文摘
We experimentally and numerically studied the pulverized-coal combustion process and NOx emissions for a 300 MWe wall-fired boiler burning bituminous coal. Measurements of the polar components of the gas velocity made with a particle-dynamics anemometer and calculated values are found to be in good agreement. Good agreement was also found for the CO2 concentration, NOx concentration, and combustible material content in the fly ash between simulation and industrial experiments performed on full-scale boilers. For enhanced ignition−dual register (EI−DR) burners, pulverized coal is spread widely from the burner. Some pulverized-coal particles are thrown to the furnace hopper, and much pulverized coal is swept to the furnace hopper at the bottom of the boiler. As the outer secondary-air vane angle increases, the temperature of the water-cooled tube wall region near the burners and furnace hopper increases. Changes in the NOx concentration at the furnace outlet are not simply linear with changes in the outer secondary-air vane angle. The NOx concentration at the furnace outlet was lowest (420.2 ppm at 6% O2) for an outer secondary-air vane angle of 35° and highest (468.2 ppm at 6% O2) for an outer secondary-air vane angle of 30°. This represents an increase of 11.4%.