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Sewage nitrogen and phosphorus removal - separates nitrogen in a main flow and strips out the phosphor in a side flow

机译:去除污水中的氮和磷-分离主流中的氮并去除侧流中的磷

摘要

To apply a continuous biochemical removal action on nitrogen and phosphorus from sewage, it is passed directly into a denitrification stage and the nitrogen is removed in a main stream through successive stages for denitrification, nitrification and sepn. The phosphorus is sepd. into a side stream where the activated sludge sepd. at the first stage is used for phosphate stripping after passing through an anaerobic stage in a second solids sepn. The sepd. sludge is returned as a sludge generally free of phosphate to the denitrification, while the phosphate-enriched water portion is passed to phosphate pptn. followed by sepn. of an assessable phosphate sludge. The activated sludge concn. is more than 4.5 kg/m3 in the denitrification, nitrification and phosphate stripping stages. The oxygen supply during nitrification is at a raised pressure of at least 1 bar. During phosphate stripping, a fatty acid material is added if there if a reduced fatty acid content. USE/ADVANTAGE - The method is for the continuous sepn. of nitrogen and phosphorus from sewage. The system does not require a number of large vol. vessels, and gives recovery of useful matter.
机译:为了对污水中的氮和磷进行连续的生化去除作用,将其直接进入反硝化阶段,并通过连续的阶段在主流中去除氮,以进行反硝化,硝化和分离。磷沉淀。进入活性污泥沉淀的侧流。在第一阶段的第一阶段用于在第二固体隔垫中经过厌氧阶段后进行磷酸盐汽提。九月。污泥以通常不含磷酸盐的污泥形式返回反硝化过程,而富含磷酸盐的水部分则传递给磷酸盐pptn。其次是sepn。可评估的磷酸盐污泥。活性污泥浓度在反硝化,硝化和磷酸盐汽提阶段,其浓度超过4.5 kg / m3。硝化过程中的氧气供应压力至少为1 bar。在磷酸盐汽提过程中,如果脂肪酸含量降低,则添加脂肪酸材料。使用/优势-该方法适用于连续隔膜。污水中的氮和磷。该系统不需要大量的体积。船只,并回收有用的物质。

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