EP0342082B1 - Method for cooling a metallic continuous casting product - Google Patents

Method for cooling a metallic continuous casting product Download PDF

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Publication number
EP0342082B1
EP0342082B1 EP89401150A EP89401150A EP0342082B1 EP 0342082 B1 EP0342082 B1 EP 0342082B1 EP 89401150 A EP89401150 A EP 89401150A EP 89401150 A EP89401150 A EP 89401150A EP 0342082 B1 EP0342082 B1 EP 0342082B1
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EP
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Prior art keywords
cooling
product
core
pasty
process according
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EP89401150A
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German (de)
French (fr)
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EP0342082A1 (en
Inventor
Manuel Bobadilla
Michel Martinot
Jean-Marc Jolivet
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ASCOMETAL EN UGINE EN UNIMETAL SOCIETE FRANCAISE D
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Unimetal SA
Ugine SA
Ascometal SA
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Application filed by Unimetal SA, Ugine SA, Ascometal SA filed Critical Unimetal SA
Priority to AT89401150T priority Critical patent/ATE91656T1/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
    • B22D11/12Accessories for subsequent treating or working cast stock in situ
    • B22D11/124Accessories for subsequent treating or working cast stock in situ for cooling

Definitions

  • the present invention relates to a method of cooling a metal product during continuous casting intended to reduce, or even eliminate the presence of a large segregated zone in the central part of the product.
  • This process is advantageously applicable to the continuous casting of steel products known to be difficult to cast according to this technique, such as steels having a wide solidification interval, that is to say for example those whose carbon content is between 0, 25 and 1.5% approximately.
  • pasty state is meant a state where the metal is at a temperature between the liquidus and the solidus, and where coexist in variable proportions of the liquid metal and solid crystals.
  • the interfaces between these various concentric bodies constitute, respectively, as we are used to designating them, the fronts of ending and beginning solidification.
  • the liquid core disappears (bottom of the beginning solidification well), and only a solidified crust and a pasty core remain.
  • the pasty zone disappears in turn (closing of the finishing solidification well) and the product is completely solidified.
  • the forced cooling of the product in the mold and after its exit from the mold provides rapid growth in the thickness of solidified skin, in order to limit the risks of breakthrough and significantly increase the speed of extraction of the product, on which the productivity of the continuous casting machine.
  • the solubility in iron of alloying elements is lower when the iron is in the solid state than in the liquid state.
  • alloying elements such as carbon
  • the other alloying elements have a behavior similar to that of carbon, and the location of the segregated zones can be deduced from the tests commonly called "Baumann imprints" which make it possible to identify the distribution of the sulfur on a polished section of the product.
  • These segregated zones also identifiable on metallographic attacks, have a detrimental influence on the homogeneity of the mechanical properties of the product.
  • the relatively higher concentration of carbon in the center leads to higher hardness in these areas than in the rest of the product after rolling.
  • the object of the present invention is to propose a simple and economical solution for reducing, or even eliminating the highly segregated zones in the core of the continuously cast products, by attacking the very cause responsible for their formation. It can be added to or a substitute for electromagnetic stirring in the end of pasty solidification zone.
  • the subject of the invention is a method of cooling a metal product, in particular steel, during continuous casting, characterized in that a forced cooling of the product is carried out, while the product is in pasty solidification phase, this cooling being carried out so that the differential thermal contraction between the pasty core and the already completely solidified crust which envelops it, permanently causes a tightening effect of the heart by the crust.
  • This cooling is carried out in an area which extends at least between the place where, in the absence of such cooling, the rate of cooling of the pasty core of the product would exceed that of the surface of the product, and a place where the thermomechanical behavior of the pasty core during cooling is identical to that of the solidified outer crust.
  • the invention consists in fact in using the solidified outer crust as a vice which accompanies the contraction of the heart during cooling.
  • the inside diameter of the ring formed by the solidified crust must decrease faster than the diameter of the pasty core would decrease if the crust had no effect on the heart.
  • This vice is put into action, by thermal, simply by means of an accelerated cooling of the surface of the product in the lower part of the machine, where usually the product was allowed to cool naturally.
  • Figure 1 is a schematic longitudinal section of a conventional continuous casting installation, and in particular it shows the product being solidified.
  • a pocket not shown, feeds liquid steel 1 to a distribution basket 2.
  • the liquid steel 1 then flows into one or more ingot molds 3 with copper or copper alloy walls energetically cooled by water. It is in each of these ingot molds or primary cooling zones X that the solidification of a product 4 begins at its periphery, which thus takes its final section.
  • the mold shown in Figure 1 has a curvature, and it is found on the product. The case of the right ingot mold giving birth to a right product is also encountered in industrial practice.
  • the secondary cooling zone Y in which the product 4 is sprayed over a variable length according to the machines by a ramp of injectors 5. These project all around the product a cooling fluid , usually sprayed or atomized water.
  • a cooling fluid usually sprayed or atomized water.
  • the natural cooling zone Z where a conventional machine such as that shown schematically does not have means for cooling the product.
  • a conventional machine such as that shown schematically does not have means for cooling the product.
  • FIG. 1 makes it possible to distinguish several concentric regions inside the product during casting, corresponding to the physical state of the material which they contain.
  • a product section located in the upper part of the machine for example in zone Y
  • the metal is entirely in the liquid state; the section of this zone decreases as the product solidifies, and after the point of closure of the liquid well 7, there is no longer any liquid metal alone.
  • a pasty region 8 corresponding to the metal being solidified, contains both liquid and solid. The proportion of the latter increases as the temperature decreases.
  • the crust 9 consists only of solidified metal. Beyond the closing point of the ending solidification well 10, this region 9 covers the entire product, the solidification of which is then completed.
  • the zone of the installation which extends between the meniscus and the level corresponding to the point of closure of the finishing solidification well 10 is called "metallurgical length".
  • Figure 2 shows the continuous casting machine of Figure 1 modified according to the invention.
  • the elements common with Figure 1 are identified by the same numbers.
  • the difference between the two configurations lies in the addition to the original machine of a second ramp of injectors 11, located in the zone Z of the machine where the product completes its solidification.
  • Curves A and B correspond to the case of FIG. 1, where the product, in the terminal part of the machine, is not subjected to any forced cooling.
  • Curve A represents the rate of surface cooling of the product. It shows that this speed remains substantially constant (a loss of 0.5 ° C / s) over the entire length of the zone considered.
  • Curve B represents the rate of cooling of the pasty core of the product. It shows that, at the start of the zone considered, the temperature of the pasty core remains practically constant, as the cooling rate appears close to 0 ° C / s. It is only from a distance to the meniscus of approximately 8 m that the cooling of the pasty heart accelerates significantly. At a distance from the meniscus of 9.5 m, curve B intersects curve A.
  • Curves C and D correspond to the case of FIG. 2, where the product, in accordance with the invention, is subjected to forced cooling in the zone Z at the end of solidification by means of the injector ramp 11.
  • These curves have been traced in the hypothesis where the product is watered, between the distances to the meniscus 8.40 m and 11.20 m, with water at a flow rate of 12 m3 per hour and per m2 of product sprayed, this flow rate being evenly distributed over the entire watering area.
  • the distance to the meniscus of 8.40 m was chosen from curves A and B in Figure 3, that is to say a distance which is less than the distance of 9.50 m at which, in the absence of such a watering zone (case of FIG.
  • the rate of cooling of the pasty core begins to exceed the rate of cooling of the surface of the product.
  • Curve C represents, when the product is watered according to the invention, the rate of cooling of the surface of the product
  • curve D represents, under the same conditions, the rate of cooling of the pasty core. Upstream of the cooling zone, these curves merge with curves A and B respectively. From the start of the forced cooling zone, the cooling of the surface accelerates suddenly, reaching 9 ° C / s at a distance at the meniscus 9 m. Then, the cooling becomes more and more slow, because of the progressive deterioration of the quality of the heat exchanges between the cooling water (whose flow and temperature are constant) and the product (whose temperature decreases as and as it progresses through the cooling zone).
  • the recommended cooling water flows are of the order of 8 to 15 m3 / h and per m2 of sprinkled metal. Preferably, a flow rate of 12 m3 / m2.h is chosen.
  • This process is easily adaptable to all continuous casting machines intended for the manufacture of steel products. It is more specifically designed for the casting of steel grades containing approximately from 0.25 to 1.5% of carbon.
  • a variant of this method would consist in designing the cooling ramp 11 so that the flow of cooling fluid varies between the start and the end of the cooling zone.
  • the value of the average overall flow over the entire area would be unchanged compared to the configuration described above. In this way, it would be possible to better control the flow of heat extracted from the product along the cooling zone, in order to attenuate the reduction, visible in FIG. 3, of the speed of cooling at the surface of the product. Thus, one would increase the probability of having until the extreme end of solidification a cooling at heart less rapid than in skin.
  • the invention is not limited to the examples described, but extends to multiple variants or equivalents insofar as the characteristics mentioned in the appended claims are respected.
  • the method according to the invention can be applied to vertical, straight or curved continuous casting machines, as well as to horizontal continuous casting machines, as well as to existing or future installations for casting. direct continuous of thin products.
  • the invention does not apply restrictively to steel semi-finished products, but extends its field of application to any metallurgical product which is poured continuously, or which may be.
  • the invention applies equally to any metallurgical product cast continuously whatever its format: blooms, billets or slabs, in particular those intended for slitting to form blooms.

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  • 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)
  • Molds, Cores, And Manufacturing Methods Thereof (AREA)
  • Superconductors And Manufacturing Methods Therefor (AREA)
  • Heat Treatment Of Articles (AREA)

Abstract

The method according to the invention is characterised in that an intense cooling of the product in the process of being continuously cast is carried out when the latter is, at its core, in the pasty solidification phase (8), as a result of which the differential thermal contraction between the pasty core and the outer shell which is already completely solidified produces a squeezing effect of the core by the shell (9). To this end, means for cooling the product are arranged on the casting machine in the region of the terminal portion of the metallurgical length. <??>The invention makes it possible to reduce, and even prevent the formation of internal cracks during the cooling of the cast product, which would lead to the presence of segregated areas in the axial region. It is applied advantageously to the casting of steels which are well known to be difficult to cast by continuous casting, such as steels with a wide solidification range, the carbon content of which is from 0.25 to 1.5%. <IMAGE>

Description

La présente invention concerne un procédé de refroidissement d'un produit métallique en cours de coulée continue destiné à réduire, voire éliminer la présence d'une importante zone ségrégée dans la partie centrale du produit. Ce procédé est avantageusement applicable à la coulée continue de produits en acier réputés difficilement coulables selon cette technique, comme les aciers ayant un large intervalle de solidification, c'est-à-dire par exemple ceux dont la teneur en carbone se situe entre 0,25 et 1,5% environ.The present invention relates to a method of cooling a metal product during continuous casting intended to reduce, or even eliminate the presence of a large segregated zone in the central part of the product. This process is advantageously applicable to the continuous casting of steel products known to be difficult to cast according to this technique, such as steels having a wide solidification interval, that is to say for example those whose carbon content is between 0, 25 and 1.5% approximately.

Pour la bonne compréhension de ce qui va suivre, on aura avantage à se représenter le produit en cours de solidification comme la combinaison de trois corps concentriques, à savoir : un anneau constitué par la croûte externe, ou peau, déjà solidifiée, enserrant un autre anneau à l'état pâteux, lequel entoure le coeur liquide de métal en fusion. Par état pâteux, on entend un état où le métal se trouve à une température comprise entre le liquidus et le solidus, et où coexistent dans des proportions variables du métal liquide et des cristaux solides. Au cours de l'extraction du produit, celui-ci défile lentement le long de la machine en étant refroidi, de sorte que la solidification progresse de la périphérie vers le centre. Le coeur liquide et l'anneau pâteux présentent ainsi des profils coniques dont les pointes sont orientées vers le bas de la machine. Les interfaces entre ces différents corps concentriques constituent, respectivement, comme on a l'habitude de les désigner, les fronts de solidification finissante et commençante. A un stade avancé de la solidification, le coeur liquide disparaît (fond du puits de solidification commençante), et seuls subsistent une croûte solidifiée et un coeur pâteux. A un stade ultérieur, la zone pâteuse disparaît à son tour (fermeture du puits de solidification finissante) et le produit est complètement solidifié.For the good understanding of what follows, it will be advantageous to represent the product being solidified as the combination of three concentric bodies, namely: a ring formed by the outer crust, or skin, already solidified, enclosing another pasty ring which surrounds the liquid core of molten metal. By pasty state is meant a state where the metal is at a temperature between the liquidus and the solidus, and where coexist in variable proportions of the liquid metal and solid crystals. During the extraction of the product, it travels slowly along the machine while being cooled, so that solidification progresses from the periphery towards the center. The liquid core and the pasty ring thus have conical profiles whose points are oriented towards the bottom of the machine. The interfaces between these various concentric bodies constitute, respectively, as we are used to designating them, the fronts of ending and beginning solidification. At an advanced stage of solidification, the liquid core disappears (bottom of the beginning solidification well), and only a solidified crust and a pasty core remain. At a later stage, the pasty zone disappears in turn (closing of the finishing solidification well) and the product is completely solidified.

La solidification et le refroidissement du produit en cours de coulée sont normalement assurés dans trois zones successives de la machine de coulée continue, à savoir, dans le sens de progression du produit au cours de son extraction :

  • la lingotière, où le métal liquide entre en contact avec des parois bonnes conductrices de la chaleur et énergiquement refroidies par circulation d'eau. C'est dans cette zone, dite de refroidissement primaire que débute la formation de la peau solidifiée qui enserre le coeur liquide du produit, et que le produit prend sa forme définitive ;
  • la zone dite de "refroidissement secondaire", qui débute juste en-dessous de la lingotière et s'étend sur une longueur variable selon les conditions locales. Dans cette zone, la peau solidifiée du produit en défilement est arrosée par un fluide refroidissant (généralement de l'eau pulvérisée, ou un mélange-air eau), ce qui a pour effet d'accélérer la progression des fronts de solidification commençante et finissante vers l'intérieur du produit. Cependant, à l'endroit où cesse l'aspersion d'eau, la solidification complète du produit n'est pas réalisée, et le coeur du produit demeure à l'état liquide ;
  • et la portion de la machine qui fait suite à la zone de refroidissement secondaire. Le produit en défilement n'y est plus arrosé et se refroidit de façon naturelle. C'est dans cette zone que s'achève la solidification du coeur du produit.
Solidification and cooling of the product during casting are normally ensured in three successive zones of the continuous casting machine, namely, in the direction of progression of the product during its extraction:
  • the ingot mold, where the liquid metal comes into contact with walls that are good conductors of heat and energetically cooled by circulation of water. It is in this zone, called primary cooling that the formation of the solidified skin begins which encloses the liquid core of the product, and that the product takes its final form;
  • the so-called "secondary cooling" zone, which begins just below the mold and extends over a variable length according to local conditions. In this zone, the solidified skin of the moving product is sprayed with a cooling fluid (generally water spray, or an air-water mixture), which has the effect of accelerating the progression of the beginning and ending solidification fronts. inward of the product. However, at the point where the spraying of water ceases, complete solidification of the product is not carried out, and the core of the product remains in the liquid state;
  • and the portion of the machine that follows the secondary cooling zone. The scrolling product is no longer watered there and cools naturally. It is in this area that the solidification of the product core ends.

Le refroidissement forcé du produit en lingotière et après sa sortie de la lingotière procure une croissance rapide de l'épaisseur de peau solidifiée, afin de limiter les risques de percée et d'augmenter sensiblement la vitesse d'extraction du produit, dont dépend directement la productivité de la machine de coulée continue.The forced cooling of the product in the mold and after its exit from the mold provides rapid growth in the thickness of solidified skin, in order to limit the risks of breakthrough and significantly increase the speed of extraction of the product, on which the productivity of the continuous casting machine.

Par ailleurs, la solubilité dans le fer des éléments d'alliage, tels que le carbone, est plus faible lorsque le fer est à l'état solide qu'à l'état liquide. Dans l'anneau pâteux, il existe donc localement dans le liquide des différences de concentration, par exemple en carbone.
Si, au sein de l'anneau pâteux, il y a mouvement du liquide enrichi en carbone cela se traduit par la présence, au centre du produit complètement solidifié, de zones dites "ségrégées", où la concentration en carbone (et/ou autres éléments ségrégants) est sensiblement plus élevée que dans les autres régions. Les autres éléments d'alliage ont un comportement analogue à celui du carbone, et l'emplacement des zones ségrégées peut être déduit des tests appelés communément "empreintes Baumann" qui permettent de repérer la répartition du soufre sur une section polie du produit. Ces zones ségrégées, repérables également sur des attaques métallographiques, ont une influence néfaste sur l'homogénéité des propriétés mécaniques du produit. C'est ainsi que la concentration relativement plus importante en carbone au centre conduit à une dureté plus élevée dans ces zones que dans le reste du produit après laminage.
Furthermore, the solubility in iron of alloying elements, such as carbon, is lower when the iron is in the solid state than in the liquid state. In the pasty ring, there are therefore locally in the liquid differences in concentration, for example in carbon.
If, within the pasty ring, there is movement of the liquid enriched in carbon, this results in the presence, in the center of the completely solidified product, of so-called "segregated" zones, where the carbon concentration (and / or other segregating elements) is significantly higher than in other regions. The other alloying elements have a behavior similar to that of carbon, and the location of the segregated zones can be deduced from the tests commonly called "Baumann imprints" which make it possible to identify the distribution of the sulfur on a polished section of the product. These segregated zones, also identifiable on metallographic attacks, have a detrimental influence on the homogeneity of the mechanical properties of the product. Thus, the relatively higher concentration of carbon in the center leads to higher hardness in these areas than in the rest of the product after rolling.

Ce phénomène est particulièrement marqué dans le cas des aciers très chargés en éléments d'alliage, tels que ceux contenant 0,5 à 1,5 % de carbone et couramment appelés aciers à large intervalle de solidification, comme la nuance d'acier à roulements 100 C6 par exemple. Une "empreinte Baumann" réalisée sur un échantillon du produit prélevé selon l'axe longitudinal de celui-ci montrerait que les ségrégations se répartissent autour de l'axe du produit suivant des "vés" dont les mécanismes de formation ne sont d'ailleurs pas encore totalement élucidés.This phenomenon is particularly marked in the case of steels heavily loaded with alloying elements, such as those containing 0.5 to 1.5% of carbon and commonly called steels with a large solidification interval, such as the grade of bearing steel. 100 C6 for example. A "Baumann imprint" made on a sample of the product taken along its longitudinal axis would show that the segregations are distributed around the axis of the product according to "ves" whose formation mechanisms are not, moreover, still completely elucidated.

On a tenté de résoudre ce problème par l'application d'un brassage électromagnétique du métal dans la zone de solidification pâteuse de manière à forcer le liquide ségrégé à se répartir sur une zone plus étendue. Mais ce faisant, on corrige en fait les effets sans s'attaquer vraiment aux causes du phénomène. De plus, cette technique implique l'acquisition d'au moins un inducteur de brassage, ainsi que des coûts de fonctionnement non négligeablesAn attempt has been made to resolve this problem by applying an electromagnetic stirring of the metal in the pasty solidification zone so as to force the segregated liquid to be distributed over a more extensive zone. But in doing so, we actually correct the effects without really addressing the causes of the phenomenon. In addition, this technique involves the acquisition of at least one stirring inductor, as well as significant operating costs.

Le but de la présente invention est de proposer une solution simple et économique pour réduire, voire éliminer les zones fortement ségrégées dans le coeur des produits coulés en continu, en s'attaquant à la cause même responsable de leur formation. Elle peut s'ajouter ou se substituer à un brassage électromagnétique dans la zone de fin de solidification pâteuse.The object of the present invention is to propose a simple and economical solution for reducing, or even eliminating the highly segregated zones in the core of the continuously cast products, by attacking the very cause responsible for their formation. It can be added to or a substitute for electromagnetic stirring in the end of pasty solidification zone.

A cet effet, l'invention a pour objet un procédé de refroidissement d'un produit métallique, notamment en acier, en cours de coulée continue, caractérisé en ce qu'on réalise un refroidissement forcé du produit, alors que le produit se trouve en phase de solidification pâteuse, ce refroidissement étant mené de manière que la contraction thermique différentielle entre le coeur pâteux et la croûte déjà complètement solidifiée qui l'enveloppe, provoque en permanence un effet de serrage du coeur par la croûte. Ce refroidissement est mis en oeuvre dans une zone qui s'étend au moins entre l'endroit où, en l'absence d'un tel refroidissement, la vitesse de refroidissement du coeur pâteux du produit dépasserait celle de la surface du produit, et un endroit où le comportement thermomécanique du coeur pâteux en cours de refroidissement est identique à celui de la croûte extérieure solidifiée.To this end, the subject of the invention is a method of cooling a metal product, in particular steel, during continuous casting, characterized in that a forced cooling of the product is carried out, while the product is in pasty solidification phase, this cooling being carried out so that the differential thermal contraction between the pasty core and the already completely solidified crust which envelops it, permanently causes a tightening effect of the heart by the crust. This cooling is carried out in an area which extends at least between the place where, in the absence of such cooling, the rate of cooling of the pasty core of the product would exceed that of the surface of the product, and a place where the thermomechanical behavior of the pasty core during cooling is identical to that of the solidified outer crust.

Comme on l'aura compris, l'invention consiste en fait à se servir de la croûte extérieure solidifiée comme d'un étau qui accompagne la contraction du coeur lors du refroidissement. Autrement dit, le diamètre intérieur de l'anneau formé par la croûte solidifiée doit diminuer plus vite que ne diminuerait le diamètre du coeur pâteux si la croûte n'exerçait aucune action sur le coeur. Cet étau est mis en action, par la thermique, simplement au moyen d'un refroidissement accéléré de la surface du produit dans la partie basse de la machine, là où habituellement on laissait le produit se refroidir naturellement.As will be understood, the invention consists in fact in using the solidified outer crust as a vice which accompanies the contraction of the heart during cooling. In other words, the inside diameter of the ring formed by the solidified crust must decrease faster than the diameter of the pasty core would decrease if the crust had no effect on the heart. This vice is put into action, by thermal, simply by means of an accelerated cooling of the surface of the product in the lower part of the machine, where usually the product was allowed to cool naturally.

On a indiqué plus haut que les causes de formation des "vés" ségrégés dans la partie centrale du produit coulé n'étaient pas à ce jour parfaitement identifiées et expliquées.It was indicated above that the causes of formation of segregated "ves" in the central part of the cast product have not yet been fully identified and explained.

Toutefois, l'hypothèse faite par les inventeurs comme étant la plus probable et qui sous-tend la présente invention, peut être schématiquement exposée de la façon suivante.However, the hypothesis made by the inventors as being the most probable and which underlies the present invention, can be schematically explained as follows.

Lors de la traversée de la zone de refroidissement secondaire, la peau du produit se refroidit rapidement, alors que le coeur liquide demeure à une température presque constante. Au passage du produit dans la zone de refroidissement naturel, le refroidissement de la peau, qui n'est plus arrosée, devient beaucoup plus lent. D'autre part, compte tenu de la longueur habituelle de la zone de refroidissement secondaire, c'est seulement lorsque le produit est déjà largement engagé dans la zone de refroidissement naturel que la température du coeur (qui se trouve alors dans l'état pâteux), tend à s'abaisser sensiblement.When passing through the secondary cooling zone, the skin of the product cools rapidly, while the liquid core remains at an almost constant temperature. As the product passes through the natural cooling zone, the cooling of the skin, which is no longer watered, becomes much slower. On the other hand, given the length usual in the secondary cooling zone, it is only when the product is already largely engaged in the natural cooling zone that the temperature of the core (which is then in the pasty state), tends to drop appreciably.

La partie interne pâteuse du produit se refroidit alors plus rapidement que la couche solide qui l'enveloppe et subit une plus forte contraction thermique. Les contraintes mécaniques ainsi créées se libèrent par formation de fissures dans le bloc central préalablement "pâteux", fissures dans lesquelles peut pénétrer par aspiration, du liquide fortement ségrégé.The pasty internal part of the product then cools more quickly than the solid layer which envelops it and undergoes a greater thermal contraction. The mechanical stresses thus created are released by the formation of cracks in the central block previously "pasty", cracks in which can penetrate by suction, highly segregated liquid.

Ainsi, dans le produit complètement solidifié, les emplacements de ces fissures seront repérés par leur concentration élevée en éléments d'alliage, conduisant aux défauts cités plus haut.Thus, in the completely solidified product, the locations of these cracks will be identified by their high concentration of alloying elements, leading to the defects mentioned above.

Dans le cas des aciers fortement chargés en éléments d'alliage, tels que le carbone, comme le 100 C6 par exemple, l'écart entre les températures de début et de fin de solidification est relativement important, et la solidification pâteuse est donc susceptible de s'effectuer sur une zone plus étendue que dans le cas des nuances peu alliées. Ceci, joint à une plus grande sensibilité à la ségrégation des éléments entre les phases liquide et solide, explique pourquoi les nuances alliées sont à ce point sujettes à la formation de zones ségrégées dans la région axiale des produits coulés en continu. Dans certains cas extrêmes, de tels défauts rendent impossible l'obtention de produit finis d'une qualité suffisante, et imposent de devoir renoncer à les produire par coulée continue.In the case of steels heavily loaded with alloying elements, such as carbon, such as 100 C6 for example, the difference between the temperatures at the start and end of solidification is relatively large, and pasty solidification is therefore likely to be carried out over a wider area than in the case of low alloy grades. This, together with a greater sensitivity to the segregation of the elements between the liquid and solid phases, explains why the alloyed grades are so subject to the formation of segregated zones in the axial region of the continuously cast products. In certain extreme cases, such defects make it impossible to obtain finished products of sufficient quality, and impose the necessity of giving up producing them by continuous casting.

On vient de voir rapidement comment l'invention, en provoquant une contraction thermique de la croûte solide périphérique, contrecarre les vélléités du produit à former ces fissures internes responsables des zones centrales fortement ségrégées. Toutefois l'invention sera bien comprise et d'autres caractéristiques et avantages ressortiront de la description détaillée suivante donnée en référence aux planches de dessins annexées, sur lesquelles :

  • la figure 1 représente schématiquement une installation de coulée continue courbe de demi-produits en acier, de conception classique ;
  • la figure 2 représente l'installation de la figure 1, modifiée selon l'invention par adjonction d'une rampe de refroidissement dans la zone de fin de solidification, du produit ;
  • la figure 3 montre un cas d'évolution des vitesses de refroidissement de la surface et du coeur du produit au cours de son défilement dans la partie inférieure de la machine. Sont figurés les deux cas de l'absence et de la présence d'un dispositif de refroidissement dans la zone de fin de solidification du produit.
We have just quickly seen how the invention, by causing a thermal contraction of the peripheral solid crust, counteracts the velocity of the product to form these cracks interns responsible for highly segregated central areas. However, the invention will be well understood and other characteristics and advantages will emerge from the following detailed description given with reference to the accompanying drawing plates, in which:
  • Figure 1 schematically shows a continuous casting installation of semi-finished steel semi-finished products, of conventional design;
  • 2 shows the installation of Figure 1, modified according to the invention by adding a cooling ramp in the end of solidification zone, of the product;
  • FIG. 3 shows a case of evolution of the cooling speeds of the surface and of the core of the product during its movement in the lower part of the machine. The two cases of the absence and the presence of a cooling device in the zone of end of solidification of the product are shown.

La figure 1 est une coupe schématique longitudinale d'une installation classique de coulée continue, et elle présente notamment le produit en cours de solidification. Une poche, non représentée, alimente en acier liquide 1 un panier répartiteur 2. L'acier liquide 1 s'écoule ensuite dans une ou plusieurs lingotières 3 aux parois en cuivre ou alliage de cuivre énergiquement refroidies par eau. C'est dans chacune de ces lingotières ou zones de refroidissement primaire Ⓧ que s'amorce par sa périphérie la solidification d'un produit 4 qui prend ainsi sa section définitive. La lingotière montrée par la figure 1 présente une courbure, et celle-ci se retrouve sur le produit. Le cas de la lingotière droite donnant naissance à un produit droit est également rencontré dans la pratique industrielle. Juste en-dessous de la lingotière 3 débute la zone de refroidissement secondaire Ⓨ dans laquelle le produit 4 est arrosé sur une longueur variable selon les machines par une rampe d'injecteurs 5. Ceux-ci projettent sur tout le pourtour du produit un fluide refroidissant, généralement de l'eau pulvérisée ou atomisée. Vient ensuite la zone de refroidissement naturel Ⓩ , où une machine classique telle que celle schématisée ne comporte pas de moyens de refroidissement du produit. Dans la partie inférieure de la machine se trouvent les moyens (non représentés) de décintrage du produit, chargés de lui donner une forme droite, et des moyens (non représentés) de tronçonnage du produit pour sa mise à longueur.Figure 1 is a schematic longitudinal section of a conventional continuous casting installation, and in particular it shows the product being solidified. A pocket, not shown, feeds liquid steel 1 to a distribution basket 2. The liquid steel 1 then flows into one or more ingot molds 3 with copper or copper alloy walls energetically cooled by water. It is in each of these ingot molds or primary cooling zones Ⓧ that the solidification of a product 4 begins at its periphery, which thus takes its final section. The mold shown in Figure 1 has a curvature, and it is found on the product. The case of the right ingot mold giving birth to a right product is also encountered in industrial practice. Just below the ingot mold 3 begins the secondary cooling zone Ⓨ in which the product 4 is sprayed over a variable length according to the machines by a ramp of injectors 5. These project all around the product a cooling fluid , usually sprayed or atomized water. Next comes the natural cooling zone Ⓩ, where a conventional machine such as that shown schematically does not have means for cooling the product. In the lower part of the machine are the means (not shown) for decentring the product, responsible for giving it a straight shape, and means (not shown) for cutting up the product for cutting it to length.

La figure 1 permet de distinguer plusieurs régions concentriques à l'intérieur du produit en cours de coulée, correspondant à l'état physique de la matière qu'elles renferment. Dans une section de produit située dans la partie supérieure de la machine (par exemple dans la zone Y), on rencontre successivement trois régions. A coeur (région 6) le métal se trouve entièrement à l'état liquide ; la section de cette zone diminue au fur et à mesure de la solidification du produit, et après le point de fermeture du puits liquide 7, on ne trouve plus de métal liquide seul. Autour du coeur liquide 6, une région pâteuse 8, correspondant au métal en cours de solidification, renferme à la fois du liquide et du solide. La proportion de ce dernier augmente à mesure que la température diminue. Autour de la région pâteuse, la croûte 9 n'est constituée que de métal solidifié. Au-delà du point de fermeture du puits de solidification finissante 10, cette région 9 recouvre l'ensemble du produit, dont la solidification est alors achevée. La zone de l'installation qui s'étend entre le ménisque et le niveau correspondant au point de fermeture du puits de solidification finissante 10 est appelée " longueur métallurgique".FIG. 1 makes it possible to distinguish several concentric regions inside the product during casting, corresponding to the physical state of the material which they contain. In a product section located in the upper part of the machine (for example in zone Y), there are successively three regions. At the core (region 6) the metal is entirely in the liquid state; the section of this zone decreases as the product solidifies, and after the point of closure of the liquid well 7, there is no longer any liquid metal alone. Around the liquid core 6, a pasty region 8, corresponding to the metal being solidified, contains both liquid and solid. The proportion of the latter increases as the temperature decreases. Around the pasty region, the crust 9 consists only of solidified metal. Beyond the closing point of the ending solidification well 10, this region 9 covers the entire product, the solidification of which is then completed. The zone of the installation which extends between the meniscus and the level corresponding to the point of closure of the finishing solidification well 10 is called "metallurgical length".

La figure 2 présente la machine de coulée continue de la figure 1 modifiée selon l'invention. Les éléments communs avec la figure 1 sont repérés par les mêmes chiffres. La différence entre les deux configurations réside dans l'adjonction à la machine originale d'une deuxième rampe d'injecteurs 11, située dans la zone Ⓩ de la machine où le produit achève sa solidification.Figure 2 shows the continuous casting machine of Figure 1 modified according to the invention. The elements common with Figure 1 are identified by the same numbers. The difference between the two configurations lies in the addition to the original machine of a second ramp of injectors 11, located in the zone Ⓩ of the machine where the product completes its solidification.

La figure 3 montre des exemples d'évolution de la vitesse V de refroidissement du métal en surface et à coeur au fur et à mesure de l'avancement du produit dans la zone Ⓩ de la machine où il achève sa solidification. Cet avancement est exprimée par la distance D au ménisque, c'est-à-dire la surface du métal liquide en lingotière. Les courbes ont été tracées à l'aide de modèles mathématiques similaires à ceux dont disposent les utilisateurs de machines de coulée continue. Elles sont valables pour les conditions de coulée suivantes :

  • format du produit : billettes de section carrée, de 105 mm de côté,
  • composition du produit : acier à 0,7 % de carbone,
  • vitesse d'extraction du produit : 3,3 m/min.
FIG. 3 shows examples of changes in the speed V of cooling of the metal at the surface and to the core as the product advances in the zone Ⓩ of the machine where it completes its solidification. This advancement is expressed by the distance D to the meniscus, that is to say the surface of the liquid metal in an ingot mold. The curves were plotted using mathematical models similar to those available to users of continuous casting machines. They are valid for the following casting conditions:
  • product format: square section billets, 105 mm side,
  • product composition: 0.7% carbon steel,
  • product extraction speed: 3.3 m / min.

Dans ces conditions la solidification complète du produit est réalisée à une distance de 11,20 m du ménisque, marquée sur la figure par la ligne S.Under these conditions, the complete solidification of the product is carried out at a distance of 11.20 m from the meniscus, marked in the figure by the line S.

Les courbes A et B correspondent au cas de la figure 1, où le produit, dans la partie terminale de la machine, n'est soumis à aucun refroidissement forcé. La courbe A représente la vitesse de refroidissement en surface du produit. Elle montre que cette vitesse reste sensiblement constante (soit une perte de 0,5°C/s) sur toute la longueur de la zone considérée. La courbe B représente la vitesse de refroidissement du coeur pâteux du produit. Elle montre que, au début de la zone considérée, la température du coeur pâteux reste pratiquement constante, comme la vitesse de refroidissement apparaît proche de 0°C/s. Ce n'est qu'à partir d'une distance au ménisque d'environ 8 m que le refroidissement du coeur pâteux s'accélère de façon notable. A une distance au ménisque de 9,5 m, la courbe B coupe la courbe A. Cela signifie qu'au-delà de ce point, le coeur pâteux commence à perdre plus de 0,5 °C/s, et donc que la vitesse de refroidissement du coeur pâteux commence à excéder la vitesse de refroidissement de la surface du produit. Cela entraîne une contraction thermique du coeur plus forte que celle de la surface, phénomène dont on a vu que, selon l'hypothèse faite par les inventeurs, il était à l'origine des défauts sur le produit que l'invention a pour but d'éviter.Curves A and B correspond to the case of FIG. 1, where the product, in the terminal part of the machine, is not subjected to any forced cooling. Curve A represents the rate of surface cooling of the product. It shows that this speed remains substantially constant (a loss of 0.5 ° C / s) over the entire length of the zone considered. Curve B represents the rate of cooling of the pasty core of the product. It shows that, at the start of the zone considered, the temperature of the pasty core remains practically constant, as the cooling rate appears close to 0 ° C / s. It is only from a distance to the meniscus of approximately 8 m that the cooling of the pasty heart accelerates significantly. At a distance from the meniscus of 9.5 m, curve B intersects curve A. This means that beyond this point, the pasty heart begins to lose more than 0.5 ° C / s, and therefore that the cooling rate of the pasty core begins to exceed the cooling rate of the product surface. This results in a stronger thermal contraction of the heart than that of the surface, a phenomenon which we have seen that, according to the hypothesis made by the inventors, it was at the origin of the defects in the product which the invention aims to 'to avoid.

Les courbes C et D correspondent au cas de la figure 2, où le produit, conformément à l'invention, est soumis à un refroidissement forcé dans la zone Ⓩ de fin de solidification au moyen de la rampe d'injecteurs 11. Ces courbes ont été tracées dans l'hypothèse où le produit est arrosé, entre les distances au ménisque 8,40 m et 11,20 m, par de l'eau à un débit de 12 m³ par heure et par m² de produit arrosé, ce débit étant réparti de façon homogène sur l'ensemble de la zone d'arrosage. La distance au ménisque de 8,40 m a été choisie d'après les courbes A et B de la Figure 3, c'est-à-dire une distance qui est inférieure à la distance de 9,50 m à laquelle, en l'absence d'une telle zone d'arrosage (cas de la figure 1), la vitesse de refroidissement du coeur pâteux commence à excéder la vitesse de refroidissement de la surface du produit. La courbe C représente, lorsque le produit est arrosé selon l'invention, la vitesse de refroidissement de la surface du produit, et la courbe D représente dans les mêmes conditions la vitesse de refroidissement du coeur pâteux. En amont de la zone de refroidissement, ces courbes se confondent respectivement avec les courbes A et B. Dès le début de la zone de refroidissement forcé, le refroidissement de la surface s'accélère brusquement, pour atteindre 9°C/s à la distance au ménisque 9 m. Ensuite, le refroidissement devient de plus en plus lent, à cause de la détérioration progressive de la qualité des échanges thermiques entre l'eau de refroidissement (dont le débit et la température sont constants) et le produit (dont la température diminue au fur et à mesure qu'il progresse dans la zone de refroidissement). Simultanément, le refroidissement forcé a pour conséquence d'accélérer le refroidissement du coeur pâteux, mais cet effet ne se fait sentir que tardivement (à partir de la distance au ménisque 10 m), et progressivement. En fin de compte, ce n'est qu'à une distance au ménisque de 11 m, que la courbe D coupe la courbe C. Cela signifie qu'à cette distance, le refroidissement du coeur pâteux devient plus rapide que celui de la surface du produit. A ce niveau, le coeur pâteux a pratiquement achevé de se solidifier, et son comportement thermomécanique est suffisamment proche de celui de la croûte entièrement solidifiée pour que le phénomène de contraction thermique différentielle soit négligeable, et que les "vés" ségrégés ne puissent être formés.Curves C and D correspond to the case of FIG. 2, where the product, in accordance with the invention, is subjected to forced cooling in the zone Ⓩ at the end of solidification by means of the injector ramp 11. These curves have been traced in the hypothesis where the product is watered, between the distances to the meniscus 8.40 m and 11.20 m, with water at a flow rate of 12 m³ per hour and per m² of product sprayed, this flow rate being evenly distributed over the entire watering area. The distance to the meniscus of 8.40 m was chosen from curves A and B in Figure 3, that is to say a distance which is less than the distance of 9.50 m at which, in the absence of such a watering zone (case of FIG. 1), the rate of cooling of the pasty core begins to exceed the rate of cooling of the surface of the product. Curve C represents, when the product is watered according to the invention, the rate of cooling of the surface of the product, and curve D represents, under the same conditions, the rate of cooling of the pasty core. Upstream of the cooling zone, these curves merge with curves A and B respectively. From the start of the forced cooling zone, the cooling of the surface accelerates suddenly, reaching 9 ° C / s at a distance at the meniscus 9 m. Then, the cooling becomes more and more slow, because of the progressive deterioration of the quality of the heat exchanges between the cooling water (whose flow and temperature are constant) and the product (whose temperature decreases as and as it progresses through the cooling zone). At the same time, forced cooling has the effect of accelerating the cooling of the pasty heart, but this effect is only felt late (from the distance to the meniscus 10 m), and gradually. In the end, it is only at a distance from the meniscus of 11 m, that curve D intersects curve C. This means that at this distance, the cooling of the pasty core becomes faster than that of the surface of the product. At this level, the pasty heart has practically solidified, and its thermomechanical behavior is sufficiently close to that of the fully solidified crust so that the phenomenon of differential thermal contraction is negligible, and that segregated "ves" cannot be formed.

L'exemple décrit ci-dessus n'est, bien sûr, pas limitatif. Une figure similaire à la figure 3 peut être tracée pour toute machine de coulée continue, sur laquelle serait coulé un produit donné dans des conditions définies.The example described above is, of course, not limiting. A figure similar to Figure 3 can be drawn for any continuous casting machine, on which a given product would be cast under defined conditions.

On considère que, au-delà de l'endroit où la fraction solide du coeur pâteux du produit atteint 90 %, il est inutile de poursuivre l'arrosage. Dans certains cas, il est même suffisant de n'arroser que jusqu'à une fraction solide de 60 %.It is considered that, beyond the point where the solid fraction of the pasty core of the product reaches 90%, it is useless to continue watering. In some cases, it is even sufficient to water only up to a solid fraction of 60%.

Il est conseillé de poursuivre le refroidissement forcé du produit jusqu'à environ 1 m au-delà du point de fin de solidification déterminé par le calcul. C'est dans cet esprit que sur la figure 3, la rampe de refroidissement 11 est représentée comme se prolongeant au-delà du point 10. De même, l'incertitude de calcul sur la détermination du point d'intersection entre les courbes A et B de la figure 3 est de ± 1 m environ. Le choix du point où débute le refroidissement forcé doit tenir compte de cette incertitude. Il est donc conseillé de placer les premiers injecteurs de la rampe 11 à au moins 1 m en amont dudit point d'intersection, ce qui a été fait dans l'exemple numérique de la figure 3, comme expliqué précédemment. Mais il faut également s'assurer que cet avancement du début du refroidissement ne provoque pas un croisement prématuré des courbes C et D de la figure 3, c'est-à-dire qui aurait lieu en un point où la fraction solide du coeur pâteux serait inférieure à 60 % au moins.It is advisable to continue forced cooling of the product to approximately 1 m beyond the end of solidification point determined by the calculation. With this in mind, in FIG. 3, the cooling ramp 11 is represented as extending beyond point 10. Likewise, the uncertainty of calculation on the determination of the point of intersection between the curves A and B in Figure 3 is approximately ± 1 m. The choice of the point where forced cooling begins must take this uncertainty into account. It is therefore advisable to place the first injectors of the ramp 11 at least 1 m upstream of said point of intersection, which was done in the digital example of FIG. 3, as explained previously. But it is also necessary to ensure that this advancement of the start of cooling does not cause a premature crossing of the curves C and D of FIG. 3, that is to say which would take place at a point where the solid fraction of the pasty core would be less than 60% at least.

Les débits d'eau de refroidissement recommandés sont de l'ordre de 8 à 15 m³/h et par m² de métal arrosé. Préférentiellement, on choisit un débit de 12 m³/m².h.The recommended cooling water flows are of the order of 8 to 15 m³ / h and per m² of sprinkled metal. Preferably, a flow rate of 12 m³ / m².h is chosen.

Ce procédé est aisément adaptable à toutes les machines de coulée continue destinées à la fabrication de produits en acier. Il est plus spécialement conçu pour la coulée de nuances d'acier contenant environ de 0,25 à 1,5 % de carbone.This process is easily adaptable to all continuous casting machines intended for the manufacture of steel products. It is more specifically designed for the casting of steel grades containing approximately from 0.25 to 1.5% of carbon.

Une variante de ce procédé consisterait à concevoir la rampe de refroidissement 11 de facon que le débit de fluide refroidissant varie entre le début et la fin de la zone de refroidissement. La valeur du débit global moyen sur l'ensemble de la zone serait inchangée par rapport à la configuration décrite précédemment. De cette façon, il serait possible de mieux contrôler le flux de chaleur extrait du produit le long de la zone de refroidissement, dans le but d'atténuer la diminution, visible sur la figure 3, de la vitessse de refroidissement en surface du produit. Ainsi, on augmenterait la probabilité d'avoir jusqu'à l'extrême fin de la solidification un refroidissement à coeur moins rapide qu'en peau.A variant of this method would consist in designing the cooling ramp 11 so that the flow of cooling fluid varies between the start and the end of the cooling zone. The value of the average overall flow over the entire area would be unchanged compared to the configuration described above. In this way, it would be possible to better control the flow of heat extracted from the product along the cooling zone, in order to attenuate the reduction, visible in FIG. 3, of the speed of cooling at the surface of the product. Thus, one would increase the probability of having until the extreme end of solidification a cooling at heart less rapid than in skin.

D'autre part, on a remarqué qu'une bonne homogénéité du coeur du produit sur lequel on allait appliquer le procédé était favorable à la reproductibilité des bons résultats métallurgiques recherchés. On a pu constater que cette homogénéité pouvait avantageusement être obtenue par une mise en mouvement du coeur liquide dans la zone du refroidissement secondaire, ou même en lingotière. Cette mise en mouvement peut être favorablement obtenue à l'aide de moyens électromagnétiques de brassage, désormais largement connus dans'le domaine de la coulée continue. Ces moyens peuvent être constitués par des inducteurs polyphasés annulaires disposés autour du produit coulé et produisant un champ magnétique tournant autour de l'axe de coulée, ou par des inducteurs polyphasés de structure plane produisant un champ glissant, parallèlement à l'axe de coulée ou perpendiculairement à ce dernier. La littérature abonde désormais à propos de ce type de brassage. Pour plus de détails, on pourra se reporter si on le souhaite aux documents suivants : le brevet français 2 315 344 pour le brassage par champ tournant en lingotière, le brevet français 2 211 304 concernant le brassage par champ tournant dans la zone du refroidissement secondaire, le brevet luxembourgeois 67 753 concernant le brassage à l'aide d'inducteurs produisant un champ glissant perpendiculairement à l'axe de coulée dans la zone du refroidissement secondaire. Les enseignements de ces différents documents sont inclus par référence dans la présente description.On the other hand, it was noted that good homogeneity of the core of the product on which the process was to be applied was favorable to the reproducibility of the good metallurgical results sought. It has been observed that this homogeneity could advantageously be obtained by setting the liquid core in motion in the secondary cooling zone, or even in an ingot mold. This setting in motion can be favorably obtained using electromagnetic stirring means, now widely known in the field of continuous casting. These means may be constituted by annular polyphase inductors arranged around the cast product and producing a magnetic field rotating around the casting axis, or by polyphase inductors of planar structure producing a sliding field, parallel to the casting axis or perpendicular to the latter. Literature now abounds about this type of brewing. For more details, reference may be made, if desired, to the following documents: French patent 2,315,344 for mixing by rotating field in an ingot mold, French patent 2,211,304 relating to mixing by rotating field in the secondary cooling zone. , the Luxembourg patent 67 753 concerning the mixing using inductors producing a sliding field perpendicular to the pouring axis in the secondary cooling zone. The lessons of these various documents are included by reference in the present description.

Il va de soi que l'invention ne se limite pas aux exemples décrits, mais s'étend à de multiples variantes ou équivalents dans la mesure où sont respectées les caractéristiques évoquées dans les revendications jointes. En particulier, le procédé selon l'invention peut s'appliquer à des machines de coulée continue verticales, droites ou courbes, de même qu'aux machines de coulée continue horizontale, de même encore qu'aux installations existantes ou à venir pour la coulée continue directe de produits de faible épaisseur.It goes without saying that the invention is not limited to the examples described, but extends to multiple variants or equivalents insofar as the characteristics mentioned in the appended claims are respected. In particular, the method according to the invention can be applied to vertical, straight or curved continuous casting machines, as well as to horizontal continuous casting machines, as well as to existing or future installations for casting. direct continuous of thin products.

D'autre part l'invention ne s'applique pas limitativement aux demi-produits sidérurgiques, mais étend son domaine d'application à tout produit métallurgique coulé en continu, ou susceptible de l'être.On the other hand, the invention does not apply restrictively to steel semi-finished products, but extends its field of application to any metallurgical product which is poured continuously, or which may be.

De même encore, l'invention s'applique indifféremment à tout produit métallurgique coulé en continu que que soit son format : blooms, billettes ou brames, notamment celles destinées au refendage pour former des blooms.Likewise also, the invention applies equally to any metallurgical product cast continuously whatever its format: blooms, billets or slabs, in particular those intended for slitting to form blooms.

Claims (13)

  1. Process for cooling a metal product (4), in particular made of steel, during continuous casting, characterised in that forced cooling of the product (4) is performed when, at the core, the product is in a phase of pasty solidification, the said cooling being conducted so that the differential thermal contraction between the pasty core (8) and the already completely solidified shell (9) surrounding it permanently gives rise to a squeezing effect of the core (8) by the shell (9) and being implemented in a zone extending along the casting machine at least between the point where, in the absence of such cooling, the speed of cooling of the pasty core (8) of the product (4) would exceed that of the surface of the product (4) and a point where the thermomechanical behaviour of the pasty core (8) during cooling is identical to that of the solidified outer shell (9).
  2. Process according to Claim 1, characterised in that the cooling is maintained so that the effect of squeezing the pasty core (8) by the solidified shell (9) is continued up to a point where the proportion of solid material within the pasty core (8) is at least 60%.
  3. Process according to Claims 1 or 2, characterised in that the forced cooling is performed by spraying a cooling fluid, such as water, onto the surface of the cast product (4).
  4. Process according to Claim 3, characterised in that the cooling is performed with water at a mean flow rate of between 8 and 15 m³ per hour and per m² of sprayed product.
  5. Process according to Claim 4, characterised in that a value of approximately 12 m³ per hour and per m² of sprayed product is chosen for the said mean flow rate.
  6. Process according to Claim 3, characterised in that the flow rate of cooling fluid varies between the start and the finish of the cooling zone.
  7. Process according to Claims 1, 2, or 3, characterised in that it is applied to the casting of products made of steel whose content of carbon by weight is of the order of 0.25 to 1.5%.
  8. Process according to Claims 1, 2, or 3, characterised in that, simultaneously, the liquid core (6) of the product (4)is stirred.with the aid of agitation means.
  9. Process according to Claim 8, characterised in that the said agitation means consist of at least one inductor with a movable electromagnetic field.
  10. Process according to Claim 9, characterised in that use is made of an inductor surrounding the cast product (4) and generating a magnetic field rotating about the casting axis.
  11. Process according to Claim 9, characterised in that use is made of an inductor of plane structure producing a sliding field within the cast product.
  12. Installation for the continuous casting of metallic products (4), particularly made of steel, such that means (11) for cooling the product are arranged in the end portion of the metallurgical length, in a zone extending along the casting machine at least between the location where, in the absence of such cooling means, the speed of cooling of the pasty core (8) of the product (4) would exceed that of the surface of the product (4), and a location where the thermomechanical behaviour of the pasty core (8) during cooling is identical to that of the solidified shell (9).
  13. Installation for continuous casting according to Claim 12, characterised in that the said cooling means (11) consist of spraying ramps spraying a cooling fluid onto the surface of the cast product (4).
EP89401150A 1988-05-13 1989-04-21 Method for cooling a metallic continuous casting product Revoked EP0342082B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT89401150T ATE91656T1 (en) 1988-05-13 1989-04-21 PROCESS FOR COOLING A METALLIC CONTINUOUS CASTING PRODUCT.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8806743A FR2631263B1 (en) 1988-05-13 1988-05-13 METHOD FOR COOLING A CONTINUOUSLY CAST METAL PRODUCT
FR8806743 1988-05-13

Publications (2)

Publication Number Publication Date
EP0342082A1 EP0342082A1 (en) 1989-11-15
EP0342082B1 true EP0342082B1 (en) 1993-07-21

Family

ID=9366459

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89401150A Revoked EP0342082B1 (en) 1988-05-13 1989-04-21 Method for cooling a metallic continuous casting product

Country Status (19)

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US (1) US5063991A (en)
EP (1) EP0342082B1 (en)
JP (1) JPH0215856A (en)
KR (1) KR960004423B1 (en)
CN (1) CN1018803B (en)
AT (1) ATE91656T1 (en)
AU (1) AU611797B2 (en)
BR (1) BR8902241A (en)
CA (1) CA1338164C (en)
CS (1) CS287289A3 (en)
DD (1) DD284175A5 (en)
DE (1) DE68907644T2 (en)
ES (1) ES2042023T3 (en)
FR (1) FR2631263B1 (en)
PL (1) PL279425A1 (en)
PT (1) PT90543B (en)
RU (1) RU1819188C (en)
UA (1) UA15737A (en)
ZA (1) ZA893402B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5725046A (en) * 1994-09-20 1998-03-10 Aluminum Company Of America Vertical bar caster
JPH08234390A (en) * 1995-02-24 1996-09-13 Fuji Photo Film Co Ltd Image forming method and silver halide photosensitive material
US6264767B1 (en) 1995-06-07 2001-07-24 Ipsco Enterprises Inc. Method of producing martensite-or bainite-rich steel using steckel mill and controlled cooling
FR2767273B1 (en) * 1997-08-14 1999-10-15 Vallourec Ind PROCESS FOR THE MANUFACTURE BY CONTINUOUS CASTING OF STEEL PRODUCTS
AU4596899A (en) 1998-07-10 2000-02-01 Ipsco Inc. Method and apparatus for producing martensite- or bainite-rich steel using steckel mill and controlled cooling
JP5145791B2 (en) 2007-06-28 2013-02-20 新日鐵住金株式会社 Continuous casting method for small section billet
US8245760B2 (en) * 2007-11-19 2012-08-21 Posco Continuous cast slab and method for manufacturing the same
EP2654990B1 (en) * 2010-12-22 2015-12-09 Novelis, Inc. Elimination of shrinkage cavity in cast ingots
CN102161090B (en) * 2010-12-23 2012-11-07 中国科学院金属研究所 Method for improving self-feeding capacity of high and thick large-cross section casting blank

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US3512574A (en) * 1966-12-02 1970-05-19 Inland Steel Co Continuous casting process and apparatus
US3502133A (en) * 1967-03-03 1970-03-24 Reynolds Metals Co Continuous casting method and apparatus for controlling freeze line location
US3771584A (en) * 1971-01-08 1973-11-13 Roblin Industries Method for continuously casting steel billet strands to minimize the porosity and chemical segregation along the center line of the strand
FR2231454A2 (en) * 1973-05-29 1974-12-27 Cem Comp Electro Mec Slab casting machine - with metal stirring by electrically wound withdrawal rolls
US3882923A (en) * 1972-06-08 1975-05-13 Siderurgie Fse Inst Rech Apparatus for magnetic stirring of continuous castings
FR2211305B1 (en) * 1972-12-21 1975-06-06 Cem Comp Electro Mec
CH559586A5 (en) * 1973-06-04 1975-03-14 Concast Ag
FR2315344A1 (en) * 1975-06-27 1977-01-21 Siderurgie Fse Inst Rech ELECTROROTATIVE CONTINUOUS CASTING LINGOTIER
JPS5342131A (en) * 1976-09-29 1978-04-17 Hitachi Ltd Method of cooling cast piece in continuous casting
DE3048711C2 (en) * 1980-12-23 1991-08-01 Hamburger Stahlwerke Gmbh, 2103 Hamburg Process for cooling strands in the continuous casting of steel billets
JPS57142752A (en) * 1981-02-27 1982-09-03 Kawasaki Steel Corp Slab casting method in vertically bent type continuous casting machine
US4617067A (en) * 1981-08-06 1986-10-14 Vallourec Process for the production of semi-finished articles of hard steels using a continuous casting operation
SE432893B (en) * 1982-09-14 1984-04-30 Asea Ab DEVICE FOR CONTINUOUS CASTING TO MOVE THE NON-LOCKED PARTS OF A CASTING STRING
JPS5987962A (en) * 1982-11-12 1984-05-21 Nippon Steel Corp Continuous casting method
JPS61119360A (en) * 1984-11-16 1986-06-06 Sumitomo Metal Ind Ltd Continuous casting method of steel
JPS62263855A (en) * 1986-05-08 1987-11-16 Kawasaki Steel Corp Method for continuous casting having little center segregation

Also Published As

Publication number Publication date
FR2631263A1 (en) 1989-11-17
PT90543B (en) 1994-05-31
KR890017020A (en) 1989-12-14
DD284175A5 (en) 1990-11-07
AU3392789A (en) 1989-11-16
CS287289A3 (en) 1992-11-18
BR8902241A (en) 1990-01-09
CA1338164C (en) 1996-03-19
EP0342082A1 (en) 1989-11-15
CN1038605A (en) 1990-01-10
AU611797B2 (en) 1991-06-20
DE68907644D1 (en) 1993-08-26
ATE91656T1 (en) 1993-08-15
PT90543A (en) 1989-11-30
US5063991A (en) 1991-11-12
JPH0215856A (en) 1990-01-19
RU1819188C (en) 1993-05-30
CN1018803B (en) 1992-10-28
DE68907644T2 (en) 1993-12-02
PL279425A1 (en) 1989-12-27
FR2631263B1 (en) 1990-07-20
ZA893402B (en) 1990-01-31
UA15737A (en) 1997-06-30
ES2042023T3 (en) 1993-12-01
KR960004423B1 (en) 1996-04-03

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