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Process and device for treating sewage through denitrification and dephosphorization by anaerobic-anoxic-oxic-anoxic (AAOA) plus membrane bioreactor (MBR) process

A sewage treatment, nitrogen and phosphorus removal technology, applied in the direction of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. Waste the energy consumption of blast aeration and other issues, and achieve the effect of improving the utilization rate of carbon source

Inactive Publication Date: 2012-07-11
GUANGZHOU MUNICIPAL ENG DESIGN & RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, due to the high gas-water ratio of the MBR membrane tank, the dissolved oxygen concentration of the mixed solution is as high as 5.0mg / L~10.0mg / L. If it is not used scientifically, not only the energy consumption of blast aeration is wasted, but also the Consumes a large amount of carbon sources available in sewage, which is not conducive to improving the water output effect of the entire sewage treatment system

Method used

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  • Process and device for treating sewage through denitrification and dephosphorization by anaerobic-anoxic-oxic-anoxic (AAOA) plus membrane bioreactor (MBR) process
  • Process and device for treating sewage through denitrification and dephosphorization by anaerobic-anoxic-oxic-anoxic (AAOA) plus membrane bioreactor (MBR) process
  • Process and device for treating sewage through denitrification and dephosphorization by anaerobic-anoxic-oxic-anoxic (AAOA) plus membrane bioreactor (MBR) process

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Embodiment Construction

[0030] The present invention will be further described below in conjunction with accompanying drawing.

[0031] refer to figure 1 , figure 2 , image 3 and Figure 4 , a kind of AAOA+MBR denitrification and dephosphorization sewage treatment process and device provided by the present invention, comprising anaerobic pool 1, anoxic pool 2, aerobic pool 3, rear anoxic pool 4 and MBR membrane pool connected in sequence 5. The anaerobic pool 1 and the anoxic pool 2 are connected by the first water delivery port 10, the anoxic pool 2 and the aerobic pool 3 are connected by the second water delivery port 20, and the aerobic pool 3 and the anoxic pool 4 are connected by the second water delivery port. The three water delivery ports 30 are connected, and the rear anoxic tank 4 and the MBR membrane tank 5 are connected by the fourth water delivery port 40. The MBR membrane tank 5 is provided with an MBR membrane module 6 and an aeration device 7, and the water outlet of the MBR memb...

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Abstract

The invention belongs to the technical field of the treatment of municipal sewage, and discloses a process and a device for treating sewage through denitrification and dephosphorization by an anaerobic-anoxic-oxic-anoxic (AAOA) plus membrane bioreactor (MBR) process. A rear anoxic tank is arranged on the basis of the traditional anaerobic-anoxic-oxic (A<2> / O) process flow; meanwhile, a membrane separation technology is used for substituting two sedimentation units of sedimentation tanks; according to the process, pre-treated sewage flows into an anaerobic tank, an anoxic tank and the rear anoxic tank respectively; and the sewage flows into an MBR tank through the anaerobic tank, the anoxic tank, an aerobic tank and the rear anoxic tank, is filtered by an MBR membrane component and is drained. By the process for treating the sewage, a carbon source in the sewage can be efficiently utilized by arranging the rear anoxic tank and changing influent and reflux modes, so that the denitrification and dephosphorization efficiency of the sewage is improved; and meanwhile, the membrane separation technology is used for increasing the concentration of activated sludge in the process for treating the sewage so as to realize the high-efficiency separation of mud and water in the sewage, so that the problems that the conventional process for treating the sewage is high in energy consumption, the floor area is large, and pollutants such as nitrogen, phosphorus and the like cannot be efficiently removed are solved. The water quality of effluent treated by the method meets the requirements of I-class A criteria of Integrated Wastewater Discharge Standard (GB 8978-1996).

Description

technical field [0001] The invention belongs to the technical field of urban sewage treatment. Background technique [0002] The shortage of water resources and energy and the deterioration of water environment quality have increasingly become the bottleneck of social and economic development. It is imperative to increase the rate and degree of sewage treatment, strengthen the efficiency of nitrogen and phosphorus removal in sewage treatment plants, and reduce the energy consumption of sewage treatment. With the improvement of the effluent quality of sewage treatment plants, the existing sewage treatment plants generally have insufficient carbon sources. How to improve the efficient utilization of carbon sources in the existing sewage treatment process and reduce the concentration of pollutants in the effluent is a problem that needs to be solved urgently. [0003] Among many nitrogen and phosphorus removal processes, anaerobic-anoxic-aerobic (A 2 / O) process is favored by...

Claims

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Application Information

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IPC IPC(8): C02F9/14
Inventor 隋军马振强李捷陈贻龙孙志民彭勃邱维杜成银
Owner GUANGZHOU MUNICIPAL ENG DESIGN & RES INST CO LTD
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