CN2387105Y - Pressure type membrane filtering and discharging anaerobic reactor - Google Patents
Pressure type membrane filtering and discharging anaerobic reactor Download PDFInfo
- Publication number
- CN2387105Y CN2387105Y CN99219286U CN99219286U CN2387105Y CN 2387105 Y CN2387105 Y CN 2387105Y CN 99219286 U CN99219286 U CN 99219286U CN 99219286 U CN99219286 U CN 99219286U CN 2387105 Y CN2387105 Y CN 2387105Y
- Authority
- CN
- China
- Prior art keywords
- reactor
- membrane
- filtering
- anaerobic reactor
- anaerobic
- 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
-
- Y02W10/12—
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a pressure film filtering drainage anaerobic reactor, the shell body of which is a sealing pressure bearing type tank structure; certain internal pressure is generated in the reactor under the action of intake pressure; a film filtering drainage device is arranged in the reactor; under the action of the internal pressure, sewage which takes the biochemistry action is drained by the film filtering drainage device, and anaerobic sludge in the water is blocked in the reactor to greatly enhance the sludge concentration in the reactor, and thus, biochemistry efficiency is greatly enhanced. The utility model can be used as a hydrolysis acidification reactor used for producing acid phases through adjusting design parameters, and can be used as an anaerobic reactor used for producing methane phases. The utility model has the advantages of small equipment volume, simple structure, high processing efficiency, good water draining quality, convenient operation management, low construction cost, etc.
Description
The present invention is a sewage disposal technology.
Anaerobic Microbiological Treatment Technology is owing to have distinguishing features such as operation energy consumption is low, sludge yield is few, organic loading height, used widely in handling high-concentration organic industrial waste water and develops.Existing various anaerobic biological treatment methods are more, but there is a common shortcoming, a large amount of anaerobic sludges are difficult to all be retained in the reactor in the water, considerable part mud runs off with water outlet the sludge concentration in the reactor is reduced, have a strong impact on the biochemical reaction efficient and the effluent quality of anaerobic reactor, cause that the anaerobic reaction equipment volume is big, cost is high.
In view of the existing above-mentioned many disadvantages of existing anaerobic biological treatment method, the objective of the invention is to invent a kind of anaerobic reactor with filtering and draining pressurized film, utilize the micro-pore-film filtration filtration of material, all be retained in the anaerobic sludge in the water outlet in the reactor, increased the sludge concentration in the reactor effectively, biochemical efficiency is greatly improved, thereby reaches the purpose that effluent quality is good, equipment volume is little, construction costs is low.
According to design, the housing of anaerobic reactor with filtering and draining pressurized film of the present invention is a seal and pressure bearing formula tank structure, presses in the generation necessarily in the reactor under the intake pressure effect.In reactor, be provided with the membrane filtering drainage device, biochemical good sewage is under interior pressure effect, after filtering, the membrane filtration module on the membrane filtering drainage device discharges, the mud that suspends in the water then all is retained in the reactor, anaerobic sludge concentration in the reactor is increased substantially, thereby sewage treating efficiency also is greatly improved thereupon.
In order to further specify implementation detail of the present invention, provide most preferred embodiment of the present invention below in conjunction with accompanying drawing.
Accompanying drawing 1 is an anaerobic reactor with filtering and draining pressurized film.
Shown in accompanying drawing 1, accompanying drawing 2, the housing 1 of anaerobic reactor with filtering and draining pressurized film of the present invention is a seal and pressure bearing formula tank structure, and safety valve 2, electric-powered air release valve 3, pressure transmitter 4, water inlet pipe 5, shore pipe 6 are installed thereon.In reactor, be provided with into water injector 10, membrane filtering drainage device 9, water level sensor 7, water level sensor 8.Many groups membrane filtration module 11 that membrane filtering drainage device 9 is made by the micro-pore-film filtration material is fixed in that ring-type is catchmented the membrane filtering drainage system that constitutes on the water shoot 12 and the automatic backwash system of the membrane filtration module 11 that is made of backwashing pump 13, electrically operated valve 14, electrically operated valve 15, pressure transmitter 4 and housing 16 forms.Wherein membrane filtration module 11 is membrane filtration bags 17 made from the micro-pore-film filtration material, be placed in percentage of open area greater than also using lock ring 19 that its sealing and fixing is formed on 50% the tubular support frame 18, the top of membrane filtration module 11 is union 20, is used for that membrane filtration module 11 is fixed in ring-type and catchments on the water shoot 12.
Implement the present invention, sewage is advanced in people's reactor by water inlet injector 10 by water inlet pipe 5, and under the mixing and stirring action of injector 10, very fast being diffused into equably in the reactor with behind the mud thorough mixing carried out biochemical reaction.Under the intake pressure effect, form certain interior pressure in the reactor, under interior pressure effect, biochemical good sewage is discharged after the membrane filtration module on the membrane filtering drainage device 9 11 filters, the mud that suspends in the water then all is retained in the reactor, sludge concentration in the reactor is improved significantly, and biochemical efficiency also is improved thereupon significantly.After operation for some time; it is more and more to be adsorbed in membrane filtration bag 17 lip-deep mud flco things; the membrane flux of membrane filtration bag 17 is progressively reduced; water displacement reduces; press constantly in the reactor and increase; in case reach the design pressure value; then pressure transmitter 4 arrives housing 16 with message feedback at once; 16 instructions of housing intake pump is shut down, and closes electrically operated valve 15, opens electrically operated valve 14; start 13 pairs of membrane filtration bags of backwashing pump 17 and carry out back flushing; its membrane flux is recovered, and under housing 16 instructions, membrane filtering drainage device 9 recovers works better afterwards.Owing to can produce a large amount of gases in the anaerobic reaction process, occupy big quantity space and make water level decline in the reactor, in case liquid level drops to barrier line, water level sensor 7 had both been carved message feedback to housing 16, housing 16 had both been carved and had been opened electric-powered air release valve 3, the liquid level that water inlet is risen is all discharged gas in the reactor, after treating that liquid level rises to set(ting)value, water level sensor 8 had both been carved and had been given housing 16 with message feedback, housing 16 is closed electric-powered air release valve door 3 at once, makes reactor recover normal operating conditions.In case some fault that occurs in service causes pressing above set(ting)value in the reactor, then safety valve 2 is opened interior pressure and the warning that sheds reactor automatically, can carry out shutdown maintenance to total system.
The present invention can make it both can be anti-as the anaerobism of producing sour phase by adjust design parameters Answer both reactor for hydrolysis and acidification of device, can use as the anaerobic reactor of methanogenic phase again, Compare with other anaerobic bio-treated method, the present invention has little, the structure letter of equipment volume Single, treatment effeciency is high, effluent quality good, operational management is easy, it is many that construction costs is low etc. Advantage.
Claims (3)
1, a kind of anaerobic reactor with filtering and draining pressurized film, the housing 1 that it is characterized in that said anaerobic reactor with filtering and draining pressurized film is seal and pressure bearing formula tank structure, safety valve 2, electric-powered air release valve 3, pressure transmitter 4, water inlet pipe 5 and shore pipe 6 are installed on it, in reactor, are provided with into water injector 10, membrane filtering drainage device 9, water level sensor 7 and water level sensor 8.
2, anaerobic reactor with filtering and draining pressurized film according to claim 1 is characterized in that many groups membrane filtration module 11 that said membrane filtering drainage device 9 is made by the micro-pore-film filtration material is fixed in that ring-type is catchmented the membrane filtering drainage system that constitutes on the water shoot 12 and the automatic backwash system of the membrane module 11 that is made of backwashing pump 13, electrically operated valve 14, electrically operated valve 15, pressure transmitter 4 and housing 16 forms.
3, as anaerobic reactor with filtering and draining pressurized film as described in the claim 1,2, it is characterized in that the membrane filtration module 11 on the said membrane filtering drainage device 9, it is the membrane filtration bag made from the micro-pore-film filtration material 17, be placed in percentage of open area greater than also using lock ring 19 that its sealing and fixing is formed on 50% the tubular support frame 18, the top of membrane filtration module 11 is union 20, is used for that membrane filtration module 11 is fixed in ring-type and catchments on the water shoot 12.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN99219286U CN2387105Y (en) | 1999-08-16 | 1999-08-16 | Pressure type membrane filtering and discharging anaerobic reactor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN99219286U CN2387105Y (en) | 1999-08-16 | 1999-08-16 | Pressure type membrane filtering and discharging anaerobic reactor |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2387105Y true CN2387105Y (en) | 2000-07-12 |
Family
ID=34010245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN99219286U Expired - Fee Related CN2387105Y (en) | 1999-08-16 | 1999-08-16 | Pressure type membrane filtering and discharging anaerobic reactor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2387105Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100534926C (en) * | 2007-10-18 | 2009-09-02 | 郑俊 | Wastewater treatment technique for pressurization static bed biomembrane reactor |
-
1999
- 1999-08-16 CN CN99219286U patent/CN2387105Y/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100534926C (en) * | 2007-10-18 | 2009-09-02 | 郑俊 | Wastewater treatment technique for pressurization static bed biomembrane reactor |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201932982U (en) | Combined system using micro-electrolysis-MBR (membrane bio-reactor) combined technology to treat printing and dyeing wastewater | |
CN211141811U (en) | Landfill leachate's positive osmotic treatment system | |
CN111249797B (en) | Volatile fatty acid recovery device based on carbon-based solid acid filled hollow fiber membrane | |
CN211035539U (en) | Take landfill leachate electrochemical treatment device of filtration membrane processing | |
CN112194250A (en) | System and method for recycling biogas energy in organic wastewater anaerobic membrane biological treatment | |
CN2387105Y (en) | Pressure type membrane filtering and discharging anaerobic reactor | |
CN107381810A (en) | A kind of MBR composite wastewaters processor | |
CN101665305B (en) | Method for processing straw-pulp-papermaking wastewater by using combined UASB plus A/O technique | |
CN112321109A (en) | Environment-friendly septic tank that security performance is high | |
CN206127080U (en) | A manufacturing equipment for refuse disposal filtration liquid | |
CN205838768U (en) | Wastewater treatment equipment | |
CN1284479A (en) | Anaerobic reactor with filtering and draining pressurized film | |
CN1281825A (en) | Pressure type membrane filtering drainage biochemical reactor | |
CN212864476U (en) | Black and odorous water treatment device for ecological dredging | |
CN105018961B (en) | It is a kind of that the method that percolate prepares alcohols is reduced with electro-catalysis | |
CN211595354U (en) | Sewage treatment system | |
CN112723555A (en) | Microbial fermentation device for sewage treatment | |
CN2393868Y (en) | Bioreactor with pressure membrane for filtering drained water | |
CN206289132U (en) | A kind of device for being applied to sulfate radical high concentration sterol production wastewater treatment high | |
CN1382651A (en) | Process for comprehensively treating sewage | |
CN211664916U (en) | UASB anaerobic tower | |
CN217972685U (en) | Leachate microfiltration filtering device | |
CN110054354B (en) | Anaerobic treatment device for leachate generated by waste incineration and power generation | |
CN215799072U (en) | System for sludge deodorization decrement | |
CN214571165U (en) | Landfill leachate fully-quantized processing device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |