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前置A2NSBR系统硝化和反硝化除磷的特性
引用本文:赵伟华,李健伟,王梅香,黄宇,冯岩,李夕耀,彭永臻. 前置A2NSBR系统硝化和反硝化除磷的特性[J]. 中国环境科学, 2019, 39(11): 4660-4665
作者姓名:赵伟华  李健伟  王梅香  黄宇  冯岩  李夕耀  彭永臻
作者单位:1. 北京工业大学, 国家工程实验室, 北京市污水脱氮除磷处理与过程控制工程技术研究中心, 北京 100124;2. 哈尔滨工业大学, 海洋科学与技术学院, 山东 威海 264209
基金项目:国家自然科学基金资助项目(51578014);北京市教委资助项目
摘    要:以处理实际低C/N生活污水的前置A2NSBR系统为研究对象,考察系统内生物膜的硝化特性和活性污泥的反硝化除磷特性.试验研究了有机物和NO2--N浓度对生物膜硝化性能的影响,以及不同电子受体浓度对反硝化吸磷速率的影响.结果测得硝化速率为11.3mgNH4+-N/(L·h),在填充率40%的条件下容积负荷为0.27kgNH4+-N/(m3·d),有机物的存在会对硝化有抑制,但是系统表现出了良好的抗有机负荷冲击能力,硝化速率为9.72mg NH4+-N/(L·h).NO2--N处理对AOB活性几乎无影响,对NOB活性抑制作用明显,当NO2--N浓度为400mg/L时,NOB活性仅为1.63%,几乎接近完全被抑制.根据本次不同电子受体条件下除磷批次试验的结果,好氧吸磷速率为17.62mg P/(g VSS·h),以NO3--N为电子受体的缺氧吸磷速率是12.94mg P/(g VSS·h),从而可知缺氧聚磷菌占总聚磷菌的比例大约是73.4%,其中在NO2--N浓度为30mg/L出现吸磷抑制,当NO2--N和NO3--N共存时,NO2--N在初始浓度为15mg/L便出现吸磷抑制.

关 键 词:低碳氮比  前置A2NSBR工艺  硝化  反硝化除磷  NO2--N抑制  
收稿时间:2019-04-24

Nitrification and denitrifying phosphorus removal performance in the pre-A2 NSBR system
ZHAO Wei-hua,LI Jian-wei,WANG Mei-xiang,HUANG Yu,FENG Yan,LI Xi-yao,PENG Yong-zhen. Nitrification and denitrifying phosphorus removal performance in the pre-A2 NSBR system[J]. China Environmental Science, 2019, 39(11): 4660-4665
Authors:ZHAO Wei-hua  LI Jian-wei  WANG Mei-xiang  HUANG Yu  FENG Yan  LI Xi-yao  PENG Yong-zhen
Affiliation:1. National Engineering Laboratory for Advanced Municipal Wastewater Treatment and Reuse Technology, Engineering Research Center of Beijing, Beijing University of Technology, Beijing 100124, China;2. School of Marine Science and Technology, Harbin Institute of Technology, Weihai 264209, China
Abstract:Biofilm nitrification and activated sludge denitrifying phosphorus removal performance were investigated in the pre-A2 NSBR system, which treated real low carbon to nitrogen (C/N) ratio domestic sewage. The effect of organic substance and NO2--N concentration on the biofilm nitrification performance, and different electronic acceptors on the denitrifying phosphorus uptake rate were studied. Results indicated that nitrification rate was 11.3 mgNH4+-N/(L·h), the ammonia volume loading was 0.27 kgNH4+-N/(m3·d) under the filling rate of 40%, the nitrification performance was inhibited by organic substance, but the system showed a good nitrification rate of 9.72 mg NH4+-N/(L·h) when organics presented. NO2--N treatment exhibited little effect on the AOB activity but obvious effect on the NOB activity, the NOB activity was almost completely inhibited (only 1.63%) when NO2--N concentration was 400mg/L. According to the phosphorus uptake rate experiment under different electronic acceptors, the phosphorus uptake rate under oxygen and NO3--N was 17.62mg P/(g VSS·h) and 12.94mg P/(g VSS·h), respectively, anoxic phosphate accumulating organisms (PAOs) occupied 73.4% of the total PAOs, phosphorus uptake performance was inhibited when the NO2--N concentration was 30mg/L, and phosphorus uptake performance was inhibited when the NO2--N concentration was 15mg/L under the condition of NO2--N and NO3--N coexisted.
Keywords:low C/N ratio  pre-A2NSBR process  nitrification  denitrifying phosphorus removal  NO2--N inhibition  
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