Method of controlling the thermal balance of the reaction shaft of a suspension smelting furnace and a concentrate burner
View Patent ↗The invention relates to a method of controlling the thermal balance of the reaction shaft of a suspension smelting furnace and to a concentrate burner for feeding reaction gas and pulverous solid mater into the reaction shaft of the suspension smelting furnace. In the method, endothermic material ( 16 ) is fed by the concentrate burner ( 4 ) to constitute part of the mixture formed from the powdery solid matter ( 6 ) and reaction gas ( 5 ), so that a mixture containing the powdery solid matter ( 6 ), reaction gas ( 5 ) and endothermic material ( 6 ) is formed in the reaction shaft ( 2 ). The concentrate burner ( 4 ) comprises cooling agent feeding equipment ( 15 ) for adding the endothermic material ( 16 ) to constitute part of the mixture, which is formed from the pulverous solid matter ( 6 ) that discharges from the orifice ( 8 ) of the feeder pipe and the reaction gas ( 5 ) that discharges through the annular discharge orifice ( 14 ).
1. A method of controlling thermal balance of a reaction shaft of a suspension smelting furnace, comprising
using a concentrate burner that comprises
a pulverous solid matter supply device for feeding pulverous solid matter into the reaction shaft, and
a gas supply device for feeding reaction gas into the reaction shaft,
the method comprising
feeding into the reaction shaft pulverous solid matter, and
feeding reaction gas into the reaction shaft for mixing reaction gas with pulverous solid matter to form a mixture by powdery solid matter and reaction gas in the reaction shaft of the suspension smelting furnace,
wherein
endothermic material is fed by the concentrate burner to constitute part of the mixture formed by powdery solid matter and reaction gas in the reaction shaft of the suspension smelting furnace, so that a mixture containing powdery solid matter, reaction gas and endothermic material is formed in the reaction shaft of the suspension smelting furnace;
and wherein the endothermic material is a liquid cooling agent.
2. A method according to claim 1 , wherein
endothermic material and pulverous solid matter is mixed outside the reaction shaft, and
mixture of endothermic material and pulverous solid matter is fed into the reaction shaft by means of the concentrate burner.
3. A method according to claim 1 , wherein
endothermic material is fed into the pulverous solid matter supply device and endothermic material and pulverous solid matter is mixed in pulverous solid matter supply device outside the reaction shaft,
mixture of endothermic material and pulverous solid matter is fed into the reaction shaft by means of the concentrate burner.
4. A method according to claim 1 , wherein
endothermic material and reaction gas is mixed outside the reaction shaft, and
mixture of endothermic material and reaction gas is fed into the reaction shaft by means of the concentrate burner.
5. A method according to claim 1 , wherein
endothermic material is fed into the gas supply device and endothermic material and reaction gas is mixed in the gas supply device outside the reaction shaft, and
mixture of endothermic material and reaction gas is fed into the reaction shaft by means of the concentrate burner.
6. A method according to claim 1 , wherein the concentrate burner is used that comprises a dispersing device for directing dispersion gas to pulverous solid matter in the reaction shaft for directing pulverous solid matter to reaction gas in the reaction shaft.
7. A method according to claim 6 , wherein
endothermic material and dispersion gas is mixed outside the reaction shaft, and
mixture of endothermic material and dispersion gas is fed into the reaction shaft by means of the concentrate burner.
8. A method according to claim 6 , wherein
endothermic material is fed into the dispersing device and endothermic material and dispersion gas is mixed in the dispersing device outside the reaction shaft, and
mixture of endothermic material and dispersion gas is fed into the reaction shaft by means of the concentrate burner.
9. A method according to claim 1 , comprising
where the concentrate burner that comprises
a pulverous solid matter supply device comprising a feeder pipe for feeding pulverous solid matter into the reaction shaft, where the orifice of the feeder pipe opens to the reaction shaft;
a dispersing device, which is arranged concentrically inside the feeder pipe and which extends to a distance from the orifice of the feeder pipe inside the reaction shaft and which comprises dispersion gas openings for directing a 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, the gas supply device opening to the reaction shaft through an annular discharge orifice that surrounds the feeder pipe concentrically for mixing reaction gas that discharges from the annular discharge orifice with pulverous solid matter, which discharges from the middle of the feeder pipe and which is directed to the side by means of dispersion gas;
the method comprising
feeding into the reaction shaft pulverous solid matter into the reaction shaft through the orifice of the feeder pipe of the concentrate burner;
feeding dispersion gas into the reaction shaft through the dispersion gas orifices of the dispersing device of the concentrate burner for directing dispersion gas to pulverous solid matter that flows around the dispersing device; and
feeding reaction gas into the reaction shaft through the annular discharge orifice of the gas supply device of the concentrate burner for mixing reaction gas with pulverous solid matter, which discharges from the middle of the feeder pipe and which is directed to the side by means of dispersion gas.
10. A method according to claim 9 , wherein endothermic material is fed through the dispersion gas openings of the dispersing device of the concentrate burner, so that dispersion gas that is to be fed at least partly consists of endothermic material.
11. A method according to claim 9 , wherein endothermic material is fed into the gas supply device of the concentrate burner, so that reaction gas, which discharges through the annular discharge orifice of the gas supply device that concentrically surrounds the feeder pipe of the concentrate burner, contains endothermic material.
12. A method according to claim 9 , wherein
cooling agent feeding equipment is arranged outside the gas supply device of the concentrate burner, comprising a cooling agent supply device, which comprises a second annular discharge orifice, which is concentric with the annular discharge orifice of the gas supply device of the concentrate burner and which opens to the reaction shaft of the suspension smelting furnace; and
endothermic material is fed through the said second annular discharge orifice into the reaction shaft of the suspension smelting furnace for mixing endothermic material with mixture of powdery solid matter and reaction gas.
13. A method according to claim 9 , wherein
a central lance is arranged inside the dispersing device of the concentrate burner, comprising a discharge orifice that opens to the reaction shaft of the suspension smelting furnace; and
endothermic material is fed through the discharge orifice of the central lance into the reaction shaft of the suspension smelting furnace for mixing endothermic material with mixture of powdery solid matter and reaction gas.
14. A method according to claim 9 , wherein endothermic material is fed into the pulverous solid matter supply device such that from the orifice of the feeder pipe mixture of pulverous solid matter and endothermic material discharged into the reaction shaft.
15. A method according to claim 1 , the endothermic material comprises at least one of a group consisting of: water, metallic salt, acid, and metallic sulfate.
16. A method according to claim 15 where the acid is sulfuric acid.
17. A method according to claim 15 where the metallic is copper sulfate or nickel sulfate.