CN201144177Y - Sewage purifier with biological carbon dynamic membrane - Google Patents
Sewage purifier with biological carbon dynamic membrane Download PDFInfo
- Publication number
- CN201144177Y CN201144177Y CNU2007201589413U CN200720158941U CN201144177Y CN 201144177 Y CN201144177 Y CN 201144177Y CN U2007201589413 U CNU2007201589413 U CN U2007201589413U CN 200720158941 U CN200720158941 U CN 200720158941U CN 201144177 Y CN201144177 Y CN 201144177Y
- Authority
- CN
- China
- Prior art keywords
- water
- bed body
- filter cloth
- filtration fabric
- membrane
- 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.)
- Expired - Fee Related
Links
Images
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)
Abstract
The invention provides a charcoal dynamic membrane sewage processing device which includes a bed body, an aerated conduit and a membrane component; one side at the lower part of the bed body is provided with a water inlet; the other side is provided with a mud drain opening; one side of the water inlet is provided with a water flow baffle; the aerated conduit is arranged between the water inlet and the baffle at the internal bottom part of the bed body; at least one 3D filtration fabric membrane component is arranged between the baffle and one side of the mud drain opening inside the bed body; the surrounding of the 3D filtration fabric membrane component is filled with reed carbon; a water outlet canal is arranged on the 3D filtration fabric membrane component; the utility model utilizes a 3D filtration fabric dynamic membrane and a reed carbon dynamic membrane to combine to purify water; the 3D filtration fabric is provided with a unique aperture space structure; the filter property is high and the service life is long; biomembranes can be formed both on the reed carbon and the 3D filtration fabric; the 3D filtration fabric membrane component is hard to be plugged; the load is high; the processing effect is stable; the utility model has a larger membrane forming area, a high microorganism content, a clear water quality, a simple structure and is convenient to be operated and ran.
Description
Technical field
The utility model relates to a kind of biological activated carbon dynamic biological membrane sewage purification device, belongs to the sewage purification technology field.
Background technology
Bioreactor of dynamic membrane is a kind ofly to utilize wide-aperture microgrid material as film base material, filters the dynamic biological film that forms by active sludge pollutent is trapped on the membrane module, generates filter cake, purifies waste water, and mud-water separation effect is preferably arranged.But when Dynamic Membrane did not form, the ability of damming caused initial effluent quality not up to standard easily, and membrane module is easy to stop up often flushing repeatedly.
Summary of the invention
The utility model is for overcoming the deficiencies in the prior art, and it is film base material that a kind of reed charcoal and 3 D filter cloth with cheapness is provided, and is easy to microorganic adhesion, initial good, the not susceptible to plugging charcoal Dynamic Membrane of the membrane module effluent treatment plant of effluent quality.
The utility model adopts following technical proposals to realize:
This charcoal Dynamic Membrane effluent treatment plant comprises a body, aeration tube and 3 D filter cloth membrane module, bed body bottom one side is provided with water-in, opposite side is provided with mud discharging mouth, water-in one side is provided with the current baffle plate, bed body inner bottom part is provided with aeration tube between water-in and baffle plate, at least be provided with a 3 D filter cloth membrane module between inherent baffle plate of bed body and mud discharging mouth one side, fill full reed carbon filling material around the 3 D filter cloth membrane module, 3 D filter cloth membrane module upper end is provided with water output duct.
The 3 D filter cloth membrane module is that the rack periphery that 3 D filter cloth is wrapped in hollow is made.
During this device operation, sewage is entered by bed body water-in, enters reaction zone behind aeration, cross-flow passes under the effect of air-flow and baffle plate, microorganism breeds in a large number, and its meta-bolites is very fast to form the xanthan gel layer at the reed carbon surface, the macrobead suspended substance is by the charcoal detention, rough purification sewage.Sewage through the reed carbon purifying passes through the 3 D filter cloth membrane module, and forms microbial film on its surface, and sewage is further purified, and flows out the water output duct in stretching into 3 D filter cloth membrane module inner chamber at last.
The utility model utilizes dynamic membrane of 3 D filter cloth and reed charcoal Dynamic Membrane associating water purification, and 3 D filter cloth has unique aperture space structure, strainability height, and long service life; All can form microbial film on reed charcoal and the 3 D filter cloth purifying waste water, and make the 3 D filter cloth membrane module be difficult for stopping up, load is high, and treatment effect is stable.The utility model biofilm surface-area is big, the content of microorganisms height, and effluent quality is limpid, and is simple in structure, and operation, operation are conveniently.
Description of drawings
Accompanying drawing is the structural representation of the utility model charcoal Dynamic Membrane effluent treatment plant.
Wherein 1, the bed body, 2, water-in, 3, aeration tube, 4, the 3 D filter cloth membrane module, 5, the reed charcoal, 6, water output duct, 7, mud discharging mouth, 8, baffle plate.
Embodiment
As shown in drawings, this charcoal Dynamic Membrane effluent treatment plant mainly comprises a body 1, aeration tube 3 and 3 D filter cloth membrane module 4, bottom one side of bed body 1 is provided with water-in 2, opposite side is provided with mud discharging mouth 7, with the water-in baffle plate 8 that is provided with separated by a distance, bed body 1 bottom is provided with aeration tube 3 between water-in 2 and baffle plate 8.Be provided with three 3 D filter cloth membrane modules 4 between bed body Internal baffle 8 and mud discharging mouth 7 sides, and around it, fill full reed charcoal 5.The height of reed charcoal 5 is lower than the height of baffle plate 8.3 D filter cloth membrane module 4 is that the wire netting periphery that 3 D filter cloth is wrapped in hollow is made, and its top is provided with the water output duct 6 that communicates with its internal cavity, gets rid of thus after the sewage purification.Bed body 1, water-in 2, mud discharging mouth 7 are all made by the PVC plastics, and baffle plate 8 is made by PVC plastics with holes, the water distribution effect of having held concurrently.Aeration tube 3 is this refining plant aeration.
Reed charcoal 5 is wrapped in the periphery of 3 D filter cloth membrane module 4, when sewage enters a bed body 1 earlier through the biomembranous purification of reed charcoal, enter 3 D filter cloth membrane module 4 water purification again, 3 D filter cloth frame membrane module 4 is fixed in the body slot, and sewage is cross-flow passes under the effect of baffle plate 8 and 3 D filter cloth membrane module 4.
During this device operation, sewage is entered by water-in 2, cross-flow passes under the effect of the air-flow of aeration tube 3 and baffle plate 8, enter the opposite side of a body by the baffle plate water distributing pore, fully contact with reed charcoal 5, microorganism breeds in a large number, and its meta-bolites forms the microbial film that one deck xanthan gel layer is formed by the surface of reed charcoal 5 and 3 D filter cloth membrane module 4.Sewage makes pollutent detention and absorption degradation by reed charcoal microbial film, purifies waste water.Subparticle and deliquescent macromole be by the small-bore microbial film on the membrane module 4, and organism is by Dynamic Membrane absorption degradation successively, and sewage is progressively purified.At last, sewage enters in the cavity of 3 D filter cloth assembly 4, under the driving power of liquid level and water output duct 6 difference of altitude, flows out from water output duct 6 automatically in the bed body.Behind the operation certain hour, the mud of accumulation can be discharged by mud discharging mouth 7.
Claims (2)
1. charcoal Dynamic Membrane effluent treatment plant, comprise a body, aeration tube and 3 D filter cloth membrane module, bed body bottom one side is provided with water-in, opposite side is provided with mud discharging mouth, water-in one side is provided with the current baffle plate, bed body inner bottom part is provided with aeration tube between water-in and baffle plate, it is characterized in that: be provided with a 3 D filter cloth membrane module at least between inherent baffle plate of bed body and mud discharging mouth one side, fill full reed carbon filling material around the 3 D filter cloth membrane module, 3 D filter cloth membrane module upper end is provided with water output duct.
2. charcoal Dynamic Membrane effluent treatment plant according to claim 1 is characterized in that: described 3 D filter cloth membrane module is that the rack periphery that 3 D filter cloth is wrapped in hollow is made.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201589413U CN201144177Y (en) | 2007-12-25 | 2007-12-25 | Sewage purifier with biological carbon dynamic membrane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201589413U CN201144177Y (en) | 2007-12-25 | 2007-12-25 | Sewage purifier with biological carbon dynamic membrane |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201144177Y true CN201144177Y (en) | 2008-11-05 |
Family
ID=40081045
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201589413U Expired - Fee Related CN201144177Y (en) | 2007-12-25 | 2007-12-25 | Sewage purifier with biological carbon dynamic membrane |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201144177Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103382047A (en) * | 2013-07-18 | 2013-11-06 | 马鞍山十七冶工程科技有限责任公司 | Bamboo charcoal packing membrane bioreaction sewage treatment method |
| CN105668792A (en) * | 2016-03-07 | 2016-06-15 | 邱学尧 | Bio-contact oxidation filter sedimentation tank |
-
2007
- 2007-12-25 CN CNU2007201589413U patent/CN201144177Y/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103382047A (en) * | 2013-07-18 | 2013-11-06 | 马鞍山十七冶工程科技有限责任公司 | Bamboo charcoal packing membrane bioreaction sewage treatment method |
| CN105668792A (en) * | 2016-03-07 | 2016-06-15 | 邱学尧 | Bio-contact oxidation filter sedimentation tank |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203866157U (en) | Integrated baffle type anaerobic/anoxic/aerobic membrane filtration high-concentration organic wastewater treatment device | |
| CN103073108A (en) | Moving bed type purification tank | |
| KR101540240B1 (en) | Filtering apparatus using carbonized wood | |
| CN201598221U (en) | Biofilter-ceramic membrane bioreactor | |
| CN201144177Y (en) | Sewage purifier with biological carbon dynamic membrane | |
| CN203558914U (en) | Membrane biological reactor (MBR) membrane rack jitter device | |
| CN201056517Y (en) | Multi-layer dynamic film waste water purifying device | |
| CN200985300Y (en) | Bristle charcoal biological contacting oxidizing reaction device | |
| CN212425789U (en) | Domestic sewage treatment device | |
| CN110862193A (en) | High-efficient municipal sewage treatment device | |
| CN204958677U (en) | Low energy consumption sewage treatment system | |
| CN203545843U (en) | Composite type oil removing equipment | |
| CN211644936U (en) | Culture water treatment system | |
| CN204281523U (en) | Integrated slaughterhouse wastewater treatment equipment | |
| CN209113682U (en) | A kind of multi-stage biological filter tank | |
| CN201427890Y (en) | Biological aerated filter for sewage purification | |
| CN205821106U (en) | Triple effect integrated combination purifier | |
| CN101323485A (en) | Self-forming dynamic membrane coupling corrosion cell type effluent purification bed | |
| CN213977231U (en) | Sewage treatment system for farm | |
| CN201272715Y (en) | Integrated membrane biological sewage treatment device | |
| CN205367866U (en) | Aeration biological filter | |
| CN210085208U (en) | Industrial wastewater purification treatment equipment | |
| CN210528715U (en) | Novel purify groove | |
| CN220116387U (en) | Non-point source buffer belt | |
| CN202063796U (en) | Three-dimensional top end gradation biological fluidized bed |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081105 Termination date: 20111225 |