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Mainstream partial nitritation and anammox in a 200,000 m(3)/day activated sludge process in Singapore: scale-down by using laboratory fed-batch reactor

机译:在新加坡,每天以200,000 m(3)/天的活性污泥法处理主流的部分硝化和厌氧氨氮:使用实验室分批进料反应器进行规模缩减

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摘要

A laboratory fed-batch reactor has been used to study under controlled conditions the performance of partial nitritation/anammox for the 200,000 m(3)/day step-feed activated sludge process at the Changi Water Reclamation Plant, Singapore. The similarity of the concentrations of NH4, NO2, NO3, PO4, suspended chemical oxygen demand (sCOD), pH, and alkalinity (ALK) between the on-site process and laboratory reactor illustrates that the laboratory fed-batch reactor can be used to simulate the site performance. The performance of the reactor fed by primary effluent illustrated the existence of anammox and heterotrophic denitrification and apparent excessive biological phosphorus removal as observed from the site. The performance of the reactor fed by final effluent proved the presence of anammox process on site. Both the laboratory reactor and on-site process showed that higher influent 5-day biochemical oxygen demand/total nitrogen (BOD5/TN) (COD/TN) ratio increases the nitrogen removal efficiency of the process.
机译:在新加坡的樟宜水回收厂,一个实验室的分批进料反应器已用于在受控条件下研究200,000 m(3)/天的分步进料活性污泥工艺的部分硝化/厌氧氨气的性能。现场过程和实验室反应器之间的NH4,NO2,NO3,PO4,悬浮化学需氧量(sCOD),pH和碱度(ALK)浓度相似,表明实验室补料分批反应器可用于模拟网站效果。从原水进料的反应器性能说明了厌氧氨氧化和异养反硝化的存在以及从现场观察到的明显过量的生物除磷。最终废水进料的反应器性能证明了现场存在厌氧氨氧化工艺。实验室反应器和现场过程均显示,较高的进水5天生化需氧量/总氮(BOD5 / TN)(COD / TN)比提高了过程的脱氮效率。

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