CN207294317U - A kind of aerator of membrane bioreactor - Google Patents
A kind of aerator of membrane bioreactor Download PDFInfo
- Publication number
- CN207294317U CN207294317U CN201721029729.7U CN201721029729U CN207294317U CN 207294317 U CN207294317 U CN 207294317U CN 201721029729 U CN201721029729 U CN 201721029729U CN 207294317 U CN207294317 U CN 207294317U
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- China
- Prior art keywords
- sieve plate
- housing
- cavity
- aerator
- pipe portion
- 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
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- 239000012528 membrane Substances 0.000 title claims abstract description 49
- 238000005276 aerator Methods 0.000 title claims abstract description 30
- 238000005273 aeration Methods 0.000 claims abstract description 46
- 239000003292 glue Substances 0.000 claims abstract description 37
- 238000005192 partition Methods 0.000 claims abstract description 24
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 42
- 239000007788 liquid Substances 0.000 claims description 16
- 238000002347 injection Methods 0.000 claims description 4
- 239000007924 injection Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 13
- 230000004907 flux Effects 0.000 abstract description 5
- 230000008901 benefit Effects 0.000 abstract description 4
- 238000009285 membrane fouling Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 12
- 238000011010 flushing procedure Methods 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 7
- 238000003756 stirring Methods 0.000 description 7
- 239000010865 sewage Substances 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000011045 prefiltration Methods 0.000 description 3
- 230000008439 repair process Effects 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012510 hollow fiber Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000013011 mating Effects 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The utility model provides a kind of aerator of membrane bioreactor, including the housing of upper end opening, the first sieve plate, the second sieve plate and aeration component；The cavity of housing is separated into upper strata cavity and lower floor's cavity by the partition plate in housing, first sieve plate and the second sieve plate are spaced apart and arranged in the cavity of upper strata and parallel to the partition plate, cavity between the first sieve plate and the second sieve plate is injecting glue layer, cavity between the second sieve plate and partition plate is water-yielding stratum, using lower floor's cavity as into gas-bearing formation；First sieve plate and the second sieve plate be equipped with it is multiple be used to wear the sieve aperture that connects film wire, sieve aperture is to be arranged in array uniform intervals；Aeration component is the fitting structure equipped with upper port and lower port, and aeration component is sequentially passed through into gas-bearing formation, water-yielding stratum and injecting glue layer from bottom to top；Aeration component, which is located at into the position in gas-bearing formation, is equipped with air admission hole.The utility model has the advantages of simple in structure, cost and operating cost are low, and membrane flux is high, and membrane fouling control effect is good.
Description
Technical field
Membrane bioreactor is the utility model is related to, more specifically to a kind of aerator of membrane bioreactor.
Background technology
In recent years, application of the membrane technology in sewage treatment field is particularly the membrane bioreaction combined with bioreactor
Device (Membrane Bioreactor, abbreviation MBR) technique is answered to be received increasingly as a kind of new and effective sewage treatment process
Extensive concern.MBR is a kind of new water technology for mutually tying platform with biological processing unit by film separation unit, with membrane module
Substitution secondary settling tank keeps high activity sludge concentration to reduce sewage treatment facility occupation of land in the bioreactor, and by keeping low dirt
Mud load reduces sludge quantity.There is MBR techniques easy to operate, hydraulic detention time (HRT) to be separated with sludge age (SRT), sludge
The advantages that concentration is high, capacity of resisting impact load is strong, effluent quality is good.In membrane bioreactor, bioreactor is mainly completed
The degraded of dirty water pollutant；Film separation unit mainly completes separation of solid and liquid and some macromolecular compounds is played with retention work
With used film is generally ultrafiltration or microfiltration membranes.
In practical applications, since the membrane module of MBR in the process of running is vulnerable to pollution, flux depression, shadow are caused
The stable operation of membrane module is rung, fouling membrane is become the key issue of limitation MBR applications.Fouling membrane refers to suspended particulate, colloid
Particle or dissolubility larger molecular organics adsorb deposition in film surface and fenestra, cause membrane aperture to reduce or block, lead to film
Measure the phenomenon declined.
In the prior art, for the treatment effect prevented fouling membrane, improve MBR, generally using following methods：
1st, bio-aeration and air water cleaning combine.
" external hollow-fiber membrane bioreactor " (CN2755081Y), including hollow fiber bundle, band center connector
Gas-liquid distributor, shell, it can be achieved that feed liquid be uniformly distributed, the cleaning on the spot of membrane module, unit is easily managed and repairs, and filters
Performance is stablized.
It is this that cleaning method is carried out to film surface using air water upper up-flow while being supplied oxygen to unit, due to meeting biology
The aeration quantity of reaction can not possibly be very big, and the simple effect for relying on air-flow rising to wash film by rubbing with the hands is limited.
2nd, compressed air is added in backwash water.
" air water reverse flushing device of membrane bioreactor film " (CN2530940Y), is related to a kind of air water back washing device, its
Feature is that film is backwashed using compressed air, improves backwash effect.
This method utilizes a small amount of backwashing water, slows down the blocking of film, extends the service life of film, to a certain extent
Backwash effect is improved, but this method is remained in the aspect of recoil, and the effect for preventing the pollution of film is limited.
3rd, disturbance device is increased in the reactor.
" membrane bioreactor " (CNl727289A), including an at least pre-filter layer, at least one biological film unit, and at least
One disturbing flow device, the disturbing flow device are clipped among pre-filter layer and biological film unit, can disturb between pre-filter layer and biomembrane
Sewage among unit, has membrane bioreactor circulation height, Membrane cleaning is convenient, the membrane operations cycle is long, operating cost is low
Advantage.
This method strengthens film surface cleaning performance by improving the turbulence intensity of liquid stream, to slow down film surface pollution thing deposition,
It is effective to improve cleaning efficiency, but since disturbance device is staticizer, film surface is cleaned by the kinetic energy of liquid stream, can not in reflux ratio
Can it is too big in the case of cleaning performance it is limited.
In addition, in existing MBR, generally also there are following defect：A. individually designed bottom aerating system is needed, equipment is multiple
It is miscellaneous huge, it is of high cost；B. film wire uses a bundle of structure, and such dirt or suspended matter can not rinse between being clipped in film wire；C. film
Silk is directly adopted after tying up and fastened with glue, and causes to cause film wire from film structure because long-time left-right and front-back is swung in operational process
In come off；D. fan energy consumption is high when aerating system is stirred using wind turbine；E. maintenance process is complicated, and equipment and technical staff are required
It is high.
Utility model content
The technical problem to be solved by the utility model is to, there is provided a kind of simple in structure, cost and operating cost are low, film
Flux is high, the good aerator for membrane bioreactor of membrane fouling control effect.
In order to solve the above-mentioned technical problem, the utility model provides a kind of aerator of membrane bioreactor, it is wrapped
Include housing, the first sieve plate, the second sieve plate and the aeration component of upper end opening；Partition plate, the partition plate are equipped with the housing
The cavity of the housing is separated into upper strata cavity and lower floor's cavity, first sieve plate and the second sieve plate are positioned apart from
In the upper strata cavity and parallel to the partition plate, the cavity between first sieve plate and the second sieve plate is injecting glue
Layer, the cavity between second sieve plate and partition plate is water-yielding stratum, using lower floor's cavity as into gas-bearing formation；First sieve
Web plate and the second sieve plate be equipped with it is multiple be used to wear the sieve aperture that connects film wire, the sieve aperture is to be arranged in array uniform intervals；Institute
It is fitting structure to state aeration component, and the aeration component is equipped with upper port and lower port, described to be aerated component from bottom to top successively
Through described into gas-bearing formation, water-yielding stratum and injecting glue layer；The aeration component is equipped with air admission hole positioned at described into the position in gas-bearing formation；Institute
The bottom for stating housing is equipped with the water inlet being connected with the lower port, and the center of first sieve plate is equipped with and institute
The gas-liquid mixed outlet of upper port mating connection is stated, the center of second sieve plate is equipped with to be passed through for the upper port
The first connecting hole, the partition plate is equipped with the second connecting hole for being passed through for the lower port.
As the preferable scheme of the utility model, small, both ends gradually increase among the lumen diameter of the aeration component.
As the preferable scheme of the utility model, the air admission hole is internally tilted upward from the outside of the aeration component
Set.
As the preferable scheme of the utility model, the aeration component is stepped fitting structure, it includes being sequentially connected
Upper pipe portion, middle pipe portion and down leg, the outside diameter of the upper pipe portion is less than the outside diameter of the middle pipe portion, the outside diameter of the middle pipe portion
Less than the outside diameter of the down leg.
As the preferable scheme of the utility model, the upper pipe portion is through first sieve plate and second sieve
Between plate, upper end and the gas-liquid mixed outlet of the upper pipe portion coordinate, and the lower end of the upper pipe portion is connected with described first
Hole coordinates；The middle pipe portion is through between second sieve plate and the partition plate；The down leg is through the partition plate
Between the bottom of the housing, the upper end of the down leg coordinates and seals with second connecting hole, the down leg
Lower end coordinates and seals with the water inlet.
As the preferable scheme of the utility model, the junction of the middle pipe portion and down leg is equipped with baffle, the baffle
Outside diameter be more than second connecting hole internal diameter.
As the preferable scheme of the utility model, it is evenly arranged with the tube wall of the upper pipe portion multiple for glue injection
Groove.
As the preferable scheme of the utility model, the both ends open of the housing, wherein one end are equipped with water outlet component, another
End is equipped with air inlet component；The water outlet component includes being covered on first end casing of one end of the housing and is arranged at described
Water outlet mouthpiece on first end casing, the water outlet mouthpiece are connected with the water-yielding stratum；The air inlet component includes being covered on institute
State the second end casing of the other end of housing and the intake interface being arranged on second end casing, the intake interface with
It is described to be connected into gas-bearing formation.
As the preferable scheme of the utility model, the inner edge of the upper end opening of the housing is equipped with and first sieve plate
First screens of engaging；The inner wall of the housing is equipped with the second screens engaged with second sieve plate.
As the preferable scheme of the utility model, the position that the housing corresponds to the injecting glue layer is equipped with hole for injecting glue, and institute
Hole for injecting glue is stated close to the second sieve plate side.
Implement a kind of aerator of membrane bioreactor of the utility model, compared with prior art, have as follows
Beneficial effect：
(1) positioned at intervals carries out every film wire using sieve plate, and by the injecting glue in injecting glue layer, glue is flowed into film
In gap between silk and film wire, fully every film wire of cementation, efficiently solves the film wire beam of current bundle type structure in machine
Cause the phenomenon that film wire comes off because long-time left-right and front-back is swung in device operational process, while such design can make every film
Silk can be fully used, and improve the membrane flux of film wire；
(2) aeration component is arranged on the central area of film wire beam, and the gas-liquid two-phase fluid that aeration component discharges can
From inside film wire beam to navigating between film wire and film wire outside film wire beam, realize and film wire air stirring rinsed and water rinses,
During also effectively rinsed positioned at the film wire in film wire beam center region, without the place not flushed, flush efficiency is high, film
Prevention and cure of pollution effect is good, and strainability is stablized；
(3) air stirring flushing+water flushing will be become to stir flushing with wind turbine merely originally, greatlys save wind turbine energy
Consumption；
(4) injecting glue layer, water-yielding stratum, the design into gas-bearing formation and aeration component are attached to same component (i.e. housing), are not required to
Individually designed bottom aerating system is wanted, simple in structure, cost is low, and is easily managed and repairs.
Brief description of the drawings
In order to illustrate more clearly of the technical solution of the utility model embodiment, the attached drawing of embodiment will be made below simple
Ground introduction.
Fig. 1 is a kind of front view of the aerator of membrane bioreactor provided by the invention；
Fig. 2 is a kind of stereogram of the positive side line of vision of the aerator of membrane bioreactor provided by the invention；
Fig. 3 is a kind of stereogram of the dorsal part line of vision of the aerator of membrane bioreactor provided by the invention；
Fig. 4 is a kind of front view of the sieve plate of the aerator of membrane bioreactor provided by the invention；
Fig. 5 is a kind of front view of the sieve Slab element of the aerator of membrane bioreactor provided by the invention；
Fig. 6 is a kind of front view of the aeration component of the aerator of membrane bioreactor provided by the invention；
Fig. 7 is a kind of front view of the water outlet component of the aerator of membrane bioreactor provided by the invention；
Fig. 8 is a kind of front view of the air inlet gas component of the aerator of membrane bioreactor provided by the invention.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without creative efforts
All other embodiments obtained, shall fall within the protection scope of the present invention.
As shown in Figures 1 to 8, the preferred embodiment of the utility model, a kind of aerator of membrane bioreactor, it is wrapped
Include housing 1, the first sieve plate 2, the second sieve plate 3 and the aeration component 4 of upper end opening.Wherein, the housing 1 of the present embodiment is in length
Groove-like structure, certainly, can also other shapes structure, such as square groove-like structure in another embodiment.
Partition plate 5 is equipped with the housing 1, the cavity of the housing 1 is separated into the partition plate 5 upper strata cavity and lower floor is empty
Chamber, 2 and second sieve plate 3 of the first sieve plate are spaced apart and arranged in the upper strata cavity and parallel to the partition plates 5, with
Cavity between first sieve plate, 2 and second sieve plate 3 is injecting glue layer 6, between second sieve plate 3 and partition plate 5
Cavity be water-yielding stratum 7, using lower floor's cavity as into gas-bearing formation 8.Wherein, injecting glue layer 6 be used for fill epoxy resin, by film wire with
Aerator is connected and fixed；Water-yielding stratum 7 is used to export the clean drainage after film wire filtering；It is used for into gas-bearing formation 8 to aeration
Component 4 inputs gas.
First sieve plate, 2 and second sieve plate 3 be equipped with it is multiple be used to wear the sieve aperture 9 that connects film wire, the sieve aperture 9 is
Arrange in array uniform intervals, be thus spaced apart every film wire, make have what is passed through for fluid between film wire and film wire
Passage.
The aeration component 4 is fitting structure, and the aeration component 4 is equipped with upper port and lower port, the aeration component 4
Sequentially pass through from bottom to top described into gas-bearing formation 8, water-yielding stratum 7 and injecting glue layer 6；The aeration component 4 is positioned at described into gas-bearing formation 8
Position is equipped with air admission hole.Wherein, upper port is output terminal, and lower port is water purification input terminal, and air admission hole is gas input, thus
The fluid that discharges of aeration component 4 can from-inner-to-outer navigate between film wire and film wire, realize and film wire air stirred
Mix flushing and water rinses.
The operation principle of this aerator is, during treated sewage, water-yielding stratum 7 forms negative pressure under the action of pumping equipment,
Sewage in cesspool is entered in hollow channel by film wire membranous wall, and during which film separation unit carries out separation of solid and liquid, to some
Suspended particulate, colloidal particle or dissolubility larger molecular organics are trapped in film surface and fenestra and deposit, and the drainage after filtering
Into film wire hollow channel and flow to water-yielding stratum 7, realize the output of clean drainage, these drainages can make industry water, life water follows
Ring uses, the environmental protection of section source.When rinsing film wire, while by wind turbine to distinguished and admirable into the offer of gas-bearing formation 8 positive pressure, it is distinguished and admirable through being aerated component 4
Air admission hole enter inside it, another side provides aeration component 4 in positive pressure current using pressure water, and water flows through aeration component 4
Lower port enters inside it, and at this moment distinguished and admirable cross inside aeration component 4 with current mixes, and from the upper port for being aerated component 4
Release, be thus aerated the gas-liquid two-phase fluid that discharges of component 4 from inside film wire beam to navigate within outside film wire beam film wire with
Between film wire, realize and the flushing of film wire air stirring and water are rinsed.
It can be seen from the above that implementing the structure of above-mentioned aerator, compared with prior art, have the advantages that：It is first
First, positioned at intervals carries out every film wire using sieve plate, and by the injecting glue in injecting glue layer 6, glue is flowed into film wire and film
In gap between silk, fully every film wire of cementation, the film wire beam for efficiently solving current bundle type structure are run in machine
During because long-time left-right and front-back is swung cause the phenomenon that film wire comes off, while such design can make every film wire can
It is fully used, improves the membrane flux of film wire；Secondly, aeration component 4 is arranged on the central area of film wire beam, is aerated component 4
The gas-liquid two-phase fluid discharged can be realized pair from inside film wire beam to navigating between film wire and film wire outside film wire beam
Film wire air stirring rinses and water rinses, during also effectively rinsed positioned at the film wire in film wire beam center region, no punching
Wash less than place, flush efficiency is high, and membrane fouling control effect is good, and strainability is stablized；3rd, will originally merely with wind turbine come
Stirring flushing becomes air stirring flushing+water and rinses, and greatlys save fan energy consumption；Finally, by injecting glue layer 6, water-yielding stratum 7, air inlet
The design of layer 8 and aeration component 4 is attached to same component (i.e. housing 1), it is not necessary to individually designed bottom aerating system, structure letter
Single, cost is low, and is easily managed and repairs.
The first sieve plate 2, the second sieve plate 3 and aeration component 4 assemble for convenience, the bottom of the housing 1 be equipped with
The water inlet 10 that the lower port is connected, the center of first sieve plate 2, which is equipped with to coordinate with the upper port, to be connected
The gas-liquid mixed outlet 11 connect, the center of second sieve plate 3 are equipped with the first connection passed through for the upper port
Hole 12, the partition plate 5 are equipped with the second connecting hole 13 passed through for the lower port.The aeration component 4 is stepped pipe fitting
Structure, it includes sequentially connected upper pipe portion, middle pipe portion and down leg, and the outside diameter of the upper pipe portion is less than the outer of the middle pipe portion
Footpath, the outside diameter of the middle pipe portion are less than the outside diameter of the down leg.The upper pipe portion through first sieve plate 2 with it is described
Between second sieve plate 3, upper end (upper port for being aerated component 4) and the gas-liquid mixed outlet 11 of the upper pipe portion are matched somebody with somebody
Close, the lower end of the upper pipe portion coordinates with first connecting hole 12；The middle pipe portion is through second sieve plate 3 and institute
State between partition plate 5；The down leg through between the partition plate 5 and the bottom of the housing 1, the upper end of the down leg with
Second connecting hole 13 coordinates and seals, lower end (lower port for being aerated component 4) and the water inlet of the down leg
10 coordinate and seal.The junction of the middle pipe portion and down leg is equipped with baffle, and the outside diameter of the baffle is more than described second and connects
Connect the internal diameter in hole 13.The inner edge of the upper end opening of the housing 1 is equipped with the first screens 15 engaged with first sieve plate 2；
The inner wall of the housing 1 is equipped with the second screens 16 engaged with second sieve plate 3.During assembling, will first component 4 be aerated
Lower port is inserted in water inlet 10 through the second connecting hole 13, and at this moment baffle is just stopped in the upper surface of partition plate 5, is realized and is exposed
Second sieve plate 3, is then directed at the upper end of aeration component 4 by the axially position of gas component 4 by the first connecting hole 12 thereon
Muzzle enters to predeterminated position (namely shoulder position between upper pipe portion and middle pipe portion), and at this moment the second sieve plate 3 is just by second
Screens 16 is blocked, finally the upper end muzzle by the first sieve plate 2 by 11 alignment aeration component 4 of gas-liquid mixed outlet thereon
Enter, at this moment the first sieve plate 2 is just blocked by the first screens 15, thus completes the first sieve plate 2, the second sieve plate 3 and aeration
Component 4 assembles.
Further, in the present embodiment, small, both ends gradually increase among the lumen diameter of the aeration component 4.It is such
Design effectively improves air lift effect, increases flow rate of water flow between film wire, improves the sluicing effect of film surface, further slows down film dirt
Dye.
Further, in the present embodiment, the air admission hole is internally tilted upward from the outside of the aeration component 4 and set
Put.Such design is able to ensure that will not have the lower port of air toward aeration component 4 to run under water pressures, gas leakage.
Further, in the present embodiment, it is evenly arranged with the tube wall of the upper pipe portion multiple for the recessed of glue injection
Groove.Specifically, the groove is equipped with 4, it is symmetrical arranged on described on the tube wall of pipe portion in two above and below both sides.It is such to set
Meter can make it is each the film block that film wire thereon forms be connected on by sieve Slab element 22 and wearing securely fix, so as to improve whole production
The stability and reliability of product structure.
Further, in the present embodiment, the both ends open of the housing 1, wherein one end are equipped with water outlet component, and the other end is set
There is air inlet component；The water outlet component includes being covered on first end casing 17 of one end of the housing 1 and is arranged at described
Water outlet mouthpiece 18 on first end casing 17, the water outlet mouthpiece 18 are connected with the water-yielding stratum 7；The air inlet component includes lid
The second end casing 19 and the intake interface 20 that is arranged on second end casing 19 arranged on the other end of the housing 1,
The intake interface 20 is connected with described into gas-bearing formation 8.Such design, optimizes the composition structure of housing 1, water outlet component and into
Gas component can be located away from housing 1, make the manufacturing of housing 1 simpler, while can be according to the requirement of client, binding modules
The sieve Slab element 22 of change designs the housing 1 of different length specification, and water outlet component and air inlet component are as both ends end cap
Structure is constant, is conducive to continue to use in follow-up products of different specifications, saves production cost, and production is more convenient, accurate, quick.
Further, in the present embodiment, the position that the housing 1 corresponds to the injecting glue layer 6 is equipped with hole for injecting glue 21, and described
Hole for injecting glue 21 is close to 3 side of the second sieve plate.Such design, on the one hand can convenient glue injection injecting glue layer 6 in, by film
Silk, aeration component 4, the first sieve plate 2 and the second sieve plate 3 and the sealing of housing 1 are fixed together, and improve the assembling effect of product
Rate, on the other hand since hole for injecting glue 21 is close to 3 side of the second sieve plate, for inversion state, (first sieves aerator during injecting glue
Web plate 2 is downward), ensure that glue and the first sieve plate 2 are fully be bonded, while prevent glue from filling in the case of injecting glue layer 6
Infiltered by the second sieve plate 3 in water-yielding stratum 7.
Above disclosed is only the preferred embodiment of the utility model, certainly cannot be new to limit this practicality with this
The interest field of type, therefore the equivalent variations made according to present utility model application the scope of the claims, still belong to the utility model and are covered
Scope.
Claims (10)
1. a kind of aerator of membrane bioreactor, it is characterised in that the housing including upper end opening, the first sieve plate,
Two sieve plates and aeration component；Partition plate is equipped with the housing, the cavity of the housing is separated into upper strata cavity by the partition plate
With lower floor's cavity, first sieve plate and the second sieve plate be spaced apart and arranged in the upper strata cavity and parallel to it is described every
Plate, the cavity between first sieve plate and the second sieve plate is injecting glue layer, between second sieve plate and partition plate
Cavity be water-yielding stratum, using lower floor's cavity as into gas-bearing formation；First sieve plate and the second sieve plate are equipped with multiple use
In wearing the sieve aperture that connects film wire, the sieve aperture is to be arranged in array uniform intervals；The aeration component is fitting structure, the aeration
Component is equipped with upper port and lower port, and the aeration component sequentially passes through described into gas-bearing formation, water-yielding stratum and injecting glue layer from bottom to top；
The aeration component is equipped with air admission hole positioned at described into the position in gas-bearing formation；The bottom of the housing is equipped with matches somebody with somebody with the lower port
The water inlet of connection is closed, the center of first sieve plate is equipped with the gas-liquid mixed being connected with the upper port and goes out
Mouthful, the center of second sieve plate is equipped with the first connecting hole passed through for the upper port, and the partition plate is equipped with can
The second connecting hole passed through for the lower port.
A kind of 2. aerator of membrane bioreactor as claimed in claim 1, it is characterised in that the pipe of the aeration component
Small, both ends gradually increase among intracavitary footpath.
3. a kind of aerator of membrane bioreactor as claimed in claim 1, it is characterised in that the air admission hole is described in
The outside of aeration component internally tilts upward setting.
4. a kind of aerator of membrane bioreactor as claimed in claim 1, it is characterised in that the aeration component is rank
Ladder type fitting structure, it includes sequentially connected upper pipe portion, middle pipe portion and down leg, the outside diameter of the upper pipe portion be less than it is described in
The outside diameter of pipe portion, the outside diameter of the middle pipe portion are less than the outside diameter of the down leg.
A kind of 5. aerator of membrane bioreactor as claimed in claim 4, it is characterised in that the upper pipe portion through
Between first sieve plate and second sieve plate, upper end and the gas-liquid mixed outlet of the upper pipe portion coordinate, institute
The lower end and first connecting hole for stating pipe portion coordinate；The middle pipe portion through second sieve plate and the partition plate it
Between；Through between the bottom of the partition plate and the housing, the upper end of the down leg connects the down leg with described second
Connect hole to coordinate and seal, the lower end of the down leg coordinates and seals with the water inlet.
6. a kind of aerator of membrane bioreactor as claimed in claim 4, it is characterised in that the middle pipe portion and down tube
The junction in portion is equipped with baffle, and the outside diameter of the baffle is more than the internal diameter of second connecting hole.
A kind of 7. aerator of membrane bioreactor as claimed in claim 4, it is characterised in that the tube wall of the upper pipe portion
On be evenly arranged with it is multiple for glue injection grooves.
8. a kind of aerator of membrane bioreactor as claimed in claim 1, it is characterised in that the both ends of the housing open
Open, wherein one end is equipped with water outlet component, and the other end is equipped with air inlet component；The water outlet component includes being covered on the one of the housing
First end casing at end and the water outlet mouthpiece being arranged on first end casing, the water outlet mouthpiece connect with the water-yielding stratum
It is logical；The air inlet component includes being covered on the second end casing of the other end of the housing and is arranged at second end casing
On intake interface, the intake interface connects with described into gas-bearing formation.
9. a kind of aerator of membrane bioreactor as claimed in claim 1, it is characterised in that open the upper end of the housing
The inner edge of mouth is equipped with the first screens engaged with first sieve plate；The inner wall of the housing is equipped with and second sieve
The second screens that board closes.
10. a kind of aerator of membrane bioreactor as claimed in claim 1, it is characterised in that the housing corresponds to institute
The position for stating injecting glue layer is equipped with hole for injecting glue, and the hole for injecting glue is close to the second sieve plate side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721029729.7U CN207294317U (en) | 2017-08-16 | 2017-08-16 | A kind of aerator of membrane bioreactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721029729.7U CN207294317U (en) | 2017-08-16 | 2017-08-16 | A kind of aerator of membrane bioreactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207294317U true CN207294317U (en) | 2018-05-01 |
Family
ID=62444438
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721029729.7U Expired - Fee Related CN207294317U (en) | 2017-08-16 | 2017-08-16 | A kind of aerator of membrane bioreactor |
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| Country | Link |
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| CN (1) | CN207294317U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107324489A (en) * | 2017-08-16 | 2017-11-07 | 广东优信力达环境科技有限公司 | A kind of aerator of membrane bioreactor |
-
2017
- 2017-08-16 CN CN201721029729.7U patent/CN207294317U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107324489A (en) * | 2017-08-16 | 2017-11-07 | 广东优信力达环境科技有限公司 | A kind of aerator of membrane bioreactor |
| CN107324489B (en) * | 2017-08-16 | 2024-07-19 | 江苏洪流环保机械有限公司 | Aeration device of membrane bioreactor |
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Granted publication date: 20180501 |