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- W2000525060 abstract "The performance of an anoxic/oxic membrane bioreactor system for the simultaneous removal of nitrogen and chemical oxygen demand (COD) was investigated. This process removed up to 87% of total nitrogen (TN) and 94% of COD, with the influent concentrations of 200 mg NH4+-N/L and 4000 mg COD/L and a recycle ratio (R) of 200%. Biological assimilation and simultaneous nitrification and denitrification (SND) were considered on nitrogen removal process. The TN removal efficiency was above 87.5%, while the nitrogen being removed through SND was above 75.5% and nitrogen assimilated into the biomass was below 24.5%, with influent concentration below 200 mg NH4+-N/L. Increasing the influent concentration to 400 mg NH4+-N/L, TN removal efficiency decreased significantly to 37.5%, of which 49.5% was provided by microorganism growth. Batch experiments provided evidence for the phenomena of SND. Furthermore, the SND removal efficiency increased gradually from 26.8 to 90.0%. © 2008 American Institute of Chemical Engineers Environ Prog, 2009" @default.
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- W2000525060 date "2009-04-01" @default.
- W2000525060 modified "2023-10-14" @default.
- W2000525060 title "Organic carbon and nitrogen removal in anoxic/oxic-membrane bioreactor treating high-strength wastewater" @default.
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- W2000525060 doi "https://doi.org/10.1002/ep.10288" @default.
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