Pilot-scale partial nitrification and anaerobic ammonium oxidation system for nitrogen removal from municipal wastewater.

Yunlong Su, Xiyao Li, Jiao Wang, Rui Du, Xiaofei Xue, Yongzhen Peng
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Abstract

Partial nitrification has the advantages of saving energy and reducing the need for carbon sources in municipal wastewater treatment. However, for municipal wastewater with low ammonia, start-up and maintenance of partial nitrification is a worldwide challenge. Here we developed a pilot-scale double sludge system consisting of two sequencing batch reactors for partial nitrification (12 m2) and denitrification/anaerobic ammonium oxidation (denitrification/anammox, 8.4 m2) to treat municipal wastewater. Partial nitrification was maintained at no ammonium remaining with a nitrite accumulation rate of 87.7%. This study found that partial nitrification system effluent chemical oxygen demand increased from 24.8 mg L-1 to 64.9 mg L-1 accompanied by transformation from complete nitrification to partial nitrification. In the denitrification/anammox system, the reduction of nitrite to nitrogen required about 40% less carbon consumption than nitrate. High nitrogen removal was achieved with effluent total inorganic nitrogen of 2.7 mg L-1 without carbon addition. This work provided a pilot-scale demonstration of low-carbon high-nitrogen removal.

部分硝化厌氧氨氧化系统用于城市污水脱氮的中试研究。
部分硝化在城市污水处理中具有节能、减少碳源需求的优点。然而,对于低氨城市污水,部分硝化的启动和维护是一个世界性的挑战。在这里,我们开发了一个中试规模的双污泥系统,包括两个顺序间歇式反应器,用于部分硝化(12平方米)和反硝化/厌氧氨氧化(反硝化/厌氧氨氧化,8.4平方米)来处理城市污水。在不剩铵的情况下保持部分硝化,亚硝酸盐积累率为87.7%。本研究发现,部分硝化系统出水化学需氧量由24.8 mg L-1增加到64.9 mg L-1,同时由完全硝化向部分硝化转变。在反硝化/厌氧氨氧化系统中,亚硝酸盐还原为氮所需的碳消耗比硝酸盐减少约40%。在不加碳的情况下,出水总无机氮为2.7 mg L-1,实现了高氮去除率。这项工作提供了一个中试规模的低碳高氮去除示范。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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