Method of controlling a boiler plant during switchover from air-combustion to oxygen-combustion
A method of controlling a boiler plant during a switchover period from an air-combustion mode to an oxygen-combustion mode. The method includes steps of feeding fuel into a furnace of the boiler plant at a rate determined by a fuel feeding scheme, feeding air into the furnace at a rate determined by a descending air feeding scheme, feeding substantially pure oxygen into the furnace at a rate determined by an ascending oxygen feeding scheme, and recirculating flue gas into the furnace at a rate determined by an ascending flue gas recirculating scheme. The fuel feeding scheme, the air feeding scheme and the oxygen feeding scheme are such that the fuel is combusted and the flue gas containing residual oxygen is produced. Also, the fuel feeding scheme, the air feeding scheme and the oxygen feeding scheme are such that the content of residual oxygen in the flue gas is, during at least a portion of the switchover period, greater than during any of the air-combustion mode and the oxygen-combustion mode. The method makes it possible to reduce CO 2 emissions and O 2 consumption quickly during the short switchover period.
1. A method of controlling a boiler plant during a switchover period from an air-combustion mode to an oxygen-combustion mode, the method comprising the steps of:
(a) feeding fuel into a furnace of the boiler plant at a rate determined by a fuel feeding scheme;
(b) feeding air into the furnace at a rate determined by a descending air feeding scheme;
(c) feeding substantially pure oxygen into the furnace at a rate determined by an ascending oxygen feeding scheme; and
(d) recirculating flue gas into the furnace at a rate determined by an ascending flue gas recirculating scheme,
wherein (i) the fuel feeding scheme, the air feeding scheme, and the oxygen feeding scheme are such that the fuel is combusted and flue gas containing residual oxygen is produced, (ii) the fuel feeding scheme, the air feeding scheme, and the oxygen feeding scheme are such that the content of the residual oxygen in the flue gas is, during at least a portion of the switchover period, greater than during any of the air-combustion mode and the oxygen-combustion mode, and (iii) the amount of the residual oxygen is, during at least a portion of the switchover period, at least 100% greater than during any one of the air-combustion mode and the oxygen-combustion mode.
2. The method according to claim 1 , wherein the amount of residual oxygen is, during at least a portion of the switchover period, at least 200% greater than during any one of the air-combustion mode and the oxygen-combustion mode.
3. The method according to claim 2 , wherein the amount of residual oxygen is, during at least a central fourth of the switchover period, at least 200% greater than during any of the air-combustion mode and the oxygen combustion mode.
4. The method according to claim 3 , wherein the amount of residual oxygen is, during at least a third of the switchover period, scheduled mostly at the second portion of the switchover period, at least 200% greater than during any of the air-combustion mode and the oxygen-combustion mode.
5. The method according to claim 1 , wherein the amount of residual oxygen is, during at least a central fourth of the switchover period, at least 100% greater than during any of the air-combustion mode and the oxygen-combustion mode.
6. The method according to claim 5 , wherein the amount of residual oxygen is, during at least a third of the switchover period, scheduled mostly at the second portion of the switchover period, at least 100% greater than during any of the air-combustion mode and the oxygen-combustion mode.
7. The method according to claim 1 , wherein the boiler plant comprises an oxygen storage, and, during the switchover period, at least a portion of the substantially pure oxygen is fed to the furnace from the oxygen storage.
8. The method according to claim 7 , wherein oxygen is stored into the oxygen storage during the air-combustion mode.
9. The method according to claim 1 , wherein the descending air feeding scheme deviates from a linear descent to zero by at most 40% of the air feeding rate at the beginning of the switchover period.
10. The method according to claim 9 , wherein the descending air feeding scheme deviates from a linear descent to zero by at most 20% of the air feeding rate at the beginning of the switchover period.
11. The method according to claim 1 , wherein the ascending flue gas recycling scheme deviates from a linear ascent from zero to a flue gas recycling rate at the beginning of the oxygen-combustion mode by at most 40% of the flue gas recycling rate at the beginning of the oxygen-combustion mode.
12. The method according to claim 11 , wherein the ascending flue gas recycling scheme deviates from a linear ascent from zero to a flue gas recycling rate at the beginning of the oxygen-combustion mode by at most 20% of the flue gas recycling rate at the beginning of the oxygen-combustion mode.
13. The method according to claim 1 , wherein the fuel feeding scheme is substantially constant and is equal to the fuel feeding rate at the beginning of the oxygen-combustion mode.
14. The method according to claim 1 , wherein the fuel feeding scheme, the air feeding scheme, the oxygen feeding scheme, and the flue gas recirculating scheme are such that deviations in the mass flow rate of the flue gas discharged from the furnace during the switchover period are within 10% of the average.