CN202322561U - Industrial park sewage treatment device - Google Patents

Industrial park sewage treatment device Download PDF

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Publication number
CN202322561U
CN202322561U CN2011204472268U CN201120447226U CN202322561U CN 202322561 U CN202322561 U CN 202322561U CN 2011204472268 U CN2011204472268 U CN 2011204472268U CN 201120447226 U CN201120447226 U CN 201120447226U CN 202322561 U CN202322561 U CN 202322561U
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CN
China
Prior art keywords
pond
baf
industrial park
pipeline
sewage treatment
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011204472268U
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Chinese (zh)
Inventor
于斌
刘文轩
王玉明
赵民
张爱青
张乃平
张佃林
赵亚平
赵宇鹏
李雅青
常晓华
李林瑗
荆志林
闫法龙
王伟
李国东
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Datong Coal Mine Group Co Ltd
Original Assignee
Datong Coal Mine Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Datong Coal Mine Group Co Ltd filed Critical Datong Coal Mine Group Co Ltd
Priority to CN2011204472268U priority Critical patent/CN202322561U/en
Application granted granted Critical
Publication of CN202322561U publication Critical patent/CN202322561U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

The utility model provides an industrial park sewage treatment device and aims to overcome the defects of individually using an A<2>/O process or a biological aerated filter (BAF) in the conventional industrial park sewage treatment process. The device comprises a high level water tank, an A<2>/O reactor, the BAF and a settling pond, wherein the high level water tank is connected with the bottom of an anaerobic pond through a pipeline; the top of an aerobic pond is connected with the settling pond through a pipeline; the upper part of the settling pond is connected with the BAF through a pipeline; aerators of which the aeration gas is supplied by an air compressor are arranged in the aerobic pond and the BAF; a nitrification liquid returning pipe and a nitrification liquid returning pump are arranged between the aerobic pond and an anoxic pond; and the bottom of the settling pond is connected with the bottom of the anaerobic pond through a sludge returning pipe which is provided with a sludge returning pump. The defects of high blockage possibility due to independent usage of the BAF and instable nitrogen content in discharged water due to independent usage of the A<2>/O process are overcome by the industrial park sewage treatment device, and the industrial park sewage treatment device is high in impact load resistance and has good denitrification and dephosphorization effects.

Description

A kind of industrial park waste disposal plant
Technical field
The utility model relates to a kind of sewage disposal device.
Background technology
At present, the A that adopt when handling industrial park sewage more 2/ O technology and biological aerated filter process.
A 2/ O technology is the mainstream technology of bio-denitrifying sewage dephosphorization, and it is on A/O technology basis, to have increased an oxygen-starved area, and system is made up of anaerobic pond, anoxic pond and three functional zone of Aerobic Pond.Get into anaerobic pond through the waste water of preliminary sedimentation tank post precipitation and returned sluge, the circulation nitrification liquid by Aerobic Pond with being pumped into anoxic pond.Carry out the release of phosphorus at anaerobic pond, carry out denitrification denitrogenation in anoxic pond, carry out nitrated and picked-up phosphorus at Aerobic Pond, water outlet is discharged through the second pond post precipitation.The flow process of this technology is comparatively simple, and working cost is lower, and has the effect of synchronous denitrification dephosphorizing, is that sewage treatment area is used more technology, but has the unsettled shortcoming of water outlet nitrogen content.
BAF (Biological aerated filter, be called for short BAF) technology comes across Europe in the seventies and eighties in 20th century, and it is on the basis of bio-contact oxidation, to introduce the thought of feedwater rapid filter and a kind of aerobic waste water treatment process that produces.This technology collection filters, bio-oxidation is three-in-one and biological absorption, can play the effect of second pond, sand filter and common aeration tank simultaneously, but has the problem of BAF strainer easy blocking.
Because the sewage situation in the industrial park is complicated, uses above treatment process effectively not handle sewage separately.
Summary of the invention
The purpose of the utility model is to adopt A in the sewage treatment process of existing industrial park separately in order to overcome 2The existing defective of/O technology or BAF provides a kind of industrial park waste disposal plant.
For realizing above-mentioned purpose, the technical scheme that the utility model adopts is: a kind of industrial park waste disposal plant comprises elevated tank, A 2/ O reactor drum, BAF pond and settling tank, A 2/ O reactor drum is made up of anaerobic pond, anoxic pond and three functional zone of Aerobic Pond; Elevated tank is connected with the bottom of anaerobic pond through pipeline; The Aerobic Pond top is connected with settling tank through pipeline; Settling tank top is connected with the BAF pond through pipeline; Be respectively arranged with the aeration head that aeration is provided by air in Aerobic Pond and the BAF pond, nitrification liquid return line and nitrification liquid reflux pump are housed between Aerobic Pond and the anoxic pond, the settling tank bottom is connected with the bottom of anaerobic pond through the mud return line that sludge reflux pump is housed.
Utilize lift pump that sewage is risen to elevated tank, sewage is at A 2In/O the reactor drum with the mud thorough mixing; Muddy water mixed solution overflow gradually gets into the settling tank deposition; Mud-water separation is passed through the water outlet of settling tank top to the BAF pond; A part of mud of settling tank is back in the anaerobic pond through sludge reflux pump, and another part is discharged from the shore pipe of settling tank bottom, and the nitrification liquid in the Aerobic Pond is back to anoxic pond.
The utility model sewage treatment facility adopts " A 2/ O technology and BAF " method that combines, overcome the problem of independent use BAF strainer easy blocking and used A separately 2The unsettled shortcoming of/O technology water outlet nitrogen content has good capacity of resisting impact load and denitrogenation dephosphorizing effect.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Among the figure, 1-elevated tank, 2-BAF pond, 3-settling tank, 4-anaerobic pond; The 5-anoxic pond, 6-Aerobic Pond, 7-air, 8-aeration head; 9-nitrification liquid reflux pump, 10-sludge reflux pump, 11-valve, 12-liquid meter; The 13-sewage draining exit, 14-ceramics filling, 15-gas meter, 16-whisking appliance.
Embodiment
As shown in Figure 1, the described a kind of industrial park of the utility model waste disposal plant comprises elevated tank 1, A 2/ O reactor drum, BAF pond 2 and settling tank 3, A 2/ O reactor drum is made up of anaerobic pond 4, anoxic pond 5 and 6 three functional zone of Aerobic Pond; Elevated tank 1 is connected with the bottom of anaerobic pond 4 through pipeline; Aerobic Pond 6 tops are connected with settling tank 3 through pipeline; Settling tank 3 tops are connected with BAF pond 2 through pipeline; Be respectively arranged with the aeration head 8 that aeration is provided by air 7 in Aerobic Pond 6 and the BAF pond 2, nitrification liquid return line and nitrification liquid reflux pump 9 are housed between Aerobic Pond 6 and the anoxic pond 5, settling tank 3 bottoms are connected with the bottom of anaerobic pond 4 through the mud return line that sludge reflux pump 10 is housed.Settling tank 3 can adopt the ramp type settling tank, in the settling tank 3 effluent weir is housed, and settling tank 3 bottoms also have sewage draining exit 13.Be filled with ceramics filling 14 in one section cell cavity of aeration head 8 tops in the BAF pond.Utilize air 7 that aeration is provided, aeration head 8 can adopt the silica sand micro porous aeration head, with support each aeration head 8 is evenly arranged, so both can make in the reactor drum aeration even, can make sewage thorough mixing in reactor drum again, and then improves treatment effect.
Valve 11 and liquid meter 12 are housed on the connecting pipeline of elevated tank 1 and anaerobic pond 4, are used for controlling and measuring the size of discharge, liquid meter 12 can adopt glass rotameter.
Gas meter 15 is housed on the escape pipe of air 7, is used for controlling and the measurement aeration rate.
In order to make sewage and mud at A 2Thorough mixing in the/O reactor drum, A 2In the anaerobic pond 4 of/O reactor drum and the anoxic pond 5 whisking appliance 16 is housed.

Claims (4)

1. an industrial park waste disposal plant comprises elevated tank (1), A 2/ O reactor drum, BAF pond (2) and settling tank (3), A 2/ O reactor drum is made up of anaerobic pond (4), anoxic pond (5) and (6) three functional zone of Aerobic Pond; It is characterized in that: elevated tank (1) is connected with the bottom of anaerobic pond (4) through pipeline; Aerobic Pond (6) top is connected with settling tank (3) through pipeline; Settling tank (3) top is connected with BAF pond (2) through pipeline; Be respectively arranged with the aeration head (8) that aeration is provided by air (7) in Aerobic Pond (6) and BAF pond (2); Nitrification liquid return line and nitrification liquid reflux pump (9) are housed between Aerobic Pond (6) and the anoxic pond (5), and settling tank (3) bottom is connected with the bottom of anaerobic pond (4) through the mud return line that sludge reflux pump (10) is housed.
2. industrial park according to claim 1 waste disposal plant is characterized in that: on the connecting pipeline of elevated tank (1) and anaerobic pond (4) valve (11) and liquid meter (12) are housed.
3. industrial park according to claim 1 and 2 waste disposal plant is characterized in that: gas meter (15) is housed on the escape pipe of air (7).
4. industrial park according to claim 1 and 2 waste disposal plant is characterized in that: A 2In anaerobic pond of/O reactor drum (4) and the anoxic pond (5) whisking appliance (16) is housed.
CN2011204472268U 2011-11-14 2011-11-14 Industrial park sewage treatment device Expired - Fee Related CN202322561U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011204472268U CN202322561U (en) 2011-11-14 2011-11-14 Industrial park sewage treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011204472268U CN202322561U (en) 2011-11-14 2011-11-14 Industrial park sewage treatment device

Publications (1)

Publication Number Publication Date
CN202322561U true CN202322561U (en) 2012-07-11

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Application Number Title Priority Date Filing Date
CN2011204472268U Expired - Fee Related CN202322561U (en) 2011-11-14 2011-11-14 Industrial park sewage treatment device

Country Status (1)

Country Link
CN (1) CN202322561U (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103395945A (en) * 2013-08-15 2013-11-20 武汉新天达美环境科技有限公司 Carbon-system carrier biological filtering pond system
CN105481201A (en) * 2016-01-26 2016-04-13 甘肃金桥水科技(集团)股份有限公司 Integrated sewage treatment and reuse device
CN106946355A (en) * 2017-05-23 2017-07-14 上海明奥环保科技有限公司 A kind of jet-flow aeration formula A/O integrated sewage treating apparatus and its sewage treatment process
CN107082540A (en) * 2017-06-27 2017-08-22 重庆大学 A kind of integrated sewage treating apparatus and its handling process
CN109867358A (en) * 2019-03-07 2019-06-11 杨林 A kind of high-salt sewage processing system and its pool capacity and aeration method of adjustment

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103395945A (en) * 2013-08-15 2013-11-20 武汉新天达美环境科技有限公司 Carbon-system carrier biological filtering pond system
CN105481201A (en) * 2016-01-26 2016-04-13 甘肃金桥水科技(集团)股份有限公司 Integrated sewage treatment and reuse device
CN106946355A (en) * 2017-05-23 2017-07-14 上海明奥环保科技有限公司 A kind of jet-flow aeration formula A/O integrated sewage treating apparatus and its sewage treatment process
CN106946355B (en) * 2017-05-23 2023-03-17 上海明奥环保科技有限公司 Jet aeration type A/O integrated sewage treatment device and sewage treatment process thereof
CN107082540A (en) * 2017-06-27 2017-08-22 重庆大学 A kind of integrated sewage treating apparatus and its handling process
CN109867358A (en) * 2019-03-07 2019-06-11 杨林 A kind of high-salt sewage processing system and its pool capacity and aeration method of adjustment
CN109867358B (en) * 2019-03-07 2020-05-08 杨林 High-salinity sewage treatment system and tank volume and aeration adjustment method thereof

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120711

Termination date: 20131114