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MBR wastewater treatment system with deep denitrification and dephosphorization functions

A sewage treatment system and deep denitrification technology, applied in the field of MBR sewage treatment system, can solve the problems of high energy consumption of aerobic MBR operation and release of total nitrogen, so as to avoid the increase of effluent TN, alleviate slow membrane pollution, and improve the quality of effluent Effect

Active Publication Date: 2019-01-22
BEIJING ORIGINWATER TECH CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The purpose of the present invention is to overcome the shortcomings of high energy consumption and total nitrogen release of traditional aerobic MBR, and provide a sewage treatment system that strengthens endogenous denitrification and reciprocating MBR process for deep nitrogen and phosphorus removal, so as to improve the efficiency of raw sewage. Efficient utilization of carbon sources and effluent quality

Method used

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  • MBR wastewater treatment system with deep denitrification and dephosphorization functions

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Experimental program
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Effect test

Embodiment 1

[0033] Such as figure 1 The system shown consists of sequentially connected anaerobic tank 1, front anoxic tank 2, aerobic tank 3, rear anoxic tank 4 and membrane tank 5, where anaerobic tank 1, front anoxic tank 2 and rear anoxic Stirring devices 6 are respectively arranged in the tank 4 , aeration devices 7 are arranged in the aerobic tank 3 , and membrane stack devices 8 are arranged in the membrane tank 5 .

[0034] The membrane stacker 8 realizes horizontal reciprocating movement by setting the pull rod connected to the membrane stacker and the motor 9, the reciprocating motion of the membrane stacker relieves the membrane fouling, and avoids setting an aeration device in the membrane pool 5, thereby reducing the dissolution rate in the membrane pool oxygen concentration.

[0035] The membrane tank 5 and the anaerobic tank 1 are provided with a 1# sludge mixed liquid return pipe 10, and a 1# return pump 12 is arranged on the pipeline of the 1# sludge mixed liquid return ...

Embodiment 2

[0044] During operation, the influent COD concentration is 150-200mg / L, TN concentration is 30-35mg / L, TP concentration is 3-5mg / L, ammonia nitrogen concentration is about 30mg / L, and the TP concentration reaches 10mg / L, a small amount of nitrate nitrogen returned by the membrane pool is also denitrified. The front anoxic tank is the main denitrification and denitrification unit. The carbon source in the raw sewage and the nitrate nitrogen returned by the rear anoxic tank are removed under the action of denitrifying bacteria. The return flow can be controlled to ensure the nitrification of the front anoxic tank Nitrogen is sufficient to ensure full utilization of raw sewage carbon sources. Then the mixed solution enters the aerobic unit, and the dissolved oxygen concentration in the aerobic tank can reach 0.5mg / L. The nitrifying bacteria use oxygen to completely oxidize the ammonia nitrogen in the raw sewage into nitrate nitrogen, and the amount of aeration can be controlled t...

Embodiment 3

[0046] Influent COD concentration is 150-200mg / L, TN concentration is 30-35mg / L, TP concentration is 3-5mg / L, ammonia nitrogen concentration is about 30mg / L, sewage passes through anaerobic, pre-anoxic and aerobic units After the action, the concentration of nitrate nitrogen flowing into the anoxic pool is about 5-7mg / L. In order to achieve a higher effluent water quality goal, the carbon source dosing pump outside the anoxic pool is turned on to control a reasonable dosing amount and further denitrification The role is to remove the nitrate nitrogen in the rear anoxic pool, and increase the backflow flow from the rear anoxic pool to the forward anoxic pool to ensure the concentration of nitrate nitrogen in the front anoxic pool. The removal concentrations of TN in each biochemical unit were 1~2, 16~18, 0~1, 11~13, 2~3 mg / L, the removal amount of ΔTN was about 35 mg / L, and the TN removal load of the anoxic pool increased To 30~35mgN / gVSS·d, to achieve effluent TN<1mg / L.

[00...

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Abstract

The invention provides an MBR wastewater treatment system with deep denitrification and dephosphorization functions. The MBR wastewater treatment system sequentially comprises an anaerobic pool, a front anoxic pool, an aerobic pool, a rear anoxic pool and a membrane pool. The membrane pool does not contain an aeration part, a membrane set device realizes reciprocating motion through a mechanical transmission device, thus the membrane pollution problem is effectively solved, MBR process aeration energy consumption is further reduced, and the situation that the content of water outlet total nitrogen is increased due to excessive oxidation of sludge is further avoided. Through improvement for the membrane pool, the membrane pool directly returns a flow to the anaerobic pool, a process flow return form is simplified, and meanwhile, the situation that the biological dephosphorization effect is affected by flow return of DO and excessive nitrate nitrogen is further avoided. Through partitionaeration, the content of the DO of the control tail end of the aerobic pool is less than 0.1 mg / L, and the denitrification effect of the rear anoxic pool is improved, a flow return point and a rear dosing point are arranged at a middle section in the rear anoxic pool, thus denitrification of an internal source and an external source can be realized simultaneously, the denitrification cost is reduced, and when a carbon source is added externally, it can be ensured that the content of the water outlet total nitrogen is less than 1 mg / L. The MBR wastewater treatment system is used for municipalwastewater treatment and can realize earth surface IV-type water outlet when the carbon source is not added externally, wherein the content of TN is less than 5 mg / L, and the content of TP is less than 0.2 mg / L.

Description

【Technical field】 [0001] The invention relates to an MBR sewage treatment system capable of deep denitrification and phosphorus removal, and an operation method of the sewage treatment system. 【Background technique】 [0002] The high concentration of nitrogen and phosphorus pollutants in water bodies is the main cause of eutrophication in water bodies. Existing sewage treatment plant discharge standards (TN<15mg / L, TP<0.5mg / L) make the sewage discharge still cause a large burden on the water environment, and it is necessary to further improve the discharge water requirements of sewage treatment plants to alleviate water environmental pollution. In order to meet higher water quality requirements, sewage treatment plants usually add excessive carbon sources and phosphorus removal agents, which will inevitably increase the cost of sewage treatment, thus making it a technical upgrade for traditional sewage treatment plants to maintain economic efficiency while deeply remov...

Claims

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Application Information

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IPC IPC(8): C02F3/30C02F3/12C02F101/16
CPCC02F3/1268C02F3/30C02F3/308C02F2209/08C02F2209/14C02F2209/16C02F2209/22C02F2301/046Y02W10/10
Inventor 陈春生张朋川薛涛俞开昌黄霞戴日成贾海涛孙大阳
Owner BEIJING ORIGINWATER TECH CO LTD
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