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通过气体混合策略实现高效部分反硝化/厌氧氨氧化(PD/A)过程:系统评估和微生物分析。

Efficient partial-denitrification/anammox (PD/A) process through gas-mixing strategy: System evaluation and microbial analysis.

机构信息

National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, China.

State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin 150090, China.

出版信息

Bioresour Technol. 2020 Mar;300:122675. doi: 10.1016/j.biortech.2019.122675. Epub 2019 Dec 24.

Abstract

Partial denitrification (PD, NO-N → NO-N) provides a promising opportunity for anammox application in wastewater nitrogen removal. In this study, a continuous-flow PD/Anammox (PD/A) process operated with a novel gas mixing was reported in an up-flow anaerobic bed reactor. A high nitrogen removal rate of 2.42 kgN/(m∙d) was achieved at a relatively short hydraulic retention time (HRT) of 0.5 h with both influent NH-N and NO-N of 30 mg/L. Sludge floatation was eliminated by mixing with gas of the reactor due to an efficiently improved mass transfer. Further optimization of gas flowrates at high NLR could avoid the overproduction of tight-bound extracellular polymeric substances (TB-EPS) and benefit sludge stability. Functional microorganisms of PD and anammox were effectively retained, and Zoogloea affecting sludge settleability kept increasing throughout the operation. This study clearly demonstrated the effectiveness of gas mixing strategy for a high-rate continuous-flow PD/A process with stable nitrogen removal performance.

摘要

部分反硝化(PD,NO-N→NO-N)为厌氧氨氧化在废水脱氮中的应用提供了一个很有前途的机会。本研究采用新型气体混合,在升流式厌氧床反应器中运行连续流 PD/厌氧氨氧化(PD/A)工艺。在水力停留时间(HRT)为 0.5 h 的较短时间内,进水 NH-N 和 NO-N 分别为 30 mg/L 时,可实现 2.42 kgN/(m·d)的高氮去除率。由于传质效率的提高,混合气体消除了污泥漂浮。在高氮负荷(NLR)下进一步优化气体流量,可以避免产生紧密结合的胞外聚合物(TB-EPS)过多,并有利于污泥稳定性。PD 和厌氧氨氧化的功能微生物得到了有效保留,影响污泥沉降性的动胶菌在整个运行过程中不断增加。本研究清楚地表明,气体混合策略对于具有稳定脱氮性能的高负荷连续流 PD/A 工艺是有效的。

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