CN206142908U - Dynamic membrane module that operational effect is good with low costs - Google Patents
Dynamic membrane module that operational effect is good with low costs Download PDFInfo
- Publication number
- CN206142908U CN206142908U CN201620847694.7U CN201620847694U CN206142908U CN 206142908 U CN206142908 U CN 206142908U CN 201620847694 U CN201620847694 U CN 201620847694U CN 206142908 U CN206142908 U CN 206142908U
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- Prior art keywords
- dynamic
- dynamic membrane
- base material
- operational effect
- good
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- 239000012528 membrane Substances 0.000 title claims abstract description 34
- 230000000694 effects Effects 0.000 title claims abstract description 19
- 239000000463 material Substances 0.000 claims description 28
- 238000006243 chemical reaction Methods 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 9
- 238000001179 sorption measurement Methods 0.000 claims description 9
- 238000006396 nitration reaction Methods 0.000 claims description 6
- 235000007164 Oryza sativa Nutrition 0.000 claims description 4
- 235000009566 rice Nutrition 0.000 claims description 4
- 240000007594 Oryza sativa Species 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 17
- 239000000758 substrate Substances 0.000 abstract description 9
- 230000015572 biosynthetic process Effects 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000012065 filter cake Substances 0.000 abstract 1
- 238000000926 separation method Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 10
- 239000010865 sewage Substances 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 230000004907 flux Effects 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 3
- 241000209094 Oryza Species 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000004744 fabric Substances 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 229910052799 carbon Inorganic materials 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
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- 239000004745 nonwoven fabric Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 230000002269 spontaneous effect Effects 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 208000035240 Disease Resistance Diseases 0.000 description 1
- 229920000914 Metallic fiber Polymers 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 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
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000005484 gravity Effects 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
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 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
- 239000000843 powder Substances 0.000 description 1
- 238000002360 preparation method Methods 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
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000004758 synthetic textile Substances 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a dynamic membrane module that operational effect is good with low costs, including substrate and the dynamic membrane of formation on the substrate, the substrate is the macropore substrate. This dynamic membrane module that operational effect is good with low costs simple structure, low cost, convenient to use 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, more particularly to a kind of stable operation flux large period length, backwash
Dynamic film component of the good low cost of spontaneous operational effect of cycle length and preparation method thereof.
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 good low cost of operational effect
Dynamic film component.
Technical scheme:This utility model provide a kind of good low cost of operational effect dynamic film component, including base material and
The Dynamic Membrane being formed on base material;The base material is macropore base material.
Used as improvement, the base material is sponge, filter screen, non-woven fabrics, porous ceramicss, sintered metal net, metallic fiber sintered
Felt, sintered powder material, sintered porous plastics, sintering aluminum oxide, bafta, wool fabric, silk fabrics, synthetic fabrics,
The combination of one or more in glass fiber cloth, non-woven fabric.
Used as another kind of improvement, the longitudinal section of the base material is hollow ring, and its external diameter is 40-150 millimeters, internal diameter is
10-30 millimeters, 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 be 40-60 millimeters, internal diameter be 10-30 millimeters, a height of 0.4-0.6 rice;Most preferably, its external diameter is 50
Millimeter, internal diameter are 20 millimeters, a height of 0.5 meter.
Used as another kind of improvement, the Dynamic Membrane from outer to inner includes successively Filtration Adsorption layer, anaerobic reaction layer and anti-nitre
Change conversion zone.
This utility model additionally provides the formation and methods for using them of above-mentioned dynamic film component, comprises 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.
In step (1) and step (2), waste water is 0.5-10h by the time in Dynamic Membrane.
In step (1) and step (2), waste water passes through Dynamic Membrane naturally by gravity.
This utility model additionally provides application of the above-mentioned dynamic film component in nitrogenous effluent treatment.
Beneficial effect:Dynamic film component simple structure, the low cost of the good low cost of operational effect that this utility model is provided
It is honest and clean, easy to use, rely on the quick activated sludge cake layer for being formed on macropore base material and complete to separate, denitrification effect is good, can have
COD, BOD drop in effect, 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 the dynamic film component of the good low cost of this utility model operational effect.
Specific embodiment
The dynamic film component of the good low cost of this utility model operational effect is further illustrated below.
Dynamic film component, is shown in Fig. 1, including base material 1 and the Dynamic Membrane 2 being formed on base material 1;Base material 1 is macropore base material.It is dynamic
State film 2 from outer to inner includes successively Filtration Adsorption layer 21, anaerobic reaction layer 22 and anti-nitration reaction layer 23.
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
Wang family of Jiangsu anaerobic tank is processed using the dynamic film component of above-mentioned operational effect good low cost, is tied
Fruit is shown in Table 2.
Table 2
Wherein, comparative example is using Dynamic Membrane obtained in conventional polyurethanes material.
As shown in Table 2, the dynamic film component of the good low cost of operational effect of the present utility model can be removed effectively in sewage
The Organic substances such as ammonia nitrogen.
Claims (2)
1. the dynamic film component of the good low cost of a kind of operational effect, it is characterised in that:Including base material (1) and it is formed in base material (1)
On Dynamic Membrane (2);The base material (1) is macropore base material;The base material (1) is sponge;The Dynamic Membrane (2) from outer to inner according to
It is secondary including Filtration Adsorption layer (21), anaerobic reaction layer (22) and anti-nitration reaction layer (23).
2. the dynamic film component of the good low cost of a kind of operational effect according to claim 1, it is characterised in that:The base material
(1) longitudinal section be hollow ring, its external diameter be 40-150 millimeters, internal diameter be 10-30 millimeters, a height of 0.1-3 rice.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620847694.7U CN206142908U (en) | 2016-08-08 | 2016-08-08 | Dynamic membrane module that operational effect is good with low costs |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201620847694.7U CN206142908U (en) | 2016-08-08 | 2016-08-08 | Dynamic membrane module that operational effect is good with low costs |
Publications (1)
Publication Number | Publication Date |
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CN206142908U true CN206142908U (en) | 2017-05-03 |
Family
ID=58628136
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201620847694.7U Expired - Fee Related CN206142908U (en) | 2016-08-08 | 2016-08-08 | Dynamic membrane module that operational effect is good with low costs |
Country Status (1)
Country | Link |
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CN (1) | CN206142908U (en) |
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2016
- 2016-08-08 CN CN201620847694.7U patent/CN206142908U/en not_active Expired - Fee Related
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Date | Code | Title | Description |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170503 |