Control of sulfides and coliphage MS2 using hydrogen peroxide and UV disinfection for non-potable reuse of pilot-scale anaerobic membrane bioreactor effluent

Anaerobic membrane bioreactors reduce the energy cost of wastewater treatment and meet filtration requirements for non-potable reuse. However, sulfides (H(2)S/HS(−)) formed during anaerobic treatment exert a high chlorine demand and inhibit UV disinfection by photon shielding at 254 nm. This study evaluated the feasibility of hydrogen peroxide (H(2)O(2)) for sulfide oxidation, UV disinfection for inactivation of MS2 bacteriophage, and chlorine to provide a residual for distribution. H(2)O(2) treatment at pH ≥ 8 favored sulfide oxidation to sulfate in 30 min at a 4:1 H(2)O(2):sulfide stoichiometry. Compared to a 6:1 H(2)O(2):sulfide molar ratio, treatment of anaerobic effluent with 0.5 mM sulfides with a 4:1 H(2)O(2):sulfide molar ratio would increase the applied UV fluence needed for 5-log MS2 inactivation from 180 mJ cm(−2) to 225 mJ cm(−2). However, the lower H(2)O(2) dose reduced the dose of chlorine needed to quench residual H(2)O(2) and provide a residual for distribution. Treatment at the 4:1 H(2)O(2):sulfide molar ratio was favored, because the cost savings in H(2)O(2) and chlorine reagents outweighed the energy savings associated with UV treatment. However, H(2)O(2)/UV/chlorine treatment of anaerobic effluent was cost-competitive with conventional treatment of aerobic effluent for non-potable reuse only for < 285 µM sulfides.