A combination
of partial nitrification and nitrite-denitrifying
phosphorus removal and simultaneous nitrification-endogenous denitrification
(nDNPR-SNED) in two sequencing batch reactors was developed for synchronous
chemical oxygen demand (COD), nitrogen (N), and phosphorus (P) removal
by regulating dissolved oxygen (DO) and influent nitrite concentrations.
COD, total nitrogen, and P removal efficiencies of 87.4 ± 0.5,
91.6 ± 1.1, and 97.8 ± 0.6% were obtained after 112 days
of anaerobic/anoxic/aerobic operation. Mass balance analysis confirmed
that 91.9% of the COD was stored as intracellular carbon at the anaerobic
stage, and 99.6% of PO4
3––P and
99.8% of NO2
––N were eliminated
via the nDNPR process at the anoxic stage, and at the aerobic stage,
the SNED process contributed to 68.7% nitrogen removal. Genera of Candidatus Competibacter, Dechloromonas, Ellin6067, and Nitrospirae were the dominant consortia with a relative abundance of 26.5, 16.5,
1.0, and 1.1%, respectively. In the metabolic pathway model, β-hydroxybutyrate
was the main endogenous driving force for nitrogen and phosphorus
removal. Compared with conventional biological nitrogen and phosphorus
removal processes, the combined process could achieve 6.7% saving
in the total cost. The proposed approach provides an economic and
technical alternative for C-, N-, and P-laden wastewater treatment,
reducing both carbon demand and aeration consumption.