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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.    2022, Vol. 16 Issue (3) : 34    https://doi.org/10.1007/s11783-021-1468-5
RESEARCH ARTICLE
Acid Orange 7 degradation using methane as the sole carbon source and electron donor
Yanan Bai1,2,3, Xiuning Wang4, Fang Zhang2, Raymond Jianxiong Zeng2,3,4()
1. School of Applied Meteorology, Nanjing University of Information Science and Technology, Nanjing 210044, China
2. Fujian Provincial Key Laboratory of Soil Environmental Health and Regulation, College of Resources and Environment, Fujian Agriculture and Forestry University, Fuzhou 350002, China
3. Advanced Laboratory for Environmental Research and Technology, USTC-CityU, Suzhou 215123, China
4. CAS Key Laboratory of Urban Pollutant Conversion, Department of Applied Chemistry, University of Science and Technology of China, Hefei 230026, China
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Abstract

• AO7 degradation was coupled with anaerobic methane oxidation.

• Higher concentration of AO7 inhibited the degradation.

• The maximum removal rate of AO7 reached 280 mg/(L·d) in HfMBR.

• ANME-2d dominated the microbial community in both batch reactor and HfMBR.

• ANME-2d alone or synergistic with the partner bacteria played a significant role.

Azo dyes are widely applied in the textile industry but are not entirely consumed during the dyeing process and can thus be discharged to the environment in wastewater. However, azo dyes can be degraded using various electron donors, and in this paper, Acid Orange 7 (AO7) degradation performance is investigated using methane (CH4) as the sole electron donor. Methane has multiple sources and is readily available and inexpensive. Experiments using 13C-labeled isotopes showed that AO7 degradation was coupled with anaerobic oxidation of methane (AOM) and, subsequently, affected by the initial concentrations of AO7. Higher concentrations of AO7 could inhibit the activity of microorganisms, which was confirmed by the long-term performance of AO7 degradation, with maximum removal rates of 8.94 mg/(L·d) in a batch reactor and 280 mg/(L·d) in a hollow fiber membrane bioreactor (HfMBR). High-throughput sequencing using 16S rRNA genes showed that Candidatus Methanoperedens, affiliated to ANME-2d, dominated the microbial community in the batch reactor and HfMBR. Additionally, the relative abundance of Proteobacteria bacteria (Phenylobacterium, Pseudomonas, and Geothermobacter) improved after AO7 degradation. This outcome suggested that ANME-2d alone, or acting synergistically with partner bacteria, played a key role in the process of AO7 degradation coupled with AOM.

Keywords Azo dyes      AO7 degradation      Anaerobic methane oxidation      Microbial community      ANME-2d     
Corresponding Author(s): Raymond Jianxiong Zeng   
Issue Date: 13 July 2021
 Cite this article:   
Yanan Bai,Xiuning Wang,Fang Zhang, et al. Acid Orange 7 degradation using methane as the sole carbon source and electron donor[J]. Front. Environ. Sci. Eng., 2022, 16(3): 34.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-021-1468-5
https://academic.hep.com.cn/fese/EN/Y2022/V16/I3/34
Fig.1  AO7 degradation coupled with methane oxidation in the methane group (AO7-13CH4) and nitrogen group (AO7-N2), and the ratio of 13CO2/(12CO2+13CO2) in the isotope tracer experiment.
Fig.2  AO7 degradation over six days with different initial AO7 concentrations (4, 8, 16, 25, 50, 100, and 160 mg/L).
Fig.3  (a) UV–Vis absorption spectra before and after AO7 degradation; (b) stoichiometric relationship between AO7 and ABA on day 0 and day 10.
Fig.4  AO7 degradation performance in batch experiments, expressed as AO7 concentration and AO7 removal rate.
Fig.5  (a) AO7 degradation performance of the HfMBR in the start-up stage; (b) The influent and effluent AO7 concentration in the continuous-flow stage; (c) AO7 removal rate, efficiency and loading rate in the continuous-flow stage.
Sample Total reads Average length Observed species Shannon ACE Chao1 Converage
Inoculum 93725 415 549 5.26 659 638 0.996
Batch reactor 85678 415 644 6.11 820 810 0.994
HfMBR 88232 411 562 5.67 711 717 0.995
Tab.1  Microbial community richness and Alpha diversity of samples in the inoculum, batch reactor, and HfMBR
Fig.6  Relative abundances of microorganisms in the inoculum, batch reactor, and HfMBR. (a) Phylum; (b) Genus.
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