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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

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2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2021, Vol. 15 Issue (6) : 139    https://doi.org/10.1007/s11783-021-1433-3
RESEARCH ARTICLE
Insights into simultaneous anammox and denitrification system with short-term pyridine exposure: Process capability, inhibition kinetics and metabolic pathways
Shuhan Li1,2, Xin Zhou1,2(), Xiwei Cao1,2, Jiabo Chen1,2
1. College of Environmental Science and Engineering, Taiyuan University of Technology, Taiyuan 030024, China
2. Innovation Center for Postgraduate Education in Municipal Engineering of Shanxi Province, Taiyuan 030024, China
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Abstract

• Short-term effect of the pyridine exposure on the SAD process was investigated.

• The SAA at 150 mg/L pyridine reduced by 56.7% of the maximum value.

• Inhibition kinetics models and inhibitory parameters were indicated.

• Collaboration of AnAOB, HDB and PDB promoted the SAD.

• Possible metabolic pathways of nitrogen and pyridine were proposed.

In-depth knowledge on the role of pyridine as a bottleneck restricting the successful application of anammox-based process treating refractory coking wastewater remains unknown. In this study, the effect of short-term pyridine addition on a simultaneous anammox and denitrification (SAD) system fed with 25–150 mg/L pyridine was explored. The short-term operation showed that the highest total nitrogen (TN) removal efficiency was achieved at 25–50 mg/L of pyridine. As the pyridine addition increased, the contribution of the anammox pathway in nitrogen removal decreased from 99.3% to 79.1%, while the denitrification capability gradually improved. The specific anammox activity (SAA) at 150 mg/L pyridine decreased by 56.7% of the maximum SAA. The modified non-competitive inhibition model indicated that the 50% inhibitory concentration (IC50) of pyridine on anammox was 84.18 mg/L and the substrate inhibition constant (Ki) of pyridine for self-degradation was 135.19 mg/L according to the Haldane model. Moreover, high-throughput sequencing confirmed the abundance of Candidatus Kuenenia as the amount of anammox species decreased, while the amounts of denitrifiers and pyridine degraders significantly increased as the pyridine stress increased. Finally, the possible pathways of nitrogen bioconversion and pyridine biodegradation in the SAD system were elucidated through metagenomic analysis and gas chromatography/mass spectrometry results. The findings of this study enlarge the understanding of the removal mechanisms of complex nitrogenous pyridine-containing wastewater treated by the SAD process.

Keywords Anammox      Inhibition      Metabolic pathway      Microbial community      Pyridine      SAD     
Corresponding Author(s): Xin Zhou   
Issue Date: 20 April 2021
 Cite this article:   
Shuhan Li,Xin Zhou,Xiwei Cao, et al. Insights into simultaneous anammox and denitrification system with short-term pyridine exposure: Process capability, inhibition kinetics and metabolic pathways[J]. Front. Environ. Sci. Eng., 2021, 15(6): 139.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-021-1433-3
https://academic.hep.com.cn/fese/EN/Y2021/V15/I6/139
Fig.1  Pyridine biodegradation in the SAD at different pyridine concentrations. (a) concentration profile and (b) removal rates.
Fig.2  Concentration profiles of NH4+-N (a), NO2--N (b), NO3--N (c) and TN (d) in a 48-h experiment under different pyridine concentrations.
Pyridine (mg/L) DNH4+-N: DNO2--N: DNO3--N SAA
(mg NH4+-N /g VSS·h)
Contribution of anammox in TN removal (%) TN removal (%)
0 1:1.38:0.31 0.282 99.3 85.5
25 1:1.62:0.23 0.270 86.4 87.6
50 1:1.64:0.18 0.206 85.5 86.5
75 1:1.66:0.17 0.200 83.8 79.5
100 1:1.76:0.35 0.149 82.7 68.8
150 1:2.00:0.39 0.122 79.1 57.4
Tab.1  Stoichiometry ratios, SAA, contribution of anammox in TN removal and TN removal rate of the SAD system fed with different pyridine concentrations
Biomass type Substrate Concentration (mg/L) SAA
(mg TN /gVSS·h)
IC50 for anammox
(mg/L)
References
Anammox biofilm Pyridine 150 0.122a) 144.10 This study
Anammox granule Phenol 50 5.54 862 Jin et al., 2013b
Anammox granule Phenol 50 2.9 678.2 Yang et al., 2013
Anammox sludge Phenol 124.55 Peng et al., 2018
Anammox granule Quinoline 5 16.72 13.07 Chen et al., 2019
Anammox granule Quinoline 31 Ramos et al., 2015
Anammox granule o-Cresol 15 Ramos et al., 2015
Anammox granule p-Nitrophenol 82 Ramos et al., 2015
Anammox sludge Benzene 9.21 Peng et al., 2018
Anammox sludge Toluene 35.28 Peng et al., 2018
Anammox sludge Benzene, toluene 18.2 Peng et al., 2018
Anammox sludge Benzene, phenol 69.23 Peng et al., 2018
Anammox sludge Benzene, toluene, phenol 92.02 Peng et al., 2018
Tab.2  Comparisons of SAA and IC50 of typical organic compounds contained in coking wastewater on anammox
Fig.3  Haldane model fitted to experimental data of inhibitory growth exposed to pyridine.
Fig.4  Taxonomic classification of the bacterial communities. (a) phylum level and (b) genus level.
Fig.5  Percentages of key functional microbial bacteria under different pyridine concentrations.
Fig.6  RDA on the relationship between environmental factors and genera species at different initial pyridine concentrations.
Fig.7  Possible pathways of the SAD process based on metagenomic analysis: (a) nitrogen removal, (b) pyridine degradation.
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