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采用新型生物载体在序批式生物膜反应器中实现同步部分硝化、厌氧氨氧化和反硝化(SNAD)过程的启动。

Start-up of simultaneous partial nitrification, anammox and denitrification (SNAD) process in sequencing batch biofilm reactor using novel biomass carriers.

机构信息

Institute of Environmental Engineering, National Chiao Tung University, Hsinchu 30010, Taiwan.

Department of Bioenvironmental Engineering, Chung-Yuan Christian University, 200 Chung Pei Road, Chung-Li 32023, Taiwan.

出版信息

Bioresour Technol. 2015 Aug;190:480-6. doi: 10.1016/j.biortech.2015.02.064. Epub 2015 Feb 20.

DOI:10.1016/j.biortech.2015.02.064
PMID:25794809
Abstract

Simultaneous partial nitrification, anammox and denitrification (SNAD) process was started-up in a 2.5L sequencing batch biofilm reactor (SBBR) using novel biomass carriers. The SNAD process took only 51d for start-up at nitrogen loading rate (NLR) and organic loading rate (OLR) of 120 and 60g/m(3)-d, respectively. Long-term stable operation of SNAD process was observed at NLR and OLR of 360 and 180g/m(3)-d with average total nitrogen and COD removal efficiencies of >88% and >90%, respectively. The values of conversion ratio [Formula: see text] remained below 0.11 after the start-up period, which further confirmed the long-term stability of SNAD process. Results of polymerase chain reaction (PCR), qualitative PCR, and scanning electron microscopic (SEM) analysis of sludge samples confirmed the co-existence and enrichment of AOB, anammox bacteria and denitrifying bacteria in the reactor and biofilm formation on to the carriers.

摘要

采用新型生物载体,在 2.5L 序批式生物膜反应器(SBBR)中启动同时硝化-反硝化-厌氧氨氧化(SNAD)工艺。在氮负荷(NLR)和有机负荷(OLR)分别为 120 和 60g/m³·d 的条件下,SNAD 工艺仅用 51d 即可启动。在 NLR 和 OLR 分别为 360 和 180g/m³·d 的条件下,SNAD 工艺能够长期稳定运行,总氮和 COD 的平均去除效率分别大于 88%和 90%。启动后[Formula: see text]值一直低于 0.11,进一步证实了 SNAD 工艺的长期稳定性。聚合酶链反应(PCR)、定性 PCR 和污泥样品扫描电子显微镜(SEM)分析的结果证实了反应器和载体上 AOB、厌氧氨氧化菌和反硝化菌的共存和富集以及生物膜的形成。

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