In this study, a sequencing batch reactor (SBR) connected with a two step a
naerobic digestion system is proposed in order to investigate the possibili
ty of simultaneous C, N and P removal from wastewater. The system was studi
ed using synthetic wastewater. In this system, the effluent of nitrate from
the SBR reactor is added to the acidogenic reactor influent. Nitrate elimi
nation and VFA production are then achieved together in the acidogenic reac
tor. The performances of three lab-scale reactors, operated for C, N and P
biological removal are analyzed. The removals of TOC, TN and TP-PO4 were gr
eater than 96%, 75% and 86%, respectively. The results show that the combin
ation of anaerobic digestion in two step-SBR treatment is effective for sim
ultaneous C, N and P removal. The benefits from this process are the saving
of carbon source for denitrification and phosphorus removal. Reactor arran
gement made possible the existence of zones where the different bacterial p
opulations involved could coexist. Complete denitrification occurs in acido
genic reactor and hence the methanogenic activity is not reduced nor inhibi
ted by N-NO3 presence, allowing greater TOC removal. A stable P-release and
P-uptake took place after coupling of the three reactors. Furthermore, a f
ast settling, compact sludge is generated in the SBR with the operational c
onditions applied. (C) 1999 Published by Elsevier Science Ltd on behalf of
the IAWQ. All rights reserved.