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Multistage anaerobic/anoxic/oxic activated sludge process

An activated sludge method, anoxic and aerobic technology, applied in aerobic and anaerobic process treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problem of increasing operation and management costs, synchronizing biological It is difficult to achieve a high level of phosphorus removal efficiency, and the volume of biological pools is small, so as to reduce the amount of excess sludge, solve the contradiction between denitrification and phosphorus removal, and save carbon sources.

Active Publication Date: 2012-06-13
中国市政工程西北设计研究院天津分院
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process has the advantages of saving carbon sources and high efficiency of nitrogen and phosphorus removal, but because it contains two internal reflux systems, the operation and management costs are increased; Multilevel Anoxic / Oxic (abbreviated as MAO) is based on The AAO deformation process developed by the traditional pre-denitrification process (AO) usually does not need to set up internal reflux facilities, and the volume of the biological pool is smaller than that of the ordinary phosphorus and nitrogen removal process. The average sludge concentration of the system is high and the nitrogen removal efficiency is high. High, easy to operate and manage
However, this process is mainly based on nitrogen removal, and it is difficult to achieve a high level of simultaneous biological phosphorus removal efficiency.

Method used

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  • Multistage anaerobic/anoxic/oxic activated sludge process
  • Multistage anaerobic/anoxic/oxic activated sludge process
  • Multistage anaerobic/anoxic/oxic activated sludge process

Examples

Experimental program
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Effect test

Embodiment 1

[0047] Achieve enhanced denitrification

[0048] The multi-stage anaerobic-anoxic-aerobic activated sludge process (MAAO) of the present invention is made up of four-stage anaerobic-anoxic-aerobic (AA'O), and each stage of AA'O consists of an anaerobic pool A, an anaerobic tank A Oxygen pool A' and an aerobic pool O are connected to each other in turn; sewage is equal flow rate Q 1 =Q 2 =Q 3 =Q 4 = 25% Q is sequentially distributed into the head end of the anaerobic tank at all levels, the total sludge return ratio is 100%, and part of the sludge return ratio is R 1 =70% return to the first stage anaerobic tank (A 1 ), the remaining sludge return ratio R 2 = 30% return to the first stage anoxic pool A' 1 . The total amount of mixed liquid in the anoxic tanks at all levels is 1.25Q, 1.5Q, 1.75Q, 2.0Q respectively. First tertiary anoxic pool mixture, part q 1 =Q,q 2 =1.25Q,q 3 = 1.25Q After the nitrification reaction is completed in the aerobic tank of this level, it ...

Embodiment 2

[0050] Realize enhanced denitrification and phosphorus removal

[0051] The multi-stage anaerobic-anoxic-aerobic activated sludge process (MAAO) of the present invention is made up of four-stage anaerobic-anoxic-aerobic (AA'O), and each stage of AA'O consists of an anaerobic pool A, an anaerobic tank A Oxygen pool A' and an aerobic pool O are connected to each other in turn; sewage is equal flow rate Q 1 =Q 2 =Q 3 =Q 4 = 25% Q is sequentially distributed into the head end of the anaerobic tank at all levels, the total sludge return ratio is 100%, and part of the sludge return ratio is R 1 = 70% return to the first stage anaerobic tank A 1 , the return ratio of the remaining sludge is R 2 = 30% return to the first stage anoxic pool A' 1 . The total amount of mixed liquid in the anoxic tanks at all levels is 1.25Q, 1.5Q, 1.75Q, 2.0Q respectively. Mixture of first three anoxic tanks, a part of q' 1 =Q,q' 2 = 1.25Q, q' 3 = 1.5Q directly enters the lower anaerobic tank f...

Embodiment 3

[0053] Low oxygen aeration energy saving operation

[0054] The above two implementations are implemented under the same working conditions. The aerobic tanks at all levels implement low-oxygen aeration, and the dissolved oxygen is between 0.2-1.0mg / l, which further saves aeration energy consumption and reduces operating costs.

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Abstract

The invention relates to a multistage anaerobic / anoxic / oxic (AAO) activated sludge process, which contains the following concrete technological steps of: M stages of AAO are combined and are connected with a sedimentation basin; sewage is distributed and enters into the head end of an anaerobic tank of each stage in the system respectively according to the flow; original sewage and one part of returned sludge in the sedimentation basin are mixed and then enter into the first-stage anaerobic tank; an effluent mixed liquor is mixed with the other part of the returned sludge and then a mixed liquor flows through the first-stage anoxic tank and the first-stage oxic tank...; after the second stage, the original sewage and a mixed liquor from the end of the last-stage anoxic tank are mixed and then enter into the m-stage anoxic tank and the m-stage aerobic tank; in circulation, an effluent of the final-stage aerobic tank enters into the sedimentation basin; part of the returned sludge from the sedimentation basin returns to the head end of the first-stage anaerobic tank, and the other part returns to the head end of the first-stage anoxic tank. The invention has beneficial effects of ''one carbon source for two uses'' and realization of denitrification and phosphorus uptake at the same time.

Description

technical field [0001] The invention belongs to sewage treatment technology, in particular to a multi-stage anaerobic-anoxic-aerobic activated sludge process. Background technique [0002] At present, the common activated sludge process generally has the following three types: [0003] 1. Anaerobic / Anoxic / Oxic (abbreviated as AAO) process is composed of three-stage biological treatment devices. The difference between it and the single-stage AO process is that an anaerobic reactor is set in the front stage, which aims to degrade and remove some refractory organic substances in the wastewater through the anaerobic process, thereby improving the biodegradability of the wastewater and providing for subsequent deficiencies. The oxygen section provides a carbon source suitable for the denitrification process, and finally achieves the purpose of efficiently removing COD, BOD, N, and P. The process flow of the AAO system is: the wastewater enters the anaerobic reactor after pretre...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F3/30
Inventor 刘胜军
Owner 中国市政工程西北设计研究院天津分院
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