CN206142997U - High -efficient sewage treatment device - Google Patents
High -efficient sewage treatment device Download PDFInfo
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- CN206142997U CN206142997U CN201620847693.2U CN201620847693U CN206142997U CN 206142997 U CN206142997 U CN 206142997U CN 201620847693 U CN201620847693 U CN 201620847693U CN 206142997 U CN206142997 U CN 206142997U
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- Prior art keywords
- pond
- dynamic membrane
- anaerobic tank
- base material
- sewage treatment
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- 239000010865 sewage Substances 0.000 title claims abstract description 28
- 239000012528 membrane Substances 0.000 claims abstract description 50
- 238000004062 sedimentation Methods 0.000 claims abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 3
- 239000001301 oxygen Substances 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 27
- 238000006243 chemical reaction Methods 0.000 claims description 15
- 238000009434 installation Methods 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 10
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 238000006396 nitration reaction Methods 0.000 claims description 8
- 239000004744 fabric Substances 0.000 claims description 6
- 235000007164 Oryza sativa Nutrition 0.000 claims description 4
- 239000004745 nonwoven fabric Substances 0.000 claims description 4
- 235000009566 rice Nutrition 0.000 claims description 4
- 229920000914 Metallic fiber Polymers 0.000 claims description 2
- 238000005276 aerator Methods 0.000 claims description 2
- 239000003365 glass fiber Substances 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 239000004033 plastic Substances 0.000 claims description 2
- 229920003023 plastic Polymers 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 229920002994 synthetic fiber Polymers 0.000 claims description 2
- 210000002268 wool Anatomy 0.000 claims description 2
- 240000007594 Oryza sativa Species 0.000 claims 1
- 239000004411 aluminium Substances 0.000 claims 1
- 229910052782 aluminium Inorganic materials 0.000 claims 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 1
- 239000004758 synthetic textile Substances 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 9
- 239000000758 substrate Substances 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 206010021143 Hypoxia Diseases 0.000 abstract 2
- 239000012065 filter cake Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 19
- 238000000034 method Methods 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 230000008569 process Effects 0.000 description 9
- 230000006872 improvement Effects 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 7
- 230000004907 flux Effects 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 241000894006 Bacteria Species 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 235000013339 cereals Nutrition 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 241000209094 Oryza Species 0.000 description 3
- 238000005273 aeration Methods 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000000280 densification Methods 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 208000035240 Disease Resistance Diseases 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000009285 membrane fouling Methods 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000012209 synthetic fiber 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
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a high -efficient sewage treatment device, including septic tank (1), anaerobism pond (2), first oxygen deficiency pond (3), second oxygen deficiency pond (4), first good oxygen pond (5), dynamic membrane pond (6) and sedimentation tank (14) that connect gradually, be equipped with a set of dynamic membrane subassembly (7) in dynamic membrane pond (6), dynamic membrane module (7) are including substrate (8) and form dynamic membrane (9) on substrate (8), substrate (8) are the macropore substrate. Dynamic membrane module simple structure, low cost, convenient to use that this operational effect is good with low costs rely on the quick activated sludge filter cake layer completion separation that forms on the macropore substrate, and the denitrogenation is effectual, can effectively fall COD, BOD, does not almost have the energy consumption, need not to safeguard, and long service life, the running cost is low.
Description
Technical field
This utility model belongs to a kind of sewage-treatment plant, and more particularly to a kind of low manufacture cost, operating cost are low, drop
COD effects are good, the efficient sewage treatment installation that denitrification effect is good.
Background technology
At present waste water treating and reutilizing and the conventional process of one-level A discharge are activated sludge process -- the combination work of depth logos
Skill or for membrane bioreactor (MBR).Activated sludge process -- the group technology of depth logos, i.e., live in original denitrogenation dephosphorizing
Property sludge processes on the basis of, increase coagulation, plate-spinning filter, the technique such as sterilization, but the technological process length, equipment is more, floor space
Greatly, stably reaching standard is difficult to indexs such as ammonia nitrogen total nitrogens.Membrane bioreactor (MBR) have floor space is little, effluent quality is excellent, can
The advantages of enhanced biological is processed, China's land used is limited, developed area good market prospect, but MBR techniques are still immature,
Membrane flux is low, high energy consumption, service life are short, limits further genralrlization and uses.
Dynamic Membrane (Dynamicmem-brane) is a kind of emerging sewage disposal film, is by being formed on film base material surface
Sludge blanket plays a kind of new membrane module of accurate crown_interception, and wherein self-forming dynamic membrane is by sludge flco in filter process
(microorganism and its metabolite) is accumulated to form film layer for class coating material.It forms time and thickness and Biomass etc. with operation bar
Part is closely related, has reported in literature sludge flco cumulative speed to be about 0～50g/ (m2H), thus " film layer " forms relatively slow
And it is difficult to stablize, the time is longer to cause Dynamic Membrane to be formed, and generally at 30 minutes to a few houres, thus initial stage water quality is difficult to
Meet and require (effective filtration is only formed to the effect of certain thickness competence exertion in sludge blanket), big capacity of returns can only be adopted
To film forming, so as to increased Qian Dao ponds load；Secondly, Dynamic Membrane operationally increased because film layer easily occurs in high sludge concentration
Hurry up, cause effluent flux to decline, effective cycle of operation is relatively short, and lack effective control measure；Besides, Dynamic Membrane
Backwash effect is poor, and effluent flux recovery rate is low, causes normal aquifer yield little, is easy to produce irreversible membrane fouling after time length, leads
Cause medicine to wash frequently, increased operating cost and complex operation degree.This three big defect becomes the good cost of the spontaneous operational effect of restriction
Low dynamic film component effectively utilizes major obstacle.
Utility model content
Technical problem：In order to solve the defect of prior art, this utility model provides a kind of low manufacture cost, running cost
With it is low, COD effects are good for drop, the efficient sewage treatment installation that denitrification effect is good.
Technical scheme：A kind of efficient sewage treatment installation that this utility model is provided, including the anaerobic tank being sequentially connected
(1), anaerobic pond (2), the first anoxic pond (3), the second anoxic pond (4), the first Aerobic Pond (5), dynamic membrane cisterna (6) and sedimentation tank
(14)；One group of dynamic film component (7) is provided with the dynamic membrane cisterna (6)；The dynamic film component (7) is including base material (8) and shape
Into the Dynamic Membrane (9) on base material (8)；The base material (8) is macropore base material.
Used as improvement, the base material (8) is sponge, filter screen, non-woven fabrics, porous ceramicss, sintered metal net, metallic fiber burn
Knot felt, sintered powder material, sintered porous plastics, sintering aluminum oxide, bafta, wool fabric, silk fabrics, synthetic fibers are knitted
The combination of one or more in thing, glass fiber cloth, non-woven fabric.
Used as another kind of improvement, it is 10-30 millimeters that its external diameter is 40-150 millimeters, internal diameter, a height of 0.1-3 rice；Preferably,
Its external diameter be 40-100 millimeters, internal diameter be 10-30 millimeters, a height of 0.3-1 rice；It is highly preferred that its external diameter is 40-60 millimeters, interior
Footpath be 10-30 millimeters, a height of 0.4-0.6 rice；Most preferably, its external diameter be 50 millimeters, internal diameter be 20 millimeters, a height of 0.5 meter.
Used as another kind of improvement, the Dynamic Membrane (9) from outer to inner includes successively Filtration Adsorption layer (91), anaerobic reaction layer
And anti-nitration reaction layer (93) (92).
Used as another kind of improvement, the formation and methods for using them of the dynamic film component (7) is comprised the following steps：
(1) formation of Dynamic Membrane：Waste water is continued through into base material 1-7 days and forms Dynamic Membrane in substrate surface, specially：
Sewage permeates from outside to inside in base material, while adsorbing the impurity and sludge of some larger particles in substrate surface, forms nascent
Dynamic Membrane；Adsorbing contaminant is continued on nascent Dynamic Membrane surface and sludge forms Filtration Adsorption layer after operation a period of time, dynamic of coming into being
Film is internally formed the sludge blanket of one layer of densification and grows anaerobe and is anaerobic reaction layer, and Dynamic Membrane of coming into being penetralia grows anti-nitre
Change antibacterial and be anti-nitration reaction layer, the base material for so far forming surface attachment Dynamic Membrane is dynamic film component；
(2) wastewater treatment：Sewage flows through Filtration Adsorption layer and filters in Filtration Adsorption layer；Pass through anaerobic reaction layer detesting
There is anaerobic reaction in the presence of oxygen bacterium, the Organic substance of macromole is decomposed；Anti-nitration reaction layer is finally flowed through in denitrifying bacterium
In the presence of, the carbon source provided using anaerobic reaction layer, to denitrogenation of waste water.
Used as another kind of improvement, the anaerobic tank (1) includes three-level anaerobic tank, and the three-level anaerobic tank includes being sequentially connected
First order anaerobic tank (11), second level anaerobic tank (12), third level anaerobic tank (13).
Used as another kind of improvement, also including the second Aerobic Pond (10), second Aerobic Pond (10) is located at the first Aerobic Pond
(5) it is used for the first Aerobic Pond of connection (5) and anaerobic tank (1) and anaerobic tank (1) between.
It is first anoxic pond (3), the second anoxic pond (4), the first Aerobic Pond (5), second aerobic as another kind of improvement
Aerator (16) is respectively equipped with pond (10).
This utility model additionally provides a kind of high-efficient sewage method of wastewater treatment, using above-mentioned efficient sewage treatment installation, step
It is rapid as follows：
(1) sewage sequentially passes through three-level anaerobic tank (1)：First order anaerobic tank (11) is for removing bulky grain pollutant and portion
Divide float, second level anaerobic tank (12) for removing small particles of pollution thing and partial suspended thing, use by third level anaerobic tank (13)
In removal part COD and ammonia nitrogen；
(2) water outlet of anaerobic tank (1) enters anaerobic pond (2), and part total nitrogen and COD are removed in anaerobic pond (2)；
(3) anaerobic pond (2) water outlet enters the first anoxic pond (3), and part total nitrogen and COD are removed in the first anoxic pond (3)；
(5) first anoxic pond (3) water outlets enter the second anoxic pond (4), remove in the second anoxic pond (4) part total nitrogen and
COD；
(6) second anoxic pond (4) water outlets enter the first Aerobic Pond (5), remove in the first Aerobic Pond (5) a large amount of COD and
BOD；
(7) first Aerobic Pond (5) water outlets enter dynamic membrane cisterna (6), react below generation in dynamic membrane cisterna (6)：
(7.1) first Aerobic Pond (5) water outlets are permeated from outside to inside in Dynamic Membrane, and Filtration Adsorption layer adsorbs some larger
The impurity and sludge of grain；
(7.2) pass through anaerobic reaction layer and anaerobic reaction occurs in the presence of anaerobe, by the Organic substance of macromole point
Solution；
(7.3) anti-nitration reaction layer is finally flowed through in the presence of denitrifying bacterium, the carbon source provided using anaerobic reaction layer,
To denitrogenation of waste water；
(7.4) if finding that the sludge blanket on film surface is too thick, affects water flux in the course of work, backwash is now needed,
Film surface is washed away by aeration, backwash completes to continue to run with；
(8) dynamic membrane cisterna (6) water outlet enters sedimentation tank (14), in the interior precipitation process of sedimentation tank (14)；Meanwhile, add dephosphorization
Agent removes most of phosphorus.
Beneficial effect：The efficient sewage treatment installation simple structure, with low cost, easy to use that this utility model is provided,
Denitrification effect is good, can effectively drop COD, BOD, almost Non-energy-consumption, and Maintenance free, long service life, operating cost is low.
Description of the drawings
Fig. 1 is the structural representation of this utility model efficient sewage treatment installation.
Fig. 2 is the structural representation of dynamic film component.
Fig. 3 is the structural representation of three-level anaerobic tank.
Specific embodiment
This utility model efficient sewage treatment installation is further illustrated below.
Efficient sewage treatment installation, is shown in Fig. 1, including two Aerobic Ponds (10) and the anaerobic tank (1), the anaerobic pond that are sequentially connected
(2), the first anoxic pond (3), the second anoxic pond (4), the first Aerobic Pond (5), dynamic membrane cisterna (6) and sedimentation tank (14)；It is described dynamic
One group of dynamic film component (7) is provided with state membrane cisterna (6)；The dynamic film component (7), sees Fig. 2, including base material (8) and is formed in
Dynamic Membrane (9) on base material (8)；The base material (8) is macropore base material.The anaerobic tank (1), sees Fig. 3, including three-level excrement
Pond, the three-level anaerobic tank includes first order anaerobic tank (11), second level anaerobic tank (12), the third level anaerobic tank being sequentially connected
(13).First anoxic pond (3), the second anoxic pond (4), the first Aerobic Pond (5), it is respectively equipped with exposure in the second Aerobic Pond (10)
Device of air (16).It is aerobic that second Aerobic Pond (10) is used for connection first between the first Aerobic Pond (5) and anaerobic tank (1)
Pond (5) and anaerobic tank (1).
Prepare the different dynamic film component of a collection of size, material and run, condition is shown in Table 1, and method is as follows：
(1) formation of Dynamic Membrane：Waste water is continued through into base material 1-7 days and forms Dynamic Membrane in substrate surface, specially：
Sewage permeates from outside to inside in base material, while adsorbing the impurity and sludge of some larger particles in substrate surface, forms nascent
Dynamic Membrane；Adsorbing contaminant is continued on nascent Dynamic Membrane surface and sludge forms Filtration Adsorption layer after operation a period of time, dynamic of coming into being
Film is internally formed the sludge blanket of one layer of densification and grows anaerobe and is anaerobic reaction layer, and Dynamic Membrane of coming into being penetralia grows anti-nitre
Change antibacterial and be anti-nitration reaction layer, the base material for so far forming surface attachment Dynamic Membrane is dynamic film component；
(2) wastewater treatment：Sewage stream continues through filter adsorption layer and filters in Filtration Adsorption layer naturally；Pass through anaerobism anti-
Answer layer that anaerobic reaction occurs in the presence of anaerobe, the Organic substance of macromole is decomposed；Finally flow through anti-nitration reaction layer to exist
In the presence of denitrifying bacterium, the carbon source provided using anaerobic reaction layer, to denitrogenation of waste water；
(3) if finding that the sludge blanket on film surface is too thick, affects water flux in the course of work, backwash is now needed, is led to
Cross aeration and wash away film surface, backwash completes to continue to run with；Because this utility model is Dynamic Membrane obtained in large pore material, because
This, it is very little to stain disease resistance, can only lean on stain disease self gravitation to complete, and its circulation is voluntarily adjusted by system；Not only
Energy-conserving and environment-protective, low cost；And backwashing period is very long, with little need for backwash.
Table 1
Run in efficient sewage treatment installation using obtained dynamic film component, process stain disease, step is as follows：
(1) sewage sequentially passes through three-level anaerobic tank (1)：First order anaerobic tank (11) is for removing bulky grain pollutant and portion
Divide float, second level anaerobic tank (12) for removing small particles of pollution thing and partial suspended thing, use by third level anaerobic tank (13)
In removal part COD and ammonia nitrogen；
(2) water outlet of anaerobic tank (1) enters anaerobic pond (2), and part total nitrogen and COD are removed in anaerobic pond (2)；
(3) anaerobic pond (2) water outlet enters the first anoxic pond (3), and part total nitrogen and COD are removed in the first anoxic pond (3)；
(5) first anoxic pond (3) water outlets enter the second anoxic pond (4), remove in the second anoxic pond (4) part total nitrogen and
COD；
(6) second anoxic pond (4) water outlets enter the first Aerobic Pond (5), remove in the first Aerobic Pond (5) a large amount of COD and
BOD；
(7) first Aerobic Pond (5) water outlets enter dynamic membrane cisterna (6), react below generation in dynamic membrane cisterna (6)：
(7) first Aerobic Pond (5) water outlets enter dynamic membrane cisterna (6), react below generation in dynamic membrane cisterna (6)：
(7.1) first Aerobic Pond (5) water outlets are permeated from outside to inside in Dynamic Membrane, and Filtration Adsorption layer adsorbs some larger
The impurity and sludge of grain；
(7.2) pass through anaerobic reaction layer and anaerobic reaction occurs in the presence of anaerobe, by the Organic substance of macromole point
Solution；
(7.3) anti-nitration reaction layer is finally flowed through in the presence of denitrifying bacterium, the carbon source provided using anaerobic reaction layer,
To denitrogenation of waste water；
(7.4) if finding that the sludge blanket on film surface is too thick, affects water flux in the course of work, backwash is now needed,
Film surface is washed away by aeration, backwash completes to continue to run with；
(8) dynamic membrane cisterna (6) water outlet enters sedimentation tank (14), in the interior precipitation process of sedimentation tank (14)；Meanwhile, add dephosphorization
Agent removes most of phosphorus.
Wang family of Jiangsu sewage is processed using the said equipment, the results are shown in Table 2.
Table 2
Wherein, comparative example is using Dynamic Membrane obtained in conventional polyurethanes material.
As shown in Table 2, this utility model equipment can effectively remove the Organic substances such as the ammonia nitrogen in sewage.
Claims (5)
1. a kind of efficient sewage treatment installation, it is characterised in that：Including the anaerobic tank (1), anaerobic pond (2) being sequentially connected, first
Anoxic pond (3), the second anoxic pond (4), the first Aerobic Pond (5), dynamic membrane cisterna (6) and sedimentation tank (14)；The dynamic membrane cisterna (6)
Inside it is provided with one group of dynamic film component (7)；The dynamic film component (7) includes base material (8) and the Dynamic Membrane being formed on base material (8)
(9)；The base material (8) is macropore base material；Also include the second Aerobic Pond (10), second Aerobic Pond (10) is aerobic located at first
It is used for the first Aerobic Pond of connection (5) and anaerobic tank (1) between pond (5) and anaerobic tank (1)；First anoxic pond (3), second lack
Oxygen pond (4), the first Aerobic Pond (5), it is respectively equipped with aerator (16) in the second Aerobic Pond (10).
2. a kind of efficient sewage treatment installation according to claim 1, it is characterised in that：The base material (8) is sponge, filter
Net, non-woven fabrics, porous ceramicss, sintered metal net, metallic fiber sintered felt, sintered powder material, sintered porous plastics, sintered aluminium
One kind in oxide, bafta, wool fabric, silk fabrics, synthetic fabrics, glass fiber cloth, non-woven fabric.
3. a kind of efficient sewage treatment installation according to claim 1, it is characterised in that：The longitudinal section of the base material (8)
For hollow ring, it is 10-30 millimeters that its external diameter is 40-150 millimeters, internal diameter, a height of 0.1-3 rice.
4. a kind of efficient sewage treatment installation according to claim 1, it is characterised in that：The Dynamic Membrane (9) is from outer
Inside include Filtration Adsorption layer (91), anaerobic reaction layer (92) and anti-nitration reaction layer (93) successively.
5. a kind of efficient sewage treatment installation according to claim 1, it is characterised in that：The anaerobic tank (1) is including three
Level anaerobic tank, the three-level anaerobic tank includes first order anaerobic tank (11), second level anaerobic tank (12), the third level being sequentially connected
Anaerobic tank (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620847693.2U CN206142997U (en) | 2016-08-08 | 2016-08-08 | High -efficient sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620847693.2U CN206142997U (en) | 2016-08-08 | 2016-08-08 | High -efficient sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206142997U true CN206142997U (en) | 2017-05-03 |
Family
ID=58627919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620847693.2U Expired - Fee Related CN206142997U (en) | 2016-08-08 | 2016-08-08 | High -efficient sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206142997U (en) |
-
2016
- 2016-08-08 CN CN201620847693.2U patent/CN206142997U/en not_active Expired - Fee Related
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|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170503 |