A<2>/O-biology synchronous nitrogen and phosphorus removal device and method for urban sewage

A technology for simultaneous denitrification and dephosphorization, and urban sewage, is applied in the field of urban sewage improvement A2/O-biological simultaneous denitrification and dephosphorization device, which can solve the problems of affecting the phosphorus removal effect of the system, affecting the denitrification effect, adverse effects, etc. Considerable economic and environmental benefits, increasing infrastructure investment, and high-efficiency nitrogen and phosphorus removal

Active Publication Date: 2016-04-06
SOUTH CHINA UNIV OF TECH +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The A2/O process consists of anaerobic zone, anoxic zone, aerobic zone, sedimentation zone and two reflux systems. Its functions are anaerobic phosphorus release, anoxic denitrification denitrification, and aerobic nitrification phosphorus absorption. After the sludge and water are separated, the remaining sludge is discharged to remove phosphorus. The conventional A2/O process has the following disadvantages: 1. Since the anaerobic zone is in the front, the nitrate in the returning sludge will have an adverse effect on the anaerobic zone, affecting the phosphorus removal of the sys

Method used

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  • A&lt;2&gt;/O-biology synchronous nitrogen and phosphorus removal device and method for urban sewage
  • A&lt;2&gt;/O-biology synchronous nitrogen and phosphorus removal device and method for urban sewage
  • A&lt;2&gt;/O-biology synchronous nitrogen and phosphorus removal device and method for urban sewage

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Embodiment 1

[0037] Such as figure 1 As shown, a kind of urban sewage A 2 / O-Biological synchronous denitrification and phosphorus removal device, including pre-anoxic pool 7, anaerobic pool 8, anoxic pool 9, aerobic pool 10 and sedimentation pool 15, which are sequentially connected. The sewage lifting pump room 2, aeration grit chamber 3, water pump 5, and water inlet pipe 6 of the grid and fine grid are respectively transported to the pre-anoxic pool 7 and the anaerobic pool 8; the pre-anoxic pool 7, the anaerobic pool A submersible mixer 13 is respectively provided in the pool 8 and the anoxic pool 9, and a disc microporous aerator is provided at the bottom of the aerobic pool 10, and the disc microporous aerator is connected with an air compressor 12; and Adopt electromagnetic flow meter to control aeration rate, described aerobic tank 10 is connected with anaerobic tank 8 through nitrification mixed return pipeline 17, anoxic tank 9 is connected with anaerobic tank 8 through anoxic m...

Embodiment 2

[0043] A kind of urban sewage A based on said device 2 / O-biological synchronous denitrification and phosphorus removal method, including steps:

[0044] 1) The urban sewage after desanding is sent to the pre-anoxic pool 7 and the anaerobic pool 8 by the water pump 5;

[0045] 2) In the pre-anoxic tank 7, the carbon source provided by urban sewage is used to denitrify the nitrate nitrogen in the return sludge to remove the rich nitrate in the return sludge, thereby reducing or eliminating the effect of nitrate on anaerobic Influenced by the phosphorus release process, the remaining part of the urban sewage and the effluent from the pre-anoxic tank 7 are mixed in the anaerobic tank 8, and the phosphorus accumulating bacteria absorb the easily degradable volatile organic acids in the incoming water and store them in the body in the form of PHB. Release polyphosphate into water in the form of orthophosphate;

[0046] 3) The mixed solution after denitrification and phosphorus re...

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Abstract

The invention discloses an A<2>/O-biology synchronous nitrogen and phosphorus removal device for urban sewage. The device comprises a pre-anoxic pond, an anaerobic pond, an anoxic pond, an aerobic pond and a settling pond; the urban sewage is conveyed to the pre-anoxic pond and the anaerobic pond through a water inlet, a sewage lifting pump room with a coarse grille and a fine grille, an aeration grit basin, a water pump and a water inlet pipe; the interior of the pre-anoxic pond, the interior of the anaerobic pond and the interior of the anoxic pond are each provided with a submersible stirrer, the bottom of the aerobic pond is provided with an aerator, the aerobic pond is connected with the anaerobic pond through a nitration mixing reflux pipeline, the anoxic pond is connected with the anaerobic pond through an anoxic mixing reflux pipeline, one part of sludge at the bottom of the settling pond is conveyed to a sludge concentrating and dewatering room, and the other part of the sludge at the bottom of the settling pond is connected with the pre-anoxic pond through a reflux sludge pipeline. The invention further discloses an A<2>/O-biology synchronous nitrogen and phosphorus removal method for the urban sewage. According to the A<2>/O-biology synchronous nitrogen and phosphorus removal device and method for the urban sewage, the influence of nitrate on the anaerobic phosphorus releasing process is reduced or eliminated, the carbon source demands for anoxic denitrification nitrogen removing and anaerobic phosphate releasing are balanced, and the efficient nitrogen and phosphorus removal effects are achieved.

Description

technical field [0001] The invention relates to waste water treatment technology, in particular to a kind of urban sewage improvement A 2 / O- Biological synchronous nitrogen and phosphorus removal device and method. Background technique [0002] In the existing sewage and wastewater biological treatment process, the removal of nitrogen and phosphorus is much more complicated than the removal of carbon, which involves nitrogen nitrification, denitrification, microbial phosphorus release and phosphorus absorption, etc. The process of each of the above processes The purpose is different, and the requirements for microbial composition, matrix type and environmental conditions are also different. How to organically combine various appropriate reaction conditions in a water treatment device is an important topic. [0003] Since Wuhrmann established the post-denitrification process to remove nitrogen in urban sewage in 1932 using microbial endogenous sources, after more than half...

Claims

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Application Information

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IPC IPC(8): C02F3/30C02F101/10C02F101/16
CPCC02F3/305C02F3/308C02F2101/105C02F2101/16
Inventor 周娟周少奇柯浪文刘峙嵘张舟
Owner SOUTH CHINA UNIV OF TECH
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