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两级PNDPR耦合Anammox脱氮除磷工艺研究
引用本文:徐贵达,李冬,刘志诚,陶博,张杰.两级PNDPR耦合Anammox脱氮除磷工艺研究[J].中国环境科学,2021,41(11):5133-5141.
作者姓名:徐贵达  李冬  刘志诚  陶博  张杰
作者单位:1. 北京工业大学, 水质科学与水环境恢复工程北京市重点实验室, 北京 100124;2. 哈尔滨工业大学, 城市水资源与水环境国家重点实验室, 黑龙江 哈尔滨 150090
基金项目:北京高效卓越青年科学家计划项目(BJJWZYJH0120191-0005019);国家水体污染控制与治理科技重大专项(2018ZX07601-001)
摘    要:鉴于厌氧氨氧化工艺进水必须包含NO2--N和NH4+-N两种基质,且只能脱氮,为在此基础上进一步实现除磷,提出辅以短程硝化技术,将除磷、脱氮技术相耦合,即短程硝化反硝化除磷串联厌氧氨氧化工艺.生活污水首先进入短程硝化反硝化除磷单元,主要实现NH4+-N转化为NO2--N并去除COD,其部分出水与生活污水原水相混合再进入厌氧氨氧化单元,同时短程硝化反硝化除磷单元于缺氧条件下反硝化吸磷,待反应结束后两个处理单元的出水混合排放.实验结果表明,控制进水混合比为4.2可保证Anammox单元中C/N和NO2--N/NH4+-N值分别为2和1.5,平均△NO2--N/△NH4+-N=1.41,△NO3--N/△NH4+-N=0.12,Anammox脱氮平均占比为85.2%,反硝化与Anammox反应耦合良好.整个系统稳定运行后出水COD、P、NH4+-N、NO2--N和NO3--N浓度分别为15.2,0.85,0.59,5.56,3.33mg/L,TN去除率为89.4%,通过PNDPR-Anammox耦合新工艺成功实现模拟生活污水的高效处理.

关 键 词:短程硝化  厌氧氨氧化  反硝化除磷  进水混合比  
收稿时间:2021-04-01

Study on two-stage PNDPR coupled with Anammox for nitrogen and phosphorus removal
XU Gui-da,LI Dong,LIU Zhi-cheng,TAO Bo,ZHANG Jie.Study on two-stage PNDPR coupled with Anammox for nitrogen and phosphorus removal[J].China Environmental Science,2021,41(11):5133-5141.
Authors:XU Gui-da  LI Dong  LIU Zhi-cheng  TAO Bo  ZHANG Jie
Affiliation:1. Key Laboratory of Beijing Water Quality Science and Water Environment Recovery Engineering, Beijing University of Technology, Beijing 100124;2. State Key Laboratory of Urban Water Resource and Environment, Harbin Institute of Technology, Harbin 150090, China
Abstract:Considering that the influent of Anammox process must contain two substrates, NO2--N and NH4+-N, and it could only be denitrified. In order to further realize phosphorus removal on this basis, this study proposed to combine phosphorus removal and nitrogen removal with partial nitrification technology, namely partial nitrification and denitrifying phosphorus removal tandem Anammox process:the partial nitrification and denitrification phosphorus removal unit was the first to pass into domestic sewage to convert NH4+-N to NO2--N and remove part of COD. Part of the effluent was mixed with domestic sewage and enters the anaerobic ammonium oxidation unit. At the same time, the partial nitrification and denitrification phosphorus removal unit was denitrified and absorbed phosphorus under the hypoxia state, and the effluent of the two treatment units was mixed and discharged after the end of the reaction. The experimental results showed that controlling the influent mixing ratio to be 4.2 could ensure that the values of C/N and NO2-N/NH4+-N in the Anammox unit were 2 and 1.5, respectively, the average △NO2--N/△NH4+-N=1.41, △NO3--N/△NH4+-N=0.12, Anammox nitrogen 85.2% on average, denitrification and Anammox coupling reaction was good. After stable operation of the whole system, the effluent COD, P, NH4+-N, NO2--N and NO3--N concentrations were 15.2, 0.85, 0.59, 5.56 and 3.33mg/L, respectively, and the TN removal rate was 89.4%. The PNDPR-Anammox coupling new process successfully realized the efficient treatment of simulated domestic sewage.
Keywords:short-cut nitrification  anaerobic ammonia oxidation  denitrifying phosphorus removal  influent mixing ratio  
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