Method for converting a blast furnace plant
US-2023008316-A1 · Jan 12, 2023 · US
US9863013B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9863013-B2 |
| Application number | US-201113096161-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 28, 2011 |
| Priority date | Feb 22, 2011 |
| Publication date | Jan 9, 2018 |
| Grant date | Jan 9, 2018 |
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A method for heating a blast furnace stove includes combusting fuel in a combustion chamber in the stove, providing combustion gases from the combustion chamber to heat refractory material in the stove, recirculating exhausted combustion gases into the combustion chamber, enriching the combustion chamber with oxygen sufficient for maintaining combustion in the combustion chamber without damaging the refractory material in the stove.
Opening claim text (preview).
What is claimed is: 1. A method for heating a blast furnace stove, comprising: combusting fuel in a combustion chamber in the stove, providing combustion gases from the combustion chamber to heat refractory material in the stove, recirculating exhausted combustion gases into the combustion chamber, enriching the combustion chamber with oxygen, the enriching comprising delivering a balance of total oxygen required in an amount sufficient for maintaining combustion in the combustion chamber with at least one oxy-fuel burner in communication with the combustion chamber without damaging the refractory material in the stove. 2. The method of claim 1 , further comprising providing the combustion gases to the refractory material and recycling the combustion gases from the refractory material into the combustion chamber. 3. The method of claim 2 , further comprising mixing the recycled combustion gases with said oxygen for providing a recycled oxygen mixture to be introduced into the combustion chamber. 4. The method of claim 1 , wherein the fuel comprises a gaseous substance selected from blast furnace gas, converter top gas, coke oven gas, natural gas, propane, liquefied petroleum gases, and mixtures thereof. 5. The method of claim 1 , wherein the fuel comprises calorifically enriched blast furnace top gas. 6. The method of claim 1 , wherein maintaining the combustion is at a temperature below 1400° C. 7. The method of claim 1 , further comprising positioning the at least one oxy-fuel burner to fire across a flow stream provided to the combustion chamber from a burner of the stove in communication with the combustion chamber. 8. The method of claim 1 , further comprising operating the at least one oxy-fuel burner with a fuel selected from blast furnace gas, converter top gas, coke oven gas, natural gas, propane, liquefied petroleum gases, and mixtures thereof. 9. The method of claim 1 , further comprising operating the at least one oxy-fuel burner with at least one of substantially pure oxygen containing at least 85% oxygen or a blend of substantially pure oxygen diluted with recirculated flue gas. 10. The method of claim 1 , further comprising operating the at least one oxy-fuel burner with oxygen in excess of a stoichiometric combustion requirement of the fuel delivered through said at least one oxy-fuel burner. 11. The method of claim 1 , further comprising providing at least one oxygen lance in communication with the combustion chamber for delivering an oxidant including the balance of oxygen required for combustion in the combustion chamber. 12. The method of claim 11 , further comprising recirculating the combustion gases in the combustion chamber outside of a combustion region of the combustion chamber, supplying the oxidant to the combustion chamber at a high velocity through the at least one oxygen lance, and entraining the combustion gases in the combustion chamber for diluting a flame in the combustion chamber. 13. The method of claim 12 , wherein the high velocity of the oxidant is at a velocity of at least 200 m/s. 14. The method of claim 11 , further comprising delivering a stream of mixed oxygen and recycled flue gas through the at least one oxygen lance to the combustion chamber. 15. The method of claim 1 , further comprising supplying the fuel adjacent to the enriching the combustion chamber with oxygen, and entraining said fuel in the combustion gases. 16. The method of claim 1 , further comprising recycling a sufficient portion of the combustion gases to maintain gas mass flow per time unit through the refractory material at a level being at least equal to the gas mass flow per time unit used when the burner was operated without recycling. 17. The method of claim 1 , further comprising providing a main burner for the combustion chamber for combusting fuel in the combustion chamber and operating the at least one oxy-fuel burner for yielding an oxygen concentration less than 40% at the main burner.
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