Patent Number: 063226103
Section: claims

1. A device to inject at least one gas selected from the group consisting of oxygen, gases containing oxygen, and other technological gases and a solid material in powder form, in a furnace used in steel and metallurgical melting processes for forming a liquid metal bath, comprising: a body suitable to be mounted fixed in an aperture made on the wall of the furnace, an emission element being housed at an end of said body, said emission element including an outlet mouth for being arranged, in an operating position, at a certain distance from an upper level of the liquid bath, said emission element having a longitudinal axis, and said body having an outer containing shell inside which are defined circulation channels for a cooling fluid,  a radially inner portion of said emission element being shaped as a double nozzle, respectively a first inner nozzle and a second nozzle, said second nozzle being annularly outside said first nozzle and substantially co-axial with said first nozzle,  the first nozzle having a first terminal section and a convergent/divergent conformation defined by a neck located at a position upstream of the first terminal section and being predisposed for the emission of a jet of gas at supersonic speed,  wherein said second nozzle has a second terminal section having a downstream end, and the downstream end has a conformation convergent towards the longitudinal axis of the emission element and is pre-disposed for the emission of a jet at subsonic speed of a member of the group consisting of oxygen alone, gases containing oxygen, other technological gases, solid material in powder form carried by a carrier gas, and liquid in atomized form.  providing the device of claim 1;  performing a melting process to form a liquid metal bath and, while the melting process is in progress, using the device in at least one operating step selected from the group consisting of: 2. The device as in claim 1, wherein said first nozzle has said first terminal section and said second nozzle has said second terminal section, said terminal sections being arranged inside said outlet mouth of said emission element. 3. The device as in claim 1, wherein said outlet mouth is arranged at a height of between about 0.5 and 2.5 m with respect to the surface of the bath. 4. The device as in claim 1, further comprising valve means suitable to regulate the outlet speed of the gas at least from said first nozzle according to the conditions of pressure/temperature/density inside the furnace so that the expansion of said gas occurs completely inside said emission element. 5. The device as in claim 1, wherein said first nozzle terminal section has inner circumferential grooves to stabilize a sublayer of the primary supersonic jet which is nearest the wall. 6. The device as in claim 1, wherein the second nozzle has an outlet section which is circular or elliptic in shape. 7. The device as in claim 1, wherein within the outlet section of the second nozzle there are deflector elements with at least an operating position suitable to partly reduce the gassy flow leaving said second nozzle to generate a swirling movement of the flow with the purpose of regulating at least one member of the group consisting of the length and the shape of the jet emerging from the first nozzle. 8. The device as in claim 1, wherein at least the first nozzle is axially movable with respect to the outlet mouth of the emission element. 9. The device as in claim 1, wherein the second nozzle is axially movable with respect to the outlet mouth of the emission element. 10. The device as in claim 1, wherein at least one member of the group consisting of the first nozzle and the second nozzle are at least partly lined on the inside with wear-resistant and/or erosion-resistant material. 11. The device as in claim 10, wherein the wear-resistant and/or erosion-resistant material is ceramic material or high-resistance resins or special varnish. 12. The device as in claim 1, further comprising a channel to feed solid fuel in powder form or particles into the first nozzle. 13. The device as in claim 1, having an axis for orienting with respect to the surface of the liquid bath, said axis defining an angle of between 30.degree. and 70.degree. with respect to said surface. 14. A method to use the device to inject at least one gas selected from the group consisting of oxygen, gases containing oxygen, and other technological gases and solid material in powder form of claim 1 comprising: 15. The method as in claim 14, further comprising operating the device in a burner step comprising burning with variable stochiometric ratios of oxygen and combustible substance and variable flame length by means of injecting at least a gas containing said oxygen through one of the two nozzles and injecting said combustible substance through the other of said nozzles. 16. The method as in claim 14, wherein the device is employed to measure the pressure of the supersonic jet delivered by the first nozzle at least at a position upstream of the neck and at a position in correspondence with said neck, and to regulate in feedback the emission pressure by means of valve means located upstream of said first nozzle. 17. The method as in claim 14, wherein in the burner step, the first nozzle is a convergent/divergent nozzle used as a Venturi tube to mix a substance, selected from the group consisting of oxygen or air enriched with oxygen, with a combustible substance. 18. The method as in claim 17, wherein in the burner step, the second nozzle emits a jet of oxygen-containing gas to maintain the fuel/oxygen ratio in the primary flow delivered by the first nozzle in sub-stochiometric conditions and to complete combustion. 19. The method as in claim 14, wherein prior to said at least one operating step the device delivers a supersonic jet through the first nozzle of a combustible gas and a subsonic jet through the second nozzle of an oxidant-rich gas, to cause scrap to descend in front of the outlet mouth of the emission element. 20. The method as in claim 15, wherein the device regulates the length and/or shape of the flame emitted by the device in the burner step by partly reducing the flow emerging from the second nozzle by means of deflector elements with adjustable positioning. 21. The method as in claim 14, comprising regulating the length and/or shape of a flame emitted by the device in the burner step by varying the longitudinal axial positioning of the first and/or the second nozzle with respect to the outlet mouth of the emission element. 22. The method as in claim 14, wherein during said injecting of said gassy jet at supersonic speed through said first convergent/divergent nozzle and of solid material in powder form through said second nozzle, the second nozzle injects said solid material in powder form selected from the group consisting of carbon or lime powder, on a fluid carrier selected from the group consisting of a gas or a liquid to increase the foaming effect of the slag and the recarburization of the liquid steel, while the first nozzle emits a supersonic gassy jet of oxygen and/or other technological gases. 23. The method as in claim 14, wherein during said injecting of said gassy jet at supersonic speed through said first convergent/divergent nozzle and of solid material in powder form through said second nozzle, the second nozzle is used to inject a subsonic gassy jet for protective and/or transporting purposes, while the first nozzle is used to inject solid materials in powder form or particles on a fluid vehicle. 24. The method as in claim 14, wherein, as the melting proceeds, the level of the surface of the liquid bath varies and the inclination of the device is varied with respect to the surface of the bath to follow the variation in the level of the liquid bath and to maintain the angle of incidence of the jet substantially constant, to prevent the jet being reflected. 25. The device as in claim 1, wherein said the first inner nozzle and a second nozzle each have a respective outlet mouth and the respective outlet mouths of the two nozzles are substantially aligned on the same transverse plane, or with the first inner nozzle mouth ending farther downstream than the mouth of the second nozzle. 26. The device as in claim 1, wherein the device has an axis which is orientable with respect to the surface of the liquid bath, said axis defining an angle of between 40.degree. and 50.degree. with respect to said surface of the liquid bath.