多级好氧缺氧生物膜反应器脱氮及污泥减量特性

    Nitrogen Removal Performance and Sludge Reduction by Using a Multi-aerobic-anoxic Bio-film Reactor

    • 摘要: 针对污水处理厂目前普遍存在碳源不足和剩余污泥量过大的问题, 以某小区低ρ(C)/ρ(N) 比生活污水为研究对象, 构建了多级好氧缺氧生物膜反应器, 考察了反应器脱氮、污泥减量效果及运行工况.试验表明反应器最优运行工况:流量分配比为3∶4∶3, HRT为11 h, ρ(DO) 为4.0 mg/L, 温度为25℃, 回流比R=1.0.在上述工况下, 当进水ρ(TN) 、ρ(NH4+-N) 、ρ(COD) 分别为80~130、75~100、260~400 mg/L时, ρ(TN) 出水约20 mg/L, ρ(NH4+-N) 、ρ(COD) 出水分别降至5.0、30 mg/L以下, TN、NH4+-N、COD平均去除率分别达到80%、95%、91%.多级好氧缺氧试验同时表明:反应器中的污泥产率仅为0.10, 优于其他生物膜工艺, 具有良好的污泥减量效果.

       

      Abstract: In order to solve problems of insufficient carbon sources during biological denitrification and too much surplus sludge in wastewater treatment plant, a multi-aerobic-anoxic bio-film reactor was built to treat low ρ(C)/ρ(N) ratio wastewater in a community.The reactor could achieve its optimal results when flow distribution ratio was 3∶ 4∶ 3, HRT was 11 h, ρ(DO) was 4.0 mg/L, temperature was at 25℃, and reflux ratio R = 1.0.Under above conditions, when ρ(TN) , ρ(NH4+-N) and ρ(COD) in raw water was 80~130, 75~100 and 260~400 mg/L, respectively, removal efficiency of TN, NH4+-N and COD reached 80%, 95% and 91%, respectively, ρ(TN) in effluent was about 20 mg/L, ρ(NH4+-N) and ρ(COD) in effluent was dropped to below 5.0 mg/L and 30 mg/L, respectively.The results also showed that the sludge production rate was only 0.10, which was superior to other bio-film processes.So the effect sludge reduction was significant.

       

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