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基于部分硝化耦合厌氧氨氧化系统的A/O构建及其反硝化性能

[Construction and Denitrification Performance of A/O Based on Partial Nitrification Coupled with an ANAMMOX System].

作者信息

Liu Xiao-Chai, Rong Yi, Wen Li-Jie, Li Dang-Yong, Jin Peng-Kang

机构信息

School of Environmental and Municipal Engineering, Xi'an University of Architecture and Technology, Xi'an 710055, China.

Shaanxi Construction Engineering Installation Group Co., Ltd., Xi'an 710068, China.

出版信息

Huan Jing Ke Xue. 2020 Apr 8;41(4):1779-1786. doi: 10.13227/j.hjkx.201910190.

Abstract

To resolve the issue of existing municipal wastewater treatment plants (WWTPs) in China with an insufficient influent carbon source, a bench-scale A/O process based on partial nitrification coupled with ANAMMOX was constructed by controlling aeration partition ratio, dissolved oxygen (DO) concentration, and sludge retention time (SRT). In this study, the nitrogen removal performance, nitrogen removal pathway, and microbial community structure of the system under different conditions were investigated. The results showed that the system had excellent nitrogen removal efficiency at low-C/N influent (C/N=5). The A/O reactor had experienced the co-culture stage (Phase 1), screening stage (Phase 2-3), and enrichment stage (Phase 4) successively during the 140-day experiment, and the nitrogen removal pathway changed from nitrification and denitrification to partial nitrification coupled ANAMMOX in the end. The optimal removal efficiencies of 97.69% for NH-N and 87.83% for TN were obtained in the enrichment stage (Phase 4), and the effluent concentration of NH-N and TN were 1.20 mg·L and 7.03 mg·L, respectively. Illumina MiSeq sequencing results showed that the enrichment of AOB including and and the elimination of NOB including , , and were the main causes of achieving partial nitrification in the system. The enrichment of AnAOB including and was the key point for the occurrence of ANAMMOX in the system, and thus, played an important role in the achievement of advanced nitrogen removal.

摘要

为解决中国现有城市污水处理厂进水碳源不足的问题,通过控制曝气分配比、溶解氧(DO)浓度和污泥停留时间(SRT),构建了基于部分硝化耦合厌氧氨氧化的实验室规模A/O工艺。本研究考察了该系统在不同条件下的脱氮性能、脱氮途径和微生物群落结构。结果表明,该系统在低进水碳氮比(C/N = 5)时具有优异的脱氮效率。在140天的实验过程中,A/O反应器依次经历了共培养阶段(第1阶段)、筛选阶段(第2 - 3阶段)和富集阶段(第4阶段),最终脱氮途径从硝化反硝化转变为部分硝化耦合厌氧氨氧化。在富集阶段(第4阶段),NH-N和TN的最佳去除效率分别达到97.69%和87.83%,NH-N和TN的出水浓度分别为1.20 mg·L和7.03 mg·L。Illumina MiSeq测序结果表明,包括 和 的氨氧化细菌(AOB)的富集以及包括 、 和 的亚硝酸盐氧化细菌(NOB)的消除是系统实现部分硝化的主要原因。包括 和 的厌氧氨氧化菌(AnAOB)的富集是系统中厌氧氨氧化发生的关键,因此在实现深度脱氮中发挥了重要作用。

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