EP0515010B1 - Temperature measurement in a slab mould - Google Patents

Temperature measurement in a slab mould Download PDF

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Publication number
EP0515010B1
EP0515010B1 EP92250124A EP92250124A EP0515010B1 EP 0515010 B1 EP0515010 B1 EP 0515010B1 EP 92250124 A EP92250124 A EP 92250124A EP 92250124 A EP92250124 A EP 92250124A EP 0515010 B1 EP0515010 B1 EP 0515010B1
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EP
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Prior art keywords
values
specific temperature
mould
liquid
measured
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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 - Lifetime
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EP92250124A
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German (de)
French (fr)
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EP0515010A2 (en
EP0515010A3 (en
Inventor
Fritz-Peter Pleschiutschnigg
Lothar Parschat
Uwe Franzen
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ARVEDI, GIOVANNI
SMS Siemag AG
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SMS Demag AG
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Publication of EP0515010A3 publication Critical patent/EP0515010A3/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/16Controlling or regulating processes or operations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/16Controlling or regulating processes or operations
    • B22D11/168Controlling or regulating processes or operations for adjusting the mould size or mould taper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/04Continuous casting of metals, i.e. casting in indefinite lengths into open-ended moulds

Definitions

  • the invention relates to a method and a device for Production of steel strands in slab format.
  • formed from individual plates Chill molds for producing strands in slab format are placed in the mold due to the low thermal conductivity of the steel, initially only one thin strand shell formed from solidified melt. It is known and is aimed by the continuous caster that the continuous shell in the mold is made with a thickness that is uniform over the circumference, because this thin strand shell outside the mold is the ferrostatic Pressure of the melt located inside must withstand.
  • the expert also knows that the thickness and uniformity of the solidified strand shell at the exit of the mold from a series of Factors, such as casting speed, Steel temperature, geometry, material and conicity of the mold and not least of the type and composition of the lubricant that is applied to the mold level and the friction between Strand shell and mold should reduce.
  • Factors such as casting speed, Steel temperature, geometry, material and conicity of the mold and not least of the type and composition of the lubricant that is applied to the mold level and the friction between Strand shell and mold should reduce.
  • the invention solves the existing problems in a liquid-cooled plate mold for the production of strands Steel in slab format with adjustable between broad side plates Narrow side panels with the Features of claim 1.
  • Advantageous Embodiments of the invention are specified in the subclaims.
  • Fig. 1 shows in principle a mold for the production of strands in slab format.
  • the mold is formed by the Broad side plates 3, 4 and arranged adjustably between them Narrow side plates 1, 2. All four sides are known per se Wise water-cooled, i.e. with one water inlet and one water outlet each provided, the narrow sides with known means for adjustment different strand widths as well as the taper. Because this is facts known to the person skilled in the art, they are in the drawing not shown.
  • the water inlet temperature is 5 recorded, as a rule this will be the same for all four plates, so that one measurement is sufficient.
  • the water has passed through the mold is for each of the narrow and broad side plates 1, 2, 3, 4 Temperature of the water as close as possible to the junction of the Water drainage detected on the mold plate, as well as that on each side of the Quantity of water supplied to plate (reference numbers 6 to 13).
  • the specific heat load (more specific Temperature value) can be determined.
  • the values K1 to K6 are evaluated at intervals or also continuously recorded, the result for an ideal state is: always defines an equal shell thickness of the strand in the mold a certain ratio of the K values to each other or a certain one Curve. Deviates one or more values by a certain amount the other simultaneous values, this is an indication of one Disruption of the heat transfer and thus for a change in Strand shell formation in a locatable area of the mold, the at the same time, a warning for a strand break to be expected indicates. This risk can be avoided early by correcting the taper the mold, changing the casting speed, the oscillation parameters or the mold powder composition can be met.

Abstract

The invention relates to a method for controlling the taper of narrow faces, adjustable between wide faces, of a liquid-cooled plate mould for the production of continuous steel slabs. In order to specify a method for controlling the taper of narrow faces, adjustable between wide faces, of a liquid-cooled plate mould for the production of continuous steel slabs, it is proposed that the temperature of the cooling fluid at the coolant outlet of each of the liquid-cooled plates of a mould should first of all be measured, that a cooling surface-related specific temperature value be formed from the measured temperature, that the specific temperature values of opposite plates be compared, furthermore that a comparison of the temperature values of each plate with the specific temperature values of the adjoining plates be carried out and that, if there is a difference between the temperature values, an actuating value corresponding to the size of the difference be applied to the drive of that narrow face which delivers the lower temperature value to bring about an increase in the taper. <IMAGE>

Description

Die Erfindung bezieht sich auf ein Verfahren und eine Einrichtung zur Erzeugung von Stahlsträngen im Brammenformat. Beim Stranggießen von Stahl in flüssigkeitsgekühlten, aus einzelnen Platten gebildeten Kokillen zur Erzeugung von Strängen im Brammenformat wird in der Kokille aufgrund der geringen Wärmeleitfähigkeit des Stahles zunächst nur eine dünne, aus erstarrter Schmelze bestehende Strangschale gebildet. Es ist bekannt und wird vom Stranggießer angestrebt, daß die Strangschale in der Kokille möglichst mit über den Umfang gleichmäßiger Dicke entsteht, da diese dünne Strangschale außerhalb der Kokille dem ferrostatischen Druck der im Innern befindlichen Schmelze Stand halten muß. Der Fachmann weiß ferner, daß die Ausbildung der Dicke und der Gleichmäßigkeit der erstarrten Strangsschale am Austritt der Kokille von einer Reihe von Faktoren abhängig ist, wie beispielsweise Gießgeschwindigkeit, Stahltemperatur, Geometrie, Werkstoff und Konizität der Kokille und nicht zuletzt von der Art und Zusammensetzung des Schmiermittels, das auf den Gießspiegel aufgebracht wird und die Reibung zwischen Strangschale und Kokille verringern soll. The invention relates to a method and a device for Production of steel strands in slab format. When continuously casting Steel in liquid-cooled, formed from individual plates Chill molds for producing strands in slab format are placed in the mold due to the low thermal conductivity of the steel, initially only one thin strand shell formed from solidified melt. It is known and is aimed by the continuous caster that the continuous shell in the mold is made with a thickness that is uniform over the circumference, because this thin strand shell outside the mold is the ferrostatic Pressure of the melt located inside must withstand. The expert also knows that the thickness and uniformity of the solidified strand shell at the exit of the mold from a series of Factors, such as casting speed, Steel temperature, geometry, material and conicity of the mold and not least of the type and composition of the lubricant that is applied to the mold level and the friction between Strand shell and mold should reduce.

Die Tatsache, daß immer wieder Strangdurchbrüche, also Schmelzenaustritte durch die Strangschale hindurch zu verzeichnen sind, die zum Abbruch des Gießvorganges führen, zeigt, daß dieses Problem noch nicht sicher beherrscht wird, obwohl eine ganze Reihe von Vorschlägen zur Lösung dieses Problems existieren.The fact that strand breaks again and again, so Melt leaks through the strand shell can be recorded, which lead to the termination of the casting process shows that this problem still not mastered with certainty, although a whole host of proposals exist to solve this problem.

So sind aus den Schriften DE 31 10 012 C1, EP 0 114 293 B1, DE 33 09 885 A1, DE 39 08 328 A1 Vorschläge bekannt, mit denen über eine Einstellung der Konizität der Schmalseiten versucht wird, die Kühlbedingungen in der Kokille und damit die Strangsschalenbildung zu bestimmen bzw. zu beeinflussen.So are the documents DE 31 10 012 C1, EP 0 114 293 B1, DE 33 09 885 A1, DE 39 08 328 A1 proposals known with which about a setting the conicity of the narrow sides is tried, the cooling conditions in the To determine the mold and thus the strand shell formation influence.

Andererseits ist es aus den Schriften DE-OS 15 08 966, DAS 23 19 323, DE-PS 23 20 277, DE-PS 24 40 273 und DE 34 23 475 C2 bekannt, die Strangschalendicke Über Messungen der Kokillenwandtemperatur oder der aus der Kokille abgeführten Wärmemenge zu steuern.On the other hand, it is from DE-OS 15 08 966, DAS 23 19 323, DE-PS 23 20 277, DE-PS 24 40 273 and DE 34 23 475 C2 known Strand shell thickness Via measurements of the mold wall temperature or the to control the amount of heat removed from the mold.

Allen bekannten Methoden ist gemeinsam, daß die Kokille bzw. die gesamte Anlage nach Meßwerten im Vergleich zu vorgegebenen Soll-Werten gesteuert wird, wobei jedoch offen ist, inwieweit die vorgegebenen Soll-Werte den tatsächlichen Gegebenheiten oder Erfordernissen Rechnung tragen.All known methods have in common that the mold or the entire System controlled according to measured values in comparison to specified target values is, but it is open to what extent the specified target values take account of actual circumstances or requirements.

Die Erfindung löst die bestehenden Probleme bei einer flüssigkeitsgekühlten Plattenkokille zur Erzeugung von Strängen aus Stahl im Brammenformat mit zwischen Breitseitenplatten verstellbaren Schmalseitenplatten mit den Merkmalen des Anspruches 1. Vorteilhafte Ausgestaltungen der Erfindung sind in den Unteransprüchen angegeben.The invention solves the existing problems in a liquid-cooled plate mold for the production of strands Steel in slab format with adjustable between broad side plates Narrow side panels with the Features of claim 1. Advantageous Embodiments of the invention are specified in the subclaims.

Anhand der beiliegenden Zeichnung soll die Erfindung im folgenden näher erläutert werden. Based on the accompanying drawing, the invention will be described in more detail below are explained.

Fig. 1 zeigt in prinzipieller Darstellung eine Kokille für die Erzeugung von Strängen im Brammenformat. Die Kokille ist gebildet von den Breitseitenplatten 3, 4 und zwischen diesen verstellbar angeordneten Schmalseitenplatten 1, 2. Alle vier Seiten sind in an sich bekannter Weise wassergekühlt, also mit je einem Wasserzulauf und Wasserablauf versehen, die Schmalseiten mit an sich bekannten Mitteln zur Einstellung verschiedener Strangbreiten sowie der Konizität. Da es sich hierbei um dem Fachmann bekannte Sachverhalte handelt, sind sie in der Zeichnung nicht dargestellt.Fig. 1 shows in principle a mold for the production of strands in slab format. The mold is formed by the Broad side plates 3, 4 and arranged adjustably between them Narrow side plates 1, 2. All four sides are known per se Wise water-cooled, i.e. with one water inlet and one water outlet each provided, the narrow sides with known means for adjustment different strand widths as well as the taper. Because this is facts known to the person skilled in the art, they are in the drawing not shown.

Für jede der vier Platten der Kokille wird die Wassereinlauftemperatur 5 erfaßt, wobei im Regelfall diese für alle vier Platten gleich sein wird, so daß ein Meßwert genügt. Nach Durchlauf des Wassers durch die Kokille wird für jede der Schmal- und Breitseitenplatten 1, 2, 3, 4 die Temperatur des Wassers möglichst nahe an der Anschlußstelle des Wasserablaufs an der Kokillenplatte erfaßt, ebenso die jeder Seite der Platte zugeführte Wassermenge (Bezugsziffern 6 bis 13).For each of the four plates of the mold, the water inlet temperature is 5 recorded, as a rule this will be the same for all four plates, so that one measurement is sufficient. After the water has passed through the mold is for each of the narrow and broad side plates 1, 2, 3, 4 Temperature of the water as close as possible to the junction of the Water drainage detected on the mold plate, as well as that on each side of the Quantity of water supplied to plate (reference numbers 6 to 13).

Hierbei steht die Bezugsziffer

  • 6 - Tnfl 1 für Wasserauslauftemperatur -linke Schmalseitenplatte
  • 7 - Mnfl für Wassermenge -linke Schmalseitenplatte
  • 8 - Twff für Wasserauslauftemperatur -vordere Breitseitenplatte
  • 9 - Mwff für Wassermenge -vordere Breitseitenplatte
  • 10 - Twfb für Wasserauslauftemperatur -hintere Breitseitenplatte
  • 11 - Mwfb für Wassermenge -hintere Breitseitenplatte
  • 12 - Tnfr für Wasserauslauftemperatur -rechte Schmalseitenplatte
  • 13 - Mnfr für Wassermenge -rechte Schmalseitenplatte
  • Here is the reference number
  • 6 - Tnfl 1 for water outlet temperature - left narrow side plate
  • 7 - Mnfl for water volume - left narrow side plate
  • 8 - Twff for water outlet temperature - front wide side plate
  • 9 - Mwff for amount of water - front broad side plate
  • 10 - Twfb for water outlet temperature - rear wide side plate
  • 11 - Mwfb for water volume - rear broadside plate
  • 12 - Tnfr for water outlet temperature - right narrow side plate
  • 13 - Mnfr for amount of water - right narrow side plate
  • In Fig. 2 ist das Verarbeitungsprogramm des Rechners 14 schematisch dargestellt. Aus den erfaßten Meßwerten 5 bis 13 werden die abgeführten Wärmemengen 21, 22, 23, 24 jeder Kokillenwand ermittelt. Die Bezugsziffern hierin bedeuten

  • 21 - Wnfl - Wärmemenge der linken Schmalseitenplatte 1
  • 22 - Wnfr - Wärmemenge der rechten Schmalseitenplatte 2
  • 23 - Wwfb - Wärmemenge der hinteren Breitseitenplatte 3
  • 24 - Wwff - Wärmemenge der vorderen Breitseitenplatte 4
  • 2, the processing program of the computer 14 is shown schematically. The heat quantities 21, 22, 23, 24 of each mold wall are determined from the measured values 5 to 13 recorded. The reference numerals herein mean
  • 21 - Wnfl - heat quantity of the left narrow side plate 1
  • 22 - Wnfr - amount of heat from the right narrow side plate 2
  • 23 - Wwfb - heat quantity of the rear broad side plate 3
  • 24 - Wwff - heat quantity of the front broad side plate 4
  • Da außerdem das Kokillenformat 25 (Moldsize) eingegeben wird, kann für jede Kokillenplatte 1 bis 4 die spezifische Wärmebelastung (spezifischer Temperaturwert) ermittelt werden.Since the mold size 25 (Moldsize) is also entered, for each mold plate 1 to 4 the specific heat load (more specific Temperature value) can be determined.

    In einem weiteren Gang werden nun die spezifischen Temperaturwerte je einer Breitseitenplatte zu denen der angrenzenden Schmalseitenplatte ins Verhältnis gesetzt, so daß sich die Werte

  • K1 - aus dem Verhältnis Schmalseitenplatte 3 zur Breitseitenplatte 1
  • K2 - aus dem Verhältnis Schmalseitenplatte 3 zur Breitseitenplatte 2
  • K3 - aus dem Verhältnis Schmalseitenplatte 4 zur Breitseitenplatte 1
  • K4 - aus dem Verhältnis Schmalseitenplatte 4 zur Breitseitenplatte 2
  • ergeben.In a further course, the specific temperature values of each broad side plate are compared to those of the adjacent narrow side plate, so that the values change
  • K1 - from the ratio of narrow side plate 3 to broad side plate 1
  • K2 - from the ratio of narrow side plate 3 to broad side plate 2
  • K3 - from the ratio of narrow side plate 4 to broad side plate 1
  • K4 - from the ratio of narrow side plate 4 to broad side plate 2
  • result.

    Im weiteren können durch einen Vergleich der abgeführten Wärmemengen der Schmalseitenplatten 1, 2 untereinander K5 bzw. der Breitseitenplatten 3, 4 untereinander K6 Rückschlüsse auf die Schalendicke des Stranges in der Kokille gezogen und diese ebenfalls zur Korrektur der Konizitätseinstellung der Schmalseitenplatten benutzt werden. Auch hier wird man die Schmalseite, die den niedrigeren Temperaturwert liefert, im Sinne einer Verstärkung der Konizität verstellen.Furthermore, by comparing the amounts of heat dissipated Narrow side plates 1, 2 with one another K5 or the wide side plates 3, 4 among themselves K6 conclusions on the shell thickness of the strand in the Chilled mold and this also to correct the Conicity adjustment of the narrow side plates can be used. Here too the narrow side, which supplies the lower temperature value, is Adjust to increase conicity.

    Werden die Werte K1 bis K6 in Zeitabständen ausgewertet oder auch kontinuierlich aufgezeichnet, so ergibt sich für einen Idealzustand, der eine gleiche Schalendicke des Stranges in der Kokille definiert, stets ein bestimmtes Verhältnis der K-Werte untereinander bzw. ein bestimmter Kurvenverlauf. Weicht ein oder mehrere Werte über ein bestimmtes Maß von den übrigen zeitgleichen Werten ab, so ist dies ein Anzeichen für eine Störung des Wärmeüberganges und damit für eine Veränderung der Strangschalenbildung in einem zuortbaren Bereich der Kokille, der gleichzeitig eine Vorwarnung für einen zu erwartenden Strangdurchbruch angibt. Diese Gefahr kann also frühzeitig durch Korrektur der Konizität der Kokille, Änderung der Gießgeschwindigkeit, der Oszillationsparameter oder der Gießpulverzusammensetzung begegnet werden.The values K1 to K6 are evaluated at intervals or also continuously recorded, the result for an ideal state is: always defines an equal shell thickness of the strand in the mold a certain ratio of the K values to each other or a certain one Curve. Deviates one or more values by a certain amount the other simultaneous values, this is an indication of one Disruption of the heat transfer and thus for a change in Strand shell formation in a locatable area of the mold, the at the same time, a warning for a strand break to be expected indicates. This risk can be avoided early by correcting the taper the mold, changing the casting speed, the oscillation parameters or the mold powder composition can be met.

    Claims (2)

    1. Method of controlling the taper of the narrow faces - adjustable between wide faces - of a liquid-cooled plate mould for the production of strands of steel in the form of slabs; initially, and for each of the liquid-cooled plates of the mould, the temperature of the coolant liquid is measured at the coolant inlet and the coolant outlet, and the volume of coolant is measured: for a given mould format, a specific temperature value, relative to the cooling surface, is formed from the measured temperatures for each plate; to form the specific temperature value of a mould side, the heat quantity dissipated in relation to each unit of surface is recorded, the specific temperature values of opposite plates are compared, and the specific temperature values of one wide face plate are compared in each case in relation to the specific temperature values of the adjacent narrow face plate, the resulting values being recorded, at intervals or continuously, as K values; under ideal conditions there is always a specific ratio among the K values, and where any deviation by more than a certain amount occurs of one or more K values in relation to the other isochronous K values, a correction value corresponding to the amount of the difference is sent to the drive unit of that narrow face for the purpose of bringing about an increase in the taper to give the lowest specific temperature value.
    2. Method as in Claim 1,
      characterised in that
      the temperature of the coolant is measured continuously.
    EP92250124A 1991-05-22 1992-05-18 Temperature measurement in a slab mould Expired - Lifetime EP0515010B1 (en)

    Applications Claiming Priority (2)

    Application Number Priority Date Filing Date Title
    DE4117073A DE4117073A1 (en) 1991-05-22 1991-05-22 TEMPERATURE MEASUREMENT SLAM CHOCOLATE
    DE4117073 1991-05-22

    Publications (3)

    Publication Number Publication Date
    EP0515010A2 EP0515010A2 (en) 1992-11-25
    EP0515010A3 EP0515010A3 (en) 1993-07-14
    EP0515010B1 true EP0515010B1 (en) 2003-09-03

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    Application Number Title Priority Date Filing Date
    EP92250124A Expired - Lifetime EP0515010B1 (en) 1991-05-22 1992-05-18 Temperature measurement in a slab mould

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    US (1) US5242010A (en)
    EP (1) EP0515010B1 (en)
    JP (1) JP3090783B2 (en)
    KR (1) KR100228598B1 (en)
    AT (1) ATE248673T1 (en)
    AU (1) AU653399B2 (en)
    CA (1) CA2069141C (en)
    DE (2) DE4117073A1 (en)
    ZA (1) ZA923712B (en)

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    DE102014227013A1 (en) 2014-09-18 2016-03-24 Sms Group Gmbh Method and device for optimizing the conicity of a mold in a continuous slab caster

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    ATE248673T1 (en) 2003-09-15
    AU1625392A (en) 1992-11-26
    ZA923712B (en) 1993-01-27
    DE4117073A1 (en) 1992-11-26
    KR100228598B1 (en) 1999-11-01
    DE59209987D1 (en) 2003-10-09
    JP3090783B2 (en) 2000-09-25
    AU653399B2 (en) 1994-09-29
    KR920021238A (en) 1992-12-18
    EP0515010A2 (en) 1992-11-25
    US5242010A (en) 1993-09-07
    CA2069141A1 (en) 1992-11-23
    JPH05177320A (en) 1993-07-20
    CA2069141C (en) 2002-11-12
    EP0515010A3 (en) 1993-07-14
    DE4117073C2 (en) 1993-03-11

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