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Enhancement of phosphorus removal in a low temperature a~2/O process by anaerobic phosphorus release of activated sludge

机译:活性污泥厌氧释放磷提高低温a〜2 / O工艺中的除磷

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An anaerobic phosphorus release tank was introduced to an anaerobic-anoxic-aerobic (A~2/O) process treating domestic sewage to enhance the phosphorus removal at low temperature. Phosphorus release of the activated sludge from the second sedimentation tank was evaluated at 14°C by batch cultures, and the nutrient removal in the modified low temperature A ~2/O process was further investigated at the same temperature. The results showed that the feasible sludge retention time was 14 h for sequencing batch reaction and 12 h for continuous flow operation. The ratio of raw sewage to activated sludge from the second sedimentation tank was 1:1 in volume to meet the demand of carbon resource for the growth of phosphorus release microbes. The feasible chemical oxygen demand (COD) loading rate of the activated sludge in the phosphorus release tank was 0.015-0.02 g COD/g MLSS (mixed liquor suspended solids) and the nitrate concentration should be less than 5 mg/L. The phosphorus release was doubled when the sludge was blended intermittently and gently. The anaerobic phosphorus release of the activated sludge improved the phosphate removal remarkably, as well as the removal of NH_4 ~+-N and total nitrogen (TN) in the modified low temperature A ~2/O process. The effluent COD, NH_4 ~+-N, TN and total phosphorus could meet a stricter discharge standard.
机译:在厌氧-缺氧-好氧(A〜2 / O)工艺中引入厌氧除磷罐,以处理生活污水,以提高低温下的除磷能力。在14°C下通过分批培养评估了第二个沉淀池中活性污泥的磷释放,并在相同温度下进一步研究了改良的低温A〜2 / O工艺中的养分去除。结果表明,可行的污泥保留时间为批处理顺序反应为14 h,连续流操作为12 h。来自第二沉淀池的原污水与活性污泥的比例为1:1,以满足碳源对磷释放微生物生长的需求。磷释放池中活性污泥的可行化学需氧量(COD)加载率为0.015-0.02 g COD / g MLSS(混合液悬浮固体),硝酸盐浓度应小于5 mg / L。当污泥断断续续地缓慢混合时,磷释放量增加了一倍。活性污泥中厌氧磷的释放显着提高了磷酸盐的去除率,以及改进的低温A〜2 / O工艺中NH_4〜+ -N和总氮(TN)的去除率。出水COD,NH_4〜+ -N,TN和总磷可以满足更严格的排放标准。

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