METHOD FOR CONTROLLING THE SUSPENSION IN A SUSPENSION SMELTING FURNACE, A SUSPENSION SMELTING FURNACE, AND A CONCENTRATE BURNER

Abstract

The invention relates to a method for controlling suspension in a suspension smelting furnace, to a suspension smelting furnace, and to a concentrate burner. The method comprises feeding additionally to pulverous solid matter and additionally to reaction gas reducing agent into the suspension smelting furnace, wherein reducing agent is fed in the form of a concentrated stream of reducing agent through the suspension in the reaction shaft onto the surface of the melt to form a reducing zone containing reducing agent within the collection zone of the melt.

Claims

1. A suspension smelting furnace for suspension smelting of pulverous solid matter, wherein the suspension smelting furnace comprises a reaction shaft having a top and a lower end, a concentrate burner that comprises a pulverous solid matter supply device for feeding pulverous solid matter and that comprises a gas supply device for feeding reaction gas into the reaction shaft to produce a suspension of pulverous solid matter and reaction gas in the reaction shaft, wherein the concentrate burner is located at the top of the reaction shaft, a lower furnace for collecting suspension in the lower furnace to form a melt having a surface, wherein the lower end of the reaction shaft ends in the lower furnace and wherein, when the suspension smelting furnace is in use, suspension that is produced in the reaction shaft and that lands on the surface of the melt in the lower furnace is configured to create a collection zone at the surface of the melt in the lower furnace, and a reducing agent feeding means for feeding additionally to pulverous solid matter and additionally to reaction gas reducing agent into the suspension smelting furnace, wherein the reducing agent feeding means is configured for feeding, when the suspension smelting furnace is in use, reducing agent in the form of a concentrated stream of reducing agent through the suspension that is produced in the reaction shaft onto the surface of the melt in the lower furnace to form a reducing zone containing reducing agent in the collection zone of the melt in the lower furnace, wherein the reducing agent feeding means is configured to feed reducing agent at an initial velocity that is at least the feeding velocity of the reaction gas, wherein the concentrate burner being configured to feed pulverous solid matter and reaction gas into the reaction shaft so that suspension produced by pulverous solid matter and reaction gas forms a suspension jet in the suspension shaft, wherein the suspension jet widens in the reaction shaft in the direction of the lower furnace and wherein the suspension jet has an imaginary vertical central axis, and wherein the reducing agent feeding means being configured to feed the concentrated stream of reducing agent essentially in the direction of the imaginary vertical central axis of the suspension jet and in the vicinity to the imaginary vertical central axis of the suspension jet to prevent reducing agent of the concentrated stream of reducing agent from reacting with reaction gas prior landing on the surface of the melt.

2. The suspension smelting furnace according to claim 1, wherein the reducing agent feeding means being configured to feed the concentrated stream of reducing agent from the inside the lower furnace of the suspension smelting furnace.

3. The suspension smelting furnace according to claim 1, wherein the reducing agent feeding means being configured to feed the concentrated stream of reducing agent from the inside the reaction shaft of the suspension smelting furnace.

4. The suspension smelting furnace according to claim 1, wherein the reducing agent feeding means being configured to feed the concentrated stream of reducing agent from the top of the reaction shaft of the suspension smelting furnace inside the reaction shaft of the suspension smelting furnace.

5. The suspension smelting furnace according to claim 1, wherein the concentrate burner being provided with a reducing agent feeding means configured to feed the concentrated stream of reducing agent.

6. The suspension smelting furnace according to claim 1, wherein the concentrate burner comprising a pulverous solid matter supply device comprising a feeder pipe for feeding pulverous solid matter into the reaction shaft, wherein the feeder pipe has an orifice that opens to the reaction shaft; a dispersing device, which is arranged concentrically inside the feeder pipe and which extends to a distance beyond the orifice of the feeder pipe into the reaction shaft and which comprises dispersion gas openings for directing dispersion gas around the dispersing device and to pulverous solid matter that flows around the dispersing device; and a gas supply device for feeding reaction gas into the reaction shaft, wherein the gas supply device opening to the reaction shaft through an annular discharge orifice that concentrically surrounds the feeder pipe for mixing reaction gas that discharges from the annular discharge orifice with pulverous solid matter, which discharges from the orifice of the feeder pipe and which is directed to the side by means of dispersion gas to produce suspension of pulverous solid matter and reaction gas in the reaction shaft.

7. The suspension smelting furnace according to claim 6, wherein the concentrate burner comprising a reducing agent feeding means in the form of a central lance that is arranged inside the dispersing device of the concentrate burner, wherein the central lance comprising a discharge orifice that opens to the reaction shaft.

8. The suspension smelting furnace according to claim 1, wherein the reducing agent feeding means being configured to feed a concentrated stream of reducing agent that contains at least one of carbon, sulphide such as coke, coke powder, pulverized biomass, pulverized charcoal, the same pulverous solid matter that is fed by means of the pulverous solid matter supply device of the concentrate burner, ground electronic scrap and circuit board chaff.

9. The suspension smelting furnace according to claim 1, wherein the reducing agent feeding means is configured to feed reducing agent at an initial velocity that is at least twice the feeding velocity of the reaction gas.

10. The suspension smelting furnace according to claim 1, wherein the gas supply device being configured to feed as reaction gas oxygen enriched gas that has an oxygen content between about 50 and about 100%.

11. The suspension smelting furnace according to claim 1, including controlling means configured to control the amount of fed reaction gas to the amount of fed reducing agent to form sub-stoichiometric conditions in the middle of the suspension of the suspension smelting furnace.

12. The suspension smelting furnace according to claim 1, including controlling means configured to control the amount of fed reaction gas to the amount of fed reducing agent to form stoichiometric or over-stoichiometric conditions in the middle of the suspension of the suspension smelting furnace.

Description

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

[0021] In the following the invention will be described in more detail by referring to the figures, of which

[0022] FIG. 1 is a schematic representation of a suspension smelting furnace according to a first preferred embodiment,

[0023] FIG. 2 is a schematic representation of a suspension smelting furnace according to a second preferred embodiment,

[0024] FIG. 3 is a schematic representation of a suspension smelting furnace according to a third preferred embodiment,

[0025] FIG. 4 is a schematic representation of a suspension smelting furnace according to a fourth preferred embodiment,

[0026] FIG. 5 is a schematic representation of a suspension smelting furnace according to a fifth preferred embodiment,

[0027] FIG. 6 is a schematic representation of a concentrate burner for a suspension smelting furnace according to a first preferred embodiment, and

[0028] FIG. 7 is a schematic representation of a concentrate burner for a suspension smelting furnace according to a second preferred embodiment.

DETAILED DESCRIPTION OF THE INVENTION

[0029] First the method for controlling suspension in a suspension smelting furnace and preferred and alternative embodiments of the method will be described in greater detail.

[0030] The method comprises using a suspension smelting furnace 1 comprising a reaction shaft 2 and a lower furnace 3 at the lower end of the reaction shaft 2 and a concentrate burner 5 at the top of the reaction shaft 2. The suspension smelting furnace 1 shown in FIGS. 1 to 5 also comprises an uptake 4.

[0031] The method comprises using a concentrate burner 5 that comprises a pulverous solid matter supply device 18 for feeding pulverous solid matter 6 into the reaction shaft 2 and that comprises a gas supply device (24) for feeding reaction gas 7 into the reaction shaft 2 to produce a suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2.

[0032] The method comprises feeding pulverous solid matter 6 and reaction gas 7 into the reaction shaft 2 by means of the concentrate burner 5 to produce a suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2.

[0033] The method comprises collecting suspension 8 in the lower furnace 3 on the surface 9 of a melt 10 in the lower furnace 3, so that suspension 8 that lands on the surface 9 creates a collection zone 14 at the surface 9 of a melt 10 in the lower furnace 3. In FIGS. 1 to 5 a melt 10 having a matte layer 11 and a slag layer 12 on top of the matte layer is shown.

[0034] The operating principle of a such suspension smelting furnace is known for example from publication U.S. Pat. No. 2,506,577.

[0035] The method comprises feeding additionally to pulverous solid matter 6 and additionally to reaction gas 7 reducing agent 13 into the suspension smelting furnace 1 so that reducing agent 13 is fed in the form of a concentrated stream of reducing agent 13 through the suspension 8 in the reaction shaft 2 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0036] The method may comprise a step for arranging a reducing agent feeding means 16 at least partly inside the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprising a nozzle 17 that opens into the suspension smelting furnace 1, and a step for feeding the concentrated stream of reducing agent 13 through the nozzle 17 of the reducing agent feeding means 16 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0037] In FIG. 1 a concentrated stream of reducing agent 13 is fed from the inside of the suspension smelting furnace 1, more precisely from the inside of the lower furnace 3 of the suspension smelting furnace 1, onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10. The method illustrated in FIG. 1 may comprise a step for arranging a reducing agent feeding means 16 at least partly inside the lower furnace 3 of the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprising a nozzle 17 that opens into the suspension smelting furnace 1, and a step for feeding the concentrated stream of reducing agent 13 through the nozzle 17 of the reducing agent feeding means 16 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0038] In FIG. 2 a concentrated stream of reducing agent 13 is fed from the inside of the reaction shaft 2 of the suspension smelting furnace 1 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10. The method illustrated in FIG. 2 may comprise a step for arranging a reducing agent feeding means 16 at least partly inside the reaction shaft 2 of the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprising a nozzle 17 that opens into the suspension smelting furnace 1 and a step for feeding the concentrated stream of reducing agent 13 through the nozzle 17 of the reducing agent feeding means 16 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0039] In FIG. 3 a concentrated stream of reducing agent 13 is fed from the inside of the reaction shaft 2 of the suspension smelting furnace 1 so that a concentrated stream of reducing agent 13 is fed from the top of the reaction shaft 2 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10. The method illustrated in FIG. 3 may comprise a step for arranging a reducing agent feeding means 16 at the top of the reaction shaft 2, inside the reaction shaft 2 of the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprising a nozzle 17 that opens into the suspension smelting furnace 1, and a step for feeding the concentrated stream of reducing agent 13 through the nozzle 17 of the reducing agent feeding means 16 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0040] In FIG. 4 a concentrated stream of reducing agent 13 is fed by means of the concentrate burner 5 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10. The method illustrated in FIG. 4 may comprise a step for providing the concentrate burner 5 with a reducing agent feeding means 16, wherein the reducing agent feeding means 16 comprising a nozzle 17 that opens into the suspension smelting furnace 1 and a step for feeding the concentrated stream of reducing agent 13 through the nozzle 17 of the reducing agent feeding means 16 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0041] In a preferred embodiment of the method, the method comprises using a concentrate burner 5 that comprises

[0042] a pulverous solid matter supply device 18 comprising a feeder pipe 19 for feeding pulverous solid matter 6 into the reaction shaft 2, wherein the feeder pipe 19 has an orifice 20 that opens to the reaction shaft 2;

[0043] a dispersing device 21, which is arranged concentrically inside the feeder pipe 19 and which extends to a distance beyond the orifice 20 of the feeder pipe 19 into the reaction shaft 2 and which comprises dispersion gas openings 22 for directing dispersion gas 23 around the dispersing device 21 and to pulverous solid matter 6 that flows around the dispersing device 21; and

[0044] a gas supply device 24 for feeding reaction gas 7 into the reaction shaft 2, wherein the gas supply device 24 opening to the reaction shaft 2 through an annular discharge orifice 25 that concentrically surrounds the feeder pipe 19 for mixing reaction gas 7 that discharges from the annular discharge orifice 25 with pulverous solid matter 6, which discharges from the orifice 20 of the feeder pipe 19 and which is directed to the side by means of dispersion gas.

[0045] In this preferred embodiment of the method, the method comprises

[0046] feeding pulverous solid matter 6 into the reaction shaft 2 through the orifice 20 of the feeder pipe 19 of the concentrate burner 5;

[0047] feeding dispersion gas 23 into the reaction shaft 2 through the dispersion gas openings 22 of the dispersing device 21 of the concentrate burner 5 for directing dispersion gas 23 to pulverous solid matter 6 that flows around the dispersing device 21 to direct pulverous solid matter 6 to the side by means of dispersion gas; and

[0048] feeding reaction gas 7 into the reaction shaft 2 through the annular discharge orifice 25 of the gas supply device 24 of the concentrate burner 5 for mixing reaction gas 7 with pulverous solid matter 6 which discharges from the middle of the feeder pipe 19 and which is directed to the side by means of dispersion gas 23 to produce suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2.

[0049] This preferred embodiment of the method may comprise using a concentrate burner 5 that comprises a reducing agent feeding means 16 in the form of a central lance 26 that is arranged inside the dispersing device 21 of the concentrate burner 5, wherein the central lance 26 comprising a discharge orifice 27 that opens to the reaction shaft 2; and by feeding a concentrated stream of reducing agent 13 through the discharge orifice 27 of the central lance 26 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.

[0050] This preferred embodiment of the method may comprise using a concentrate burner 5 that comprises a reducing agent feeding means 16 that is arranged inside the concentrate burner 5, wherein the central lance 26 comprising a discharge orifice 27 that opens to the reaction shaft 2; and by feeding a concentrated stream of reducing agent 13 through the discharge orifice 27 of the central lance 26 onto the surface 9 of the melt 10 to form a reducing zone 15 containing reducing agent 13 within the collection zone 14 of the melt 10.The method may comprise using reducing agent 13 that contains at least one of carbon and sulphide such as coke, coke powder, pulverized biomass, pulverized charcoal, the same pulverous solid matter that is fed by means of the pulverous solid matter supply device 18 of the concentrate burner, ground electronic scrap and/or circuit board chaff.

[0051] Reducing agent 13 is preferably, but not necessarily, fed at an initial velocity that is at least the feeding velocity of the reaction gas 7, more preferably at an initial velocity that is at least twice the feeding velocity of the reaction gas 7.

[0052] Reaction gas 7 in the form of oxygen enriched gas that has an oxygen content between about 50 and about 100% is preferably, but not necessarily, used in the method.

[0053] In the method pulverous solid matter 6 and reaction gas 7 is preferably, but not necessarily, fed into the reaction shaft 2 by means of the concentrate burner 5 so that suspension 8 produced by pulverous solid matter 6 and reaction gas 7 forms a suspension jet 28 in the suspension shaft 2, wherein the suspension jet 28 widens in the reaction shaft 2 in the direction of the lower furnace 3 and wherein the suspension jet 28 has an imaginary vertical central axis 29. If pulverous solid matter 6 and reaction gas 7 by means of the concentrate burner 5 so that a such suspension jet 28 is formed, the method may include directing a concentrated stream of reducing agent 13 essentially in the direction of the imaginary vertical central axis 29 of the suspension jet 28 and in the vicinity to the imaginary vertical central axis 29 of the suspension jet 28 to at least partly prevent reducing agent of the concentrated stream of reducing agent 13 from reacting with reaction gas prior landing on the surface of the melt. In this embodiment reducing agent of the concentrated stream of reducing agent 13 is at least partly prevented from reacting with reaction gas prior landing on the surface of the melt, because the reaction gas content is lower in the vicinity to the imaginary vertical central axis 29 of a such suspension jet 28 than outside the suspension jet.

[0054] The method may include forming a concentrated stream of reducing agent by directing a part of the pulverous solid matter that is fed by means of the pulverous solid matter supply device 18 of the concentrate burner towards the middle of the reaction shaft 2 where the reaction gas content is low to prevent at least a part of said part of the pulverous solid matter that is fed by means of the pulverous solid matter supply device 18 of the concentrate burner and that is directed towards the middle of the reaction shaft 2 where the reaction gas content is low to react with reaction gas prior landing on the surface of the melt.

[0055] The method may include forming controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form sub-stoichiometric conditions in the reaction shaft 2 of the suspension smelting furnace. This is preferably done so that first the feeing amount of reducing agent 13 is determined and thereafter the feeding amount of reaction gas 7 is adjusted to form sub-stoichiometric conditions in the reaction shaft 2 of the suspension smelting furnace.

[0056] The method may include forming controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form sub-stoichiometric conditions in the middle of the suspension 8 in the reaction shaft 2 of the suspension smelting furnace. This is preferably done so that first the feeing amount of reducing agent 13 is determined and thereafter the feeding amount of reaction gas 7 is adjusted to form sub-stoichiometric conditions in the middle of the suspension 8 in the reaction shaft 2 of the suspension smelting furnace.

[0057] The method may include controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form over-stoichiometric conditions in the reaction shaft 2 of the suspension smelting furnace. This is preferably done so that first the feeing amount of reducing agent 13 is determined and thereafter the feeding amount of reaction gas 7 is adjusted to form over-stoichiometric conditions in the reaction shaft 2 of the suspension smelting furnace.

[0058] The method may include controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form over-stoichiometric conditions in the middle of the suspension 8 of the reaction shaft 2 of the suspension smelting furnace. This is preferably done so that first the feeing amount of reducing agent 13 is determined and thereafter the feeding amount of reaction gas 7 is adjusted to form over-stoichiometric conditions in the middle of the suspension 8 in the reaction shaft 2 of the suspension smelting furnace.

[0059] Next the suspension smelting furnace 1 for suspension smelting of pulverous solid matter 6 and preferred and alternative embodiments of the suspension smelting furnace 1 will be described in greater detail.

[0060] The suspension smelting furnace 1 comprises a reaction shaft 2 having a top and a lower end.

[0061] The suspension smelting furnace 1 comprises additionally a concentrate burner 5 that comprises a pulverous solid matter supply device 18 for feeding pulverous solid matter 6 and that comprises a gas supply device 24 for feeding reaction gas 7 into the reaction shaft 2 to produce a suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2, wherein the concentrate burner 5 is located at the top of the reaction shaft 2.

[0062] The suspension smelting furnace 1 comprises additionally a lower furnace 3 for collecting suspension 8 in the lower furnace 3 to form a melt 10 having a surface 9, wherein the lower end of the reaction shaft 2 ends in the lower furnace 3 and wherein, when the suspension smelting furnace 1 is in use, suspension 8 that is produced in the reaction shaft 2 and that lands on the surface 9 of the melt 10 in the lower furnace 3 is configured to create a collection zone 14 at the surface 9 of the melt 10 in the lower furnace 3.

[0063] The suspension smelting furnace 1 shown in the FIGS. 1 to 5 comprises additionally an uptake 4.

[0064] The operating principle of a such suspension smelting furnace is known for example from publication U.S. Pat. No. 2,506,577.

[0065] The suspension smelting furnace 1 comprises reducing agent feeding means 16 for feeding additionally to pulverous solid matter 6 and additionally to reaction gas 7 reducing agent 13 into the suspension smelting furnace 1. The reducing agent feeding means 16 are configured for feeding, when the suspension smelting furnace 1 is in use, reducing agent 13 in the form of a concentrated stream of reducing agent 13 through the suspension 8 that is produced in the reaction shaft 2 onto the surface 9 of the melt 10 in the lower furnace 3 to form a reducing zone 15 containing reducing agent 13 in the collection zone 14 of the melt 10 in the lower furnace 3.

[0066] The suspension smelting furnace 1 may comprise a reducing agent feeding means 16 in the form of a reducing agent feeding means 16 arranged at least partly inside the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprises a nozzle 17 that opens into the suspension smelting furnace 1.

[0067] The suspension smelting furnace 1 shown in FIG. 1 comprises a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13 from the inside of the suspension smelting furnace 1, more precisely a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13 from the inside of the lower furnace 3 of the suspension smelting furnace 1. It is possible that suspension smelting furnace 1 comprises a reducing agent feeding means 16 in the form of a reducing agent feeding means 16 arranged at least partly inside the lower furnace 3 of the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprises a nozzle 17 that opens into the lower furnace 3 of the suspension smelting furnace 1.

[0068] The suspension smelting furnace 1 shown in FIG. 2 comprises a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13 from the inside of the reaction shaft 2 of the suspension smelting furnace 1. It is possible that suspension smelting furnace 1 comprises a reducing agent feeding means 16 in the form of a reducing agent feeding means 16 arranged at least partly inside the reaction shaft 2 of the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprises a nozzle 17 that opens into the reaction shaft 2 of the suspension smelting furnace 1.

[0069] The suspension smelting furnace 1 shown in FIG. 3 comprises a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13 inside the suspension smelting furnace 1 from the top of reaction shaft 2 of the suspension smelting furnace 1. It is possible that the suspension smelting furnace 1 comprises a reducing agent feeding means 16 in the form of a reducing agent feeding means 16 arranged at the top of the reaction shaft 2 of the suspension smelting furnace 1, wherein the reducing agent feeding means 16 comprises a nozzle 17 that opens into the reaction shaft 2 of the suspension smelting furnace 1 at the top of the reaction shaft 2.

[0070] In the suspension smelting furnace 1 shown in FIG. 4 the concentrate burner 5 is provided with a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13.

[0071] In a preferred embodiment of the suspension smelting furnace 1 the concentrate burner 5 comprises

[0072] a pulverous solid matter supply device 18 comprising a feeder pipe 19 for feeding pulverous solid matter 6 into the reaction shaft 2, wherein the feeder pipe 19 has an orifice 20 that opens to the reaction shaft 2;

[0073] a dispersing device 21, which is arranged concentrically inside the feeder pipe 19 and which extends to a distance beyond the orifice 20 of the feeder pipe 19 into the reaction shaft 2 and which comprises dispersion gas openings 22 for directing dispersion gas 23 around the dispersing device 21 and to pulverous solid matter 6 that flows around the dispersing device 21; and

[0074] a gas supply device 24 for feeding reaction gas 7 into the reaction shaft 2, wherein the gas supply device 24 opens to the reaction shaft 2 through an annular discharge orifice 25 that concentrically surrounds the feeder pipe 19 for mixing reaction gas 7 that discharges from the annular discharge orifice 25 with pulverous solid matter 6, which discharges from the orifice 20 of the feeder pipe 19 and which is directed to the side by means of dispersion gas 23 to produce suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2. In this preferred embodiment of the suspension smelting furnace 1 the concentrate burner 5 may comprise a reducing agent feeding means 16 in the form of a central lance 26 that is arranged inside the dispersing device 21 of the concentrate burner 5, wherein the central lance 26 comprising a discharge orifice 27 that opens to the reaction shaft 2.

[0075] The suspension smelting furnace 1 may comprise a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13 that contains at least one of carbon and sulphide such as coke, coke powder, pulverized biomass, pulverized charcoal, the same pulverous solid matter that is fed by means of the pulverous solid matter supply device 18 of the concentrate burner, ground electronic scrap and/or circuit board chaff.

[0076] The suspension smelting furnace 1 may comprise a reducing agent feeding means 16 for feeding reducing agent 13 at an initial velocity that is at least the feeding velocity of the reaction gas 7, preferably at an initial velocity that is at least twice the feeding velocity of the reaction gas 7.

[0077] The suspension smelting furnace 1 may comprise a gas supply device 24 for feeding as reaction gas 7 oxygen enriched gas that has an oxygen content between about 50 and about 100%.

[0078] The concentrate burner 5 of the suspension smelting furnace may be arranged for feeding pulverous solid matter 6 and reaction gas 7 into the reaction shaft 2 so that suspension 8 produced by pulverous solid matter 6 and reaction gas 7 forms a suspension jet 28 in the suspension shaft 2, which the suspension jet 28 widens in the reaction shaft 2 in the direction of the lower furnace 3 and which the suspension jet has an imaginary vertical central axis 29. In this case, the suspension smelting furnace 1 may comprise a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13 essentially in the direction of the imaginary vertical central axis 29 of the suspension jet 28 and in the vicinity to the imaginary vertical central axis 29 of the suspension jet 28 to at least partly prevent reducing agent of the concentrated stream of reducing agent from reacting with reaction gas prior landing on the surface of the melt.

[0079] The suspension smelting furnace 1 may comprise a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent by forming a concentrated stream of reducing agent by directing a part of the pulverous solid matter that is fed by means of the pulverous solid matter supply device 18 of the concentrate burner towards the middle of the reaction shaft 2 where the reaction gas content is low to prevent at least a part of said part of the pulverous solid matter that is fed by means of the pulverous solid matter supply device 18 of the concentrate burner and that is directed towards the middle of the reaction shaft 2 where the reaction gas content is low to react with reaction gas prior landing on the surface of the melt.

[0080] The suspension smelting furnace 1 may comprise controlling means for controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form sub-stoichiometric conditions in the suspension smelting furnace.

[0081] The suspension smelting furnace 1 may comprise controlling means for controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form sub-stoichiometric conditions in the middle of the suspension 8 in the reaction shaft 2 of the suspension smelting furnace.

[0082] The suspension smelting furnace 1 may comprise controlling means for controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form over-stoichiometric conditions in the suspension smelting furnace.

[0083] The suspension smelting furnace 1 may comprise controlling means for controlling the amount of fed reaction gas 7 to the amount of fed reducing agent 13 to form over-stoichiometric conditions in the middle of the suspension 8 in the reaction shaft 2 of the suspension smelting furnace. Next the concentrate burner 5 for feeding reaction gas 7 and pulverous solid matter 6 into the reaction shaft 2 of suspension smelting furnace 1 and preferred and alternative embodiments of the concentrate burner 5 will be described in greater detail.

[0084] The concentrate burner 5 comprises a pulverous solid matter supply device 18 comprising a feeder pipe 19 for feeding pulverous solid matter 6 into the reaction shaft 2, wherein the feeder pipe 19 has an orifice 20 that opens to the reaction shaft 2.

[0085] The concentrate burner 5 comprises additionally a dispersing device 21, which is arranged concentrically inside the feeder pipe 19 and which extends to a distance beyond the orifice 20 of the feeder pipe 19 into the reaction shaft 2 and which comprises dispersion gas openings 22 for directing dispersion gas 23 around the dispersing device 21 and to pulverous solid matter 6 that flows around the dispersing device 21.

[0086] The concentrate burner 5 comprises additionally a gas supply device 24 for feeding reaction gas 7 into the reaction shaft 2 wherein the gas supply device 24 opens to the reaction shaft 2 through an annular discharge orifice 25 that concentrically surrounds the feeder pipe 19 for mixing reaction gas 7 that discharges from the annular discharge orifice 25 with pulverous solid matter 6, which discharges from the orifice 20 of the feeder pipe 19 and which is directed to the side by means of dispersion gas 23 to produce suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2.

[0087] The concentrate burner 5 is provided with a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13.

[0088] The concentrate burner 5 may comprise, as shown in FIG. 7, a reducing agent feeding means 16 in the form of a central lance 26 that is arranged inside the dispersing device 21 of the concentrate burner 5, wherein the central lance 26 comprising a discharge orifice 27 that opens to the reaction shaft 2.

[0089] The concentrate burner 5 may comprise, as shown in FIG. 8, a reducing agent feeding means 16 in the form of a reducing agent feeding means 16, wherein the reducing agent feeding means 16 comprises a nozzle 17 that opens into the reaction shaft 2 of the suspension smelting furnace 1.

[0090] The invention also relates to a concentrate burner 5 for use in a method according to the invention or in a suspension smelting furnace 1 according to the invention.

[0091] The concentrate burner 5 comprises a pulverous solid matter supply device 18 comprising a feeder pipe 19 for feeding pulverous solid matter 6 into the reaction shaft 2, wherein the feeder pipe 19 has an orifice 20 that opens to the reaction shaft.

[0092] The concentrate burner 5 comprises additionally a dispersing device 21, which is arranged concentrically inside the feeder pipe 19 and which extends to a distance beyond the orifice 20 of the feeder pipe 19 into the reaction shaft 2 and which comprises dispersion gas openings 22 for directing dispersion gas 23 around the dispersing device 21 and to pulverous solid matter 6 that flows around the dispersing device 21.

[0093] The concentrate burner 5 comprises additionally a gas supply device 24 for feeding reaction gas 7 into the reaction shaft 2 wherein the gas supply device 24 opens to the reaction shaft 2 through an annular discharge orifice 25 that concentrically surrounds the feeder pipe 19 for mixing reaction gas 7 that discharges from the annular discharge orifice 25 with pulverous solid matter 6, which discharges from the orifice 20 of the feeder pipe 19 and which is directed to the side by means of dispersion gas 23 to produce suspension 8 of pulverous solid matter 6 and reaction gas 7 in the reaction shaft 2.

[0094] The concentrate burner 5 is provided with a reducing agent feeding means 16 for feeding a concentrated stream of reducing agent 13.

[0095] The concentrate burner 5 may comprise, as shown in FIG. 7, a reducing agent feeding means 16 in the form of a central lance 26 that is arranged inside the dispersing device 21 of the concentrate burner 5, wherein the central lance 26 comprising a discharge orifice 27 that opens to the reaction shaft 2.

[0096] The concentrate burner 5 may comprise, as shown in FIG. 8, a reducing agent feeding means 16 in the form of a reducing agent feeding means 16, wherein the reducing agent feeding means 16 comprising a nozzle 17 that opens into the reaction shaft 2 of the suspension smelting furnace 1.

[0097] It is apparent to a person skilled in the art that as technology advances, the basic idea of the invention can be implemented in various ways. The invention and its embodiments are therefore not restricted to the above examples, but they may vary within the scope of the claims.