EP2762251B1 - Method and device for casting a strand - Google Patents
Method and device for casting a strand 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
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- EP
- European Patent Office
- Prior art keywords
- casting
- regulating
- volume flow
- cast
- width
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- 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)
Description
Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Gießen eines Stranges mit einer Breite b und einer Dicke d, wobei flüssiges Metall in einem Zwischenbehälter mit einer Abflussöffnung zum Abfließen des flüssigen Metalls mit einem Volumenstrom V durch ein Gießrohr in eine Stranggießkokille zum Gießen des Stranges mit einer vorgegebenen Gießgeschwindigkeit vcast bereitgestellt wird. Der Volumenstrom V an flüssigem Metall im Gießrohr wird als Istwert VIst mittels eines Durchflusssensors gemessen. Die Gießspiegelhöhe h des flüssigen Metalls in der Stranggießkokille wird als Istwert HIST mittels Gießspiegelmesseinrichtung erfasst. Die Gießspiegelhöhe h und der Volumenstroms V des flüssigen Metalls werden mittels einer Regelungseinrichtung nach Maßgabe der gemessenen Istwerte hIST, V̇Ist auf vorgegebene Sollwerte hSOLL, VSoll geregelt durch Ansteuern eines Verschlusselements, das an der Abflussöffnung des Zwischenbehälters oder in dem Gießrohr angeordnet ist.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 Gießspiegelhöhe h of the liquid metal in the continuous casting mold is detected as the actual value H IST by Gießspiegelmesseinrichtung. The Gießspiegelhöhe 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 , V̇ 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 ,
Beim Stranggießen von Metallen in einer Stranggießanlage wird die Breite b des Strangs mit verstellbaren Schmalseiten geregelt. Im Bereich der Sekundärkühlung, also unterhalb der Stranggießkokille, wird der Strang mit Hilfe parallel zur Breitseite des Strangs angeordneten Rollen geführt. Dadurch wird die Dicke d des Strangs gewährleistet. Die Schmalseiten des Strangs haben im Bereich unterhalb der Kokille keine Stützung. Infolge des ferrostatischen Druckes breitet und baucht sich der Strang somit im Bereich unterhalb der Kokille in Breitenrichtung, also quer zur Gießrichtung, aus. Die Breitung des Strangs kann mehrere Prozent der nominellen Breite erreichen.In the continuous casting of metals in a continuous caster, the width b of the strand is controlled with adjustable narrow sides. Around Secondary cooling, ie below the continuous casting mold, 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. As a result of the ferrostatic pressure, 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.
In den Fachartikeln "
Die
Weiterhin sind Lösungen, basierend auf mechanischen Kantentastern bekannt; siehe "Messsysteme für Knüppel und Brammen" Broschüre herausgegeben von der LAP GmbH, Laserapplikationen, Zeppelinstraße 23, 21337 Lüneburg, Deutschland. Zu den Nachteilen solcher Systeme zählen das mechanische Spiel und die erforderliche Wartung der bewegten Komponenten in einer extrem hitzebelasteten Zone.Furthermore, solutions based on mechanical edge buttons are known; see "Measuring systems for billets and slabs" Brochure published by LAP GmbH, Laserapplikationen, Zeppelinstraße 23, 21337 Lüneburg, Germany. Disadvantages of such systems include mechanical play and the required maintenance of the moving components in an extremely heat-stressed zone.
Weiterhin sind optische Systeme, wie Laser-Triangulation (z.B. von LAP-Laser, LIMAB (SlabProfiler)), für die optische Breitenmessung des Strangs bekannt. Solche Laser-basierten Messsysteme werden hinter den Brennschneidmaschinen in einer Stranggießanlage eingesetzt, da die hohe Materialtemperatur eine frühere Messung verhindert.Furthermore, optical systems, such as laser triangulation (eg LAP laser, LIMAB (SlabProfiler)), for the optical width measurement of the strand are known. 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.
Bei diesen bekannten Systemen zur Breitenmessung des Strangs, wie beispielsweise die Lasermessung, ist der Abstand vom Kokillenaustritt, wo die Regelung der Strangbreite vorgenommen wird und dem Punkt, an dem die optischen Messsysteme installiert werden mehr als 20 Meter. Hieraus resultiert eine sehr große Totzeit zum Regeln der Strangbreite. Dies kann eine qualitative Herabstufung des gegossenen Produktes zur Folge haben.In these known systems for measuring the width of the strand, such as the laser measurement, the distance from Kokillenaustritt where the control of the strand width is made and the point at which the optical measuring systems are installed more than 20 meters. This results in a very large dead time for controlling the strand width. This can result in a qualitative downgrade of the cast product.
In den Druckschriften
Aufgabe der Erfindung ist es, bei einem bekannten Verfahren und einer bekannten Vorrichtung zum Gießen eines Stranges die Einstellung der Breite des Strangs dahingehend zu optimieren, dass eine frühe Detektion der Breitung des Strangs erfolgt, um eine sofortige Regelung der Breite des zu gießenden Stranges zu erreichen, damit die Qualität des Produktes bezüglich der Präzision der Endabmessungen des Strangs verbessert wird. Weiterhin ist es Aufgabe der Erfindung, vorhandene Komponenten einer Stranggießanlage, insbesondere vorhandene Messmittel zu verwenden, um Kosten zu sparen.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.
Diese Aufgabe wird gelöst durch das Verfahren nach Anspruch 1.This object is achieved by the method according to claim 1.
Das Verfahren ist dadurch gekennzeichnet, dass eine Breitenkorrektur Δb in Abhängigkeit einer ermittelten Volumenstromregeldifferenz aus dem gemessenen Istwert V̇Ist und dem vorgegebenen Sollwert V̇soll des Volumenstroms V̇ unter Berücksichtigung der Dicke d des zu gießenden Stranges und der Gießgeschwindigkeit vcast in einem ersten Regler berechnet wird. Anschließend wird die berechnete Breitenkorrektur Δb als erste Stellgröße u1(t) an ein erstes Stellglied zum Verstellen mindestens einer Schmalseite der Stranggießkokille ausgegeben, so dass eine Änderung der Breite b des zu gießenden Stranges erfolgt. Eine Höhenänderung Δh der Gießspiegelhöhe h wird in Abhängigkeit der Breitenkorrektur Δb berechnet und an einen Soll-/Istwert-Vergleicher eines zweiten Regelkreises ausgegeben. Eine Gießspiegelhöhenregeldifferenz e2(t) wird aus dem gemessenen Istwert hIST, dem vorgegebenen Sollwert hSOLL und der berechneten Höhenänderung Δh der Gießspiegelhöhe h ermittelt und als Eingangsgröße einem zweiten Regler des zweiten Regelkreis zum Regeln der Gießspiegelhöhe h zugeführt. Der Volumenstrom V̇ wird unter Berücksichtigung der geänderten Gießspiegelhöhe h durch Ansteuern des Verschlusselementes geregelt.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 V̇ Ist and the predetermined desired value V̇ soll of the volume flow V̇ 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 Gießspiegelhöhe 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 Gießspiegelhöhenregeldifferenz 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 Gießspiegelhöhe h and fed as input to a second controller of the second control loop for controlling the Gießspiegelhöhe h. The volume flow V̇ is controlled taking into account the changed Gießspiegelhöhe h by driving the closure element .
Dass gemäß Anspruch 1 eine Breitenkorrektur Δb in Abhängigkeit einer ermittelten Volumenstromregeldifferenz aus dem gemessenen Istwert V̇ Ist und einem vorgegebenen Sollwert V̇Soll des Volumenstroms V̇ unter Berücksichtigung der Dicke d des zu gießenden Stranges und der Gießgeschwindigkeit vcast in einem ersten Regler berechnet wird, ergibt den Vorteil, dass eine Online-Kalkulation möglich ist.That according to claim 1, a width correction .DELTA.b as a function of a determined volumetric flow control difference from the measured actual value V̇ Is t and a predetermined desired value V̇ target the volumetric flow V̇ 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.
Vorteilhafterweise wird die berechnete Breitenkorrektur Δb in Form der Stellgröße u1(t) an ein erstes Stellglied zum Verstellen mindestens einer Schmalseite der Stranggießkokille ausgegeben, so dass eine Änderung der Breite b des zu gießenden Stranges erfolgt. Durch die schnelle Berechnung der Breitenkorrektur Δb ohne Totzeitbehaftung des Systems erfährt die Breite des zu gießenden Stranges eine umgehende Korrektur und Ausschuss wird vermieden. Vorteilhafterweise erfolgt eine schnelle Reaktion, also Regelung, auf die unerwünschte Breitung des zu gießenden Stranges und die aktuelle Gießbreite der Stranggießkokille wird angepasst.Advantageously, 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 Δb 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.
Vorteilhafterweise wird eine Höhenänderung Δh der Gießspiegelhöhe h in Abhängigkeit der Breitenkorrektur Δb berechnet, die an einen Soll-/Istwert-Vergleicher eines zweiten Regelkreises ausgegeben wird. Vorteilhafterweise wird für einen zweiten Regler des zweiten Regelkreises zum Regeln der Gießspiegelhöhe h eine Gießspiegelhöhenregeldifferenz e2(t) aus dem gemessenen Istwert hIST, dem vorgegebenen Sollwert hSOLL und der berechneten Höhenänderung Δh der Gießspiegelhöhe h als Eingangsgröße ermittelt. Die sich ändernde Gießspiegelhöhe h wird im inneren Regelkreis zeitnah ausgeregelt.Advantageously, a height change .DELTA.h of the Gießspiegelhöhe h is calculated as a function of the width correction Δb, which is output to a setpoint / actual value comparator of a second control loop. Advantageously, a Gießspiegelhöhenregeldifferenz e 2 (t) from the measured actual value h IST , the predetermined setpoint h SOLL and the calculated height change .DELTA.h the Gießspiegelhöhe h is determined as input for a second controller of the second control loop for controlling the Gießspiegelhöhe. The changing Gießspiegelhöhe h is corrected in the inner loop promptly.
Dadurch, dass der Volumenstrom V̇ unter Berücksichtigung der geänderten Gießspiegelhöhe h durch Ansteuern des Verschlusselements geregelt wird, ergibt sich der Vorteil, dass sich der Volumenstrom auf die aktuelle Gießbreite einstellt und die Gießspiegelhöhe h weitgehend konstant gehalten wird, damit die Produktqualität stabil bleibt.The fact that the volume flow V̇ is controlled by controlling the closure element taking into account the changed Gießspiegelhöhe , there is the advantage that adjusts the flow on the current casting width and the Gießspiegelhöhe h is kept substantially constant, so that the product quality remains stable.
Gemäß einem ersten Ausführungsbeispiel ist der Sollwert V̇soll des Volumenstroms V̇ abhängig von der Gießgeschwindigkeit vcast, der Breite b und der Dicke d des zu gießenden Stranges (V̇Soll = vcast *b*d). Vorteilhafterweise ergibt sich somit ein Zusammenhang zwischen Volumenstrom und Breite des zu gießenden Stranges.According to a first embodiment, the desired value V̇ soll of the volume flow V̇ is dependent on the casting speed v cast , the width b and the thickness d of the strand to be cast (V̇S oll = v cast * b * d). Advantageously, this results in a relationship between the volume flow and the width of the strand to be cast.
Dadurch, dass eine Volumenstromregeldifferenz e1(t) aus dem gemessenen Istwert V̇Ist und dem Sollwert V̇Soll des Volumenstroms V̇ als Eingangsgröße für den ersten Regler in einem ersten Regelkreis verwendet wird und die Breitenkorrektur Δb wie folgt: Δb= e1(t) * 1/(vcast*d) berechnet wird, ergibt sich der Vorteil, dass die Istbreite des zu gießenden Stranges nicht mit einer aufwendigen zusätzlichen Messeinrichtung gemessen werden muss und vorteilhafterweise nicht totzeitbehaftet ist. Characterized in that a volumetric flow control difference e 1 (t) from the measured actual value V̇ Ist and the setpoint V̇ setpoint of the volumetric flow V̇ is used as an input variable for the first controller in a first control loop and the width correction Δb is as follows: Δb = e 1 (t) * 1 / (v cast * d) is calculated, there is the advantage that the actual width of the strand to be cast does not have to be measured with a complicated additional measuring device and advantageously is not subject to dead-time.
Vorteilhafterweise wird die Höhenänderung Δh der Gießspiegelhöhe h wie folgt berechnet: Δh= Δb /b * hSOLL
Dadurch ergibt sich der Vorteil, dass die Höhenregelung im inneren zweiten Regelkreis schneller und genauer erfolgt.Advantageously, the height change Δh of the casting-mirror height h is calculated as follows: Δh = Δb / b * h SOLL
This results in the advantage that the height control in the inner second control loop is faster and more accurate.
Die oben genannte Aufgabe wird weiterhin durch die beanspruchte Vorrichtung gemäß den Ansprüchen 6 bis 12 gelöst. Die Vorteile dieser Lösungen entsprechen den oben mit Bezug auf das Verfahren genannten Vorteilen.The above object is further achieved by the claimed device according to claims 6 to 12. The advantages of these solutions correspond to the advantages mentioned above with respect to the method.
Weitere vorteilhafte Ausgestaltungen der Vorrichtung und des Verfahrens der Erfindung sind in den abhängigen Ansprüchen angegeben.Further advantageous embodiments of the device and the method of the invention are specified in the dependent claims.
Der Beschreibung sind insgesamt zwei Figuren beigefügt, wobei
- Figur 1
- schematisch eine Stranggießanlage und
- Figur 2
- ein Regelschema
- FIG. 1
- schematically a continuous casting and
- FIG. 2
- a rule scheme
Die erfindungsgemäße Vorrichtung und das erfindungsgemäße Verfahren werden nachfolgend unter Bezugnahme auf die Figuren detailliert beschrieben.The device according to the invention and the method according to the invention are described in detail below with reference to the figures.
In
Eine derartige Führung und Stützung ist an den Schmalseiten des Stranges 190 im Bereich der Sekundärkühlung nicht gegeben. In Folge des ferrostatischen Drucks breitet und baucht sich der Strang 190 in diesem Bereich in Breitenrichtung, also quer zur Gießrichtung, aus und es entsteht eine unerwünschte Breitung des zu gießenden Strangs 190. Dies erfolgt insbesondere bei weichen Stahlgüten. Die Breitung des Strangs 190 kann mehrere Prozente der nominellen Breite b erreichen und wirkt sich nachteilig auf die Produktendabmessung und somit auf die Produktqualität aus.Such guidance and support is not given on the narrow sides of the strand 190 in the secondary cooling. As a result of the ferrostatic pressure, the strand 190 spreads and bulges in this area in the width direction, ie transversely to the casting direction, and an unwanted spreading of the strand 190 to be cast arises. This occurs in particular for soft steel grades. The spread of the strand 190 can reach several percent of the nominal width b and adversely affects the final product dimension and thus the product quality.
Die erfindungsgemäße Regelung wirkt dieser Breitung entgegen.The control according to the invention counteracts this spread.
Die Regelungseinrichtung 300 regelt den Volumenstrom V̇ an flüssigem Metall 200, indem sie entsprechende Stellgrößen u1(t), u2(t) als Stell-Signale an die jeweiligen Stellglieder 420, 520 ausgibt. Als Eingangsgrößen erhält die Regelungseinrichtung 300 insbesondere einen Istwert des Volumenstroms V̇Ist , der von dem Durchflusssensor 440 erfasst wird, einen Istwert der Gießspiegelhöhe hIST, der von einer Gießspiegelmesseinrichtung 540 erfasst wird, und Sollwerte des Volumenstroms V̇Soll und der Gießspiegelhöhe hsoll von einer übergeordneten Ebene zur Überwachung bzw. Regelung des Gießprozesses. Weitere Größen, die von der Regelungseinrichtung 300 verarbeitet werden sind die Breite b und Dicke d des zu gießenden Stranges 190 und die Gießgeschwindigkeit vcast. Die Regelungseinrichtung 300 gibt eine erste Stellgröße u1(t) an das erste Stellglied 420, vorzugsweise einen Hydraulikzylinder oder einen Spindelantrieb, um die mindestens eine Schmalseite 170 der Stranggießkokille 160 zu verstellen. Eine zweite Stellgröße u2(t) wird von der Regelungseinrichtung 300 an das zweite Stellglied 520 ausgegeben, um die Position des Verschlusselements 120 des Zwischenbehälters 140 zu verstellen und damit den Volumenstrom durch die Abflussöffnung 130 zu regeln.The
In
Für die primär zu regelnde Regelgröße, den Volumenstrom V̇ an flüssigem Metall 200, wird ein Sollwert V̇Soll von einer übergeordneten Ebene vorgegeben und auf einen ersten Soll-/Istwert-Vergleicher 450 des ersten Regelkreises 400 geführt. Dieser Sollwert V̇Soll ist abhängig von der Gießgeschwindigkeit vcast, der Breite b und der Dicke d des Stranges 190 gemäß folgender Gesetzmäßigkeit: V̇ Soll = vcast *b*d. Der von dem Durchflusssensor 440 erfasste Istwert des Volumenstroms V̇Ist an flüssigem Metall 200 wird ebenfalls auf den ersten Soll-/Istwert-Vergleicher 450 des ersten Regelkreises 400 gegeben. Aus dem gemessenen Istwert V̇Ist und dem vorgegebenen Sollwert V̇Soll des Volumenstroms ergibt sich eine Volumenstromregeldifferenz e1(t) als Eingangsgröße für einen ersten Regler 410 in dem ersten Regelkreis 400. Dieser erste Regler 410 berechnet die Breitenkorrektur Δb= e1(t) * 1/(vcast*d) als Stellgröße u1(t) für das erstes Stellglied 420. Das erste Stellglied 420 bewirkt, dass die mindestens eine Schmalseite 170 der Stranggießkokille 160 aufgrund der berechneten Breitenkorrektur Δb verstellt wird. Diese Korrektur der Breite der Stranggießkokille 160 wirkt der unerwünschten Breitung des zu gießenden Stranges 190 entgegen. Beispielsweise werden die Schmalseiten 170 der Stranggießkokille 160 enger eingestellt, wenn der Istwert des Volumenstroms V̇Ist größer als der Sollwert des Volumenstroms V̇ Soll ist und umgekehrt.For the controlled variable to be controlled primarily, the volume flow V̇ to
Die Verstellung der mindestens einen Schmalseite 170 der Stranggießkokille 160 bewirkt eine Höhenänderung Δh=Δb/b * h der Gießspiegelhöhe h des flüssigen Metalls 200 in der Stranggießkokille 160. Diese Höhenänderung Δh, ein vorgegebener Sollwert der Gießspiegelhöhe hSOLL und ein erfasster Istwert der Gießspiegelhöhe hIST werden auf einen zweiten Soll-Istwert-Vergleicher (550) des zweiten Regelkreises 500 geführt, der aus diesen Größen eine Gießspiegelhöhenegeldifferenz e2(t) = HSOLL - HIST - Δh bildet, die als Eingangsgröße für einen zweiten Regler 510 weitergeben wird. Der zweite Regler 510 berechnet eine zweite Stellgröße u2(t) für das zweite Stellglied 520, welches die Position des Verschlusselements 120 verstellt, worauf eine Regelung des Volumenstroms V̇ erfolgt.The adjustment of the at least one
Aufgrund der Verstellung der Schmalseiten 170 ergibt sich eine Änderung der Gießspiegelhöhe h des flüssigen Metalls 200. Der Istwert der Gießspiegelhöhe hIST wird erfasst und der innere Regelkreis, also der zweite Regelkreis 500, regelt die Gießspiegelhöhe h auf den vorgegebenen Sollwert hSOLL aus.Due to the adjustment of the
- 100100
- Stranggießanlagecontinuous casting plant
- 120120
- Verschlusselementclosure element
- 130130
- Abflussöffnungdrain opening
- 140140
- Zwischenbehälterintermediate container
- 150150
- Gießrohrcasting tube
- 160160
- Stranggießkokillecontinuous casting
- 170170
- Schmalseitenarrow side
- 180180
- Stranggießrollecontinuous casting
- 190190
- Strangstrand
- 200200
- flüssiges Metall (Schmelze)liquid metal (melt)
- 210210
- Gießspiegelmeniscus
- 300300
- Regelungseinrichtungcontrol device
- 400400
- erster Regelkreisfirst control loop
- 410410
- erster Reglerfirst controller
- 420420
- erstes Stellgliedfirst actuator
- 430430
- erste Regelstreckefirst controlled system
- 440440
- DurchflusssensorFlow Sensor
- 450450
- erster Soll-/Istwert-Vergleicherfirst setpoint / actual value comparator
- 500500
- zweiter Regelkreissecond control loop
- 510510
- zweiter Reglersecond controller
- 520520
- zweites Stellgliedsecond actuator
- 530530
- zweite Regelstreckesecond controlled system
- 540540
- GießspiegelmesseinrichtungGießspiegelmesseinrichtung
- 550550
- zweiter Soll-/Istwert-Vergleichersecond setpoint / actual value comparator
- V̇V
- Volumenstrom an flüssigem MetallVolume flow of liquid metal
- V̇Soll V̇ Soll
- Sollwert des VolumenstromsSetpoint of the volumetric flow
- V̇Ist V̇ is
- Istwert des VolumenstromsActual value of the volume flow
- hH
- Gießspiegelhöhecasting level
- hSOLL h SHOULD
- Sollwert der GießspiegelhöheTarget value of the casting level height
- hIST h IS
- Istwert der GießspiegelhöheActual value of the pouring height
- Δh.delta.h
- Höhenänderung des GießspiegelsHeight change of the pouring mirror
- dd
- Dickethickness
- bb
- Breitewidth
- Δb.DELTA.b
- Breitenkorrekturwidth correction
- Vcast V cast
- Gießgeschwindigkeitcasting speed
- e1(t)e 1 (t)
- VolumenstromregeldifferenzFlow control difference
- u1(t)u 1 (t)
- erste Stellgrößefirst manipulated variable
- e2(t)e 2 (t)
- GießspiegelhöhenregeldifferenzGießspiegelhöhenregeldifferenz
- u2(t)u 2 (t)
- zweite Stellgrößesecond manipulated variable
Claims (12)
- Method of casting a strip (190) with a width b and a thickness d, comprising the following steps:providing liquid metal (200) in a tundish (140) with an outflow opening (130) for the outflow of the liquid metal (200) at a volume flow V̇ through a pouring spout (150) into a continuous casting mould (160) for the casting of the strip (190) at a predetermined casting speed vcast,measuring the volume flow V̇ of liquid metal (200) in the pouring spout (150) as actual value V̇Ist by means of a throughflow sensor (44);detecting the casting meniscus height h of the liquid metal (200) in the continuous casting mould (16) as actual value hIST by means of a casting meniscus measuring device (540); andregulating the casting meniscus height h and the volume flow V̇ of the liquid metal (200) by means of a regulating device (300) in accordance with the measured actual values hist, V̇Ist to predetermined target values hSOLL, V̇Soll by activating a closure element (120), which is arranged at the outflow opening (130) of the tundish (140) or in the pouring spout (150);characterised bycalculation in a first regulator (410) of a width correction Δb in dependence on a determined volume flow regulating difference e1(t) from the measured actual value V̇Ist and the predetermined target value V̇Soll with consideration of the thickness d of the strip (190) to be cast and the casting speed vcast;issue of the calculated width correction Δb in the form of a setting variable u1(t) to a first setting element (420) for adjusting at least one narrow side (170) of the continuous casting mould (16) so that a change in the width b of the strip (190) to be cast takes place;calculation of a height change Δh of the casting meniscus height h in dependence on the width correction Δb for issue to a second target-value/actual-value value comparator (550) of a second regulating circuit (500);determining a casting meniscus height regulating difference e2(t) from the measured actual value hIST, the predetermined target value hSOLL and the calculated height change Δh of the casting meniscus height h as input variable for a second regulator (510) of the second regulating circuit (500) for regulating the casting meniscus height h; andregulating the volume flow V̇ with consideration of the changed casting meniscus height h by activating the closure element (120).
- Method according to claim 1, characterised in that the target value V̇Soll of the volume flow V̇ is dependent on the casting speed vcast, the width b and the thickness d of the strip to be cast in accordance with the following law: V̇Soll = vcast * b * d.
- Method according to one of the preceding claims, characterised in that the volume flow regulating difference e1(t) of the measured actual value V̇Ist and the predetermined target value V̇Soll of the volume flow V is used as input variable for the first regulator (410) in a first regulating circuit (400).
- Method according to any one of the preceding claims, characterised in that the width correction Δb is calculated as follows: Δb = e1(t) * 1/(vcast * d).
- Method according to any one of the preceding claims, characterised in that the height change Δh of the casting meniscus height h is calculated as follows: Δh = Δb / b * hSOLL.
- Device (100) for casting a strip (190) with a width b and a thickness d, for carrying out the claimed method according to any one of claims 1 to 5, comprising:a tundish (10) for providing liquid metal (200), the tundish having an outflow opening (130) for the outflow of the liquid metal (200) at a volume flow V̇ through a pouring spout (150) into a continuous casting mould (160) for the casting of the strip (190) at a predetermined casting speed vcast;a closure element (120) at the outflow opening (130) of the tundish (140) or in the pouring spout (150) for influencing the volume flow V̇ of liquid metal (200);a throughflow sensor (440) for measuring the volume flow V̇ of liquid metal (200) in the pouring spout (150) as actual value V̇Ist;a casting meniscus measuring device (540) for detecting the casting meniscus height h of the liquid metal (200) in the continuous casting mould (16) as actual value hIST; anda regulating device (300) for regulating the casting meniscus height h and the volume flow V of the liquid metal (200) in accordance with the measured actual values hist, V̇Ist to predetermined target values hSOLL, V̇Soll by activating the closure element (120);characterised in thata first regulator (410) in the regulating device (300) is constructed for calculating a width correction Δb of the width b of the strip (190) to be cast and for calculating a height change Δh of the casting meniscus height h in dependence on the width correction Δb;a first setting element (420) is constructed for adjusting at least one narrow side (170) of the continuous casting mould (160) in response to the width correction Δb in the form of the setting variable u1(t), wherein a change in the width b of the strip (190) to be cast takes place;a second regulator (510) in the regulating device (300)' is constructed for regulating the casting meniscus height h with consideration of the calculated height change Δh; andthe closure element (120) for regulating the volume flow V̇ is activatable in response to the changed casting meniscus height h.
- Device according to claim 6, characterised in that the first setting element (420) is constructed in the form of a hydraulic cylinder or a spindle drive.
- Device according to one of claims 6 and 7, characterised in that the closure element (120) is constructed as a stopper rod or as a slide.
- Device according to claim 8, characterised in that the stopper rod is arranged to be vertically movable above the outflow opening (130).
- Device according to claim 8, characterised in that the slide is arranged below the outflow opening (130) of the tundish (140) to be horizontally movable for closing the outflow opening (130).
- Device according to any one of claims 6 to 10, characterised in that the throughflow sensor (440) is constructed as a Lorentz anemometer.
- Device according to any one of claims 6 to 11, characterised in that the regulating device (300) can be constructed with at least two regulating circuits (400, 500), which are arranged in cascade form.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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DE102013001556 | 2013-01-30 | ||
DE201310214811 DE102013214811A1 (en) | 2013-01-30 | 2013-07-30 | Method and apparatus for casting a strand |
Publications (2)
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EP2762251A1 EP2762251A1 (en) | 2014-08-06 |
EP2762251B1 true EP2762251B1 (en) | 2015-07-08 |
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Application Number | Title | Priority Date | Filing Date |
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EP14151733.4A Not-in-force EP2762251B1 (en) | 2013-01-30 | 2014-01-20 | Method and device for casting a strand |
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EP (1) | EP2762251B1 (en) |
DE (1) | DE102013214811A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3173166A1 (en) | 2015-11-26 | 2017-05-31 | SMS group GmbH | Method and device for setting the width of a continuously cast metal strand |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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AT515244A2 (en) | 2013-12-30 | 2015-07-15 | Inteco Special Melting Technologies Gmbh | Method for producing long ingots of large cross section |
CN109848387B (en) * | 2017-11-30 | 2021-02-05 | 上海梅山钢铁股份有限公司 | Automatic control method for preventing steel overflow of continuous casting crystallizer |
CN111006728B (en) * | 2019-12-23 | 2022-02-18 | 上海一诺仪表有限公司 | Flow rate controller converter and control method thereof |
WO2024017831A1 (en) * | 2022-07-18 | 2024-01-25 | Primetals Technologies Austria GmbH | Virtual fill level sensor for a mould of a continuous casting machine |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS61232049A (en) * | 1985-04-09 | 1986-10-16 | Nippon Steel Corp | Method for controlling continuously cast ingot to specified width |
DE102009057861A1 (en) | 2008-12-11 | 2010-07-01 | Sms Siemag Ag | Device for detecting the flow and method therefor |
DE102011085932A1 (en) | 2011-06-07 | 2012-12-13 | Sms Siemag Ag | Method for regulating the height of the casting mirror in a mold of a continuous casting plant |
-
2013
- 2013-07-30 DE DE201310214811 patent/DE102013214811A1/en not_active Withdrawn
-
2014
- 2014-01-20 EP EP14151733.4A patent/EP2762251B1/en not_active Not-in-force
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3173166A1 (en) | 2015-11-26 | 2017-05-31 | SMS group GmbH | Method and device for setting the width of a continuously cast metal strand |
DE102015223496A1 (en) | 2015-11-26 | 2017-06-01 | Sms Group Gmbh | Method and apparatus for adjusting the width of a continuously cast metal strand |
Also Published As
Publication number | Publication date |
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DE102013214811A1 (en) | 2014-07-31 |
EP2762251A1 (en) | 2014-08-06 |
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