TREATMENT OF MELTS IN A LADLE AND APPARATUS FOR SUCH TREATMENT

Abstract: A ladle arrangement intended for use when treating a metal melt, in which gas or gas/powder mixture is delivered to the melt (2) which substantially fills the ladle (1), and departing gases are extracted by suction through a hood mounted above the ladle. The inventive ladle arrangement is effective to permit the gas or gas/powder mixture to be delivered to the melt in a large volumetric flow, wherewith the melt will bubble and splash vigorously. For the purpose of restricting the effects of these melt splashes to a defined space above the melt (2), the gas extraction hood has the form of a lid (7) which is intended to substantially seal against the upper edge of the ladle (1). The lid is configured so that the volume (6) defined by the lid above the melt will correspond to a substantial part, preferably at least half, of the volume of the melt (2) in the ladle (1). The side surfaces of the lid (7) define splash-droplet pathways operative to return the droplets to the melt in the ladle. The invention also relates to a method of treating a metal melt in a ladle.

Description: Treatment of Melts in a Ladle and Apparatus for Such Treatment The present invention relates to a method of treating a metal melt in a ladle, in which a gas or gas/powder mixture is introduced to the melt in a substantially completely filled ladle and departing gas is removed by suction through a hood mounted above the ladle. The invention also relates to a ladle arrangement for use in such treatment of a metal melt. Steel is produced from pig iron, scrap or sponge iron starting materials which are melted and decarburized in different types of furnaces, converters or like appara- tus. The metal melt is handled and transported with the aid of ladles having a volumetric capacity which is adapted to the process concerned. The ladles have the form of upwardly open vessels. Steel could be manufactured more effectively if the time that the melt spends in a ladle could be utilized to effect some part of the treatment to which the melt shall be subjected. For instance, this would decrease the time spent by the melt in a converter. In modern times, the term ladle metallurgy includes such efforts to utilize the ladle as a treatment station in steel manufacturing processes. Examples of those processes to which the melt can be subjected in a ladle are the various purifying proces¬ ses effected by introducing additives into the melt and agitating the melt with the aid of gases, and the in¬ troduction of pulverous alloying substances and slag formers, which is often effected in combination with the supply of a gas so as to achieve effective admixture of the alloying substances with the melt. Since the ladle is relatively deep, effective admixture of material with the melt with the aid of gas can be achieved when the additive material and the gas are in- troduced into the ladle at a location adjacent the bottom thereof. When applying ladle metallurgy, one problem is that only a very restricted gas flow can be delivered to a full ladle, since otherwise splash-over becomes un¬ acceptable, or the melt "boils over" the ladle rim. The volumetric capacity of the ladle is namely so adapted to the process concerned as to be substantially totally filled with melt. It is therewith impossible to reduce the volume of melt in the ladle, for practical and economic reasons. By way of comparison, it can be mentioned that in those processes in which gas is delivered to converters, the converters are filled only with a relatively small volume of melt, therewith enabling the specific gas flow to be maintained at a very high level. It can be mentioned as an example that in the case of the process known under the acronym BOF (Basic Oxygen Furnace), the converter is normally filled with melt solely to 10% of its volumetric capacity, therewith enabling a specific gas flow of 4.0 NM 3/tonne/mm to be used. When manufac¬ turing stainless steel in accordance with the AOD- process (Argon Oxygen Decarburization) , the converter is filled to 50% of its volumetric capacity, permitting a specific gas flow of 1.0 Nm /tonne/min to be used. On the other hand, in conventional ladle metallurgy, the ladle is normally filled to about 90% of its volumetric capacity, wherein a specific gas flow of only 0.002 Nm 3/tonne/mm can be used. It i.s quite probable that this low gas flow is the reason why, for instance, the hydrogen content of the melt cannot be decreased to any appreciable extent when treating the melt with an inert gas. Accordingly, the prime object of the present invention is to solve the problem of enabling metal melts to be treated effectively in ladles of conventional design, by delivering large specific gas flows to such ladles without the melt bubbling over or splashing from the ladle. The inventive solution is based on the realization that the aforesaid object can be achieved by providing above the ladle a closed splash chamber of sufficient volume to permit "boiling over" and splashing to take place without detriment when introducing large quantities of gas into the melt. The splash chamber must also be so configured that molten metal which splashes from the ladle is returned effectively to the melt in said ladle. The aforesaid objects are achieved in accordance with the present invention with a method of the kind defined in the introductory paragraph of the description which is characterized by introducing the gas or gas/powder mixture into the melt in a large volumetric flow, therewith causing the melt to bubble and splash vigor¬ ously; by limiting the effects of such bubbling and splashing to a defined space above the melt; by con¬ figuring the gas suction hood in the form of a lid which is placed substantially sealingly against the upper edge of the ladle; by giving the lid a configura¬ tion such that the volume of the space defined above the melt by means of the lid corresponds to a substantial part of the melt volume in the ladle, pre¬ ferably at least half of said volume; and by returning melt which has splashed-up on the inside of the lid to the melt in the ladle with the aid of the sides of said lid. The melt splashes are preferably returned to the ladle by guiding said melt splashes along the sides of the lid in pathways which terminate radially inwards of the upper defining edge of the ladle. The inner sur¬ faces of the lid are preferably formed from a refrac- tory material or some other heat-resistant construction which is capable of withstanding the het given-off by the upwardly splashing or "overboiling" melt. The inventive method thus enables a metal melt to be treated highly effectively during that time the melt remains in the ladle, since it is possible to supply large quantities of gas over short time periods at a relatively deep depth in the melt. In this way, there is achieved maximum admixture of gas and optionally powder with the melt in combination with effected agi¬ tation of the melt and long gas-residence times in said melt. In the case of one ladle embodiment for use when carry- ing out the method, the lid has a frustoconical con¬ figuration and the lid is intended to support against the upper defining edge of the ladle along the lower edge surface of the lid. This lid configuration is convenient for restricting the effect of melt splashes and for returning the splashed melt back to the ladle. The diameter of the cone opening facing towards the ladle will preferably be smaller than the diameter of the upper opening of said ladle. In the case of one practical lid configuration, the lower edge surface of the cone has extending circumferentially therearound a flange which forms a supporting and sealing surface against the upper edge surface of the ladle. Other characteristic features of the invention will be apparent from the following Claims. The invention will now be described in more detail with reference to the accompanying drawings. Figure 1 illustrates schematically a ladle arrangement of known construction intended for ladle metallurgy. Figure 2 illustrates schematically an inventive ladle arrangement. Figure l illustrates a conventional ladle 1, which is filled substantially to capacity with a metal melt 2. The reference numeral 3 designates a nozzle through which gas or a gas/powder mixture is introduced into the ladle for treating the melt 2, for instance purify¬ ing and/or alloying the melt. A hood 4, provided with a suction conduit 5, is mounted above the ladle 1 for the purpose of removing by suction gas and smoke rising from the melt. It will be evident that the specific gas flow which can be used with this known ladle arrangement is highly restricted because of the absence of space for accom¬ modating splashes from the melt and the absence of means for returning melt splashes to the melt contained by the ladle. If the specific gas flow to this ladle arrangement were to be increased, a large part of the melt would "boil over", therewith blocking the flue gas conduit and rendering further operation of the ladle impossible. In the case of this known ladle arrangement, only a relatively small specific gas flow can be utilized, this gas flow being in the order of 0.002 Nm 3/tonne/ min, as before mentioned. This limitation constitutes a serious drawback and restricts the utility of ladle metallurgy. Figure 2 illustrates schematically an inventive ladle arrangement, with which a sealed splash space or cham¬ ber 6 is formed above the surface of the melt 2. This space is obtained by giving the suction hood the form of a lid 7 which seals against the ladle 1 and which is of such configuration as to define a large free volume between the melt and the lid. It is necessary for this volume to correspond to an essential part of the volume of melt in the ladle, at least 1/3 of the melt volume, and preferably between 0.5 and 1 times the melt volume. This will enable the nozzle 3 to be designed for a very high specific gas flow in the same order of magnitude as that used in the conventional treatment of melts in converters, i.e. 1-4 Nm 3/tonne/min. The molten metal that bubbles and splashes vigorously from the ladle is therewith contained in the closed space, while retaining an effective gas-extracting effect through the lid. As will be seen from Figure 2, the lid 7 sealingly abuts the ladle 1, so as not to form a gap through which molten metal is able to escape. This greater gas flow enables the gas to be introduced into the melt and to agitate said melt more effectively than was earlier the case. The lid 7 will preferably have the shape of a frustated cone. This shape affords successive limitation of the splash space in a lateral or radial direction and the lid may be given a vertical extension or height such as to prevent undesirable melt deposits forming on its top surface. By providing the frustoconical lid with a lower opening of smaller diamter than the upper opening of the ladle l, the inner walls of the cone will form splash-metal paths which function to conduct splashed melt down into the melt in the ladle, without risk of the splashed melt running out onto the outer ladle surface. For practical reasons, the lower part of the lid will preferably be provided with a circumferential flange 8 which forms a combined support and sealing surface in coaction with the upper defining edge of the ladle 1. This provides a very simple and practical solution to the problem of providing a seal between lid and ladle and of returning upwardly splashing melt back to the ladle. A lid 7 of specific configuration has been described above. This configuration, however, can be varied in several respects within the scope of the following Claims while retaining the main lid function of de¬ fining a splash space of requisite size and of con¬ ducting melt splashes back to the ladle. Although not shown, at least the inner surfaces of the lid will have a heat-resistant construction and will preferably com¬ prise a layer of refractory material, so as to with¬ stand contact with the hot molten metal.

Claims: CLAIMS 1. A method of treating molten metal in a ladle, in which a gas or gas/powder mixture is introduced to the melt in a substantially full ladle and in which depart¬ ing gases are removed by suction through a hood mounted above the ladle, c h a r a c t e r i z e d by deli¬ vering a large volumetric flow of gas or gas/powder mixture to the melt, resulting in highly vigorous bubbling and splashing of molten metal from the melt; restricting the effects of said bubbling and splashing melt to a defined space above the melt, by giving the gas extraction hood the form of a lid and mounting said lid essentially sealingly against the upper edge of the ladle; by configuring the lid such that the volume defined by the lid above the melt corresponds to a substantial part of the volume of melt in the ladle, preferably at least half of said volume; and by causing melt which has splashed up on the inside of the lid to return to the melt in the ladle along the sides of said lid. 2. A method according to Claim 1, c h a r a c ¬ t e r i z e d by returning melt which splashes on the inside of the lid to the melt contained in the ladle by conducting said melt splashes along pathways on the inner surfaces of the lid which terminate radially inwards of the upper defining edge of the ladle. 3. A ladle arrangement intended for use when treating a metal melt, in which gas or gas/powder mixture is delivered to the melt (2) which substantially fills the ladle (1) completely, and in which gas is extracted by suction through a hood mounted above the ladle. c h a r a c t e r i z e d in that the hood is con¬ structed to permit a large volumetric flow of gas or gas/powder to be delivered to the melt, which results in vigorous splashing and bubbling of the melt; in that 5 for the purpose of limiting the effects of such metal splashes to a defined space above the melt (2) , the hood is configured as a lid (7) which is intended to substantially seal against the upper edge of the ladle (1); in that the lid has a configuration such that the 10 volume (6) defined by the lid above the melt corres¬ ponds to a substantial part of the volume of melt (2) in the ladle (1), preferably at least half said volume; and in that the side surfaces of the lid (7) define conducting pathways for splash-metal droplets such that 15 the droplets are returned to the melt in the ladle by the inner lid surfaces. 4. A ladle arrangement according to Claim 3, c h a r a c t e r i z e d in that the inner surfaces 20 of the lid (7) form splash-metal pathways which ter¬ minate radially inwards of the upper defining edge of the ladle (1). 5. A ladle arrangement according to Claim 3 or 4, 25 c h a r a c t e r i z e d in that at least the inner surfaces of the lid (7) have a heat-resistant construc¬ tion, and preferably include a layer of refractory material. 30 6. A ladle arrangement according to any one of Claims 3-5, c h a r a c t e r i z e d in that the lid (7) has a frustoconical configuration and is intended to support against the upper defining edge of the ladle / (1) along a lower lid edge surface. 35 7. A ladle arrangement according to Claim 6, c h a r a c t e r i z e d in that the diameter of the cone opening facing towards the ladle (1) is smaller than the diameter of the upper ladle opening. 8. A ladle arrangement according to Claim 7, c h a r a c t e r i z e d in that the lower edge of the cone is configured with a circumferentially ex¬ tending flange (8) which forms a support and sealing surface against the upper edge of the ladle (1).

Inventors: BRUNNER MIKAEL, BRUNNER, MIKAEL
Applicants: AGA AB
Application year: 1990
Main classification: B22D41
IPC codes: B22D1, B22D27, B22D41, C21C7, C22B9