Biomass segregation between biofilm and flocs improves the control of nitrite-oxidizing bacteria in mainstream partial nitritation and anammox processes

Journal Article (2019)
Author(s)

Michele Laureni (Eawag - Swiss Federal Institute of Aquatic Science and Technology, ETH Zürich)

David G. Weissbrodt (TU Delft - OLD BT/Cell Systems Engineering, Aalborg University, TU Delft - Applied Sciences)

Kris Villez (Eawag - Swiss Federal Institute of Aquatic Science and Technology)

Orlane Robin (Eawag - Swiss Federal Institute of Aquatic Science and Technology)

Nadieh de Jonge (Aalborg University)

Alex Rosenthal (Northwestern University)

George Wells (Northwestern University)

Jeppe Lund Nielsen (Aalborg University)

Eberhard Morgenroth (ETH Zürich, Eawag - Swiss Federal Institute of Aquatic Science and Technology)

Adriano Joss (Eawag - Swiss Federal Institute of Aquatic Science and Technology)

Research Group
BT/Environmental Biotechnology
DOI related publication
https://doi.org/10.1016/j.watres.2018.12.051 Final published version
More Info
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Publication Year
2019
Language
English
Research Group
BT/Environmental Biotechnology
Volume number
154
Pages (from-to)
104-116
Downloads counter
290
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Institutional Repository
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Abstract


The control of nitrite-oxidizing bacteria (NOB) challenges the implementation of partial nitritation and anammox (PN/A) processes under mainstream conditions. The aim of the present study was to understand how operating conditions impact microbial competition and the control of NOB in hybrid PN/A systems, where biofilm and flocs coexist. A hybrid PN/A moving-bed biofilm reactor (MBBR; also referred to as integrated fixed film activated sludge or IFAS) was operated at 15 °C on aerobically pre-treated municipal wastewater (23 mg
NH4-N
L
−1
). Ammonium-oxidizing bacteria (AOB) and NOB were enriched primarily in the flocs, and anammox bacteria (AMX) in the biofilm. After decreasing the dissolved oxygen concentration (DO) from 1.2 to 0.17 mg
O2
L
−1
- with all other operating conditions unchanged - washout of NOB from the flocs was observed. The activity of the minor NOB fraction remaining in the biofilm was suppressed at low DO. As a result, low effluent NO
3


concentrations (0.5 mg
N
L
−1
) were consistently achieved at aerobic nitrogen removal rates (80 mg
N
L
−1
d
−1
) comparable to those of conventional treatment plants. A simple dynamic mathematical model, assuming perfect biomass segregation with AOB and NOB in the flocs and AMX in the biofilm, was able to qualitatively reproduce the selective washout of NOB from the flocs in response to the decrease in DO-setpoint. Similarly, numerical simulations indicated that flocs removal is an effective operational strategy to achieve the selective washout of NOB. The direct competition for NO
2


between NOB and AMX - the latter retained in the biofilm and acting as a “NO
2
-sink” - was identified by the model as key mechanism leading to a difference in the actual growth rates of AOB and NOB (i.e., μ
NOB
< μ
AOB
in flocs) and allowing for the selective NOB washout over a broad range of simulated sludge retention times (SRT = 6.8–24.5 d). Experimental results and model predictions demonstrate the increased operational flexibility, in terms of variables that can be easily controlled by operators, offered by hybrid systems as compared to solely biofilm systems for the control of NOB in mainstream PN/A applications.