Abstract: Simultaneous removal of SO_2 and NO from flue gas
by the highly active absorbent prepared from fly ash, lime and a few oxidizing
manganese compound additive was studied using a flue gas circulating fluidized
bed (CFB) under different experimental conditions. The effects influencing the
removal effiencies were discussed. The optimal flue gas temperature, flue gas
humidity, gas velocity of CFB and Ca/(S+N) molar ratio with this process
were approximately 110°C, 6%, 1.8 m/s and 1.05, respectively. Removal
efficiencies of 92.3% for SO_2 and 60.88% for NO were
obtained under the optimal experimental conditions. While the spent absorbent
appeared in the form of dry powder, the mechanism of removal for
SO_2 and NO based on the highly active absorbent was
investigated by a scanning electron microscope (SEM), a X-ray energy
spectrometer and the chemical analysis methods. The valuable references can be
provided for industrial application by the process. The foreground of
application will be vast in China and in the world.
Keywords: simultaneous desulfurization and denitrification, CFB, removal efficiency, mechanism