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JPH0751257B2 - Twin-belt continuous casting level control method - Google Patents
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JPH0751257B2 - Twin-belt continuous casting level control method - Google Patents

Twin-belt continuous casting level control method

Info

Publication number
JPH0751257B2
JPH0751257B2 JP7186391A JP7186391A JPH0751257B2 JP H0751257 B2 JPH0751257 B2 JP H0751257B2 JP 7186391 A JP7186391 A JP 7186391A JP 7186391 A JP7186391 A JP 7186391A JP H0751257 B2 JPH0751257 B2 JP H0751257B2
Authority
JP
Japan
Prior art keywords
molten metal
level
command value
pouring amount
pouring
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.)
Expired - Fee Related
Application number
JP7186391A
Other languages
Japanese (ja)
Other versions
JPH04309439A (en
Inventor
木 淳 定
野 進 也 平
沼 洋 一 永
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.)
Mitsubishi Heavy Industries Ltd
Nippon Steel Corp
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd, Nippon Steel Corp filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP7186391A priority Critical patent/JPH0751257B2/en
Publication of JPH04309439A publication Critical patent/JPH04309439A/en
Publication of JPH0751257B2 publication Critical patent/JPH0751257B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Continuous Casting (AREA)
  • Control Of Non-Electrical Variables (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、双ベルト連続鋳造の湯
面制御方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a molten metal level control method for twin belt continuous casting.

【0002】[0002]

【従来技術】湯面レベルの検出方法としては、以下に示
すようなものがある。
2. Description of the Related Art There are the following methods for detecting the level of molten metal.

【0003】1.浮き子を利用する方法 湯面に浮き子を浮かべ、この浮き子の位置を棒またはチ
ェ−ン等により検出する方法。
1. Method of using a float A method of floating a float on the surface of the molten metal and detecting the position of this float with a stick or a chain.

【0004】2.光学的(光電変換)方法 湯面と容器等の接触位置における輝度の違いに着目し、
この境界線を例えばアレイセンサあるいはテレビカメラ
等を用いて三角測量法によって測定する方法。 3.超音波による方法 超音波を湯面表面に照射し、その反射した音波がもどっ
てくる時間をはかることで湯面までの距離を測定する方
法。
2. Optical (photoelectric conversion) method Focusing on the difference in brightness at the contact position between the molten metal surface and the container,
A method of measuring this boundary line by a triangulation method using, for example, an array sensor or a television camera. 3. Method using ultrasonic wave A method of measuring the distance to the surface of the molten metal by irradiating it with ultrasonic waves and measuring the time it takes for the reflected sound waves to return.

【0005】4.放射線を利用する方法 湯面に対し斜め方向に放射線を透過させ、この放射線の
減衰量により湯面レベルを検出する方法。
4. Method of using radiation A method of transmitting radiation diagonally to the surface of the molten metal and detecting the level of the molten metal by the attenuation of this radiation.

【0006】5.浸漬電極法 電極と湯面により電気回路のON−OFF状態を作って
湯面レベルを検出する方法。
5. Immersion electrode method A method of detecting the level of the molten metal by creating an ON-OFF state of the electric circuit with the electrode and the molten metal.

【0007】6.電磁誘導法 特開昭48−93539号公報の方法は、モ−ルド外壁
面に深さ方向に長いコイルを設け、このコイルをインピ
−ダンスブリッジ回路の一辺に接続する方法で、モ−ル
ド内の湯面レベルの変化をモ−ルド壁温度変化としてと
らえ、これによって生じるモ−ルド壁の固有抵抗変化に
よりモ−ルド内に発生する渦電流の変化を利用して湯面
レベルを検出する方法である。
6. Electromagnetic Induction Method The method disclosed in Japanese Patent Laid-Open No. 48-93539 is a method in which a coil long in the depth direction is provided on the outer wall surface of the mold and this coil is connected to one side of an impedance bridge circuit. A method for detecting the level of the molten metal surface by detecting the change in the molten metal surface level as a change in the temperature of the mold wall and utilizing the change in the eddy current generated in the mold due to the change in the specific resistance of the mold wall caused thereby. Is.

【0008】双ベルト連続鋳造の湯面制御方法として
は、上述の湯面レベル検出器で測定された一か所での湯
面レベル測定値に基づき、この湯面レベル測定値と湯面
レベル目標値との差をPI制御器またはPID制御器に
入力し、注湯量指令値を演算し、この注湯量指令値を注
湯量操作器に出力するのが従来の一搬的な技術である。
The molten metal level control method for twin-belt continuous casting is based on the measured molten metal level at one location measured by the above-mentioned molten metal level detector, and the measured molten metal level and the molten metal level target. A conventional portable technique is to input a difference from the value to a PI controller or a PID controller, calculate a pouring amount command value, and output the pouring amount command value to a pouring amount operation device.

【0009】[0009]

【発明が解決しようとする課題】一か所での湯面レベル
測定値に基づきPI制御器またはPID制御器を用いる
双ベルト連続鋳造の湯面制御方法は、湯面の振動を考慮
することができないので、演算された注湯量指令値によ
る注湯量変化が、湯面の振動を引き起こす場合があり、
製品の品質または歩留まり、操業率,操業時の安全性の
点で問題を生じる。
In the twin-belt continuous casting liquid level control method using the PI controller or the PID controller based on the measured value of the molten metal level at one place, the vibration of the molten metal level may be taken into consideration. Since it is not possible, changes in the pouring amount due to the calculated pouring amount command value may cause vibration of the molten metal surface,
This causes problems in terms of product quality or yield, operating rate, and safety during operation.

【0010】本発明は、湯面の平均レベルに影響を与え
る外乱を補償し、湯面の平均レベルを目標値に追従させ
るとともに、湯面の振動を積極的に抑制する制御方法を
提供することを目的とする。
The present invention provides a control method that compensates for disturbances that affect the average level of the molten metal surface, makes the average level of the molten metal surface follow a target value, and positively suppresses vibration of the molten metal surface. With the goal.

【0011】[0011]

【課題を解決するための手段】本発明は、双ベルト連続
鋳造の湯面制御方法において、 (イ) 湯面レベルを水平方向に互いに異なる位置で二
か所以上で測定し、 (ロ)モ−ダルフィルタ処理により、上記二か所上以上
での湯面レベル測定値をいて湯面の平均レベルおよび
組以上の湯面の振動モ−ド演算し、 (ハ) 上記湯面の平均レベルおよび上記振動モ−ドか
ら注湯量指令値1を演算し、 (ニ) 湯面レベル目標値と(イ)で測定された湯面レ
ベル測定値のうちの一つから注湯指令値2を演算し、 (ホ) 上記注湯量指令値1と注湯量指令値2から注湯
量指令値を演算し、 (ヘ) (ホ)で演算された注湯量指令値を注湯量操作
器に出力する、 ことにより、湯面の平均レベルに影響を与える外乱を補
償し、湯面の平均レベルを目標値に追従にさせるととも
に、湯面の振動を抑制することを特徴とする。
Means for Solving the Problems The present invention provides a molten metal surface control method for a twin-belt continuous casting, measured in (b) molten metal surface level two places or more at different positions in the horizontal direction, (b) Mo - by Dal filtering, and have use of melt surface level measurement at the two locations on or vibration mode of the average level and single Kumi以 Kaminoyu surface of the molten metal surface - calculating the de average of (c) above the melt surface The pouring amount command value 1 is calculated from the level and the vibration mode, and (d) the pouring command value 2 is obtained from one of the melt level target value and the melt level measured value measured in (a). (E) The pouring amount command value is calculated from the pouring amount command value 1 and the pouring amount command value 2 described above, and (f) the pouring amount command value calculated in (e) is output to the pouring amount controller. By doing so, the disturbance that affects the average level of the molten metal surface is compensated, and the average level of the molten metal surface is set Together is to follow, which comprises suppressing the vibration of the molten metal surface.

【0012】[0012]

【作用】以下、本発明について詳細に説明する。モ−ル
ドに向かってモ−ルドの左端上の1点を原点として、水
平方向にy軸,鉛直上向きにz軸をとり、時刻t,位置
yでの湯面の変位をz=ζ(y,t)とするとき、 ζ(y,t)[m]はN+1項(N≧1)の和
The present invention will be described in detail below. Taking a point on the left end of the mold as an origin toward the mold, a horizontal y-axis and a vertical upward z-axis are set, and the displacement of the molten metal surface at time t and position y is z = ζ (y , T), ζ (y, t) [m] is the sum of N + 1 terms (N ≧ 1)

【0013】[0013]

【数1】 [Equation 1]

【0014】で近似される。「′」は時間微分を表す。
n [1/m]は次式で表される。
Is approximated by "'" Represents a time derivative.
k n [1 / m] is represented by the following equation.

【0015】 kn =nπ/L(1≦n≦N) ・・・(2) L[m]はモ−ルド幅である。x0 (t)[m]は湯面
の平均レベル、xn ′(t)[m]は湯面のn次の振動
モ−ドのモ−ド変位であり、それぞれ次の微分方程式で
表される。
K n = nπ / L (1 ≦ n ≦ N) (2) L [m] is a mold width. x 0 (t) [m] is the average level of the molten metal surface, and x n ′ (t) [m] is the mode displacement of the nth-order vibration mode of the molten metal surface, which is expressed by the following differential equations. To be done.

【0016】 x0 ′(t)=U0 u(t)−W(t), xn ″(t)+gknn (t)=Un u(t)(1≦n≦N)・・・(3) gは重力加速度で、g=9.8[m/s2]である。X 0 ′ (t) = U 0 u (t) −W (t), x n ″ (t) + gk n x n (t) = U n u (t) (1 ≦ n ≦ N) · .. (3) g is the gravitational acceleration, and g = 9.8 [m / s 2 ].

【0017】W(t)[m/s]は引き抜き速度であ
る。
W (t) [m / s] is a drawing speed.

【0018】Uo [m/s],Un [m/s]は次式で
表される。
U o [m / s] and U n [m / s] are expressed by the following equations.

【0019】[0019]

【数2】 [Equation 2]

【0020】ノズルからの注湯速度のy方向の分布はU
(y)u(t)で表され、U(y)の次元は[m/
s],u(t)は無次元である。U(y)は、u(t)
=1のときのノズルからの注湯速度のy方向の分布であ
り、ノズルの寸法・形状およびモ−ルド内での位置によ
り決定する。式(3)から、u(t)は、重みU0 で湯
面の平均レベルに影響を与え、重みUn で湯面のn次の
振動モ−ドに影響を与える。
The distribution of the pouring speed from the nozzle in the y direction is U
(Y) is represented by u (t), and the dimension of U (y) is [m /
s], u (t) are dimensionless. U (y) is u (t)
It is the distribution of the pouring speed from the nozzle in the y direction when = 1 and is determined by the size and shape of the nozzle and the position in the mold. From the equation (3), u (t) affects the average level of the molten metal surface with the weight U 0 , and affects the n-th order vibration mode of the molten metal surface with the weight U n .

【0021】本発明は、以上の知見をもとになされたも
のである。以下に、本発明の作用について、図1を参照
しながら詳細に説明する。
The present invention is based on the above findings. The operation of the present invention will be described in detail below with reference to FIG.

【0022】図1は、本発明において、二か所での湯面
レベル測定値を用いる場合の、湯面レベル制御のため
の、注湯量制御システム構成を示したものである。これ
は、上述のモデルでN=1の場合に基づいている。図1
で、三角形の中に積分記号を書いたものは積分器,大き
い円の中に変数を書いたものは変数の値を乗じる乗算
器,小さい円の中に加算記号を書いたものは加算器,小
さい円の中に減算記号を書いたものは減算器を表す。こ
のうち、減算器は減算の順序を明示するために、加算記
号と減算記号とを添えてある。「プラント」は、注湯量
指令値を入力とする注湯量操作器,注湯ノズル,モ−ル
ド等の湯面プロセス要素、および、湯面レベル測定値を
出力とする湯面検出器等からなる。
FIG. 1 shows the configuration of a pouring amount control system for controlling the level of the molten metal when the measured values of the molten metal level at two points are used in the present invention. This is based on the case of N = 1 in the above model. Figure 1
, The one with the integral symbol written in the triangle is the integrator, the one with the variable written in the large circle is the multiplier that multiplies the value of the variable, the one with the addition symbol written in the small circle is the adder, A subtraction symbol written in a small circle represents a subtractor. Of these, the subtractor is provided with an addition symbol and a subtraction symbol to clearly indicate the order of subtraction. The "plant" is composed of a pouring amount operation device that receives a pouring amount command value, a pouring nozzle, a pouring process element such as a mold, and a pouring detector that outputs a pouring level measurement value. .

【0023】二式の湯面レベル検出器を用いて、湯面レ
ベルを水平方向に互いに異なる位置y=y1 ,y=y2
(y1 ≠y2 )の二か所で測定し、その湯面レベル測定
値をそれぞれ湯面レベル測定値1 ζ1 (t)=ζ(y1 ,t) ・・・(5) 湯面レベル測定値2 ζ2 (t)=ζ(y2 ,t) ・・・(6) とする。湯面レベル測定値1および湯面レベル測定値2
は式(1)より
Using the two types of molten metal level detectors, the molten metal levels are horizontally different from each other at positions y = y 1 and y = y 2.
(Y 1 ≠ y 2 ), and the melt level measurement values are measured at the melt level level 1 ζ 1 (t) = ζ (y 1 , t) (5) Level measurement value 2 ζ 2 (t) = ζ (y 2 , t) (6) Surface level measurement value 1 and surface level measurement value 2
Is from equation (1)

【0024】[0024]

【数3】 [Equation 3]

【0025】と表される。これより、x0 (t),x
1 ′(t)は
It is expressed as From this, x 0 (t), x
1 '(t) is

【0026】[0026]

【数4】 [Equation 4]

【0027】と表される。ここで、It is expressed as follows. here,

【0028】[0028]

【数5】 [Equation 5]

【0029】である。[0029]

【0030】モ−ダルフィルタに入力された湯面レベル
測定値1および湯面レベル測定値2より、式(9)のa
11 ,a12 ,a21 ,a22 を乗じる乗算器および加算器
を用いて、式(8)により、湯面の平均レベルx0
(t)および湯面の1次の振動モ−ドのモ−ド変位x
1 ′(t)が求められる。モ−ド変位x1 ′(t)は、
積分器により演算され、x1 (t)が求められる。x
1 ′(t),x1 (t)は湯面の1次の振動モ-ドの状態
と呼ばれる。x0 (t),x1 ′(t),x1 (t)は状
態と呼ばれる。すなわち、モ−ダルフィルタは、湯面レ
ベル測定値1および湯面レベル測定値2から状態を演算
する。演算された状態x0 (t),x1 ′(t),x1
(t)から、乗算器および加算器により、注湯量指令値
1を演算する。
From the molten metal level measured value 1 and the molten metal level measured value 2 input to the modal filter, a in the equation (9) is obtained.
Using the multiplier and the adder that multiply 11 , a 12 , a 21 , and a 22 , the average level x 0 of the molten metal surface is calculated by the equation (8).
(T) and the mode displacement x of the primary vibration mode of the molten metal surface
1 '(t) is required. The mode displacement x 1 ′ (t) is
It is calculated by an integrator and x 1 (t) is obtained. x
1 '(t), x 1 (t) is called the state of the first vibration mode of the molten metal surface. x 0 (t), x 1 ′ (t), x 1 (t) are called states. That is, the modal filter calculates the state from the melt level measurement value 1 and the melt level measurement value 2. Calculated state x 0 (t), x 1 ′ (t), x 1
From (t), the pouring amount command value 1 is calculated by the multiplier and the adder.

【0031】湯面の平均レベルに影響を与える外乱とし
ては、注湯量操作器の特性の変動、鋳造速度の変動など
が考えられる。湯面レベル目標値と湯面レベル測定値1
から、減算器,積分器および乗算器を用いて注湯量指令
値2を演算し、注湯量指令値2と注湯量指令値1から、
減算器を用いて注湯量指令値を演算する。この部分は、
湯面の平均レベルを目標値に追従させ、湯面の平均レベ
ルの影響を与える外乱を補償する。
Disturbances that affect the average level of the molten metal surface are considered to be fluctuations in the characteristics of the pouring amount operation device, fluctuations in the casting speed, and the like. Target surface level and measured surface level 1
Then, the pouring amount command value 2 is calculated using a subtractor, an integrator, and a multiplier, and from the pouring amount command value 2 and the pouring amount command value 1,
A pouring amount command value is calculated using a subtractor. This part is
The average level of the molten metal surface is made to follow the target value, and the disturbance that affects the average level of the molten metal surface is compensated.

【0032】湯面制御の目的は、湯面レベルを与えられ
た目標値に追従させ、湯面レベルに影響を与える外乱を
補償し、湯面の振動を抑制することである。すなわち、
0(t),x1 ′(t)において、湯面の平均レベルx
0 (t)に影響を与える外乱を補償し、湯面の平均レベ
ルx0 (t)を目標値に追従させ、振動のモ−ド変位x
1 ′(t)を漸近的に零に近づけることにより目的の制
御が達成される。本発明では、注湯量指令値1が、湯面
の平均レベルx0 (t)を目標値に追従させ、振動のモ
−ド変位x1 ′(t)を漸近的に零に近づけ、注湯量指
令値2が、湯面の平均レベルx0 (t)に影響を与える
外乱を補償することにより目的の制御を達成している。
k,k0 ,k11 ,k10 を乗じる乗算器において、k,k
0 ,k11,k10 の値は、湯面の振動および湯面の平均レ
ベルを目標値に収束させる速度(応答速度)に影響を与
える重要な作用をするので、実際のプラントで実験して
適正値を決定することが望ましい。
The purpose of the molten metal level control is to cause the molten metal level to follow a given target value, compensate for disturbances that affect the molten metal level, and suppress vibration of the molten metal level. That is,
At x 0 (t), x 1 ′ (t), the average level x
The disturbance that affects 0 (t) is compensated, the average level x 0 (t) of the molten metal surface is made to follow the target value, and the vibration mode displacement x
The desired control is achieved by asymptotically approaching 1 '(t) to zero. According to the present invention, the pouring amount command value 1 causes the average level x 0 (t) of the molten metal surface to follow the target value, and the vibration mode displacement x 1 ′ (t) asymptotically approaches zero. The command value 2 achieves the target control by compensating for the disturbance that affects the average level x 0 (t) of the molten metal surface.
In the multiplier that multiplies k, k 0 , k 11 , and k 10 , k, k
The values of 0 , k 11 , and k 10 have important effects that affect the vibration of the molten metal surface and the speed at which the average level of the molten metal surface converges to the target value (response speed). It is desirable to determine an appropriate value.

【0033】以上で、二か所で湯面レベルを測定し、二
か所の測定値を用いる場合を図1に基づき説明を行っ
た。図3に三か所で湯面レベルを測定し、三か所の湯面
レベル測定値を用いる場合を示す。これは、上述のモデ
ルでN=2の場合に基づいている。この場合、モ−ダル
フィルタは、9個の乗算器、4個の加算器、2個の積分
器をもち、三か所で測定した湯面レベルが入力され、5
個の状態が出力される。モ−ダルフィルタから出力され
た5個の状態から、5個の乗算器、4個の加算器を用い
て注湯量指令値1が演算される。注湯量指令値2は、二
か所での湯面レベル測定値を用いる場合と全く同様に演
算される。注湯量指令値は、注湯量指令値2と注湯量指
令値1から、減算器を用いて演算される。
The case where the molten metal level is measured at two points and the measured values at two points are used has been described above with reference to FIG. FIG. 3 shows a case where the molten metal level is measured at three locations and the measured molten metal level at three locations is used. This is based on the case of N = 2 in the above model. In this case, the modal filter has nine multipliers, four adders, and two integrators, and the melt level measured at three points is input to the modal filter.
Status is output. From the 5 states output from the modal filter, the pouring amount command value 1 is calculated using 5 multipliers and 4 adders. The pouring amount command value 2 is calculated in exactly the same manner as when the measured values of the molten metal level at two places are used. The pouring amount command value is calculated from the pouring amount command value 2 and the pouring amount command value 1 using a subtracter.

【0034】以上の展開は、一般のN(N≧1)につい
て、N+1か所での湯面レベル測定値を用いる場合に拡
張される。この場合、モ−ダルフィルタは、(N+1)
2 個の乗算器、N2 個の加算器、N個の積分器をもち、
N+1か所で測定した湯面レベルが入力され、2N+1
個の状態が出力される。モ−ダルフィルタから出力され
た2N+1個の状態から、2N+1個の乗算器、2N個
の加算器を用いて注湯量指令値1が演算される。注湯量
指令値2は、二か所での湯面レベル測定値を用いる場合
と全く同様に演算される。注湯量指令値は、注湯量指令
値2と注湯量指令値1から、減算器を用いて演算され
る。
The above expansion is extended to the general N (N ≧ 1) when using the melt level measurement values at N + 1 places. In this case, the modal filter is (N + 1)
Has 2 multipliers, N 2 adders, N integrators,
The bath level measured at N + 1 places is input and 2N + 1
Status is output. From the 2N + 1 states output from the modal filter, the pouring amount command value 1 is calculated using 2N + 1 multipliers and 2N adders. The pouring amount command value 2 is calculated in exactly the same manner as when the measured values of the molten metal level at two places are used. The pouring amount command value is calculated from the pouring amount command value 2 and the pouring amount command value 1 using a subtracter.

【0035】[0035]

【実施例】本発明をシミュレ−ションにより実施した例
を図2に示す。図2は、図1すなわち二か所での湯面レ
ベル測定値を用いる場合を実施した例である。実線は本
発明の湯面レベル制御方法の場合の湯面レベル推移を、
破線は従来のPI制御方法による湯面レベル制御の場合
の湯面レベル推移を示す。図2の(a)では、時刻t<
0で引き抜き速度0.1〔m/s〕の定常状態の後、t
=0で湯面レベル目標値を+1〔cm〕変更した場合
を、図2の(b)は、t=0で引き抜き速度に+1〔c
m/s〕の外乱が加わった場合のモ−ルドの左端での湯
面レベルを示している。横軸は時刻で単位は〔se
c〕、縦軸は左端の湯面レベルで単位は〔cm〕であ
る。モ−ルドの幅をL=1〔m〕とし、0.25〔m〕
の幅のノズルをノズルの左端とモ−ルドの中心が一致す
るように位置している。本発明の制御方法(本発明例)
では、湯面レベルはモ−ルドの両端で測定しているの
で、式(9)でy1 =0、y2 =Lとおくことにより、 a11 =0.5, a12 =0.5, a21 =0.5, a22 =−0.5 ・・・(10) が得られる。種々のシミュレ−ションを行い、湯面レベ
ル測定値の安定性、速応性を考慮して、各パラメ−タ
は、 k0 =40, k10 =−240, k11 =−80 k=45 ・・・(11) と設定した。PI制御方法(比較例)では、湯面レベル
をモ−ルドの左端の一か所で測定し、PI制御器の伝達
関数を (c0 +c1 p)/p ・・・(12) としたとき、本発明例と速応性が同程度になるように、
各パラメ−タは、 c0 =15, c1 =5 ・・・(13) と設定した。
FIG. 2 shows an example in which the present invention is carried out by simulation. FIG. 2 is an example in which FIG. 1 is used, that is, the case where the measured values of the molten metal level at two locations are used. The solid line shows the level transition of the level in the case of the level control method of the present invention,
The broken line shows the transition of the molten metal level in the case of the molten metal level control by the conventional PI control method. In FIG. 2A, time t <
At a steady state with a drawing speed of 0.1 [m / s] at 0, t
2 (b), the drawing speed is changed to +1 [c] at t = 0 when the target level value is changed by +1 [cm] at = 0.
m / s] shows the level of the molten metal at the left end of the mold when a disturbance is applied. The horizontal axis is time and the unit is [se
c], the vertical axis is the level of the molten metal at the left end, and the unit is [cm]. The width of the mold is L = 1 [m] and 0.25 [m]
The nozzle of the width is positioned so that the left end of the nozzle and the center of the mold coincide with each other. Control method of the present invention (example of the present invention)
Then, since the molten metal level is measured at both ends of the mold, by setting y 1 = 0 and y 2 = L in the equation (9), a 11 = 0.5, a 12 = 0.5 , A 21 = 0.5, a 22 = −0.5 (10) are obtained. In consideration of the stability and quick response of the measured value of the molten metal surface level by performing various simulations, each parameter is k 0 = 40, k 10 = -240, k 11 = -80 k = 45・ ・ (11) was set. In the PI control method (comparative example), the molten metal level was measured at one location on the left end of the mold, and the transfer function of the PI controller was (c 0 + c 1 p) / p (12). At this time, so that the quick response is similar to that of the example of the present invention,
Each parameter was set as c 0 = 15, c 1 = 5 ... (13).

【0036】図2の(a)は、目標値への追従の様子を
示し、図2の(b)は、外乱の補償の様子を示してい
る。PI制御方法(比較例)では、目標値への追従、外
乱の補償いずれの場合も湯面レベル測定値は振動的であ
るのに対して、本発明の制御方法(本発明例)では、目
標値への追従、外乱の補償いずれの場合も速やかに行わ
れ、湯面レベルは実質上振動していない。
FIG. 2A shows how the target value is followed, and FIG. 2B shows how the disturbance is compensated. In the PI control method (comparative example), the measured level of the molten metal surface is oscillating in both cases of following the target value and compensating for the disturbance. Both the tracking of the value and the compensation of the disturbance are performed promptly, and the molten metal level does not substantially vibrate.

【0037】[0037]

【発明の効果】本発明によれば、湯面の平均レベルを目
標値に追従させ、外乱を補償するとともに、湯面の振動
を積極的に抑制することができ、連続鋳造においては製
品の品質および歩留まりの向上、操業率の向上、操業時
の安全性の向上の効果がある。
According to the present invention, the average level of the molten metal surface can be made to follow the target value, the disturbance can be compensated, and the vibration of the molten metal surface can be actively suppressed. It also has the effects of improving yield, improving the operating rate, and improving the safety during operation.

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

【図1】 本発明を、二か所の湯面レベル測定値を用い
る態様で実施する湯面レベル制御系の演算システムを示
すブロック図である。
FIG. 1 is a block diagram showing a calculation system of a molten metal level control system for carrying out the present invention in a mode in which measured values of molten metal level at two places are used.

【図2】 本発明を実施する場合と従来例を実施する場
合の湯面レベルの時系列推移を示すグラフであり、図2
の(a)は目標値を変更した直後の湯面レベル変動を、
図2の(b)は鋳片引抜き速度が一時的に変動したとき
の湯面レベル変動を示す。
FIG. 2 is a graph showing a time series transition of a molten metal level when the present invention is carried out and when a conventional example is carried out.
(A) shows the fluctuation of the molten metal level immediately after the target value is changed,
FIG. 2B shows the fluctuation of the molten metal level when the slab drawing speed temporarily changes.

【図3】 本発明を、三か所の湯面レベル測定値を用い
る態様で実施する湯面レベル制御系の演算システムを示
すブロック図である。
FIG. 3 is a block diagram showing an arithmetic system of a molten metal level control system for carrying out the present invention in a mode using the measured molten metal level at three points.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 双ベルト連続鋳造の湯面制御方法におい
て、 (イ) 湯面レベルを水平方向に互いに異なる位置で二
か所以上で測定し、 (ロ) モ−ダルフィルタ処理により、上記二か所上以
上での湯面レベル測定値をいて湯面の平均レベルおよ
び一組以上の湯面の振動モ−ド演算し、 (ハ) 上記湯面の平均レベルおよび上記振動モ−ドか
ら注湯量指令値1を演算し、 (ニ) 湯面レベル目標値と(イ)で測定された湯面レ
ベル測定値のうちの一つから注湯指令値2を演算し、 (ホ) 上記注湯量指令値1と注湯量指令値2から注湯
量指令値を演算し、 (ヘ) (ホ)で演算された注湯量指令値を注湯量操作
器に出力する、 ことにより、湯面の平均レベルに影響を与える外乱を補
償し、湯面の平均レベルを目標値に追従にさせるととも
に、湯面の振動を抑制することを特徴とする双ベルト連
続鋳造の湯面制御方法。
1. A molten metal surface level control method for a twin-belt continuous casting, measured in (b) molten metal surface level two places or more at different positions in the horizontal direction, (b) mode - by Dal filtering, the two- calculates the de average level and the vibration mode of (c) above the melt surface - - vibration mode of the mean level and single Kumi以 Kaminoyu surface of the molten metal surface by have use the melt surface level measurement at least on the locations from de The pouring amount command value 1 is calculated, and (d) the pouring command value 2 is calculated from one of the melt surface level target value and the melt surface level measured value measured in (a). The pouring amount command value is calculated from the pouring amount command value 1 and the pouring amount command value 2, and the pouring amount command value calculated in (f) and (e) is output to the pouring amount controller, whereby the average level of the pouring surface It compensates for disturbances that affect the A molten metal level control method for twin-belt continuous casting characterized by suppressing surface vibration.
JP7186391A 1991-04-04 1991-04-04 Twin-belt continuous casting level control method Expired - Fee Related JPH0751257B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7186391A JPH0751257B2 (en) 1991-04-04 1991-04-04 Twin-belt continuous casting level control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7186391A JPH0751257B2 (en) 1991-04-04 1991-04-04 Twin-belt continuous casting level control method

Publications (2)

Publication Number Publication Date
JPH04309439A JPH04309439A (en) 1992-11-02
JPH0751257B2 true JPH0751257B2 (en) 1995-06-05

Family

ID=13472786

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7186391A Expired - Fee Related JPH0751257B2 (en) 1991-04-04 1991-04-04 Twin-belt continuous casting level control method

Country Status (1)

Country Link
JP (1) JPH0751257B2 (en)

Also Published As

Publication number Publication date
JPH04309439A (en) 1992-11-02

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