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Biological removal of phosphorus and denitrification of waste water - by addn. of easily degradable organic acids during denitrification-anaerobic stage

机译:生物除磷和废水反硝化-加法。反硝化-厌氧阶段中易降解有机酸的分离

摘要

In the biological elimination of P, combined with nitrification and denitrification of waste water, easily degradable organic acids are added to the denitrification/anaerobic stage, these acids being liberated during the anaerobic treatment of the raw waste water. The space loading for N breakdown is 30 vols.% for denitrification and 70% for nitrification, with 300% recirculation of the activated sludge resulting from the aerobic stage of the denitrification stage, at the same time as the P elimination. Later clarification and removal of excess sludge are carried out by the process of an activated sludge plant; excess sludge may be removed before the settling step in the later clarification, to avoid unwanted recycling of P in the later clarification. The ratio of recycled sludge is 80%. The sludge level in the pre-clarification is held constant at 0.6 m, when easily degradable organic acids are liberated in an anaerobic process (acid fermentation). The sludge is mixed by means of a plate or propeller pumps. Excessive thickening of the sludge is prevented by briefly pressing in air, e.g. through a sand trap jet, before withdrawal of the sludge. ADVANTAGE - Eutrophication of watercourse is limited, in a cheaper, simple process.
机译:在生物除磷过程中,结合废水的硝化作用和反硝化作用,易降解的有机酸被添加到反硝化/厌氧阶段,这些酸在原废水的厌氧处理过程中被释放出来。 N分解的空间负荷对于反硝化是30体积%,对于硝化是70%,其中活性污泥的再循环是在P消除的同时,由反硝化阶段的好氧阶段引起的活性污泥的300%再循环。后期的澄清和去除多余的污泥是通过活性污泥装置进行的。可以在以后的澄清步骤中的沉淀步骤之前除去过量的污泥,以避免在以后的澄清步骤中不必要地回收P。再生污泥的比例为80%。当在厌氧过程中释放出易于降解的有机酸(酸发酵)时,预澄清中的污泥水平保持恒定在0.6 m。污泥通过平板泵或螺旋桨泵混合。通过短暂地压入空气(例如,空气)可防止污泥过度增稠。在收集污泥之前,先通过集沙器喷射。优势-以更便宜,更简单的方法来限制河道的富营养化。

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