electromagnetic induction stirring was performed during the first casting period corresponding to about one-fourth of the total casting amount from the start of casting, and about one-fourth to about one-half In the second casting period, a steady swirling flow shown in FIG. 3B is formed at 10 kN / m 2 and agitated, and about 1/2 to about 3/4 is cast. ) And (C) are switched at a cycle of 3 seconds. Note thrust of 9-1 and 9-2 of the third molding stage (B) is at 10kN / m 2 (C) of 9-1 ', 9-2' thrust is 5 kN / m 2. In the fourth casting period from the third casting period to the end of casting, (B) and (D) of FIG.
The present invention has been implemented in which switching is performed in a second cycle. Incidentally, 9-1 and 9-2 of (B) and 9-1 "and 9-2" of (D) in the fourth casting period.
Are 10 kN / m 2 .

【0020】鋳造終了後に、各鋳造期の鋳片から試料を
採取し、ルーズサイド側の長辺表面下20mm〜40m
mの部分の不純物の存在量を評価した。図2はその結果
である。尚図中幅端部は、鋳片の短辺から40mmの位
置で、幅中央は、鋳片幅の中央部である。
After completion of the casting, a sample was taken from the slab at each casting period, and was 20 mm to 40 m below the long side surface on the loose side.
The abundance of impurities in the portion m was evaluated. FIG. 2 shows the result. The width end in the figure is a position 40 mm from the short side of the slab, and the center of the width is the center of the slab width.

【0021】図2にみられる如く、電磁誘導撹拌を行わ
ない第1鋳造期は、不純物評価は全体に高く、不純物量
が多い。従来の定常の旋回流を形成する第2鋳造期は、
幅中央部と1方の幅端部の不純物評点は低く良好である
が、旋回流の下流になる幅端部の不純物評点が極めて高
く、この部分に不純物が集積している。本発明の第3鋳
造期、第4鋳造期は、第1鋳造期に比べて不純物の評点
が顕著に低く、かつ不純物の集積もない。
As shown in FIG. 2, during the first casting period in which electromagnetic induction stirring is not performed, the evaluation of impurities is generally high and the amount of impurities is large. The second casting stage, which forms a conventional steady swirl flow,
The impurity score at the center of the width and one of the width ends is low and good, but the impurity score at the width end downstream of the swirling flow is extremely high, and impurities are accumulated in this portion. In the third casting period and the fourth casting period of the present invention, the scores of impurities are remarkably lower than those in the first casting period, and there is no accumulation of impurities.

【0022】本発明の第3鋳造期、第4鋳造期において
不純物が少なく且つ不純物の集積がない理由は詳かでは
ないが、本発明の例えば強い旋回流により発生した淀み
の場所は次の弱い旋回流では淀みとはならないで、従っ
て強い旋回流の淀みに集まった不純物は次の弱い旋回流
により洗い流されるために、不純物の集積の発生を防止
したものと推考される。同様に例えば右回りの旋回流に
より発生した淀みに集まった不純物は、次の左回りの旋
回流により洗い流されるために、不純物の集積の発生を
防止したものと推考される。上記の理由で、本発明では
まんべんなく溶鋼が流動し、この流動により、図3の不
純物7は図3の不純物8の位置に移動し、あるいは点線
で図示した如く、凝固シェルと溶鋼の界面11から離れ
て浮上除去されたものと想考される。
Although the reason why the amount of impurities is small and there is no accumulation of impurities in the third casting period and the fourth casting period of the present invention is not clear, the location of stagnation generated by, for example, a strong swirling flow of the present invention is the following weak point. It is presumed that the stagnation does not occur in the swirling flow, and the impurities collected in the stagnation of the strong swirling flow are washed away by the next weak swirling flow, thereby preventing the accumulation of impurities. Similarly, for example, impurities collected in the stagnation generated by the clockwise swirling flow are washed away by the next counterclockwise swirling flow, and thus it is presumed that the accumulation of impurities is prevented. For the above reason, in the present invention, the molten steel flows evenly, and this flow causes the impurity 7 in FIG. 3 to move to the position of the impurity 8 in FIG. It is thought that it was separated from the surface.

【0023】[0023]

【発明の効果】本発明によると、湾曲式連続鋳造機でス
ラブを製造する際に、スラブのルーズサイド側の不純物
を低減する事ができる。また不純物の集積部が発生する
事を有効に防止する事ができる。
According to the present invention, when a slab is manufactured by a curved continuous casting machine, impurities on the loose side of the slab can be reduced. In addition, it is possible to effectively prevent generation of an impurity accumulation portion.

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

【図1】は本発明の溶鋼流動の制御方法の説明図。FIG. 1 is an explanatory diagram of a method for controlling molten steel flow according to the present invention.

【図2】は従来の湾曲式連続鋳造の模式説明図。FIG. 2 is a schematic explanatory view of a conventional curved continuous casting.

【図3】は本発明の効果の説明図。FIG. 3 is an explanatory diagram of an effect of the present invention.

【符号の説明】[Explanation of symbols]

1:鋳型、 2:溶鋼、 2’:溶鋼の注入流、 3:
凝固シェル、 4:浸漬ノズル、 5(5−1,5−
2):電磁誘導撹拌装置、 6:フラックス、7:不純
物、 8:不純物、 9:(9−1,9−2,9−
1’,9−2’,9−1”,9−2”):溶鋼の移動方
向及び流れの強さ、 10:溶鋼のメニスカス、 1
1:凝固シェルと溶鋼の界面。
1: Mold, 2: Molten steel, 2 ': Injection flow of molten steel, 3:
Solidified shell, 4: immersion nozzle, 5 (5-1, 5-
2): electromagnetic induction stirrer, 6: flux, 7: impurity, 8: impurity, 9: (9-1, 9-2, 9-)
1 ′, 9-2 ′, 9-1 ″, 9-2 ″): moving direction and flow strength of molten steel, 10: meniscus of molten steel, 1
1: Interface between solidified shell and molten steel.

フロントページの続き (72)発明者 磯野 貴宏 兵庫県姫路市広畑区富士町1番地 新日本 製鐵株式会社広畑製鐵所内Continuation of the front page (72) Inventor Takahiro Isono 1 Fujimachi, Hirohata-ku, Himeji-shi, Hyogo Nippon Steel Corporation Hirohata Works

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】湾曲式連続鋳造機によるスラブ連続鋳造に
際し、溶鋼のメニスカスまでが下記(1)式のLとなる
高さに鋳片の長辺面を挟むように配された一対の電磁誘
導撹拌装置を用いて、凝固シェル内部の溶鋼に凝固シェ
ルとの界面に沿って水平に流れる旋回流を形成し、かつ
該旋回流の強さを下記(2)式の周期fで強流と弱流に
切り替えることを特徴とする、連続鋳造における溶鋼流
動の制御方法。 L0+H/2<L<2−H/2………(1) 但しL:溶鋼のメニスカスと電磁誘導撹拌装置の装置高
さの中心までの距離(m) L0:溶鋼のメニスカスからルーズサイドの凝固シェル
と溶鋼の界面が垂直になる位置までの距離(m) H:電磁誘導撹拌装置の装置高さ(m) 1秒≦f≦(103・W/√F)秒…………(2) 但しf:強旋回流と弱旋回流の周期(秒) W:鋳造幅(m) F:電磁誘導撹拌装置の推力(N/m2
In a slab continuous casting by a curved continuous casting machine, a pair of electromagnetic inductions arranged so as to sandwich a long side surface of a slab at a height where the meniscus of molten steel becomes L in the following formula (1). Using a stirrer, a swirl flow that flows horizontally along the interface with the solidified shell is formed in the molten steel inside the solidified shell, and the strength of the swirl flow is set to a strong flow and a weak flow at a period f of the following equation (2). A method for controlling molten steel flow in continuous casting, characterized by switching to flow. L 0 + H / 2 <L <2-H / 2 (1) where L: distance from the meniscus of molten steel to the center of the height of the electromagnetic induction stirrer (m) L 0 : loose from meniscus of molten steel Distance to the position where the interface between the solidified shell on the side and the molten steel is vertical (m) H: Device height of the electromagnetic induction stirrer (m) 1 second ≤ f ≤ (10 3 · W / √F) seconds ... … (2) where f: cycle of strong swirling flow and weak swirling flow (second) W: casting width (m) F: thrust of electromagnetic induction stirrer (N / m 2 )
【請求項2】湾曲式連続鋳造機によるスラブ連続鋳造に
際し、溶鋼のメニスカスまでが下記(3)式のLとなる
高さに鋳片の長辺面を挟むように配された一対の電磁誘
導撹拌装置を用いて、凝固シェル内部の溶鋼に凝固シェ
ルとの界面に沿って水平に流れる旋回流を形成し、かつ
該旋回流の旋回方向を下記(4)式の周期fで切り替え
ることを特徴とする、連続鋳造における溶鋼流動の制御
方法。 L0+H/2<L<2−H/2…………(3) 但しL:溶鋼のメニスカスと電磁誘導撹拌装置の装置高
さの中心までの距離(m) L0:溶鋼のメニスカスから凝固シェルと溶鋼の界面が
垂直になる位置まででの距離(m) H:電磁誘導撹拌装置の装置高さ(m) 1秒≦f≦(103・W/√F)秒…………(4) 但しf:一方向向きの旋回流と逆方向向きの旋回流の周
期(秒) W:鋳造幅(m) F:電磁誘導撹拌装置の推力(N/m2
In a continuous slab casting by a curved continuous casting machine, a pair of electromagnetic inductions arranged so as to sandwich the long side surface of the slab at a height where the meniscus of the molten steel becomes L in the following formula (3). Using a stirrer, a swirling flow that flows horizontally along the interface with the solidified shell is formed in the molten steel inside the solidified shell, and the swirling direction of the swirling flow is switched at a period f in the following equation (4). A method for controlling the flow of molten steel in continuous casting. L 0 + H / 2 <L <2-H / 2 (3) where L: distance (m) from the meniscus of the molten steel to the center of the height of the electromagnetic induction stirrer L 0 : from the meniscus of the molten steel Distance to the position where the interface between the solidified shell and molten steel is vertical (m) H: Height of the electromagnetic induction stirrer (m) 1 sec ≤ f ≤ (10 3 · W / √F) sec ... (4) where f: cycle (seconds) of the swirl flow in one direction and the swirl flow in the reverse direction (second) W: casting width (m) F: thrust of electromagnetic induction stirrer (N / m 2 )
JP13806398A 1998-05-20 1998-05-20 Method for controlling fluid of molten steel in continuous casting Withdrawn JPH11320052A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13806398A JPH11320052A (en) 1998-05-20 1998-05-20 Method for controlling fluid of molten steel in continuous casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13806398A JPH11320052A (en) 1998-05-20 1998-05-20 Method for controlling fluid of molten steel in continuous casting

Publications (1)

Publication Number Publication Date
JPH11320052A true JPH11320052A (en) 1999-11-24

Family

ID=15213119

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13806398A Withdrawn JPH11320052A (en) 1998-05-20 1998-05-20 Method for controlling fluid of molten steel in continuous casting

Country Status (1)

Country Link
JP (1) JPH11320052A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016168603A (en) * 2015-03-12 2016-09-23 Jfeスチール株式会社 Continuous casting method of steel
WO2020249004A1 (en) * 2019-06-12 2020-12-17 宝山钢铁股份有限公司 Electromagnetic stirring device and method for secondary cooling zone during slab continuous casting

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016168603A (en) * 2015-03-12 2016-09-23 Jfeスチール株式会社 Continuous casting method of steel
WO2020249004A1 (en) * 2019-06-12 2020-12-17 宝山钢铁股份有限公司 Electromagnetic stirring device and method for secondary cooling zone during slab continuous casting
US11772153B2 (en) 2019-06-12 2023-10-03 Baoshan Iron & Steel Co., Ltd. Electromagnetic stirring device and method for secondary cooling zone during slab continuous casting

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