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NITROGEN AND PHOSPHORUS REMOVAL METHOD AND NITROGEN AND PHOSPHORUS REMOVAL APPARATUS

机译:氮磷去除方法及氮磷去除装置

摘要

- 36 - ABSTRACT (FIG. 1)"NITROGEN AND PHOSPHORUS REMOVAL METHOD AND NITROGEN AND PHOSPHORUS REMOVAL APPARATUS"5There is provided a nitrogen and phosphorus removal method including i) when NH4-NNlim and PO4-PPlim, driving a DTA in the high-speed mode to aerate and stir the anaerobically treated water in a10multiple-use tank, thereby increasing a ratio of a water volume in an aerobic condition to a water volume in an anaerobic condition, ii) when NH4-NNlim and PO4-PPlim, driving the DTA in the low-speed mode to stir the anaerobically treated water, thereby15increasing a ratio of a water volume in an anaerobic condition to a water volume in an aerobic condition, iii) when NH4-NNlim and PO4-PPlim, reducing a volume of the wastewater to be introduced, or switching the DTA from the high-speed mode to the low-speed mode or20stopping the driving a pump, thereby decreasing a ratio of a water volume in an anaerobic condition to a water volume in an aerobic condition, and iv) when NH4-NNlim and PO4-PPlim, driving the DTA in the low-speed modeuntil the concentration of the nitrogen compound25becomes NH4-N=Nlim or the concentration of the phosphorus compound becomes PO4-P-Plim, thereby increasing a ratio of a water volume in an anaerobic condition to a water volume in an aerobic condition.
机译:-36-抽象(图1)“氮和磷的去除方法及氮和磷的去除装置”5提供了一种脱氮除磷的方法,包括:i)当NH4-N> Nlim和PO4-PPlim时,以高速模式驱动DTA对厌氧处理过的水进行曝气和搅拌。10个多用途水箱,从而增加了好氧条件下的水量与厌氧条件下的水量的比率,ii)NH4-NNlim和PO4-P> Plim时,以低速模式驱动DTA到搅拌厌氧处理过的水,从而15增加厌氧条件下的水量与有氧条件下的水量之比,iii)当NH4-N> Nlim和PO4-P> Plim时,减少要引入的废水量,或切换DTA从高速模式到低速模式或20停止驱动泵,从而降低厌氧条件下的水量与有氧条件下的水量的比值,并且iv)NH4-NNlim和PO4-PPlim时,以低速模式驱动DTA直到氮化合物的浓度25变为NH4-N = Nlim或磷化合物的浓度变为PO4-P-Plim,从而增加了厌氧条件下的水量与好氧条件下的水量的比。

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