Oxy-combustion coal fired boiler and method of transitioning between air and oxygen firing
View Patent ↗A new and unique boiler and method of transition between air and Oxy-combustion in a coal fired combustion process wherein near pure oxygen may be introduced to the boiler furnace in several locations including directly into the flame through the burner and/or directly into the furnace as nearly pure oxygen, and/or into the recycle flue gas streams to the burners, including both primary and secondary streams.
1. A method of transitioning to oxy-combustion comprising:
providing a boiler;
combusting a fossil fuel in the presence of air to create a flue gas wherein a burner is provided with a primary air stream and a secondary air stream;
measuring a flue gas oxygen concentration at the boiler exit;
increasing the flue gas oxygen concentration at the boiler exit by introducing an oxygen stream to the burner;
opening a flue gas recycle damper;
providing an additional oxygen stream to an oxygen mixer;
creating a secondary oxygenated recycled flue gas by mixing the flue gas with the additional oxygen stream;
transitioning from the secondary air to the secondary oxygenated recycled flue gas by incrementally closing a secondary fresh air intake damper;
creating a primary oxygenated recycled flue gas by mixing the flue gas with the additional oxygen stream; and
transitioning from the primary air stream to the primary oxygenated recycled flue gas by incrementally closing a primary fresh air intake damper;
wherein the primary oxygenated recycled flue gas and the secondary oxygenated recycled flue gas are preheated via an air heater; and
wherein the primary oxygenated recycled flue gas and the secondary oxygenated recycled flue gas are created upstream of the air heater.
2. The method of claim 1 including the step of measuring an oxygen concentration of the primary oxygenated recycled flue gas downstream of a primary oxygen mixer.
3. The method of claim 2 including the step of measuring an oxygen concentration of secondary oxygenated recycled flue gas downstream of a secondary oxygen mixer.
4. The method of claim 3 wherein the oxygen concentration of secondary oxygenated recycled flue gas downstream of the secondary oxygen mixer is maintained between about 18 and about 28 percent during transition.
5. The method of claim 4 wherein the oxygen concentration of the primary oxygenated recycled flue gas downstream of the primary oxygen mixer is maintained between about 16 and about 23.5 percent during transition.
6. The method of claim 5 wherein the oxygen concentration of the flue gas at the boiler exit is maintained between about 2 and about 7 percent during transition.
7. The method of claim 6 wherein the transition to the secondary oxygenated recycled flue gas occurs before the transition to the primary oxygenated recycled flue gas.
8. The method of claim 6 wherein the transition to the primary oxygenated recycled flue gas occurs before the transition to the secondary oxygenated recycled flue gas.
9. The method of claim 6 wherein the transition to the primary oxygenated recycled flue gas occurs concurrently with the transition to the secondary oxygenated recycled flue gas.
10. The method of claim 6 wherein a primary oxygen mixer oxygenates both the primary oxygenated recycled flue gas and the secondary oxygenated recycled flue gas.
11. The method of claim 10 wherein a secondary oxygen mixer further oxygenates the secondary oxygenated recycled flue gas to a level higher that the primary oxygenated recycled flue gas.
12. The method of claim 11 wherein the oxygen concentration of the primary oxygenated recycled flue gas measured downstream of the primary oxygen mixer is maintained between about 16 and about 20 percent during transition.
13. The method of claim 12 wherein the oxygen concentration of the secondary oxygenated recycled flue gas measured downstream of the secondary oxygen mixer is maintained between about 18 and about 23 percent during transition.
14. The method of claim 13 including the step of closing a primary fresh air intake tight shut off damper once the primary fresh air intake damper is closed to minimize air infiltration.
15. The method of claim 14 including the step of closing a secondary fresh air intake tight shut off damper once the secondary fresh air intake damper is closed to minimize air infiltration.
16. The method of claim 14 wherein boiler load is maintained relatively constant during transition.
17. The method of claim 6 wherein the primary oxygenated recycled flue gas is heated in the air heater prior to reaching a pulverizer.
18. The method of claim 17 wherein the secondary oxygenated recycled flue gas is heated in the air heater prior to reaching a windbox.
19. A method of transitioning from oxy-combustion to air combustion comprising:
providing a boiler combusting a fossil fuel in the presence of oxygen to create a flue gas wherein a burner is provided with a primary oxygenated recycled flue gas stream and a secondary oxygenated recycled flue gas stream, wherein the primary oxygenated recycled flue gas stream and the secondary oxygenated recycled flue gas stream are preheated via an air heater;
reducing a flow of primary oxygen stream to a primary oxygen mixer;
transitioning from the primary oxygenated recycle stream to the primary air stream by opening a primary fresh air tight shut off valve and a primary fresh air intake damper;
reducing a flow of secondary oxygen to a secondary oxygen mixer;
transition from the secondary oxygenated recycle steam to the primary air stream by opening a secondary fresh air tight shut off valve and a secondary fresh air intake damper; and
closing a recycle damper;
wherein the primary oxygenated recycled flue gas and the secondary oxygenated recycled flue gas are created upstream of the air heater.
20. The method of claim 19 , wherein a flow of oxygen provided to the burner during oxy-combustion is shut-off after closing the recycle damper.