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[中试规模饮用水生物处理中NH4+-N去除的非硝化途径]

[Non-nitrification pathway for NH4+ -N removal in pilot-scale drinking water biological processes].

作者信息

Yu Xin, Ye Lin, Li Xu-dong, Zhang Xiao-jian, Shi Xu, Liu Bo, Li Rui-hua

机构信息

State Key Laboratory of Pollution Control and Resource Reuse, School of the Environment, Nanjing University, Nanjing 210093, China.

出版信息

Huan Jing Ke Xue. 2008 Apr;29(4):909-14.

Abstract

The non-nitrification pathway for NH4+ -N removal in pilot-scale drinking water biological treatment processes and its possible mechanism were investigated through calculating N and DO stoichiometric balance. With more than 2 mg/L NH4+ -N in the influent, for the fluidized bed bioreactor (FBBR), the total of NH4+ -N, NO2(-) -N, NO3(-) -N in the influent was 0.91 mg/L higher than that in the effluent, and for the biofilter, its DO consumption was 2.90 mg/L less than the stoichiometric amount. The results suggested that nitrogen loss occurred in both reactors and a part of NH4+ -N was removed through non-nitrification pathway. Because the utilization of phosphorus and organic matters was independent of nitrogen loss, the assimilation and denitrification could be excluded from the possible mechanisms. Because the very low C/N in the influent and the accumulation of NO2(-) -N in the reactors were similar with the wastewater biological processes, the "autotrophic removal of nitrogen" was regarded as the most probable non-nitrification pathway. In this mechanism, the couple of short-cut nitrification and ANAMMOX (or OLAND) leading to the transformation of NH4+ -N and NO2(-) -N into gaseous N2 was responsible for the nitrogen loss in drinking water biological processes.

摘要

通过计算氮和溶解氧的化学计量平衡,研究了中试规模饮用水生物处理过程中NH4+-N去除的非硝化途径及其可能机制。当进水NH4+-N浓度超过2mg/L时,对于流化床生物反应器(FBBR),进水NH4+-N、NO2(-)-N、NO3(-)-N的总量比出水高0.91mg/L,对于生物滤池,其溶解氧消耗量比化学计量少2.90mg/L。结果表明,两个反应器中均发生了氮损失,部分NH4+-N通过非硝化途径被去除。由于磷和有机物的利用与氮损失无关,因此同化作用和反硝化作用不可能是可能的机制。由于进水C/N极低,且反应器中NO2(-)-N积累情况与废水生物处理过程相似,因此“自养脱氮”被认为是最可能的非硝化途径。在此机制中,由短程硝化和厌氧氨氧化(或OLAND)耦合导致NH4+-N和NO2(-)-N转化为气态N2,这是饮用水生物处理过程中氮损失的原因。

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