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Sewage treatment system and method for nitrogen removal and phosphorus recovery

A sewage treatment system and sewage technology, applied in the direction of flotation water/sewage treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problem of high TP content in the effluent of the secondary sedimentation tank, waste of phosphorus, Increase the burden of biological phosphorus removal and other problems, achieve the effect of population advantage and activity enhancement, reasonable design, excellent ammonia nitrogen and total nitrogen effluent effect

Pending Publication Date: 2022-04-08
WUXI MUNICIPAL DESIGN INST
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, the discharge standards of domestic sewage plants usually have relatively strict nitrogen and phosphorus effluent indicators, so the AAO process with simultaneous denitrification and phosphorus removal and its deformation process are usually used in the design as the main biochemical treatment process of sewage treatment plants; AAO process is a process with simultaneous denitrification The phosphorus removal process is mainly composed of anaerobic section, anoxic section and aerobic section; the principle of the phosphorus removal process is to release phosphorus through anaerobic, aerobic excess phosphorus absorption, and discharge excess phosphorus absorption sludge to achieve removal The purpose of phosphorus in water; however, according to the "Survey Plan for Upgrading Urban Sewage Treatment Plants Based on New Local Standards" and the evaluation report on the operation of sewage treatment plants made by our unit, the anaerobic section of most sewage treatment plants is due to the drop of influent oxygen and The content of nitrate nitrogen is high, it is difficult to form an obvious anaerobic environment, and the lack of obvious anaerobic phosphorus release process causes the anaerobic pond to fail to perform the function of biological phosphorus removal but to operate as an anoxic pond, making it difficult to form effective biological phosphorus removal process, resulting in high TP content in the effluent of the secondary sedimentation tank. During the operation, excessive chemical phosphorus removal agents are often added to the end of the biological tank or into the secondary sedimentation tank to ensure the TP of the effluent water. Entering the anaerobic tank, further inhibiting the activity of phosphorus-accumulating microorganisms
[0003] On the other hand, after adding chemical phosphorus removal agents at the end of the aerobic tank, the sewage sludge mixture enters the secondary settling tank for mud-water separation, and part of the separated sludge is discharged to the sludge as residual sludge at the bottom of the secondary settling tank The thickening tank is concentrated; the sludge thickening tank is an anaerobic environment, which will produce a large amount of anaerobic phosphorus release phenomenon, and as the concentration process proceeds, it is necessary to continuously remove the supernatant rich in phosphate, and the supernatant usually enters The sewage pipe network in the factory area is aggregated to the front end of the entire treatment process and mixed with the influent water again, which increases the burden of biological phosphorus removal
[0004] According to the above introduction, in the traditional sewage system, the phosphorus element entering the sewage plant will eventually become part of the dried sludge and be transported to the outside of the plant for disposal. It is difficult to extract phosphate from the dried sludge mixed with a large amount of phosphate. The usual way out is incineration or landfill, resulting in a great waste of phosphorus

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  • Sewage treatment system and method for nitrogen removal and phosphorus recovery

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Embodiment 1

[0032] Such as figure 1 , the present embodiment provides a sewage treatment system for denitrification and phosphorus recovery, including a pretreatment system 1, a biological treatment system 2, an advanced treatment system 3, a sludge treatment system 4 and a phosphorus recovery system 5 connected in sequence, the pretreatment System 1 comprises coarse grid 11, fine grid and aerated grit chamber 12 and fine grid tank 13 connected in sequence, and described biological treatment system 2 comprises AO processing unit 21 and secondary sedimentation tank unit 22 connected in sequence, so The advanced treatment system 3 includes a denitrification filter 31, an air flotation tank 32 and a contact disinfection tank 33 connected in sequence; the sludge treatment system 4 includes a sludge thickening tank unit 41, a sludge conditioning tank 42 and sludge Dehydration machine room 43; the phosphorus recovery system 5 includes a phosphorus slag stirring tank 51, a phosphorus slag concen...

Embodiment 2

[0044] Such as figure 1 , the present embodiment provides a sewage treatment method for denitrification and recovery of phosphorus, which includes the following steps:

[0045] S1. The sewage enters the coarse grid 11, the fine grid and the aeration grit chamber 12 and the fine grid tank 13 in order to remove garbage, fine suspended matter and sludge sand particles in the sewage;

[0046] S2. The sewage treated by the fine grid pool 13 is transferred to the water intake channel of the AO treatment unit 21 through the biological pool water inlet main pipe 23, and the sewage is distributed in proportion to the anoxic pools at all levels through the water inlet branch pipe 24, and the sewage Ammonia nitrogen, total nitrogen, and organic matter are removed in the AO treatment unit, and each level of AO unit is equipped with a nitrifying liquid internal reflux system to strengthen the removal of total nitrogen; the muddy water mixture treated by the AO treatment unit 21 enters the ...

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Abstract

The invention provides a nitrogen removal and phosphorus recovery sewage treatment system which comprises a pretreatment system, a biological treatment system, an advanced treatment system, a sludge treatment system and a phosphorus recovery system which are connected in sequence, and the pretreatment system comprises a coarse screen, a fine screen, an aerated grit chamber and a fine screen tank which are connected in sequence; the biological treatment system comprises an AO treatment unit and a secondary sedimentation tank unit which are connected in sequence; the deep treatment system comprises a denitrification filter tank, an air floatation tank and a contact disinfection tank which are connected in sequence; the sludge treatment system comprises a sludge thickening tank unit, a sludge conditioning tank and a sludge dewatering machine room which are connected in sequence; the phosphorus recovery system comprises a phosphorus slag stirring tank, a phosphorus slag concentration tank and a phosphorus slag dehydration workshop which are connected in sequence. According to the sewage treatment system, the technological process is simple, all functional sections are reasonably arranged, the pretreatment system removes large suspended solids and inorganic sand grains, the biological treatment system strengthens removal of total nitrogen and organic matter, and the deep treatment system further removes TN and TP.

Description

technical field [0001] The invention relates to the technical field of sewage treatment, in particular to a sewage treatment system and method for denitrification and phosphorus recovery. Background technique [0002] At present, the discharge standards of domestic sewage plants usually have relatively strict nitrogen and phosphorus effluent indicators, so the AAO process with simultaneous denitrification and phosphorus removal and its deformation process are usually used in the design as the main biochemical treatment process of sewage treatment plants; AAO process is a process with simultaneous denitrification The phosphorus removal process is mainly composed of anaerobic section, anoxic section and aerobic section; the principle of the phosphorus removal process is to release phosphorus through anaerobic, aerobic excess phosphorus absorption, and discharge excess phosphorus absorption sludge to achieve removal The purpose of phosphorus in water; however, according to the ...

Claims

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Application Information

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IPC IPC(8): C02F9/14C02F11/04C02F11/12C02F11/14C02F11/122C01B25/26C02F1/24C02F1/50C02F1/52C02F3/30
CPCY02W10/10
Inventor 薛峰张万里冯仕训刘晋
Owner WUXI MUNICIPAL DESIGN INST
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