CN106745745A - A kind of improved MBR equipment - Google Patents
A kind of improved MBR equipment Download PDFInfo
- Publication number
- CN106745745A CN106745745A CN201710027814.8A CN201710027814A CN106745745A CN 106745745 A CN106745745 A CN 106745745A CN 201710027814 A CN201710027814 A CN 201710027814A CN 106745745 A CN106745745 A CN 106745745A
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- pond
- sewage
- aeration tank
- membrane
- transition
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- 239000010865 sewage Substances 0.000 claims abstract description 63
- 238000005273 aeration Methods 0.000 claims abstract description 46
- 230000007704 transition Effects 0.000 claims abstract description 45
- 239000012528 membrane Substances 0.000 claims abstract description 41
- 238000005842 biochemical reaction Methods 0.000 claims abstract description 20
- 238000000034 method Methods 0.000 claims abstract description 15
- 230000008569 process Effects 0.000 claims abstract description 9
- 238000001471 micro-filtration Methods 0.000 claims abstract description 5
- 238000000429 assembly Methods 0.000 claims abstract description 4
- 230000000712 assembly Effects 0.000 claims abstract description 4
- 238000005374 membrane filtration Methods 0.000 claims abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- 238000005276 aerator Methods 0.000 claims description 11
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 238000005265 energy consumption Methods 0.000 abstract description 8
- 230000000694 effects Effects 0.000 description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 238000000926 separation method Methods 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 5
- 238000007254 oxidation reaction Methods 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- 241000276457 Gadidae Species 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 235000013405 beer Nutrition 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 210000004681 ovum Anatomy 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 244000045947 parasite Species 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 230000037452 priming Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
- 238000005303 weighing 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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification 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
- C02F3/30—Aerobic and anaerobic processes
- C02F3/308—Biological phosphorus removal
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention discloses a kind of improved MBR equipment, the fields such as sewage disposal and reusing sewage are can be applied to.Other assemblies and facility of the MBR equipment needed for the operation of aeration tank, transition pond, UF membrane pond and equipment are constituted；Wherein, transition pond at least is allowed to form vertical gallery with 1 piece of cut-off, sewage is advanced in the way of plug-flow；Sewage is introduced into aeration tank, enters back into transition pond, subsequently into UF membrane pond, the qualified discharge after separating membrane filtration；Aeration tank provides aerobic biochemical reaction environment for sewage, and transition pond provides the aerobic biochemical reaction environment under anaerobic condition, and UF membrane pond provides aerobic biochemical reaction environment and microfiltration process.MBR equipment disclosed by the invention have compact conformation, technique flexibly, biochemical reaction efficiency high, the low feature of operation energy consumption.
Description
Technical field
The present invention relates to sewage disposal and reusing sewage field, more particularly to a kind of MBR equipment.
Background technology
Membrane bioreactor（Membrane Bio-Reactor, MBR）It is a kind of by membrane separation technique and biological treatment skill
The sewage disposal system that art is combined.With membrane module substitution traditional biological treatment technology end second pond, engineering is not only reduced
High activity sludge concentration is kept in floor space, and bioreactor, the ability that system processes organic loading is improve.Simultaneously
Due to the retention of seperation film, generation cycle microorganism more long, such as nitrifier can fully breed in system, therefore MBR system
Nitrification effect it is notable.
MBR system is widely used in the daily of the dispersion users such as residence district, hotel, holiday resort, school, office building
Sanitary sewage disposal, and the industry such as beer, process hides, food, chemical industry high concentration organic sewage treatment.The product water of MBR system
Can be used to irrigating, wash, environmental sanitation, making that scape etc. is non-to drink function.If adding the technique such as counter-infiltration and sterilization, produce water and can be used for
Industry and the purposes such as drink.
In traditional MBR system, often aerator and film device are installed together.Purpose is by being aerated reduction
Fouling membrane.This configuration mode has two：One is that aeration rate is big, operation energy consumption is high；Two be front and rear entrance sewage mix
It is combined, is unfavorable for that system continous way is run.The two problems seriously constrain the application of MBR technology.
The content of the invention
The present invention is separated aerator and membrane module by the improvement to traditional MBR system, and is connected with transition pond,
Aeration rate can be substantially reduced, increase the biochemical reaction environment of sewage effective process time, neatly control system, thus solve be
The shortcoming that system operation energy consumption is high, continuous operation water yield is low.
A kind of improved MBR equipment disclosed by the invention, including aeration tank, transition pond, UF membrane pond and equipment operation institute
The other assemblies and facility for needing.Aeration tank, transition pond and UF membrane pond are both designed as narrow vertical space, and wherein transition pond is used
Cut-off forms long and narrow passage makes sewage advance in plug-flow mode.
One of improvement is aeration tank, transition pond and UF membrane pond to be both designed as into narrow vertical space, it is therefore an objective to allow
Sewage is advanced without mixing along a direction in plug-flow mode as far as possible so that sewage stream formed pollutant concentration by
High to Low gradient.The improved MBR equipment is tried one's best and avoids the mixed flow state of traditional MBR equipment, therefore is remarkably improved
Effluent quality, and can improve seperation film go out water speed.
The two of improvement are that transition pond cut-off forms long and narrow passage makes the sewage of different biochemical stages not mix
Close, so that sewage stream forms dissolved oxygen concentration gradient from high to low, make to be formed by the aerobic biochemistry to anoxic in transition pond
Reaction environment.And by adjusting the quantity of cut-off, can adjust the anaerobic condition of transition pond end.
The operation method and functions of MBR equipment of the present invention are described in detail below：
Sewage is introduced into aeration tank, enters back into transition pond, subsequently into UF membrane pond, the qualified discharge after separating membrane filtration；
Aeration tank provides aerobic biochemical reaction environment for sewage, and transition pond provides the aerobic biochemical reaction environment under anaerobic condition, film
Separate tank provides aerobic biochemical reaction environment and microfiltration process.
Into the sewage of aeration tank, can be with or without including pre- including clarification, anaerobism, anoxic, super oxidation etc.
Treatment.
In the aeration tank, bottom is provided with sewage inlet and aerator.Sewage inlet may be disposed at aeration
Above or below pipe.Sewage inlet can use distributed antipriming pipe.Aerator can use distributed antipriming pipe or porous
Plate.Because aeration tank is narrow vertical space, therefore aeration bubbles have long period and sewage during the water surface is risen to
Contact, so as to improve concentration of ordinary dissolution of the oxygen in sewage.Preferably, aerator can be using aperture is tiny, hole density is big
Porous material is manufactured, and makes aeration bubbles fine and smooth, has both reduced the rate of climb of bubble, and the contact surface of bubble and sewage is increased again
Product, so as to improve the dissolved efficiency of oxygen, it is possible to decrease aeration intensity, reduces operation energy consumption.
The aeration tank is adjacent with the transition pond, and the sewage in aeration tank can be in overflow to transition pond.Transition pond is along it
Length and width direction is separated, and sewage is passed through from the top of cut-off or bottom, so as to form one group of vertical folding
Passage.When sewage flows through transition pond, dissolved oxygen is gradually by microbial consumption, thus its concentration is gradually reduced.If increasing cut-off
Quantity, then the passage length in transition pond and the flow time of sewage accordingly increase, now, can form scarce in the end in transition pond
Oxygen animalcule environment.Therefore, in transition pond, a series of aerobic biochemical reactions to anoxic can occur, makes hardly degraded organic substance
Degraded is fully stopped, nitrification and denitrification is reacted and is strengthened, and ensure that phosphor-removing effect.
In the final overflow of sewage to adjacent UF membrane pond in the transition pond.The bottom in the UF membrane pond is provided with
Separating film module.Separating film module has aeration and filtering function concurrently.Aeration makes UF membrane pond form aerobe environment, reinforcing drop
COD and phosphor-removing effect.Filtering then retains the molecule in pond, including microorganism, parasite（Ovum）Deng making delivery turbidity and thin
Bacterium number amount reaches water outlet requirement.
In the UF membrane pond, several groups of separating film modules can replace water outlet and air recoil.During water outlet, discharge pressure can
Come from the liquid level static pressure in UF membrane pond, also may be from the vacuum of self priming pump.During air recoil, seperation film can both be carried out clearly
It is clean, aeration can be played a part of again.Similar to the aeration tank, UF membrane pond is also narrow vertical space, therefore liquid level is quiet
Pressure ratio is larger, aeration efficiency comparison is high, so as to greatly reduce the operation energy consumption in UF membrane pond.
Sewage in the UF membrane pond can wholly or largely separated film discharge.Fraction sewage is reflowable to described
In the anoxic pond of MBR front equipment ends or in the aeration tank of the MBR equipment.
Improved MBR equipment of the present invention, similar to oxidation ditch process facility.In oxidation ditch process, by roundabout
Bilge form anaerobism, anoxic and the region such as aerobic.Same effect is then reached by narrow vertical space in the present invention.
Unlike, oxidation ditch process needs the engineering land used of large area, and the present invention makes full use of vertical space to substantially reduce equipment
Floor space.
The beneficial effects of the invention are as follows：Improved MBR equipment have compact conformation, technique flexibly, biochemical reaction efficiency high,
The low feature of operation energy consumption；Both it had been adapted to the small-sized integrated sewage disposal device of manufacture, also had been adapted for extensive sewage disposal application；Both
The treatment with common sanitary sewage can be applied, the treatment of the high-concentration sewages such as percolate, industrial wastewater is can also be applied to, and
More significant treatment effect can be obtained.
Brief description of the drawings
Fig. 1 is a kind of agent structure schematic diagram of improved MBR device instances 1 of the present invention；
Fig. 2 is a kind of overlooking the structure diagram of improved MBR device instances 2 of the present invention.
The mark of each part is as follows in accompanying drawing：1st, aeration tank；11st, sewage inlet；12nd, aerator；2nd, transition pond；21、
Cut-off；22nd, overflow liquid level；23rd, system exhaust/system overfall；24th, the sewage flow mouthful of cut-off bottom（Density bullet）；
25th, the sewage overflow mouthful on cut-off top（White marking）；3rd, UF membrane pond；31st, separating film module（Band water outlet and gas recoil tube
Road）；4th, sludge outlet.
Specific embodiment
Presently preferred embodiments of the present invention is described in detail below in conjunction with the accompanying drawings, so that advantages and features of the invention energy
It is easier to be readily appreciated by one skilled in the art, is more specifically defined so as to be made to protection scope of the present invention.
Embodiment 1
Fig. 1 is the agent structure schematic diagram of the embodiment of the present invention 1.This improved MBR stainless steel for equipment material manufacture, including
Aeration tank 1, transition pond 2, UF membrane pond 3, also including do not have in figure display, can guarantee that the equipment operation needed for other assemblies
And facility.Equipment body size is 1.3 m long, 0.3 m wide, 1 m high, and 0.25 m, the length of transition pond 2 0.75 are grown in wherein aeration tank 1
Grow 0.3 m in m, UF membrane pond 3.Equipment compact, is suitable for the sewage disposal and reuse of domestic consumer.
In this example, sewage inlet 11 and aerator 12 are provided with aeration tank 1.Aerator 12 is by hollow structure
Flat ceramic separation film composition, the aperture of ceramic separation film is 1 ~ 5 μm.Sewage inlet 11 is located at the top of aerator 12,
The distributed drainage arrangement being made up of stainless steel tube；The circular hole of the mm of one row's diameter 2 is arranged at the bottom of stainless steel tube, is beneficial to dirt
Current direction aerator 12, makes sewage be sufficiently mixed with bubble, and prevents from depositing solid-state debris in stainless steel tube, causes sewage to enter
Mouth 11 is blocked.
Transition pond 2 is separated into 4 long and narrow spaces with 3 pieces of cut-offs 21.As illustrated, this 4 long and narrow spaces by every
The overfall on disconnected 21 tops or the outlet of bottom, form about 4 m water stream channels long, before making sewage in plug-flow mode
Enter, prevent the sewage of different biochemical stages from mixing.
Two groups of separating film modules 31 are provided with UF membrane pond 3, separating film element is using flat with hollow structure
Ceramic separation film, it is 0.1 ~ 0.5 μm to separate membrane aperture.This two groups of separating film modules alternately water outlet and air recoil are washed
Journey.The wherein washed journey of air recoil plays a part of two aspects：One is that clean separation film is allowed to keep flux, and two has been aeration
Effect.The double action of cleaning and aeration, advantageously reduces the operation energy consumption in UF membrane pond.
On the top in UF membrane pond, system exhaust/system overfall 23 is provided with, for the flat of system air pressure and water level
Weighing apparatus.The sewage of overflow is reflowable to aeration tank 1, also the reflowable front end cesspool to this equipment（Such as Buffer Pool, or anoxic pond
Deng）.
When equipment is run, sewage is introduced into aeration tank, enters back into transition pond, subsequently into UF membrane pond, by seperation film
Qualified discharge after filtering.Sewage flowing in a device, comes from the static pressure of liquid level.
Aeration tank provides aerobic biochemical reaction environment for sewage, and transition pond provides the aerobic biochemical reaction under anaerobic condition
Environment, UF membrane pond provides aerobic biochemical reaction environment and microfiltration process.
This example have compact conformation, technique flexibly, biochemical reaction efficiency high, the low feature of operation energy consumption, be suitable for house
The treatment of a small amount of sewage yield such as front yard.
Embodiment 2
Fig. 2 is a kind of overlooking the structure diagram of improved MBR device instances 2 of the present invention.Aeration tank 1, transition in the present embodiment
Pond 2, UF membrane pond 3 and miscellaneous part and facility, its function are similar to Example 1.
Using engineering plastics such as SBS or PP, each part is manufactured the main body of the present embodiment by the method for injection moulding, then group
It is combined.
Wherein, transition pond 2 is separated into 8 narrow spaces with cut-off 21.The bottom sewage that this 8 narrow spaces pass through cut-off
The sewage overflow mouthful 25 on outlet 24 or cut-off top is connected, and forms a long and narrow water stream channel, makes sewage more stably to push away
Stream mode is advanced.Can so make to form the more stably aerobic transition to anoxic biochemical environment in transition pond 2.
The situation for processing certain dye house effluents with the equipment is as follows：The volume difference of aeration tank, transition pond and UF membrane pond
It is 4 m3,16 m3 and 4 m3, seperation film uses aperture for 0.1 μm of ceramic separation film, and effective area is 10 m2.Factory building is arranged
The waste water for going out enters the MBR equipment after being processed through hydrolysis acidification pool, biochemical degradation, the nitre that organic matter occurs first in aeration tank
The effect such as change, and last till transition pond；In the second half section in transition pond, the drop of the reduction of carbon source and dissolved oxygen concentration in waste water
It is low, denitrification phosphorus-collecting biochemical process is accounted for leading；In UF membrane pond, waste water is again introduced into the biological oxidation stage, further strong
Change drop COD, nitrification and phosphor-removing effect.When MBR influent CODs, NH3-N and TN are respectively 320,32.04 and 29. 28 mg/L,
In the case where hydraulic detention time is 5 h, water outlet COD, NH3-N and TN are respectively 71,0.36 and 5.76 mg/L.
The foregoing is only embodiments of the invention, simply the application example is gathered around for the size of equipment, part and material etc.
Some special types, not thereby limit the scope of the claims of the invention, and according to applied environment and scale, equipment can select suitable chi
Very little, part and material etc..Equivalent structure or equivalent flow conversion that every utilization description of the invention and accompanying drawing content are made, or
Other related technical fields are directly or indirectly used in, are included within the scope of the present invention.
Claims (7)
1. a kind of improved MBR equipment, including aeration tank, transition pond, UF membrane pond and equipment operation needed for other assemblies and
Facility, it is characterised in that：Transition pond at least is allowed to form vertical gallery with 1 piece of cut-off, makes sewage in the way of plug-flow
Advance；Aeration tank provides aerobic biochemical reaction environment for sewage, and transition pond provides the aerobic biochemical reaction ring under anaerobic condition
Border, UF membrane pond provides aerobic biochemical reaction environment and microfiltration process.
2. transition pond according to claim 1, it is characterised in that：The cut-off in transition pond for its length and width direction every
It is disconnected, sewage is passed through from the top of cut-off or bottom.
3. the transition pond according to claim 1 and claim 2, it is characterised in that：By increasing the quantity of cut-off, make dirt
Water energy is advanced with more stable plug-flow, and the sewage of different biochemical stages does not mix, so that being formed in transition pond from aerobic
To the transition of anaerobic environment.
4. aeration tank according to claim 1, it is characterised in that：Sewage inlet and aerator are provided with aeration tank.
5. aeration tank and UF membrane pond according to claim 1, it is characterised in that：The length and width of aeration tank is not more than exposure
2 times of device of air upright projection size, the length and width in UF membrane pond is not more than 2 times of membrane module upright projection size；It is excellent
Selection of land, aeration tank and UF membrane pond are designed as narrow vertical space, the sewage in two reaction tanks is fully mixed with bubble
Close, and sewage is advanced in plug-flow mode.
6. MBR equipment according to claim 1, it is characterised in that：Sewage is introduced into aeration tank, enters back into transition pond, so
Enter UF membrane pond, qualified discharge after separated membrane filtration afterwards.
7. MBR equipment according to claim 1, it is characterised in that：Aeration tank provides aerobic biochemical reaction environment for sewage,
Transition pond provides the aerobic biochemical reaction environment under anaerobic condition, and UF membrane pond provides aerobic biochemical reaction environment and micro-filtration mistake
Journey.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710027814.8A CN106745745A (en) | 2017-01-16 | 2017-01-16 | A kind of improved MBR equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710027814.8A CN106745745A (en) | 2017-01-16 | 2017-01-16 | A kind of improved MBR equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106745745A true CN106745745A (en) | 2017-05-31 |
Family
ID=58945487
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| Application Number | Title | Priority Date | Filing Date |
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| CN201710027814.8A Pending CN106745745A (en) | 2017-01-16 | 2017-01-16 | A kind of improved MBR equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046476A (en) * | 2017-12-27 | 2018-05-18 | 佛山市中国科学院上海硅酸盐研究所陶瓷研发中心 | A kind of device and technique for being related to cutting/grinding/glossing wastewater treatment |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105293700A (en) * | 2015-10-29 | 2016-02-03 | 北京格兰特膜分离设备有限公司 | Low-energy-consumption membrane bioreactor and sewage treatment method |
| CN205170495U (en) * | 2015-10-29 | 2016-04-20 | 北京格兰特膜分离设备有限公司 | Low energy consumption membrane bioreactor |
| CN206562332U (en) * | 2017-01-16 | 2017-10-17 | 邵俊轩 | A kind of improved MBR equipment |
-
2017
- 2017-01-16 CN CN201710027814.8A patent/CN106745745A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105293700A (en) * | 2015-10-29 | 2016-02-03 | 北京格兰特膜分离设备有限公司 | Low-energy-consumption membrane bioreactor and sewage treatment method |
| CN205170495U (en) * | 2015-10-29 | 2016-04-20 | 北京格兰特膜分离设备有限公司 | Low energy consumption membrane bioreactor |
| CN206562332U (en) * | 2017-01-16 | 2017-10-17 | 邵俊轩 | A kind of improved MBR equipment |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108046476A (en) * | 2017-12-27 | 2018-05-18 | 佛山市中国科学院上海硅酸盐研究所陶瓷研发中心 | A kind of device and technique for being related to cutting/grinding/glossing wastewater treatment |
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