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Combined partial nitritation/Anammox systern for treatment of digester supernatant

机译:联合部分硝化/厌氧氨氮系统处理消化池上清液

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One-year (2004) comprehensive investigations in a semi-industrial pilot plant (5 m(3)) were carried out with the aim of assessing the influence of operational parameters on the partial nitritation/Anammox system performance. In the system designed as a moving-bed biofilm reactor, the influent nitrogen load to the Anammox reactor was progressively increased and a stable Anammox bacterial culture was obtained. Interaction between subsequent, aerobic and anaerobic conditions in the partial nitritation and Anammox reactors, respectively, granted conditions to remove nitrogen through the nitrite route. It implies that the oxygen supply can be limited to a high extent. A control strategy for the partial nitritation step relied on concomitant adjustment of the air supply with a variable influent nitrogen load, which can be monitored by both pH and conductivity measurements. In the Anammox reactor, an influent nitrite-to-ammonium ratio plays a vital role in obtaining efficient nitrogen removal. During the 1-year experimental period, the Anammox reactor was operated steadily and average nitrogen removal efficiency was 84% with 97% as the maximum value.
机译:一年(2004年)在半工业试验工厂(5 m(3))中进行了全面调查,目的是评估操作参数对部分硝化/厌氧氨氧化系统性能的影响。在设计为移动床生物膜反应器的系统中,逐渐增加了Anammox反应器的进水氮负荷,并获得了稳定的Anammox细菌培养物。分别在部分硝化反应器和厌氧氨氧化反应器中的后续,好氧和厌氧条件之间的相互作用,为通过亚硝酸盐路线除去氮提供了条件。这意味着氧气供应可能受到很大程度的限制。部分亚硝化步骤的控制策略依赖于伴随可变的进水氮负荷的空气供应的调节,这可以通过pH和电导率测量进行监控。在Anammox反应器中,进水亚硝酸盐与铵之比在有效去除氮中起着至关重要的作用。在1年的实验期内,Anammox反应器稳定运行,平均脱氮效率为84%,最大值为97%。

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