CAJ | 학술논문

针对农村生活污水低碳高氮磷特点,研究两级回流连续曝气生物膜工艺处理农村生活污水的效果和机理.在平均处理量90 t/d、水力停留时间为3.0 d,稳定运行12个月结果表明,该工艺对化学需氧量、五日生化需氧量、氨氮、全氮、全磷和悬浮物的平均去除率分别为75.7%、84.8%、69.2%、68.0%、58.9%和87.9%;出水化学需氧量、五日生化需氧量、氨氮、全氮、全磷和悬浮物的平均质量浓度分别在51.0、15.8、10.8、16.5、2.3和15.7 mg/L以下,满足天津市农村污水处理厂排水标准,改造后工艺运行更加稳定,出水 NH3-N 和 TN 有明显改善,符合农村污水处理要求.
침대농촌생활오수저탄고담린특점,연구량급회류련속폭기생물막공예처리농촌생활오수적효과화궤리.재평균처리량90 t/d、수력정류시간위3.0 d,은정운행12개월결과표명,해공예대화학수양량、오일생화수양량、안담、전담、전린화현부물적평균거제솔분별위75.7%、84.8%、69.2%、68.0%、58.9%화87.9%;출수화학수양량、오일생화수양량、안담、전담、전린화현부물적평균질량농도분별재51.0、15.8、10.8、16.5、2.3화15.7 mg/L이하,만족천진시농촌오수처리엄배수표준,개조후공예운행경가은정,출수 NH3-N 화 TN 유명현개선,부합농촌오수처리요구.
A new suit of equipment combined two-stage reflux continuing aeration with a biofilm process was developed to treat the rural distributed domestic sewage with the characteristics of low carbon source and comparative high nitrogen and phosphorus concentration. The treatment effects and operating mechanism were studied. The effective volume of this equipment was 270 m3, including the volumes of 207, 24, 14, 7 and 18 m3 for the sewage adjusting tank, the anaerobic hydrolysis tank, the contact oxidation tank, the secondary sedimentation tank, and the effluent circulation tank, respectively. The reflux sludge pump and the circulating water pump were located on the bottom of the secondary sedimentation tank and the effluent circulation tank, respectively. There was one gate for sludge discharge at the end of the water outlet of the anaerobic tank. The depth of the packed and combined filler was 1.0 m. The treating capacity of the equipment was 90 t sewage daily, with the hydraulic retention time (HRT) of 3.0 d. The returning rate is 2:1 and the packing ratio of bio-balls in the hydrolyzation-acidification stage and the contact oxygenation stage was 60% and 75%, respectively. After the sewage was once lifted by the water pump, it could be completed for all procedures by the way of self-flow. This equipment had kept stable running for over twelve months. The results showed that the removal rate of chemical oxygen demand (CODcr), biological oxygen demand (BOD5), ammonia nitrogen (NH3-N), total nitrogen (TN), total phosphorus (TP) and suspension solid (SS) were 75.7%, 84.8%, 69.2%, 68.0%, 58.9% and 87.9%, respectively. The average effluent concentration of CODcr, BOD5, NH3-N, TN, TP and SS were 51, 15.8, 1.8, 16.5, 2.3 and 15.7mg/L, respectively, which reached the criterions of the effusion for the rural sewage treatment of Tianjin. We found that oxygenation stage and hydrolyzation-acidification stage were mainly controlled by nitrification and denitrifying, respectively. The treatment process was more stable with less land occupation, lower cost, and easier maintenance and management. In conclusions, this procedure greatly improves the treatment efficiency and is suitable for treatment of domestic sewage in the rural areas.