CN106082435A - A kind of dynamic film component of the good low cost of operational effect - Google Patents
A kind of dynamic film component of the good low cost of operational effect Download PDFInfo
- Publication number
- CN106082435A CN106082435A CN201610643967.0A CN201610643967A CN106082435A CN 106082435 A CN106082435 A CN 106082435A CN 201610643967 A CN201610643967 A CN 201610643967A CN 106082435 A CN106082435 A CN 106082435A
- Authority
- CN
- China
- Prior art keywords
- dynamic
- base material
- film component
- low cost
- dynamic film
- 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.)
- Pending
Links
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
- C02F3/28—Anaerobic digestion processes
- C02F3/2853—Anaerobic digestion processes using anaerobic membrane bioreactors
-
- 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
- C02F3/2806—Anaerobic processes using solid supports for microorganisms
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention provides the dynamic film component of the good low cost of a kind of operational effect, including base material and the Dynamic Membrane being formed on base material；Described base material is macropore base material.The dynamic film component simple in construction of the good low cost of this operational effect, with low cost, easy to use, rely on the activated sludge cake layer quickly formed on macropore base material and complete to separate, denitrification effect is good, COD, BOD can effectively drop, almost without energy consumption, it is not necessary to safeguard, service life is long, and operating cost is low.
Description
Technical field
The invention belongs to a kind of sewage-treatment plant, particularly to a kind of stable operation flux large period length, backwash cycle
Long dynamic film component of the good low cost of spontaneous operational effect and preparation method thereof.
Background technology
The conventional process of waste water treating and reutilizing and the discharge of one-level A is activated sludge process at present--the combination work of depth logos
Skill or be membrane bioreactor (MBR).Activated sludge process--the group technology of depth logos, i.e. lives at original denitrogenation dephosphorizing
Property sludge processes on the basis of, increase the technique such as coagulation, plate-spinning filter, sterilization, but this technological process length, equipment be many, floor space
Greatly, the indexs such as ammonia nitrogen total nitrogen are difficult to stably reaching standard.Membrane bioreactor (MBR) has that floor space is little, effluent quality is excellent, can
The advantages such as enhanced biological process, in China, land used is limited, developed area good market prospect, but MBR technique is the most immature,
Membrane flux is low, energy consumption is high, service life is short, limits further genralrlization and uses.
Dynamic Membrane (Dynamicmem-brane) is emerging a kind of sewage disposal film, for by being formed on film base material surface
Sludge blanket plays a kind of new membrane assembly of accurate crown_interception, and wherein self-forming dynamic membrane is by mud flco in filter process
(microorganism and metabolite thereof) is class coating material accumulation shape film forming layer.It forms time and thickness and Biomass etc. and runs bar
Part is closely related, has reported in literature mud flco cumulative speed to be about 0～50g/ (m2H), thus " film layer " is formed relatively slow
And being difficult to stable, cause Dynamic Membrane to form the time longer, generally at 30 minutes to several hours, thus initial stage water quality is difficult to
Meet and require (effective filtration is only formed to certain thickness competence exertion effect at sludge blanket), big capacity of returns can only be used
To film forming, thus add Qian Dao pond load；Secondly, Dynamic Membrane operationally easily occurs because of high sludge concentration that film layer increased
Hurry up, cause effluent flux to decline, effective cycle of operation is relatively short, and lacks effective control measure；Besides, Dynamic Membrane
Backwash weak effect, effluent flux recovery rate is low, causes normal aquifer yield little, is easy to produce irreversible membrane fouling, leads after time length
Cause medicine to wash frequently, add operating cost and operation complexity.This three big defect becomes the restriction good cost of spontaneous operational effect
Low dynamic film component effectively utilizes major obstacle.
Summary of the invention
Technical problem: in order to solve the defect of prior art, the invention provides the dynamic of the good low cost of a kind of operational effect
State membrane module.
Technical scheme: the dynamic film component of the good low cost of a kind of operational effect that the present invention provides, including base material and formation
Dynamic Membrane on base material；Described base material is macropore base material.
As improvement, described base material is sponge, filter screen, non-woven fabrics, porous ceramics, sintered metal net, metallic fiber sintered
Felt, sintered powder material, sintered porous plastics, sintered aluminium oxide, bafta, wool fabric, silk fabrics, synthetic fabrics,
The combination of one or more in glass fiber cloth, non-woven fabric.
Improving as another kind, the longitudinal section of described base material is hollow ring, and its external diameter is that 40-150 millimeter, internal diameter are
10-30 millimeter, a height of 0.1-3 rice；Preferably, its external diameter be 40-100 millimeter, internal diameter be 10-30 millimeter, a height of 0.3-1 rice；
It is highly preferred that its external diameter is 40-60 millimeter, internal diameter is 10-30 millimeter, 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.
Improving as another kind, described Dynamic Membrane includes Filtration Adsorption layer, anaerobic reaction layer and anti-nitre the most successively
Change conversion zone.
Present invention also offers the formation and methods for using them of above-mentioned dynamic film component, comprise the following steps:
(1) formation of Dynamic Membrane: waste water is continued through base material and i.e. forms Dynamic Membrane at substrate surface in 1-7 days, particularly as follows:
Sewage permeates from outside to inside in base material, adsorbs impurity and the mud of some larger particles at substrate surface simultaneously, is formed nascent
Dynamic Membrane；After running a period of time, adsorbing contaminant is continued on nascent Dynamic Membrane surface and mud forms Filtration Adsorption layer, comes into being dynamically
Film is internally formed one layer of fine and close sludge blanket and grows anaerobe and be anaerobic reaction layer, and nascent Dynamic Membrane penetralia grows anti-nitre
Changing antibacterial and be anti-nitration reaction layer, the base material so far forming surface attachment Dynamic Membrane is dynamic film component；
(2) waste water processes: sewage flows through Filtration Adsorption layer at Filtration Adsorption layer inner filtration；Pass through anaerobic reaction layer detesting
The effect of oxygen bacterium issues raw anaerobic reaction, is decomposed by the Organic substance of macromole；Finally flow through anti-nitration reaction layer at denitrifying bacterium
Effect under, utilize the carbon source that anaerobic reaction layer provides, 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 relies on gravity naturally to pass through Dynamic Membrane.
Present invention also offers the application in nitrogenous effluent treatment of the above-mentioned dynamic film component.
Beneficial effect: the present invention provide the good low cost of operational effect dynamic film component simple in construction, with low cost, make
With convenient, relying on the activated sludge cake layer quickly formed on macropore base material and complete to separate, denitrification effect is good, can effectively drop
COD, BOD, almost without energy consumption, it is not necessary to safeguarding, service life is long, and operating cost is low.
Accompanying drawing explanation
Fig. 1 is the structural representation of the dynamic film component of the good low cost of operational effect of the present invention.
Detailed description of the invention
The dynamic film component of low cost good to operational effect of the present invention further illustrates 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.Dynamic
State film 2 includes Filtration Adsorption layer 21, anaerobic reaction layer 22 and anti-nitration reaction layer 23 the most successively.
Preparing 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 base material and i.e. forms Dynamic Membrane at substrate surface in 1-7 days, particularly as follows:
Sewage permeates from outside to inside in base material, adsorbs impurity and the mud of some larger particles at substrate surface simultaneously, is formed nascent
Dynamic Membrane；After running a period of time, adsorbing contaminant is continued on nascent Dynamic Membrane surface and mud forms Filtration Adsorption layer, comes into being dynamically
Film is internally formed one layer of fine and close sludge blanket and grows anaerobe and be anaerobic reaction layer, and nascent Dynamic Membrane penetralia grows anti-nitre
Changing antibacterial and be anti-nitration reaction layer, the base material so far forming surface attachment Dynamic Membrane is dynamic film component；
(2) waste water processes: sewage stream continues through filter adsorption layer naturally at Filtration Adsorption layer inner filtration；Pass through anaerobism anti-
Answer layer to issue raw anaerobic reaction in the effect of anaerobe, the Organic substance of macromole is decomposed；Finally flow through anti-nitration reaction layer to exist
Under the effect of denitrifying bacterium, utilize the carbon source that anaerobic reaction layer provides, to denitrogenation of waste water；
(3) if work process finding, the sludge blanket on film surface is the thickest, affects water flux, now needs backwash, logical
Crossing aeration and wash away film surface, backwash completes to continue to run with；Owing to the present invention is the Dynamic Membrane that large pore material prepares, therefore,
It is the least to stain disease resistance, can only lean on stain disease self gravitation to complete, and its circulation is regulated voluntarily by system；The most energy-conservation
Environmental protection, low cost；And backwashing period is the longest, with little need for backwash.
Table 1
Wang family of Jiangsu anaerobic tank is processed by the dynamic film component utilizing the good low cost of above-mentioned operational effect, knot
Fruit is shown in Table 2.
Table 2
Wherein, comparative example is the Dynamic Membrane using conventional polyurethanes material to prepare.
As shown in Table 2, the dynamic film component of the good low cost of the operational effect of the present invention can effectively remove the ammonia nitrogen in sewage
Deng Organic substance.
Claims (8)
1. the dynamic film component of the good low cost of operational effect, it is characterised in that: include base material (1) and be formed at base material (1)
On Dynamic Membrane (2)；Described base material (1) is macropore base material.
The dynamic film component of the good low cost of a kind of operational effect the most according to claim 1, it is characterised in that: described base material
(1) it is that sponge, filter screen, non-woven fabrics, porous ceramics, sintered metal net, metallic fiber sintered felt, sintered powder material, sintering are many
Hole plastics, sintered aluminium oxide, bafta, wool fabric, silk fabrics, synthetic fabrics, glass fiber cloth, non woven fibre
The combination of one or more in fabric.
The dynamic film component of the good low cost of a kind of operational effect the most according to claim 1, it is characterised in that: described base material
(1) longitudinal section is hollow ring, its external diameter be 40-150 millimeter, internal diameter be 10-30 millimeter, a height of 0.1-3 rice；Preferably,
Its external diameter be 40-100 millimeter, internal diameter be 10-30 millimeter, a height of 0.3-1 rice；It is highly preferred that its external diameter is 40-60 millimeter, interior
Footpath is 10-30 millimeter, a height of 0.4-0.6 rice；Most preferably, its external diameter is 50 millimeters, internal diameter is 20 millimeters, a height of 0.5 meter.
The dynamic film component of the good low cost of a kind of operational effect the most according to claim 1, it is characterised in that: described dynamically
Film (2) includes Filtration Adsorption layer (21), anaerobic reaction layer (22) and anti-nitration reaction layer (23) the most successively.
5. the formation and methods for using them of the dynamic film component described in claim 1, it is characterised in that: comprise the following steps:
(1) formation of Dynamic Membrane: waste water is continued through base material and i.e. forms Dynamic Membrane at substrate surface in 1-7 days, particularly as follows: sewage
Permeate in base material from outside to inside, adsorb impurity and the mud of some larger particles simultaneously at substrate surface, formed nascent dynamic
Film；After running a period of time, adsorbing contaminant is continued on nascent Dynamic Membrane surface and mud forms Filtration Adsorption layer, in nascent Dynamic Membrane
Portion forms one layer of fine and close sludge blanket and grows anaerobe and be anaerobic reaction layer, and nascent Dynamic Membrane penetralia growth denitrification is thin
Bacterium is anti-nitration reaction layer, and the base material so far forming surface attachment Dynamic Membrane is dynamic film component；
(2) waste water processes: sewage flows through Filtration Adsorption layer at Filtration Adsorption layer inner filtration；Pass through anaerobic reaction layer in anaerobe
Effect issue raw anaerobic reaction, the Organic substance of macromole is decomposed；Finally flow through the anti-nitration reaction layer work at denitrifying bacterium
Under with, utilize the carbon source that anaerobic reaction layer provides, to denitrogenation of waste water.
The formation and methods for using them of dynamic film component the most according to claim 5, it is characterised in that: step (1) and step
(2), in, waste water is 0.5-10h by the time in Dynamic Membrane.
The formation and methods for using them of dynamic film component the most according to claim 5, it is characterised in that: step (1) and step
(2), in, waste water relies on gravity naturally to pass through Dynamic Membrane.
8. the application in nitrogenous effluent treatment of the dynamic film component described in claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610643967.0A CN106082435A (en) | 2016-08-08 | 2016-08-08 | A kind of dynamic film component of the good low cost of operational effect |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610643967.0A CN106082435A (en) | 2016-08-08 | 2016-08-08 | A kind of dynamic film component of the good low cost of operational effect |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106082435A true CN106082435A (en) | 2016-11-09 |
Family
ID=57454869
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610643967.0A Pending CN106082435A (en) | 2016-08-08 | 2016-08-08 | A kind of dynamic film component of the good low cost of operational effect |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106082435A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109078371A (en) * | 2018-08-29 | 2018-12-25 | 戚汝常 | The detachable lautertuns of waveform and filter method |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1363526A (en) * | 2001-12-14 | 2002-08-14 | 清华大学 | Process and equipment for filtering liquid mixture of bioreactor by dynamic membrane |
| CN101817588A (en) * | 2010-05-10 | 2010-09-01 | 东南大学 | Activated sludge reaction separation method and device for sewage by sponge substrate |
| CN101857307A (en) * | 2010-06-17 | 2010-10-13 | 同济大学 | Synchronous nitrogen and phosphorus removal process of integral bio-enhancement activated carbon dynamic membrane |
| CN102030409A (en) * | 2011-01-27 | 2011-04-27 | 华侨大学 | Sewage treatment device and process for large modularized gravity-flow self-forming dynamic membrane bio-reactor (MBR) |
| CN102951734A (en) * | 2012-11-26 | 2013-03-06 | 同济大学 | Wastewater treatment device with anaerobic dynamic membrane reactor |
-
2016
- 2016-08-08 CN CN201610643967.0A patent/CN106082435A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1363526A (en) * | 2001-12-14 | 2002-08-14 | 清华大学 | Process and equipment for filtering liquid mixture of bioreactor by dynamic membrane |
| CN101817588A (en) * | 2010-05-10 | 2010-09-01 | 东南大学 | Activated sludge reaction separation method and device for sewage by sponge substrate |
| CN101857307A (en) * | 2010-06-17 | 2010-10-13 | 同济大学 | Synchronous nitrogen and phosphorus removal process of integral bio-enhancement activated carbon dynamic membrane |
| CN102030409A (en) * | 2011-01-27 | 2011-04-27 | 华侨大学 | Sewage treatment device and process for large modularized gravity-flow self-forming dynamic membrane bio-reactor (MBR) |
| CN102951734A (en) * | 2012-11-26 | 2013-03-06 | 同济大学 | Wastewater treatment device with anaerobic dynamic membrane reactor |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109078371A (en) * | 2018-08-29 | 2018-12-25 | 戚汝常 | The detachable lautertuns of waveform and filter method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102863081B (en) | Three-dimensional ecological deodorization dephosphorization denitrification method as well as device and application | |
| CN105668943B (en) | For the multi-stage aeration biological filter tank of purification of water quality and its purification process | |
| JPH0450880B2 (en) | ||
| CN106977042A (en) | A kind of modularization integrated approach handled suitable for soy sauce brewing wastewater | |
| CN101708933A (en) | Water treatment device | |
| Feng et al. | The effects of different carriers on removal performance and membrane fouling by HMBR in treating sewage with low carbon-to-nitrogen ratio | |
| Nikoonahad et al. | Application of novel Modified Biological Aerated Filter (MBAF) as a promising post-treatment for water reuse: Modification in configuration and backwashing process | |
| CN111362402A (en) | Method for reinforcing anaerobic dynamic membrane bioreactor by combining GAC and PAC and application thereof | |
| CN106277567A (en) | A kind of high efficiency sewage disposal device | |
| CN106082435A (en) | A kind of dynamic film component of the good low cost of operational effect | |
| Li et al. | The performance of a biological aerated filter loaded with a novel non-sintered fly-ash ceramsite as pretreatment for dual membrane processes | |
| Alavi Moghaddam et al. | Performance of coarse pore filtration activated sludge system | |
| CN205953773U (en) | High efficiency sewage treatment device | |
| CN206142908U (en) | Dynamic membrane module that operational effect is good with low costs | |
| CN206142999U (en) | Low energy consumption high efficiency sewage treatment device | |
| CN209338220U (en) | A kind of sewage disposal system based on anaerobism-AO- combined artificial wetland | |
| CN204079731U (en) | Creeping bed | |
| CN206142998U (en) | Sewage treatment device of high total nitrogen clearance | |
| CN206142997U (en) | High -efficient sewage treatment device | |
| CN206143003U (en) | Sewage treatment equipment | |
| CN206143000U (en) | Novel high -efficient sewage treatment device | |
| CN206143001U (en) | Novel sewage treatment device | |
| CN105540825A (en) | Fiber bundle bioreactor for sewage treatment | |
| CN206089333U (en) | Sewage treatment device of total nitrogen is got rid of to high efficiency | |
| CN205328695U (en) | A tow biological reaction device for sewage treatment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20161109 |