Tri-sector regenerative oxidant preheater for oxy-fired pulverized coal combustion
View Patent ↗A tri-sector regenerative oxidant preheater apparatus, method and arrangement for utilization with oxy-fired pulverized coal combustion power plants. The preheater includes a stationary housing and a rotor rotatably mounted in the housing. Sector plates are located at the axial ends of the rotor and divide the preheater into a flue gas sector, two primary oxidant sectors, and a secondary oxidant sector interposed between the two primary oxidant sectors. A primary oxidant fan is located downstream of the preheater to create a negative environment in the primary oxidant sectors. During operation of the preheater, the environments of the two primary oxidant sectors and the flue gas sector are at about the same negative pressure, and thus there is very limited leakage between the oxidant side and the flue gas side of the preheater. The environment of the secondary oxidant sector is at a positive pressure and leakage to the negative environment of the primary oxidant sectors will be that of secondary oxidant to primary oxidant with no loss secondary oxidant to the gas side of the preheater.
1. A method for preheating primary and secondary oxidant in a tri-sector rotary regenerative oxidant preheater including a stationary housing, a rotor rotatably mounted in the housing, sector plates located at the axial ends of the rotor dividing the preheater into a flue gas sector, a secondary oxidant sector, and two primary oxidant sectors, the secondary oxidant sector being interposed between the primary oxidant sectors, the method comprising providing:
a tri-sector rotary regenerative oxidant preheater including a stationary housing, a rotor rotatably mounted in the housing, sector plates located at the axial ends of the rotor dividing the preheater into a flue gas sector, a secondary oxidant sector, and two primary oxidant sectors, the secondary oxidant sector being interposed between the primary oxidant sectors;
passing primary oxidant to be heated through the primary oxidant sectors;
passing secondary oxidant to be heated through the secondary oxidant sector;
passing hot flue gas through the flue gas sector to heat the primary and secondary oxidants; and
maintaining the environment in both primary oxidant sectors at about the same negative pressure as that of the flue gas sector; and
maintaining the environment in the secondary oxidant sector at a positive pressure.
2. A method according to claim 1 , including the step of maintaining the environment in both primary oxidant sectors at a negative pressure of about 5 inches wg.
3. A method according to claim 1 , including the step of maintaining the environment in wherein the secondary oxidant sector is maintained at a positive pressure of about 20 inches wg.
4. A method according to claim 1 , including the step of rotating the rotor in a clockwise direction.
5. A method according to claim 4 , including the step of sizing the primary oxidant sector bordering the leading edge of the rotor side 3 o'clock side of the flue gas sector to deliver a required primary oxidant temperature.
6. A method according to claim 1 , including the step of rotating the rotor in a counterclockwise direction.
7. A method according to claim 6 , including the step of sizing the primary oxidant sector bordering the leading edge of the rotor side 9 o'clock side of the flue gas sector to deliver a required primary oxidant temperature.
8. A method according to claim 1 , including the step of sizing the primary oxidant sectors to be of substantially equal size.
9. A method according to claim 1 , including the step of sizing the primary oxidant sectors so as together to deliver a required primary oxidant temperature.
10. A method according to claim 1 , including the step of sizing the secondary oxidant sector to deliver a required secondary oxidant temperature.