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- W2014256935 abstract "A laboratory scale rotating biological contactor (RBC) predenitrification system incorporating anoxic and aerobic units was evaluated for the treatment of settled high-strength municipal wastewater. The system was operated under four recycle ratios (1, 2, 3 and 4) and loading rates of 38-182 gCOD/m(2)d and 0.22-14 gOxid-N/m(2)d on the anoxic unit and 3.4-18 gCOD/m(2)d and 0.24-1.8 gNH(4)-N/m(2)d on the aerobic. The average removal efficiency in terms of chemical oxygen demand (COD), biochemical oxygen demand (BOD(5)), total suspended solids (TSS) and total nitrogen (Total-N) was 82%, 86%, 63% and 54%; settling of the RBC effluent increased COD and TSS removal to 94% and 97%. An increase in hydraulic loading resulting from higher recirculation, had limited negative effect on organic removal but improved nitrogen removal, and in terms of Total-N removal efficiency increased up to a ratio of 3 and then decreased." @default.
- W2014256935 created "2016-06-24" @default.
- W2014256935 creator A5054172771 @default.
- W2014256935 date "2004-05-01" @default.
- W2014256935 modified "2023-09-23" @default.
- W2014256935 title "Organic and nitrogen removal in a two-stage rotating biological contactor treating municipal wastewater" @default.
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- W2014256935 doi "https://doi.org/10.1016/j.biortech.2003.06.005" @default.
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