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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2023, Vol. 17 Issue (6) : 68    https://doi.org/10.1007/s11783-023-1668-2
RESEARCH ARTICLE
Methanation and chemolitrophic nitrogen removal by an anaerobic membrane bioreactor coupled partial nitrification and Anammox
Qian Li1,3, Zhaoyang Hou1, Xingyuan Huang1, Shuming Yang1, Jinfan Zhang1, Jingwei Fu1, Yu-You Li2, Rong Chen1,3()
1. Key Laboratory of Environmental Engineering of Shaanxi Province, Xi’an University of Architecture and Technology, Xi’an 710055, China
2. Department of Civil and Environmental Engineering, Graduate School of Engineering, Tohoku University, Sendai Miyagi 980-8579, Japan
3. International S&T Cooperation Center for Urban Alternative Water Resources Development, Key Laboratory of Northwest Water Resource, Environment and Ecology (Ministry of Education), Xi’an University of Architecture and Technology, Xi’an 710055, China
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Abstract

● Efficient carbon methanation and nitrogen removal was achieved in AnMBR-PN/A system.

● AOB outcompeted NOB in PN section by limiting aeration and shortening SRT.

● The moderate residual organic matter of PN section triggered PD in anammox unit.

● AnAOB located at the bottom of UASB played an important role in nitrogen removal.

An AnMBR-PN/A system was developed for mainstream sewage treatment. To verify the efficient methanation and subsequent chemolitrophic nitrogen removal, a long-term experiment and analysis of microbial activity were carried out. AnMBR performance was less affected by the change of hydraulic retention time (HRT), which could provide a stable influent for subsequent PN/A units. The COD removal efficiency of AnMBR was > 93% during the experiment, 85.5% of COD could be recovered in form of CH4. With the HRT of PN/A being shortened from 10 to 6 h, nitrogen removal efficiency (NRE) of PN/A increased from 60.5% to 80.4%, but decreased to 68.8% when the HRTPN/A further decreased to 4 h. Microbial analysis revealed that the highest specific ammonia oxidation activity (SAOA) and the ratio of SAOA to specific nitrate oxidation activity (SNOA) provide stable NO2-N/NH4+-N for anammox, and anammox bacteria (mainly identified as Candidatus Brocadia) enriched at the bottom of Anammox-UASB might play an important role in nitrogen removal. In addition, the decrease of COD in Anammox-UASB indicated partial denitrification occurred, which jointly promoted nitrogen removal with anammox.

Keywords Anaerobic membrane bioreactor      Partial nitrification/Anammox      Carbon separation      Chemolitrophic nitrogen removal     
Corresponding Author(s): Rong Chen   
Issue Date: 22 December 2022
 Cite this article:   
Qian Li,Zhaoyang Hou,Xingyuan Huang, et al. Methanation and chemolitrophic nitrogen removal by an anaerobic membrane bioreactor coupled partial nitrification and Anammox[J]. Front. Environ. Sci. Eng., 2023, 17(6): 68.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-023-1668-2
https://academic.hep.com.cn/fese/EN/Y2023/V17/I6/68
Time (d) HRTAnMBR (h) HRTPN (h) HRTAnammox (h) HRTPN/A (h) HRTTotal (h)
1–33 16 3.3 6.7 10 26
34–89 12 2.7 5.3 8 20
90–166 10 2.0 4.0 6 16
167–217 7 1.3 2.7 4 11
Tab.1  Operating conditions of the AnMBR-PN/A
Fig.1  (a) COD removal performance in the AnMBR-PN/A; (b) the proportion of CH4 and CO2 in the biogas; (c) total nitrogen removal performance in PN/A.
HRTTotal (h) HRTAnMBR (h) HRTPN/A (h) Proportion of CH4 in biogas of AnMBR (%) COD removal efficiency of AnMBR (%) COD removal efficiency of AnMBR-PN/A (%) NRE of AnMBR-PN/A (%)
26 16 10 84.7±3.5 93.2±4.5 97.1±0.6 60.6±4.2
20 12 8 86.2±2.1 95.9±1.9 97.3±1.3 74.9±4.0
16 10 6 85.8±1.6 93.3±4.7 96.2±4.1 80.4±2.9
11 7 4 86.0±1.9 94.2±2.4 96.8±0.9 68.8±3.1
Tab.2  Conversion and removal effects of COD and nitrogen under different HRTs
Fig.2  (a) Nitrogen concentrations and the NO2-N/NH4+-N value of the PN-SBR effluent at various HRTs; (b) nitrogen concentrations, ΔNO2-N/ΔNH4+-N, and ΔNO3-N/ΔNH4+-N of the Anammox-UASB at various HRTs.
Fig.3  (a) Specific microbial activity of AOB and NOB in the PN-SBR; (b) relative abundance of major microorganisms in the PN-SBR when HRTPN/A was 6 h.
Fig.4  Microbial activity in the Anammox-UASB: (a) UASB upper (27 cm), (b) UASB middle (17 cm), (c) UASB bottom (0 cm).
Fig.5  Relative abundance of major microorganisms in the Anammox-UASB system when HRTPN/A was 6 h. Numbers on the branches of the phylogenetic tree indicate the branch distance. On the horizontal axis, US, UZ, and UX, respectively, indicate that the samples are taken from the upper, middle, and bottom of the UASB.
Fig.6  Spatial distribution of functional microorganisms in the PN-SBR and Anammox-UASB.
Fig.7  COD and nitrogen conversion paths in the AnMBR-PN/A system.
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