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改良型A2/O-MBR工艺的反硝化除磷性能研究
引用本文:王荣昌,欧阳琛,司书鹏. 改良型A2/O-MBR工艺的反硝化除磷性能研究[J]. 环境工程学报, 2014, 8(2): 401-407
作者姓名:王荣昌  欧阳琛  司书鹏
作者单位:同济大学环境科学与工程学院污染控制与资源化研究国家重点实验室, 长江水环境教育部重点实验室, 上海 200092;同济大学环境科学与工程学院污染控制与资源化研究国家重点实验室, 长江水环境教育部重点实验室, 上海 200092;同济大学环境科学与工程学院污染控制与资源化研究国家重点实验室, 长江水环境教育部重点实验室, 上海 200092
基金项目:“十二五”国家科技支撑计划项目(2012BAJ21B01)
摘    要:重点考察了一种改良型膜生物反应器(A2/O-MBR)的脱氮除磷性能。该工艺主要特点在于对膜池硝化回流液进行了固液分离,并将上清液和浓缩污泥分别回流至缺氧池和厌氧池,这种改进提高了系统对氮、磷的同步去除效率。实验结果表明,在水力停留时间(HRT)为12 h,污泥龄(SRT)为30 d,混合液回流比为200%的运行条件下,进水COD、NH4+-N、TN和TP平均浓度分别为(225±38)、(24.8±3.9)、(26.7±2.9)和(2.90±0.53)mg/L时,增加膜池硝化回流液固液分离装置前后,系统对COD和NH4+-N的去除都维持在较高水平,而系统对TN和TP的去除效果显著提高,出水TN和TP平均浓度分别由(14.9±3.3)mg/L和(1.95±0.72)mg/L下降到(9.4± 1.9)mg/L和(0.91±0.38)mg/L,表明增加膜池硝化回流液固液分离装置显著改善了A2/O-MBR系统的脱氮除磷效果。反硝化除磷活性实验结果进一步表明,改进后系统中反硝化除磷活性占总除磷活性的比例由51.5%上升至61.7%,说明增加膜池硝化回流液固液分离装置强化了系统的反硝化除磷性能。

关 键 词:A2/O-MBR工艺  脱氮除磷  反硝化除磷菌(DPAOs)  聚磷菌(PAOs)

Performance of denitrifying phosphorus removal in modified A2/O-MBR process
Wang Rongchang,Ouyang Chen and Si Shupeng. Performance of denitrifying phosphorus removal in modified A2/O-MBR process[J]. Techniques and Equipment for Environmental Pollution Control, 2014, 8(2): 401-407
Authors:Wang Rongchang  Ouyang Chen  Si Shupeng
Affiliation:State Key Laboratory of Pollution Control and Resource Reuse, Key Laboratory of Yangtze Aquatic Environment, Ministry of Education, College of Environmental Science and Engineering, Tongji University, Shanghai 200092, China;State Key Laboratory of Pollution Control and Resource Reuse, Key Laboratory of Yangtze Aquatic Environment, Ministry of Education, College of Environmental Science and Engineering, Tongji University, Shanghai 200092, China;State Key Laboratory of Pollution Control and Resource Reuse, Key Laboratory of Yangtze Aquatic Environment, Ministry of Education, College of Environmental Science and Engineering, Tongji University, Shanghai 200092, China
Abstract:A modified anaerobic-anoxic-aerobic-membrane bioreactor(A2/O-MBR)was used to investigate its nitrogen and phosphorus removal performance. The main features of the process include separation of reflux liquid from the membrane reactor, as well as the recirculation of supernatant and concentrated sludge into anoxic tank and anaerobic tank, respectively, which improve the nitrogen and phosphorus removal efficiency simultaneously. The experiment was conducted at HRT of 12 hours, SRT of 30 days and recirculation ratio of 200%. The results showed that when the average influent concentrations of COD, NH4+-N, TN and TP were (225±38) mg/L,(24.8±3.9) mg/L,(26.7±2.9) mg/L and (2.90±0.53) mg/L, respectively, no significant difference of the effluent COD and NH4+-N concentration was found between the systems with and without solid-liquid separator. However, the effluent TN and TP concentration were brought down from (14.9±3.3) mg/L and (1.95±0.72) mg/L to (9.4± 1.9) mg/L and (0.91±0.38) mg/L, respectively, when the system was equipped with solid-liquid separator. The results indicated that the nitrogen and phosphorus removal of the MBR system was significantly enhanced by addition of solid-liquid separator on nitrification reflux pipe. In addition, the denitrifying phosphorus removal activity assay showed that the ratio of denitrifying phosphorus removal activity to total phosphorus removal activity increased from 51.5% to 61.7% after addition of solid-liquid separator for nitrification reflux liquid, which indicated that the denitrifying phosphorus removal performance was strengthened by the modification.
Keywords:anaerobic-anoxic-aerobic-membrane bioreactor (A2/O-MBR) process  nitrogen and phosphorus removal  denitrifying phosphate accumulating organisms (DPAOs)  phosphate accumulating organisms(PAOs)
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