CHARACTERISTICS OF DENITRIFYING PHOSPHORUS REMOVAL AND N2O EMISSION OF AN AOA-SBR UNDER DIFFERENT CARBON TO NITROGEN RATIOS (C/N)
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摘要: 通过逐步减少外加碳源降低进水碳氮比(C/N)、降低好氧曝气速率、延长好氧和缺氧阶段停留时间的方式,在厌氧/好氧/缺氧交替运行的SBR反应器(AOA-SBR)内,成功实现了生活污水同步脱氮除磷过程(SNDPR),并利用化学计量学方法考察了不同反应条件下AOA-SBR内PAOs、GAOs间竞争特性,确定了系统脱氮除磷性能及N2O释放。结果表明:C/N降低同时减少好氧曝气量,增加好氧停留时间,有利于AOA-SBR内PAOs增殖,促进了反硝化除磷过程;C/N由7.0降至3.3,反应器平均TN去除率均达到80%以上,平均TP去除率则由65.2%增至81.2%。不同C/N条件下,AOA-SBR内厌氧、缺氧、好氧阶段微生物内源物质变化均呈现PAOs-GAOs共存特性,高COD/N条件下(COD/N=7.0),AOA-SBR倾向于富集GAOs的内源物质变化特性。高C/N条件促进了DGAOs内源反硝化过程,N2O释放量增加,低COD/N条件下(COD/N=3.0),DPAOs大量增殖,DGAOs-DGAOs两者耦合内源反硝化过程,促进了N2O还原,减少了N2O释放;C/N由7.0降至3.3,N2O释放量由2.23 mg/L降至1.05 mg/L,产率由7.21%降至3.94%。DGAOs内源反硝化与DPAOs反硝化除磷过程协同,能够充分利用原水中碳源,破解城市生活污水脱氮瓶颈。Abstract: In the paper, the simultaneous nitrogen and phosphorus removal process (SNDPR) of domestic sewage was accomplished in the anaerobic/aerobic/anaerobic SBR (AAO-SBR) by gradually reducing the external carbon source addition, to reduce the carbon nitrogen ratio (C/N) of influent water, reducing the aerobic aeration rate, and increasing the residence time of aerobic and anoxic stages. The competition between PAOs and GAOs in AOA-SBR under different reaction conditions was investigated by the stoichiometric method, and the nitrogen and phosphorus removal performance, as well as the N2O emission ratio of the system were determined. The results showed that reducing the aerobic aeration rate and increasing the aerobic residence time were conducive to the proliferation of PAOs in AOA-SBR under the condition of low carbon to nitrogen ratio, which promoted denitrification and phosphorus removal. When the C/N ratio decreased from 7.0 to 3.3, the average TN removal rate reached more than 80%, and the average TP removal rate increased from 65.2% to 81.2%. Under different C/N conditions, the changes of microbial endogenous substances in AOA-SBR at anaerobic, anoxic and aerobic stages showed the coexistence characteristics of PAOs-GAO. AOA-SBR tended to enrich the characteristics of GAOs endogenous substances at a higher C/N. Higher C/N condition promoted the endogenous denitrification process of DGAOs and increased the release of N2O, and lower C/N promoted the proliferation of DPAOs. The coupled endogenous denitrification process of DGAOs-DGAOS promoted the reduction of N2O, which reduced the emission of N2O. As the C/N decreased from 7.0 to 3.3, the N2O release decreased from 2.23 to 1.05 mg/L, and the emission ratio decreased from 7.21% to 3.94%. The collaboration between DGAOs endogenous denitrification and DPAOs endogenous denitrification phosphorus removal processes can make full use of carbon sources in raw domestic sewage, which may break the bottleneck of nitrogen removal in urban domestic sewage.
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[1] HUANG X, ZHU J, DUAN W Y, et al. Biological nitrogen removal and metabolic characteristics in a full-scale two-staged anoxic-oxic(A/O) system to treat optoelectronic wastewater[J]. Bioresource Technology, 2020, 300: 122595. [2] 李易寰,奚蕾蕾,钟奕杰,等. 倒置A2/O工艺运行效果及优化控制方案[J]. 环境工程,2020,38(3):76-81. [3] 赵伟华,王梅香,李健伟,等. A2O工艺和A2O+BCO工艺的脱氮除磷性能比较[J]. 中国环境科学,2019,39(3):994-999. [4] 陈诗,彭来,徐一峰,等. 废水生物脱氮过程中N2O排放数学模型研究进展[J]. 环境工程,2022,40(6):97-106,122. [5] 康华,李红艳,龙北生,等.改进型A2NSBR工艺参数及其除磷脱氮特性[J].环境工程,2023,41(4):123-130. [6] LUO Y H, YI K, ZHANG X Y, et al. Simultaneous partial nitrification, denitrification, and phosphorus removal in sequencing batch reactors via controlled reduced aeration and short-term sludge retention time decrease[J]. Journal of Environmental Management,2023,344:118598. [7] LI D Y, GUO W, LIANG D B, et al. Rapid start-up and advanced nutrient removal of simultaneous nitrification, endogenous denitrification and phosphorus removal aerobic granular sequence batch reactor for treating low C/N domestic wastewater[J]. Environmental Research, 2022,212:113464. [8] RUBIO-RINCON F J, LOPEZ-VAZQUES C M, WELLES L, et al. Cooperation between Candidatus competibacter and Candidatus accumulibacter clade Ⅰ, in denitrification and phosphate removal processes[J]. Water Research, 2017, 120: 156-164. [9] FAN Z W, ZENG W, WANG B G, et al. Microbial community at transcription level in the synergy of GAOs and Candidatus accumulibacter for saving carbon source in wastewater treatment[J]. Bioresource Technology, 2020, 297: 122454. [10] WANG X X, WANG S Y, ZHAO J, et al. Combining simultaneous nitrification-endogenous denitrification and phosphorus removal with post-denitrification for low carbon/nitrogen wastewater treatment[J]. Bioresource Technology, 2016, 220: 17-25. [11] WANG X X, WANG S Y, XUE T L,et al.Treating low carbon/nitrogen (C/N) wastewater in simultaneous nitrification-endogenous denitrification and phosphorous removal (SNDPR) systems by strengthening anaerobic intracellular carbon storage[J]. Water Research, 2015,77:191-200. [12] SUN Z Y, LV Y K, LIU Y X, et al. Removal of nitrogen by heterotrophic nitrification-aerobic denitrification of a novel metal resistant bacterium Cupriavidus sp. S1[J]. Bioresource Technology, 2016,220:142-150. [13] ZHANG J H, ZHANG Q, LI X Y, et al. Rapid start-up of partial nitritation and simultaneously phosphorus removal (PNSPR) granular sludge reactor treating low-strength domestic sewage[J]. Bioresource Technology, 2017,243:660-666. [14] HU T T, PENG Y Z, YUAN C S, et al. Enhanced nutrient removal and facilitating granulation via intermittent aeration in simultaneous partial nitrification endogenous denitrification and phosphorus removal (SPNEDpr) process[J]. Chemosphere, 2021,285:131443. [15] RIBERA-GUARDIA A, MARQUES R, ARANGIO C, et al. Distinctive denitrifying capabilities lead to differences in N2O production by denitrifying polyphosphate accumulating organisms and denitrifying glycogen accumulating organisms[J]. Bioresource Technology, 2016, 219: 106-113. [16] APHA(American Public Health Association). Standard Methods for the Examination of Water and Wastewater[M]. Baltimore: Port City Press, 1998. [17] OEHMEN A, KELLER B, ZENG R J, et al. Optimisation of poly-beta-hydroxyalkanoate analysis using gas chromatography for enhanced biological phosphorus removal systems[J]. Journal of Chromatography A, 2005, 107(1/2): 131-136. [18] OEHMEN A, ZENG R J, YUAN Z, et al. Anaerobic metabolism of propionate by polyphosphate-accumulating organisms in enhanced biological phosphorus removal systems[J]. Biotechnology and Bioengineering, 2005, 91(1): 43-53. [19] YANG Q, LIU X H, PENG C Y, et al. N2O production during nitrogen removal via nitrite from domestic wastewater: main sources and control method[J]. Environmental Science & Technology, 2009,43(24): 9400-9406. [20] CARVALHEIRA M, OEHEMEN A, CARVALHO G, et al. Survival strategies of polyphosphate accumulating organisms and glycogen accumulating organisms under conditions of low organic loading[J]. Bioresource Technology, 2014,172: 290-296. [21] DAN Q P, PENG Y Z, WANG B, et al. Side-stream phosphorus famine selectively strengthens glycogen accumulating organisms (GAOs) for advanced nutrient removal in an anaerobic-aerobic-anoxic system[J]. Chemical Engineering Journal, 2021,420:129554. [22] SMOLDERS G J F, VANDERMEIJ J, van LOOSDRECHT M C M, et al. Model of the anaerobic metabolism of the biological phosphorus removal process: stoichiometry and pH influence[J]. Biotechnology and Bioengineering, 1994,43(6): 461-470. [23] ZENG R J, SAUNDERS A M, YUAN Z, et al. Identification and comparison of aerobic and denitrifying polyphosphate-accumulating organisms[J]. Biotechnology and Bioengineering, 2003,83(2): 140-148. [24] ZENG R J,VAN LOOSDRECHT M C M, YUAN Z, et al. Metabolic model for glycogen-accumulating organisms in anaerobic/aerobic activated sludge systems[J]. Biotechnology and Bioengineering, 2003,81(1):92-105. [25] IZADI P, IZADI P, ELDYASTI A. Understanding microbial shift of enhanced biological phosphorus removal process (EBPR) under different dissolved oxygen (DO) concentrations and hydraulic retention time (HRTs)[J]. Biochemical Engineering Journal,2021,166:107833. [26] LIU W T, NAKAMURA K, MATSUO T, et al. Internal energy-based competition between polyphosphate- and glycogen- accumulating bacteria in biological phosphorus removal reactors-effect of P/C feeding ratio[J]. Water Research, 2015,31(6): 1430-1438. [27] ZHAO J, WANG X X, LI X Y, et al. Combining partial nitrification and post endogenous denitrification in an EBPR system for deep-level nutrient removal from low carbon/nitrogen (C/N) domestic wastewater[J]. Chemosphere,2018,210: 19-28. [28] MAJED N, GU A Z. Phenotypic dynamics in polyphosphate and glycogen accumulating organisms in response to varying influent C/P ratios in EBPR systems[J]. Science of the Total Environment, 2020, 743(7): 140603. [29] SGUANCI S, LUBELLO C, CAFFAZ S, et al. Long-term stability of aerobic granular sludge for the treatment of very low-strength real domestic wastewater[J]. Journal of Cleaner Production, 2019,222: 882-890. [30] WEISSBRODT D G, SCHNEITER G S, FUERBRINGCR J M, et al. Identification of trigger factors selecting for polyphosphate- and glycogen-accumulating organisms in aerobic granular sludge sequencing batch reactors[J]. Water Research, 2013,47(19): 7006-7018. [31] OEHMEN A, SAUNDERS A M, VIVES M T, et al. Competition between polyphosphate and glycogen accumulating organisms in enhanced biological phosphorus removal systems with acetate and propionate as carbon sources[J]. Journal of Biotechnology, 2006,123(1): 22-32. [32] YUAN C S, WANG B, PENG Y Z, et al. Enhanced nutrient removal of simultaneous partial nitrification, denitrification and phosphorus removal (SPNDPR) in a single-stage anaerobic/micro-aerobic sequencing batch reactor for treating real sewage with low carbon/nitrogen[J]. Chemosphere, 2020, 257: 127097. [33] ZHOU Y, PIJUAN M, ZENG R J, et al. Free nitrous acid inhibition on nitrous oxide reduction by a denitrifying-enhanced biological phosphorus removal sludge[J]. Environmental Science and Technology, 2008, 42(22):8260-8265.
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