两级厌氧时间比对PNPR-SAEPD工艺同步脱氮除磷的影响

李冬, 吕璐, 赖会彬, 张杰, 王凯

中国环境科学 ›› 2025, Vol. 45 ›› Issue (8) : 4245-4255.

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中国环境科学 ›› 2025, Vol. 45 ›› Issue (8) : 4245-4255.
水污染与控制

两级厌氧时间比对PNPR-SAEPD工艺同步脱氮除磷的影响

  • 李冬1, 吕璐1, 赖会彬1, 张杰1,2, 王凯1
作者信息 +

Impact of two-stage anaerobic time ratio on simultaneous nitrogen and phosphorus removal in PNPR-SAEPD process

  • LI Dong1, LV Lu1, LAI Hui-bin1, ZHANG Jie1,2, WANG Kai1
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摘要

本研究将生物除磷结合至PN-SAEPD工艺中,建立了PNPR-SAEPD系统,为了对有限的碳源进行合理分配,实验将两级厌氧时间比由S1阶段3:1(90min:30min)依次调整为S2阶段1:1(60min:60min)、S3阶段1:3(30min:90min),考察了两级厌氧时间比对PNPR-SAEPD系统的进水有机物转化、脱氮除磷性能以及微生物群落结构的影响.结果表明:S2阶段两级厌氧时间比为1:1,对进水有机碳源的分配最为合理,SAEPD、PNPR反应器储存内碳源所消耗的COD分别为(89.3±8.4)mg/L和(82.6±7.7)mg/L,PNPR反应器的除磷贡献度为(79.1%±8.5%),为后续SAEPD反应器缺氧阶段营造了磷饥饿条件.SAEPD反应器DPAOs对内碳源储存的贡献比例仅为15%,储存内碳源所消耗的COD量为(10.1±4.0)mg/L,DPAOs相对丰度降至3.01%.将生物除磷结合到PN反应器中提高了短程硝化的稳定性,NOB相对丰度由3.86%逐渐降至0.64%,NAR保持在(82.1%±4.0%).S2阶段PNPR反应器优越的PN性能和SAEPD反应器内DGAOs主导的EPD途径为AnAOB提供了充足的电子受体,厌氧氨氧化脱氮贡献度保持在(81.8%±3.6%),总氮去除率保持在(88.3%±1.6%),出水总氮浓度低于10mg/L且未出现硝酸盐积累;TP去除率最高可达93.7%,出水TP浓度基本降低到0.5mg/L以下.

Abstract

This study integrated biological phosphorus removal into the PN-SAEPD process, establishing a PNPR-SAEPD system. To allocate the limited carbon source reasonably, the experiment gradually adjusted the two-stage anaerobic time ratio from 3:1 (90min:30min) in the S1stage to 1:1 (60min:60min) in the S2 stage, and then to 1:3 (30min:90min) in the S3stage. The study investigated the impact of the two-stage anaerobic time ratio on the conversion of influent organic matter, nitrogen and phosphorus removal performance, and microbial community structure of the PNPR-SAEPD system. The results showed that in the S2 stage, with a two-stage anaerobic time ratio of 1:1, the allocation of inflow organic carbon sources was most reasonable. The average COD consumed by the SAEPD and PNPR reactors for storing internal carbon sources was (89.3±8.4)mg/L and (82.6±7.7)mg/L, respectively. The phosphorus removal contribution of the PNPR reactor was (79.1%±8.5%), creating phosphorus starvation conditions for the subsequent anaerobic stage of the SAEPD reactor. The contribution of DPAOs in the SAEPD reactor to the storage of internal carbon sources was only 15%, consuming (10.1±4.0)mg/L of COD. The relative abundance of DPAOs dropped to 3.01%, enhancing the synergistic denitrification of DGAOs and AnAOB. Integrating biological phosphorus removal into the PN reactor improved the stability of short-cut nitrification, with the relative abundance of NOB gradually decreasing from 3.86% to 0.64% and NAR maintaining at around (82.1%±4.0%). In the S2stage, the superior PN performance of the PNPR reactor and the EPD pathway dominated by DGAOs in the SAEPD reactor provided sufficient electron acceptors for AnAOB. The anaerobic ammonium oxidation denitrification contribution remained at about (81.8%±3.6%), the total nitrogen removal rate was maintained at around (88.3%±1.6%), and the effluent total nitrogen concentration was below 10mg/L. The TP removal rate could reach up to 93.7%, and the effluent TP concentration was basically reduced to below 0.5mg/L.

关键词

两级厌氧时间比 / 内源性短程反硝化(EPD) / 厌氧氨氧化(Anammox) / 内碳源 / 反硝化聚糖菌(DGAOs)

Key words

two-stage anaerobic time ratio / endogenous partial denitrification (EPD) / Anammox / internal carbon source / denitrifying glycogen-accumulating organisms (DGAOs)

引用本文

导出引用
李冬, 吕璐, 赖会彬, 张杰, 王凯. 两级厌氧时间比对PNPR-SAEPD工艺同步脱氮除磷的影响[J]. 中国环境科学. 2025, 45(8): 4245-4255
LI Dong, LV Lu, LAI Hui-bin, ZHANG Jie, WANG Kai. Impact of two-stage anaerobic time ratio on simultaneous nitrogen and phosphorus removal in PNPR-SAEPD process[J]. China Environmental Science. 2025, 45(8): 4245-4255
中图分类号: X703   

参考文献

[1] 王夏童,房平,赵学敏,等.水体中氮素污染危害及其治理的研究综述[J].广东化工, 2021,48(5):92-93. Wang X T, Fang P, Zhao X M, et al. Review on the hazards and treatment of nitrogen pollution in rivers [J]. Guangdong Chemical Industry, 2021,48(5):92-93.
[2] 冯琪瑞,唐玉朝,伍昌年,等.反硝化除磷工艺进展及影响因素[J].环境监测管理与技术, 2023,35(4):7-12. Feng Q R, Tang Y C, Wu C N, et al. Progress and influencing factors of denitrifying phosphorus removal process [J]. The Administration and Technique of Environmental Monitoring, 2023,35(4):7-12.
[3] Gu J, Yang Q, Liu Y. Mainstream anammox in a novel A-2B process for energy-efficient municipal wastewater treatment with minimized sludge production [J]. Water Research, 2018,138:1-6.
[4] Cao Y, Van Loosdrecht M C M, Daigger G T. Mainstream partial nitritation-anammox in municipal wastewater treatment: status, bottlenecks, and further studies [J]. Applied Microbiology and Biotechnology, 2017,101(4):1365-1383.
[5] Daigger G T. Oxygen and carbon requirements for biological nitrogen removal processes accomplishing nitrification, nitritation, and anammox [J]. Water Environment Research, 2014,86(3):204-209.
[6] Izadi P, Izadi P, Eldyasti A. Towards mainstream deammonification: Comprehensive review on potential mainstream applications and developed sidestream technologies [J]. Journal of Environmental Management, 2021,279.
[7] Zhou M, Wang J, Wang H, et al. Revealing the comprehensive impact of organic compounds on the partial nitrification-anammox system during incineration leachate treatment: metabolic hierarchy and adaptation [J]. Water Research, 2024,255.
[8] Dan Q, Wang T, Li J, et al. Enhanced anammox performance under lower nitrite accumulation in modified partial nitritation-anammox (PN/A) process [J]. Bioresource Technology, 2024,406.
[9] 万家秀,王家骐,郑平,等.厌氧氨氧化组合脱氮工艺研究进展[J].生物工程学报, 2022,38(4):1351-1359. Wan J X, Wang J Q, Zheng P, et al. Research progress of combined anaerobic ammonium oxidation (ANAMMOX) process for nitrogen removal [J]. Chinese Journal of Biotechnology, 2022,38(4):1351- 1359.
[10] 左富民,郑蕊,隋倩雯,等.一体式短程硝化-厌氧氨氧化工艺启动过程的亚硝酸盐调控[J].环境科学, 2021,42(11):5472-5480. Zuo F M, Zheng R, Sui Q W, et al. Nitrite regulation during start-up of combined partial nitritation and ANAMMOX process [J]. Environmental Science, 2021,42(11):5472-5480.
[11] Xu G, Zhang Z, Gao F. Effect of COD/N ratios and DO concentrations on the NOB suppression in a multi-cycle SBR [J]. Journal of Environmental Chemical Engineering, 2021,9(4):105735.
[12] 谢怡漪,李祥,袁怡,等.主流条件下间歇曝气抑制NOB与微生物动态响应[J].中国环境科学, 2023,43(9):4616-4625. Xie Y Y, Li X, Yuan Y, et al. The way of coupling intermittent aeration strategy to inhibit NOB activity in mainstream environment and the dynamic response of microorganisms [J]. China Environmental Science, 2023,43(9):4616-4625.
[13] 李冬,王凯璐,祝彦均,等.进水分配比对分段进水PN/A工艺脱氮性能影响[J].中国环境科学, 2024,44(7):3672-3681. Li D, Wang K L, Zhu Y J, et al. Optimizing nitrogen removal in PN/A process: Step-feed influence analysis [J]. China Environmental Science, 2024,44(7):3672-3681.
[14] Li J, Zhang L, Peng Y, et al. NOB suppression in partial nitritation-anammox (PNA) process by discharging aged flocs: Performance and microbial community dynamics [J]. Chemosphere, 2019,227:26-33.
[15] Rubio-Rincón F J, Lopez-Vazquez 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.
[16] Ji J, Peng Y, Wang B, et al. Achievement of high nitrite accumulation via endogenous partial denitrification (EPD)[J]. Bioresource Technology, 2017,224:140-146.
[17] Chen S, Zhang Q P, Zhang J S, et al. Enhanced nitrogen removal for low C/N wastewater via preventing futile carbon oxidation and augmenting anammox [J]. Water Research X, 2024,25.
[18] Ji J, Peng Y, Li X, et al. A novel partial nitrification-synchronous anammox and endogenous partial denitrification (PN-SAEPD) process for advanced nitrogen removal from municipal wastewater at ambient temperatures [J]. Water Research, 2020,175.
[19] Shang T, Zhu X, Gong X, et al. Efficient nitrogen removal in a total floc sludge system from domestic wastewater with low C/N: High anammox nitrogen removal contribution driven by endogenous partial denitrification [J]. Bioresource Technology, 2023,378.
[20] Wang H, Zhang L, Dan Q, et al. Ultra-high nitrogen removal from real municipal wastewater using selective enhancement of glycogen accumulating organisms (GAOs) in a partial nitrification-anammox (PNA) system [J]. Water Research, 2023,230.
[21] Sun T, Du R, Dan Q, et al. Rapidly achieving partial nitrification of municipal wastewater in enhanced biological phosphorus removal (EBPR) reactor: Effect of heterotrophs proliferation and microbial interactions [J]. Bioresource Technology, 2021,340.
[22] Daverey A, Su S H, Huang Y T, et al. Partial nitrification and anammox process: A method for high strength optoelectronic industrial wastewater treatment [J]. Water Research, 2013,47(9):2929- 2937.
[23] Ding J, Gao X, Peng Y, et al. Anaerobic duration optimization improves endogenous denitrification efficiency by glycogen accumulating organisms enhancement [J]. Bioresource Technology, 2022,348.
[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, 2002,81(1): 92-105.
[25] Welles L, Tian W D, Saad S, et al. Accumulibacter clades Type I and II performing kinetically different glycogen-accumulating organisms metabolisms for anaerobic substrate uptake [J]. Water Research, 2015,83:354-366.
[26] Petriglieri F, Singleton C, Peces M, et al. “Candidatus Dechloromonas phosphoritropha” and “Ca. D. phosphorivorans”, novel polyphosphate accumulating organisms abundant in wastewater treatment systems [J]. The ISME Journal, 2021,15(12):3605-3614.
[27] GB 18918—2002城镇污水处理厂污染物排放标准[S]. GB 18918—2002 Discharge standard of pollutants for municipal wastewater treatment plant [S].
[28] Zhang H, Zhang S S, Zhang W, et al. Clarification of the phosphorus release mechanism for recovering phosphorus from biofilm sludge in alternating aerobic/anaerobic biofilm system [J]. Science of The Total Environment, 2023,904.
[29] Li S, Guo Y, Zhang X, et al. Advanced nitrogen and phosphorus removal by the symbiosis of PAOs, DPAOs and DGAOs in a pilot-scale A2O/A+MBR process with a low C/N ratio of influent [J]. Water Research, 2023,229.
[30] 张贤庆,俞小军,张琨,等.基于碳源转变的协同生物除磷模式构建及运行效能[J].中国给水排水, 2024,40(19):1-8. Zhang X Q, Yu X J, Zhang K, et al. Establishment of synergistic biological phosphorus removal pattern based on carbon source transformation and its performance [J]. China Water & Wastewater, 2024,40(19):1-8.
[31] Fan Z, Zeng W, Wang B, et al. Transcriptional responses of Candidatus Accumulibacter clades to environmental dynamics in enhanced biological phosphorus removal [J]. Bioresource Technology, 2020,306.
[32] Chen P, Wu J, Lu X, et al. Denitrifying phosphorus removal and microbial community characteristics of two-sludge DEPHANOX system: Effects of COD/TP ratio [J]. Biochemical Engineering Journal, 2021,172.
[33] Xu X, Qiu L, Wang C, et al. Achieving mainstream nitrogen and phosphorus removal through Simultaneous partial Nitrification, Anammox, Denitrification, and Denitrifying Phosphorus Removal (SNADPR) process in a single-tank integrative reactor [J]. Bioresource Technology, 2019,284:80-89.
[34] Zhao W, Bi X, Peng Y, et al. Research advances of the phosphorus- accumulating organisms of Candidatus Accumulibacter, Dechloromonas and Tetrasphaera: Metabolic mechanisms, applications and influencing factors [J]. Chemosphere, 2022,307.
[35] O'shaughnessy M, Nyhuis G, Takács I, et al. Going for mainstream deammonification from bench to full scale for maximized resource efficiency [J]. Water Science and Technology, 2013,68(2):283-289.
[36] Liu G, Wang J. Long-term low DO enriches and shifts nitrifier community in activated sludge [J]. Environmental Science & Technology, 2013,47(10):5109-5117.

基金

北京高校卓越青年科学家计划项目(BJJWZYJH01201910005019)

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