EP1066898A1 - Verfahren und System zur Schmelzenführung in einer Stranggiessmaschine - Google Patents
Verfahren und System zur Schmelzenführung in einer Stranggiessmaschine Download PDFInfo
- Publication number
- EP1066898A1 EP1066898A1 EP00114274A EP00114274A EP1066898A1 EP 1066898 A1 EP1066898 A1 EP 1066898A1 EP 00114274 A EP00114274 A EP 00114274A EP 00114274 A EP00114274 A EP 00114274A EP 1066898 A1 EP1066898 A1 EP 1066898A1
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- EP
- European Patent Office
- Prior art keywords
- distributor
- melt
- temperature
- casting
- liq
- Prior art date
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- Granted
Links
- 238000009749 continuous casting Methods 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims description 30
- 239000002184 metal Substances 0.000 title 1
- 238000005266 casting Methods 0.000 claims abstract description 100
- 239000000155 melt Substances 0.000 claims description 79
- 238000010586 diagram Methods 0.000 claims description 15
- 239000000956 alloy Substances 0.000 claims description 4
- 229910045601 alloy Inorganic materials 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000002955 isolation Methods 0.000 claims description 4
- 230000007423 decrease Effects 0.000 claims description 3
- 230000005855 radiation Effects 0.000 claims description 3
- 238000007654 immersion Methods 0.000 claims 1
- 230000003287 optical effect Effects 0.000 claims 1
- 238000002844 melting Methods 0.000 abstract description 2
- 230000008018 melting Effects 0.000 abstract description 2
- 238000007711 solidification Methods 0.000 description 13
- 230000008023 solidification Effects 0.000 description 13
- 229910000831 Steel Inorganic materials 0.000 description 8
- 239000010959 steel Substances 0.000 description 8
- 238000013021 overheating Methods 0.000 description 6
- 238000009826 distribution Methods 0.000 description 5
- 238000005461 lubrication Methods 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000005259 measurement Methods 0.000 description 3
- 238000009529 body temperature measurement Methods 0.000 description 2
- 230000001419 dependent effect Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 101150006573 PAN1 gene Proteins 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
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- 238000005457 optimization Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000161 steel melt Substances 0.000 description 1
Images
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
- B22D11/20—Controlling or regulating processes or operations for removing cast stock
-
- 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
Definitions
- the invention relates to a method for guiding the melt in a continuous casting machine, the melt of a specific alloy having a liquidus temperature T liq being poured into a casting mold via a distributor and the strand which has solidified within the casting mold being drawn off, and a system therefor.
- the invention relates to a continuous casting machine with a system according to the invention.
- the object of the present invention is to provide a method and a system for To provide melt guidance in a continuous casting machine, with which one precise temperature and casting speed control for a reliable operation and in particular automated casting is possible.
- the actual temperature of the melt in the distributor is recorded at an actual casting speed, the temperature being measured discontinuously or continuously by means of suitable known temperature recording means, for example thermocouples or temperature sensors.
- suitable known temperature recording means for example thermocouples or temperature sensors.
- the actual heat loss of the melt in the distributor and during its residence time between the distributor and the casting level in the casting mold, for example an oscillating mold, is determined by taking into account factors which are responsible for the heat loss. Knowing the liquidus temperature T liq of the melt to be cast and the current heat loss, an equivalent liquidus temperature T * liq (+ 0 ° C) is determined as the limit range for the temperature of the melt in the distributor, at which continuous casting defects occur in the mold.
- the temperature of the melt in the distributor or the temperature curve is determined via the casting speed at which the melt solidifies in the casting mold at an undesirably early stage, ie in the casting level or in the area of the level. If the liquidus temperature is already reached in the mold level of the mold, there is a risk of bridging in the solidifying structure combined with a strand break through lack of slag lubrication or damaged strand surfaces.
- the steel temperature in the mold must be chosen so that there is no pre-solidification in the mold level and the mold powder is melted sufficiently to ensure good lubrication and insulation of the strand as it travels through the mold.
- the temperature of the melt in the distributor is used as a measure of the prediction the temperature conditions used in the mold.
- the current temperature conditions in the mold can be predicted or indirectly within an "incubation period" and for adjustment an optimal casting speed or a casting speed range be used.
- the casting speed is therefore not directly dependent from the temperature of the melt in the mold, but indirectly above the manifold temperature is set.
- the method offers the possibility of an emerging, for example excessive cooling of the melt in the mold level of the mold, which is indicated by the determination of the equivalent T * liq temperature in the distributor, which is based on the melt temperature measurement in the distributor to react by a corresponding increase in the casting speed in order to avoid a casting defect in the mold in the form of surface defects on the cast product or a breakthrough.
- T * liq temperature in the distributor which is based on the melt temperature measurement in the distributor to react by a corresponding increase in the casting speed in order to avoid a casting defect in the mold in the form of surface defects on the cast product or a breakthrough.
- data is "online” to achieve good process management be measured, the solidification process in the mold at one of these optimal casting speed and at the same time a reinforcement-free production and ensure good surface quality.
- the invention makes it clear that with the detection of the melt temperature in the distributor by discontinuous and / or continuous measurement and by the qualitative "online" detection of the heat losses of the melt in the distributor and between the distributor and the casting mold, an optimal, breakdown-proof and possibly fully automatic melt guidance alone on the data of the melt temperature in the distributor and the equivalent T * liq temperature of the melt in the distributor, T * liq. + 0 ° C and their isotherms +5 to + 20 ° C, preferably in a step interval of 5 ° C each, or the temperature profiles can be ensured via the casting speed to generate an isothermal window.
- the casting speed is chosen so that the temperature of the melt in the distributor runs along or above the isotherms of the equivalent liquidus temperature curve T * liq + 5 ° C.
- the temperature of the melt in the distributor should preferably run along or below the isotherms of the equivalent liquidus temperature profile T * liq + 20 ° C, particularly preferably below the isotherms of the equivalent liquidus temperature profile T * liq + 15 ° C.
- the residence time of the melt goes into the heat loss of the melt in the distributor in the distributor, the residence time of the melt in the distributor being dependent the casting performance, which in turn is determined by the casting width, the solidification thickness, the casting speed, the current distributor level and the Ratio of distributor surface to its volume or the distributor size, the decrease in the melt weight in the distributor depending on it Surface / volume ratio, the initial heating time of the distributor for setting the equilibrium temperature corresponding to the melt temperature as well as the isolation or the isolation status of the distributor and thus the Heat radiation from the distributor.
- the system proposed according to the invention is used in a continuous casting machine with an oscillating stand mold or traveling mold, also in Continuous casting machines with a casting mold that acts as a 2-roller mold (twin roller) or belt mold are formed. Allowed especially in the last two procedures the proposed system at the necessary high casting speeds with shorter solidification times with a smaller solidification thickness one optimal process control.
- FIG. 1a schematically represents part of the casting process of a molten steel in a continuous casting machine
- Figure 5 gives an overview of a complete continuous casting machine.
- the melt is poured via a pan 1 into a distributor 2, from which it then flows into the mold 4 via a dip spout (also SEN) 3.
- a stationary mold for example a thin slab mold, which oscillates vertically with respect to the solidifying strand shell 5a, b (see arrows in the mold side walls 6a, b).
- the outflow speed of the melt from the distributor is regulated by means of a vertically movable plug 7 with a displacement device 7a or a slide 8.
- the dip tube 3 dips into the mold 4.
- 9 is the casting mold which is set, 10 is the casting powder or pouring slag.
- the casting speed v c results.
- X denotes the slab width resulting from the mold dimensions when it emerges from the mold.
- the distributor 2 has a thermal radiation in the thermal equilibrium with the melt, here indicated by 11, which can be specified with a skin temperature of, for example, 100 ° C. and which thus leads to a loss of heat in the steel during its dwell time in the distributor.
- the distributor 2 is further characterized by a maximum weight of the melt with a maximum filling height (h max ) in relation to the respective actual filling height h ist .
- FIGS. 1a and 1b it is clear that the method according to the invention or system is not limited to continuous casting with an oscillating mold is, there are also casting processes using the strip casting process (Fig. 1a), in which the melt from a distributor 102 onto a cooled endless belt 104, which runs around two rollers 114, 115, is cast and drawn off, or for example 2-roll casting (Fig. 1b), in which the melt from one Distributor 202 is cast between two counter-rotating rollers 214, 215 and then subtracted, conceivable.
- Fig. 1a strip casting process
- Fig. 1b 2-roll casting
- FIGS. 2 and 2a show the relationships between the melt temperature in the distributor or the Overheating of the melt in the distributor (or the heat loss of the melt in the distributor and between the distributor and bath level of the mold) and the casting speed and the utilization of these relationships for the mathematical prediction of the temperature of the melt in the bath level in the mold.
- FIG. 2a shows a section from FIG. 2 in the casting speed range from 3.5 to 6.0 m / min. The temperature of the is below the manifold temperature Understand melt in the manifold.
- T * liq temperature of the melt in the distributor 15
- T * liq temperature curve T * liq + 0 ° C shown in the diagram show the temperature in the distributor at which the steel temperature in the Mold will reach the liquidus temperature. If the liquidus temperature (here about 1500 ° C) in the mold is reached too early, the solidification already takes place in the mold level and not only when it comes into contact with the mold walls to form the desired strand shell, which leads to bridging and thus a breakthrough due to the lack of it Slag lubrication or defective strand surfaces are connected.
- the ratio of the temperature of the melt to the casting speed shown in FIGS. 2 and 2a can be influenced by various factors which shift the T / v c grid to higher or lower temperatures and thus introduce a dynamic.
- the influence of various factors is shown in Figure 3.
- the heat loss increases with the drop in the weight of the distributor as a function of the surface / volume ratio of the distributor and the residence time (influence B), as shown schematically in FIG. 3b.
- the heat loss and thus the necessary overheating due to the so-called "liquid core reduction” also increase, the strand with still liquid sump being reduced from a mold exit thickness x to a smaller solidification thickness y (influence C).
- the heat loss with greater casting performance is reduced by an initially increasing heating process of the distributor 2 when casting the first melt, the temperature adjusting to an equilibrium temperature after a certain time (cf. FIG. 2b).
- the time t GG is approximately 20-30 minutes until a temperature equilibrium is established between the distributor and the melt (influence A).
- the heat loss decreases with increasing pouring width, shown in Fig. 3a with the ratio D to D1) as well as with increasing solidification thickness (D2) and with improved insulation of the distributor of the distributor lining (influence E, Fig. 3a) or falling outer distributor skin temperature and the Dipping spout.
- the T / v C grid becomes dynamic and can be constantly updated during casting with the help of process data recorded online.
- a further course of the melt is also shown (20), in which the strand is poured too slowly or has insufficient overheating, and the temperature of the melt is already in the mold level of the mold T liq. was achieved.
- the temperature of the melt in the distributor corresponds to the equivalent temperature T * liq or is less than T * liq , (21); the strand breaks through a pre-solidification in the mold level and thus the slag lubrication between the strand shell and the mold wall is disturbed and thus rejects.
- FIG. 5 shows an overview of a continuous casting machine with a pan 300 and a holding device 301 receiving the pan 300 and a distributor 302 with corresponding holding device 303.
- the heat loss of the melt in The distributor is determined by means of suitable measuring devices 304 and the data fed into a computer 307 via corresponding lines 305, 306. It is also conceivable to reduce the heat loss of the melt in the pan to be measured by means of measuring devices 308 and via line 309 into the computer feed. It is also conceivable in a first approximation of a constant Steel temperature in the pan with a temperature drop of, for example 0.1 ° C / min.
- the liquidus temperature of the alloy is the equivalent liquidus temperature calculated and in the temperature / casting speed diagram represented by a monitor 310.
- a target casting speed which is in the isothermal window shown, set, and via a line 312 the slide or plug of the distributor as setting means (315) controlled for the casting speed.
- the method and the system are preferably used for thin slab casting.
- a thin slab of, for example, 50 mm solidification thickness requires a setting time of about 1 min.
- the events in the Mold at casting speeds of up to 8 m / min so far and in the near future 10 m / min make a precise temperature and Speed control necessary, which is provided according to the invention becomes.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Continuous Casting (AREA)
- Investigating Or Analyzing Materials Using Thermal Means (AREA)
Abstract
Description
- Fig. 1
- schematisch einen Querschnitt eines Ausschnitts einer Stranggießmaschine mit einem Verteiler und einer oszillierenden Kokille;
- Fig. 1a
- schematisch einen Längsschnitt einer Bandgießanlage mit Bandkokille;
- Fig. 1b
- schematisch einen Querschnitt einer 2-Rollen-Anlage mit 2-Rollen-Kokille;
- Fig. 2a
- ein Verteilertemperatur-/Gießgeschwindigkeitsdiagramm bzw. T/vC-Raster nach der Erfindung;
- Fig. 2b
- das Verteilertemperatur-/Gießgeschwindigkeitsdiagramm bzw. T/vc-Raster der Fig. 2a mit eingetragenen äquivalenten T*liq-Verläufen;
- Fig. 3
- ein dynamisches Verteilertemperatur-/Gießgeschwindigkeits diagramm (T/vc-Raster) nach der Erfindung;
- Fig. 3a
- die schematische Darstellung des Einflusses der Verteilerisolation (E) und der Gießleistung (D) auf das Verteilertemperatur-/Gieß geschwindigkeitsdiagramm;
- Fig. 3b
- die schematische Darstellung des Einflusses der anfänglichen Aufheizphase des Verteilers zur Einstellung eines Temperatur-Gleichgewichtszustands (A), des Absinkens des Gewichts der Schmelze im Verteiler (B) sowie einer Liquid-Core-Reduction (C);
- Fig. 4
- dynamisches Verteilertemperatur-/Gießgeschwindigkeitsdiagramm (T/vc-Raster) mit einer Häufigkeitsverteilung von ordnungsgemäßen Schmelzen und einem Durchbruch über einen Zeitabschnitt;
- Fig. 5
- eine schematische Darstellung einer Stranggießmaschine mit einer oszillierenden Kokille sowie einer Steuerungs- und Darstellungsein heit.
Claims (12)
- Verfahren zur Schmelzenführung in einer Stranggießmaschine, wobei die Schmelze einer bestimmten Legierung mit einer Liquidus-Temperatur Tliq über einen Verteiler (2, 102, 202, 302) in eine Gießform (4, 104, 214, 215) gegossen wird und der innerhalb der Gießform erstarrte Strang (314) abgezogen wird,
gekennzeichnet durchErlassen der Ist-Temperatur der Schmelze im Verteiler bei einer Ist-Gießgeschwindigkeit,Ermittlung des Ist-Wärmeverlustes der Schmelze im Verteiler und während ihrer Verweilzeit zwischen Verteiler und Gießspiegel (9) in der Gießform,Ermitteln einer äquivalenten Liquidus-Temperatur T*liq +0 (15) als Grenztemperatur für die Temperatur der Schmelze im Verteiler, bei der bereits im Gießspiegelbereich der Gießform die Liquidus-Temperatur Tliq bei einer gegebenen Gießgeschwindigkeit erreicht wird, sowieder Isothermen der äquivalenten Liquidus-Temperatur T*liq +x in Abhängigkeit von Überhitzungstemperaturen x mit x>0, die Isothermen jeweils im Verhältnis zu den Schmelzetemperaturen im Verteiler und Gießgeschwindigkeiten,Anpassen der Ist-Stranggießgeschwindigkeit an eine Soll-Stranggießgeschwindigkeit innerhalb eines vorgegebenen Isothermenfensters, dessen unterste Grenze oberhalb des äquivalenten Liquidus-Temperaturverlaufs T*liq +0 liegt. - Verfahren nach Anspruch 1,
dadurch gekennzeichnet,daß die Isothermen der äquivalenten Liquidus-Temperatur T*liq + x schrittweise in Intervallen von 5°C ermittelt werden. - Verfahren nach Anspruch 1 oder 2,
dadurch gekennzeichnet,daß die Gießgeschwindigkeit so gewählt wird, daß die Temperatur der Schmelze im Verteiler entlang oder oberhalb der Isothermen des äquivalenten Liquidus-Temperaturverlaufs T*liq + 5°C verläuft. - Verfahren nach Anspruch 1 oder 2,
dadurch gekennzeichnet,daß die Gießgeschwindigkeit so gewählt wird,daß die Temperatur der Schmelze im Verteiler entlang oder oberhalb der Isothermen des äquivalenten Liquidus-Temperaturverlaufs T*liq + 5°C verläuft unddaß die Temperatur der Schmelze im Verteiler entlang oder unterhalb der Isothermen des äquivalenten Liquidus-Temperaturverlaufs T*liq + 20°C, vorzugsweise + 15°C, verläuft. - Verfahren nach einem der Ansprüche 1 bis 4,
dadurch gekennzeichnet,daß in den Wärmeverlust der Schmelze im Verteiler eingehen: Verweilzeit der Schmelze im Verteiler und/oderAbsinken des Schmelzegewichts im Verteiler in Abhängigkeit zu dessen Oberflächen/Volumen-Verhältnis und/oderanfängliche Aufheizungszeit des Verteilers zur Einstellung der der Schmelzetemperatur entsprechenden Temperatur und/oderIsolation bzw. der Isolationszustand des Verteilers. - Verfahren nach einem der Ansprüche 1 bis 5,
dadurch gekennzeichnet,daß in die Ermittlung des Wärmeverlustes der Schmelze während ihrer Verweilzeit zwischen Verteiler und Gießspiegel in der Gießform die Wärmeabstrahlung eines Tauchausgusses des Verteilers, der in die Kokille als Gießform eintaucht, eingeht. - Verfahren nach einem der Ansprüche 1 bis 6,
dadurch gekennzeichnet,daß die äquivalenten Liquidus-Temperaturverläufe T*liq +0 sowie + T*liq +x einer Schmelze mit vorgegebenen Isothermenfenster in einem Verteilertemperatur-/Gießgeschwindigkeitsdiagramm über die Gießzeit einer Schmelze dargestellt werden und optisch sichtbar gemacht werden. - Verfahren nach Anspruch 7,
dadurch gekennzeichnet,daß in dem Verteilertemperatur-/Gießgeschwindigkeitsdiagramm Faktoren, die den Wärmeverlust beeinflussen, eingehen und optisch dargestellt werden. - Verfahren nach einem der Ansprüche 1 bis 8,
dadurch gekennzeichnet,daß die Soll-Stranggießgeschwindigkeit innerhalb des vorgegebenen Isothermenfensters, dessen unterste Grenze oberhalb des äquivalenten Liquidus-Temperaturverlaufs T*liq + 0 verläuft, automatisch eingestellt wird. - System zur Schmelzenführung in einer Stranggießmaschine, mit einem Verteiler (2, 102, 202, 302), von dem die Schmelze in eine Gießform (4, 104, 214, 215) gegossen wird, aus der der erstarrte Strang (314) abgezogen wird, sowie mit Mitteln (315) zur Einstellung der Stranggießgeschwindigkeit,mit Mitteln (12) zum Erfassen der Ist-Temperatur der Schmelze im Verteiler bei einer Ist-Gießgeschwindigkeit,Mitteln (304) zum Ermitteln des Wärmeverlustes der Schmelze im Verteiler und während ihrer Verweilzeit zwischen Verteiler und Gießspiegel in der Kokille,Steuerungsmitteln für die Einstellungsmittel (7, 8) der Stranggießgeschwindigkeit zur Anpassung der Ist-Stranggießgeschwindigkeit an eine Soll-Stranggießgeschwindigkeit innerhalb eines vorgegebenen Isothermenfensters, dessen unterste Grenze oberhalb des äquivalenten Liquidus-Temperaturverlaufs T*liq +0 liegt, wobei sich das Isothermenfenster ergibt durch Ermitteln einer äquivalenten Liquidus-Temperatur T*liq +0 (15) als Grenztemperatur für die Temperatur der Schmelze im Verteiler, bei der bereits im Gießspiegelbereich der Gießform die Liquidus-Temperatur Tliq bei einer gegebenen Gießgeschwindigkeit erreicht wird, sowie der Isothermen der äquivalenten Liquidus-Temperatur T*liq +x in Abhängigkeit von Überhitzungstemperaturen x mit x>0, die Isothermen jeweils im Verhältnis zu den Schmelzetemperaturen im Verteiler und Gießgeschwindigkeiten.
- System nach Anspruch 10,
gekennzeichnet durch Mittel (310) zur optischen Darstellung der isothermen Temperaturverläufe in einem Verteilertemperatur-/Gießgeschwindigkeitsdiagramms und deren Einflußgrößen. - Stranggießmaschine mit einem System nach einem der Ansprüche 10 und 11 mit einer oszillierenden Standkokille (4, 304) oder Wanderkokille oder 2-Rollen-Kokille (214, 215) oder Bandkokille (104) als Gießform.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19930909 | 1999-07-06 | ||
DE19930909 | 1999-07-06 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1066898A1 true EP1066898A1 (de) | 2001-01-10 |
EP1066898B1 EP1066898B1 (de) | 2005-03-09 |
Family
ID=7913672
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP00114274A Expired - Lifetime EP1066898B1 (de) | 1999-07-06 | 2000-07-04 | Verfahren zur Schmelzenführung in einer Stranggiessmaschine |
Country Status (9)
Country | Link |
---|---|
US (1) | US6539273B1 (de) |
EP (1) | EP1066898B1 (de) |
JP (1) | JP2001038456A (de) |
KR (1) | KR100720429B1 (de) |
CN (1) | CN1258415C (de) |
AT (1) | ATE290446T1 (de) |
DE (1) | DE50009703D1 (de) |
ES (1) | ES2238224T3 (de) |
TW (1) | TW452515B (de) |
Cited By (3)
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FR2864844A1 (fr) * | 2004-01-07 | 2005-07-08 | Saint Gobain | Dispositif d'eclairage autonettoyant |
CN104226951A (zh) * | 2014-09-05 | 2014-12-24 | 河北钢铁股份有限公司邯郸分公司 | 一种连铸机停浇阶段提高合格定尺铸坯产量的方法 |
CN103464699B (zh) * | 2013-08-13 | 2016-01-20 | 新疆八一钢铁股份有限公司 | 一种提高连铸机中间包热交换成功率的方法 |
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Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10027324C2 (de) * | 1999-06-07 | 2003-04-10 | Sms Demag Ag | Verfahren zum Gießen eines metallischen Strangs sowie System hierzu |
AT413950B (de) * | 2004-05-26 | 2006-07-15 | Voest Alpine Ind Anlagen | Stranggiessanlage mit mindestens einem roboter und verfahren zum betrieb einer stranggiessanlage unter einbindung von mindestens einem roboter |
KR101485663B1 (ko) | 2013-04-16 | 2015-01-22 | 주식회사 포스코 | 연속주조 주편의 폭 제어방법 |
CN106141132A (zh) * | 2015-03-31 | 2016-11-23 | 新日铁住金工程技术株式会社 | 铸坯的制造方法及连续铸造装置 |
CN105127390B (zh) * | 2015-09-02 | 2017-08-29 | 中冶连铸技术工程有限责任公司 | 连铸用电磁搅拌控制方法及*** |
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ES2949545T3 (es) | 2018-02-28 | 2023-09-29 | Heraeus Electro Nite Int | Método y aparato para monitorizar un proceso de colada de acero continuo |
CN110057864B (zh) * | 2019-05-08 | 2020-02-07 | 北京科技大学 | 一种钢液在水口通道内加热过程的模拟装置和方法 |
CN111199119B (zh) * | 2019-12-18 | 2022-06-17 | 中冶南方连铸技术工程有限责任公司 | 连铸异形坯坯头温度模拟方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4235276A (en) * | 1979-04-16 | 1980-11-25 | Bethlehem Steel Corporation | Method and apparatus for controlling caster heat removal by varying casting speed |
CH646352A5 (en) * | 1980-01-11 | 1984-11-30 | Vnii Avtom Chernoi Metallurg | Apparatus for regulating the secondary cooling in a continuous-casting installation with batchwise smelt supply via a tundish |
JPH07112260A (ja) * | 1993-10-14 | 1995-05-02 | Nippon Steel Corp | 連続鋳造装置のピンチローラ速度制御装置 |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE415535B (sv) * | 1978-06-13 | 1980-10-13 | Asea Ab | Anordning vid kontinuerlig gjutning, sasom strenggjutning |
JP2543909B2 (ja) * | 1987-09-24 | 1996-10-16 | 新日本製鐵株式会社 | 鋼帯の連続鋳造方法 |
JPH07132349A (ja) * | 1993-11-10 | 1995-05-23 | Nippon Steel Corp | 双ロール式連続鋳造方法 |
FR2734186B1 (fr) * | 1995-05-17 | 1997-06-13 | Unimetall Sa | Procede de lubrification des parois d'une lingotiere de coulee continue des metaux et lingotiere pour sa mise en oeuvre |
JP3188148B2 (ja) * | 1995-07-25 | 2001-07-16 | 三菱重工業株式会社 | 連続鋳造機 |
DE19529046A1 (de) * | 1995-07-31 | 1997-02-06 | Mannesmann Ag | Verfahren und Einrichtung zum Betreiben einer Stranggießanlage |
DE19725433C1 (de) * | 1997-06-16 | 1999-01-21 | Schloemann Siemag Ag | Verfahren und Vorrichtung zur Durchbruchfrüherkennung beim Stranggießen von Stahl mit einer oszillierenden Kokille |
DE10027324C2 (de) * | 1999-06-07 | 2003-04-10 | Sms Demag Ag | Verfahren zum Gießen eines metallischen Strangs sowie System hierzu |
UA74557C2 (en) * | 1999-09-03 | 2006-01-16 | Applied Research Systems | A method for producing a heterologous secreted protein from chinese hamster ovaries cells grown on microcarriers |
-
2000
- 2000-07-04 EP EP00114274A patent/EP1066898B1/de not_active Expired - Lifetime
- 2000-07-04 ES ES00114274T patent/ES2238224T3/es not_active Expired - Lifetime
- 2000-07-04 AT AT00114274T patent/ATE290446T1/de active
- 2000-07-04 DE DE50009703T patent/DE50009703D1/de not_active Expired - Lifetime
- 2000-07-05 US US09/610,412 patent/US6539273B1/en not_active Expired - Lifetime
- 2000-07-06 JP JP2000205380A patent/JP2001038456A/ja active Pending
- 2000-07-06 CN CNB001242369A patent/CN1258415C/zh not_active Expired - Fee Related
- 2000-07-06 KR KR1020000038484A patent/KR100720429B1/ko not_active IP Right Cessation
- 2000-08-03 TW TW089113281A patent/TW452515B/zh not_active IP Right Cessation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4235276A (en) * | 1979-04-16 | 1980-11-25 | Bethlehem Steel Corporation | Method and apparatus for controlling caster heat removal by varying casting speed |
CH646352A5 (en) * | 1980-01-11 | 1984-11-30 | Vnii Avtom Chernoi Metallurg | Apparatus for regulating the secondary cooling in a continuous-casting installation with batchwise smelt supply via a tundish |
JPH07112260A (ja) * | 1993-10-14 | 1995-05-02 | Nippon Steel Corp | 連続鋳造装置のピンチローラ速度制御装置 |
Non-Patent Citations (1)
Title |
---|
PATENT ABSTRACTS OF JAPAN vol. 1995, no. 08 29 September 1995 (1995-09-29) * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2864844A1 (fr) * | 2004-01-07 | 2005-07-08 | Saint Gobain | Dispositif d'eclairage autonettoyant |
CN103464699B (zh) * | 2013-08-13 | 2016-01-20 | 新疆八一钢铁股份有限公司 | 一种提高连铸机中间包热交换成功率的方法 |
CN104226951A (zh) * | 2014-09-05 | 2014-12-24 | 河北钢铁股份有限公司邯郸分公司 | 一种连铸机停浇阶段提高合格定尺铸坯产量的方法 |
Also Published As
Publication number | Publication date |
---|---|
CN1258415C (zh) | 2006-06-07 |
US6539273B1 (en) | 2003-03-25 |
JP2001038456A (ja) | 2001-02-13 |
TW452515B (en) | 2001-09-01 |
ATE290446T1 (de) | 2005-03-15 |
KR20010015196A (ko) | 2001-02-26 |
CN1280041A (zh) | 2001-01-17 |
DE50009703D1 (de) | 2005-04-14 |
EP1066898B1 (de) | 2005-03-09 |
KR100720429B1 (ko) | 2007-05-21 |
ES2238224T3 (es) | 2005-09-01 |
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