JPH11267813A - Control method of molten steel surface level mold of continuous casting machine and control equipment - Google Patents

Control method of molten steel surface level mold of continuous casting machine and control equipment

Info

Publication number
JPH11267813A
JPH11267813A JP7457298A JP7457298A JPH11267813A JP H11267813 A JPH11267813 A JP H11267813A JP 7457298 A JP7457298 A JP 7457298A JP 7457298 A JP7457298 A JP 7457298A JP H11267813 A JPH11267813 A JP H11267813A
Authority
JP
Japan
Prior art keywords
level
molten metal
mold
value
nozzle
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
JP7457298A
Other languages
Japanese (ja)
Other versions
JP3843588B2 (en
Inventor
Hiroshi Kitada
宏 北田
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
Sumitomo Metal Industries 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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP07457298A priority Critical patent/JP3843588B2/en
Publication of JPH11267813A publication Critical patent/JPH11267813A/en
Application granted granted Critical
Publication of JP3843588B2 publication Critical patent/JP3843588B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Continuous Casting (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the increase in the molten steel surface level fluctuation when the clogging in the nozzle for the molten metal injection happens. SOLUTION: Under the normal operating state, level deviation e(t) between molten steel surface level target value r(t) in a mold and molten steel surface level measured value y(t) in the mold is input into the first compensator 13 having the integral function and also into the second compensator 14 which does not have the integral function, and the sliding nozzle gate opening order MV(t) is obtained from the sum of this output and the opening order is given to an actuator 7. On the other hand, when the molten metal injection volume becomes the saturation state due to the generation of the clogging of a sliding nozzle gate 3 or a submerged nozzle 4, an output of the first compensator 13 is stopped, and an output of the second compensator 14 is made to be the sliding nozzle gate opening order MV(t).

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】本発明は連続鋳造機における
鋳型内の湯面レベルを目標値に安定維持すべく溶湯注入
量を調節する鋳型内湯面レベル制御方法及びその装置に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and a device for controlling a molten metal level in a continuous casting machine, which adjusts a molten metal pouring amount so as to stably maintain a molten metal level in a mold at a target value.

【0002】[0002]

【従来の技術】連続鋳造過程で鋳型内湯面レベルが変動
すると、湯面上のパウダが溶湯内に巻き込まれ、溶湯中
に巻き込まれたパウダは、そのまま鋳片の表皮欠陥とな
って圧延後の成品に疵を発生させてしまうこととなる。
このため、湯面レベル変動を制御することは成品品質の
向上を図る上で極めて重要な意味を有している。湯面レ
ベル変動の要因は種々知られているが、鋳片の引抜きに
よる鋳片内未凝固溶湯静圧の変動によって、鋳片の凝固
シェルが周期的に膨張と収縮を繰り返す非定常バルジン
グに起因して、生じる鋳型からの溶湯流出量変動、浸漬
ノズル内の詰まりの進行に伴う溶湯流量の時間的不均一
性等の外乱が主たる原因と言うことが出来る。
2. Description of the Related Art When the level of a molten metal in a mold fluctuates in a continuous casting process, powder on the molten metal surface is caught in the molten metal, and the powder caught in the molten metal becomes a skin defect of a slab as it is and after rolling. This will result in flaws in the product.
For this reason, controlling the fluctuation in the level of the molten metal has a very important meaning in improving the quality of the product. Various factors are known to cause the level change of the molten metal, but it is caused by unsteady bulging in which the solidified shell of the slab periodically expands and contracts due to the fluctuation of the static pressure of the unsolidified molten metal in the slab due to drawing of the slab Disturbances such as fluctuations in the amount of molten metal flowing out of the casting mold and non-uniformity in the flow rate of molten metal due to the progress of clogging in the immersion nozzle can be said to be the main causes.

【0003】この対策として、従来にあっては湯面レベ
ルセンサにより湯面レベルを所定の時間間隔で測定し、
この湯面レベル測定値を湯面レベル目標値と比較し、そ
のレベル偏差を解消するようにタンディッシュ底部に設
けてあるスライディングノズルゲートの開度、又はスト
ッパの開度を調節し、鋳型内への注入溶湯量を調節し、
鋳片として引き抜かれる溶湯量に相当する溶湯量を鋳型
に供給しつつ、前記外乱による溶湯注入量変動を補償し
て鋳型内の溶湯体積を一定にすることが行われている。
As a countermeasure against this, conventionally, the level of the molten metal is measured at a predetermined time interval by a molten metal level sensor.
Compare the measured level value with the target level, adjust the opening of the sliding nozzle gate or stopper provided at the bottom of the tundish to eliminate the level deviation, and place it in the mold. Adjust the amount of molten metal
2. Description of the Related Art While supplying a molten metal amount corresponding to an amount of a molten metal to be drawn as a cast slab to a mold, compensation of fluctuation in the molten metal injection amount due to the disturbance is performed to make the molten metal volume in the mold constant.

【0004】ところで、湯面レベルを所定の目標値に維
持するために必要なスライディングノズルゲート、又は
ストッパの開度を調節する湯面レベル制御装置は、通
常、湯面レベル測定値と湯面レベル目標値とのレベル偏
差を時間的に積分する要素、例えばPID調節装置等を
備えており、この積分要素の作用により湯面レベルの平
均値を湯面レベル目標値に略一致させるようにスライデ
ィングノズルゲート、又はストッパのアクチュエータに
対する開度指令を演算している。
[0004] By the way, a level control device for adjusting the opening of a sliding nozzle gate or a stopper necessary for maintaining the level of a molten metal at a predetermined target value usually includes a measured level of the molten metal and a level of the molten metal. An element for temporally integrating a level deviation from a target value, for example, a PID adjusting device, is provided. A sliding nozzle is provided so that an average value of the liquid level is made to substantially coincide with the target value of the liquid level by the operation of the integrating element. An opening command for the gate or stopper actuator is calculated.

【0005】ところが、連続鋳造機の操業中には、スラ
イディングノズルゲートの開口部、または浸漬ノズルの
内部に溶湯中の介在物が固着することによりノズル詰ま
りが発生する。例えば、スライディングノズルにノズル
詰まりが発生すると、次のような不都合を招来する。
[0005] However, during operation of the continuous casting machine, nozzle clogging occurs because inclusions in the molten metal adhere to the opening of the sliding nozzle gate or the inside of the immersion nozzle. For example, if the nozzle clogging occurs in the sliding nozzle, the following inconvenience is caused.

【0006】即ち、 ノズル詰まりが軽微な場合は、スライディングノズ
ルゲート開度の変更に対する鋳型への溶湯注入量ゲイン
が低下するため、湯面レベル制御装置における制御パラ
メータの湯面レベル変動幅抑制に対する最適性が失わ
れ、ノズル詰まりがない場合に比べて湯面レベル変動幅
が大きくなる。 ノズル詰まりが進行した場合は、鋳型への溶湯注入
量がある上限値で飽和する。このため湯面レベル制御装
置がスライディングノズルゲートを開操作するような開
度指令値を出力しても、外乱による溶湯流出量変動に対
して溶湯注入量が不足し、ノズル詰まりが軽微な場合に
比べてさらに湯面レベル変動幅が大きくなる。
That is, when the nozzle clogging is slight, the gain of the amount of molten metal injected into the casting mold with respect to the change in the opening of the sliding nozzle gate is reduced. Performance is lost, and the fluctuation level of the molten metal level becomes larger than in the case where there is no nozzle clogging. When nozzle clogging proceeds, the amount of molten metal injected into the mold is saturated at a certain upper limit. For this reason, even if the molten metal level control device outputs an opening command value such as to open the sliding nozzle gate, the molten metal injection amount is insufficient with respect to the molten metal outflow amount fluctuation due to disturbance, and the nozzle clogging is slight. In comparison with this, the fluctuation range of the molten metal level becomes larger.

【0007】 ノズル詰まりがよりもさらに進行し
た場合には、鋳片として鋳型から流出する溶湯量に対し
ても溶湯注入量が不足する状態となり、湯面レベルは下
降し続け、鋳片の引抜き速度を低下させて鋳型からの溶
湯流出量を低減せざるを得ず、効率的な鋳造は不可能と
なる。前記のの対策としては、特開昭64−5374
7号公報にはスライディングノズルゲート開度に対する
鋳型への溶湯注入量ゲインの推定値に基づき、スライデ
ィングノズルゲートにおけるPID調節装置の制御パラ
メータを修正し、湯面レベル制御装置のループゲインを
最適に保つ方法が開示されている。また、特開昭59−
27762号公報には、ストッパによる流量調節時にお
ける同様の方法が開示されている。
If the nozzle clogging is further advanced, the molten metal injection amount is insufficient with respect to the amount of molten metal flowing out of the mold as a slab, the level of the molten metal continues to drop, and the slab drawing speed is reduced. Therefore, the amount of molten metal flowing out of the mold must be reduced, and efficient casting becomes impossible. As a countermeasure for the above, JP-A-64-5374 has been proposed.
In Japanese Patent Application Laid-Open Publication No. 7-107, a control parameter of a PID adjusting device in a sliding nozzle gate is corrected based on an estimated value of a molten metal injection amount gain with respect to a sliding nozzle gate opening degree, and a loop gain of a molten metal level control device is kept optimal. A method is disclosed. Also, Japanese Unexamined Patent Publication No.
No. 27762 discloses a similar method at the time of flow rate adjustment by a stopper.

【0008】これらの方法では、詰まりが軽微であって
スライディングノズル、又は浸漬ノズルの流量上限値が
前述した外乱による溶湯流出量変動を補償するために必
要な溶湯注入量を常に上回っている限りにおいて、湯面
レベル変動の抑制効果は期待できる。
In these methods, as long as the clogging is slight and the upper limit of the flow rate of the sliding nozzle or the immersion nozzle always exceeds the molten metal injection amount necessary to compensate for the fluctuation of the molten metal outflow amount due to the above-described disturbance. The effect of suppressing fluctuations in the level of the molten metal can be expected.

【0009】[0009]

【発明が解決しようとする課題】反面、これらの従来の
方法では、前記に示す不都合に対しては効果がない。
何故なら、溶湯注入量が飽和している場合の湯面レベル
変動が、以下の2つの要因でノズル詰まりが軽微な場合
に比べて大きくなるためである。 (a)溶湯注入量が飽和すると、外乱による鋳型からの
溶湯流出量の増加分を補充するための溶湯注入量が不足
する。その結果、湯面レベルが下降する方向の変動幅が
大きくなる。
On the other hand, these conventional methods have no effect on the above-mentioned disadvantages.
This is because the fluctuation of the molten metal level when the molten metal injection amount is saturated is larger than that when the nozzle clogging is slight due to the following two factors. (A) When the molten metal injection amount is saturated, the molten metal injection amount for replenishing the increase in the molten metal outflow amount from the mold due to disturbance becomes insufficient. As a result, the fluctuation width in the direction in which the level of the molten metal decreases is increased.

【0010】(b)外乱による鋳型からの溶湯流出量が
減少し、湯面レベルが上昇方向に転じた後も、湯面レベ
ル測定値が湯面レベル目標値を下回っている間は湯面レ
ベル制御装置の積分要素がレベル偏差を蓄積し、スライ
ディングノズルゲートが溶湯注入量の上限に対応する開
度を越えて開く方向に開度指令値を算出し続ける。しか
し、スライディングノズルゲート開度に対して溶湯注入
量が飽和しているため、この間の鋳型への溶湯注入量は
一定であり、加えて湯面レベル測定値が湯面レベル目標
値を上回り、積分要素がレベル偏差の蓄積分を逐次減じ
てスライディングノズルゲートの開度指令値を溶湯注入
量の上限に対応する開度以下に閉じるまでは鋳型に対す
る溶湯注入量が減少しない。
(B) Even after the amount of molten metal flowing out of the mold due to disturbance is reduced and the level of the molten metal is turned upward, while the measured level of the molten metal is below the target level, the level of the molten metal is maintained. The integral element of the control device accumulates the level deviation, and continuously calculates the opening command value in the direction in which the sliding nozzle gate opens beyond the opening corresponding to the upper limit of the molten metal injection amount. However, since the molten metal injection amount is saturated with respect to the opening of the sliding nozzle gate, the molten metal injection amount into the mold during this period is constant, and in addition, the molten metal level measured value exceeds the molten metal level target value, and The amount of molten metal injected into the mold does not decrease until the element gradually reduces the accumulated amount of the level deviation and closes the opening command value of the sliding nozzle gate below the opening corresponding to the upper limit of the molten metal injection amount.

【0011】その結果、溶湯流入量が飽和している間
は、湯面レベルが上昇する方向にレベル変動幅が増大す
る。前記の要因(a)の場合、溶湯注入量が飽和してい
る状態においては、溶湯注入量の不足状態を回避するの
が難しい。本発明は、ノズル詰まりが進行し、溶湯注入
量が飽和している状態においては、溶湯注入量の不足状
態の場合における前記要因(b)の問題点を解決し、湯
面レベル変動を抑制する装置を提供することを目的とす
る。
As a result, while the molten metal inflow is saturated, the level fluctuation width increases in the direction in which the molten metal level rises. In the case of the above factor (a), it is difficult to avoid a shortage of the molten metal injection amount when the molten metal injection amount is saturated. The present invention solves the problem of the factor (b) in the case where the molten metal injection amount is insufficient when the nozzle clogging progresses and the molten metal injection amount is saturated, and suppresses the fluctuation of the molten metal level. It is intended to provide a device.

【0012】[0012]

【課題を解決するための手段】第1の発明に係る連続鋳
造機の鋳型内湯面レベル制御方法は、鋳型内の湯面レベ
ル目標値に対する湯面レベル測定値のレベル偏差に基づ
いて、鋳型に対する溶湯注入ノズルの開度調節用アクチ
ュエータを操作し、鋳型内湯面レベルを湯面レベル目標
値に維持すべく制御する鋳型内湯面レベル制御方法にお
いて、前記レベル偏差に時間積分処理した第1の値と、
前記レベル偏差に積分処理を含まない処理を施した第2
の値との和を前記アクチェータに対するノズル開度指令
とすると共に、ノズルから鋳型への溶湯注入量が飽和状
態にあって、しかも前記湯面レベル測定値が湯面レベル
目標値を以下の場合に、前記第1の値零とすることを特
徴とする。
According to a first aspect of the present invention, there is provided a method for controlling a mold level in a mold of a continuous casting machine, the method comprising the steps of: In the mold level control method for controlling the opening level of the molten metal injection nozzle to maintain the mold level in the mold so as to maintain the mold level target value, a first value obtained by time-integrating the level deviation with the first value. ,
A second processing in which the level deviation does not include the integration processing;
And the sum of the above values as the nozzle opening command for the actuator, and when the molten metal injection amount from the nozzle to the mold is in a saturated state, and the measured molten metal level is below the molten metal level target value. , The first value being zero.

【0013】第2の発明に係る連続鋳造機の鋳型内湯面
レベル制御装置は、鋳型内の湯面レベル目標値に対する
湯面レベル測定値のレベル偏差に基づいて、鋳型に対す
る溶湯注入ノズルの開度調節用アクチュエータを操作
し、鋳型内湯面レベルを湯面レベル目標値に維持すべく
制御する鋳型内湯面レベル制御装置において、前記レベ
ル偏差に時間積分処理した値を出力する第1の手段と、
前記レベル偏差に積分処理を含まない処理を施した値を
出力する第2の手段と、前記第1の手段の動作、非動作
を切り替える切替手段と、前記第1及び第2の手段の出
力を加算して、前記アクチュエータに対しノズル開度指
令として出力する手段と、ノズル開度の変更に対して鋳
型への溶湯注入量が飽和状態にあるか否かを検知し、飽
和状態にあり、しかも前記レベル偏差が正の場合に、前
記第1の手段を非動作とすべく切替手段を動作させる飽
和検知手段とを備えることを特徴とする。
According to a second aspect of the present invention, there is provided a mold level control device in a mold of a continuous casting machine, wherein an opening degree of a molten metal injection nozzle with respect to a mold is determined based on a level deviation of a measured level value with respect to a target level value in the mold. A first means for operating an adjusting actuator to output a value obtained by performing a time integration process on the level deviation, in a mold level control device for controlling the mold level in the mold to maintain the mold level at a target level;
A second unit that outputs a value obtained by performing a process that does not include an integration process on the level deviation; a switching unit that switches operation and non-operation of the first unit; and an output of the first and second units. Means for outputting as a nozzle opening command to the actuator, and detecting whether or not the molten metal injection amount into the mold is saturated with respect to the change in the nozzle opening, and is in a saturated state, and When the level deviation is positive, a saturation detecting means for operating the switching means to deactivate the first means is provided.

【0014】第1、第2の発明にあっては、これによっ
てノズル詰まりにより鋳型内への溶湯注入量が飽和状態
となったことが検知されると、ノズル開度調節用のアク
チュエータに対する積分処理値の出力を停止させること
で鋳型内湯面レベル変動を抑制し、パウダの巻き込みに
よる鋳片の表皮下欠陥の発生を低減し得ることとなる。
According to the first and second aspects of the present invention, when it is detected that the amount of molten metal injected into the mold is saturated due to nozzle clogging, the integration process for the nozzle opening adjustment actuator is performed. By stopping the output of the value, fluctuations in the level of the molten metal level in the mold can be suppressed, and the occurrence of subcutaneous defects in the slab due to entrainment of the powder can be reduced.

【0015】[0015]

【発明の実施の形態】以下本発明をその実施の形態を示
す図面に基づき具体的に説明する。図1は、本発明に係
る連続鋳造機の鋳型内湯面レベル制御装置の構成を示す
ブロック図であり、図中1は鋳型、2は鋳型1に溶湯を
供給するタンデッシュを示している。タンデッシュ2
は、その底壁にスライディングノズルゲート3を介在さ
せて浸漬ノズル4が垂設されており、この浸漬ノズル4
の下端部が鋳型1内の溶湯8内に浸漬された状態で位置
せしめられている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in detail with reference to the drawings showing the embodiments. FIG. 1 is a block diagram showing a configuration of a mold level control device in a mold of a continuous casting machine according to the present invention. In the figure, reference numeral 1 denotes a mold, and 2 denotes a tundish for supplying molten metal to the mold 1. Tundesh 2
Has an immersion nozzle 4 suspended from the bottom wall thereof with a sliding nozzle gate 3 interposed therebetween.
Is positioned while being immersed in the molten metal 8 in the mold 1.

【0016】スライディングノズルゲート3には、これ
を開閉操作するための油圧シリンダ等で構成されたアク
チュエータ7が設けられており、該アクチュエータ7の
操作によってスライディングノズルゲート3の開度を調
整するようにしてある。10は前記アクチュエータ7に
対する制御系であり、与えられた湯面レベル目標値r
(t)と、鋳型1内に臨ませた湯面レベルセンサ5の検
出値である湯面レベル測定値y(t)とのレベル偏差e
(t)を求めて出力する減算器11と、レベル偏差e
(t)が切替手段たるスイッチ12を介して入力され、
レベル偏差e(t)に対し所定の処理を施して出力する
第1の補償器13及びレベル偏差e(t)が直接入力さ
れる第2の補償器14と、第1,第2の補償器13,1
4の出力を加算してアクチュエータ7へ出力する加算器
15と、溶湯注入量飽和検知手段16とを備えている。
The sliding nozzle gate 3 is provided with an actuator 7 composed of a hydraulic cylinder or the like for opening and closing the sliding nozzle gate 3. The opening of the sliding nozzle gate 3 is adjusted by operating the actuator 7. It is. Reference numeral 10 denotes a control system for the actuator 7, which is a given molten metal level target value r.
The level deviation e between (t) and the measured level y (t) of the molten metal level sensor 5 that is exposed in the mold 1.
A subtracter 11 for obtaining and outputting (t), and a level deviation e
(T) is input via the switch 12 as a switching means,
A first compensator 13 for performing predetermined processing on the level deviation e (t) and outputting the same, a second compensator 14 for directly receiving the level deviation e (t), and first and second compensators 13,1
4 is provided with an adder 15 that adds the outputs of the outputs 4 and outputs the result to the actuator 7 and a molten metal injection amount saturation detecting unit 16.

【0017】第1の補償器13は、下記(1)式に示す
如く経時的にレベル偏差e(t)を積分し、その値に制
御パラメータK1を乗じた値をスライディングノズルゲ
ート開度指令MV1(t)として加算器15へ出力す
る。 MV1(t)=K1∫e(t)dt …(1)
The first compensator 13 integrates the level deviation e (t) with time as shown in the following equation (1), and multiplies the value by a control parameter K1 to obtain a sliding nozzle gate opening command MV1. Output to the adder 15 as (t). MV1 (t) = K1∫e (t) dt (1)

【0018】また、第2の補償器14は、積分器を有さ
ず、伝達関数C(s)で表される特性を備えており、入
力されたレベル偏差e(t)に対し、下記(2)式に従
ってスライディングノズルゲート開度指令MV2(t)
を演算し、加算器15へ出力 する。 MV2(t)=L- [C(s)L[e(t)]] …(2) 但し L :ラプラス変換 L- :逆ラプラス変換
The second compensator 14 does not have an integrator and has a characteristic represented by a transfer function C (s). Sliding nozzle gate opening command MV2 (t) according to equation 2)
Is calculated and output to the adder 15. MV2 (t) = L - [ C (s) L [e (t)]] ... (2) where L: Laplace transformation L -: inverse Laplace transform

【0019】第2の補償器14の伝達関数C(s)を定
数KPと置換すれば(2)式は下記(3)式の如くに書
き直せる。 MV2(t)=KP×e(t) …(3) 加算器15は、スライディングノズルゲート開度指令M
V1(t)とMV2(t)との和であるスライディング
ノズルゲート開度指令MV(t)をスライディングノズ
ルゲート3のアクチュエータ7へ与える。
If the transfer function C (s) of the second compensator 14 is replaced with a constant KP, the equation (2) can be rewritten as the following equation (3). MV2 (t) = KP × e (t) (3) The adder 15 outputs the sliding nozzle gate opening command M
A sliding nozzle gate opening command MV (t), which is the sum of V1 (t) and MV2 (t), is given to the actuator 7 of the sliding nozzle gate 3.

【0020】溶湯注入量飽和検知手段16は、湯面レベ
ルセンサ5の測定値である鋳型1内の湯面レベル測定値
y(t)、鋳片の引抜き速度計6の測定値である引抜き
速度Vc(t)、スライディングノズルゲート開度指令
MV(t)、及び鋳型断面積に基づいて、鋳型への溶湯
注入量が未飽和の状態か、又は溶湯注入量が飽和状態に
あるかを判断し、未飽和の状態にある場合は、スイッチ
12を閉状態に維持し、また飽和状態にあって、しかも
湯面レベル測定値y(t)が湯面レベル目標値r(t)
以下の場合、換言すれば、レベル偏差e(t)>0の場
合には、スイッチ12を開放状態とする。飽和状態にあ
るか否かは、スライディングノズルゲートの開度変化、
換言すればアクチュエータ7のシリンダロッドの伸縮に
対応して溶湯注入量が変化するか否かによって判断され
る。ノズルからの溶湯注入量が飽和状態にあるか否かを
見るために特別にゲートの開度を微量に変えてもよい
が、それまでの間のゲート開度の変化に対応して溶湯注
入量が変化したか否かに基づいて判断してもよい。
The molten metal injection amount saturation detecting means 16 measures a molten metal level y (t) in the mold 1, which is a measured value of the molten metal level sensor 5, and a drawing speed which is a measured value of the slab drawing speed meter 6. Based on Vc (t), the sliding nozzle gate opening command MV (t), and the sectional area of the mold, it is determined whether the amount of molten metal injected into the mold is not saturated or the amount of molten metal injected is saturated. , When it is not saturated, the switch 12 is kept closed, and when it is saturated, the measured level y (t) is the target level r (t).
In the following cases, in other words, when the level deviation e (t)> 0, the switch 12 is opened. Whether the nozzle is saturated or not depends on the opening of the sliding nozzle gate,
In other words, the determination is made based on whether or not the molten metal injection amount changes in accordance with the expansion and contraction of the cylinder rod of the actuator 7. The gate opening may be slightly changed to check whether the injection amount of the molten metal from the nozzle is saturated or not. May be determined based on whether or not has changed.

【0021】これによって未飽和状態にある場合には、
レベル偏差e(t)は第1,第2の補償器13,14へ
入力され、夫々の出力MV1(t)、MV2(t)が加
算器15にて加算され、下記(4)式の如くその加算値
がスライディングノズルゲート開度指令MV(t)とし
てアクチュエータ7へ出力される。 MV(t)= MV1(t)+MV2(t) …(4)
As a result, when in the unsaturated state,
The level deviation e (t) is input to the first and second compensators 13 and 14, and the respective outputs MV1 (t) and MV2 (t) are added by the adder 15, and as shown in the following equation (4). The added value is output to the actuator 7 as the sliding nozzle gate opening command MV (t). MV (t) = MV1 (t) + MV2 (t) (4)

【0022】一方飽和状態にある場合には、スイッチ1
2が開放され、レベル偏差e(t)は第2の補償器14
にのみ入力され、下記(5)式の如くその出力MV2
(t)がスライディングノズルゲート3の開度指令MV
(t)としてアクチュエータ7へ出力される。 MV(t)= MV2(t) …(5)
On the other hand, when the switch is in a saturated state,
2 is released, and the level deviation e (t) is
And output MV2 as shown in the following equation (5).
(T) is the opening degree command MV of the sliding nozzle gate 3
(T) is output to the actuator 7. MV (t) = MV2 (t) (5)

【0023】[0023]

【実施例】鋳片9の引抜きによる鋳型1からの溶湯流出
量が設計上の溶湯注入量上限値の50%、また外乱によ
る鋳型1からの溶湯流出量変動が設計上の溶湯注入量上
限値の±6%とし、鋳型1への溶湯注入量が設計上の上
限値の52%で飽和した状態とし、本発明装置と従来装
置とを適用した。上記の状態は、鋳片9の引抜きによる
鋳型1からの溶湯流出量と釣り合うように鋳型1への溶
湯注入は可能であるが、外乱による鋳型1からの溶湯流
出量変動を完全に補償するには鋳型への溶湯注入量が不
足する状態にある。
EXAMPLE The molten metal outflow from the mold 1 due to the drawing of the slab 9 is 50% of the designed upper limit of the molten metal injection amount, and the fluctuation of the molten metal outflow from the mold 1 due to disturbance is the designed upper limit of the molten metal injection amount. ± 6%, and the molten metal injection amount into the mold 1 was saturated at 52% of the upper limit in design, and the apparatus of the present invention and the conventional apparatus were applied. In the above state, the molten metal can be injected into the mold 1 so as to be balanced with the molten metal outflow from the mold 1 due to the drawing of the slab 9, but it is necessary to completely compensate for the variation in the molten metal outflow from the mold 1 due to disturbance. Means that the amount of molten metal injected into the mold is insufficient.

【0024】図2は、スライディングノズルゲートのア
クチュエータ7に対し、積分器の出力を入力して湯面レ
ベル制御を実施する従来技術を適用した場合と、本発明
を実施した場合とにおける湯面レベル(図2(a))、
スライディングノズルゲート開度指令(図2(b))、
溶湯注入流量(図2(c))夫々の時間的推移を示した
グラフである。
FIG. 2 shows the level of the molten metal in the case where the conventional technique of performing the level control by inputting the output of the integrator to the actuator 7 of the sliding nozzle gate and the case where the present invention is implemented. (FIG. 2 (a)),
Sliding nozzle gate opening command (FIG. 2B),
It is a graph which showed a time transition of each molten metal injection flow rate (FIG. 2 (c)).

【0025】図2(c)に示す如く溶湯注入量が所定レ
ベルで飽和状態となっている場合においても、図2
(a)に示す如く湯面レベルが湯面レベル目標値を越え
るタイミングで、図2(b)に示す如くスライディング
ノズルゲート開度指令を、ノズルを閉じる側、換言すれ
ばノズル開度を減じる側に切り換えることで湯面レベル
の上昇が従来技術では13mmであったのに対し、本発
明装置では8mmに留め得ており、湯面レベル変動を低
減し得ていることが解る。
As shown in FIG. 2 (c), even when the molten metal injection amount is saturated at a predetermined level,
At the timing when the liquid level exceeds the target level as shown in FIG. 2A, a sliding nozzle gate opening command is issued as shown in FIG. 2B to the nozzle closing side, in other words, the nozzle opening degree is reduced. The rise in the level of the molten metal is 13 mm in the prior art by switching to, but can be reduced to 8 mm in the apparatus of the present invention, and it can be seen that the fluctuation in the level of the molten metal can be reduced.

【0026】[0026]

【発明の効果】以上の如く本発明装置にあっては、鋳型
への溶湯供給用ノズルの詰まりが進行し、溶湯注入量が
飽和した状態においても、鋳型内湯面レベル変動を効果
的に抑制出来、鋳片の表皮下欠陥の発生を防止出来て、
圧延後の成品品質を高め得ることとなる。
As described above, in the apparatus of the present invention, even when the molten metal supply nozzle is clogged and the injection amount of the molten metal is saturated, fluctuations in the level of the molten metal in the mold can be effectively suppressed. , Prevents the occurrence of subepidermal defects in the slab,
The product quality after rolling can be improved.

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

【図1】本発明に係る連続鋳造機の鋳型内湯面レベル制
御装置の構成を示すブロック図である。
FIG. 1 is a block diagram showing a configuration of a mold level control device in a mold of a continuous casting machine according to the present invention.

【図2】本発明装置と従来装置との比較試験結果を示す
グラフである。
FIG. 2 is a graph showing a comparison test result between the device of the present invention and a conventional device.

【符号の説明】[Explanation of symbols]

1 鋳型 2 タンデッシュ 3 スライディングノズルゲート 4 浸漬ノズル 5 湯面レベルセンサ 6 鋳片の引抜き速度計 11 減算器 12 スイッチ 13 第1の補償器 14 第2の補償器 15 加算器 16 溶湯注入量飽和検知手段 DESCRIPTION OF SYMBOLS 1 Mold 2 Tundish 3 Sliding nozzle gate 4 Immersion nozzle 5 Metal surface level sensor 6 Casting speedometer 11 Subtractor 12 Switch 13 First compensator 14 Second compensator 15 Adder 16 Molten metal injection amount saturation detection means

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 鋳型内の湯面レベル目標値に対する湯面
レベル測定値のレベル偏差に基づいて、鋳型に対する溶
湯注入ノズルの開度調節用アクチュエータを操作し、鋳
型内湯面レベルを湯面レベル目標値に維持すべく制御す
る鋳型内湯面レベル制御方法において、 前記レベル偏差に時間積分処理した第1の値と、前記レ
ベル偏差に積分処理を含まない処理を施した第2の値と
の和を前記アクチェータに対するノズル開度指令とする
と共に、ノズルから鋳型への溶湯注入量が飽和状態にあ
って、しかも前記湯面レベル測定値が湯面レベル目標値
を以下の場合に、前記第1の値零とすることを特徴とす
る連続鋳造機の鋳型内湯面レベル制御方法。
An actuator for adjusting the opening of a molten metal injection nozzle with respect to a mold is operated based on a level deviation of a measured value of a molten metal level with respect to a target value of a molten metal level in the mold to set the molten metal level in the mold to the target. In the mold level control method for controlling the level in the mold to maintain the value, a sum of a first value obtained by performing a time integration process on the level deviation and a second value obtained by performing a process not including the integration process on the level deviation is obtained. In addition to the nozzle opening command for the actuator, the first value is set when the molten metal injection amount from the nozzle to the mold is in a saturated state and the measured level value is below the target level value. A method for controlling a level of a molten metal in a mold of a continuous casting machine, wherein the method is set to zero.
【請求項2】 鋳型内の湯面レベル目標値に対する湯面
レベル測定値のレベル偏差に基づいて、鋳型に対する溶
湯注入ノズルの開度調節用アクチュエータを操作し、鋳
型内湯面レベルを湯面レベル目標値に維持すべく制御す
る鋳型内湯面レベル制御装置において、 前記レベル偏差に時間積分処理した値を出力する第1の
手段と、 前記レベル偏差に積分処理を含まない処理を施した値を
出力する第2の手段と、 前記第1の手段の動作、非動作を切り替える切替手段
と、 前記第1及び第2の手段の出力を加算して、前記アクチ
ュエータに対しノズル開度指令として出力する手段と、 ノズル開度の変更に対して鋳型への溶湯注入量が飽和状
態にあるか否かを検知し、飽和状態にあり、しかも前記
レベル偏差が正の場合に、前記第1の手段を非動作とす
べく切替手段を動作させる飽和検知手段とを備えること
を特徴とする連続鋳造機の鋳型内湯面レベル制御装置。
2. An actuator for adjusting an opening of a molten metal injection nozzle with respect to a mold is operated based on a level deviation of a measured value of a molten metal level with respect to a target value of a molten metal level in the mold to set a molten metal level in the mold. In a mold level control device in a mold for controlling to maintain the level deviation, a first means for outputting a value obtained by performing a time integration process on the level deviation, and outputting a value obtained by performing a process not including an integration process on the level deviation. A second means, a switching means for switching between operation and non-operation of the first means, and a means for adding the outputs of the first and second means and outputting the result as a nozzle opening command to the actuator. Detecting whether or not the amount of molten metal injected into the mold is saturated with respect to a change in the nozzle opening, and if the level is positive and the level deviation is positive, the first means is not operated; Continuous caster mold molten steel surface level controller, characterized in that it comprises a saturation detection means for operating the switching means so as to.
JP07457298A 1998-03-23 1998-03-23 Method and apparatus for controlling level in mold in continuous casting machine Expired - Fee Related JP3843588B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP07457298A JP3843588B2 (en) 1998-03-23 1998-03-23 Method and apparatus for controlling level in mold in continuous casting machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP07457298A JP3843588B2 (en) 1998-03-23 1998-03-23 Method and apparatus for controlling level in mold in continuous casting machine

Publications (2)

Publication Number Publication Date
JPH11267813A true JPH11267813A (en) 1999-10-05
JP3843588B2 JP3843588B2 (en) 2006-11-08

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Country Link
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Publication number Priority date Publication date Assignee Title
CN102266927B (en) * 2011-08-01 2013-02-13 东北大学 Control method for molten-steel casting sequence of continuous casting machine

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