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

Michele Torregrossa; Santo Fabio Corsino

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

Michele Torregrossa, Santo Fabio Corsino

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Risultato della ricerca: Conference contribution

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.

Lingua originale	English
Titolo della pubblicazione ospite	91st Annual Water Environment Federation Technical Exhibition and Conference (WEFTEC 2018)
Numero di pagine	4
Stato di pubblicazione	Published - 2018

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title = "Anaerobic moving bed biofilm reactor followed by aerobic granular sludge for brewery wastewater treatment",

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.",

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T1 - Anaerobic moving bed biofilm reactor followed by aerobic granular sludge for brewery wastewater treatment

AU - Torregrossa, Michele

AU - Corsino, Santo Fabio

PY - 2018

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N2 - 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.

AB - 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.

UR - http://hdl.handle.net/10447/381194

M3 - Conference contribution

BT - 91st Annual Water Environment Federation Technical Exhibition and Conference (WEFTEC 2018)

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