Effect of Dissolved Oxygen and Chemical Oxygen Demand to Nitrogen Ratios on the Partial Nitrification/Denitrification Process in Moving bed Biofilm Reactors

Partial nitrification was reported to be technically feasible and economically favorable, especially for wastewaterwith high ammonium concentration or low C/N ratio. In this study, the effect of dissolved oxygen (DO)and influent ratio of chemical oxygen demand to nitrogen (COD/N) ratio on biological nitrogen removal fromsynthetic wastewater was investigated. Experiments were conducted in moving bed biofilm reactors(MBBRs) on partial nitrification process in pilot-plant configuration for 300 days. DO levels were changedfrom 0.04 to 0.12 and 0.42 to 3.4 mg/l in the anoxic (R1) and aerobic (R2) reactors, respectively. The optimum DO for partial nitrification was between 1-1.5 mg/l in the aerobic reactor (R2). Influent COD/N ratiosbetween 20 and 2 g COD/g-N were tested by changing the nitrogen loading rate (NLR) supplied to the pilotplant. During operational conditions when the DO concentration in aerobic reactor was above 1 mg/l, nearcomplete organic carbon removal occurred in the total MBBRs system. The effluent total nitrogen concentrationin the operational conditions (1.7-2.1 mg O2/l and NH+4-N=35.7 mg N/l) was obtained in the range of0.85-2 mg/l. The highest nitrite accumulation (50%-52%) took place at the DO concentration of 1-1.5 mg/land increased with decreasing COD/N ratio in aerobic reactor (R2). This study showed that the average nitrification rate at various COD/N ratios is about 0.96gN/m2 per day while the maximum nitrification rate isabout 2 gN/m2 per day at COD/N ratios lower than 6. The experimental COD/N ratio for denitrification wasclose to complete sum of NO2- and NO3- (NOx) removal efficiency (about 99%) at COD/N ratio equal14 in the operational conditions in the anoxic reactor (R1).