CN202415243U - MBR (membrane bioreactor) membrane module instrument for descaling by adopting mechanical vibration - Google Patents
MBR (membrane bioreactor) membrane module instrument for descaling by adopting mechanical vibration Download PDFInfo
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- CN202415243U CN202415243U CN2011205451413U CN201120545141U CN202415243U CN 202415243 U CN202415243 U CN 202415243U CN 2011205451413 U CN2011205451413 U CN 2011205451413U CN 201120545141 U CN201120545141 U CN 201120545141U CN 202415243 U CN202415243 U CN 202415243U
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- membrane
- graticule mesh
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- group device
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- 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
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Abstract
The utility model discloses an MBR (membrane bioreactor) membrane module instrument for descaling by adopting mechanical vibration, which comprises membrane modules which are vertically arranged side by side, wherein each membrane module comprises a membrane wire, wherein the upper end and the lower end of the membrane wire are fixed in a membrane box in wax sealing; two grid nets are arranged in a clearance between each two membrane modules, wherein two ends of a grid net at the right side are fixed by a connecting rod; the tail end of the connecting rod is connected to and arranged on a moving grid net at one side out of the membrane module instrument; the outer side of the outer moving grid net is fixed by a vertical post; the vertical post is connected with a motive power device for supplying motive power sources; two ends of a grid net at the left side are fixed by a connecting rod; the tail end of the connecting rod is connected to and arranged on a static grid net at the other side out of the membrane module instrument; the outer side of the outer static grid net is fixed by a vertical post; and the width of the grid net at the right side is greater than the width of the grid net at the left side. According to the utility model, the membrane wire is extruded and vibrated, the dirt on the surface of the membrane wire can be removed effectively, the removing rate is high, and also energy is saved, thus the MBR technology is more perfect.
Description
Technical field
The utility model relates to sewage treatment area, and specifically, the utility model relates to a kind of MBR film group device that adopts the mechanical vibration scale removal.
Background technology
China's water resources owning amount per capita is merely 2250m
3/ people. year, 1/4 of not enough world average level.In more than 600 city of China, have 300 surplus a urban water shortage, surplus wherein the city of severe water shortage has 100, year nearly 6,000,000,000 m of water deficit
3, cause financial loss about 2,000 hundred million yuan because of lack of water every year.North China's water resources ownership per capita has only 250-480m
3/ people. year, being lower than 1/5 of national per capita share, these geographic all cities nearly all face water shortage problem.Therefore reusing sewage is one of important measures of alleviating North China Plain water crisis.
Membrane bioreactor (Membrane Bioreactor is called for short MBR) is one of novel waste water technology of membrane separation technique and biotechnology combination, also claims the film separated activated sludge method.The efficient cutoff performance that it utilizes membrane separation assemblies carries out solid-liquid separation, has effectively reached the purpose of mud-water separation.The efficient crown_interception of film can the effectively catching nitrifier, and it is trapped in the bio-reactor fully, makes nitration reaction smooth, effectively removes ammonia nitrogen, avoids the loss of mud.Can hold back simultaneously the larger molecular organics that for the moment is difficult to degrade, prolong the residence time of these organism, make it to be decomposed to greatest extent at reactor drum.Because the high filtering precision of film, thereby guaranteed the as clear as crystal second pond that saves of water outlet.After using the MBR technology, compare with traditional bioremediation, principal pollutant (COD) clearance can reach 90%, produces water suspension and is bordering on zero with turbidity, and water quality is good and stablize, can direct reuse, realized sewage recycling.Have that biochemical efficiency height, anti-load impact ability are strong, stable effluent quality, floor space is little, sludge discharging period is long, be prone to realize advantages such as automatic control, is one of the most promising wastewater treatment new technology at present.Membrane Bio-reactor Technology is mainly used in municipal sewage treatment/crude sewage and handles and utilization again, fields such as high concentrated organic wastewater processing.
The major equipment of MBR is a film group device; A large amount of hollow fiber ultrafiltration membrane is installed on the film group device; About the general 2mm of ultra-filtration membrane external diameter, about internal diameter 1mm, the ultra-filtration membrane surface is covered with 0.04 micron aperture; See tubular fibre film silk from the outside just as the fine plastics silk of a rule, tubular fibre is arranged in parallel on the film group device.When operation, film group device is placed in the sewage, clear water is inner to the film silk through micropore permeation from the outside of film silk, and mud is blocked in the outside of film silk.With water pump clear water is drawn into the clean water basin from film group device again.High density mixed solution in the membrane biological reaction pond is through membrane sepn, and pollutent is left in the reaction tank with other mikrobe, and treated water then passes through negative pressure-pumping, qualified discharge.
Like Fig. 1, shown in 2, MBR is that the core component of membrane bioreactor is a film group device.Tens of membrane modules are installed on each film group device.Membrane module is made up of with bellows 2 the hollow-fibre membrane silk 1 that the surface is covered with micropore.Tens membrane modules as shown in Figure 1 are installed on the stainless steel stent, become film group device.
Traditional M BR film group device adopts the mode of bottom aeration to remove the dirt on film silk surface.See Fig. 2; Film group device is placed in the sewage lagoon, and pressurized gas flows out from the aperture of boring aeration pipe 3, forms bubble 4, and bubble rises, and drives current and rises, and forms the air water mixed flow, and this fluid ratio heavy and light is unsettled turbulent flow.When gas, water flow through film silk 1, the dirt that the film silk is surperficial washed away.
Owing to contain a large amount of bacterium excretory extracellular polymerics in the sewage, this organism is thickness very, attaches easily on the surface of hollow-fibre membrane silk, stops up the micropore on film silk 1 surface.And this polymeric adhesive is big, and the air water flushing is difficult to cause the film silk frequently to need matting its removing.Influence the normal operation of Sewage Plant.
Above-mentioned deficiency to prior art exists proposes utility model.
The utility model content
In view of the problem that exists in the prior art, the purpose of the utility model is to provide a kind of MBR film group device that adopts the mechanical vibration scale removal.
For realizing above-mentioned utility model purpose; The technical scheme that the utility model provides is: a kind of MBR film group device that adopts the mechanical vibration scale removal, comprise the membrane module that tile vertically is provided with, and membrane module comprises the film silk; The upper and lower end sealing of film silk is fixed in the bellows; Be provided with the twice graticule mesh in the gap between per two membrane modules, wherein graticule mesh two ends in right side are fixed with connecting rod, and the end of connecting rod is connected on the moving graticule mesh that is arranged on the outside side of film group device; The outside of outside moving graticule mesh is fixed with column, and column is connected with the PWR PLT that propulsion source is provided; Graticule mesh two ends, left side are fixed with connecting rod, and the end of connecting rod is connected on the quiet graticule mesh that is arranged on the outside opposite side of film group device, and the outside of outside quiet graticule mesh is fixed with column; The width of right side graticule mesh is greater than the width of left side graticule mesh.
Described PWR PLT comprise the rubber air spring that is arranged between column and the moving graticule mesh, and rubber air spring is connected with air compressor machine through airduct.
The connecting rod outer setting that described and moving graticule mesh is connected has vibrating head.
Described air compressor machine and vibrating head are through a unit control.
The beneficial effect of the utility model is: the utility model adopts the extruding to the film silk to add vibration, can remove the dirt on film silk surface effectively, and elimination efficiency is high, and energy-conservation, makes the MBR membrane Bio-reactor Technology more become perfect.
Description of drawings
When combining accompanying drawing to consider; Through with reference to following detailed, can more completely understand the utility model better and learn wherein many attendant advantages easily, but accompanying drawing described herein is used to provide the further understanding to the utility model; Constitute the part of the utility model; Illustrative examples of the utility model and explanation thereof are used to explain the utility model, do not constitute the improper qualification to the utility model, wherein:
Fig. 1 is the structural representation of prior art membrane module and film group device;
Fig. 2 adopts the structural representation of aeration tube aeration scale removal for prior art;
Fig. 3 is the structural representation of the utility model.
Embodiment
Embodiment to the utility model describes below in conjunction with accompanying drawing.
As shown in Figure 3; A kind of MBR film group device that adopts the mechanical vibration scale removal of the utility model comprises the membrane module that tile vertically is provided with, and membrane module comprises film silk 1; The upper and lower end sealing of film silk is fixed in the bellows 2; Be provided with the twice graticule mesh between the membrane module, wherein graticule mesh two ends in right side are fixing with connecting rod 9, and the end of connecting rod 9 is connected on the moving graticule mesh 8 that is arranged on the outside side of film group device; The outside of outside moving graticule mesh 8 is fixed on the column 11 through rubber air spring 10, and rubber air spring 10 is connected with air compressor machine 14 through airduct 13; Graticule mesh two ends, left side are fixing with connecting rod 6, and the end of connecting rod 6 is connected on the quiet graticule mesh 5 that is arranged on the outside opposite side of film group device, and the outside of outside quiet graticule mesh 5 is fixing with column 7; The width of right side graticule mesh is greater than the width of left side graticule mesh.Connecting rod 9 outer setting that moving graticule mesh 8 connects have vibrating head 12.Air compressor machine 14 is controlled interoperation with vibrating head 12 through a unit (not shown).
The working routine of mechanical vibration scrubbing is: start air compressor machine 14, and through tracheae 13, inflation to rubber air spring 10 in, rubber air spring 10 elongations, promotion dynamic mesh 8 travels forward, and quiet grid 5 is motionless, and film silk 1 is compressed between dynamic mesh 8 and the quiet grid 5.The pressure size is by the air pressure size decision of air compressor machine 14.When to predefined pressure, vibrating head 12 starts.Dynamic mesh 8 begins vibration, drives 1 vibration of film silk, because the film silk of loose distribution is compressed to one, very tight between the film silk, wave of oscillation can be delivered to another root film silk from a film silk.The dirt desorption mechanism on film silk 1 surface: the one, because film silk 1 high-frequency vibration produces acceleration stresses, make dirt receive desorption power, the dirt that attaches on the surface is removed.The 2nd, the friction between the film silk, the dirt that it is surperficial rubs off.Behind the vibration number minute, through the venting port exhaust of tracheae 13, rubber bullet air spring 10 resets, and the moving graticule mesh 8 of pulling is returned.Accomplish a cleaning and descaling operation.
Adopting graticule mesh is to make air-flow, current between the film tow unobstructed as the purpose of the stripper plate of film silk, takes dirt out of film group device.The air water cycling stream of bottom does not stop when the film silk vibrates.
The utility model adopts the extruding to the film silk to add vibration, can remove the dirt on film silk surface effectively, and elimination efficiency is high, and energy-conservation, makes the MBR membrane Bio-reactor Technology more become perfect.
As stated, the embodiment of the utility model has been carried out explanation at length, but as long as break away from the utility model point and the effect of the utility model in fact a lot of distortion can not arranged, this will be readily apparent to persons skilled in the art.Therefore, such variation also all is included within the protection domain of the utility model.
Claims (4)
1. a MBR film group device that adopts the mechanical vibration scale removal comprises the membrane module that tile vertically is provided with, and membrane module comprises the film silk; The upper and lower end sealing of film silk is fixed in the bellows, it is characterized in that, is provided with the twice graticule mesh in the gap between described per two membrane modules; Wherein graticule mesh two ends in right side are fixed with connecting rod; The end of connecting rod is connected on the moving graticule mesh that is arranged on the outside side of film group device, and the outside of outside moving graticule mesh is fixed with column, and column is connected with the PWR PLT that propulsion source is provided; Graticule mesh two ends, left side are fixed with connecting rod, and the end of connecting rod is connected on the quiet graticule mesh that is arranged on the outside opposite side of film group device, and the outside of outside quiet graticule mesh is fixed with column; The width of right side graticule mesh is greater than the width of left side graticule mesh.
2. a kind of MBR film group device that adopts the mechanical vibration scale removal according to claim 1 is characterized in that described PWR PLT comprise the rubber air spring that is arranged between column and the moving graticule mesh, and rubber air spring is connected with air compressor machine through tracheae.
3. a kind of MBR film group device that adopts the mechanical vibration scale removal according to claim 2 is characterized in that the connecting rod outer setting that described and moving graticule mesh is connected has vibrating head.
4. a kind of MBR film group device that adopts the mechanical vibration scale removal according to claim 3 is characterized in that, described air compressor machine and vibrating head are through a unit control.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205451413U CN202415243U (en) | 2011-12-22 | 2011-12-22 | MBR (membrane bioreactor) membrane module instrument for descaling by adopting mechanical vibration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205451413U CN202415243U (en) | 2011-12-22 | 2011-12-22 | MBR (membrane bioreactor) membrane module instrument for descaling by adopting mechanical vibration |
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| Publication Number | Publication Date |
|---|---|
| CN202415243U true CN202415243U (en) | 2012-09-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205451413U Expired - Lifetime CN202415243U (en) | 2011-12-22 | 2011-12-22 | MBR (membrane bioreactor) membrane module instrument for descaling by adopting mechanical vibration |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104003512A (en) * | 2014-06-10 | 2014-08-27 | 清华大学 | Immersion plate-type membrane bioreactor for improving membrane pollution control and wastewater treatment method using same |
| US9333464B1 (en) | 2014-10-22 | 2016-05-10 | Koch Membrane Systems, Inc. | Membrane module system with bundle enclosures and pulsed aeration and method of operation |
| CN106237689A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Floating air-flotation type pollution-resistant vibration filtering structure |
| CN106237690A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Intelligent vacuum floating type vibration filtering structure |
| CN106237687A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Floating air-flotation type vibration filtering structure |
| CN106237688A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Resistant to pollution air supporting vibration filtering structure |
| CN106310758A (en) * | 2015-08-29 | 2017-01-11 | 无锡亮慧环保机械有限公司 | Air floatation type vibration filtering structure |
| USD779631S1 (en) | 2015-08-10 | 2017-02-21 | Koch Membrane Systems, Inc. | Gasification device |
| CN115074243A (en) * | 2022-05-19 | 2022-09-20 | 泰舸赛迩生命科技(无锡)有限公司 | High-membrane column flux cell perfusion culture membrane column system and method and application thereof |
-
2011
- 2011-12-22 CN CN2011205451413U patent/CN202415243U/en not_active Expired - Lifetime
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104003512B (en) * | 2014-06-10 | 2016-03-23 | 清华大学 | A kind of immersed plate type membrane bioreactor of reinforced film Environmental capacity and the method for sewage disposal thereof |
| CN104003512A (en) * | 2014-06-10 | 2014-08-27 | 清华大学 | Immersion plate-type membrane bioreactor for improving membrane pollution control and wastewater treatment method using same |
| US9333464B1 (en) | 2014-10-22 | 2016-05-10 | Koch Membrane Systems, Inc. | Membrane module system with bundle enclosures and pulsed aeration and method of operation |
| US10702831B2 (en) | 2014-10-22 | 2020-07-07 | Koch Separation Solutions, Inc. | Membrane module system with bundle enclosures and pulsed aeration and method of operation |
| US9956530B2 (en) | 2014-10-22 | 2018-05-01 | Koch Membrane Systems, Inc. | Membrane module system with bundle enclosures and pulsed aeration and method of operation |
| USD779631S1 (en) | 2015-08-10 | 2017-02-21 | Koch Membrane Systems, Inc. | Gasification device |
| USD779632S1 (en) | 2015-08-10 | 2017-02-21 | Koch Membrane Systems, Inc. | Bundle body |
| CN106237689A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Floating air-flotation type pollution-resistant vibration filtering structure |
| CN106310758A (en) * | 2015-08-29 | 2017-01-11 | 无锡亮慧环保机械有限公司 | Air floatation type vibration filtering structure |
| CN106237688A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Resistant to pollution air supporting vibration filtering structure |
| CN106237687A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Floating air-flotation type vibration filtering structure |
| CN106237690A (en) * | 2015-08-29 | 2016-12-21 | 无锡亮慧环保机械有限公司 | Intelligent vacuum floating type vibration filtering structure |
| CN115074243A (en) * | 2022-05-19 | 2022-09-20 | 泰舸赛迩生命科技(无锡)有限公司 | High-membrane column flux cell perfusion culture membrane column system and method and application thereof |
| CN115074243B (en) * | 2022-05-19 | 2023-08-04 | 泰舸赛迩生命科技(无锡)有限公司 | Gao Mozhu flux cell perfusion culture membrane column system and method and application thereof |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20120905 |
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| CX01 | Expiry of patent term |