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JPS5978763A - Method for controlling the level of molten steel in the mold in continuous casting - Google Patents

Method for controlling the level of molten steel in the mold in continuous casting

Info

Publication number
JPS5978763A
JPS5978763A JP19055282A JP19055282A JPS5978763A JP S5978763 A JPS5978763 A JP S5978763A JP 19055282 A JP19055282 A JP 19055282A JP 19055282 A JP19055282 A JP 19055282A JP S5978763 A JPS5978763 A JP S5978763A
Authority
JP
Japan
Prior art keywords
mold
level
molten steel
width
change
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
JP19055282A
Other languages
Japanese (ja)
Other versions
JPS6261383B2 (en
Inventor
Masami Tenma
天満 雅美
Akira Matsushita
昭 松下
Koichi Fujiki
藤木 紘一
Yoichi Azuma
陽一 東
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 JP19055282A priority Critical patent/JPS5978763A/en
Publication of JPS5978763A publication Critical patent/JPS5978763A/en
Publication of JPS6261383B2 publication Critical patent/JPS6261383B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/16Controlling or regulating processes or operations
    • B22D11/18Controlling or regulating processes or operations for pouring
    • B22D11/181Controlling or regulating processes or operations for pouring responsive to molten metal level or slag level

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Continuous Casting (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 この発明は、連続鋳造における鋳型内溶銅湯面レベル制
御方法に関し、詳しくは連続鋳造中に鋳型短片を移動せ
しめ鋳片幅を変更するεJ−片幅定幅変更時記湯面レベ
ル制御方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for controlling the level of molten copper in a mold in continuous casting, and more specifically, during continuous casting, when changing the width of a slab by moving a short mold piece during continuous casting. The present invention relates to a method for controlling a hot water surface level.

連続鋳造において、タンディツシュからの溶鋼の注入速
[争IJ fiiIを行い鋳型内の溶銅湯面レベル(以
下湯面レベルと云う)を一定に制御するには、一般に、
第1図に示すように、鋳型1に設置された鋳型自溶鋼湯
面レベル検出器2によシ鋳型1内の溶鋼3の湯面レベル
を検出し、この溶鋼湯面レベルが一定となるようにタン
ディツシュ4よシ注入される溶鋼3の注入速度をタンデ
ィツシュ4に設置されているスライディングノズル5ま
たはノズルストツノクー(図示せず)によって注入穴4
aの開度をW1v節することによシ、制御する方法が実
施されている。
In continuous casting, in order to control the injection speed of molten steel from the tundish to a constant level of the molten copper in the mold (hereinafter referred to as the molten metal level), generally,
As shown in Fig. 1, the mold self-molten steel level detector 2 installed in the mold 1 detects the level of the molten steel 3 in the mold 1, and makes sure that the molten steel level remains constant. The injection speed of the molten steel 3 injected through the tundish 4 is controlled by the sliding nozzle 5 or nozzle tip (not shown) installed in the tundish 4.
A method has been implemented in which the opening degree of a is controlled by W1v.

第2図は、前記第1図の制御機構を示すブロック図であ
シ、鋳型内湯面レベル検出器2で検出した鋳型内湯面レ
ベル信号は、レベル調節計6に入力され、該レベル調節
計6において、あらかじめ記憶せしめられていた鋳型内
湯面レベルの目標値と比較される。而して前記目標値の
湯面レベル(以下目標湯面レベルと云う)と差異が生じ
た場合にはレベル調節計6よシスライディングノズル5
の開度調節引7に信号が発せられ、開度調節計7によっ
てスライディングノズル50開度が調節され、タンディ
ツシュ4よシ鋳型1への溶鋼注入速度が適宜制御される
FIG. 2 is a block diagram showing the control mechanism shown in FIG. At this point, the mold level is compared with a pre-stored target value for the level of the mold. If there is a difference from the target hot water level (hereinafter referred to as the target hot water level), the level controller 6 and the system sliding nozzle 5
A signal is issued to the opening adjustment pull 7, the opening of the sliding nozzle 50 is adjusted by the opening controller 7, and the speed of pouring molten steel into the tundish 4 and the mold 1 is appropriately controlled.

上記開度調節計7は目標とするスライディングノズル開
度とスライディングノズル開度検出器8で検出したスラ
イディングノズル開度の実績値とを比較し、スライデン
グノズル5の駆動装置9に駆動指令信号を与え、スライ
ディングノズル開度が目標スライディングノズル開度と
なるように自動的に修正しつ\制御する機能を有してい
る。
The opening controller 7 compares the target sliding nozzle opening with the actual value of the sliding nozzle opening detected by the sliding nozzle opening detector 8, and sends a drive command signal to the driving device 9 of the sliding nozzle 5. It has a function to automatically correct and control the sliding nozzle opening degree so that it becomes the target sliding nozzle opening degree.

以上のように鋳型内湯面レベルを検出し、スライデイン
−グノズル開度を変更し、タンディツシュよ少の溶鋼注
入速度を制御することによシ、鋳型内湯面レベルを適正
に制御するよう構成されていた。
As described above, by detecting the level of the molten metal in the mold, changing the opening of the sliding nozzle, and controlling the molten steel injection speed at a rate smaller than that of the tundish, the level of the molten metal in the mold can be appropriately controlled. .

ところで周知の如く近年連続鋳造においてはその生産性
を向上させるために鋳造中に鋳片幅変更が頻繁に行われ
るようにな)、シかもその幅変更速度は一段と高速化さ
れる傾向となっている。該鋳片幅変更は例えば第2図に
示すように鋳型短片1aに油圧・電気シリンダー等を利
用した抑圧装置縦14を連結し、該抑圧装置14t−駆
動して短片la’を鋳片の幅方向に移動せしめることに
よって行われる。而して前記鋳片幅変更時は鋳型内の容
積が大きく変化し、このため、前記第2図に示す制御法
では前記容積変化に追従する精度の高い湯面レベル制御
が行えず鋳片の品質を悪化させたルブレークアウト等の
トラブルを生ずる等鋳片幅変更ケ実施するうえで大きな
障害となっていた。
By the way, as is well known, in recent years in continuous casting, in order to improve productivity, the slab width has been changed frequently during casting), and the speed at which the width can be changed has tended to become even faster. There is. To change the width of the slab, for example, as shown in FIG. 2, a vertical suppression device 14 using a hydraulic or electric cylinder is connected to the mold short piece 1a, and the suppression device 14t is driven to change the width of the short piece la' to the slab width. This is done by moving in the direction. When changing the width of the slab, the volume inside the mold changes significantly. Therefore, the control method shown in Fig. 2 cannot accurately control the level of the molten metal to follow the volume change, and the slab width changes. This was a major obstacle to changing the width of the slab, as it caused problems such as breakout, which deteriorated quality.

本発明は、前記欠点を除去し、鋳片幅変更時における鋳
型内容積の変化があっても、精贋良く、鋳型内の湯面レ
ベル制衝1を行うことを目的とするもので、その要旨は
、設定短片位1f!−1: ’f−基準とする鋳片幅変
更信号と、鋳造速度信号および設定鋳片厚から鋳型内容
積変化を経時的に算出し、計算出値に基いて、タンディ
ツシュの溶鋼注入速度制御を行々うことを特徴とする鋳
型内溶鋼湯面レベル制御方法である。
The object of the present invention is to eliminate the above-mentioned drawbacks and precisely control the level of molten metal in the mold even if the internal volume of the mold changes when changing the width of the slab. The gist is the setting short piece 1f! -1: 'f- Calculate the mold internal volume change over time from the standard slab width change signal, casting speed signal, and set slab thickness, and control the molten steel injection speed of the tundish based on the calculated value. This is a method for controlling the level of molten steel in a mold, which is characterized by:

次に本発明の1実施例を第3図に従って説明する。Next, one embodiment of the present invention will be described with reference to FIG.

第3図において、鋳型1には鋳型内の湯面レベルを検出
する検出器2および短片位置検出器10が設置され、ま
た、タンディツシュ4には、スライディングノズル5が
設置され、ノズル開度を調整することによって溶鋼の注
入速度が調節できる構成となっている。
In FIG. 3, the mold 1 is equipped with a detector 2 for detecting the level of hot water in the mold and a short piece position detector 10, and the tundish 4 is equipped with a sliding nozzle 5, which adjusts the nozzle opening. By doing so, the injection speed of molten steel can be adjusted.

湯面レベル検出器2としては、例えば鋳型1内に埋設さ
れた熱箪対金利用したものあるいは電磁式レベルセンサ
ーケ利用したもの等を、それぞれ単独で、又は縮合せて
用いればよい。又短片位置検出器10は短片1aの設定
位置よりの移動量、つまシ幅変更量を検出するもので、
短片1aの位置を直接検出するもの、あるいは前記押圧
装置14の移動量を検出し、該抑圧装置14の移動量か
ら短片位置を検出するものでもよい。本発明者等の経験
では、抑圧装置14にステッピングシリンダーを用いた
ものにおいては該ステッピングシリンダーに発せられる
指令パルスをカウントし、カウノ′トされた該ノぐルス
よシスチッピングシリンダー移動量ヲ検出する機構のも
のが高鞘朋の位置検出が可能とな逆効果的であった。
As the hot water level detector 2, for example, one using a heat sink buried in the mold 1 or one using an electromagnetic level sensor may be used alone or in combination. The short piece position detector 10 detects the amount of movement of the short piece 1a from the set position and the amount of change in the width of the tab.
It may be possible to directly detect the position of the short piece 1a or to detect the amount of movement of the pressing device 14 and detect the position of the short piece from the amount of movement of the suppressing device 14. In the experience of the present inventors, in the case where a stepping cylinder is used as the suppression device 14, the command pulses issued to the stepping cylinder are counted, and the amount of movement of the stepping cylinder is detected by the counted noggles. The one with the mechanism was counterproductive as it was possible to detect the position of Takaya Tomo.

11は鋳造速度検出器で鋳型1より引抜かれた鋳片15
の速[f例えば鋳片引抜用ロール(ピンチロール)の回
転速度′検出器等によって検出するととにより鋳造速度
が検出される。
Reference numeral 11 indicates the slab 15 pulled out from the mold 1 by a casting speed detector.
The casting speed is detected by the speed [f, for example, the rotational speed of a roll for drawing slabs (pinch rolls)' detected by a detector or the like.

さて、本実施例においては、前述の短片位置検出器10
からの鋳型幅変更信号aおよび鋳造速度検出器11から
の鋳造速[(M号すは、演算装置12に入力される。演
算装置12には設定鋳片厚、即ち、鋳造中の鋳片の厚み
が例えば鋳造指令条件よシ予め入力され、あるいは鋳型
1よシ引抜かれた鋳片15の厚みを実測し、その実測値
が入力されておシ、該鋳片厚と前記鋳型幅変更信号aお
よび鋳造速度信号すよシ、鋳型内容積変化(以下単に容
積変化と云う)を経時的に算出する。次に演算装置12
による前記容積変化斜−出法の一実施例について説明す
る。下記(1)式は鋳型1に目標湯面レベルまで溶鋼3
t−注入する場合の鋳型内溶鋼受入れ可能容積(以下、
可能容積と云う>vt算出する計算式を示すものである
Now, in this embodiment, the above-mentioned short piece position detector 10
The mold width change signal a from the casting speed detector 11 and the casting speed [(M) from the casting speed detector 11 are input to the calculation device 12. For example, the thickness may be input in advance according to the casting command conditions, or the thickness of the slab 15 drawn from the mold 1 may be actually measured and the measured value input, and the thickness of the slab and the mold width change signal a. and the casting speed signal, and the change in mold internal volume (hereinafter simply referred to as volume change) are calculated over time.Next, the calculation unit 12
An example of the volume change oblique output method will be described. Equation (1) below shows how to fill mold 1 with molten steel 3 up to the target level.
t-Capacity that can accommodate molten steel in the mold when injecting (hereinafter referred to as
This is a calculation formula for calculating the possible volume >vt.

V (m′′/min ) =W(Jn) X D(I
n) X U (m/m1n) −−(11但し、V:
可能容積 W:鋳型幅 l)二鋳片厚 U:鋳造速度 従って鋳片幅変更時の1鋳型幅Wの変化に伴う可能容積
Vを所定時間毎に算出するとその変化h(に対応する可
能容積が求められそれらを相互に比較することによって
可能容積Vの変化量、即ち本発明で称する容積変化が算
出される。第4図は鋳造速度が一定の条件下での鋳片幅
変更時の容積変化を図表化したもので範囲Xが幅拡大時
、範囲Yが幅縮小時を表わすものである。該第4図よシ
判るように算出単位時間△tを短かくすればする程算出
された容積変化は連続した直線状に表わされ、経時的な
容積変化を正確に算出できる。
V (m′′/min) = W(Jn)
n) X U (m/m1n) --(11 However, V:
Possible volume W: Mold width l) Slab thickness U: Casting speed Accordingly, when changing the slab width, if the possible volume V associated with a change in mold width W is calculated every predetermined time, the possible volume corresponding to the change h ( are determined and compared with each other to calculate the amount of change in the possible volume V, that is, the volume change referred to in the present invention. Figure 4 shows the volume when changing the slab width under the condition that the casting speed is constant. This graph shows the changes, where range X shows when the width is expanded and range Y shows when the width is reduced.As can be seen from Figure 4, the shorter the calculation unit time △t, the better the calculation. The volume change is expressed in a continuous straight line, and the volume change over time can be calculated accurately.

而して、演舞、装置12によって経時的に算出された前
記容積変化の算出値は加算装#13を介してスライディ
ングノズル5の開度調節計7に入力され、前記算出値に
基づいてスライディングノズルの開度を調整しタンディ
ツシュ4から鋳型1へ注入される溶鋼注入速度制御を行
う。例えば幅拡大時にeよ、可能容積は順次増大し、容
積変1ヒは第4図に示すように正の方向へ変化するため
にスライプ・イングノズル5の開度を太きくする方向に
制御する。尚、第3図の実施例では加算装置13に演算
装置12よシ容積変化の算出値を入力すると共にレベル
調節計6よシの信号が入力される。レベル調節計6では
、前述したように目標湯面レベルと湯面レベル計2によ
る湯面レベル実測値とが比較され、それに差異が生じた
場合にはその差位に応じた信号が発せられる。而して幅
変更時の鋳型幅あるいはlx造速匪の変更以外の外乱要
因によって湯面レベルが目標湯面レベルに対して差異を
生じた場合、加算装置13によって演算装置12よりの
算出値に、レベル調創′i言16よシの信号(変動値)
を加算して開LW調節計7に発する指令信号全自動的に
補正する。
Then, the calculated value of the volume change calculated over time by the performance device 12 is inputted to the opening degree controller 7 of the sliding nozzle 5 via the adding device #13, and the sliding nozzle is adjusted based on the calculated value. The opening degree of the molten steel is adjusted to control the injection speed of molten steel from the tundish 4 to the mold 1. For example, when the width is expanded, the possible volume (e) increases sequentially, and the volume change (1) changes in the positive direction as shown in Figure 4, so the opening degree of the sliding nozzle 5 is controlled in the direction of increasing . In the embodiment shown in FIG. 3, the calculated value of the volume change from the arithmetic unit 12 is inputted to the adding device 13, and the signal from the level controller 6 is also inputted thereto. As described above, the level controller 6 compares the target hot water level with the actual hot water level measured by the hot water level meter 2, and if a difference occurs, a signal corresponding to the difference is generated. If the melt level differs from the target melt level due to a disturbance factor other than a change in the mold width at the time of width change or a change in lx production speed, the addition device 13 adjusts the value calculated by the calculation device 12 to the value calculated by the calculation device 12. , level adjustment'i word 16 signal (fluctuation value)
The command signal issued to the open LW controller 7 is automatically corrected by adding the following.

以上のように本発明では短片1aの設定位置を基阜とす
る鋳型幅変更信号と鋳造速度信号および設定鋳片厚7J
\ら容積変化を経時的にη6出し、との算出値を基準と
してタンディツシュの溶鋼注入速度制御を行うもので、
本発明の実施によって容積変化の激しい幅変更時におい
てもスライディングノズル開度をただちに調整すること
ができ、鋳型内湯面レベルを乱すことなく、制御するこ
とカス可能となった。従って、本発明によれば鋳芥・中
鋳片幅変更時においても、非常に安定した鋳型内溶鋼湯
面レベル制御を行なうことか可能で、鋳片品質の向上や
、操業を安定させる上で、その効果は非常に太きい。
As described above, in the present invention, the mold width change signal, the casting speed signal, and the set slab thickness 7J are based on the set position of the short piece 1a.
The molten steel injection speed of the tanditshu is controlled based on the calculated value of the volume change over time, η6.
By implementing the present invention, the opening degree of the sliding nozzle can be immediately adjusted even when the width is changed due to a drastic change in volume, and it has become possible to control the molten metal level in the mold without disturbing it. Therefore, according to the present invention, even when changing the width of the cast iron or medium slab, it is possible to control the level of molten steel in the mold in a very stable manner, which is useful for improving slab quality and stabilizing operations. , the effect is very strong.

本発明者等の経験では20 #lI /minの速度で
幅変更を実施した場合、第2図に示す従来の制御方法で
は目標湯面レベルに対し、実測した湯面レベルは±20
前の変動が生じたが、本発明の実施で社±101111
以下となシ、極めて亮精度の湯面レベル制御が可能であ
ることが確認された。又本発明では幅変更速度が前記2
0M/minよシ晶〈なってもその精度は殆んど変化は
°なかったが従来の制御法では、目標湯面レベルと実測
湯面レベルの差はさらに太きくなシ実質的に幅変更がで
きなかつた。
In the experience of the present inventors, when the width is changed at a speed of 20 #lI /min, the actually measured hot water level is ±20% of the target hot water level using the conventional control method shown in Fig. 2.
However, with the implementation of this invention, the company ±101111
It was confirmed that it is possible to control the hot water level with extremely high precision as shown below. Further, in the present invention, the width change speed is
Even if the temperature decreases to 0M/min, there is almost no change in accuracy, but with the conventional control method, the difference between the target level and the measured level becomes even wider. I couldn't do it.

以上のように本発明の実用的効果iff極めて犬である
As described above, the practical effects of the present invention are extremely significant.

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

第1図は、鋳型内溶鋼湯面レベル制御を行うタンディツ
シュと鋳型の構成図、 第2図は、従来の鋳型内溶鋼湯面レベル制御方法を示す
ブロック図、 第3図は、本発明による鋳型内溶鋼湯百レベル制御方法
を示すブロック図、 第4図は、幅変更時の容積変化状況な示す図表である。 1・・・鋳型、2・・・鋳型内溶鋼湯面しベル検出器、
3−・・溶鋼、4・・・タンディツシュ、5・・・スラ
イディングノズル、6・・・レベル調節計、7・・・ス
ライディングノズル開度調節計、9・・・スライディン
グノズル駆動装置、10・・・短片位置検出器、11・
・・鋳造速度検出器、12・・・演算装置K(:、13
・・・力lη装置f114・・・押圧装置、15・・・
鋳片。 代理人 弁理士 秋 沢 政 光 潟I図 9 め、3図 名4図
Figure 1 is a block diagram of a tundish and mold that control the level of molten steel in the mold. Figure 2 is a block diagram showing a conventional method for controlling the level of molten steel in the mold. Figure 3 is a mold according to the present invention. Figure 4 is a block diagram showing the control method for internally molten steel at 100 levels. 1... Mold, 2... Molten steel level bell detector in the mold,
3-... Molten steel, 4... Tandish, 5... Sliding nozzle, 6... Level controller, 7... Sliding nozzle opening controller, 9... Sliding nozzle drive device, 10...・Short piece position detector, 11・
...Casting speed detector, 12...Arithmetic unit K (:, 13
...Force lη device f114...Press device, 15...
Cast piece. Agent Patent Attorney Masaaki Akizawa

Claims (1)

【特許請求の範囲】 (11連続鋳造中に鋳型短片を移動ぜしめ鋳片幅を変更
する連続鋳造方法において、 設定短片位置を基準とする鋳造速度信号と鋳造速度信号
および設定鋳片厚から鋳型内容積変化を経時的に算出し
、該算出値に基いてタンディツシュの溶鋼注入速度制御
全行なうことを特徴とする鋳型自溶鋼湯面レベル制御方
法。
[Scope of Claims] (11) In a continuous casting method in which the strip width is changed by moving the mold strip during continuous casting, a casting speed signal based on a set strip position, a casting speed signal, and a set strip thickness are used to form a mold. 1. A method for controlling the level of self-molten steel in a mold, characterized in that the internal volume change is calculated over time, and the molten steel injection rate of the tundish is fully controlled based on the calculated value.
JP19055282A 1982-10-29 1982-10-29 Method for controlling the level of molten steel in the mold in continuous casting Granted JPS5978763A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19055282A JPS5978763A (en) 1982-10-29 1982-10-29 Method for controlling the level of molten steel in the mold in continuous casting

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19055282A JPS5978763A (en) 1982-10-29 1982-10-29 Method for controlling the level of molten steel in the mold in continuous casting

Publications (2)

Publication Number Publication Date
JPS5978763A true JPS5978763A (en) 1984-05-07
JPS6261383B2 JPS6261383B2 (en) 1987-12-21

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP19055282A Granted JPS5978763A (en) 1982-10-29 1982-10-29 Method for controlling the level of molten steel in the mold in continuous casting

Country Status (1)

Country Link
JP (1) JPS5978763A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01293954A (en) * 1988-05-19 1989-11-27 Nippon Steel Corp Molten metal level control method for continuous thin slab casting machine with variable width
KR100529062B1 (en) * 2003-12-23 2005-11-15 재단법인 포항산업과학연구원 Apparatus for controlling mold level in liquid core reduction
US7779891B2 (en) 2001-04-09 2010-08-24 Sumitomo Electric Industries, Ltd. Method of manufacturing magnesium alloy material
WO2019099480A1 (en) * 2017-11-15 2019-05-23 Novelis Inc. Metal level overshoot or undershoot mitigation at transition of flow rate demand

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4661857B2 (en) * 2001-04-09 2011-03-30 住友電気工業株式会社 Magnesium alloy material and method for producing the same

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5342018A (en) * 1976-09-28 1978-04-17 Matsushita Electric Ind Co Ltd Magnetic head and preparation thereof
JPS56126065A (en) * 1980-03-10 1981-10-02 Nippon Steel Corp Sn automatic casting control method
JPS57159252A (en) * 1981-03-27 1982-10-01 Sumitomo Metal Ind Ltd Controlling method for molten metal level of continuous casting mold

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5342018A (en) * 1976-09-28 1978-04-17 Matsushita Electric Ind Co Ltd Magnetic head and preparation thereof
JPS56126065A (en) * 1980-03-10 1981-10-02 Nippon Steel Corp Sn automatic casting control method
JPS57159252A (en) * 1981-03-27 1982-10-01 Sumitomo Metal Ind Ltd Controlling method for molten metal level of continuous casting mold

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01293954A (en) * 1988-05-19 1989-11-27 Nippon Steel Corp Molten metal level control method for continuous thin slab casting machine with variable width
US7779891B2 (en) 2001-04-09 2010-08-24 Sumitomo Electric Industries, Ltd. Method of manufacturing magnesium alloy material
KR100529062B1 (en) * 2003-12-23 2005-11-15 재단법인 포항산업과학연구원 Apparatus for controlling mold level in liquid core reduction
WO2019099480A1 (en) * 2017-11-15 2019-05-23 Novelis Inc. Metal level overshoot or undershoot mitigation at transition of flow rate demand
JP2020505235A (en) * 2017-11-15 2020-02-20 ノベリス・インコーポレイテッドNovelis Inc. Reduction of metal level overshoot or undershoot during transition of flow demand
US10632528B2 (en) 2017-11-15 2020-04-28 Novelis Inc. Metal level overshoot or undershoot mitigation at transition of flow rate demand

Also Published As

Publication number Publication date
JPS6261383B2 (en) 1987-12-21

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