CN206069650U - A kind of combination type MBR membrane bioreactors - Google Patents
A kind of combination type MBR membrane bioreactors Download PDFInfo
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- CN206069650U CN206069650U CN201621114340.8U CN201621114340U CN206069650U CN 206069650 U CN206069650 U CN 206069650U CN 201621114340 U CN201621114340 U CN 201621114340U CN 206069650 U CN206069650 U CN 206069650U
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- pond
- water
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- combination type
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- 239000012528 membrane Substances 0.000 title claims abstract description 66
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 53
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 20
- 230000003647 oxidation Effects 0.000 claims abstract description 19
- 238000004062 sedimentation Methods 0.000 claims description 13
- 239000000945 filler Substances 0.000 claims description 12
- 230000001413 cellular Effects 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 12
- 239000010865 sewage Substances 0.000 abstract description 11
- 239000010802 sludge Substances 0.000 abstract description 9
- 239000002351 wastewater Substances 0.000 abstract description 3
- 239000010815 organic waste Substances 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 description 15
- 230000000694 effects Effects 0.000 description 8
- 238000003756 stirring Methods 0.000 description 6
- 238000000926 separation method Methods 0.000 description 5
- 244000005700 microbiome Species 0.000 description 4
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 230000004907 flux Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 230000037250 Clearance Effects 0.000 description 2
- 241000276438 Gadus morhua Species 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000035512 clearance Effects 0.000 description 2
- 235000019516 cod Nutrition 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 230000000844 anti-bacterial Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005374 membrane filtration Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
Abstract
This utility model discloses a kind of combination type MBR membrane bioreactors, combination type MBR membrane bioreactors membrane module and inversion A 2/O, the combination of Biological Contact Oxidation Process, control fouling membrane can effectively be prevented and treated, the long service life of membrane module, with high-quality water outlet, the characteristics of high-efficiency activated sludge and higher nitrification efficiency can be maintained, can be widely used in the process of skyscraper and cell Treated sewage reusing, sanitary sewage disposal, high-concentration industrial organic waste water and organic wastewater.
Description
Technical field
This utility model is related to a kind of field of sewage treatment, more particularly to a kind of combination type MBR membrane bioreactors.
Background technology
As shortage of water resources and water pollution are on the rise, membrane bioreactor is returned with middle water as a kind of water pollution control
New and high technology and more and more paid attention to.Membrane bioreactor is one kind by film separation unit and biological processing unit
The new water technology for combining.As submerged membrane bioreactor (MBR) is with treatment effeciency is high, sludge yield is low
The features such as little with floor space, its research and application receive extensive concern.When particularly processing hospital wastewater, the water outlet of MBR
Concentration of suspension is very low, in sewage it is untreated fall antibacterial and virus lose barrier, so as to be also easy to be killed.However,
The application of membrane bioreactor is still affected by fouling membrane, so as to cause membrane flux less, cleans more difficult, and operational management is not
It is too convenient.
(Membrane bioreactor, referred to as (MBR) are a kind of by film separation unit and biological to membrane bioreactor
The new water technology that reason unit combines.The mud-water separation of traditional activated sludge process is completed in second pond, its point
The settling property of activated sludge is depended entirely on from rate.Membrane bioreactor is in tradition by the application of membrane in separation engineering
Waste Water Treatment, substitutes second pond with membrane filtration, improves mud-water separation efficiency, solve muddy water in traditional activated sludge process
Separate difficult, the big outstanding problem of sludge yield.Membrane biological reactor process, cannot with which compared with traditional activated sludge process
The advantage of analogy.Membrane bioreactor also has the advantages that not available for many other sewage water treatment methods, particularly water outlet water
Matter can meet current most stringent of sewage drainage standard, even emission request tightened up from now on.Membrane bioreactor makes
With problem present in the current sewage water treatment method of China can either be solved, sewage disposal is made to reach preferable effect；The opposing party
Face, membrane bioreactor floor space are little, are easy to the process of the various concentration sewage of various places, can be widely used in each row each
Industry, various places.
Membrane technology is developed rapidly in recent years as most potential water technology.With conventional biology
Treatment technology compares, and membrane bioreactor has the clearance height of pollutant, good anti impulsion load, stable effluent quality, surplus
The advantages of remaining sludge quantity is few.But in wastewater treatment process, although operating condition keeps constant, membrane flux still gradually can drop
It is low.So that cost for wastewater treatment increases, its popularization and application is affected.
The content of the invention
In order to solve the above problems；This utility model provides a kind of combination type MBR membrane bioreactors, combination type MBR
Membrane bioreactor membrane module and inversion A 2/O, the combination of Biological Contact Oxidation Process, can effectively prevent and treat control fouling membrane, film group
The long service life of part, with high-quality water outlet, the characteristics of high-efficiency activated sludge and higher nitrification efficiency can be maintained, can be extensive
Apply the process in skyscraper and cell Treated sewage reusing, sanitary sewage disposal, high-concentration industrial organic waste water and organic wastewater
On.
This utility model solves the technical scheme adopted by its technical problem：A kind of combination type MBR membrane bioreactors,
Using the cuboid framework of cellular, respectively six ponds of reactor point, anoxic pond, anaerobic pond, Aerobic Pond, sedimentation tank, biology
Contact-oxidation pool and membrane module pond；It is provided with anoxic pond on spiral tube, and the tube wall that spirals and opens up through hole；Spiral tube and water inlet pipe phase
Even；Water in water tank is squeezed into the water inlet on anoxic pond top by dosing pump by water inlet pipe, and water is from spiral tube outlet and through hole
Anoxic pond being exited into, turbulent flow being formed in anoxic pond, water enters anaerobic pond by anoxic pond bottom again；Anaerobic pond top is by a bend pipe
Aerobic Pond bottom is introduced, Aerobic Pond top introduces sedimentation tank bottom by a bend pipe, and the downflow weir on sedimentation tank top flow to biology and connects
Tactile oxidation pond, the hole of biological contact oxidation pond bottom flow to membrane module pond, are finally taking out from the membrane module installed in membrane module pond
Water outlet is filtered in the presence of sucking pump, water flow is by water ga(u)ge control, so that the operation of the reactor continuous-stable, described
Membrane module adopts curtain type film assembly.
Spiral tube is provided with anoxic pond, water is flowed out from spiral tube outlet and the through hole spiraled on tube wall, in anoxic pond
Agitating device need not be additionally installed, the water in anoxic pond can be formed from agitation formation and be circulated, and its stirring effect is uniform,
Overcome and uneven defect is stirred using what stirring paddle stirring was caused, improve the clean effect of anoxic pond, and be more suitable for
Combination type MBR membrane bioreactors continuously run.
Preferably, suspension-type combined filler is housed in biological contact oxidation pond, filler is at least by double annulars of two-layer
Frame and tow groups are into the net being made into for cordage in the interior annular at filler center.The filler of biological contact oxidation pond is using light
Matter, high-strength, anticorrosion, it is easy to the assembly that biofilm, specific surface area are big and voidage is high.Fibre bundle on suspension-type combined filler
Be easier to allow microorganism to adhere to, substantial amounts of apposition growth place is provided for microorganism.
Preferably, curtain type film assembly by square outer edges frame with hang over tow groups therein into.
Preferably, aerating system is set below the membrane module, and is connected with electromagnetic air pump, air mass flow is by being located at
Mass air flow sensor control on breather line, is conducive to increasing the cross-flow velocity on film surface.
A kind of combination type MBR membrane bioreactors of this utility model, its advantage is：
1) combination type MBR membrane bioreactors have good to the various contamination indexs such as COD, TOC, TN, TP and SS
Removal effect, with good capacity of resisting impact load.
2) membrane module and inversion A 2/O, the combination of Biological Contact Oxidation Process, refer to denitrogenation dephosphorizing and the various pollutions of process
Mark has reached good effect.
3) clearance of pollutant is different in the removal effect of different phase, and membrane bioreactor is to nitrogen, the removal master of phosphorus
Will be in anoxic pond, anaerobic pond and Aerobic Pond；The efficiency that biological contact oxidation pond is removed to which is not high effectively can remove COD,
TOC pollutant；Removal of the membrane module to SS is highly effective.
4) biological contact oxidation pond is set before membrane module, TOC is advantageously reduced, so as to reduces fouling membrane.Under membrane module
Side arranges aerating system and is beneficial to increase the cross-flow velocity on film surface, and the two combination can increase membrane flux, ensure membrane bioreaction
Answer the operation that device is steady in a long-term.
5) sedimentation tank adopts vertical sedimentation basin form, spatially increases the height of sedimentation tank, reduces combination type MBR films
The floor space of bioreactor.
Description of the drawings
With reference to the accompanying drawings and examples this utility model is further illustrated.
Fig. 1 is a kind of structural representation of combination type MBR membrane bioreactors of this utility model.
Fig. 2 is the structural representation of suspension-type combined filler.
Fig. 3 is the top view of suspension-type combined filler.
Fig. 4 is the structural representation of curtain type film assembly.
In figure, 1, anoxic pond, 2, anaerobic pond, 3, Aerobic Pond, 4, sedimentation tank, 5, biological contact oxidation pond, 6, membrane module pond,
11st, water tank, 12, dosing pump, 13, spiral tube, 14, the through hole spiraled on tube wall, 15, spiral tube outlet, 16, aeration system
System, 17, mass air flow sensor, 18, filler, 19, curtain type film assembly, 21, suction pump, 22, water ga(u)ge, 23, electromagnetic air pump,
24th, double annular stents, 25, tow groups, 26, the net being made into for cordage in the interior annular at filler center, 27, square outer edges
Frame, 28, the fibre bundle hung in square outer edges frame.
Specific embodiment
Refer to Fig. 1, a kind of combination type MBR membrane bioreactors of this specific embodiment, using the cuboid frame of cellular
Frame, respectively six ponds of reactor point, anoxic pond, anaerobic pond, Aerobic Pond, sedimentation tank, biological contact oxidation pond and membrane module pond；
It is provided with anoxic pond on spiral tube, and the tube wall that spirals and opens up through hole；Spiral tube is connected with water inlet pipe；Water in water tank is by dosing pump
The water inlet on anoxic pond top is squeezed into by water inlet pipe, water exits into anoxic pond from spiral tube outlet and through hole, in anoxia
Pond forms turbulent flow, and water enters anaerobic pond by anoxic pond bottom again；Anaerobic pond top introduces Aerobic Pond bottom, Aerobic Pond by a bend pipe
Top introduces sedimentation tank bottom by a bend pipe, and the downflow weir on sedimentation tank top flow to biological contact oxidation pond, bio-contact oxidation
The hole of pond bottom flow to membrane module pond, and water outlet is filtered in the presence of suction pump from the membrane module installed in membrane module pond finally,
Water flow is by water ga(u)ge control, so that the operation of the reactor continuous-stable, the membrane module adopts curtain type film assembly.
Spiral tube is provided with anoxic pond, water is flowed out from spiral tube outlet and the through hole spiraled on tube wall, in anoxic pond
Agitating device need not be additionally installed, the water in anoxic pond can be formed from agitation formation and be circulated, and its stirring effect is uniform,
Overcome and uneven defect is stirred using what stirring paddle stirring was caused, improve the clean effect of anoxic pond, and be more suitable for
Combination type MBR membrane bioreactors continuously run.
Aerating system is set below membrane module and is connected with electromagnetic air pump, air mass flow is by breather line
Mass air flow sensor is controlled, and is conducive to increasing the cross-flow velocity on film surface.
Fig. 2 and Fig. 3 is refer to, suspension-type combined filler is housed in biological contact oxidation pond, filler is at least by the double of two-layer
Annular stent and tow groups are into the net being made into for cordage in the interior annular at filler center.Biological contact oxidation pond is filled out
Expect using lightweight, high-strength, anticorrosion, be easy to the assembly that biofilm, specific surface area are big and voidage is high.On suspension-type combined filler
Fibre bundle be easier to allow microorganism to adhere to, provide substantial amounts of apposition growth place for microorganism.
Refer to Fig. 4, curtain type film assembly by square outer edges frame with hang over tow groups therein into.
Exemplary description is carried out to this utility model above in conjunction with accompanying drawing, it is clear that realization of the present utility model is not received
The restriction of aforesaid way, as long as employing the various improvement that technical solutions of the utility model are carried out, or not improved says practical
New design and technical scheme are applied to other occasions, in protection model of the present utility model.
Claims (4)
1. a kind of combination type MBR membrane bioreactors, using the cuboid framework of cellular, six ponds of reactor point, respectively
Anoxic pond, anaerobic pond, Aerobic Pond, sedimentation tank, biological contact oxidation pond and membrane module pond, it is characterised in that：It is provided with anoxic pond
Through hole is opened up on spiral tube, and the tube wall that spirals；Spiral tube is connected with water inlet pipe；Water in water tank is beaten by water inlet pipe by dosing pump
Enter the water inlet on anoxic pond top, water exits into anoxic pond from spiral tube outlet and through hole, turbulent flow, water are formed in anoxic pond
Anaerobic pond is entered by anoxic pond bottom again；Anaerobic pond top introduces Aerobic Pond bottom by a bend pipe, and Aerobic Pond top is by a bend pipe
Sedimentation tank bottom is introduced, the downflow weir on sedimentation tank top flow to biological contact oxidation pond, the hole stream of biological contact oxidation pond bottom
To membrane module pond, water outlet is filtered in the presence of suction pump from the membrane module installed in membrane module pond finally, water flow is by water
Effusion meter is controlled, and the membrane module adopts curtain type film assembly.
2. a kind of combination type MBR membrane bioreactors according to claim 1, it is characterised in that：Biological contact oxidation pond
In be equipped with suspension-type combined filler, filler is at least by double annular stents and tow groups of two-layer into the inner circle at filler center
The net being made into for cordage on ring.
3. a kind of combination type MBR membrane bioreactors according to claim 1, it is characterised in that：Curtain type film assembly is by side
Shape outer rim with hang over tow groups therein into.
4. a kind of combination type MBR membrane bioreactors according to claim 1 or 2 or 3, it is characterised in that：The film group
Aerating system is set below part, and is connected with electromagnetic air pump, air mass flow is by the mass air flow sensor on breather line
Control.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621114340.8U CN206069650U (en) | 2016-10-11 | 2016-10-11 | A kind of combination type MBR membrane bioreactors |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621114340.8U CN206069650U (en) | 2016-10-11 | 2016-10-11 | A kind of combination type MBR membrane bioreactors |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206069650U true CN206069650U (en) | 2017-04-05 |
Family
ID=58440725
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621114340.8U Expired - Fee Related CN206069650U (en) | 2016-10-11 | 2016-10-11 | A kind of combination type MBR membrane bioreactors |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206069650U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467268A (en) * | 2018-12-06 | 2019-03-15 | 中国科学院合肥物质科学研究院 | A kind of waste water treatment system and its advanced treatment process for hospital wastewater |
-
2016
- 2016-10-11 CN CN201621114340.8U patent/CN206069650U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109467268A (en) * | 2018-12-06 | 2019-03-15 | 中国科学院合肥物质科学研究院 | A kind of waste water treatment system and its advanced treatment process for hospital wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zuo Changping Inventor before: Zuo Changping Inventor before: Li Meiying |
|
| CB03 | Change of inventor or designer information | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170405 Termination date: 20181011 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |