Please wait a minute...
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 Envir Sci Eng Chin    2010, Vol. 4 Issue (4) : 490-499    https://doi.org/10.1007/s11783-010-0248-4
RESEARCH ARTICLE
Effect of the addition of organic carbon sources on nitrous oxide emission in anaerobic-aerobic (low dissolved oxygen) sequencing batch reactors
Hongjing LI1(), Xiurong CHEN2, Yinguang CHEN3
1. Department of Environmental Science and Engineering, Fudan University, Shanghai 200433, China; 2. School of Resource and Environmental Engineering, East China University of Science and Technology, Shanghai 200237, China; 3. School of Environmental Science and Engineering, Tongji University, Shanghai 200092, China
 Download: PDF(381 KB)   HTML
 Export: BibTeX | EndNote | Reference Manager | ProCite | RefWorks
Abstract

The effect of additional organic carbon sources on the production of nitrous oxide (N2O) in anaerobic-aerobic (low dissolved oxygen) real wastewater treatment system was investigated. In this paper, three laboratory-scale sequencing batch reactors (SBRs) (SBR-1, SBR-2 and SBR-3) were operating under an anaerobic-aerobic (low dissolved oxygen, 0.15–0.45 mg·L-1) configuration. The SBRs were ‘long-term cultured’ respectively with a single municipal wastewater sample, sodium acetate, and a waste-activated sludge alkaline fermentation liquid as the additional carbon sources of real wastewater. Off-gas analysis showed that N2O was emitted into the atmosphere during the aerobic (low dissolved oxygen) period in the three SBRs, and the order of N2O emission rate was SBR-2>SBR-1>SBR-3. It was observed that the higher poly-β-hydroxyvalerate fraction of polyhydroxyalkanoates, the lower glycogen transformation and less nitrite accumulation was in SBR-3, while the opposite behavior was observed in SBR-2. Further research indicated that the interaction of the factors above potentially affected the N2O emission in the anaerobic-aerobic (low dissolved oxygen) system.

Keywords anaerobic-aerobic (low dissolved oxygen)      nitrous oxide (N2O) emitting rate      municipal wastewater      waste activated sludge      alkaline fermentation liquid     
Corresponding Author(s): LI Hongjing,Email:lihongjing2371@163.com   
Issue Date: 05 December 2010
 Cite this article:   
Yinguang CHEN,Hongjing LI,Xiurong CHEN. Effect of the addition of organic carbon sources on nitrous oxide emission in anaerobic-aerobic (low dissolved oxygen) sequencing batch reactors[J]. Front Envir Sci Eng Chin, 2010, 4(4): 490-499.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-010-0248-4
https://academic.hep.com.cn/fese/EN/Y2010/V4/I4/490
Fig.1  

Typical variations of glycogen during one cycle of all three SBRs

Fig.2  

Typical variations of total PHA, PHB, PHV, and PH2MV during one cycle in three SBRs. (a) PHA; (b) PHB; (c) PHV; (d) PH2MV

Fig.3  

Comparison of TP concentrations in three anaerobic-aerobic (low DO) systems

Fig.4  

Typical variations of NH4+-N, NO3--N, NO2--N, and TN during one cycle in three SBRs. (a) NH4+-N; (b) NO3--N; (c) NO2--N; (d) TN

Fig.5  

Comparison of emitting rate of N2O in the aerobic (low DO) time among three SBRs

null

Note:*Unit is mg·L-1 except pH

Tab.1  

Main composition and their concentrations of real wastewater*

null

Note: * Unit of SCFAs is mg COD·L-1; soluble ortho-phosphate is abbreviated for SOP; soluble chemical oxygen demand is abbreviated for SCOD. **SCFAs were composed of acetic 1917, propionic 1725, n-butyric 568, iso-butyric 704, n-valeric 267, and iso-valeric acid 908 mg COD·L-1

Tab.2  

Variations of the main composition of alkaline fermentation liquid before and after phosphorus and nitrogen recovery

Tab.3  

Main carbon source and BOD5 concentrations in the influent of the three SBRs

null

Note: *The values given are the averages of the results from three different cycles and their standard deviations

Tab.4  

Anaerobic and aerobic (low DO) transformations of PHA and glycogen in the three SBRs (n = 3)*

null

Note: *The values given are the averages of the results from three different cycles and their standard deviations

Tab.5  

Comparison of nitrogen and phosphorus removal in three SBRs (n = 3)*

1 Tam N F Y, Leung G L W, Wong Y S. The effects of external carbon loading on nitrogen removal in sequencing batch reactors. Water Science and Technology , 1994, 30(6): 83-90
2 Guisasola A, Pijuan M, Baeza J A, Carrera J, Casas C, Lafuente J. Aerobic phosphorus release linked to acetate uptake in bio-P sludge: process modeling using oxygen uptake rate. Biotechnology and Bioengineering , 2004, 85(7): 722-733
3 Pijuan M, Saunders A M, Guisasola A, Baeza J A, Casas C, Blackall L L. Enhanced biological phosphorus removal in a sequencing batch reactor using propionate as the sole carbon source. Biotechnology and Bioengineering , 2004, 85(1): 56-67
4 Thomas M, Wright P, Blackall L, Urbain V, Keller J. Optimisation of Noosa BNR plant to improve performance and reduce operating costs. Water Science and Technology , 2003, 47(12): 141-148
5 Zeng R J, Lemaire R, Yuan Z, Keller J. A novel wastewater treatment process: simultaneous nitrification, denitrification and phosphorus removal. Water Science and Technology , 2004, 50(10): 163-170
6 de Kreuk M K, Heijnen J J, van Loosdrecht M C M. Simultaneous COD, nitrogen, and phosphate removal by aerobic granular sludge. Biotechnology and Bioengineering , 2005, 90(6): 761-769
7 Zeng R J, Lemaire R, Yuan Z, Keller J. Simultaneous nitrification, denitrification, and phosphorus removal in a lab-scale sequencing batch reactor. Biotechnology and Bioengineering , 2003, 84(2): 170-178
8 Meyer R L, Zeng R J, Giugliano V, Blackall L L. Challenges for simultaneous nitrification, denitrification, and phosphorus removal in microbial aggregates: mass transfer limitation and nitrous oxide production. FEMS Microbiology Ecology , 2005, 52(3): 329-338
9 J?nsson K, Johansson P, Christensson M, Lee N, Lie E, Welander T. Operational factors affecting enhanced biological phosphorus removal at the waste water treatment plant in Helsingborg, Sweden. Water Science and Technology , 1996, 34(1-2): 67-74
10 Moser-Engeler R, Udert K M, Wild D, Siegrist H. Products from primary sludge fermentation and their suitability for nutrient removal. Water Science and Technology , 1998, 38(1): 265-273
11 Tong J, Chen Y. Enhanced biological phosphorus removal driven by short-chain fatty acids produced from waste activated sludge alkaline fermentation. Environmental Science & Technology , 2007, 41(20): 7126-7130
12 Li H J, Chen Y G, Gu G. The effect of propionic to acetic acid ratio on anaerobic-aerobic (low dissolved oxygen) biological phosphorus and nitrogen removal. Bioresource Technology , 2008, 99(10): 4400-4407
13 Zheng X, Tong J, Li H J, Chen Y G. The investigation of effect of organic carbon sources addition in anaerobic-aerobic (low dissolved oxygen) sequencing batch reactor for nutrients removal from wastewaters. Bioresource Technology , 2009, 100(9): 2515-2520
14 Kimochi Y, Inamori Y, Mizuochi M, Xu K, Matsumura M. Nitrogen removal and N2O emission in a full-scale domestic wastewater treatment plant with intermittent aeration. Journal of Fermentation and Bioengineering , 1998, 86(2): 202-206
15 Kartal B, Kuypers M M, Lavik G, Schalk J, Op den Camp H J, Jetten M S, Strous M. Anammox bacteria disguised as denitrifiers: nitrate reduction to dinitrogen gas via nitrite and ammonium. Environmental Microbiology , 2007, 9(3): 635-642
16 Kampschreur M J, van der Star W R L, Wielders H A, Mulder J W, Jetten M S M, van Loosdrecht M C M. Dynamics of nitric oxide and nitrous oxide emission during full-scale reject water treatment. Water Research , 2008, 42(3): 812-826
17 Foley J, de Haas D, Yuan Z G, Lant P. Nitrous oxide generation in full-scale biological nutrient removal wastewater treatment plants. Water Research , 2010, 44(3): 831-844
18 Schulthess R V, Gujer W. Release of nitrous oxide (N2O) from denitrifying activated sludge: verification and application of a mathematical model. Water Research , 1996, 30(3): 521-530
19 Itokawa H, Hanaki K, Matsuo T. Nitrous oxide production in high-loading biological nitrogen removal process under low COD/N ratio condition. Water Research , 2001, 35(3): 657-664
20 Schalk-Otte S, Seviour R J, Kuenen J G, Jetten M S M. Nitrous oxide (N2O) production by Alcaligenes faecalis during feast and famine regimes. Water Research , 2000, 34(7): 2080-2088
21 Comeau Y, Hall K J, Oldham W K. Determination of poly-β-hydroxybutylate and poly-β-hydroxyvalerate in activated sludge by gas-liquid chromatography. Appl Environ Microbiol , 1988, 54(9): 2325-2327
22 Oehmen A, Keller-Lehmann B, Zeng R J, Yuan Z, Keller J. Optimisation of poly-β-hydroxyalkanoate analysis using gas chromatography for enhanced biological phosphorus removal systems. Journal of Chromatography. A , 2005, 1070(1-2): 131-136
23 Jenkins D, Richard M G, Daigger G T. Manual on the causes and control of activated sludge bulking, foaming and other solids separation problems, third ed., IWA publishing, London, UK, 2003
24 American Public Health Association (APHA). Standard Methods for the Examination of Water and Wastewater, 20th edition. American Public Health Association, Washington, DC, USA , 1998
25 Lemos P C, Viana C, Salgueiro E N, Ramos A M, Crespo J P S G, Reis M A M. Effect of carbon source on the formation of polyhydroxyalkanoates (PHA) by a phosphate-accumulating mixed culture. Enzyme and Microbial Technology , 1998, 22(8): 662-671
26 Mino T, Tsuzuki Y, Matsuo T. Effect of phosphorus accumulation on acetate metabolism in the biological phosphorus removal process. In: Ramadori R, Advances In Water Pollution Control, ed. Procceedings of IAWPRC International Conference on Biological Phosphate Removal from Wastewaters , Rome, Oxford pergamon press, 1987, 27-38
27 Wentzel M C, Lotter L H, Ekama G A, Loewenthal R E. Marais G v R. Evaluation of biochemical models for biological excess phosphorus removal. Water Science and Technology , 1991, 23: 567-576
28 Randall A A, Benefield L D, Hill W E, Nicol J, Boman G K, Jing S. The effect of volatile fatty acids on enhanced biological phosphorus removal and population structure in anaerobic/aerobic sequencing batch reactors. Water Science and Technology , 1997, 35(1): 153-160
30 Wu J, Zhang J, Jia W L, Xie H J, Gu R R, Li C, Gao B Y. Impact of COD/N ratio on nitrous oxide emission from microcosm wetlands and their performance in removing nitrogen from wastewater. Bioresource Technology , 2009, 100(12): 2910-2917
31 Hanaki K, Hong Z, Matsuo T. Production of nitrous oxide gas during denitrificaiton of wastewater. Water Science and Technology , 1992, 26(5-6): 1027-1036
32 Chen Y, Liu Y, Zhou Q, Gu G. Enhanced phosphorus biological removal from wastewater—effect of microorganism acclimatization with different ratios of short-chain fatty acids mixture. Biochemical Engineering Journal , 2005, 27(1): 24-32
doi: 10.1016/j.bej.2005.06.003
33 Oehmen A, Saunders A M, Vives M T, Yuan Z, Keller J. Competition between polyphosphate and glycogen accumulating organisms in enhanced biological phosphorus removal systems with acetate and propionate as carbon sources. Journal of Biotechnology , 2006, 123(1): 22-32
doi: 10.1016/j.jbiotec.2005.10.009
34 Zeng R J, Yuan Z, Keller J. Enrichment of denitrifying glycogen-accumulating organisms in anaerobic/anoxic activated sludge system. Biotechnology and Bioengineering , 2003, 81(4): 397-404
doi: 10.1002/bit.10484
35 Zhou Y, Pijuan M, Zeng R J, Yuan Z. Free nitrous acid inhibition on nitrous oxide reduction by a denitrifying-enhanced biological phosphorus removal sludge. Environmental Science & Technology , 2008, 42(22): 8260-8265
doi: 10.1021/es800650j
[1] Ling Wang, Chunxue Yang, Sangeetha Thangavel, Zechong Guo, Chuan Chen, Aijie Wang, Wenzong Liu. Enhanced hydrogen production in microbial electrolysis through strategies of carbon recovery from alkaline/thermal treated sludge[J]. Front. Environ. Sci. Eng., 2021, 15(4): 56-.
[2] Shengjie Qiu, Jinjin Liu, Liang Zhang, Qiong Zhang, Yongzhen Peng. Sludge fermentation liquid addition attained advanced nitrogen removal in low C/N ratio municipal wastewater through short-cut nitrification-denitrification and partial anammox[J]. Front. Environ. Sci. Eng., 2021, 15(2): 26-.
[3] Zhenlian Qi, Shijie You, Ranbin Liu, C. Joon Chuah. Performance and mechanistic study on electrocoagulation process for municipal wastewater treatment based on horizontal bipolar electrodes[J]. Front. Environ. Sci. Eng., 2020, 14(3): 40-.
[4] Yanqing Duan, Aijuan Zhou, Kaili Wen, Zhihong Liu, Wenzong Liu, Aijie Wang, Xiuping Yue. Upgrading VFAs bioproduction from waste activated sludge via co-fermentation with soy sauce residue[J]. Front. Environ. Sci. Eng., 2019, 13(1): 3-.
[5] Sijia Ai, Hongyu Liu, Mengjie Wu, Guangming Zeng, Chunping Yang. Roles of acid-producing bacteria in anaerobic digestion of waste activated sludge[J]. Front. Environ. Sci. Eng., 2018, 12(6): 3-.
[6] Yandong Yang,Liang Zhang,Hedong Shao,Shujun Zhang,Pengchao Gu,Yongzhen Peng. Enhanced nutrients removal from municipal wastewater through biological phosphorus removal followed by partial nitritation/anammox[J]. Front. Environ. Sci. Eng., 2017, 11(2): 8-.
[7] Leiyu FENG, Yuanyuan YAN, Yinguang CHEN. Co-fermentation of waste activated sludge with food waste for short-chain fatty acids production: effect of pH at ambient temperature[J]. Front Envir Sci Eng Chin, 2011, 5(4): 623-632.
[8] Tonggang SHEN, Hanchang SHI, Huiming SHI, He JING, Huilei XIONG. Feedforward control for nitrogen removal in a pilot-scale anaerobic-anoxic-oxic plant for municipal wastewater treatment[J]. Front Envir Sci Eng Chin, 2011, 5(1): 130-139.
[9] Zhiwei WANG, Qiaoying WANG, Zhichao WU, Xinhua WANG, . A hybrid membrane process for simultaneous thickening and digestion of waste activated sludge[J]. Front.Environ.Sci.Eng., 2010, 4(3): 272-279.
[10] Xia HUANG, Kang XIAO, Yuexiao SHEN. Recent advances in membrane bioreactor technology for wastewater treatment in China[J]. Front.Environ.Sci.Eng., 2010, 4(3): 245-271.
Viewed
Full text


Abstract

Cited

  Shared   
  Discussed