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实现污水处理厂(WWTP)可持续发展的污泥上清液、废活性污泥和二级出水的协同处理。

Achieving synergetic treatment of sludge supernatant, waste activated sludge and secondary effluent for wastewater treatment plants (WWTPs) sustainable development.

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, PR China.

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

出版信息

Bioresour Technol. 2021 Oct;337:125416. doi: 10.1016/j.biortech.2021.125416. Epub 2021 Jun 16.

DOI:10.1016/j.biortech.2021.125416
PMID:34320732
Abstract

A novel process that combines partial nitrification, fermentation and Anammox-partial denitrification (NFAD) was proposed to co-treat ammonia rich sludge supernatant (NH-N = 1194.1 mg/L), external WAS (MLSS = 22092.6 mg/L) and WWTP secondary effluent (NO-N = 58.6 mg/L). Three separated reactors were used for partial nitrification (PN-SBR), integrated fermentation and denitrification (IFD-SBR) and combined Anammox-partial denitrification (AD-UASB), respectively. The process resulted in excellent nitrogen removal efficiency (NRE) of 98.7%, external sludge reduction efficiency (SRE) of 44.6% and external sludge reduction rate of 4.1 kg/m after 200 days of continuous operation. IFD-SBR and AD-UASB contributed towards 89.4% and 9.2% nitrogen removal, respectively. In AD-UASB, cooperation between Anammox bacteria (4.1% Candidatus Brocadia) and partial denitrifying bacteria (3.2% Thauera) resulted in significant stability of Anammox pathway, which contributed up to 84.1% nitrogen removal in the combined Anammox-partial denitrification process. NFAD saved up to 100% organic resource demand and 25% of aeration consumption compared with the traditional nitrification-denitrification process.

摘要

提出了一种将部分硝化、发酵和厌氧氨氧化-部分反硝化(NFAD)相结合的新工艺,用于共处理富含氨的污泥上清液(NH-N=1194.1mg/L)、外部 WAS(MLSS=22092.6mg/L)和 WWTP 二级出水(NO-N=58.6mg/L)。分别使用三个分离的反应器进行部分硝化(PN-SBR)、集成发酵和反硝化(IFD-SBR)和组合厌氧氨氧化-部分反硝化(AD-UASB)。在连续运行 200 天后,该工艺实现了 98.7%的优异氮去除效率(NRE)、44.6%的外部污泥减少效率(SRE)和 4.1kg/m 的外部污泥减少率。IFD-SBR 和 AD-UASB 分别贡献了 89.4%和 9.2%的氮去除。在 AD-UASB 中,厌氧氨氧化菌(4.1%Candidatus Brocadia)和部分反硝化菌(3.2%Thauera)之间的合作导致了厌氧氨氧化途径的显著稳定性,在组合的厌氧氨氧化-部分反硝化过程中,该途径贡献了高达 84.1%的氮去除。与传统的硝化-反硝化工艺相比,NFAD 节省了 100%的有机资源需求和 25%的曝气消耗。

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