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An a2o-mbr sewage treatment device and method

A sewage treatment device and water outlet technology, applied in the field of A2O-MBR sewage treatment device, can solve the problems of high energy consumption, limited effluent water quality, poor phosphorus removal effect, etc., so as to reduce the energy consumption of the system operation, improve the effective utilization rate, The effect of saving the amount of aerobic aeration

Active Publication Date: 2016-02-17
GUANGZHOU MUNICIPAL ENG DESIGN & RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] However, the inherent defects of high energy consumption, high treatment cost, and poor phosphorus removal effect of the MBR process have also become bottlenecks in the popularization and application of this technology; The concentration of medium pollutants is usually low (CODcr concentration is usually lower than 300mg / L), and the current situation of one low and two high (low carbon and high nitrogen and phosphorus) in sewage leads to a low level of sludge load in urban sewage treatment plants. The decrease in activity limits the further improvement of effluent water quality; at the same time, the seasonal change of the actual influent water quality of the sewage plant, and the invariability of the existing treatment process also limit the improvement of the effluent water quality; The MBR process must adopt strong aeration to purge the membrane surface during operation, which brings a lot of energy consumption
These all limit the further popularization and application of the MBR process.
[0005]The traditional MBR process simply connects the biochemical tank and the membrane tank of the activated sludge treatment process (such as A2O, oxidation ditch or its variant process) in series. The connection is only maintained by the large ratio (300%~800%) reflux of the high-concentration mixed solution in the membrane pool. In addition, the two pools basically maintain independent operation; the high energy consumption and high cost of the MBR process are only from controlling the membrane cost. and membrane fouling, lack of systematic consideration of both

Method used

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  • An a2o-mbr sewage treatment device and method
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Examples

Experimental program
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Embodiment 1

[0045] Use the device of the present invention to carry out the method for sewage treatment, comprise steps: the sewage after pretreatment flows into anaerobic pond 22 and the second water inlet 2 respectively through first water inlet hole 1 and flows into anoxic pond 23; Under the action of the first water inlet hole 1, the sewage flowing into the anaerobic tank 22 is completely mixed with the anoxic tank mixed solution pumped through the first mixed solution return pump 18; the mixed solution after the biochemical treatment of the anaerobic tank 22 is The first water outlet hole 3 enters the anoxic pool 23, and under the action of the second agitator 13, it is completely mixed with the sewage flowing in from the second water inlet hole 2 and the mixed liquid in the aerobic pool pumped by the second mixed liquid return pump 19, And biochemical reaction takes place here; the mixed solution in the anoxic tank 23 flows into the aerobic tank partly through the second water outlet...

Embodiment 2

[0052] The difference between this embodiment and Example 1 is: the valve at the fourth water outlet in the anoxic pool is fully opened, the gate at the connecting hole between the first corridor and the second corridor in the aerobic pool, and the valve at the third water outlet The sluice gate is closed, the second mixed liquid return pump, the second aeration facility, and the third aeration facility are closed. The mixed solution treated in the anaerobic tank and the anoxic tank all flows into the membrane tank through the fourth outlet hole, the second pipe, and the fifth outlet hole; The three mixed liquid reflux pumps are pumped into the first corridor of the aerobic pool; the mixed liquid after the aerated biochemical reaction in the first corridor of the aerobic pool flows into the anoxic pool through the second outlet hole.

[0053] The schematic diagram of the technological process of this embodiment is shown in image 3 shown.

[0054] In this example, the amount...

Embodiment 3

[0056] This embodiment is different from Embodiment 2 in that: the first aeration facility, the second aeration facility, and the third aeration facility in the aerobic tank are all closed, and the push flow facility in the first corridor of the aerobic tank is opened; The high dissolved oxygen produced by the strong aeration of the membrane tank makes the mixed solution of the membrane tank pumped into the first corridor of the aerobic tank through the third mixed solution return pump still maintain a high dissolved oxygen. The first corridor of the oxygen pool can continue to carry out biochemical reactions such as aerobic nitrification, removal of ammonia nitrogen and other pollutants; Also in sequence naturally undergoes aerobic-anoxic habitats.

[0057] The schematic diagram of the technological process of this embodiment is shown in Figure 4 shown.

[0058] In this example, the amount of sewage entering the anaerobic pool and the anoxic pool after pretreatment (based ...

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Abstract

The invention discloses an A2O-MBR sewage treatment device, which comprises an anaerobic pool, an anoxic pool, an aerobic pool, and a membrane pool connected to each other in sequence, and the anoxic pool and the membrane pool are also connected. A sewage treatment method is also disclosed: the pretreated sewage flows into the anaerobic pool and the anoxic pool respectively; After the mixed solution enters the anoxic tank continuously, it is completely mixed with the inflowing pretreated sewage and the mixed solution returned from the aerobic tank; the mixed solution after the anoxic tank flows into the aerobic tank and the membrane tank respectively; the membrane tank is mixed Part of the liquid flows back into the first corridor of the aerobic pool, completely mixes with the mixed liquid flowing into the anoxic pool, pushes it to other corridors of the aerobic pool, and then flows into the membrane pool. The invention organically combines the A2O process and the MBR process, better solves the defects existing in the traditional A2O and MBR processes, improves the water quality of the effluent, greatly reduces the energy consumption of the system operation, reduces the cost of sewage treatment, and realizes energy saving and emission reduction.

Description

Technical field [0001] The invention is a sewage treatment technology field, involving A2O-MBR sewage treatment devices and methods. Background technique [0002] The worsening situation of the water environment has exacerbated the sewage treatment rate and the degree of treatment. At the same time, with the acceleration of the urbanization process, the degree of sewage treatment, the land for treatment facilities, and the surrounding surroundings after completion are completed.The adverse effects of the environment have put forward stricter requirements.Among them, the development and application of high -efficiency and low consumption sewage deep treatment processes have become a hot spot for current water environmental governance. [0003] MBR (membrane bioreactor) is a sewage treatment technology combining membrane separation technology with biological treatment. It has a good solid solid separation effect (using membrane filtering method) and small grounded area (eliminated ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/14
Inventor 李捷隋军
Owner GUANGZHOU MUNICIPAL ENG DESIGN & RES INST CO LTD
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