CN101104534A - Community closed medium water landscape water system organism gas float BOAG treatment method and device - Google Patents
Community closed medium water landscape water system organism gas float BOAG treatment method and device Download PDFInfo
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- CN101104534A CN101104534A CNA2006100288194A CN200610028819A CN101104534A CN 101104534 A CN101104534 A CN 101104534A CN A2006100288194 A CNA2006100288194 A CN A2006100288194A CN 200610028819 A CN200610028819 A CN 200610028819A CN 101104534 A CN101104534 A CN 101104534A
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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
Abstract
Provided is a BOAF treating method for purifying the water landscape, water system and water quality in the sealed small social region and the apparatus thereof. The method substitutes a drug feeding system necessary for all of the gas flotation apparatus by a biological reacting pool, mixes the original water in the water landscape and water system in the sealed small social region with the active bio-floculation from the BOAF pool. A mixed liquid flow formed by depositing in the biochemical reacting pool for a certain period is flowing into the BOAF pool for a treatment. The water output from the BOAF pool is returned to the water landscape and water system after sterilizing by the ultraviolet sterilizer. The mixing liquid flowing into the BOAF pool obtains a separation of the water output and the active bio-floculation by the means of gas flotation. The active bio-floculation returns to the front end of the biochemical reacting pool and continues to mix with the original water for a recycle reaction. A small part of water output forms the gas dissolving water and returns to the BOAF pool to provide slight bubbles for the bio-floculation separation. The system apparatus ensures a qualified landscape water and keeps a water environment balance in the water system in the sealed small social region.
Description
Technical field
The present invention relates to a kind of BOAF treatment process and system and device thereof that is used for community closed water landscape water system purification of water quality, belong to water technology and water resources recycle utilization field.
Background technology
Sub-district view water system has characteristics such as water surface area is relatively little, water environment capacity is little, water body self-purification ability is low usually.Especially seal and mobile poor unhurried current water body, climate change, mankind's activity and surrounding enviroment all can pollute it, cause water quality deterioration, are embodied in that transparency is low, water body is muddy, wawter bloom is spread unchecked, even it is smelly to turn black, and therefore must carry out the purification treatment of view water system.Make a general survey of domestic and international view water system process technologies shape, can be divided into physics method, chemical method and biology/ecological method three major types in the view water system improvement technology of using or entered the pilot scale stage.
Physical method mainly contains bed mud dredging, machinery except that silt is dashed in algae, artificial oxygenation, diversion, water etc. is changed in diversion.
The bed mud dredging mainly is to improve at the high water body of bed mud nutrition content, but in excavating depth, prevents that the control of aspect such as titanium pigment and the release of ammonia nitrogen secondary in the deep layer bed mud is difficult.It is that the mistake Sheng algae in the water body is removed that machinery removes algae, though effective in short-term, often cure the symptoms, not the disease.Artificial oxygenation is the aeration aerating that relies on water, can only the local dissolved oxygen content that improves in the water body, and be difficult to guarantee the aerobic environment of whole water body.The diversion dirt removal comes down to the dilution diffusion to water pollutant and planktonic algae, and is real in pollution transportation, substantial improvement do not carried out in pollution at all.Water is changed in diversion then must the competent clean water source card of going bail for.
Chemical process comprises that mainly the adding chemical agent kills the precipitation of algae, adding molysite promotion phosphorus, adds lime denitrogenation etc.Characteristics such as chemical process has less investment, and Operation and maintenance are convenient, and are effective at different pollutents in the water, need add corresponding medicament and realize, but must take the secondary pollution of chemicals to the hydrobiological toxicity and the ecosystem into account.Therefore, the application of chemical method has significant limitation, generally uses as jury.
Biology/ecological method recovery technique principle is to utilize the vital movement of the biological or cultivation of cultivating, the microorganism that inoculates, to water pollutant shift, conversion and Degradation, thereby water body is restored, and this technology is a kind of reinforcement to nature restorability and self-purification capacity.But it is harsh that this method requires biomembranous cultivation domestication, the program complexity, the treatment time is long, artificial swamp treatment technology especially, floor space is big and be subjected to weather effect big, especially at water body than hour playing a role.
A kind of in recent years physico-chemical process that is normally used in the past to water treatment---air supporting method, because separation efficiency height, and have the effect of oxygenic aeration in water concurrently, begin the former water that is widely used in handling low temperature, low turbid, high algae, high luminance relay and is subjected to Organic pollutants.Show all that about studying and using remove and separate inorganic and organic suspension beyond the region of objective existence, the air supporting method also has certain removal effect for dissolved organic matter in the water.Because that the view water system is rendered as usually that algae amount is many as containing, look is heavily distinguished the flavor of is smelly, water quality is followed water quality characteristics such as seasonal variation, increase to a certain degree coagulation one precipitate the intractability of a filtration process.Therefore, air-float technology is introduced in the landscape water treatment technology, can be given full play to the air supporting method and precipitator method characteristics separately, and obtain treatment effect preferably.But, the subject matter of air supporting method existence at present is: no matter adopt traditional air supporting or shallow air-floatation, still need dosing coagulant owing to enter the former water of air flotation pool, just inevitably bring secondary pollution---problems such as the treatment and disposal of chemical body refuse, any coagulating agent adds the suspension pollutent that all can only remove in the sewage and few part dissolved organic matter in addition, for the basic reason that causes water pollution---nitrogen, phosphorus problem, then can't effectively remove.
In sum, make a general survey of various landscape water treatment technologies, no matter adopt which kind of single view treatment technology, there is problem more or less respectively at aspects such as economy, energy consumption, timeliness or secondary pollution controls, particularly the chief culprit who causes the body eutrophication problem---aspect the removal of nitrogen and phosphorus and dissolubility pollutant, there are not a cover economical, practical approach or system reliably so far.
Summary of the invention
For overcoming above-mentioned shortcoming, the present invention proposes a kind of community closed middle water landscape water system BOAF (based on the air supporting of biology) treatment process and system and device thereof, purpose is to provide a kind of economical and efficient free of contamination new technology for the purification of water quality of middle water landscape water system.By making up a kind of like this treatment process and system and device thereof that combines biological and air flotation technology advantage of BOAF, realize community closed in the purification of water quality of water landscape water system, solve current view water system treatment process the nitrogen that can't effect a radical cure and the problem of phosphorus and dissolubility pollutant.
Medium water landscape water system organism gas float BOAG treatment method in community closed is characterized in: the former water in the landscape water body is sinked the scum silica frost mixing zone of biological reaction tank earlier by intake pump, and former water enters the catalytic oxidation district after the scum silica frost with the backflow of BOAF pond mixes; The air in catalytic oxidation district is provided by roots blower, the muddy water mixed solution in catalytic oxidation district flows in the BOAF pool device through water inlet pipe, the dissolved air water that the BOAF pool device provides by air dissolved pump is realized separating of system's water outlet and active bio flco, the scum silica frost of its generation is back to the scum silica frost mixing zone of biological reaction tank after handle in the BOAF pond, proceeds biological respinse with the former water in the landscape water body; Most of water outlet behind its separating clarifying is recycled into middle water landscape water system by going out water pump after the uv steriliser sterilization, and the small portion water outlet is used to provide dissolved air water by air dissolved pump.
The scum silica frost mixing zone is the amphimicrobian environment, and its dissolved oxygen (DO) remains on below the 0.2mg/L, and hydraulic detention time is about 15min; The catalytic oxidation district is an aerobic environment, and its DO remains on 3～4mg/L, and hydraulic detention time is about 45min.
Water landscape water system BOAF treatment system in community closed, can pass through magnetic flow meter, level relay, magnetic valve, controller etc. connects with computer, according to the water-quality guideline value that water quality monitoring system obtains, realize the automatization of operation of high-level system and water quality monitoring (WQM).
Medium water landscape water system organism gas float BOAG treatment unit in community closed, it comprises a BOAF pond, is characterized in: be divided into two functional zone in the BOAF pond: current stabilization zone of action and disengaging zone, its ratio are 1: 8, are separated fully by the subregion dividing plate.
The current stabilization zone of action: a rotating operation platform is arranged on the BOAF pond, and the rotating operation platform is crossed on the current stabilization zone of action, is connected with the subregion dividing plate, is driven by the peripheral drive device on the rim track of being located at flotation cell; A subregion dividing plate wherein opposite, water overflow direction with sense of rotation, and an opening is arranged between the rotating operation platform; Several honeycomb screens are the concentric tapered plate, are fixed on the rotating operation platform; Water inlet pipe is connected by rotation waterpower joint with rotatable center sleeve, and into water water distributing pipe and dissolved air water water distributing pipe are arranged in the rotatable center sleeve, and water inlet water distributing pipe uniform distribution stretches into bottom, current stabilization zone of action; The dissolved air water water distributing pipe is divided into several dissolved air water range pipes after stretching into bottom, current stabilization zone of action, at bottom, current stabilization zone of action uniform distribution; The other end of water inlet pipe is connected with biological reaction tank, and the other end of dissolved air water pipe is connected with air dissolved pump.
Disengaging zone: include the scum silica frost collection bucket, clear water water collector and bucket; The scum silica frost collection bucket below the rotating operation platform, the front portion of water distribution system, form by two flow deflector and spiral scum silica frost slag scrapers at an angle, the scum silica frost comb is arranged at scum silica frost collection bucket bottom, the scum silica frost comb is connected with the scum silica frost mixing zone by pipeline; The clear water water collector is made up of several clear water headers, is covered by the shroud that catchments, and the water side is connected with rising pipe and return line; Rising pipe is connected with the view water system, and return line is connected with air dissolved pump; Bucket is positioned at the bottom, pond, with the mud discharging pipe coupling.The pool bottom sludge scraper plate is fixed on the bottom of pond body rotational structure, is controlled by the rotating operation platform.
Current stabilization zone of action, BOAF pond constitutes a belt current stabilization zone by several honeycomb screens, under the current stabilization effect, the mixed solution of former water and active bio flco and dissolved air water evenly enter bottom, current stabilization zone of action synchronously, and it is the micro-bubble of 10 μ m that dissolved air water discharges the back a large amount of diameters of generation.These micro-bubbles contact with the mixed solution thorough mixing in the metastable current stabilization of water body zone of action, adsorb the biological floe come-up in the mixed solution simultaneously, and separate to the disengaging zone along the rapid overflow of flow deflector direction.
The BOAF pond is driven by the peripheral drive device that is fixed on the rotating operation platform, and the rotating operation platform through driving drives parts rotations such as rotatable center sleeve, water inlet water distributing pipe, honeycomb screen, dissolved air water water distributing pipe, spiral scum silica frost slag scraper, pool bottom sludge scraper plate, clear water header.Because the velocity of rotation size of rotating operation platform equals the speed that mixed solution flows into the contact reacts district, direction is just in time opposite, and Inlet and outlet water carries out synchronously, so the speed of relative movement of water inlet mixed solution the BOAF pond in and water outlet is zero.In addition, by the pool bottom sludge scraper plate of rotating operation platform interlock with the pond at the bottom of and heavy mud on the pool wall scrape in the bucket, regularly by the pool bottom sludge discharged.Honeycomb screen is the concentric tapered plate that is fixed on the rotating operation platform, with the rotation synchronously of water distribution part, every simultaneously adjacent two conical plates are formed the belt air supporting of an inclination, make the water in this belt air supporting zone be in laminar flow regime always, quickened the lift velocity of granule foreign like this with micro-bubble.Header is covered with and places clear water header top, guarantees the hydraulics of water outlet.
The rotating operation platform is the steel bridge of forming with the U-steel girder, outstanding year all running parts, and lay diamond plate and handrail, handled easily and sampling.
Water inlet pipe of installing in rotatable center sleeve and various control signal wires etc., they can not rotate.
It is that the mud scum silica frost that former water and BOAF pool device are refluxed carries out thorough mixing that the scum silica frost mixing zone mainly acts on, amphimicrobian environment provides denitrifying condition for the nitrogen-containing pollutant in the former water, for its further aerobic removal pollutent in the catalytic oxidation district is given security;
It is former water and the abundant contact reacts of active sludge dross mixture that makes after the anaerobism contact that the catalytic oxidation district mainly acts on, and utilizes the metabolism of active sludge microorganism, further removes organic pollutant and nitrogen and phosphorus pollutants in the polluted raw.
BOAF technology of the present invention and system and device thereof, simultaneously based on biological respinse and physical reaction principle, its water inlet is the mixed solution of former water and active bio flco, need not other dosing coagulant, dynamically water inlet in the operational process, static water outlet, assisting down of center rotating operation platform, the speed of relative movement that makes mixed solution enter the BOAF pool device is zero, thereby suppressed the turbulent flow in the groove, guarantee that flotation biological floe lift velocity reaches or approaching theoretical raising speed, thereby can stablize the free of contamination dissolved air flotation of carrying out by economical and efficient, and greatly improved the quick-acting of traditional biological processing aspect solid-liquid separation, shortened the time of mud-water separation greatly.
The present invention has following characteristics and positively effect:
(1) the former water of community closed middle water landscape water system and additional water source adopt community life sewage to reach the middle water of landscape water quality standard after Treatment for Reuse, reduce water pollution, conserve water resource to greatest extent.
(2) water inlet of BOAF treatment unit is the mixed solution of former water and active bio flco, promptly replace the necessary medicine system of air supporting with biological reaction tank, utilize the degraded and the adsorption of biological floe, solubility pollutent in the more effective removal sewage (COD, nitrogen, phosphorus etc.), and need not other dosing coagulant, stop secondary pollution, significantly reduced working cost and maintenance workload.
(3) BOAF treatment unit, realized dynamically water inlet, static water outlet in the operational process, structure design by water distribution and collection clear water part, down auxiliary at center rotating operation platform, the speed of relative movement that makes the mixed solution access to plant is zero, thereby the turbulent flow in the restrain tank, guaranteed that flotation biological floe lift velocity reaches or approaching theoretical raising speed, thereby can stablize the free of contamination dissolved air flotation of carrying out by economical and efficient, greatly improve the quick-acting aspect solid-liquid separation, shortened the time of mud-water separation greatly.
(4) community closed middle water landscape water system BOAF treatment process and system and device thereof, combine biological and air flotation technology advantage, as shown in table 1, and connect with computer by magnetic flow meter, level relay, magnetic valve, controller etc., according to the water-quality guideline value that water quality monitoring system obtains, realize the automatization of operation of high-level system and water quality monitoring (WQM).
The comparison of table 1 BOAF treatment process and traditional landscape water treatment system
| Traditional biological landscape water treatment system shortcoming | Reason | Shallow pool air-floatation landscape water treatment system shortcoming | Reason |
| Floor space is big | The residence time is long, and reactor is excessive. | Can't effectively remove deliquescent organic and nitrogen and phosphorus pollutants | Simple materialization is handled, can't biodegrade. |
| There is the secondary pollution problem | The biological sludge amount is big | There is the secondary pollution problem | Realize coagulation by adding chemical agent, chemical body refuse amount is big, difficult. |
| Solid-liquid separation efficiency is lower | Mud settling of floccus speed is slow | Maintenance cost is higher | The regular replenishment chemical agent |
| BOAF treatment process characteristics | BOAF treatment process advantage | ||
| Effectively solve the secondary pollution problem | Biological scum silica frost reclaiming utilizes, control biological sludge amount. | ||
| Effectively remove organic and nitrogen and phosphorus pollutants | The biological reflection of aerobic/anaerobic enhanced biological reaction dephosphorization denitrogenation | ||
| The high-efficient separation biological flco | With BOAF air supporting is the high efficiency separation means | ||
| Operation and maintenance cost is lower | With the throwing out substituted chemistry flocculation agent of biological floe, it is additional to need not the later stage | ||
The present invention will be further described below in conjunction with drawings and Examples.
Description of drawings
Accompanying drawing 1 is a BOAF treatment unit section of structure;
Accompanying drawing 2 is a BOAF treatment unit structure vertical view;
Accompanying drawing 3 is the local A-A sectional view of BOAF treatment unit;
Accompanying drawing 4 is community closed middle water landscape water system BOAF treatment process and system and device thereof.
1. water inlet pipe, 2. rising pipe, 3. scum silica frost scum pipe, 4. return line, 5. pool bottom sludge delivery pipe, 6. pool bottom sludge scraper plate, 7. honeycomb screen, 8. water inlet water distributing pipe, 9. shroud catchments, 10. rotating operation platform, 11. dissolved air water water distributing pipe, 12. rotatable center sleeve, 13. spiral scum silica frost slag scraper, 14. clear water header, 15. air dissolved pump, 16. peripheral drive device, 17. bucket, 18. rotation waterpower joint, 19. subregion dividing plate, 20. flow deflector, 21. dissolved air water range pipe, 22.BOAF current stabilization zone of action, pond, 23.BOAF disengaging zone, pond, 24 intake pumps, 25. scum silica frost mixing zone, 26. catalytic oxidation district, 27.BOAF pool device, 28. roots blower, 29. go out water pump, 30. uv steriliser, 31. middle water landscape water body.
Embodiment
Technical scheme of the present invention is a kind of combine community closed middle water landscape water system treatment process and device biological and the air flotation technology advantage, be divided into two functional zone in the BOAF pond: current stabilization zone of action 22 and disengaging zone 23, separated by subregion dividing plate 19, its ratio is 1: 8, is opened by the complete lattice of dividing plate.The belt current stabilization zone that wherein constitutes by honeycomb screen 7 in the current stabilization zone of action.Water inlet pipe 1, rotation waterpower joint 18, the water inlet water distributing pipe 8 of the mixed solution of former water and active bio flco in rotatable center sleeve 12 evenly allocated bottom, current stabilization zone of action into.Simultaneously, the dissolved air water that is produced by air dissolved pump 15 enters bottom, current stabilization zone of action through dissolved air water distribution main 11, dissolved air water range pipe 21 synchronously with mixed solution, and producing a large amount of diameters after discharging is the micro-bubble of 10 μ m.Under the current stabilization effect of honeycomb screen 7, these micro-bubbles contact with the mixed solution thorough mixing in the metastable current stabilization of water body zone of action, and the come-up of the biological floe in the absorption mixed solution, separate to the disengaging zone along flow deflector 20 overflows rapidly along the flow deflector direction after the residence time through 15～25s, wherein flow deflector is positioned at 10cm under the horizontal liquid level, is 45.In the disengaging zone, the micro-bubble with certain buoyancy continues come-up, and behind 2～3min disengaging time, all biological floe come-ups are to the surface, disengaging zone.The active bio flco layer that the surface, disengaging zone forms is collected by spiral scum silica frost slag scraper 13, flow to scum silica frost mixing zone 25 certainly through scum silica frost scum pipe 3 then.Water outlet major part after dissolved air flotation clarification collect by clear water header 14 after rising pipe 2 and by go out water pump 29 pumps through uv steriliser 30 sterilization back re-injections in middle water landscape water body 31, the water after all the other small portions are clarified is back to air dissolved pump 15 through return line 4 and is used to provide dissolved air water.
The BOAF device is a peripheral drive, driven by the peripheral drive device 16 that is fixed on the rotating operation platform 10, the rotating operation platform 10 through driving drives parts rotations such as rotatable center sleeve 12, water inlet water distributing pipe 8, honeycomb screen 7, dissolved air water distribution main 11, dissolved air water range pipe 21, spiral scum silica frost slag scraper 13, pool bottom sludge scraper plate 6, clear water header 14.Because the velocity of rotation size of rotating operation platform 10 equals the speed that mixed solution flows into the contact reacts district, direction is just in time opposite, and Inlet and outlet water carries out synchronously, so the speed of relative movement of water inlet mixed solution the BOAF pond in and water outlet is zero.In addition, the heavy mud at the bottom of the pond and on the pool wall is scraped in the bucket 17, regularly by 5 dischargings of pool bottom sludge delivery pipe by the pool bottom sludge scraper plate 6 of rotating operation platform 10 interlocks.Honeycomb screen 7 is for being fixed on the concentric tapered plate on the rotating operation platform 10, with the rotation synchronously of water distribution part, every simultaneously adjacent two conical plates are formed the belt air supporting of an inclination, make the water in this belt air supporting zone be in laminar flow regime always, quickened the lift velocity of granule foreign like this with micro-bubble.The shroud 9 that catchments is arranged at clear water header 14 tops, guarantees the hydraulics of water outlet.
Its technical process as shown in Figure 4.Former water in the middle water landscape water body 31 sinks the biological reaction tank of being made up of scum silica frost mixing zone 25, catalytic oxidation district 26 through intake pump 24 pumps, and wherein the air in catalytic oxidation district 26 is provided by roots blower 28.Muddy water mixed solution after catalytic oxidation district 26 stops certain hour flows in the BOAF pool device 27 through water inlet pipe 1, the dissolved air water that BOAF pool device 27 provides by air dissolved pump 15 is realized separating of system's water outlet and active bio flco, the scum silica frost of its generation is back to the scum silica frost mixing zone 25 of biological reaction tank, most of water outlet behind its separating clarifying is by going out water pump 29 pumps through uv steriliser 30, in the water landscape water body 31, the small portion water outlet is used to provide dissolved air water by air dissolved pump 15 in being recycled into after the sterilization.
The biological reaction tank in scum silica frost mixing zone 25 and catalytic oxidation district 26 common formations.Scum silica frost mixing zone 25 is the amphimicrobian environment, its DO remains on below the 0.2mg/L, hydraulic detention time is about 15min, the mud scum silica frost that former water and BOAF pool device are refluxed carries out thorough mixing, amphimicrobian environment provides denitrifying condition for the nitrogen-containing pollutant in the former water, for its further aerobic removal pollutent in catalytic oxidation district 26 is given security.Catalytic oxidation district 26 is an aerobic environment, its DO remains on 3～4mg/L, hydraulic detention time is about 45min, make former water and the abundant contact reacts of active sludge dross mixture after the anaerobism contact, utilize the metabolism of active sludge microorganism, further remove organic pollutant and nitrogen and phosphorus pollutants in the polluted raw.
Water landscape water system BOAF treatment system in community closed, can pass through magnetic flow meter, level relay, magnetic valve, controller etc. connects with computer, according to the water-quality guideline value that water quality monitoring system obtains, realize the automatization of operation of high-level system and water quality monitoring (WQM).
Adopt method of the present invention and system and device thereof effluent quality after treatment can reach landscape water quality standard (GB/T18921-2002).The present invention can be widely used in the water treatment and the recycle of community closed view water system.
Claims (4)
1. medium water landscape water system organism gas float BOAG treatment method in community closed is characterized in that: the former water in the landscape water body is sinked the scum silica frost mixing zone of biological reaction tank earlier by intake pump, and former water enters the catalytic oxidation district after the scum silica frost with the backflow of BOAF pond mixes; The air in catalytic oxidation district is provided by roots blower.The muddy water mixed solution in catalytic oxidation district flows in the BOAF pool device through water inlet pipe, the dissolved air water that the BOAF pool device provides by air dissolved pump is realized separating of system's water outlet and active bio flco, the scum silica frost of its generation is back to the scum silica frost mixing zone of biological reaction tank after handle in the BOAF pond, proceeds biological respinse with the former water in the landscape water body; Most of water outlet behind its separating clarifying is recycled into middle water landscape water system by going out water pump after the uv steriliser sterilization, and the small portion water outlet is used to provide dissolved air water by air dissolved pump.
2. community closed middle medium water landscape water system organism gas float BOAG treatment method according to claim 1, it is characterized in that: the scum silica frost mixing zone is the amphimicrobian environment, and its dissolved oxygen (DO) remains on below the 0.2mg/L, and hydraulic detention time is about 15min; The catalytic oxidation district is an aerobic environment, and its DO remains on 3～4mg/L, and hydraulic detention time is about 45min.
3. medium water landscape water system organism gas float BOAG treatment unit in community closed, it comprises a BOAF pond, it is characterized in that: be divided into two functional zone in the BOAF pond: current stabilization zone of action and disengaging zone, its ratio are 1: 8, are separated fully by the subregion dividing plate.
4. community closed middle medium water landscape water system organism gas float BOAG treatment unit according to claim 3 is characterized in that:
1) current stabilization zone of action: a rotating operation platform is arranged on the BOAF pond, and the rotating operation platform is crossed on the current stabilization zone of action, is connected with the subregion dividing plate, is driven by the peripheral drive device on the rim track of being located at flotation cell; A subregion dividing plate wherein opposite, water overflow direction with sense of rotation, and an opening is arranged between the rotating operation platform, several honeycomb screens are the concentric tapered plate, be fixed on the rotating operation platform, water inlet pipe is connected by rotation waterpower joint with rotatable center sleeve, into water water distributing pipe and dissolved air water distribution main are arranged in the rotatable center sleeve, and water inlet water distributing pipe uniform distribution stretches into bottom, current stabilization zone of action; The dissolved air water distribution main is divided into several dissolved air water range pipes after stretching into bottom, current stabilization zone of action, is uniformly distributed in bottom, current stabilization zone of action; The other end of water inlet pipe is connected with biological reaction tank, and dissolved air water house steward's the other end is connected with air dissolved pump.
2) disengaging zone: include the scum silica frost collection bucket, clear water water collector and bucket; The scum silica frost collection bucket below the rotating operation platform, the front portion of water distribution system, form by two flow deflector and spiral scum silica frost slag scrapers at an angle, the scum silica frost comb is arranged at scum silica frost collection bucket bottom, the scum silica frost comb is connected with the scum silica frost mixing zone by pipeline; The clear water water collector is made up of several clear water headers, is covered by the shroud that catchments, and the water side is connected with rising pipe and return line; Rising pipe is connected with the view water system, and return line is connected with air dissolved pump; Bucket is positioned at the bottom, pond, with the mud discharging pipe coupling.The pool bottom sludge scraper plate is fixed on the bottom of pond body rotational structure, is controlled by the rotating operation platform.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100288194A CN100572292C (en) | 2006-07-11 | 2006-07-11 | Medium water landscape water system organism gas float BOAG treatment method and device in community closed |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100288194A CN100572292C (en) | 2006-07-11 | 2006-07-11 | Medium water landscape water system organism gas float BOAG treatment method and device in community closed |
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| Publication Number | Publication Date |
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| CN101104534A true CN101104534A (en) | 2008-01-16 |
| CN100572292C CN100572292C (en) | 2009-12-23 |
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| CNB2006100288194A Expired - Fee Related CN100572292C (en) | 2006-07-11 | 2006-07-11 | Medium water landscape water system organism gas float BOAG treatment method and device in community closed |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102491519A (en) * | 2011-12-26 | 2012-06-13 | 重庆大学 | Water pollution control method for landscape |
| CN102815823A (en) * | 2012-08-28 | 2012-12-12 | 宜兴市金德环保设备有限公司 | Air-flotation and oxidation machine |
| CN103991950A (en) * | 2014-05-30 | 2014-08-20 | 上海理工大学 | Biological air flotation-based reclaimed water landscape water system treatment method and device |
| CN108033614A (en) * | 2017-12-29 | 2018-05-15 | 成都大东科技有限公司 | A kind of sewage disposal device |
| CN108483813A (en) * | 2018-04-25 | 2018-09-04 | 四川农业大学 | A kind of Landscape utilizes device with environment-friendly type water multiple stage circulation |
-
2006
- 2006-07-11 CN CNB2006100288194A patent/CN100572292C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102491519A (en) * | 2011-12-26 | 2012-06-13 | 重庆大学 | Water pollution control method for landscape |
| CN102491519B (en) * | 2011-12-26 | 2013-06-19 | 重庆大学 | Water pollution control method for landscape |
| CN102815823A (en) * | 2012-08-28 | 2012-12-12 | 宜兴市金德环保设备有限公司 | Air-flotation and oxidation machine |
| CN103991950A (en) * | 2014-05-30 | 2014-08-20 | 上海理工大学 | Biological air flotation-based reclaimed water landscape water system treatment method and device |
| CN108033614A (en) * | 2017-12-29 | 2018-05-15 | 成都大东科技有限公司 | A kind of sewage disposal device |
| CN108483813A (en) * | 2018-04-25 | 2018-09-04 | 四川农业大学 | A kind of Landscape utilizes device with environment-friendly type water multiple stage circulation |
Also Published As
| Publication number | Publication date |
|---|---|
| CN100572292C (en) | 2009-12-23 |
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