EP2762251B1 - Procédé et dispositif de coulée d'une tige - Google Patents
Procédé et dispositif de coulée d'une tige Download PDFInfo
- Publication number
- EP2762251B1 EP2762251B1 EP14151733.4A EP14151733A EP2762251B1 EP 2762251 B1 EP2762251 B1 EP 2762251B1 EP 14151733 A EP14151733 A EP 14151733A EP 2762251 B1 EP2762251 B1 EP 2762251B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- casting
- regulating
- volume flow
- cast
- width
- 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.)
- Not-in-force
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/16—Controlling or regulating processes or operations
- B22D11/168—Controlling or regulating processes or operations for adjusting the mould size or mould taper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D11/00—Continuous casting of metals, i.e. casting in indefinite lengths
- B22D11/16—Controlling or regulating processes or operations
- B22D11/18—Controlling or regulating processes or operations for pouring
- B22D11/181—Controlling or regulating processes or operations for pouring responsive to molten metal level or slag level
Definitions
- the invention relates to a method and apparatus for casting a strand having a width b and a thickness d, wherein liquid metal in an intermediate container having a drain opening for flowing off the liquid metal with a flow rate V through a pouring tube into a continuous casting mold for casting the strand with a predetermined casting speed v cast is provided.
- the volume flow V of liquid metal in the pouring tube is measured as actual value V actual by means of a flow sensor.
- the G garbageLiteLite Little h of the liquid metal in the continuous casting mold is detected as the actual value H IST by G fauxLitemessooth.
- the G convinceadorproof way h and the volume flow V of the liquid metal are by means of a control device in accordance with the measured actual values h IST , V ⁇ Is to predetermined target values h SOLL , V target controlled by driving a closure element, which is arranged at the outlet opening of the intermediate container or in the pouring tube ,
- the width b of the strand is controlled with adjustable narrow sides.
- the strand is guided by means of rollers arranged parallel to the broad side of the strand. This ensures the thickness d of the strand.
- the narrow sides of the strand have no support in the area below the mold.
- the strand thus spreads and bulges in the region below the mold in the width direction, ie transversely to the casting direction.
- the width of the strand can reach several percent of the nominal width.
- the Japanese Patent Application JP S 61232049 discloses a method for adjusting the width of a continuous casting mold. Specifically, the desired width of the mold, the changes in the mold width at the beginning and at the end of a continuous casting process and the casting speed are entered as parameters in a computing unit, which calculates suitable manipulated variables for adjusting the mold width from these input parameters. As a result, a high-speed casting is possible, in which the variations of the mold width are reduced, even if otherwise the mold width fluctuates greatly during continuous casting.
- optical systems such as laser triangulation (eg LAP laser, LIMAB (SlabProfiler)), for the optical width measurement of the strand are known.
- laser triangulation eg LAP laser, LIMAB (SlabProfiler)
- LAP laser LAP laser
- LIMAB LIMAB
- Such laser-based measuring systems are used behind the flame cutting machines in a continuous casting plant, since the high material temperature prevents earlier measurement.
- the object of the invention is to optimize in a known method and a known device for casting a strand, the adjustment of the width of the strand to the effect that an early detection of the spreading of the strand takes place in order to achieve an immediate control of the width of the strand to be cast in order to improve the quality of the product with respect to the precision of the final dimensions of the strand. It is another object of the invention to use existing components of a continuous casting, in particular existing measuring means to save costs.
- the method is characterized in that a width correction .DELTA.b as a function of a determined volume flow control difference from the measured actual value V ⁇ Ist and the predetermined desired value V ⁇ soll of the volume flow V ⁇ under Considering the thickness d of the strand to be cast and the casting speed v cast is calculated in a first controller. Subsequently, the calculated width correction .DELTA.b as the first manipulated variable u 1 (t) to a first actuator for adjusting output of at least one narrow side of the casting mold, so that changing the width b of the article to be cast strand takes place.
- a height change .DELTA.h of the G garbageLitetown h is calculated as a function of the width correction .DELTA.b and output to a setpoint / actual value comparator of a second control loop.
- a G garbageLitetownnregeldifferenz e 2 (t) is determined from the measured actual value h IST , the predetermined setpoint h SOLL and the calculated height change .DELTA.h the G machineapt altar h and fed as input to a second controller of the second control loop for controlling the G faux Spiegeltown h.
- the volume flow V ⁇ is controlled taking into account the changed G dirtyaptiere Little h by driving the closure element .
- a width correction .DELTA.b as a function of a determined volumetric flow control difference from the measured actual value V ⁇ Is t and a predetermined desired value V ⁇ target the volumetric flow V ⁇ is calculated taking into account the thickness d of the strand to be cast and the casting speed v cast in a first controller results the advantage that an online calculation is possible.
- the calculated width correction .DELTA.b u is 1 in the form of the manipulated variable (t) to a first actuator for adjusting output of at least one narrow side of the casting mold, so that changing the width b of the article to be cast strand takes place. Due to the fast calculation of the width correction ⁇ b without deadlocking of the system, the width of the strand to be cast undergoes an immediate correction and rejects are avoided. Advantageously, a rapid reaction, so regulation, to the unwanted spreading of the strand to be cast and the current casting width of the continuous casting mold is adjusted.
- a height change .DELTA.h of the G garbageLitetown h is calculated as a function of the width correction ⁇ b, which is output to a setpoint / actual value comparator of a second control loop.
- a G garbageLitetown e 2 (t) from the measured actual value h IST , the predetermined setpoint h SOLL and the calculated height change .DELTA.h the G chiptage civilization h is determined as input for a second controller of the second control loop for controlling the G garbageLitesburg.
- the changing G garbageLitesburg h is corrected in the inner loop promptly.
- a continuous caster 100 for pouring liquid metal 200 with a controller 300 is shown.
- the liquid metal 200 ie the melt
- the drainage opening 130 is preferably closed with a closure element 120 that is adjustable.
- the closure element 120 is actuated by the regulating device 300 for opening or closing the outflow opening 130 of the intermediate container 140.
- the closure element 120 is preferably designed as a stopper rod or as a slide and is movable.
- a volume flow V ⁇ of liquid metal 200 in the pouring tube 150 is measured and detected as the actual value of the volume flow V ⁇ Ist .
- the continuous casting mold 160 with broad sides and adjustable narrow sides 170 receives the liquid metal 200.
- the liquid metal 200 forms a casting mirror 210, which has a casting level height h in the continuous casting mold 160.
- the casting-mirror height h in the continuous casting mold 160 is kept substantially constant with the aid of the regulating device 300 in order to ensure a required product quality.
- a strand 190 is subsequently produced from the liquid metal 200.
- the broad sides of the continuous casting mold 160 give the thickness d and the adjustable narrow sides 170 the width b of the strand 190 to be cast.
- the strand 190 is guided and supported by means of parallel to the broad side of the strand 190 arranged continuous casting 180. Due to these continuous casting rolls 180, the predetermined thickness d of the strand 190 is ensured below the mold.
- the control according to the invention counteracts this spread.
- the control device 300 regulates the volume flow V ⁇ of liquid metal 200 by outputting corresponding manipulated variables u 1 (t), u 2 (t) as actuating signals to the respective actuators 420, 520.
- the control device 300 receives as input variables an actual value of the volume flow V ⁇ Ist , which is detected by the flow sensor 440, an actual value of the casting mirror height h IST , which is detected by a G manLitemess worn 540, and target values of the volume flow V ⁇ Soll and the G fauxLite Little h should from a superior level for monitoring or regulating the casting process.
- Other variables that are processed by the control device 300 are the width b and thickness d of the strand 190 to be cast and the casting speed v cast .
- the control device 300 outputs a first manipulated variable u 1 (t) to the first actuator 420, preferably a hydraulic cylinder or a Spindle drive to adjust the at least one narrow side 170 of the continuous casting mold 160.
- a second manipulated variable u 2 (t) is output from the control device 300 to the second actuator 520 in order to adjust the position of the closure element 120 of the intermediate container 140 and thus to regulate the volume flow through the outflow opening 130.
- FIG. 2 a control scheme of the control device 300 is shown.
- the control scheme comprises two control loops, which act together as a cascade control.
- the control variable of a first control loop 400 is the volume flow V ⁇ of liquid metal 200.
- the control variable of a second control loop 500 is the casting level h of the liquid metal 200 in the continuous casting mold 160.
- the second control loop 500 is the inner loop of the cascade control.
- a target value V ⁇ target is specified by a higher level and performed on a first setpoint / actual value comparator 450 of the first control loop 400.
- the actual value of the volume flow V ⁇ Ist of liquid metal 200 detected by the flow sensor 440 is likewise given to the first setpoint / actual value comparator 450 of the first control loop 400.
- a volumetric flow control difference e 1 (t) results as an input variable for a first controller 410 in the first control loop 400.
- the first actuator 420 causes the at least one narrow side 170 the continuous casting mold 160 is adjusted on the basis of the calculated width correction .DELTA.b.
- This correction of the width of the continuous casting mold 160 counteracts the unwanted spreading of the strand 190 to be cast.
- the narrow sides 170 of the continuous casting mold 160 are set narrower if the actual value of the volume flow V ⁇ Ist is greater than the setpoint value of the volume flow V ⁇ Soll and vice versa.
- the second controller 510 calculates a second manipulated variable u 2 (t) for the second actuator 520, which adjusts the position of the closure element 120, whereupon the volume flow V ⁇ is regulated .
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Continuous Casting (AREA)
Claims (12)
- Procédé pour la coulée d'une barre (190) possédant une largeur b et une épaisseur d, présentant les étapes suivantes dans lesquelles :on met du métal en fusion (200) à disposition dans un distributeur (140) comprenant une ouverture d'évacuation (130) pour l'évacuation du métal en fusion (200) avec un courant volumique V̇ à travers un tube de coulée (150) dans une lingotière de coulée continue (160) pour la coulée de la barre (190) à une vitesse de coulée prédéfinie vcast ;on mesure le courant volumique V̇ du métal en fusion (200) dans le tube de coulée (150) à titre de valeur réelle V̇Ist au moyen d'un capteur du débit (440) ;on enregistre le niveau de coulée h du métal en fusion (200) dans la lingotière de coulée continue (160) à titre de valeur réelle hIST au moyen d'un dispositif de mesure du niveau de coulée (540) ;on règle le niveau de coulée h et le courant volumique V̇ du métal en fusion (200) au moyen d'un dispositif de réglage (300) en fonction des valeurs réelles mesurées hIST , V̇Ist à des valeurs de consigne prédéfinies h V̇ SOLL . V̇Soll , à travers l'excitation d'un élément de fermeture (120) qui est disposé à l'ouverture d'évacuation (130) du distributeur (140) ou dans le tube de coulée (150) ;caractérisé par le fait decalcule une correction de largeur Δb en fonction d'une différence déterminée de réglage du courant volumique e1(t) à partir de la valeur réelle mesurée V̇Ist et de la valeur de consigne prédéterminée V̇ Soll , en prenant en compte l'épaisseur d de la barre à couler (190) et la vitesse de coulée vcast dans un premier régulateur (410) ;transmettre la correction de largeur calculée Δb sous la forme d'une valeur de réglage u1(t) à un premier élément de réglage (420) pour le réglage d'au moins un petit côté (170) de la lingotière de coulée continue (160), si bien que l'on obtient une modification de la largeur b de la barre à couler (190) ;calculer une modification de la hauteur Δh du niveau de coulée h en fonction de la correction de largeur Δb afin de la transmettre à un deuxième comparateur de valeur de consigne/valeur réelle (550) d'un deuxième circuit de réglage (500) ;déterminer une différence de réglage du niveau de coulée e2(t) à partir de la valeur réelle mesurée hIst , de la valeur de consigne prédéfinie hSOLL et de la modification calculée de la hauteur Δh du niveau de coulée h, à titre de valeur d'entrée pour un deuxième régulateur (510) du deuxième circuit de réglage (500) pour le réglage du niveau de coulée h ; etrégler le courant volumique V̇ en prenant en compte le niveau de coulée modifié h à travers l'excitation de l'élément de fermeture (120).
- Procédé selon la revendication 1, caractérisé en ce que la valeur de consigne V̇Soll du courant volumique V̇ dépend de la vitesse de coulée vcast , de la largeur b et de l'épaisseur d de la barre à couler, conformément à la loi : V̇Soll = vcast * b * d.
- Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce qu'on utilise la différence de réglage du courant volumique e1(t) à partir de la valeur réelle mesurée V̇Ist et de la valeur de consigne prédéterminée V̇Soll du courant volumique V̇ , à titre de valeur d'entrée pour le premier régulateur (410) dans un premier circuit de réglage (400).
- Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce qu'on calcule la correction de largeur Δb comme suit : Δb= e1(t) * 1/(vcast*d).
- Procédé selon l'une quelconque des revendications précédentes, caractérisé en ce qu'on calcule la modification de la hauteur Δh du niveau de coulée h comme suit : Δh= Δb /b * hSOLL.
- Dispositif (100) pour la coulée d'une barre (190) possédant une largeur b et une épaisseur d pour la mise en oeuvre du procédé revendiqué selon l'une quelconque des revendications 1 à 5, présentant :un distributeur (140) pour la mise à disposition du métal en fusion (200), comprenant une ouverture d'évacuation (130) pour l'évacuation du métal en fusion (200) avec un courantvolumique V̇ à travers un tube de coulée (150) dans une lingotière de coulée continue (160) pour la coulée de la barre (190) à une vitesse de coulée prédéfinie vcast ;un élément de fermeture (120) à l'ouverture d'évacuation (130) du distributeur (140) ou dans le tube de coulée (150) pour influencer le courant volumique V̇ du métal en fusion (200) ;un capteur du débit (440) pour la mesure le courant volumique V̇ du métal en fusion (200) dans le tube de coulée (150) à titre de valeur réelle V̇Ist ;un dispositif de mesure du niveau de coulée (540) pour enregistrer le niveau de coulée h du métal en fusion (200) dans la lingotière de coulée continue (160) à titre de valeur réelle hIST .un dispositif de réglage (300) pour le réglage du niveau de coulée h et du courant volumique V̇ du métal en fusion (200) en fonction des valeurs réelles mesurées hIST, V̇Ist à des valeurs de consigne prédéfinies hSOLL, V̇Soll , à travers l'excitation de l'élément de fermeture (120) ;caractérisé en ce qu'un premier régulateur (410) dans le dispositif de réglage (300) est réalisé pour calculer une correction Δb de la largeur b de la barre à couler (190) et est réalisé pour le calcul d'une modification de la hauteur Δh du niveau de coulée h en fonction de la correction de largeur Δb;un premier élément de réglage (420) est réalisé pour le réglage d'au moins un petit côté (170) de la lingotière de coulée continue (160), en faisant appel à la correction de largeur Δb, sous la forme de la valeur de réglage u1(t), si bien que l'on obtient une modification de la largeur b de la barre à couler (190) ;un deuxième régulateur (510) dans le dispositif de réglage de (300) est réalisé pour le réglage du niveau de coulée h en prenant en compte la modification de hauteur calculée Δh ; etl'élément de fermeture (120) pour le réglage du courant volumique V̇ peut être excité en faisant appel au niveau de coulée modifié h.
- Dispositif selon la revendication 6, caractérisé en ce que le premier élément de réglage (420) est réalisé sous la forme d'un cylindre hydraulique ou d'un entraînement à broche.
- Dispositif selon l'une quelconque des revendications 6 à 7, caractérisé en ce que l'élément de fermeture (120) est réalisé sous la forme d'une quenouille ou sous la forme d'un coulisseau.
- Dispositif selon la revendication 8, caractérisé en ce que la quenouille est disposée de manière à pouvoir se déplacer en direction verticale, au-dessus de l'ouverture d'évacuation (130).
- Dispositif selon la revendication 8, caractérisé en ce que le coulisseau est disposé de manière à pouvoir se déplacer à l'horizontale en dessous de l'ouverture d'évacuation (130) du distributeur (140) pour la fermeture de l'ouverture d'évacuation (130).
- Dispositif selon l'une quelconque des revendications 6 à 10, caractérisé en ce que le capteur du débit (440) est réalisé sous la forme d'un anémomètre qui mesure la force de Lorentz.
- Dispositif selon l'une quelconque des revendications 6 à 11, caractérisé en ce que le dispositif de réglage (300) peut être réalisé avec au moins deux circuits de réglage (400, 500) qui sont montés en cascade.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102013001556 | 2013-01-30 | ||
DE201310214811 DE102013214811A1 (de) | 2013-01-30 | 2013-07-30 | Verfahren und Vorrichtung zum Gießen eines Strangs |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2762251A1 EP2762251A1 (fr) | 2014-08-06 |
EP2762251B1 true EP2762251B1 (fr) | 2015-07-08 |
Family
ID=49955232
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP14151733.4A Not-in-force EP2762251B1 (fr) | 2013-01-30 | 2014-01-20 | Procédé et dispositif de coulée d'une tige |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP2762251B1 (fr) |
DE (1) | DE102013214811A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3173166A1 (fr) | 2015-11-26 | 2017-05-31 | SMS group GmbH | Procédé et dispositif de réglage de la largeur d'une barre métallique coulée en continu |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AT515244A2 (de) | 2013-12-30 | 2015-07-15 | Inteco Special Melting Technologies Gmbh | Verfahren zur Herstellung von langen Gussblöcken großen Querschnitts |
CN109848387B (zh) * | 2017-11-30 | 2021-02-05 | 上海梅山钢铁股份有限公司 | 一种防止连铸结晶器溢钢的自动控制方法 |
CN111006728B (zh) * | 2019-12-23 | 2022-02-18 | 上海一诺仪表有限公司 | 流量自控仪转换器和流量自控仪转换器的控制方法 |
WO2024017831A1 (fr) * | 2022-07-18 | 2024-01-25 | Primetals Technologies Austria GmbH | Capteur virtuel de niveau de remplissage pour un moule d'une machine de coulée continue |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61232049A (ja) * | 1985-04-09 | 1986-10-16 | Nippon Steel Corp | 連鋳鋳片幅一定制御方法 |
EP2376243B1 (fr) | 2008-12-11 | 2013-02-13 | SMS Siemag AG | Dispositif de détection du débit, et procédé correspondant |
DE102011085932A1 (de) | 2011-06-07 | 2012-12-13 | Sms Siemag Ag | Verfahren zum Regeln der Höhe des Gießspiegels in einer Kokille einer Stranggießanlage |
-
2013
- 2013-07-30 DE DE201310214811 patent/DE102013214811A1/de not_active Withdrawn
-
2014
- 2014-01-20 EP EP14151733.4A patent/EP2762251B1/fr not_active Not-in-force
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3173166A1 (fr) | 2015-11-26 | 2017-05-31 | SMS group GmbH | Procédé et dispositif de réglage de la largeur d'une barre métallique coulée en continu |
DE102015223496A1 (de) | 2015-11-26 | 2017-06-01 | Sms Group Gmbh | Verfahren und Vorrichtung zum Einstellen der Breite eines stranggegossenen Metallstrangs |
Also Published As
Publication number | Publication date |
---|---|
DE102013214811A1 (de) | 2014-07-31 |
EP2762251A1 (fr) | 2014-08-06 |
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