Abstract
An anoxic moving bed biofilm reactor (ANMBBR) followed by an aerobic moving bed biofilm reactor (AEMBBR) operated as pre-denitrification system was used to investigate the effect of different influent NO3 −-N concentrations on performance of the pre-denitrification system in treating real coal gasification wastewater. Influent NO3 −-N concentration was controlled at 50, 100, 200, and 400 mg/L during the experiments. Evolution of COD and phenols in the effluent of the ANMBBR and AEMBBR, and performance of nitrification in the AEMBBR with different influent NO3 −-N concentrations were studied. Almost complete denitrification was achieved when influent NO3 −-N concentration was 100 mg/L. NO3 −-N and NO2 −-N accumulated in the effluent of the ANMBBR with influent NO3 −-N concentrations of 200 and 400 mg/L. NO3 −-N concentration of 400 mg/L facilitated high NH4 +-N removal efficiency in the AEMBBR when influent NH4 +-N concentration was around 165 mg/L. The ratio of CODconsumed/NO3 −-Nconsumed along with phenols removal of the ANMBBR under different influent NO3 −-N concentrations was discussed.
Acknowledgments
This work was supported by National High Technology Research Development Plan (863) of China (No. 2007AA06A411).