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  • AG,短程硝化反硝化AOOA工艺处理老龄垃圾渗滤液 作者: 王永庆 1 , 陈振国 1 , 汪晓军 1 , 简磊 2 , 陈静 1 , 陈晓坤 1 (1.华南理工大学环境与能源学院,广东广州510006
AG,短程硝化反硝化AOOA工艺处理老龄垃圾渗滤液 作者: 王永庆 1 , 陈振国 1 , 汪晓军 1 , 简磊 2 , 陈静 1 , 陈晓坤 1 (1.华南理工大学环境与能源学院,广东广州510006

焦点提醒:短程硝化反硝化AOOA工艺处置老龄垃圾渗滤液 作者: 王永庆 1 , 陈振国 1 , 汪晓军 1 , 简磊 2 , 陈静 1 , 陈晓坤 1 (1.华南理工年夜学情况与能源学院,广东广州510006;2.广州市华绿环保科技无限公司,广东广州510006)中国给水排水2023年中国污水处理厂提标改造(污水处理提质增效)高级研讨会(第七届)邀请函暨征稿启事中国给水排水2023年中国污水处理厂提标改造(污水处理提质增效)高级研讨会(第七届)邀请函暨征稿启事

短程硝化反硝化AOOA工艺处置老龄垃圾渗滤液

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[1]王永庆,陈振国,汪晓军,等.短程硝化反硝化AOOA工艺处置老龄垃圾渗滤液[J].中国给水排水,2018,34(21):18-23.

WANG Yong qing,CHEN Zhen guo,WANG Xiao jun,et al.Partial Nitrification and Denitrification of Mature Landfill Leachate Using Pilot-scale Anaerobic/Oxic/Oxic/Anaerobic Process[J].China Water & Wastewater,2018,34(21):18-23.

短程硝化反硝化AOOA工艺处置老龄垃圾渗滤液

  • 作者:

  • 王永庆 1 , 陈振国 1 , 汪晓军 1 , 简磊 2 , 陈静 1 , 陈晓坤 1

  • (1.华南理工年夜学情况与能源学院,广东广州510006;2.广州市华绿环保科技无限公司,广东广州AG����APP510006)

    摘要:采取厌氧/好氧/好氧/厌氧(AOOA)中试系统处置老龄垃圾渗滤液,经由过程节制DO在0.1~0.5 mg/L等前提成功实现了短程硝化反硝化。在低消融氧和碱度足够的前提下, O1池的NO-2-N堆集率不变在90%以上,系统对NH+4-N和TN的去除率别离高在95%和66.5%,有用处理了老龄垃圾渗滤液的脱氮困难。在节制消融氧为0.3~0.5 mg/L的前提下,O1池进行亚硝化的限制前提是现实水力逗留时候(AHRT),宜节制在13.9 h以上。在一般运转阶段,A1池中的劣势菌种为反硝化菌,而O1池的劣势菌为AOB。另外,O1/O2池实现了NO-2-N的堆集,并在必然水平上构成了同步亚硝化反硝化(SND)系统。

    Abstract:

    A pilot-scale anaerobic/oxic/oxic/anaerobic (AOOA) process was applied for treatment of maturelandfill leachate, and partial nitrification and denitrification was achieved by controlling the dissolved oxygen (DO) to a low value of 0.1-0.5 mg/L. Under the condition of low dissolved oxygen and sufficient alkalinity, the nitrite accumulation rate in the first aerobic reactor(O1)was stably above 90%, and the removal rate of ammonium and total nitrogen of the whole process was higher than 95% and 66.5% respectively, which indicated that AOOA process could effectively solve the difficult problem of nitrogen removal in landfill leachate. The limiting factor of partial nitrification of O1 was the actual hydraulic retention time (AHRT) and should be controlled above 13.9 h under the condition of DO of 0.3-0.5 mg/L. In the normal operation stage, the dominant bacteria in the first anaerobic reactor (A1) were denitrifying bacteria, while the dominant bacteria in the O1 were ammoniaoxidizing bacteria (AOB). In addition, nitrite accumulation was realized in O1/O2, and simultaneous partial nitrification and denitrification (SND) was formed to a certain extent.

    中国给水排水1000-406212-1073/TU]卷:第34卷期数:2018年21期页码:18-23栏目:阐述与研究出书日期:2018-10-20

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