Tertiary air addition to solid waste-fired furnaces for NOx control
Through the addition of tertiary air and a reduction of secondary air, NOx emissions from a waste-to-energy (WTE) boiler may be reduced. The tertiary air is added to the WTE at a distance from the secondary air, in a boiler region of relatively lower temperatures. A secondary NOx reduction system, such as a selective non-catalytic reduction (SNCR) system using ammonia or urea, may also be added to the boiler with tertiary air to achieve desirable high levels of NOx reductions. The SNCR additives are introduced to the WTE boiler proximate to the tertiary air.
1. A waste combustion system for reducing NOx emission, the system comprising:
a furnace, said furnace comprising a grate supporting a combusting waste bed, a primary air source introducing primary air upstream from the grate, at least one secondary nozzle introducing secondary air downstream from the combusting waste bed, and at least one tertiary nozzle introducing tertiary air, the at least one tertiary nozzle located at a distance downstream from said at least one secondary nozzle;
a continuous emissions monitoring system configured to monitor NOx emissions from the furnace;
a controller configured to receive measurements from the continuous emissions monitoring system and to dynamically adjust the allocation of the secondary air and the tertiary air in response to said measurements so as to reduce the NOx emissions from the furnace, while simultaneously minimizing thermal degradation of a wall of the furnace,
wherein the secondary air enters the furnace system at a velocity such that it causes only negligible mixing in the furnace;
a selective non-catalytic reduction (SNCR) system, the SNCR system comprising at least one SNCR nozzle configured to inject a reagent into the furnace, said at least one SNCR nozzle positioned downstream from the at least one tertiary air nozzle;
wherein the at least one SNCR nozzle is located within a turbulence zone generated by the at least one tertiary air nozzle to improve the mixing and reaction effectiveness of the reagent introduced by the SNCR system; and
wherein the controller is further configured to dynamically adjust the allocation of the secondary air and the tertiary air so as to improve effectiveness of the reagent introduced by the SNCR system.
2. The system of claim 1 , wherein the temperature near the at least one tertiary nozzle is less than about 2000° F.
3. The system of claim 1 , wherein the controller is further configured to dynamically adjust the allocation of the primary air to the primary air source.
4. The system of claim 1 , wherein the controller is further configured to dynamically adjust the amounts of the secondary air and the tertiary air to minimize Oxygen levels in the furnace upstream of the at least one tertiary air nozzle.
5. The system of claim 1 , wherein the secondary air stays close to a wall of the furnace to protect the wall from high temperatures.
6. The system of claim 1 , wherein the temperature near the at least one secondary nozzle is from about 2000° F. to about 2500° F.
7. The system of claim 1 , wherein the oxygen concentration between the at least one secondary nozzle and the at least one tertiary nozzle is nearly stoichiometric.
8. The system of claim 1 , wherein an amount of air present between the at least one secondary nozzle and the at least one tertiary nozzle exceeds stoichiometric conditions by about 10% to about 30%.