CN106186564A - Membrane bioreactor sewage purification system and operational approach thereof - Google Patents
Membrane bioreactor sewage purification system and operational approach thereof Download PDFInfo
- Publication number
- CN106186564A CN106186564A CN201610750991.4A CN201610750991A CN106186564A CN 106186564 A CN106186564 A CN 106186564A CN 201610750991 A CN201610750991 A CN 201610750991A CN 106186564 A CN106186564 A CN 106186564A
- Authority
- CN
- China
- Prior art keywords
- immobilized microorganism
- purification system
- sewage purification
- membrane bioreactor
- microorganism ball
- 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.)
- Withdrawn
Links
- 239000012528 membrane Substances 0.000 title claims abstract description 114
- 239000010865 sewage Substances 0.000 title claims abstract description 107
- 238000000746 purification Methods 0.000 title claims abstract description 77
- 244000005700 microbiome Species 0.000 claims abstract description 138
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 64
- 230000006835 compression Effects 0.000 claims abstract description 31
- 238000007906 compression Methods 0.000 claims abstract description 31
- 230000000694 effects Effects 0.000 claims abstract description 21
- 230000001954 sterilising effect Effects 0.000 claims abstract description 18
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 18
- 239000010802 sludge Substances 0.000 claims description 31
- 239000011324 bead Substances 0.000 claims description 24
- 238000005276 aerator Methods 0.000 claims description 19
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 9
- 238000002360 preparation method Methods 0.000 claims description 6
- 230000002000 scavenging effect Effects 0.000 claims description 6
- 238000007605 air drying Methods 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 5
- 230000005484 gravity Effects 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 5
- 238000011084 recovery Methods 0.000 claims description 5
- 239000002904 solvent Substances 0.000 claims description 5
- 230000026676 system process Effects 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 claims description 2
- 230000002906 microbiologic effect Effects 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 230000000813 microbial effect Effects 0.000 abstract description 2
- 230000005611 electricity Effects 0.000 description 5
- 238000002161 passivation Methods 0.000 description 4
- 238000000926 separation method Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- VTEIFHQUZWABDE-UHFFFAOYSA-N 2-(2,5-dimethoxy-4-methylphenyl)-2-methoxyethanamine Chemical compound COC(CN)C1=CC(OC)=C(C)C=C1OC VTEIFHQUZWABDE-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 208000005156 Dehydration Diseases 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000011534 incubation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Activated Sludge Processes (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses membrane bioreactor sewage purification system and operational approach thereof, including anoxic pond, Aerobic Pond, MBR pond and sterilization pool；It is first turned on container, makes in immobilized microorganism ball inflow system, then the immobilized microorganism ball using time length is collected, the most again makes, regulate the compression of membrane module indirect and the cycle recovered and size further according to the water flow velocity in membrane cisterna；Immobilized microorganism ball used in membrane bioreactor sewage purification system and operational approach thereof can maintain the activity of microorganism, reduces fouling membrane；The effect in magnetic field makes immobilized microorganism ball be in suspended state, improves microbial activity；Immobilized microorganism ball can recycle, so that the microorganism in immobilized microorganism ball is in high activity state all the time, during the compression of membrane module indirect and recovering, make mud be difficult to be attached to film surface, and the mud having attached to membrane module surface can be removed.
Description
Technical field
The present invention relates to sewage treatment area, specially membrane bioreactor sewage purification system and operational approach thereof.
Background technology
China is the most unbalanced country of distribution of water resources, and the water resource that each place has is the most unbalanced, totally
On be a hydropenia country, the whole nation has the city of 70% to be in exsiccosis；China or a with serious pollution state of water simultaneously
Family, annual because water pollutes the loss caused accounts for the 2% of GDP, water pollution condition is constantly aggravated so that sewage disposal and regeneration
Industry is by unprecedented concern.
Being mainly used in denitrogenation in anoxic pond, nitrate nitrogen is back to anoxic pond by interior circulation by MBR pond；Aerobic Pond is used for
Except BOD, ammonia and nitrogen organic and nitrification and absorption phosphorus in water, Organic substance in water is decomposed into inorganic matter；MBR pond is used for purifying
Water, the water after MBR pond is filtered can be expelled directly out through sterilization again.
MBR is membrane bioreactor, carries the key player ensureing high-quality water quality output, is cut by the impurity in sewage
Staying through degrading to greatest extent, be achieved dirty water purification, sewage is in the reactor through having carried out a biological disposal upon to organic dirt
After the decomposition of dye material and conversion, utilize the high efficiency separation of micro-filtration membrane or ultrafilter membrane to complete the solid-liquid separation of sewage, thus reach
The final purification effect of sewage.The membrane module being arranged in reactor can replace the second pond in traditional handicraft and conventional mistake completely
Filter, absorbing unit, make hydraulic detention time and sludge age be kept completely separate, and obtains stable, the effluent quality of high-quality.
In sewage treatment area, film plays the biggest effect, how to improve the filter efficiency of film, and film purifies sewage
It is all to need to consider with urgently to be resolved hurrily that the of long duration mud occurred is attached to the solution on film surface, and that commonly uses uses high pressure
Gas or current impact inside film, and the harm causing film is relatively big, use different cycles to make electricity with the alternating current of size
Magnet produces intermittent magnetic, can more efficiently make mud be difficult to be attached to film surface, and can remove the most attached
In the mud on film surface.
Summary of the invention
It is an object of the invention to provide membrane bioreactor sewage purification system and operational approach thereof, to solve the above-mentioned back of the body
The problem proposed in scape technology.
For achieving the above object, the present invention provides following technical scheme: membrane bioreactor sewage purification system, including lacking
Oxygen pond, Aerobic Pond, MBR pond and sterilization pool；Sewage through filtering sequentially enters anoxic pond, Aerobic Pond and MBR pond, eventually passes
Discharging after sterilization pool sterilization, the immobilized microorganism ball of a part can be back to anoxic pond, another part by described MBR pond
It is expelled in collection device；
Described anoxic pond includes water inlet pipe, outlet pipe, container, aerator and magnetic field generator；In described Aerobic Pond
Including water inlet pipe, outlet pipe, aerator and magnetic field generator；Described MBR pond includes that water inlet pipe, outlet pipe, aeration fill
Put, return duct, collection device and membrane module；
Membrane module in described MBR pond connects outlet pipe；Described container is used for containing immobilized microorganism ball；Described
The bottom in MBR pond is provided with collection device, is used for collecting immobilized microorganism ball；The bottom in described MBR pond connects back to flow tube, uses
In the immobilized microorganism of a part is back to anoxic pond；
Described immobilized microorganism bag includes magnetizing mediums and activated sludge, described magnetizing mediums without magnetic, but can
Magnetizing under the influence of a magnetic field, described activated sludge is rich in microorganism；Described activated sludge is wrapped in magnetizing mediums, shape
Glomeration；Described magnetic field generator produces magnetic field, and then makes immobilized microorganism ball at described membrane bioreactor sewage
Cleaning system is in suspended state；
Described membrane module includes that membrane body, top cover, base and spring, described described membrane body include water-supply-pipe, water outlet
Mouth and film, be provided with electric magnet and Flow speed measurer in described top cover, described electric magnet is hollow ring structure, and centre is worn
Crossing water-supply-pipe, described electric magnet connects wire, and wire connects alternating-current power supply, so that electric magnet produces intermittent magnetic
Property, attracting to be positioned at the magnetizing mediums of base, described magnetizing mediums can be attracted by electric magnet；Described Flow speed measurer is used for measuring
Sewage flow rate of water flow；
Described spring is positioned at film, the surrounding of water-supply-pipe, and described spring connects top cover and base, the described electricity in top cover
The attraction of Magnet indirect is positioned at the magnetizing mediums of base, compression spring during attracting, and makes film also produce indirect
Compression, during the intermittent compression of film and restoring to the original state, makes mud be difficult to be attached to film surface, and can remove
Have attached to the mud on film surface；
By, in the case of different flow rate of water flow with alternating voltage, detecting the preferable scavenging effect of the alternating current of different cycles,
Draw equation below:
As 0≤v ＜ 0.5m/s, T=900s；
As 0.5≤v ＜ 1.0m/s, T=600s；
As 1.0≤v ＜ 1.5m/s, T=300s；
I=600v；
Wherein: T is ac period, unit is s；
I is alternating current size, and unit is mA；
V is sewage water velocity, and unit is m/s.
Preferably, the preparation of the described immobilized microorganism ball in membrane bioreactor sewage purification system with recovery is
By will be enriched in the activated sludge of microorganism by solvent be dissolved into thick after be sufficiently mixed with magnetizing mediums, then mixture is led to
Cross Mold Making become bead go forward side by side sector-style do；Bead after air-drying again is placed among magnetic field, under the active force in magnetic field, internal
Bead containing magnetizing mediums does not contains the bead of magnetizing mediums and separates with inside, and it is micro-that the internal bead containing magnetizing mediums is immobilization
Biological ball；Immobilized microorganism ball is used in described membrane bioreactor sewage purification system, and biological at described film
By arranging magnetic field generator generation magnetic field around reactor sewage purification system, make immobilized microorganism ball raw at described film
Thing reactor sewage purification system is in suspended state；Immobilized microorganism ball is in long-time use, and the activity on surface is dirty
Mud loses activity gradually, by closing magnetic field, makes immobilized microorganism ball sink to bottom by the gravity of self and reclaims,
Finally passing through to soak by the immobilized microorganism ball reclaimed, roll, centrifugal mode reclaims magnetizing mediums；Again the magnetic being recovered to is situated between
Matter and activated sludge are sufficiently mixed makes immobilized microorganism ball again.
Preferably, a diameter of 7 ~ 13mm of described immobilized microorganism ball.
Preferably, described magnetizing mediums is metallic nickel.
Preferably, described metallic nickel is the metallic nickel after Passivation Treatment.
Preferably, a diameter of 1 ~ 2mm of described magnetizing mediums.
Described membrane bioreactor sewage purification system, its operational approach is:
The first step, open container, make the immobilized microorganism ball of inside be flowed into described membrane bioreactor sewage purification system
In system；
Second step, open magnetic field generator and aerator, make that described membrane bioreactor sewage purification system is internal to be produced
Magnetic field, and then make immobilized microorganism ball be in suspended state in described membrane bioreactor sewage purification system；
3rd step, the outlet pipe in MBR pond is connected the outlet of upper water-supply-pipe one end；
4th step, opening conduits valve, make sewage be flowed in described membrane bioreactor sewage purification system；
5th step, being positioned in MBR pond by described membrane module, the flow velocity tachymeter being positioned at top cover is capable of detecting when water flow velocity
Degree；
6th step, the wire connected by electric magnet connect upper alternating current power supply, and are capable of detecting when water flow velocity by flow velocity tachymeter
Degree size, in conjunction with cycle and the size of formula regulation alternating current, makes electric magnet under the effect of alternating current, produces intermittent magnetic
Property, attract magnetizing mediums, compression spring during attracting, make film also produce the compression of indirect, by the intermittent pressure of film
During contracting and reinstatement, make mud be difficult to be attached to film surface, and the dirt having attached to film surface can be removed
Mud；
7th step, sewage are discharged after described membrane bioreactor sewage purification system processes；Immobilized microorganism ball exists
After described membrane bioreactor sewage purification system uses a period of time, it is flowed in the MBR pond not having magnetic field, a part
Immobilized microorganism ball be flowed in collection device, another part immobilized microorganism ball be back in anoxic pond circulation makes
With.
Compared with prior art, the invention has the beneficial effects as follows: described membrane bioreactor sewage purification system and
The immobilized microorganism ball that operational approach is used uses immobilized mode can make Microorganism incubation, and this mode is not
It is only capable of the activity maintaining microorganism, preferably purifies water, and can preferably make mud-water separation；Immobilized microorganism
A diameter of 7 ~ 13mm of ball, will not block fenestra, and can reduce fouling membrane, and the diameter of immobilized microorganism ball will not be because of
Too big and need bigger magnetic field that immobilized microorganism ball just can be made to suspend, sewage also will not straight because of immobilized microorganism ball
Footpath is too big and is difficult to touch the microorganism inside immobilized microorganism ball, and immobilized microorganism ball also will not be the least because of diameter
And be difficult to prepare and reclaim；Two, immobilized microorganism bag includes magnetizing mediums and activated sludge, and magnetizing mediums can be at externally-applied magnetic field
Make magnetizing mediums magnetize under effect, enable immobilized microorganism ball to be in suspended state under the influence of a magnetic field, thus have
It is beneficial to promote the circulation of microorganism and improve microbial activity, can preferably purify water；Immobilization is controlled by magnetic field
The mode of microorganism ball also will not make immobilized microorganism ball be damaged；Three, immobilized microorganism ball can recycle, and one
Aspect is due to the bacteria metabolism in immobilized microorganism ball and processes sewage for a long time, causes immobilized microorganism
Microorganism in ball is slowly old dead, uses the mode reclaimed periodically discharge and supplement immobilized microorganism ball, can make immobilization
Microorganism in microorganism ball is in high activity state all the time；On the other hand in water, flocculence or floating microorganism can be along with
Immobilized microorganism ball is discharged together, is possible to prevent microorganism to block fenestra, and it is fixing that the microorganism of discharge is also used as preparation
Change the raw material of microorganism ball；Four, described membrane module is by being internally provided with electric magnet at top cover, and chassis interior is provided with magnetic
Medium, is provided with spring between top cover and base, according to different sewage water flow velocities, electric magnet is passed to scavenging effect preferably
Ac period and size make membrane module produce intermittent contraction, and then make mud be difficult to be attached to film surface, and can
Removing the mud having attached to membrane module surface, simple to operate, effect is obvious.
Accompanying drawing explanation
Fig. 1 is the system structure schematic diagram of the present invention；
Fig. 2 is the structural representation of anoxic pond of the present invention；
Fig. 3 is the structural representation of Aerobic Pond of the present invention；
Fig. 4 is the structural representation in MBR pond of the present invention；
Fig. 5 is the structural representation of the immobilized microorganism ball of the present invention；
The structural representation of Fig. 6 position inventive film assembly；
Fig. 7 is schematic diagram under working condition of the present invention；
Fig. 8 is the top view of the present invention.
In figure: 1, anoxic pond, 2, Aerobic Pond, 3, MBR pond, 4, sterilization pool, 5, water inlet pipe, 6, outlet pipe, 7, container, 8, expose
Device of air, 9, magnetic field generator, 10, return duct, 11, collection device, 12, membrane module, 13, immobilized microorganism ball, 14, magnetic is situated between
Matter, 15, activated sludge, 16, membrane body, 17, water-supply-pipe, 18, outlet, 19, film, 20, top cover, 21, electric magnet, 22, flow velocity
Measuring instrument, 23, base, 24, magnetizing mediums, 25, spring.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Describe, it is clear that described embodiment is only a part of embodiment of the present invention rather than whole embodiments wholely.Based on
Embodiment in the present invention, it is every other that those of ordinary skill in the art are obtained under not making creative work premise
Embodiment, broadly falls into the scope of protection of the invention.
Embodiment 1:
Referring to Fig. 1-8, the present invention provides a kind of technical scheme: membrane bioreactor sewage purification system, including anoxic pond 1,
Aerobic Pond 2, MBR pond 3 and sterilization pool 4；Sewage through filtering sequentially enters anoxic pond 1, Aerobic Pond 2 and MBR pond 3, after warp
Discharging after crossing sterilization pool 4 sterilization, the immobilized microorganism ball 13 of a part can be back to anoxic pond 1 by MBR pond 3, another portion
Divide and be expelled in collection device 11；
Anoxic pond 1 includes water inlet pipe 5, outlet pipe 6, container 7, aerator 8 and magnetic field generator 9；Aerobic Pond 2 include into
Water pipe 5, outlet pipe 6, aerator 8 and magnetic field generator 9；MBR pond 3 includes water inlet pipe 5, outlet pipe 6, aerator 8, returns
Flow tube 10, collection device 11 and membrane module 12；
Membrane module 12 in MBR pond 3 connects outlet pipe 6；Container 7 is used for containing immobilized microorganism ball 13；The bottom in MBR pond 3
It is provided with collection device 11, is used for collecting immobilized microorganism ball 13；The bottom in MBR pond 3 connects back to flow tube 10, for by a part
Immobilized microorganism 13 be back to anoxic pond 1；
Immobilized microorganism ball 13 includes magnetizing mediums 14 and activated sludge 15, a diameter of 7mm of immobilized microorganism ball 13；Magnetic is situated between
Matter 14 is to be the metallic nickel after Passivation Treatment, a diameter of 1mm of magnetizing mediums 14, and magnetizing mediums 14 is without magnetic, but energy
Enough magnetizing under the influence of a magnetic field, activated sludge 15 is rich in microorganism；Activated sludge 15 is wrapped in magnetizing mediums 14, forms ball
Shape；Magnetic field generator 9 produces magnetic field, and then makes immobilized microorganism ball 13 be in membrane bioreactor sewage purification system
Suspended state；
Membrane module 12 includes membrane body 16, top cover 20, base 23 and spring 25, and membrane body 16 includes water-supply-pipe 17, outlet 18
With film 19, being provided with electric magnet 21 and Flow speed measurer 22 in top cover 20, electric magnet 21 is hollow ring structure, middle through defeated
Water pipe 17, electric magnet 21 connects wire, and wire connects alternating-current power supply, so that electric magnet 21 produces intermittent magnetic, inhales
Drawing the magnetizing mediums 24 being positioned at base 23, magnetizing mediums 24 can be attracted by electric magnet 21；Flow speed measurer 22 is used for measuring sewage water
Stream flow velocity；
Spring 25 is positioned at film 19, the surrounding of water-supply-pipe 17, and spring 25 connects top cover 20 and base 23, the electric magnet in top cover 20
The attraction of 21 indirect is positioned at the magnetizing mediums 24 of base 23, and compression spring 25 during attracting, between making film 19 also produce
The compression of connecing property, during the intermittent compression of film 19 and restoring to the original state, makes mud be difficult to be attached to film 19 surface, and
And the mud having attached to film 19 surface can be removed；
By, in the case of different flow rate of water flow with alternating voltage, detecting the preferable scavenging effect of the alternating current of different cycles,
Draw equation below:
As 0≤v ＜ 0.5m/s, T=900s；
As 0.5≤v ＜ 1.0m/s, T=600s；
As 1.0≤v ＜ 1.5m/s, T=300s；
I=600v；
Wherein: T is ac period, unit is s；
I is alternating current size, and unit is mA；
V is sewage water velocity, and unit is m/s.
The preparation of the immobilized microorganism ball 13 in membrane bioreactor sewage purification system and recovery are by will be enriched in
The activated sludge 15 of microorganism by solvent be dissolved into thick after be sufficiently mixed with magnetizing mediums 14, then mixture is passed through mould
Be fabricated to bead go forward side by side sector-style do；Bead after air-drying again is placed among magnetic field, under the active force in magnetic field, internal containing magnetic
The bead of medium 14 does not contains the bead of magnetizing mediums 14 and separates with inside, and it is micro-that the internal bead containing magnetizing mediums 14 is immobilization
Biological ball 13；Immobilized microorganism ball 13 is used in membrane bioreactor sewage purification system, and dirty at membrane bioreactor
Produce magnetic field by arranging magnetic field generator 9 around water purification system, make immobilized microorganism ball 13 dirty at membrane bioreactor
Water purification system is in suspended state；Immobilized microorganism ball 13 is in long-time use, and the activated sludge 15 on surface is gradually
Lose activity, by closing magnetic field, make immobilized microorganism ball 13 sink to bottom by the gravity of self and reclaim, finally
Passing through to soak by the immobilized microorganism ball 13 reclaimed, roll, centrifugal mode reclaims magnetizing mediums 14；Again the magnetic being recovered to is situated between
Matter 14 and activated sludge 15 are sufficiently mixed makes immobilized microorganism ball 13 again.
Membrane bioreactor sewage purification system, its operational approach is:
The first step, open container 7, make the immobilized microorganism ball 13 of inside be flowed into membrane bioreactor sewage purification system
In；
Second step, open magnetic field generator 9 and aerator 8, make that membrane bioreactor sewage purification system is internal produces magnetic field,
And then make immobilized microorganism ball 13 be in suspended state in membrane bioreactor sewage purification system；
3rd step, the outlet pipe 6 in MBR pond 3 is connected the outlet 18 of upper water-supply-pipe 17 one end；
4th step, opening conduits valve, make sewage be flowed in membrane bioreactor sewage purification system；
5th step, being positioned in MBR pond 3 by membrane module 12, the flow velocity tachymeter 22 being positioned at top cover 20 is capable of detecting when current
Speed is 0.2m/s；
6th step, the wire connected by electric magnet 21 connect upper alternating current power supply, and are capable of detecting when water by flow velocity tachymeter 22
Flow Velocity size, the cycle in conjunction with formula regulation alternating current is 900s, and alternating current size I=600v=600*0.2=120mA makes electricity
Magnet 21, under the effect of alternating current, produces intermittent magnetic, attracts magnetizing mediums 24, compression spring during attracting
25, make film 19 also produce the compression of indirect, during the intermittent compression of film 19 and restoring to the original state, make mud be difficult to
It is attached to film 19 surface, and the mud having attached to film 19 surface can be removed；
7th step, sewage are discharged after membrane bioreactor sewage purification system processes；Immobilized microorganism ball 13 is raw at film
After thing reactor sewage purification system uses a period of time, it is flowed in the MBR pond 3 not having magnetic field, the immobilization of a part
Microorganism ball 13 is flowed in collection device 11, and another part immobilized microorganism ball 13 is back in anoxic pond 1 recycle.
Embodiment 2:
Referring to Fig. 1-8, the present invention provides a kind of technical scheme: membrane bioreactor sewage purification system, including anoxic pond 1,
Aerobic Pond 2, MBR pond 3 and sterilization pool 4；Sewage through filtering sequentially enters anoxic pond 1, Aerobic Pond 2 and MBR pond 3, after warp
Discharging after crossing sterilization pool 4 sterilization, the immobilized microorganism ball 13 of a part can be back to anoxic pond 1 by MBR pond 3, another portion
Divide and be expelled in collection device 11；
Anoxic pond 1 includes water inlet pipe 5, outlet pipe 6, container 7, aerator 8 and magnetic field generator 9；Aerobic Pond 2 include into
Water pipe 5, outlet pipe 6, aerator 8 and magnetic field generator 9；MBR pond 3 includes water inlet pipe 5, outlet pipe 6, aerator 8, returns
Flow tube 10, collection device 11 and membrane module 12；
Membrane module 12 in MBR pond 3 connects outlet pipe 6；Container 7 is used for containing immobilized microorganism ball 13；The bottom in MBR pond 3
It is provided with collection device 11, is used for collecting immobilized microorganism ball 13；The bottom in MBR pond 3 connects back to flow tube 10, for by a part
Immobilized microorganism 13 be back to anoxic pond 1；
Immobilized microorganism ball 13 includes magnetizing mediums 14 and activated sludge 15, a diameter of 13mm of immobilized microorganism ball 13；Magnetic
Medium 14 is the metallic nickel for after Passivation Treatment, a diameter of 2mm of magnetizing mediums 14, magnetizing mediums 14 without magnetic, but
Can magnetize under the influence of a magnetic field, activated sludge 15 is rich in microorganism；Activated sludge 15 is wrapped in magnetizing mediums 14, is formed
Spherical；Magnetic field generator 9 produces magnetic field, and then makes immobilized microorganism ball 13 locate in membrane bioreactor sewage purification system
In suspended state；
Membrane module 12 includes membrane body 16, top cover 20, base 23 and spring 25, and membrane body 16 includes water-supply-pipe 17, outlet 18
With film 19, being provided with electric magnet 21 and Flow speed measurer 22 in top cover 20, electric magnet 21 is hollow ring structure, middle through defeated
Water pipe 17, electric magnet 21 connects wire, and wire connects alternating-current power supply, so that electric magnet 21 produces intermittent magnetic, inhales
Drawing the magnetizing mediums 24 being positioned at base 23, magnetizing mediums 24 can be attracted by electric magnet 21；Flow speed measurer 22 is used for measuring sewage water
Stream flow velocity；
Spring 25 is positioned at film 19, the surrounding of water-supply-pipe 17, and spring 25 connects top cover 20 and base 23, the electric magnet in top cover 20
The attraction of 21 indirect is positioned at the magnetizing mediums 24 of base 23, and compression spring 25 during attracting, between making film 19 also produce
The compression of connecing property, during the intermittent compression of film 19 and restoring to the original state, makes mud be difficult to be attached to film 19 surface, and
And the mud having attached to film 19 surface can be removed；
By, in the case of different flow rate of water flow with alternating voltage, detecting the preferable scavenging effect of the alternating current of different cycles,
Draw equation below:
As 0≤v ＜ 0.5m/s, T=900s；
As 0.5≤v ＜ 1.0m/s, T=600s；
As 1.0≤v ＜ 1.5m/s, T=300s；
I=600v；
Wherein: T is ac period, unit is s；
I is alternating current size, and unit is mA；
V is sewage water velocity, and unit is m/s.
The preparation of the immobilized microorganism ball 13 in membrane bioreactor sewage purification system and recovery are by will be enriched in
The activated sludge 15 of microorganism by solvent be dissolved into thick after be sufficiently mixed with magnetizing mediums 14, then mixture is passed through mould
Be fabricated to bead go forward side by side sector-style do；Bead after air-drying again is placed among magnetic field, under the active force in magnetic field, internal containing magnetic
The bead of medium 14 does not contains the bead of magnetizing mediums 14 and separates with inside, and it is micro-that the internal bead containing magnetizing mediums 14 is immobilization
Biological ball 13；Immobilized microorganism ball 13 is used in membrane bioreactor sewage purification system, and dirty at membrane bioreactor
Produce magnetic field by arranging magnetic field generator 9 around water purification system, make immobilized microorganism ball 13 dirty at membrane bioreactor
Water purification system is in suspended state；Immobilized microorganism ball 13 is in long-time use, and the activated sludge 15 on surface is gradually
Lose activity, by closing magnetic field, make immobilized microorganism ball 13 sink to bottom by the gravity of self and reclaim, finally
Passing through to soak by the immobilized microorganism ball 13 reclaimed, roll, centrifugal mode reclaims magnetizing mediums 14；Again the magnetic being recovered to is situated between
Matter 14 and activated sludge 15 are sufficiently mixed makes immobilized microorganism ball 13 again.
Membrane bioreactor sewage purification system, its operational approach is:
The first step, open container 7, make the immobilized microorganism ball 13 of inside be flowed into membrane bioreactor sewage purification system
In；
Second step, open magnetic field generator 9 and aerator 8, make that membrane bioreactor sewage purification system is internal produces magnetic field,
And then make immobilized microorganism ball 13 be in suspended state in membrane bioreactor sewage purification system；
3rd step, the outlet pipe 6 in MBR pond 3 is connected the outlet 18 of upper water-supply-pipe 17 one end；
4th step, opening conduits valve, make sewage be flowed in membrane bioreactor sewage purification system；
5th step, being positioned in MBR pond 3 by membrane module 12, the flow velocity tachymeter 22 being positioned at top cover 20 is capable of detecting when current
Speed is 0.9m/s；
6th step, the wire connected by electric magnet 21 connect upper alternating current power supply, and are capable of detecting when water by flow velocity tachymeter 22
Flow Velocity size, the cycle in conjunction with formula regulation alternating current is 600s, and alternating current size I=600v=600*0.9=540mA makes electricity
Magnet 21, under the effect of alternating current, produces intermittent magnetic, attracts magnetizing mediums 24, compression spring during attracting
25, make film 19 also produce the compression of indirect, during the intermittent compression of film 19 and restoring to the original state, make mud be difficult to
It is attached to film 19 surface, and the mud having attached to film 19 surface can be removed；
7th step, sewage are discharged after membrane bioreactor sewage purification system processes；Immobilized microorganism ball 13 is raw at film
After thing reactor sewage purification system uses a period of time, it is flowed in the MBR pond 3 not having magnetic field, the immobilization of a part
Microorganism ball 13 is flowed in collection device 11, and another part immobilized microorganism ball 13 is back in anoxic pond 1 recycle.
Embodiment 3:
Referring to Fig. 1-8, the present invention provides a kind of technical scheme: membrane bioreactor sewage purification system, including anoxic pond 1,
Aerobic Pond 2, MBR pond 3 and sterilization pool 4；Sewage through filtering sequentially enters anoxic pond 1, Aerobic Pond 2 and MBR pond 3, after warp
Discharging after crossing sterilization pool 4 sterilization, the immobilized microorganism ball 13 of a part can be back to anoxic pond 1 by MBR pond 3, another portion
Divide and be expelled in collection device 11；
Anoxic pond 1 includes water inlet pipe 5, outlet pipe 6, container 7, aerator 8 and magnetic field generator 9；Aerobic Pond 2 include into
Water pipe 5, outlet pipe 6, aerator 8 and magnetic field generator 9；MBR pond 3 includes water inlet pipe 5, outlet pipe 6, aerator 8, returns
Flow tube 10, collection device 11 and membrane module 12；
Membrane module 12 in MBR pond 3 connects outlet pipe 6；Container 7 is used for containing immobilized microorganism ball 13；The bottom in MBR pond 3
It is provided with collection device 11, is used for collecting immobilized microorganism ball 13；The bottom in MBR pond 3 connects back to flow tube 10, for by a part
Immobilized microorganism 13 be back to anoxic pond 1；
Immobilized microorganism ball 13 includes magnetizing mediums 14 and activated sludge 15, a diameter of 10mm of immobilized microorganism ball 13；Magnetic
Medium 14 is the metallic nickel for after Passivation Treatment, a diameter of 1.5mm of magnetizing mediums 14, magnetizing mediums 14 without magnetic, but
Being to magnetize under the influence of a magnetic field, activated sludge 15 is rich in microorganism；Activated sludge 15 is wrapped in magnetizing mediums 14, shape
Glomeration；Magnetic field generator 9 produces magnetic field, and then makes immobilized microorganism ball 13 in membrane bioreactor sewage purification system
It is in suspended state；
Membrane module 12 includes membrane body 16, top cover 20, base 23 and spring 25, and membrane body 16 includes water-supply-pipe 17, outlet 18
With film 19, being provided with electric magnet 21 and Flow speed measurer 22 in top cover 20, electric magnet 21 is hollow ring structure, middle through defeated
Water pipe 17, electric magnet 21 connects wire, and wire connects alternating-current power supply, so that electric magnet 21 produces intermittent magnetic, inhales
Drawing the magnetizing mediums 24 being positioned at base 23, magnetizing mediums 24 can be attracted by electric magnet 21；Flow speed measurer 22 is used for measuring sewage water
Stream flow velocity；
Spring 25 is positioned at film 19, the surrounding of water-supply-pipe 17, and spring 25 connects top cover 20 and base 23, the electric magnet in top cover 20
The attraction of 21 indirect is positioned at the magnetizing mediums 24 of base 23, and compression spring 25 during attracting, between making film 19 also produce
The compression of connecing property, during the intermittent compression of film 19 and restoring to the original state, makes mud be difficult to be attached to film 19 surface, and
And the mud having attached to film 19 surface can be removed；
By, in the case of different flow rate of water flow with alternating voltage, detecting the preferable scavenging effect of the alternating current of different cycles,
Draw equation below:
As 0≤v ＜ 0.5m/s, T=900s；
As 0.5≤v ＜ 1.0m/s, T=600s；
As 1.0≤v ＜ 1.5m/s, T=300s；
I=600v；
Wherein: T is ac period, unit is s；
I is alternating current size, and unit is mA；
V is sewage water velocity, and unit is m/s.
The preparation of the immobilized microorganism ball 13 in membrane bioreactor sewage purification system and recovery are by will be enriched in
The activated sludge 15 of microorganism by solvent be dissolved into thick after be sufficiently mixed with magnetizing mediums 14, then mixture is passed through mould
Be fabricated to bead go forward side by side sector-style do；Bead after air-drying again is placed among magnetic field, under the active force in magnetic field, internal containing magnetic
The bead of medium 14 does not contains the bead of magnetizing mediums 14 and separates with inside, and it is micro-that the internal bead containing magnetizing mediums 14 is immobilization
Biological ball 13；Immobilized microorganism ball 13 is used in membrane bioreactor sewage purification system, and dirty at membrane bioreactor
Produce magnetic field by arranging magnetic field generator 9 around water purification system, make immobilized microorganism ball 13 dirty at membrane bioreactor
Water purification system is in suspended state；Immobilized microorganism ball 13 is in long-time use, and the activated sludge 15 on surface is gradually
Lose activity, by closing magnetic field, make immobilized microorganism ball 13 sink to bottom by the gravity of self and reclaim, finally
Passing through to soak by the immobilized microorganism ball 13 reclaimed, roll, centrifugal mode reclaims magnetizing mediums 14；Again the magnetic being recovered to is situated between
Matter 14 and activated sludge 15 are sufficiently mixed makes immobilized microorganism ball 13 again.
Membrane bioreactor sewage purification system, its operational approach is:
The first step, open container 7, make the immobilized microorganism ball 13 of inside be flowed into membrane bioreactor sewage purification system
In；
Second step, open magnetic field generator 9 and aerator 8, make that membrane bioreactor sewage purification system is internal produces magnetic field,
And then make immobilized microorganism ball 13 be in suspended state in membrane bioreactor sewage purification system；
3rd step, the outlet pipe 6 in MBR pond 3 is connected the outlet 18 of upper water-supply-pipe 17 one end；
4th step, opening conduits valve, make sewage be flowed in membrane bioreactor sewage purification system；
5th step, being positioned in MBR pond 3 by membrane module 12, the flow velocity tachymeter 22 being positioned at top cover 20 is capable of detecting when current
Speed is 1.4m/s；
6th step, the wire connected by electric magnet 21 connect upper alternating current power supply, and are capable of detecting when water by flow velocity tachymeter 22
Flow Velocity size, the cycle in conjunction with formula regulation alternating current is 300s, and alternating current size I=600v=600*1.4=840mA makes electricity
Magnet 21, under the effect of alternating current, produces intermittent magnetic, attracts magnetizing mediums 24, compression spring during attracting
25, make film 19 also produce the compression of indirect, during the intermittent compression of film 19 and restoring to the original state, make mud be difficult to
It is attached to film 19 surface, and the mud having attached to film 19 surface can be removed；
7th step, sewage are discharged after membrane bioreactor sewage purification system processes；Immobilized microorganism ball 13 is raw at film
After thing reactor sewage purification system uses a period of time, it is flowed in the MBR pond 3 not having magnetic field, the immobilization of a part
Microorganism ball 13 is flowed in collection device 11, and another part immobilized microorganism ball 13 is back in anoxic pond 1 recycle.
The above, the only present invention preferably detailed description of the invention, but protection scope of the present invention is not limited thereto,
Any those familiar with the art in the technical scope that the invention discloses, according to technical scheme and
In addition equivalent or change are conceived in improvement, all should contain within the scope of the present invention.
Claims (7)
1. membrane bioreactor sewage purification system, it is characterised in that: include anoxic pond (1), Aerobic Pond (2), MBR pond (3) and
Sterilization pool (4)；Sewage through filtering sequentially enters anoxic pond (1), Aerobic Pond (2) and MBR pond (3), eventually passes sterilization pool
(4) discharging after sterilization, the immobilized microorganism ball (13) of a part can be back to anoxic pond (1) by described MBR pond (3),
Another part is expelled in collection device (11)；
Described anoxic pond (1) includes water inlet pipe (5), outlet pipe (6), container (7), aerator (8) and magnetic field generator
(9)；Described Aerobic Pond (2) includes water inlet pipe (5), outlet pipe (6), aerator (8) and magnetic field generator (9)；Described
MBR pond (3) include water inlet pipe (5), outlet pipe (6), aerator (8), return duct (10), collection device (11) and film group
Part (12)；
Membrane module (12) in described MBR pond (3) connects outlet pipe (6)；Described container (7) is used for containing the micro-life of immobilization
Thing ball (13)；The bottom in described MBR pond (3) is provided with collection device (11), is used for collecting immobilized microorganism ball (13)；Described
The bottom in MBR pond (3) connect back to flow tube (10), for the immobilized microorganism (13) of a part is back to anoxic pond (1)；
Described immobilized microorganism ball (13) includes magnetizing mediums (14) and activated sludge (15), described magnetizing mediums (14) without
Being magnetic, but can magnetize under the influence of a magnetic field, described activated sludge (15) is rich in microorganism；Described activity
Mud (15) is wrapped in magnetizing mediums (14), is formed spherical；Described magnetic field generator (9) produces magnetic field, and then makes immobilization micro-
Biological ball (13) is in suspended state in described membrane bioreactor sewage purification system；
Described membrane module (12) includes membrane body (16), top cover (20), base (23) and spring (25), described described film
Body (16) includes water-supply-pipe (17), outlet (18) and film (19), be provided with in described top cover (20) electric magnet (21) and
Flow speed measurer (22), described electric magnet (21) is hollow ring structure, middle through water-supply-pipe (17), described electric magnet
(21) connecting wire, wire connects alternating-current power supply, so that electric magnet (21) produces intermittent magnetic, attracts to be positioned at base
(23) magnetizing mediums (24), described magnetizing mediums (24) can be attracted by electric magnet (21)；Described Flow speed measurer (22) is used
In measuring sewage flow rate of water flow；
Described spring (25) is positioned at film (19), the surrounding of water-supply-pipe (17), described spring (25) connect top cover (20) with
Base (23), the attraction of described electric magnet (21) indirect in top cover (20) is positioned at the magnetizing mediums (24) of base (23),
Compression spring (25) during attracting, makes film (19) also produce the compression of indirect, by film (19) intermittent compression
During restoring to the original state, make mud be difficult to be attached to film (19) surface, and can remove and have attached to film (19) table
The mud in face；
By, in the case of different flow rate of water flow with alternating voltage, detecting the preferable scavenging effect of the alternating current of different cycles,
Draw equation below:
As 0≤v ＜ 0.5m/s, T=900s；
As 0.5≤v ＜ 1.0m/s, T=600s；
As 1.0≤v ＜ 1.5m/s, T=300s；
I=600v；
Wherein: T is ac period, unit is s；
I is alternating current size, and unit is mA；
V is sewage water velocity, and unit is m/s.
Membrane bioreactor sewage purification system the most according to claim 1, it is characterised in that: described membrane biological reaction
The preparation of the immobilized microorganism ball (13) in device sewage purification system is the activated sludge by will be enriched in microorganism with recovery
(15) by solvent be dissolved into thick after be sufficiently mixed with magnetizing mediums (14), then become bead also by Mold Making in mixture
Air-dry；Bead after air-drying again is placed among magnetic field, and under the active force in magnetic field, inside is little containing magnetizing mediums (14)
Ball does not contains the bead of magnetizing mediums (14) and separates with inside, and the internal bead containing magnetizing mediums (14) is immobilized microorganism ball
(13)；By immobilized microorganism ball (13) in described membrane bioreactor sewage purification system and raw at described film
By arranging magnetic field generator (9) generation magnetic field around thing reactor sewage purification system, immobilized microorganism ball (13) is made to exist
Described membrane bioreactor sewage purification system is in suspended state；Immobilized microorganism ball (13) uses long-time
In, the activated sludge (15) on surface loses activity gradually, by closing magnetic field, makes immobilized microorganism ball (13) pass through self
Gravity sinks to bottom and reclaims, and finally passes through to soak by the immobilized microorganism ball (13) reclaimed, rolls, centrifugal mode
Reclaim magnetizing mediums (14)；Again the magnetizing mediums (14) being recovered to and activated sludge (15) are sufficiently mixed and again make the micro-life of immobilization
Thing ball (13).
Membrane bioreactor sewage purification system the most according to claim 2, it is characterised in that: the micro-life of described immobilization
A diameter of 7 ~ 13mm of thing ball (13).
Membrane bioreactor sewage purification system the most according to claim 1, it is characterised in that: described magnetizing mediums (14)
For metallic nickel.
Membrane bioreactor sewage purification system the most according to claim 4, it is characterised in that: described metallic nickel is warp
Metallic nickel after transpassivation process.
Membrane bioreactor sewage purification system the most according to claim 4, it is characterised in that: described magnetizing mediums (14)
A diameter of 1 ~ 2mm.
Membrane bioreactor sewage purification system the most according to claim 1, its operational approach is:
The first step, open container (7), make the immobilized microorganism ball (13) of inside be flowed into described membrane bioreactor sewage
In cleaning system；
Second step, open magnetic field generator (9) and aerator (8), in making described membrane bioreactor sewage purification system
Generation magnetic field, portion, and then make immobilized microorganism ball (13) be in suspension in described membrane bioreactor sewage purification system
State；
3rd step, by the outlet (18) of water-supply-pipe (17) one end in outlet pipe (6) connection in MBR pond (3)；
4th step, opening conduits valve, make sewage be flowed in described membrane bioreactor sewage purification system；
5th step, described membrane module (12) is positioned in MBR pond (3), is positioned at the flow velocity tachymeter (22) of top cover (20)
It is capable of detecting when water velocity；
6th step, the wire connected by electric magnet (21) connect upper alternating current power supply, and can be detected by flow velocity tachymeter (22)
Water discharge flow speed degree size, in conjunction with cycle and the size of formula regulation alternating current, makes electric magnet (21) under the effect of alternating current, produces
Raw intermittent magnetic, attracts magnetizing mediums (24), and compression spring (25) during attracting makes film (19) also produce indirect
Compression, by film (19) intermittent compression with restore to the original state during, make mud be difficult to be attached to film (19) surface, and
And the mud having attached to film (19) surface can be removed；
7th step, sewage are discharged after described membrane bioreactor sewage purification system processes；Immobilized microorganism ball
(13), after using a period of time in described membrane bioreactor sewage purification system, it is flowed into the MBR pond (3) not having magnetic field
In, the immobilized microorganism ball (13) of a part is flowed in collection device (11), another part immobilized microorganism ball (13)
It is back in anoxic pond (1) recycle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610750991.4A CN106186564A (en) | 2016-08-30 | 2016-08-30 | Membrane bioreactor sewage purification system and operational approach thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610750991.4A CN106186564A (en) | 2016-08-30 | 2016-08-30 | Membrane bioreactor sewage purification system and operational approach thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106186564A true CN106186564A (en) | 2016-12-07 |
Family
ID=57526503
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610750991.4A Withdrawn CN106186564A (en) | 2016-08-30 | 2016-08-30 | Membrane bioreactor sewage purification system and operational approach thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106186564A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108892232A (en) * | 2018-07-05 | 2018-11-27 | 嘉兴市盛翔织造有限公司 | A kind of membrane bioreactor cleared up automatically |
| CN114804336A (en) * | 2022-01-20 | 2022-07-29 | 辽宁师范大学 | Device and method for reducing membrane pollution of membrane bioreactor |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1204625A (en) * | 1997-07-02 | 1999-01-13 | 科学技术振兴事业团 | Magnetic microorganism immobilization carrier, method for producing the carrier and method for treating waste water |
| WO2001005715A1 (en) * | 1999-07-20 | 2001-01-25 | Zenon Environmental Inc. | Biological process for removing phosphorus involving a membrane filter |
| CN102228796A (en) * | 2011-05-13 | 2011-11-02 | 叶茂盛 | Pollution resistant membrane module and use method thereof |
| CN104030521A (en) * | 2014-05-21 | 2014-09-10 | 成都振中电气有限公司 | Wastewater treatment device |
| CN105347627A (en) * | 2015-12-07 | 2016-02-24 | 北京城市排水集团有限责任公司 | Movable MBR-process sewage treatment device and treatment method thereof |
-
2016
- 2016-08-30 CN CN201610750991.4A patent/CN106186564A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1204625A (en) * | 1997-07-02 | 1999-01-13 | 科学技术振兴事业团 | Magnetic microorganism immobilization carrier, method for producing the carrier and method for treating waste water |
| WO2001005715A1 (en) * | 1999-07-20 | 2001-01-25 | Zenon Environmental Inc. | Biological process for removing phosphorus involving a membrane filter |
| CN102228796A (en) * | 2011-05-13 | 2011-11-02 | 叶茂盛 | Pollution resistant membrane module and use method thereof |
| CN104030521A (en) * | 2014-05-21 | 2014-09-10 | 成都振中电气有限公司 | Wastewater treatment device |
| CN105347627A (en) * | 2015-12-07 | 2016-02-24 | 北京城市排水集团有限责任公司 | Movable MBR-process sewage treatment device and treatment method thereof |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108892232A (en) * | 2018-07-05 | 2018-11-27 | 嘉兴市盛翔织造有限公司 | A kind of membrane bioreactor cleared up automatically |
| CN108892232B (en) * | 2018-07-05 | 2021-02-26 | 嘉兴市盛翔织造有限公司 | Automatic membrane bioreactor who clears up |
| CN114804336A (en) * | 2022-01-20 | 2022-07-29 | 辽宁师范大学 | Device and method for reducing membrane pollution of membrane bioreactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104649519A (en) | Sewage treatment device and method by combining bio-ferric process and anaerobic MBR method | |
| CN202465359U (en) | Self-cleaning membrane bio-reaction tank of membrane bio-reactor unit | |
| CN106186564A (en) | Membrane bioreactor sewage purification system and operational approach thereof | |
| CN215667605U (en) | Domestic sewage treatment detection device | |
| CN106045043A (en) | System for removing nitrogen and phosphorus in sewage and operation method of system | |
| CN202465361U (en) | Membrane filament unit of immersed membrane module instrument | |
| CN108946939A (en) | A kind of distributed domestic sewage treatment equipment and its technique | |
| CN106186327A (en) | Waste water pollutant-removing system and using method | |
| CN211311017U (en) | Sewage advanced treatment equipment based on activated carbon technology | |
| CN105502658B (en) | And oxygen Flat Membrane gasification dephosphorization apparatus and its method | |
| CN202465370U (en) | Novel MBR (Membrane Bioreactor) | |
| CN208414166U (en) | A kind of aquaculture ecological purified water system | |
| CN106145556A (en) | Waste water purifying treatment system and operational approach thereof | |
| CN207091245U (en) | A kind of biological treatment combines the integrated sewage treating apparatus of vortex flocculation | |
| CN106186326A (en) | A kind of sewage purification pollutant-removing system and its operational approach | |
| CN106277607A (en) | A kind of water purification system containing membrane module and using method thereof | |
| CN205820978U (en) | A kind of hybrid biological contact oxidation pond | |
| CN106186330A (en) | The processing system of sewage and using method thereof | |
| CN106277612A (en) | Sewage purification system and operational approach thereof | |
| CN105948417A (en) | Sewage treatment system of membrane bioreactor and using method thereof | |
| CN106045039A (en) | Sewage treatment system of membrane-containing process and operation method of sewage treatment system | |
| CN106186296A (en) | Oxidation ditch sewage purification system and using method thereof | |
| CN106186307A (en) | Connect the anaerobic baffled reactor for sewage disposal and its using method of membrane cisterna | |
| CN212559880U (en) | Aeration oxygen supply device for biochemical system | |
| CN201971709U (en) | Sewage treatment system in regeneration textile industry |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WW01 | Invention patent application withdrawn after publication | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20161207 |