EP0046721B1 - Nozzle for oxygen-injection lances used in the decarburisation of pig iron, in particular chromium pig iron - Google Patents

Nozzle for oxygen-injection lances used in the decarburisation of pig iron, in particular chromium pig iron Download PDF

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Publication number
EP0046721B1
EP0046721B1 EP81420127A EP81420127A EP0046721B1 EP 0046721 B1 EP0046721 B1 EP 0046721B1 EP 81420127 A EP81420127 A EP 81420127A EP 81420127 A EP81420127 A EP 81420127A EP 0046721 B1 EP0046721 B1 EP 0046721B1
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Prior art keywords
nozzle
oxygen
pig iron
iron
angle
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EP81420127A
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German (de)
French (fr)
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EP0046721A1 (en
Inventor
Jean Brancaz
Georges Marizy
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Ugine Aciers
Ugine Savoie SA
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Ugine Aciers
Ugine Savoie SA
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    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/42Constructional features of converters
    • C21C5/46Details or accessories
    • C21C5/48Bottoms or tuyéres of converters
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28Manufacture of steel in the converter
    • C21C5/42Constructional features of converters
    • C21C5/46Details or accessories
    • C21C5/4606Lances or injectors
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/005Manufacture of stainless steel

Definitions

  • the nozzle which is the subject of the invention relates in the most general way to the decarburization of cast irons by means of lances disposed above the level of the liquid iron, which emit through a nozzle a jet of oxygen in the direction of the surface of this font.
  • the invention relates more particularly to the characteristics of the oxygen jets from injection lances equipped with this new nozzle and the influence of these characteristics on the conditions of interaction between these oxygen jets and the liquid iron.
  • This new nozzle applies in particular, but not limited to, the decarburization of chrome cast irons.
  • the means which is the subject of the invention is a new nozzle for an oxygen injection lance with a supersonic jet, thanks to which it is possible to cause with much greater efficiency the formation of the gas / cast iron emulsion. liquid.
  • This new nozzle according to the invention is characterized by a divergent which comprises, beyond the neck or throttling, a frustoconical part whose angle at the top is between 60 and 70 ° and, preferably, between 62 and 66 °, the angle of 65 ° being close to the optimum under the conditions of the tests.
  • This frustoconical part can be extended by a surface of revolution around the same axis, the generator of which has a concavity turned inwards, so as to reduce the dispersion of the jet.
  • the new nozzle according to the invention makes it possible to implement in a particularly effective manner the process for decarburizing chromium cast irons by a jet of supersonic oxygen which had been developed.
  • This new nozzle also applies in a much more general way to the decarburization of cast irons of all types thanks to a particular efficiency for causing the emulsion of liquid cast iron by means of the gas phase, and, possibly also, the emulsion of liquid dairy.
  • Fig. 1 shows a nozzle of known type for supersonic oxygen jet.
  • Fig. 2 represents the variation of the thrust of the jet as a function of the angle at the top of the diverging point of a frustoconical nozzle.
  • Fig. 3 shows a nozzle for a supersonic oxygen jet according to the invention.
  • Fig. 4 shows the variation of the chromium yield as a function of the angle at the top of the frustoconical diverging portion of the nozzle.
  • Fig. 5 shows the variation of the iron yield as a function of this same angle at the top.
  • Fig. 6 shows a nozzle according to the invention with an improved profile.
  • an oxygen lance comprising a nozzle, the throat or neck of which consisted of a cylindrical tubular zone of approximately 2 mm in diameter and 20 mm in length.
  • the end of this zone bu bu Iaire on the outlet side was not extended by a divergent and the expansion of the oxygen jet was therefore absolutely not limited to the outlet of the constriction.
  • the nozzle was covered with a layer of refractory oxides based on chromium oxide. This layer was deposited mainly during the period of formation and then maintenance of the gas / liquid iron emulsion.
  • composition An analysis of such a layer had given for example as composition:
  • this layer resulted essentially from the oxidation of the components of chromium cast iron, with the intervention of only a few percent of lime coming from the slag initially introduced - alumina and magnesia came from the lining. It was found that this deposit tended to surround the orifice of the nozzle and to form a more or less well-defined funnel around this orifice.
  • Nozzles were then produced, the general shape of which is shown in FIG. 1. These nozzles have an inlet 1 connected to the oxygen supply pipe, then a cylindrical neck 2 of approximately 2 mm in diameter and 20 mm in length and, finally, a frustoconical diverging portion 3 whose angle at the top a1 is approximately 10 ° according to the teaching of the book "BOF Steelmaking" cited above.
  • Fig. 2 gives the results of such tests in the case of a series of eight nozzles with the same characteristics as those of FIG. 1, except the angle of the divergent.
  • Nozzle 1 did not have a divergent
  • nozzles 2, 3, 4, 5, 6, 7 and 8 had divergent frustoconical 4 mm high whose angles at the top were respectively 41, 53, 61, 65, 69, 77 and 100 °.
  • nozzles for the decarburization of cast irons by supersonic oxygen jet comprising a frustoconical diverging whose angle at the top is between 60 and 70 ° and preferably between 62 and 66 °, the angle of 65 ° corresponding, to the accuracy of the measurements, to the minimum thrust, under the conditions of the test.
  • Fig. 3 shows a nozzle according to the invention. It comprises an inlet 4 and a neck 5 whose characteristics are similar to those of the inlet 1 and the neck 2 of FIG. 1.
  • the frustoconical divergent 6 has an apex angle a2 of 65 °. It has been found that it is possible, by means of such a nozzle, to bring about a completely reproducible emulsion of chromium cast irons by means of a jet of supersonic oxygen, according to the process defined by the tests. mentioned above. In addition, this emulsion, once formed, has great stability and is maintained until final decarburization of the cast iron, that is to say until a carbon content close to 0.2%.
  • the six apex angle values thus produced are: 41, 53, 61, 65, 69 and 77 °.
  • Each of these nozzles has a cylindrical neck 2 mm in diameter and 20 mm long and the height of the divergent truncated cone is in all cases 4 mm.
  • a batch of homogeneous pig iron was prepared having the following composition: Cr 17%, C 6%, Si 0.3%, Mn 0.3%, S ⁇ 0.03%, P ⁇ 0.03%.
  • the oxygen reacts mainly on the surface of the iron bath, preferably oxidizing Cr, Si and Fe: as the oxides formed which contain mainly Cr 2 0 3 accumulate at on the surface of the bath, a secondary reaction of reduction of these oxides by carbon begins.
  • the speed of this reduction reaction increases gradually at the same time as the temperature rises to about 1650 ° C around the tenth minute.
  • the CO formed is released during this time and burns, giving flames.
  • the reaction rates are high, which allows decarburization to continue at a rapid rate, until a final carbon content of approximately 0.2% is reached. the twenty-ninth minute. The temperature is then around 1820 ° C. and the oxygen blowing is stopped.
  • Figs. 4 and 5 make it possible to observe the variations in these yields as a function of the angle of the frustoconical diverging portion of the nozzle. It is very clearly seen that these yields go through a maximum for the nozzle which has an angle of 65 °. Although certain factors may slightly modify the optimal angle of the tapered diverging member according to the invention, it is, according to the tests carried out, between 62 and 66 ° in the field of the operating conditions which can be used.
  • Fig. 6 shows a nozzle according to the invention thus improved.
  • the part 10 which extends the frustoconical part 9 has a concavity facing the axis.
  • the tangent to the generatrix of the latter merges with the generatrix of the truncated cone.
  • the tangent to the generatrix of the concave part is almost parallel to the axis of the nozzle.
  • the nozzle according to the invention can be made of various materials. It is often preferred to use copper. It is important to machine the interior surfaces properly and to give them a good surface finish to avoid catching particles of oxide or projected metal. In general, the nozzle is connected to a metal lance cooled by a suitable fluid.
  • oxygen lances equipped with nozzles according to the invention for the decarburization of cast irons in basic converter by methods such as LD or by similar methods.
  • the use of the nozzles according to the invention makes it possible to increase the efficiency and the speed of decarburization and also makes it possible to increase the iron yield.

Abstract

A nozzle is disclosed for use in the decarburization of molten pig iron by means of a jet of oxygen from a lance provided with such nozzle. The nozzle according to the invention is characterized by a divergent portion which, beyond the neck, has a frustoconical part, with an apex angle of between 60 DEG and 70 DEG and preferably between 62 DEG and 66 DEG , and wherein an angle of 65 DEG is preferred. The nozzle according to the invention can be used in particular for the decarburization of chromium containing pig iron and makes it possible to achieve very high chromium and iron yields.

Description

La buse qui fait l'objet de l'invention concerne de la façon la plus générale la décarburation des fontes au moyen de lances disposées au-dessus du niveau de la fonte liquide, qui émettent à travers une buse un jet d'oxygène en direction de la surface de cette fonte. L'invention concerne plus particulièrement les caractéristiques des jets d'oxygène issus de lances d'injection équipées de cette nouvelle buse et l'influence de ces caractéristiques sur les conditions d'interaction entre ces jets d'oxygène et la fonte liquide. Cette nouvelle buse s'applique en particulier, mais de façon non limitative, à la décarburation des fontes au chrome.The nozzle which is the subject of the invention relates in the most general way to the decarburization of cast irons by means of lances disposed above the level of the liquid iron, which emit through a nozzle a jet of oxygen in the direction of the surface of this font. The invention relates more particularly to the characteristics of the oxygen jets from injection lances equipped with this new nozzle and the influence of these characteristics on the conditions of interaction between these oxygen jets and the liquid iron. This new nozzle applies in particular, but not limited to, the decarburization of chrome cast irons.

Un certain nombre d'études ont été faites sur les caractéristiques que doivent présenter les buses montées à l'extrémité des lances d'injection d'oxygène utilisées pour la décarburation des fontes. C'est ainsi que, dans l'ouvrage qui concerne la métallurgie de l'acier au moyen de convertisseurs basiques, intitulé «BOF Steelmaking», qui a été publié en 1976 aux Etats-Unis par l'Iron and Steel Society, on trouve des indications précises au volume 3, chapitre 8, pp. 150 à 153, sur les caractéristiques des buses montées sur les lances à oxygène. Il est précisé, en particulier à la p. 150, lignes 28 à 35, qu'un écoulement supersonique raisonnablement uniforme peut être obtenu au moyen d'une simple partie conique divergente qui fait suite à l'étranglement. La fig. 8-5, p. 151, reproduit unetelle buse pour lance à oxygène. Enfin, p. 153, lignes 7 à 17, des renseignements précis sont donnés sur le demi-angle au sommet qu'il convient d'adopter pour la partie tronconique divergente. On doit éviter des angles trop grands qui renforcent les ondes de choc causant une trop rapide dispersion du jet. Il est proposé de choisir le demi-angle au sommet de la buse d'injection dans l'intervalle compris entre 2,5 et 10°, un demi-angle de 5° étant considéré comme un compromis pratique.A certain number of studies have been made on the characteristics which the nozzles mounted at the end of the oxygen injection lances used for decarburizing the irons must have. Thus, in the work which concerns the metallurgy of steel by means of basic converters, entitled “BOF Steelmaking”, which was published in 1976 in the United States by the Iron and Steel Society, precise indications in volume 3, chapter 8, pp. 150 to 153, on the characteristics of the nozzles mounted on the oxygen lances. It is stated, in particular at p. 150, lines 28 to 35, that a reasonably uniform supersonic flow can be obtained by means of a simple divergent conical part which follows the constriction. Fig. 8-5, p. 151, shows such a nozzle for an oxygen lance. Finally, p. 153, lines 7 to 17, precise information is given on the half-angle at the top which should be adopted for the divergent tapered part. Avoid too large angles which reinforce the shock waves causing the jet to disperse too quickly. It is proposed to choose the half angle at the top of the injection nozzle in the range between 2.5 and 10 °, a half angle of 5 ° being considered as a practical compromise.

L'expérience a montré que les buses ainsi réalisées donnent des résultats relativement satisfaisants dans le cas général de la décarburation des fontes ordinaires mais, par contre, des difficultés ont été rencontrées dans le cas du traitement des fontes au chrome.Experience has shown that the nozzles thus produced give relatively satisfactory results in the general case of decarburization of ordinary cast irons, but, on the other hand, difficulties have been encountered in the treatment of cast irons with chromium.

On a d'abord étudié un procédé de décarburation des fontes au chrome ou au chrome nickel contenant en pour-cent en poids 1,5 à 8 de C, 10 à 30 de Cr et jusqu'à 30 de Ni, qui comporte, au moins dans la phase finale de la décarburation, la formation d'une émulsion gaz/fonte liquide au sein de laquelle le carbone est oxydé directement par l'oxygène.We first studied a decarburization process for chromium or chromium nickel cast iron containing in weight percent 1.5 to 8 of C, 10 to 30 of Cr and up to 30 of Ni, which comprises, at less in the final phase of decarburization, the formation of a gas / liquid iron emulsion in which the carbon is oxidized directly by oxygen.

Les conditions nécessaires à la réalisation de cette émulsion sont critiques. En effet, il est connu que la réalisation d'émulsions entre une fonte liquide, un laitier et une phase gazeuse est relativement facile. C'est le cas de la décarburation des fontes par le procédé LD. Ce sont alors les caractéristiques de viscosité du laitier qui jouent le rôle le plus important, comme cela est montré dans l'article de A. Chatterjee, N.O. Lindfor et J.A. Wes- ter: «Process metallurgy of LD Steelmaking» («Ironmaking and steelmaking 1976», No 1). Par contre, pour qu'une émulsion entre une phase gazeuse et le métal liquide puisse se former et se maintenir de façon stable, même en l'absence quasi totale de laitier, jusqu'à ce que la teneur en carbone soit abaissée jusqu'à un niveau final proche de 0,2%, des conditions bien définies de température de la fonte liquide, de teneur en carbone, de distance lance-bain, de débit et de pression d'oxygène doivent être réalisées.The conditions necessary for the production of this emulsion are critical. Indeed, it is known that the production of emulsions between a liquid pig iron, a slag and a gas phase is relatively easy. This is the case with the decarburization of cast irons by the LD process. It is then the viscosity characteristics of the slag which play the most important role, as shown in the article by A. Chatterjee, NO Lindfor and JA Wester: “Process metallurgy of LD Steelmaking” (“Ironmaking and steelmaking” 1976 ", No. 1). On the other hand, so that an emulsion between a gaseous phase and the liquid metal can form and be maintained in a stable manner, even in the almost total absence of slag, until the carbon content is lowered to a final level close to 0.2%, well-defined conditions of liquid iron temperature, carbon content, distance to the bath, flow rate and oxygen pressure must be achieved.

Les essais ont montré que, lorsque les conditions favorables sont réunies et que l'émulsion entre phase gazeuse et fonte liquide se forme et se maintient de façon satisfaisante, on obtient à la fois une décarburation rapide et poussée et, en même temps, un rendement en chrome métal particulièrement élevé. On a ainsi effectué des essais sur des quantités unitaires de fonte au chrome d'environ 60 kg. La buse utilisée avait un diamètre au col de 2 mm, et un débit de 168 NI/min d'oxygène.The tests have shown that, when the favorable conditions are met and the emulsion between the gas phase and the liquid iron is formed and is maintained satisfactorily, both rapid and extensive decarburization are obtained and, at the same time, a yield in particularly high chrome metal. Tests were thus carried out on unit quantities of chromium cast iron of approximately 60 kg. The nozzle used had a neck diameter of 2 mm, and a flow rate of 168 NI / min of oxygen.

Les études poursuivies et les nombreux essais effectués pour le développement de ce procédé de décarburation des fontes au chrome ont montré qu'il ne suffisait pas d'ajuster convenablement les paramètres opératoires qui avaient été identifiés pour obtenir de façon reproductible l'établissement d'une émulsion stable. Dans bien des cas, des retards à la formation de l'émulsion et une certaine instabilité de celle-ci étaient observés; ces retards et/ou cette instabilité entraînaient une chute des rendements en chrome et en fer. Dans quelques cas même, l'émulsion ne se formait pas du tout.The studies carried out and the numerous tests carried out for the development of this decarburization process for chromium cast irons have shown that it was not enough to adequately adjust the operating parameters which had been identified in order to obtain a reproducible establishment of a stable emulsion. In many cases, delays in the formation of the emulsion and a certain instability thereof were observed; these delays and / or this instability led to a fall in the yields of chromium and iron. In some cases even, the emulsion did not form at all.

On a donc recherché le moyen d'améliorer la reproductibilité du déclenchement de l'émulsion gaz/fonte liquide et aussi d'accroître la stabilité de cette émulsion une fois formée.We therefore sought a means of improving the reproducibility of the triggering of the gas / liquid iron emulsion and also of increasing the stability of this emulsion once formed.

Le moyen qui fait l'objet de l'invention est une nouvelle buse pour lance d'injection d'oxygène à jet supersonique, grâce à laquelle il est possible de provoquer avec une beaucoup plus grande efficacité la formation de l'émulsion gaz/fonte liquide.The means which is the subject of the invention is a new nozzle for an oxygen injection lance with a supersonic jet, thanks to which it is possible to cause with much greater efficiency the formation of the gas / cast iron emulsion. liquid.

Cette nouvelle buse suivant l'invention se caractérise par un divergent qui comporte, au-delà du col ou étranglement, une partie tronconique dont l'angle au sommet est compris entre 60 et 70° et, de préférence, entre 62 et 66°, l'angle de 65° étant proche de l'optimum dans les conditions des essais. Cette partie tronconique peut être prolongée par une surface de révolution autour du même axe dont la génératrice présente une concavité tournée vers l'intérieur, de façon à diminuer la dispersion du jet.This new nozzle according to the invention is characterized by a divergent which comprises, beyond the neck or throttling, a frustoconical part whose angle at the top is between 60 and 70 ° and, preferably, between 62 and 66 °, the angle of 65 ° being close to the optimum under the conditions of the tests. This frustoconical part can be extended by a surface of revolution around the same axis, the generator of which has a concavity turned inwards, so as to reduce the dispersion of the jet.

La nouvelle buse suivant l'invention permet de mettre en oeuvre de façon particulièrement efficace le procédé de décarburation des fontes au chrome par jet d'oxygène supersonique qui avait été développé.The new nozzle according to the invention makes it possible to implement in a particularly effective manner the process for decarburizing chromium cast irons by a jet of supersonic oxygen which had been developed.

Cette nouvelle buse s'applique aussi de façon beaucoup plus générale à la décarburation des fontes de tous types grâce à une efficacité particulière pour provoquer l'émulsion de la fonte liquide au moyen de la phase gazeuse, et, éventuellement aussi, l'émulsion du laitier liquide.This new nozzle also applies in a much more general way to the decarburization of cast irons of all types thanks to a particular efficiency for causing the emulsion of liquid cast iron by means of the gas phase, and, possibly also, the emulsion of liquid dairy.

L'exemple et les figures ci-après permettent de mieux comprendre les caractéritiques de la buse qui fait l'objet de l'invention ainsi que son application à la décarburation des fontes au chrome.The example and the figures below make it possible to better understand the characteristics of the nozzle which is the subject of the invention as well as its application to the decarburization of chromium cast irons.

La fig. 1 représente une buse de type connu pour jet d'oxygène supersonique.Fig. 1 shows a nozzle of known type for supersonic oxygen jet.

La fig. 2 représente la variation de la poussée du jet en fonction de l'angle au sommet du divergent d'une buse tronconique.Fig. 2 represents the variation of the thrust of the jet as a function of the angle at the top of the diverging point of a frustoconical nozzle.

La fig. 3 représente une buse pour jet d'oxygène supersonique suivant l'invention.Fig. 3 shows a nozzle for a supersonic oxygen jet according to the invention.

La fig. 4 représente la variation du rendement en chrome en fonction de l'angle au sommet du divergent tronconique de la buse.Fig. 4 shows the variation of the chromium yield as a function of the angle at the top of the frustoconical diverging portion of the nozzle.

La fig. 5 représente la variation du rendement en fer en fonction de ce même angle au sommet. La fig. 6 représente une buse suivant l'invention à profil amélioré.Fig. 5 shows the variation of the iron yield as a function of this same angle at the top. Fig. 6 shows a nozzle according to the invention with an improved profile.

Dans les premiers essais de décarburation des fontes au chrome effectués, on utilisait une lance à oxygène comportant une buse dont l'étranglement ou col était constitué par une zone tubulaire cylindrique d'environ 2 mm de diamètre et 20 mm de long. L'extrémité de cette zone tu bu Iaire du côté sortie n'était pas prolongée par un divergent et l'expansion du jet d'oxygène n'était donc absolument pas limitée à la sortie de l'étranglement. L'expérience avait montré que, dans ces conditions, la buse se recouvrait d'une couche d'oxydes réfractaires à base d'oxyde de chrome. Cette couche se déposait principalement pendant la période de formation puis de maintien de l'émulsion gaz/fonte liquide.In the first decarburization tests on chrome cast irons carried out, an oxygen lance was used comprising a nozzle, the throat or neck of which consisted of a cylindrical tubular zone of approximately 2 mm in diameter and 20 mm in length. The end of this zone bu bu Iaire on the outlet side was not extended by a divergent and the expansion of the oxygen jet was therefore absolutely not limited to the outlet of the constriction. Experience had shown that, under these conditions, the nozzle was covered with a layer of refractory oxides based on chromium oxide. This layer was deposited mainly during the period of formation and then maintenance of the gas / liquid iron emulsion.

Une analyse d'une telle couche avait donné par exemple comme composition:

Figure imgb0001
An analysis of such a layer had given for example as composition:
Figure imgb0001

On voit d'après cet exemple que cette couche résultait essentiellement de l'oxydation des composants de la fonte au chrome, avec intervention de seulement quelques pour-cent de chaux provenant du laitier initialement introduit - alumine et magnésie venaient du garnissage. On avait constaté que ce dépôt tendait à entourer l'orifice de la buse et à former un entonnoir plus ou moins bien défini autour de cet orifice.We see from this example that this layer resulted essentially from the oxidation of the components of chromium cast iron, with the intervention of only a few percent of lime coming from the slag initially introduced - alumina and magnesia came from the lining. It was found that this deposit tended to surround the orifice of the nozzle and to form a more or less well-defined funnel around this orifice.

On a eu l'idée de réaliser une buse présentant un divergent, à la fois pour essayer d'améliorer l'efficacité du jet et pour éviter les risques de perturbation de ce jet par des dépôts d'oxydes réfractaires projetés à partir de la fonte liquide. On a alors réalisé des buses dont la forme générale est représentée fig. 1. Ces buses comportent une entrée 1 raccordée à la canalisation d'arrivée d'oxygène, puis un col cylindrique 2 d'environ 2 mm de diamètre et 20 mm de long et, enfin, un divergent tronconique 3 dont l'angle au sommet a1 est d'environ 10° suivant l'enseignement de l'ouvrage «BOF Steelmaking» cité plus haut.We had the idea of making a nozzle with a divergent, both to try to improve the efficiency of the jet and to avoid the risks of disturbance of this jet by refractory oxide deposits projected from the cast iron liquid. Nozzles were then produced, the general shape of which is shown in FIG. 1. These nozzles have an inlet 1 connected to the oxygen supply pipe, then a cylindrical neck 2 of approximately 2 mm in diameter and 20 mm in length and, finally, a frustoconical diverging portion 3 whose angle at the top a1 is approximately 10 ° according to the teaching of the book "BOF Steelmaking" cited above.

Les résultats d'essais de ces buses ont été négatifs. On constatait, effectivement, qu'il ne se formait pas de projections d'oxydes à l'intérieur du divergent mais on n'arrivait pas à former l'émulsion gaz/fonte liquide de façon reproductible et stable.The test results for these nozzles have been negative. It was found, in fact, that there were no projections of oxides inside the divergent but it was not possible to form the gas / liquid iron emulsion in a reproducible and stable manner.

On a alors entrepris des essais afin de préciser en particulier l'influence de l'angle au sommet du divergent tronconique sur la poussée du jet à débit constant. La fig. 2 donne des résultats de tels essais dans le cas d'une série de huit buses de mêmes caractéristiques que celles de la fig. 1, excepté l'angle du divergent. La buse No 1 ne comportait pas de divergent, les buses 2, 3, 4, 5, 6, 7 et 8 comportaient des divergents tronconiques de 4 mm de hauteur dont les angles au sommet étaient respectivement de 41, 53, 61, 65, 69, 77 et 100°.Tests were then undertaken in order to specify in particular the influence of the angle at the apex of the frustoconical divergence on the thrust of the jet at constant flow. Fig. 2 gives the results of such tests in the case of a series of eight nozzles with the same characteristics as those of FIG. 1, except the angle of the divergent. Nozzle 1 did not have a divergent, nozzles 2, 3, 4, 5, 6, 7 and 8 had divergent frustoconical 4 mm high whose angles at the top were respectively 41, 53, 61, 65, 69, 77 and 100 °.

Trois séries d'essais ont été faites pour trois niveaux de débits différents en oxygène: 172,181 et 193 NI/min. On mesurait pour chaque essai la poussée en N exercée par le jet sur le plateau d'une balance disposé à une distance d'environ 3 cm de l'orifice.Three series of tests were carried out for three different levels of oxygen flow: 172.181 and 193 NI / min. For each test, the N-shaped thrust exerted by the jet on the platform of a balance disposed at a distance of about 3 cm from the orifice was measured.

Les courbes 1, 2 et 3 tracées respectivement pour les débits de 193, 181 et 172 NI/min montrent chaque fois l'existence d'un même point singulier dans le cas du divergent de 65°.The curves 1, 2 and 3 plotted respectively for the flows of 193, 181 and 172 NI / min each time show the existence of the same singular point in the case of the divergence of 65 °.

Bien que ce point singulier corresponde à une poussée minimale, on a eu l'idée de réaliser suivant l'invention des buses pour la décarburation des fontes par jet d'oxygène supersonique, comportant un divergent tronconique dont l'angle au sommet est compris entre 60 et 70° et, de préférence, compris entre 62 et 66°, l'angle de 65° correspondant, à la précision des mesures près, à la poussée minimale, dans les conditions de l'essai.Although this singular point corresponds to a minimum thrust, we had the idea of realizing according to the invention nozzles for the decarburization of cast irons by supersonic oxygen jet, comprising a frustoconical diverging whose angle at the top is between 60 and 70 ° and preferably between 62 and 66 °, the angle of 65 ° corresponding, to the accuracy of the measurements, to the minimum thrust, under the conditions of the test.

La fig. 3 représente une buse suivant l'invention. Elle comporte une entrée 4 et un col 5 dont les caractéristiques sont semblables à celles de l'entrée 1 et du col 2 de la fig. 1. Par contre, le divergent tronconique 6 présente un angle au sommet a2 de 65°. On a constaté qu'il est possible, au moyen d'une telle buse, de provoquer de façon tout à fait reproductible l'émulsion des fontes au chrome au moyen d'un jet d'oxygène supersonique, suivant le procédé défini par les essais mentionnés plus haut. De plus, cette émulsion, une fois formée, présente une grande stabilité et se maintient jusqu'à décarburation finale de la fonte, c'est-à-dire jusqu'à une teneur en carbone voisine de 0,2%. Il est possible, sans qu'on puisse l'affirmer, que l'efficacité particulière des divergents à angle de 60 à 70° et, de préférence compris entre 62 et 66°, soit due à la turbulence particulièrement importante provoquée dans l'écoulement de l'oxygène par cette forme de divergent.Fig. 3 shows a nozzle according to the invention. It comprises an inlet 4 and a neck 5 whose characteristics are similar to those of the inlet 1 and the neck 2 of FIG. 1. On the other hand, the frustoconical divergent 6 has an apex angle a2 of 65 °. It has been found that it is possible, by means of such a nozzle, to bring about a completely reproducible emulsion of chromium cast irons by means of a jet of supersonic oxygen, according to the process defined by the tests. mentioned above. In addition, this emulsion, once formed, has great stability and is maintained until final decarburization of the cast iron, that is to say until a carbon content close to 0.2%. It is possible, without being able to affirm it, that the particular efficiency of the diverging at an angle of 60 to 70 ° and, preferably between 62 and 66 °, is due to the particularly important turbulence caused in the flow oxygen through this form of divergence.

On a alors étudié l'influence de l'angle au sommet du divergent sur les rendements moyens en Cr et en Fe de l'opération de décarburation. Les essais avaient en effet montré que, généralement, une grande stabilité de formation et de maintien de l'émulsion gaz/fonte liquide s'accompagnait de rendements très élevés en Fe et Cr. Ces rendements sont calculés en pour-cent en poids en rapportant les quantités de Fe et Cr contenues dans l'acier obtenu après décarburation à celles contenues initialement dans la fonte.We then studied the influence of the angle at the top of the divergent on the average yields of Cr and Fe of the decarburization operation. The tests had in fact shown that, generally, great stability in the formation and maintenance of the gas / liquid iron emulsion was accompanied by very high yields of Fe and Cr. These yields are calculated in percent by weight by reporting the amounts of Fe and Cr contained in the steel obtained after decarburization to those initially contained in the cast iron.

L'exemple ci-après donne les résultats d'une série d'essais de décarburation de fonte effectués de façon identique en faisant varier seulement les angles de divergent des buses.The example below gives the results of a series of decarburization tests of cast iron carried out in an identical manner by varying only the angles of divergence of the nozzles.

On a préparé une série de six buses du même type que celle de la fig. 3, mais ayant chacune un divergent tronconique d'angle au sommet différent. Les six valeurs d'angle au sommet ainsi réalisées sont: 41, 53, 61, 65, 69 et 77°. Chacune de ces buses comporte un col cylindrique de 2 mm de diamètre et 20 mm de long et la hauteur du tronc de cône du divergent est dans tous les cas de 4 mm. Au moyen de chacune de ces buses, on a effectué de trois à neuf coulées de fonte au chrome suivant un mode opératoire unique similaire à celui déjà décrit.A series of six nozzles of the same type as that of FIG. 3, but each having a tapered diverging angle with a different apex. The six apex angle values thus produced are: 41, 53, 61, 65, 69 and 77 °. Each of these nozzles has a cylindrical neck 2 mm in diameter and 20 mm long and the height of the divergent truncated cone is in all cases 4 mm. By means of each of these nozzles, three to nine castings of chromium cast iron were carried out according to a single procedure similar to that already described.

On a élaboré un lot de fonte homogène ayant la composition suivante: Cr 17%, C 6%, Si 0,3%, Mn 0,3%, S < 0,03%, P < 0,03%.A batch of homogeneous pig iron was prepared having the following composition: Cr 17%, C 6%, Si 0.3%, Mn 0.3%, S <0.03%, P <0.03%.

Pour chaque essai, on porte à 1380° C une quantité de 60 kg de cette fonte dans un four comportant un chauffage par induction, la surface de la fonte liquide étant recouverte de 340 g de chaux. On injecte alors de l'oxygène au moyen d'une lance verticale avec un débit d'environ 180 NI/min. On utilise une des six buses qui viennent d'être décrites et la distance verticale entre l'extrémité de la buse et le bain est de 26 mm. L'oxygène ainsi éjecté entre en réaction avec le bain et on peut observer trois phases successives. Dans une première phase, l'oxygène réagit principalement à la surface du bain de fonte en oxydant de préférence Cr, Si et Fe: au fur et à mesure que les oxydes formés qui contiennent en majeure partie du Cr203 s'accumulent à la surface du bain, une réaction secondaire de réduction de ces oxydes par le carbone s'amorce. La vitesse de cette réaction de réduction s'accroît peu à peu en même temps que la température s'élève jusqu'à environ 1650°C vers la dixième minute. Le CO formé se dégage pendant ce temps et brûle en donnant des flammes.For each test, a quantity of 60 kg of this cast iron is brought to 1380 ° C. in an oven comprising induction heating, the surface of the liquid cast iron being covered with 340 g of lime. Oxygen is then injected by means of a vertical lance with a flow rate of approximately 180 NI / min. One of the six nozzles just described is used and the vertical distance between the end of the nozzle and the bath is 26 mm. The oxygen thus ejected reacts with the bath and one can observe three successive phases. In a first phase, the oxygen reacts mainly on the surface of the iron bath, preferably oxidizing Cr, Si and Fe: as the oxides formed which contain mainly Cr 2 0 3 accumulate at on the surface of the bath, a secondary reaction of reduction of these oxides by carbon begins. The speed of this reduction reaction increases gradually at the same time as the temperature rises to about 1650 ° C around the tenth minute. The CO formed is released during this time and burns, giving flames.

Dans une deuxième phase, à partir de la onzième minute, la réduction des oxydes, principalement de l'oxyde de chrome, par le carbone devient plus rapide que la formation de ces oxydes. Dans cette période de vive réaction, la température s'élève encore, de façon cependant moins rapide. A partir de la quinzième minute environ, la vitesse de décarburation se stabilise, la teneur en carbone, qui est alors d'environ 4%, continue à décroître au rythme d'à peu près 0,3% par minute et, en même temps, on observe une réduction correspondante de l'oxyde de chrome. Ce mécanisme se poursuit jusque vers la vingtième minute: la température du bain atteint alors environ 1750°C, tandis que la teneur en C s'est abaissée à environ 2,9%. A la fin de cette deuxième phase, les oxydes métalliques formés initialement sont presque complètement réduits.In a second phase, from the eleventh minute, the reduction of oxides, mainly chromium oxide, by carbon becomes faster than the formation of these oxides. In this period of strong reaction, the temperature rises again, however less quickly. From about the fifteenth minute, the decarburization speed stabilizes, the carbon content, which is then about 4%, continues to decrease at a rate of about 0.3% per minute and, at the same time , a corresponding reduction in chromium oxide is observed. This mechanism continues until about the twentieth minute: the temperature of the bath then reaches approximately 1750 ° C., while the C content has dropped to approximately 2.9%. At the end of this second phase, the metal oxides formed initially are almost completely reduced.

Vers la vingtième minute, les conditions sont réunies pour le démarrage d'une troisième phase, qui permettra d'abaisser la teneur en carbone jusque vers 0,2%. Au début de cette troisième phase, la température du bain de fonte est très élevée. Dans ces conditions, en maintenant inchangées les conditions de débit d'oxygène et de distance entre l'extrémité de la buse et le bain de fonte, on observe la formation, à partir du bain de fonte lui-même, d'une émulsion entre gaz et fonte qui recouvre rapidement la surface du bain puis se développe en épaisseur jusqu'à doubler le volume initial de la fonte. Tout se passe comme si la fonte elle-même, sous l'action du jet d'oxygène et de la formation de CO, par réaction directe de l'oxygène avec le carbone contenu dans cette fonte, entrait en ébullition dans toute sa masse, grâce aux conditions physico-chimiques réalisées. Au sein de l'émulsion ainsi formée, les vitesses de réaction sont élevées, ce qui permet la poursuite de la décarburation, à un rythme rapide, jusqu'à une teneur finale en carbone d'environ 0,2% qui est atteinte.à la vingt-neuvième minute. La température est alors d'environ 1820° C et on arrête le soufflage d'oxygène.Around the twentieth minute, the conditions are met for the start of a third phase, which will make it possible to lower the carbon content up to around 0.2%. At the start of this third phase, the temperature of the molten bath is very high. Under these conditions, while maintaining the conditions of oxygen flow and distance between the end of the nozzle and the melt bath unchanged, the formation, from the melt bath itself, of an emulsion between gas and cast iron which quickly covers the surface of the bath then develops in thickness until doubling the initial volume of the cast iron. Everything happens as if the iron itself, under the action of the jet of oxygen and the formation of CO, by direct reaction of the oxygen with the carbon contained in this iron, boiled in all its mass, thanks to the physico-chemical conditions achieved. Within the emulsion thus formed, the reaction rates are high, which allows decarburization to continue at a rapid rate, until a final carbon content of approximately 0.2% is reached. the twenty-ninth minute. The temperature is then around 1820 ° C. and the oxygen blowing is stopped.

La pesée de l'acier obtenu après solidification et l'analyse de sa teneur en fer et en chrome permettent de déterminer les rendements en Fe et Cr correspondants.The weighing of the steel obtained after solidification and the analysis of its iron and chromium content make it possible to determine the yields of corresponding Fe and Cr.

Les fig. 4 et 5 permettent d'observer les variations de ces rendements en fonction de l'angle du divergent tronconique de la buse. On voit très clairement que ces rendements passent par un maximum pour la buse qui présente un angle de 65°. Bien que certains facteurs puissent modifier légèrement l'angle optimal du divergent tronconique suivant l'invention, celui-ci est, d'après les essais effectués, compris entre 62 et 66° dans le domaine des conditions opératoires utilisables.Figs. 4 and 5 make it possible to observe the variations in these yields as a function of the angle of the frustoconical diverging portion of the nozzle. It is very clearly seen that these yields go through a maximum for the nozzle which has an angle of 65 °. Although certain factors may slightly modify the optimal angle of the tapered diverging member according to the invention, it is, according to the tests carried out, between 62 and 66 ° in the field of the operating conditions which can be used.

Avec une buse de 65° d'angle au sommet, les dépôts sur la paroi interne de la buse, dus à des projections d'oxydes réfractaires à partir du métal liquide, sont faibles.With a nozzle with a 65 ° angle at the top, the deposits on the internal wall of the nozzle, due to projections of refractory oxides from the liquid metal, are low.

Des essais complémentaires ont montré qu'on peut encore réduire ces dépôts et réduire aussi la dispersion du jet en prolongeant la partie tronconique du divergent par une surface de révolution autour du même axe, dont la génératrice présente une concavité orientée vers l'intérieur. Il convient, de préférence, que la tangente à la courbe génératrice de cette partie de la buse soit confondue à l'origine avec la génératrice du cône. A l'extrémité de la génératrice, la tangente peut devenir parallèle à l'axe ou proche du parallélisme.Additional tests have shown that these deposits can be further reduced and also reduce the dispersion of the jet by extending the frustoconical part of the divergent by a surface of revolution around the same axis, the generator of which has a concavity oriented inward. It is preferable that the tangent to the generating curve of this part of the nozzle is originally confused with the generator of the cone. At the end of the generator, the tangent can become parallel to the axis or close to parallelism.

La fig. 6 présente une buse suivant l'invention ainsi perfectionnée. On voit l'entrée 7, le col cylindrique 8 et le divergent tronconique 9 d'angle au sommet a2 qui sont semblables aux parties correspondantes de la buse suivant l'invention de la fig. 3. La partie 10 qui prolonge la partie tronconique 9 comporte une concavité tournée vers l'axe. Au point 11 de raccordement entre le tronc de cône et la partie 10, la tangente à la génératrice de celle-ci se confond avec la génératrice du tronc de cône. Au point 12 à l'extrémité de la buse, la tangente à la génératrice de la partie concave est presque parallèle à l'axe de la buse. Une telle buse perfectionnée suivant l'invention présente l'avantage non négligeable, grâce à la forme de son extrémité de sortie, d'éliminer les risques de pénétration de projections d'oxydes ou même de métal à partir du bain de métal fondu.Fig. 6 shows a nozzle according to the invention thus improved. We see the inlet 7, the cylindrical neck 8 and the frustoconical divergent angle 9 at the apex a2 which are similar to the corresponding parts of the nozzle according to the invention of FIG. 3. The part 10 which extends the frustoconical part 9 has a concavity facing the axis. At point 11 of connection between the truncated cone and the part 10, the tangent to the generatrix of the latter merges with the generatrix of the truncated cone. At point 12 at the end of the nozzle, the tangent to the generatrix of the concave part is almost parallel to the axis of the nozzle. Such an improved nozzle according to the invention has the non-negligible advantage, thanks to the shape of its outlet end, of eliminating the risks of penetration of oxide or even metal projections from the bath of molten metal.

La buse suivant l'invention peut être réalisée en divers matériaux. On préfère souvent utiliser le cuivre. Il est important d'usiner convenablement les surfaces intérieures et de leur donner un bon état de surface pour éviter l'accrochage de particules d'oxydes ou de métal projetées. En général, on raccorde la buse à une lance métallique refroidie par un fluide convenable.The nozzle according to the invention can be made of various materials. It is often preferred to use copper. It is important to machine the interior surfaces properly and to give them a good surface finish to avoid catching particles of oxide or projected metal. In general, the nozzle is connected to a metal lance cooled by a suitable fluid.

Bien que les exemples qui viennent d'être donnés portent sur des essais effectués sur de petites quantités, on a vérifié que les résultats obtenus sont extrapolables à l'échelle industrielle. C'est ainsi que les angles au sommet des divergents tronconiques suivant l'invention conduisent aussi à des résultats optimaux dans le cas des buses de forte section utilisées pour le traitement des fontes en quantités industrielles.Although the examples which have just been given relate to tests carried out on small quantities, it has been verified that the results obtained can be extrapolated on an industrial scale. Thus, the angles at the apex of the frustoconical divergences according to the invention also lead to optimal results in the case of large section nozzles used for the treatment of cast irons in industrial quantities.

De plus, bien que la buse qui fait l'objet de l'invention ait été expérimentée principalement dans le cas de la décarburation des fontes au chrome, des essais ont montré qu'elle pouvait être utilisée aussi avantageusement pour la décarburation de tous types de fontes.In addition, although the nozzle which is the subject of the invention has been tested mainly in the case of decarburization of chromium cast irons, tests have shown that it could also be used advantageously for the decarburization of all types of fonts.

C'est ainsi que, de la façon la plus générale, on peut utiliser des lances à oxygène équipées de buses suivant l'invention pour la décarburation des fontes en convertisseur basique par des procédés tels que le LD ou par des procédés analogues.Thus, in the most general manner, it is possible to use oxygen lances equipped with nozzles according to the invention for the decarburization of cast irons in basic converter by methods such as LD or by similar methods.

Dans ces différents cas, l'utilisation des buses suivant l'invention permet d'accroître l'efficacité et la rapidité de la décarburation et permet aussi d'augmenter le rendement en fer.In these different cases, the use of the nozzles according to the invention makes it possible to increase the efficiency and the speed of decarburization and also makes it possible to increase the iron yield.

Claims (4)

1. A nozzle for the decarburisation of cast irons by a supersonic oxygen jet comprising an inlet (4 or 7), a cylindrical neck portion (5 or 8) and a divergent portion having a frustoconical part (6 or 9) which is connected to the cylindrical neck portion, characterised in that the frustoconical part (6 or 9) of the divergent portion has an angle at the apex (a2) of between 60 and 70°.
2. A nozzle according to claim 1, characterised in that the frustoconical part (6 or 9) of the divergent portion has an angle at the apex (a2) of between 62 and 66° and preferably close to 65°.
3. A nozzle according to claim 1 or 2, characterised in that the divergent portion thereof comprises, extending the frustoconical part (9), a portion having a surface of revolution (10) about the same axis, the generating curve of which has an inwardly directed concavity.
4. Use of the nozzle according to one of claims 1 to 3 for the decarburisation of chromium cast irons.
EP81420127A 1980-08-26 1981-08-25 Nozzle for oxygen-injection lances used in the decarburisation of pig iron, in particular chromium pig iron Expired EP0046721B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81420127T ATE8413T1 (en) 1980-08-26 1981-08-25 INJECTION NOZZLE FOR OXYGEN LANCES FOR DECARBONING PIG IRON, ESPECIALLY PIG IRON CONTAINING CHROMIUM.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8018846 1980-08-26
FR8018846A FR2489368A1 (en) 1980-08-26 1980-08-26 NEW NOZZLE FOR OXYGEN INJECTION LAUNCHER FOR DECARBURATION OF FONTES AND APPLICATION TO DECARBURATION OF CHROMIUM WAFERS

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EP0046721A1 EP0046721A1 (en) 1982-03-03
EP0046721B1 true EP0046721B1 (en) 1984-07-11

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US (1) US4455166A (en)
EP (1) EP0046721B1 (en)
JP (1) JPS5952202B2 (en)
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AU (1) AU7449181A (en)
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CA (1) CA1177642A (en)
DE (1) DE3164731D1 (en)
ES (1) ES268630Y (en)
FI (1) FI66432C (en)
FR (1) FR2489368A1 (en)
IN (1) IN154747B (en)
NO (1) NO812881L (en)
SU (1) SU1199203A3 (en)
TR (1) TR21290A (en)
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USH1624H (en) * 1993-06-02 1997-01-07 The United States Of America As Represented By The Secretary Of The Navy Stabilizer for submerged gaseous jets in liquids
US5782414A (en) * 1995-06-26 1998-07-21 Nathenson; Richard D. Contoured supersonic nozzle
US5647201A (en) * 1995-08-02 1997-07-15 Trw Inc. Cavitating venturi for low reynolds number flows
AT408348B (en) * 1999-12-20 2001-10-25 Voest Alpine Ind Anlagen METHOD AND DEVICE FOR SUPPLYING A GAS IN A METALLURGICAL VESSEL
US7182279B2 (en) * 2004-10-28 2007-02-27 National Cheng Kung University Atomizer for atomizing molten metal
ITMI20050241A1 (en) * 2005-02-18 2006-08-19 Techint Spa MULTIFUNCTIONAL INJECTOR AND ITS COMBUSTION PROCEDURE FOR METALLURGICAL TREATMENT IN AN ELECTRIC ARC FURNACE

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US2175160A (en) * 1935-07-02 1939-10-03 Linde Air Prod Co Nozzle for cutting blowpipes
GB800833A (en) * 1956-05-29 1958-09-03 British Oxygen Co Ltd Nozzles
FR1476043A (en) * 1966-03-30 1967-04-07 Oxygen injection lance with tubes protruding outside
US3559974A (en) * 1969-03-03 1971-02-02 Berry Metal Co Oxygen lances having a high resistance to deterioration and multipiece nozzle heads therefor
US3876190A (en) * 1969-06-25 1975-04-08 Commw Ind Gases Method and apparatus for feeding particulate materials to furnaces and the like
IT997285B (en) * 1973-08-08 1975-12-30 Italsider Spa IMPROVEMENTS TO THE NOZZLES FOR THE LANCE HEADS FOR BLOWING OXYGEN FROM ABOVE IN THE REFINING PROCESSES
FR2474531B1 (en) * 1980-01-24 1986-08-14 Ugine Gueugnon Sa PROCESS FOR DECARBURIZING CHROME FOUNDS FOR THE PREPARATION OF STAINLESS STEELS BY JET OF SUPERSONIC OXYGEN

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ZA815877B (en) 1982-08-25
DE3164731D1 (en) 1984-08-16
KR830006442A (en) 1983-09-24
SU1199203A3 (en) 1985-12-15
ATE8413T1 (en) 1984-07-15
JPS5773113A (en) 1982-05-07
ES268630U (en) 1983-05-16
YU205781A (en) 1984-02-29
FR2489368A1 (en) 1982-03-05
EP0046721A1 (en) 1982-03-03
FI66432C (en) 1984-10-10
JPS5952202B2 (en) 1984-12-18
ZW20581A1 (en) 1981-12-09
AU7449181A (en) 1982-03-04
US4455166A (en) 1984-06-19
NO812881L (en) 1982-03-01
CA1177642A (en) 1984-11-13
ES268630Y (en) 1983-12-01
FI812612L (en) 1982-02-27
TR21290A (en) 1984-02-28
IN154747B (en) 1984-12-15
FI66432B (en) 1984-06-29
BR8105366A (en) 1982-05-11

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