초록 ▼

Fuel such as coal is combusted by feeding fuel and gaseous oxidant containing more than 21 vol. % oxygen, and preferably 21.8 to 29 vol. % oxygen, to a combustion stage at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx woul

Fuel such as coal is combusted by feeding fuel and gaseous oxidant containing more than 21 vol. % oxygen, and preferably 21.8 to 29 vol. % oxygen, to a combustion stage at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting the fuel and oxidant in said stage to produce combustion products and unburned fuel.

대표청구항 ▼

1. A method for combusting hydrocarbon fuel, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having a

1. A method for combusting hydrocarbon fuel, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, further comprising combusting said unburned fuel in a second combustion stage with additional gaseous oxidant comprised such that the average oxygen content of the oxidant fed to said first and second stages is in the range of 20.9-27.4 vol. % oxygen while removing sufficient heat from the combustion products and unburned fuel produced in said single or first stage to reach a temperature low enough to minimize additional formation of NOx in said combustion in said second stage. 2. A method according to claim 1 further comprising heating the oxidant before it is fed to said fuel rich region.3. A method according to claim 1 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.4. A method according to claim 1 wherein said fuel is coal.5. A method according to claim 4 further comprising heating the oxidant before it is fed to said fuel rich region.6. A method according to claim 4 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.7. A method according to claim 4 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.8. A method according to claim 4 wherein said gaseous oxidant is fed to said fuel rich region by feeding one stream or more than one stream of oxygen enriched air, or by feeding one stream or more than one stream of air and one stream or more than one stream of oxygen or oxygen-enriched air.9. A method according to claim 4 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.10. A method according to claim 1 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.11. A method according to claim 1 wherein said gaseous oxidant is fed to said fuel rich region by feeding one stream or more than one stream of oxygen enriched air, or by feeding one stream or more than one stream of air and one stream or more than one stream of oxygen or oxygen enriched air.12. A method according to claim 1 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.13. A method for retrofitting a furnace in which a hydrocarbon fuel is combusted in air as the only oxidant, so as to reduce the amount of NOx formed by the furnace compared to the amount of NOx formed by combustion of said fuel in said furnace with air as the only oxidant, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages of said furnace fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, further comprising combusting said unburned fuel in a second combustion stage with additional gaseous oxidant comprised such that the average oxygen content of the oxidant fed to said first and second stages is in the range of 20.9-27.4 vol. % oxygen while removing sufficient heat from the combustion products and unburned fuel produced in said single or first stage to reach a temperature low enough to minimize additional formation of NOx in said combustion in said second stage. 14. A method according to claim 13 further comprising heating the oxidant before it is fed to said fuel rich region.15. A method according to claim 13 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.16. A method according to claim 13 wherein said fuel is coal.17. A method according to claim 16 further comprising heating the oxidant before it is fed to said fuel rich region.18. A method according to claim 16 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.19. A method according to claim 16 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.20. A method according to claim 16 wherein said gaseous oxidant is fed to said fuel rich region by feeding one stream or more than one stream of oxygen-enriched air, or by feeding one stream or more than one stream of air and one stream or more than one stream of oxygen or oxygen enriched air.21. A method according to claim 16 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.22. A method according to claim 13 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.23. A method according to claim 13 wherein said gaseous oxidant is fed to said fuel rich region by feeding one stream or more than one stream of oxygen enriched air, or by feeding one stream or more than one stream of air and one stream or more than one stream of oxygen or oxygen enriched air.24. A method according to claim 13 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.25. A method for combusting hydrocarbon fuel, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, and feeding air downstream of said fuel rich region and combusting said unburned fuel in said air downstream of said fuel rich region, wherein said unburned fuel is combusted downstream of said fuel rich region with additional gaseous oxidant comprised such that the average oxygen content of the oxidant fed to said fuel rich region and said additional gaseous oxidant is in the range of 20.9-27.4 vol. % oxygen while removing sufficient heat from the combustion products and unburned fuel produced in the fuel rich region to reach a temperature low enough to minimize additional formation of NOx in said combustion of said unburned fuel. 26. A method according to claim 25 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.27. A method according to claim 25 wherein said gaseous oxidant is fed to said fuel rich region by feeding one stream or more than one stream of oxygen enriched air, or by feeding one stream or more than one stream of air and one stream or more than one stream of oxygen or oxygen enriched air.28. A method according to claim 25 further comprising heating the oxidant before it is fed to said fuel rich region.29. A method according to claim 25 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.30. A method according to claim 25 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.31. A method according to claim 25 wherein said fuel is coal.32. A method according to claim 31 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.33. A method according to claim 31 wherein said gaseous oxidant is fed to said fuel rich region by feeding one stream or more than one stream of oxygen-enriched air, or by feeding one stream or more than one stream of air and one stream or more than one stream of oxygen or oxygen enriched air.34. A method according to claim 31 further comprising heating the oxidant before it is fed to said fuel rich region.35. A method according to claim 31 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.36. A method according to claim 31 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.37. A method for combusting hydrocarbon fuel, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount. 38. A method according to claim 37 further comprising heating the oxidant before it is fed to said fuel rich region.39. A method according to claim 37 wherein said fuel is coal.40. A method according to claim 39 further comprising heating the oxidant before it is fed to said fuel rich region.41. A method according to claim 39 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.42. A method according to claim 39 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.43. A method according to claim 37 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.44. A method according to claim 37 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.45. A method for retrofitting a furnace in which a hydrocarbon fuel is combusted in air as the only oxidant, so as to reduce the amount of NOx formed by the furnace compared to the amount of NOx formed by combustion of said fuel in said furnace with air as the only oxidant, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages of said furnace fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount. 46. A method according to claim 45 further comprising heating the oxidant before it is fed to said fuel rich region.47. A method according to claim 45 wherein said fuel is coal.48. A method according to claim 47 further comprising heating the oxidant before it is fed to said fuel rich region.49. A method according to claim 47 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.50. A method according to claim 47 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.51. A method according to claim 47 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.52. A method according to claim 45 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.53. A method for combusting hydrocarbon fuel, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, and feeding air downstream of said fuel rich region and combusting said unburned fuel in said air downstream of said fuel rich region, wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount. 54. A method according to claim 53 further comprising heating the oxidant before it is fed to said fuel rich region.55. A method according to claim 53 wherein said fuel is coal.56. A method according to claim 55 further comprising heating the oxidant before it is fed to said fuel rich region.57. A method according to claim 55 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.58. A method according to claim 55 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.59. A method according to claim 53 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.60. A method according to claim 53 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.61. A method for combusting hydrocarbon fuel, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, further comprising combusting said unburned fuel in a second combustion stage downstream of said first stage with additional gaseous oxidant comprised such that the average oxygen content of the oxidant fed to said first and second stages is in the range of 20.9-27.4 vol. % oxygen while removing sufficient heat from the combustion products and unburned fuel produced in said single or first stage to reach a temperature low enough to minimize additional formation of NOx in said combustion in said second stage. 62. A method according to claim 61 further comprising heating the oxidant before it is fed to said fuel rich region.63. A method according to claim 61 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.64. A method according to claim 61 wherein said fuel is coal.65. A method according to claim 64 further comprising heating the oxidant before it is fed to said fuel rich region.66. A method according to claim 64 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.67. A method according to claim 64 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.68. A method according to claim 64 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.69. A method according to claim 61 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.70. A method according to claim 61 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.71. A method for retrofitting a furnace in which a hydrocarbon fuel is combusted in air as the only oxidant, so as to reduce the amount of NOx formed by the furnace compared to the amount of NOx formed by combustion of said fuel in said furnace with air as the only oxidant, comprising:feeding into the fuel rich region of a single combustion stage or the fuel rich region of the first combustion stage of first and second combustion stages of said furnace fuel containing one or more nitrogenous hydrocarbon compound and gaseous oxidant having an average oxygen concentration of more than 21 vol. % oxygen, at a stoichiometric ratio below that at which, if the stage were operated with air as the only oxidant, the same amount of NOx would be produced, and combusting said fuel with said gaseous oxidant in said single or first combustion stage to produce combustion products and unburned fuel, further comprising combusting said unburned fuel in a second combustion stage downstream of said first stage with additional gaseous oxidant comprised such that the average oxygen content of the oxidant fed to said first and second stages is in the range of 20.9-27.4 vol. % oxygen while removing sufficient heat from the combustion products and unburned fuel produced in said single or first stage to reach a temperature low enough to minimize additional formation of NOx in said combustion in said second stage. 72. A method according to claim 71 further comprising heating the oxidant before it is fed to said fuel rich region.73. A method according to claim 71 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.74. A method according to claim 71 wherein said fuel is coal.75. A method according to claim 74 further comprising heating the oxidant before it is fed to said fuel rich region.76. A method according to claim 74 wherein the stoichiometric ratio in said fuel rich region is below that at which, if the fuel rich region were operated with air as the only oxidant, the same amount of NOx would be produced, but is at least the lower stoichiometric ratio at which the amount of NOx formed by combustion of said fuel with said oxidant under otherwise identical conditions is said same amount.77. A method according to claim 74 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.78. A method according to claim 74 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.79. A method according to claim 71 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 21.8 vol. %.80. A method according to claim 71 wherein the average oxygen concentration of the oxidant fed to said fuel rich region is up to 24.8 vol. %.