A sewage treatment method and device with both deep nitrogen and phosphorus removal and mud-water gravity separation

A technology of advanced treatment and gravity separation, applied in biological water/sewage treatment, water/sludge/sewage treatment, biological treatment devices, etc. The effect of large hydraulic load, long backwash interval and reduced treatment cost

Active Publication Date: 2018-06-01
刘国强
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Based on the above reasons, there is an urgent need for a low-cost, high-efficiency deep nitrogen and phosphorus removal process and a gravity flow membrane separation device, which can not only take advantage of the small footprint of the membrane bioreactor while completing the deep nitrogen and phosphorus removal It has the advantages of high load and low sludge output, and can overcome the disadvantages of easy membrane fouling, complicated operation and high energy consumption.

Method used

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  • A sewage treatment method and device with both deep nitrogen and phosphorus removal and mud-water gravity separation
  • A sewage treatment method and device with both deep nitrogen and phosphorus removal and mud-water gravity separation
  • A sewage treatment method and device with both deep nitrogen and phosphorus removal and mud-water gravity separation

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Embodiment 1

[0053] Such as figure 1 As shown, a kind of sewage treatment device of the present invention has both deep denitrification and dephosphorization and gravity separation of mud and water, including agitation pool 1, agitation second pool 2, aeration / stirring alternate pool 3, oxygenation pool 4, mud water gravity Separation device: The mud-water gravity separation device includes a membrane module 11, a clear water tank 5 and a backwashing device. The bottoms of the first stirring pool 1 and the second stirring pool 2 are connected, and both the first stirring pool 1 and the second stirring pool 2 are equipped with independent stirring devices 9 . The aeration / stirring alternate tank 3 is equipped with a stirring device 9, a first aeration device 10 and a mud water internal circulation device 8 (so that part of the mud water can flow back from the aeration / stirring alternate tank 3 to the second stirring tank 2), the first aeration The device is connected to the first blower 29...

Embodiment 2

[0070] This embodiment is the second embodiment of the present invention, and the difference from Embodiment 1 is that the water collection channel includes a water collection pipe 13, an electric valve 23 and a filtrate outlet pipe 28 that communicate with each other, and the water collection pipe 13 and the low liquid level line 14 are in the At the same level, the backwash suction pipe 24 is provided with a backwash pump 19, and the electric valve 23 is connected with the backwash pump 19 and the controller 18; the membrane element 12 is connected with the water collection pipe 13, and the filtrate outlet pipe 28 is connected with the clear water tank 5 Through, the backwash suction pipe 24 communicates with the clear water tank 5. All the other parts are identical with embodiment 1 with connection mode, as figure 2 shown. When the liquid level reaches the high liquid level line 15, the backwash pump 19 is started through the liquid level monitor 16 and the controller 18,...

Embodiment 3

[0072] This embodiment is the third embodiment of the present invention. The difference from Embodiment 1 is that the second aeration device 20 includes an aeration tube, and the membrane element 12 is a flat membrane element ( Figure 6 ), the angle formed by the flat membrane element and the bottom of the oxygenation tank 4 is 50~70°, and the aeration pipe is parallel to the flat membrane element. All the other parts are identical with embodiment 1 with connection mode, as image 3 shown. When the second blower 21 is started, the air bubbles will rise rapidly against the surface of the membrane, which will alleviate membrane fouling and increase the unit membrane flux.

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Abstract

The invention discloses a sewage treatment method and a sewage treatment device integrating deep nitrogen and phosphorous removing and sludge-water gravitational separation. The sewage treatment device comprises a stirring pond I, a stirring pond II, an aeration / stirring alternating pond, an oxygenating pond and a sludge-water gravitational separation device. The sewage treatment method for completing the deep nitrogen and phosphorous removing comprises the steps of firstly, enabling sewage to enter the stirring pond I to complete a hydrolyzing and phosphorous releasing process; secondly, enabling the sewage to enter the stirring pond II to complete nitrogen removal by denitrification; thirdly, enabling the sewage to enter the aeration / stirring alternating pond to complete a nitration reaction and dephosphorization by adsorption; finally, enabling the sewage to enter the oxygenating pond and the sludge-water gravitational separation device to further remove BOD (Biochemical Oxygen Demand), ammonia nitrogen and total phosphorous and complete the sludge-water gravitational separation. According to the sewage treatment method and the sewage treatment device integrating the deep nitrogen and phosphorous removing and the sludge-water gravitational separation, disclosed by the invention, dual anaerobic-anoxic-aerobic cycling is created, not only are advantages of a traditional nitrogen and phosphorous removing technology exerted, but also the bottlenecks of a traditional technology that backflow of a digestive solution is incomplete and organic matters are insufficiently utilized are completely solved, the efficiency of removing nitrogen and phosphorous in the sewage can be increased from 50 to 70 percent to 90 percent or more than 90 percent, and the content of the total nitrogen and the total phosphorous in outlet water can be respectively reduced to 3mg / L and 0.4mg / L when conventional municipal sewage is treated.

Description

technical field [0001] The present invention relates to a sewage treatment method and device, more specifically, to a sewage treatment method and device capable of deep denitrification and phosphorus removal and gravity separation of mud and water. Background technique [0002] Nitrogen and phosphorus are key pollutants that lead to eutrophication of water bodies, and are much more difficult to remove than COD and TSS. According to my country's "Pollutant Discharge Standards for Urban Sewage Treatment Plants" (GB 18918-2002) Class A standard, the effluent ammonia nitrogen, total nitrogen and total phosphorus should be less than 5, 15 and 0.5 mg / L respectively. However, my country's "Surface Water Environmental Quality Standards" (GB 3838-2002) stipulates that ammonia nitrogen, total nitrogen and total phosphorus in Class V water environment should be less than 2.0, 2.0 and 0.4 mg / L respectively. This means that even if the effluent of urban sewage treatment plants reaches t...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F3/30
CPCC02F3/302C02F2203/006C02F2209/42
Inventor 刘国强
Owner 刘国强
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