[1]王思琦,刘旭,张连,等.基于PN/A的组合工艺处理餐厨沼液的中试研究[J].中国给水排水,2025,41(21):1-9.
WANGSi-qi,LIUXu,ZHANGLian,et al.A Pilot-scale Investigation into Treatment of Kitchen Waste Biogas Slurry Using Partial Nitrification-Anammox Combined Process[J].China Water & Wastewater,2025,41(21):1-9.
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WANGSi-qi,LIUXu,ZHANGLian,et al.A Pilot-scale Investigation into Treatment of Kitchen Waste Biogas Slurry Using Partial Nitrification-Anammox Combined Process[J].China Water & Wastewater,2025,41(21):1-9.
基于PN/A的组合工艺处理餐厨沼液的中试研究
中国给水排水[ISSN:1000-4062/CN:12-1073/TU]
卷:
第41卷
期数:
2025年第21期
页码:
1-9
栏目:
出版日期:
2025-11-01
- Title:
- A Pilot-scale Investigation into Treatment of Kitchen Waste Biogas Slurry Using Partial Nitrification-Anammox Combined Process
- 关键词:
- 餐厨沼液; 短程硝化-厌氧氨氧化; 脱氮
- 摘要:
- 开发了一套缺氧/反应沉淀一体式矩形气升环流反应池-短程硝化/厌氧氨氧化反应池-反应沉淀一体式矩形气升环流反应池(A/RPIR-PN/A-RPIR)组合工艺,并开展了中试规模的餐厨沼液处理研究,考察该组合工艺的脱氮除碳性能及其机理。结果表明,A/RPIR-PN/A-RPIR组合工艺对NH4+-N、TN和COD的平均去除率分别可达到97.10%、87.39%和82.36%,总氮去除负荷最高可达到0.31 kg/(m3·d)。A/RPIR单元在进水水质波动较大的情况下,出水C/N值始终保持在0~1的较低范围,保障了后续PN/A单元厌氧氨氧化反应的稳定进行。PN/A单元的总氮去除负荷可达到0.57 kg/(m3·d),厌氧氨氧化菌(AnAOB)和氨氧化菌(AOB)的相对丰度分别由低负荷运行阶段的6.18%和0.66%升至满负荷运行阶段的12.59%和2.23%,亚硝酸盐氧化菌(NOB)和反硝化菌(DNB)的相对丰度则分别由0.59%和15.20%降至0.49%和4.04%,说明该组合工艺可以有效解决PN/A反应过程中菌群竞争和短程硝化不稳定的问题,实现高效稳定脱氮。
- Abstract:
- A combined process comprising an anoxic/reaction-precipitation integrated rectangular airlift circulation reactor, followed by a partial nitrification/Anammox reactor and a subsequent reaction-precipitation integrated rectangular airlift circulation reactor (A/RPIR-PN/A-RPIR), was developed and implemented for the pilot-scale treatment of kitchen waste biogas slurry. The performance and underlying mechanisms of nitrogen and carbon removal in this integrated system were systematically investigated. The average removal efficiencies of NH4+-N, TN, and COD achieved by the A/RPIR-PN/A-RPIR combined process were 97.10%, 87.39%, and 82.36%, respectively, with a maximum TN removal load of 0.31 kg/(m3·d). Even under significant fluctuations in influent quality, the effluent C/N ratio of the A/RPIR unit remained consistently low, within the range of 0 to 1, thereby ensuring stable operation of the subsequent Anammox process in the PN/A unit. The TN removal load of the PN/A unit reached 0.57 kg/(m3·d). The relative abundances of Anammox bacteria (AnAOB) and ammonia-oxidizing bacteria (AOB) increased from 6.18% and 0.66% during the low-load operation phase to 12.59% and 2.23% during the full-load operation phase. In contrast, the relative abundances of nitrite-oxidizing bacteria (NOB) and denitrifying bacteria (DNB) decreased from 0.59% and 15.20% to 0.49% and 4.04%, respectively. The above results indicated that the combined process effectively mitigated bacterial competition and maintained stable partial nitrification throughout the PN/A reaction, thereby enabling efficient and sustained nitrogen removal.
相似文献/References:
[1]宋欣欣,闵海华,丁西明.预处理+两级A/O+UF+Fenton+BAF处理餐厨沼液[J].中国给水排水,2021,37(8):143.
SONG Xin-xin,MIN Hai-hua,DING Xi-ming.Treatment of Food Waste Biogas Slurry by Process of Pretreatment, Two-stage A/O, UF, Fenton Advanced Oxidation and BAF[J].China Water & Wastewater,2021,37(21):143.
更新日期/Last Update:
2025-11-01