Small and medium breweries discharging to municipal sewers without treatment generate significant loads with typical concentrations reported by Valta et al. (2014) as 2-6 g COD L-1, 25-80 mg TN L-1, 10-50 mg TP L-1, with pH between 4.5 and 12. Treatment of the high-strength wastewater requires specialized low footprint processes, such as aerobic granular sludge (AGS), capable of high-rate degradation, as well as simultaneous nitrogen and phosphorous removal (Wang et al., 2007). The objective of this study was to evaluate the start-up period of AGS receiving brewery wastewater after initial anaerobic pre-treatment.

di Biase A., Corsino S.F., Devlin T.R., Torregrossa M., Munz G., Oleszkiewicz J.A. (2018). Anaerobic moving bed biofilm reactor followed by aerobic granular sludge for brewery wastewater treatment. In 91st Annual Water Environment Federation Technical Exhibition and Conference (WEFTEC 2018).

Anaerobic moving bed biofilm reactor followed by aerobic granular sludge for brewery wastewater treatment

Corsino S. F.;Torregrossa M.;
2018-01-01

Abstract

Small and medium breweries discharging to municipal sewers without treatment generate significant loads with typical concentrations reported by Valta et al. (2014) as 2-6 g COD L-1, 25-80 mg TN L-1, 10-50 mg TP L-1, with pH between 4.5 and 12. Treatment of the high-strength wastewater requires specialized low footprint processes, such as aerobic granular sludge (AGS), capable of high-rate degradation, as well as simultaneous nitrogen and phosphorous removal (Wang et al., 2007). The objective of this study was to evaluate the start-up period of AGS receiving brewery wastewater after initial anaerobic pre-treatment.
2018
Anaerobic moving bed biofilm reactor; Aerobic granular sludge
di Biase A., Corsino S.F., Devlin T.R., Torregrossa M., Munz G., Oleszkiewicz J.A. (2018). Anaerobic moving bed biofilm reactor followed by aerobic granular sludge for brewery wastewater treatment. In 91st Annual Water Environment Federation Technical Exhibition and Conference (WEFTEC 2018).
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/10447/381194
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