CN1789172A - Integrated sewage treatment equipment with multi-biomembrane - Google Patents
Integrated sewage treatment equipment with multi-biomembrane Download PDFInfo
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- CN1789172A CN1789172A CN 200510057464 CN200510057464A CN1789172A CN 1789172 A CN1789172 A CN 1789172A CN 200510057464 CN200510057464 CN 200510057464 CN 200510057464 A CN200510057464 A CN 200510057464A CN 1789172 A CN1789172 A CN 1789172A
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Abstract
The invention discloses an integral multistage biological membrane wastewater treating device, comprising tank, filling material, influent pipe and exhaust pipe. The said tank comprises a quaternary concentric circle, and the outer circle is separated into different reaction areas by baffle board with alternative operation of aerobic and anaerobic, semi-flexible composite filling material is equipped in every reaction area, the intermediate circle is filled with semi-flexible composite filling material, the inner circle is the settling area and the center is the sterilizing area. The said influent pipe is connected with the reaction areas of the outer circle, and supplies water in point, the reaction areas of the outer circle is connected with intermediate circle, inner circle and central sterilizing area in order through water pipe, the exhaust pipe is connected with the central sterilizing area to extends out and the underwater aerator is installed in the bottom of the outer circle and intermediate circle. The device is characterized by the resistance to impact load, high treating effect, low running energy consumption, small surplus sludge, short process, little accommodation area, low investment and convenient management.
Description
Technical field:
The invention belongs to sewage disposal, environmental protection technical field, be specifically related to a kind of integrated sewage treatment equipment with multi-biomembrane.
Background technology:
Do not see report at present both at home and abroad as yet relevant for integrated sewage treatment equipment with multi-biomembrane.In sewage disposal technology, general process for removing nitrogen and phosphor from sewage is A at present
2/ O and various improved form thereof, it all needs nitrification liquid and mud to reflux equipment to satisfy the requirement of denitrogenation dephosphorizing.In the practical engineering application, this technical process complexity, reactor unit is many, moves loaded down with trivial detailsly, and cost height and denitrogenation dephosphorizing effect are difficult to further improve.
Summary of the invention:
The present invention is directed to the deficiency that general dephosphorize denitrification reactor exists, designed a kind of integrated sewage treatment equipment with multi-biomembrane, save the mixed solution and the mud return-flow system of dephosphorization denitrogenation system complex, reduce the energy consumption in the sewage treatment process, reduce surplus sludge volume, simplify treatment process, improve the water treatment efficiency, reduce and take up an area of.
Technical scheme of the present invention is as follows:
This treatment facility comprises pond body, filler, dividing plate, swash plate, water inlet pipe and rising pipe etc., the pond body is made up of the level Four concentric(al) circles, wherein: outer shroud is divided into different reaction zones by the diaphragm plate, in establish the medium-soft combined stuffing, aerobic-anoxic alternate run in each district, each reaction zone all is connected to water inlet pipe, adopts the branch water inlet to strengthen carbon source and supplies with, make this reaction zone that the usefulness of stronger removal organism, nitrogen, phosphorus be arranged, the setting of dividing plate simultaneously can effectively prevent the short stream of current.In ring for aerobic reactor zone, in establish the medium-soft combined stuffing, be used for the guarantee and the mud decrement of effluent characteristics.Interior ring is the settling region, is used for mud-water separation, preferably adopts the swash plate structure to precipitate, and for the high town sewage of water inlet phosphorus concentration, can establish the reinforcement dephosphorization of the rich calcium of rich iron packing area on top, interior ring swash plate district.The pool center zone is a sterilizating area.By cross current, rising pipe is picked out by the center sterilizating area successively for each reaction zone of above-mentioned outer shroud and middle ring, interior ring and center sterilizating area.In addition, be furnished with underwater aeration device in described outer shroud, middle ring reaction zone bottom.
Sewage divides multiple spot to enter a plurality of reaction zones of outer shroud respectively continuously, these reaction zones are plural serial stage, current pass through successively, make each reaction zone alternately be in aerobic and anaerobic state by intermittent aeration simultaneously, so that make the microbial film of reaction zone when aerobic, carry out while nitration denitrification denitrogenation and suction phosphorus, microbial film is released phosphorus when anaerobism, the branch water inlet can improve denitrification denitrogenation and release the demand of phosphorus to carbon source, and the ring aerobic zone utilizes protozoon to carry out mud decrement in entering after outer shroud is finished dephosphorization denitrogenation; The ring depositing separation area carries out mud-water separation in entering subsequently, enters the center sterilizating area at last and handles back discharge system.Regularly from the depositing separation area spoil disposal.
Above-mentioned integrated equipment for wastewater treatment compared with prior art has following characteristics:
1. anti impulsion load, reactor for treatment usefulness height.
This treatment facility aerated reaction in the phase admixture of itself belong to typically hybridly fully, microbial film has higher sludge concentration in the reactor in addition, makes the reduction of F/M value, so anti impulsion load and adaptability are strong; By the medium-soft combined stuffing is set in reactor, and the suitable DO level of control, can form abundant microenvironment in that microbial film is inner, be easy to realize synchronous nitration denitrification denitrogenation, can realize synchronous nitration and denitrification efficiently.Simultaneously, the dividing plate subregion is set in reactor, carries out the aerobic-anoxic alternate run, and adopt the supply of the method reinforcement carbon source of branch water inlet, for the biomembrance process efficient dephosphorization has made up good environment by each district.Middle ring can be used as the guarantee district of effluent characteristics.In addition, can establish the rich calcium of rich iron packing area on top, interior ring swash plate district for the high town sewage of water inlet phosphorus concentration and strengthen dephosphorization, these have guaranteed that all treater obtains high processing usefulness.
2. need not to establish special mixed solution and mud reflux, operation energy consumption is low.
Usually the energy consumption cost in the sewage treatment process accounts for the large percentage of its running cost, and cutting down the consumption of energy is the key point that reduces running cost.The energy consumption of general sewage treatment process is mainly used in lifting, aeration and the nitrification liquid of sewage, the backflow of mud.This treatment facility can be realized synchronous nitration and denitrification efficiently by the medium-soft combined stuffing is set in reactor, saved the mixed-liquor return system.Simultaneously, the dividing plate subregion is set, and in each district, carries out the aerobic-anoxic alternate run,, saved the mud reflux of general dephosphorization system for the biomembrance process efficient dephosphorization has made up good environment at the reactor outer shroud.In addition, adopting biomembrance process to make up this treatment unit, saved general reactor required whipping device in anaerobic phosphorus release and anoxic denitrification process, is that treatment facility has efficient feature therefore.
3. surplus sludge volume is minimum.
In treatment facility, establish the medium-soft combined stuffing and reduced sludge yield, adopt sequencing batch biofilm decoupling zero connection technology and the molten born of the same parents of mud of middle ring and the decrement that microfauna sludge predation technology has been strengthened mud of outer shroud simultaneously by plural serial stage microbial film and longer microorganism food chain thereof.
4. technology brief, take up an area of less, low, the convenient management of investment.
This treatment facility utilizes reactor wall altogether with becoming one of technique unit treatment facilities such as biological dephosphorize denitrification, mud decrement, precipitation, sterilizations, has significantly reduced the investment and the occupation of land of equipment.The Inlet and outlet water Continuous Flow has the characteristics of convenient operation and management.
Description of drawings
Fig. 1 is the plane structure chart of this integrated sewage treatment equipment with multi-biomembrane;
Fig. 2 is the A-A sectional view of Fig. 1;
Fig. 3 is the B-B sectional view of Fig. 1.
Embodiment
Referring to Fig. 1,2 and Fig. 3, this integrated equipment for wastewater treatment includes pond body 1, water inlet pipe 2 and water shoot 3 etc.Pond body 1 adopts circular pond body, form by the level Four concentric(al) circles, body inside, pond is divided into four functional zone: outer shroud 4 is divided into different reaction zones by dividing plate 14, in establish medium-soft combined stuffing 8, aerobic-anoxic alternate run in each reaction zone, each reaction zone all is connected to water inlet pipe 2, and branch supplies water, and establishes the rising pipe 15 to middle ring.In ring 5 be aerobic zone, in establish medium-soft combined stuffing 8, and the water outlet 16 of interior ring extremely.Ring 5 bottoms are furnished with underwater aeration device 10 in above-mentioned outer shroud 4 reaches.Interior ring is settling region 6, in establish swash plate 9 (the long 0.5m of swash plate, spacing 0.1m, 60 ° of setting angles), and in the bottom of this settling region do concave configuration, form bucket 11, and be connected to shore pipe 12, and gate valve 13 is set, interior ring is provided with the water outlet 17 to center sterilizating area 7 equally, the central zone of pond body is a sterilizating area 7, picks out water pipe 3 in this district.
Main technical details:
The residence time: reaction zone total residence time: 4～10 hours, wherein: outer zone 2.4～6 hours, Central District 1.6～4 hours.The disengaging zone Nei Huan district residence time: 2～4 hours.
Structural parameter:
Integration apparatus specification D (m);
Central District available depth H outward,
1=H-0.3 (m);
Outer zone useful area A
1=Q * HRT
1/ H
Central District useful area A
2=Q * HRT
2/ H
Filler type: medium-soft combined fiber filler.
Claims (3)
1. integrated sewage treatment equipment with multi-biomembrane, comprise pond body, filler, water inlet pipe and rising pipe, it is characterized in that: this pond body is made up of the level Four concentric(al) circles, wherein outer shroud is divided into different reaction zones by dividing plate, and the aerobic-anaerobic alternate run is established the medium-soft combined stuffing in each reaction zone, middle ring is aerobic reactor zone, in establish the medium-soft combined stuffing, interior ring is the settling region, the center is a sterilizating area; Described water inlet pipe connects each reaction zone of outer shroud respectively, takes branch to supply water, and by cross current, rising pipe is picked out by the center sterilizating area successively for each reaction zone of outer shroud and middle ring, interior ring and center sterilizating area; Arrange underwater aeration device in described outer shroud, middle ring reaction zone bottom.
2. integrated sewage treatment equipment with multi-biomembrane according to claim 1 is characterized in that being: the settling region of interior ring is provided with swash plate, and there is bucket the bottom, settling region and is connected to shore pipe.
3, multi-stage biofilm integrated reactor according to claim 1 is characterized in that: establish the rich calcium of rich iron packing area on top, interior ring described sloping plate deposition district.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100574647A CN100344558C (en) | 2005-12-24 | 2005-12-24 | Integrated sewage treatment equipment with multi-biomembrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100574647A CN100344558C (en) | 2005-12-24 | 2005-12-24 | Integrated sewage treatment equipment with multi-biomembrane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1789172A true CN1789172A (en) | 2006-06-21 |
| CN100344558C CN100344558C (en) | 2007-10-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2005100574647A Expired - Fee Related CN100344558C (en) | 2005-12-24 | 2005-12-24 | Integrated sewage treatment equipment with multi-biomembrane |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100441521C (en) * | 2006-12-08 | 2008-12-10 | 重庆大学 | Peripherally-distributed water deflection composite reactor for hydrolysis and acidification |
| CN102010061A (en) * | 2010-10-28 | 2011-04-13 | 广州大学 | Nitrification and denitrification sewage treatment device and system |
| CN102642925A (en) * | 2012-04-28 | 2012-08-22 | 重庆大学 | Annular aeration biological filter sewage low carbon treatment reactor |
| CN103993627A (en) * | 2014-05-27 | 2014-08-20 | 中国电力工程顾问集团西北电力设计院 | Method for arranging reservoirs in indirect cooling tower |
| CN105174477A (en) * | 2015-09-25 | 2015-12-23 | 哈尔滨工业大学 | Annular flow-pushing type microfauna biological bed and method for treating wastewater sludge with the same |
| CN107010798A (en) * | 2017-06-15 | 2017-08-04 | 盐城工学院 | A kind of waste water treatment reactor |
| CN108439598A (en) * | 2018-05-02 | 2018-08-24 | 长沙中联重科环境产业有限公司 | Integrated sewage treating apparatus |
| CN109052814A (en) * | 2018-08-06 | 2018-12-21 | 铜陵市天峰汽车维修服务有限责任公司 | A kind of biomembrane filter tank of classification processing |
| CN110550731A (en) * | 2019-07-23 | 2019-12-10 | 长江大学 | Utilize magnetic force to optimize multistage membrane reaction unit of spiral MBR membrane module |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB9524404D0 (en) * | 1995-11-29 | 1996-01-31 | Anglian Water Services Ltd | Activated sludge treatment |
| US7045063B2 (en) * | 2002-07-26 | 2006-05-16 | The Regents Of The University Of California | Treatment of swine wastewater by biological and membrane separation technologies |
| CN2725288Y (en) * | 2004-09-20 | 2005-09-14 | 中国石油天然气股份有限公司 | Anaerobic and aerobic integrated fixed bed biofilm reactor |
| CN2846409Y (en) * | 2005-12-24 | 2006-12-13 | 重庆大学 | Combined multistage waste water treating device by biological film method |
-
2005
- 2005-12-24 CN CNB2005100574647A patent/CN100344558C/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100441521C (en) * | 2006-12-08 | 2008-12-10 | 重庆大学 | Peripherally-distributed water deflection composite reactor for hydrolysis and acidification |
| CN102010061A (en) * | 2010-10-28 | 2011-04-13 | 广州大学 | Nitrification and denitrification sewage treatment device and system |
| CN102010061B (en) * | 2010-10-28 | 2012-05-09 | 广州大学 | Nitrification and denitrification sewage treatment device and system |
| CN102642925A (en) * | 2012-04-28 | 2012-08-22 | 重庆大学 | Annular aeration biological filter sewage low carbon treatment reactor |
| CN102642925B (en) * | 2012-04-28 | 2014-02-12 | 重庆大学 | Annular aeration biological filter sewage low carbon treatment reactor |
| CN103993627A (en) * | 2014-05-27 | 2014-08-20 | 中国电力工程顾问集团西北电力设计院 | Method for arranging reservoirs in indirect cooling tower |
| CN103993627B (en) * | 2014-05-27 | 2015-07-15 | 中国电力工程顾问集团西北电力设计院有限公司 | Method for arranging reservoirs in indirect cooling tower |
| CN105174477A (en) * | 2015-09-25 | 2015-12-23 | 哈尔滨工业大学 | Annular flow-pushing type microfauna biological bed and method for treating wastewater sludge with the same |
| CN107010798A (en) * | 2017-06-15 | 2017-08-04 | 盐城工学院 | A kind of waste water treatment reactor |
| CN108439598A (en) * | 2018-05-02 | 2018-08-24 | 长沙中联重科环境产业有限公司 | Integrated sewage treating apparatus |
| CN109052814A (en) * | 2018-08-06 | 2018-12-21 | 铜陵市天峰汽车维修服务有限责任公司 | A kind of biomembrane filter tank of classification processing |
| CN110550731A (en) * | 2019-07-23 | 2019-12-10 | 长江大学 | Utilize magnetic force to optimize multistage membrane reaction unit of spiral MBR membrane module |
| CN110550731B (en) * | 2019-07-23 | 2021-12-24 | 长江大学 | Utilize magnetic force to optimize multistage membrane reaction unit of spiral MBR membrane module |
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| Publication number | Publication date |
|---|---|
| CN100344558C (en) | 2007-10-24 |
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Granted publication date: 20071024 Termination date: 20131224 |