EP1432539B1 - Procede et dispositif de refoidissement des plaques de cuivre d'une coquille pour la coulee continue de metaux liquides, en particulier d'acier liquide - Google Patents

Procede et dispositif de refoidissement des plaques de cuivre d'une coquille pour la coulee continue de metaux liquides, en particulier d'acier liquide Download PDF

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Publication number
EP1432539B1
EP1432539B1 EP02777034A EP02777034A EP1432539B1 EP 1432539 B1 EP1432539 B1 EP 1432539B1 EP 02777034 A EP02777034 A EP 02777034A EP 02777034 A EP02777034 A EP 02777034A EP 1432539 B1 EP1432539 B1 EP 1432539B1
Authority
EP
European Patent Office
Prior art keywords
casting
mould
temperature
copper plate
coolant
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 - Lifetime
Application number
EP02777034A
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German (de)
English (en)
Other versions
EP1432539A2 (fr
Inventor
Fritz-Peter Pleschiutschnigg
Stephan Feldhaus
Wolfgang Mossner
Werner Rahmfeld
Lothar Parschat
Erwin Wosch
Uwe Kopfstedt
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.)
SMS Siemag AG
Original Assignee
SMS Demag AG
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
Priority claimed from DE10160739A external-priority patent/DE10160739C2/de
Application filed by SMS Demag AG filed Critical SMS Demag AG
Publication of EP1432539A2 publication Critical patent/EP1432539A2/fr
Application granted granted Critical
Publication of EP1432539B1 publication Critical patent/EP1432539B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • 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
    • B22D11/22Controlling or regulating processes or operations for cooling cast stock or mould
    • 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
    • B22D11/055Cooling the moulds

Definitions

  • the invention relates to a method and a device for cooling the copper plates of a continuous casting mold for liquid metals, in particular for liquid steel, with chill coolant guided in cooling channels and wherein during the speed ramp to target casting speed or exceeding the target casting speed or one of Kupferplatten- Target skin temperature deviating temperature, the amount or the flow rate of the coolant can be controlled.
  • EP-A-1 103 322 The initially described method and device are known from EP-A-1 103 322 for the control of the internal temperature within the die plate thickness.
  • the method referred to at the outset as known from EP 1 103 323 A2 determines an alternating copper plate temperature and corrects the mold coolant quantity and the actual casting speed by means of a computer.
  • the object of the invention is to propose specifications for a more exact control of the regulation of the controlled variables with regard to the copper plate skin temperature.
  • the stated object is achieved according to the invention in that, with changing casting speed between 1 m / min to a maximum of 12 m / min, the copper plate skin temperature by a quantitative correction of the mold coolant quantity and the mold coolant inlet temperature depending on the actual casting speed and depending on the copper plate thickness is set to a desired, constant size and that for controlling the Kokillen- coolant quantity and the Kokillenkühlstoff inlet temperature process data and system data, which are processed in controlled variables to an online simulation model, are used.
  • the copper plate skin temperature can be selected favorably even at different copper plate thicknesses and kept constant.
  • the described effects can also be achieved either completely or partially when the mold coolant is passed from top to bottom or from bottom to top through the cooling channels.
  • the continuous casting mold is oscillated.
  • the accuracy of the method can be further increased by using an immediate determination of the copper plate skin temperature in the Gblinapt Scheme addition or alternative to the online simulation model.
  • the copper plate skin temperature on the hot side already at the start of casting much lower than previously observed and the copper plate is spared in a way that the recrystallization temperature of the copper is far from reached. This advantage affects large casting speeds.
  • the mold coolant inlet can be arranged at a distance above the casting mirror.
  • the continuous casting mold is oscillated by means of an oscillating device.
  • this regulation can also be carried out in such a way that, in addition to or instead of the process computer, a device is used for determining the copper plate skin temperature in the molten metal region for controlling the mold coolant inlet temperature and / or the mold coolant quantity.
  • a continuous casting mold 1 in which liquid steel is poured, is cooled in such a way that the mold coolant 2 at the mold coolant inlet 3 is introduced into the continuous casting mold 1 in its mold coolant quantity 4 and its mold coolant temperature. Inlet temperature 5 is kept constant regardless of the casting speed 6.
  • the faults occur both from a watercourse 13.1 of the mold water 13 in the continuous casting mold 1 from bottom to top and in a watercourse 13.2 from top to bottom (see FIG. However, it can be noted that the watercourse 13.2 from top to bottom, the copper plate skin temperature 8 is lower than the watercourse 13.1 from bottom to top.
  • the continuous casting mold 1 is cooled by an inner coolant circuit 19 and an outer coolant circuit 20.
  • the outer coolant circuit 20 which runs over a heat exchanger 21, serves to cool the mold coolant 2 in the inner coolant circuit 19.
  • the inner coolant circuit 19 is guided over the heat exchanger 21 in such a way that the mold coolant quantity 4, which is set constant by means of a pump 22, is likewise kept constant in its inlet temperature 23 (T in ) independently of the casting speed 6.
  • the Kokillenkühlstoff 2 is performed as a watercourse 13.1 from bottom to top, in Dünnstranget also as watercourse 13.2 from top to bottom.
  • the coolant circuit in Fig. 1A is shown in block diagram, but with increasing casting speed 6 of 1 m / min to a maximum of 12 m / min, the copper plate skin temperature 8 by a quantitative correction of the mold coolant quantity 4 and 1 or the Kokillenkühlsch inlet temperature 5 regardless of the casting speed 6 and regardless of the copper plate thickness 9 is set at a constant controlled Kokillenkühlstoff inlet temperature 5 to a desired, constant copper plate skin temperature 8.
  • the regulation of the mold coolant quantity 4 and the mold coolant inlet temperature 5 can be achieved via a process computer 27 for an online simulation model 27.4 and process data 27.1 of the continuous casting mold 1 at a constant copper plate skin temperature 8 via an inlet speed window 6.2 (see FIG.
  • the process computer 27 requires process data 27.1 and system data 27.2 in order to control the mold coolant quantity 4 via a pump station 22.1 and / or control valves 29 and the mold coolant inlet temperature 5 through the three-way valve 24 via controlled variables 27.3.
  • a surge tank 30th Before the pump station 22.1 is a surge tank 30th
  • FIGS. 2A to 2D the procedural relationships are explained.
  • Fig. 2A shows a heat flow 17 and a profile 16 of the casting speed 6 over the casting time 18.
  • the graph describes a casting run from the start via a constant run-in speed window 6.2 with subsequent acceleration to a high speed level.
  • Fig. 2B shows the state of the art.
  • the real copper plate skin temperature 8, denoted T Cu-real increases with the casting speed 6 and deviates from the desired copper plate skin temperature 8, referred to as the target copper plate temperature 8.1, (T Cu target ) since the mold coolant quantity is 4 and the mold coolant inlet temperature 5 for cooling the continuous casting mold 1 is kept constant.
  • the real copper plate skin temperature 8 (T Cu-real ) is determined by a corresponding quantitative correction of the mold coolant quantity 4 irrespective of the casting speed 6 at a constant mold coolant inlet temperature 5 having the desired copper plate skin temperature 8, the copper plate target temperature 8.1 (T Cu target ) brought to cover.
  • the copper plate skin temperature 8 (T Cu-real ) with the target copper plate temperature 8.1 (T Cu target ) is determined by the corresponding quantitative adjustment of the mold coolant quantity 4 and the mold coolant inlet temperature 5 as a function of the profile 16 the casting speed 6 over the casting time 18 brought to coincide.
  • the inlet velocity windows 6.2 with respect to the casting speed 6 are for a desired, real copper plate skin temperature 8 at a given copper plate thickness 9 greater than in the case of variation of only one of the two influencing variables.
  • Fig. 3 the difference of the known method for the invention can be clearly read. It is the copper plate skin temperature 8 in response to the increasing casting speed 6, the max. 12 m / min., Based on.
  • a horizontal straight line of the recrystallization temperature 12 represents the end of the heat load of the copper plate made of cold-rolled copper, at which the copper loses its strength and / or cold rolling structure and thus its properties important for the casting of molten steel.
  • the temperature curve 14 in the prior art is described with the curve 14.1 (water flow from bottom to top) and the curve 14.2 (water flow from top to bottom).
  • the strongly increasing behavior of the copper plate skin temperature 8 in the casting mirror with increasing casting speed 6 and increasing copper plate thickness 9 is due to the constant in the prior art casting molds Kokillen- 4 and the constant Kokillenkühtmittet inlet temperature 5 at mold coolant inlet 3.
  • the principle of the invention can also be applied to strip casters operating at up to 100 m / min casting speed. In this case, all measures applied to the height of the continuous casting mold 1 are applied to the circumference of the twin rolls.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Continuous Casting (AREA)
  • Heat Treatments In General, Especially Conveying And Cooling (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Claims (11)

  1. Procédé de refroidissement des plaques de cuivre (1.1) d'une lingotière de coulée continue (1) pour métaux liquides, notamment pour de l'acier liquide; à l'aide de refroidisseur (2) conduit dans des canaux de refroidissement et dans lequel, pendant la rampe de démarrage de vitesse jusqu'à la vitesse de coulée théorique ou en cas de dépassement de la vitesse de coulée théorique ou d'une température divergeant de la température théorique de la pellicule des plaques de cuivre (8), on règle la quantité ou la vitesse de débit du refroidisseur (2),
    caractérisé en ce que,
    dans le cas d'une vitesse de coulée (6) variable entre 1 m/min. et 12/min. au maximum, la température de pellicule des plaques de cuivre (8) est réglée par correction quantitative de la quantité de refroidisseur à lingotière (4) et de la température d'arrivée du refroidisseur à lingotière (5), en fonction de la vitesse de coulée momentanée (6) et en fonction de l'épaisseur des plaques de cuivre (9), à une valeur constante voulu et que, pour régler la quantité de refroidisseur à lingotière (4) et la température d'arrivée du refroidisseur à lingotière (5), on utilise des données de processus (27.1) et des données d'installation (27.2) qui sont transformées en grandeurs de réglage pour former un modèle de simulation en ligne (27.4).
  2. Procédé selon la revendication 1,
    caractérisé en ce que
    la température constante voulue de la pellicule des plaques de cuivre (8) est réglée à une valeur constante dans le secteur du niveau de la coulée.
  3. Procédé selon la revendication 1,
    caractérisé en ce que
    le refroidisseur de lingotière (2) est conduit du haut vers le bas ou du bas vers le haut par les canaux de refroidissement.
  4. Procédé selon une des revendications 1 à 3,
    caractérisé en ce que
    la lingotière de coulée continue (1) est mise en oscillation.
  5. Procédé selon une des revendications 1 à 4,
    caractérisé en ce que
    la barre de coulée (11) se coule ensemble lorsqu'une scorie de poudre de coulée (10) se forme.
  6. Procédé selon une des revendications 1 à 5,
    caractérisé en ce que
    on utilise une détermination directe de la température de pellicule des plaques de coulée (8) dans le secteur du niveau de la coulée en complément ou en alternative du modèle de simulation en ligne (27.4).
  7. Dispositif de refroidissement des plaques de cuivre (1.1) d'une lingotière de coulée continue (1), notamment pour de l'acier liquide, à l'aide de refroidisseur de lingotière (2) conduit dans des canaux de refroidissement, dans lequel, dans le cas de températures divergeant de la température théorique dans les plaques de cuivre, entre 4 mm et environ 50 mm, il est prévu un calculateur et des moyens de régulation pour la quantité ou la vitesse de débit du refroidisseur,
    caractérisé en ce que
    un calculateur de processus (27) qui établit, au moyen de données de processus (27.1) et de données d'installation (27.2), un modèle de simulation en ligne (27.4) pour des grandeurs de réglage (27.3) servant à réguler la température d'arrivée (5) du refroidisseur à lingotière et la quantité de refroidisseur à lingotière (4), commande une soupape à trois distributions (24) et une soupape de réglage (29) ainsi qu'une pompe à vitesse de rotation régulée (22) dans le circuit de refroidisseur (19 ; 20).
  8. Dispositif selon la revendication 7,
    caractérisé en ce que
    l'arrivée de refroidisseur à lingotière (3) est disposée à distance au dessus du niveau de la coulée.
  9. Dispositif selon la revendication 7,
    caractérisé en ce que
    la lingotière de coulée continue (1) est mise en oscillation au moyen d'un dispositif d'oscillation.
  10. Dispositif selon une des revendications 7 ou 8,
    caractérisé en ce que,
    lors de la coulée, de la poudre de coulée est apportée à la barre coulée (11)
  11. Dispositif selon une des revendications 7 à 10,
    caractérisé en ce que,
    en complément ou à la place du calculateur de processus (27), on utilise un dispositif de détermination de la température de la pellicule des plaques de cuivre (8) dans le secteur du niveau de la coulée pour réguler la température d'arrivée du refroidisseur à lingotière (5) et/ou la quantité de refroidisseur à lingotière (4).
EP02777034A 2001-09-28 2002-09-07 Procede et dispositif de refoidissement des plaques de cuivre d'une coquille pour la coulee continue de metaux liquides, en particulier d'acier liquide Expired - Lifetime EP1432539B1 (fr)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
DE10148135 2001-09-28
DE10148135 2001-09-28
DE10160739A DE10160739C2 (de) 2001-09-28 2001-12-11 Verfahren und Einrichtung zum Kühlen der Kupferplatten einer Stranggießkokille für flüssige Metalle, insbesondere für flüssigen Stahl
DE10160739 2001-12-11
PCT/EP2002/010030 WO2003028921A2 (fr) 2001-09-28 2002-09-07 Procede et dispositif de refoidissement des plaques de cuivre d'une coquille pour la coulee continue de metaux liquides, en particulier d'acier liquide

Publications (2)

Publication Number Publication Date
EP1432539A2 EP1432539A2 (fr) 2004-06-30
EP1432539B1 true EP1432539B1 (fr) 2006-05-03

Family

ID=26010255

Family Applications (1)

Application Number Title Priority Date Filing Date
EP02777034A Expired - Lifetime EP1432539B1 (fr) 2001-09-28 2002-09-07 Procede et dispositif de refoidissement des plaques de cuivre d'une coquille pour la coulee continue de metaux liquides, en particulier d'acier liquide

Country Status (13)

Country Link
US (1) US20040256078A1 (fr)
EP (1) EP1432539B1 (fr)
JP (1) JP2005503927A (fr)
CN (1) CN1561273A (fr)
AT (1) ATE324953T1 (fr)
BR (1) BR0212935A (fr)
CA (1) CA2460897A1 (fr)
DE (1) DE50206693D1 (fr)
HU (1) HUP0402138A2 (fr)
MX (1) MXPA04002744A (fr)
PL (1) PL367404A1 (fr)
RU (1) RU2004113105A (fr)
WO (1) WO2003028921A2 (fr)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1292858C (zh) * 2004-01-17 2007-01-03 宝山钢铁股份有限公司 一种水冷的金属连铸结晶器
DE102009023677A1 (de) * 2009-06-03 2010-12-09 Egon Evertz Kg (Gmbh & Co.) Verfahren zur Regelung der Flüssigkeitskühlung von Stranggießkokillen

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58151952A (ja) * 1982-03-02 1983-09-09 Kobe Steel Ltd 電磁撹「はん」用鋳型の冷却方法
JPS63104754A (ja) * 1986-10-20 1988-05-10 Mitsubishi Heavy Ind Ltd スプレ冷却モ−ルドの水量調節方法
DE4127333C2 (de) * 1991-08-19 2000-02-24 Schloemann Siemag Ag Stahlstranggießkokille
DE19956577A1 (de) * 1999-11-25 2001-05-31 Sms Demag Ag Verfahren zum Stranggießen von Brammen, insbesondere von Dünnbrammen, sowie eine Vorrichtung zu dessen Durchführung

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Publication number Publication date
CN1561273A (zh) 2005-01-05
DE50206693D1 (de) 2006-06-08
US20040256078A1 (en) 2004-12-23
RU2004113105A (ru) 2005-05-20
MXPA04002744A (es) 2004-07-29
WO2003028921A2 (fr) 2003-04-10
JP2005503927A (ja) 2005-02-10
EP1432539A2 (fr) 2004-06-30
ATE324953T1 (de) 2006-06-15
WO2003028921A3 (fr) 2003-10-23
BR0212935A (pt) 2004-10-13
CA2460897A1 (fr) 2003-04-10
HUP0402138A2 (hu) 2005-02-28
PL367404A1 (en) 2005-02-21

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