Variable-volume improved A<2>/O deep nitrogen and phosphorus removal process for sewage

A deep denitrification, variable volume technology, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, aerobic and anaerobic process treatment, etc. Nitrogen effect, anaerobic tank phosphorus removal effect and other issues

Inactive Publication Date: 2015-02-11
CHINESE RES ACAD OF ENVIRONMENTAL SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] Traditional A 2 In the / O nitrogen and phosphorus removal process, due to the influence of dissolved oxygen and nitric acid oxygen carried in the return sludge, it has a certain impact on the phosphorus removal effect of the anaerobic tank
At the same time, the dissolved oxygen in this section consumes the carbon source in the raw sewage, which affects the subsequent denitrification effect, often leading to the traditional A 2 / O process can not achieve the best effect of nitrogen and phosphorus removal

Method used

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  • Variable-volume improved A&lt;2&gt;/O deep nitrogen and phosphorus removal process for sewage

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Embodiment Construction

[0011] Concrete flow process of the present invention and operating parameter are described as follows:

[0012] First, 5-25% of the flow of domestic sewage or industrial wastewater enters the pre-anoxic tank through the inlet pipe of the pre-anoxic tank, and 75-95% of the flow enters the anaerobic tank through the inlet pipe of the anaerobic tank. 50-150%, under the condition that the reflux ratio of nitrifying liquid is 100-200%, after improved A 2 / O pre-anoxic-anaerobic-anoxic-aerobic organic matter removal and denitrification and phosphorus removal treatment, the effluent meets the national first-class A discharge standard. At the same time, according to the different ratios of C:N:P in the sewage, in the pre-anoxic tank and anaerobic tank separator adjustment tank, anaerobic tank and anoxic tank separator adjustment tank, anoxic tank and aerobic tank separator Adjust the position of each partition in the adjustment tank, that is, change the volume ratio and hydraulic re...

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Abstract

The invention discloses a variable-volume improved A<2> / O deep nitrogen and phosphorus removal process for sewage, belongs to the field of urban sewage and industrial waste water treatment, and particularly relates to a deep nitrogen and phosphorus removal process for the sewage. Specific to the problem concerned with synchronous removal of organic matters and the problem of poor nitrogen and phosphorus removal effect in a conventional A<2> / O process, the process is characterized in that firstly, a pre-anoxic pool is arranged in front of an anaerobic pool to lower the influences of dissolved oxygen and nitric oxygen carried in returned sludge on the phosphorus removal effect, wherein 5-25 percent of sewage enters the pre-anoxic pool, and 75-95 percent of the sewage enters the anaerobic pool; and secondly, movable clapboards are arranged among the pre-anoxic pool, the anaerobic pool, an anoxic pool and an aerobic pool, and the volume ratio of each water pool can be adjusted flexibly according to the ratio of C:N:P in the sewage in order to change the hydraulic retention time of the sewage in each water pool. Meanwhile, the aim of deep nitrogen and phosphorus removal of the sewage is fulfilled under the condition that the inner reflux ratio is 100-200 percent and the sludge reflux ratio is 50-150 percent; and output water is stable, and reaches the national grade-A discharge standard.

Description

technical field [0001] The invention belongs to the field of urban domestic sewage and industrial wastewater treatment, and in particular relates to a process for deep denitrification and dephosphorization of sewage. Background technique [0002] Traditional A 2 In the / O nitrogen and phosphorus removal process, due to the influence of dissolved oxygen and nitric acid oxygen carried in the return sludge, it has a certain impact on the phosphorus removal effect of the anaerobic tank. At the same time, the dissolved oxygen in this section consumes the carbon source in the raw sewage, which affects the subsequent denitrification effect, often leading to the traditional A 2 The / O process cannot achieve the best effect of nitrogen and phosphorus removal. [0003] Improved A 2 / O process is in traditional A 2 On the basis of / O process, absorbing the advantages of MUCT and oxidation ditch process, the developed low energy consumption, simultaneous denitrification and dephosph...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14
CPCC02F3/30C02F2101/105C02F2101/16C02F2101/163C02F2101/166C02F2101/30
Inventor 林齐宋永会向连城田智勇孙晨
Owner CHINESE RES ACAD OF ENVIRONMENTAL SCI
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