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采用创新的三段式工艺,通过外部污泥减量实现节能高效的成熟垃圾渗滤液处理中的同步氨氧化脱氮(SAD)。

Simultaneous Ammonium oxidation denitrifying (SAD) in an innovative three-stage process for energy-efficient mature landfill leachate treatment with external sludge reduction.

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

Water Res. 2020 Feb 1;169:115156. doi: 10.1016/j.watres.2019.115156. Epub 2019 Oct 11.

Abstract

High-loaded ammonia and low-strength organics mature landfill leachate is not effectively treated by conventional biological processes. Herein, an innovative solution was proposed using a three-stage Simultaneous Ammonium oxidation Denitrifying (SAD) process. Firstly, ammonia (1760 ± 126 mg N/L) in wastewater was oxidized to nitrite in a partial nitrification sequencing batch reactor (PN-SBR). Next, 93% PN-SBR effluent and concentrated external waste activated sludge (WAS; MLSS = 23057 ± 6014 mg/L) were introduced to an anoxic reactor for integrated fermentation and denitrification (IFD-SBR). Finally, ammonia (101.4 ± 13.8 mg N/L) released by fermentation in the IFD-SBR and residual 7% nitrite in the PN-SBR were removed through the anaerobic ammonium oxidation (anammox) process in the SAD up-flow anaerobic sludge bed (SAD-UASB). In addition, NO-N generation during the anammox process could be reduced to nitrite by partial denitrification (PD) and reused as substrate for anammox. A satisfactory total nitrogen (TN) removal efficiency (98.3%), external sludge reduction rate (2.5 kg/m d) and effluent TN concentration (16.7 mg/L) were achieved after long-term operation (280 days). The IFD-SBR and SAD-UASB contributed to 81.9% and 12.3% nitrogen removal, respectively. Microbial analysis showed that anammox bacteria (1.5% Candidatus Brocadia) cooperated well with partial denitrifying bacteria (4.3% Thauera) in SAD-UASB, and average nitrogen removal contribution were 83.1% during significant stability of anammox and 9.2% during the denitrification process, respectively. The three-stage SAD process provides an environmental and economic approach for landfill leachate treatment since it has the advantage of 25.4% less oxygen, 100% organic matter savings and 47.9% less external sludge than traditional biological processes.

摘要

高负荷氨和低强度有机物成熟垃圾渗滤液不能被传统的生物处理过程有效处理。在这里,提出了一种使用三阶段同步氨氧化反硝化(SAD)工艺的创新解决方案。首先,在部分硝化序批式反应器(PN-SBR)中将废水中的氨(1760±126mgN/L)氧化为亚硝酸盐。接下来,将 93%的 PN-SBR 出水和浓缩的外部废活性污泥(WAS;MLSS=23057±6014mg/L)引入缺氧反应器进行集成发酵和反硝化(IFD-SBR)。最后,通过 IFD-SBR 中的发酵释放的氨(101.4±13.8mgN/L)和 PN-SBR 中的剩余 7%亚硝酸盐通过 SAD 上流厌氧污泥床(SAD-UASB)中的厌氧氨氧化(anammox)过程去除。此外,在 anammox 过程中产生的 NO-N 可以通过部分反硝化(PD)还原为亚硝酸盐,并重新用作 anammox 的底物。经过长期运行(280 天),实现了令人满意的总氮(TN)去除效率(98.3%)、外部污泥减少率(2.5kg/m d)和出水 TN 浓度(16.7mg/L)。IFD-SBR 和 SAD-UASB 分别贡献了 81.9%和 12.3%的氮去除。微生物分析表明,anammox 细菌(1.5%Candidatus Brocadia)与 SAD-UASB 中的部分反硝化细菌(4.3%Thauera)协同作用良好,在 anammox 显著稳定期间的平均氮去除贡献为 83.1%,在反硝化过程中的平均氮去除贡献为 9.2%。与传统生物处理过程相比,三阶段 SAD 工艺具有 25.4%更少的氧气、100%的有机物节约和 47.9%更少的外部污泥的优势,为垃圾渗滤液处理提供了一种环境和经济的方法。

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