CN201914974U - Dual-circular groove membrane bioreactor (MBR) waste water treatment system - Google Patents
Dual-circular groove membrane bioreactor (MBR) waste water treatment system Download PDFInfo
- Publication number
- CN201914974U CN201914974U CN201020685005XU CN201020685005U CN201914974U CN 201914974 U CN201914974 U CN 201914974U CN 201020685005X U CN201020685005X U CN 201020685005XU CN 201020685005 U CN201020685005 U CN 201020685005U CN 201914974 U CN201914974 U CN 201914974U
- Authority
- CN
- China
- Prior art keywords
- channel
- water treatment
- mbr
- membrane bioreactor
- waste water
- 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 - Lifetime
Links
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model relates to a dual-circular groove membrane bioreactor (MBR) waste water treatment system, which comprises a water inlet pipe, a water outlet pipe and a water treatment area which is provided with a membrane bioreactor (MBR), wherein the water treatment area comprises an outer groove channel and an inner groove channel which are partitioned by a pool wall; the membrane bioreactor is arranged in the inner groove channel; overflow weirs are arranged in the pool walls of the inner and outer groove channels; a flow pusher, a reflux hole and an aeration rotation disc are also arranged in the system; and the center of the inner groove channel is provided with a central island. In the utility model, an oxidation ditch and the membrane bioreactor are skillfully combined by the system, and the sludge concentration in grooves is effectively improved through controlling the reflux ratio and the hydraulic retention time, and simultaneously, the concerted reaction of oxidation, nitrification, denitrification and short-cut denitrification is promoted to happen; by utilizing the synergistic action of air backflushing and biochemical oxygen supply, the use ratio of oxygen in the treatment is improved, the process running energy consumption is effectively reduced, the requirement on the carbon nitrogen ratio is lowered and the nitrogen removal efficiency is improved.
Description
[technical field]
The utility model belongs to wastewater processing technology.More specifically, the utility model relates to a kind of dicyclo ditch shape Waste Water Treatment of collaborative use MBR membrane bioreactor.
[background technology]
The body eutrophication phenomenon is serious, a global day by day water environmental problems, its major cause is exactly that the water body that is rich in nutritive substances such as nitrogen, phosphorus enters in river or the lake, make algae and other waterplant hypertrophy in the water, thereby oxygen in water concentration is fallen sharply and cause the mass mortality of hydrocoles such as fish, finally make water body stench Heisui River that becomes, the havoc ecotope, even can damage human health safety.In order effectively to contain body eutrophication, domestic effluent-disposal standard improves gradually, and is particularly quite strict in the control of nitrogen and phosphorus.Traditional technology is difficulty up to standard on the index of water outlet TN, TP, and the enforcement of new standard must cause that newly-built sewage work is to the demand of novel process and the technology upgrading needs of old sewage work.
Existing denitrogenation of waste water dephosphorization equipment is widely used in China municipal sewage plant.But also exist simultaneously phosphor-removing effect poor, defectives such as the two-stage precipitation floor space is bigger need be set independently, wherein, when the denitrification in the settling tank takes place thoroughly, can make second pond that denitrification also takes place, cause sludge settling property variation in the waste water, it is muddy that water outlet becomes, and haves much room for improvement.
Membrane bioreactor (MBR) is a kind of novel wastewater treatment and reuse technology that membrane separation technique is combined with biological treatment.MBR can replace the second pond in the conventional activated sludge process, can realize that sludge retention time separates with hydraulic detention time, have nitrated, the denitrifying bacterium that floor space is little, sludge concentration is high, the processing volume load is high, effluent quality is good, be beneficial to length generation time and breed, easily be automated advantages such as control.Based on above advantage, the MBR technology has all obtained widespread use at home and abroad, becomes the new developing direction of municipal sewage treatment, for the sewage recycling utilization provides more economically viable space.
[utility model content]
" technical problem that will solve "
The purpose of this utility model provides the dicyclo ditch MBR Waste Water Treatment that can work in coordination with use MBR membrane bioreactor that a kind of effectiveness is higher, the processing volume load is higher, floor space is littler.
" technical scheme "
In order to realize the purpose of this utility model, the utility model provides a kind of dicyclo ditch MBR Waste Water Treatment, described system comprises water inlet pipe 1, rising pipe 9 and is provided with the water treatment zone of MBR membrane bioreactor 6, wherein, described water treatment zone comprises outer channel 2 and the interior channel 3 that is separated by pool wall, described water inlet pipe 1 communicates with outer channel 2, and described rising pipe 1 communicates with interior channel 3; In the channel 3, have overflow weir 8 in the pool wall outside described between channel 2 and the interior channel 3 in described MBR membrane bioreactor 6 is located at, also be provided with many group impellers 4 and refluxing opening on the pool wall outside described between channel 2 and the interior channel 3 symmetrically; Outside described, be provided with aeration device 5 in the channel; Channel central authorities are provided with central island 7 in described.
After waste water entered described outer channel 2 by described water inlet pipe 1, channel 2 flowed outside the promotion lower edge of described aeration device 5, channel 3 in entering by described overflow weir 8; Part mud in interior channel 3 and waste water by described impeller and refluxing opening be back to described outside in the channel, part waste water is discharged by described rising pipe.
According to site condition and treatment scale, the outer channel of dicyclo ditch MBR Waste Water Treatment of the present utility model and the shape of interior channel can be concentric circles, or concentric two ends are semicircle, the middle ellipse of straight way that is.Therefore, the central island that is positioned at channel central authorities can be set to circle or ellipse accordingly.The selection of these shapes all has guide functions, is beneficial to inside and outside channel and forms circulation.
Because in the channel, the requirement that therefore interior channel should satisfy the film flushing was provided with aerator in the MBR membrane bioreactor was located at.In order to increase aeration rate, can also be at a spot of aeration tube of septal fossula channel bottom uniform distribution, and be furnished with the regulated valve that can regulate aeration rate.The routine techniques that the term wastewater treatment industry is set of aerator belongs to those skilled in the art's the knowledge that must grasp, so repeats no more in the utility model.
According to a kind of preferred embodiment of the utility model, for described outer channel and interior channel is that concentric two ends are the oval-shaped situation of straight way for semicircle, centre, in this treatment system, described impeller and refluxing opening are arranged on the straight way pool wall.More preferably, described aeration device also is arranged in the straight way of outer channel.
The effect of impeller and refluxing opening is that the mud mixture in the interior channel is back to outer channel, further mixes with pending water in the outer channel.Therefore impeller and refluxing opening all are located on the pool wall between the inside and outside channel, and wherein, the type of impeller is axial flow thruster under water.Generally speaking, impeller should not be less than two groups, and should be symmetrically distributed.More preferably, the impeller installation site should be in the straight way zone, upstream of changeing the butterfly group.
According to a kind of in addition preferred embodiment of the utility model, described aeration device is arranged on 230mm-400mm place under water.
In the utility model, the described waste water hydraulic detention time in the channel outside is the 65-75% of total hrt, and total hrt is generally 8-15h.
(Hydraulic Retention Time HRT) should be understood to pending waste water at intrasystem mean residence time of the present utility model to term " hydraulic detention time ", just the average reaction time of microbial process in waste water and the system.
According to a kind of preferred embodiment of the present utility model, described interior channel arrives the control of reflux ratio of outer channel at 100%-400%.
In the utility model, term " reflux ratio " is meant by interior channel and is back to the water yield of outer channel and the ratio of outer channel flooding quantity.
" beneficial effect "
Dicyclo ditch MBR Waste Water Treatment of the present utility model is with oxidation ditch and the ingenious combination of membrane bioreactor, and by control to reflux ratio and hydraulic detention time, effectively improved sludge concentration in the ditch, impel the generation of the concerted reaction of oxidation, nitrated, denitrification and short-cut denitrification simultaneously, utilize the synergy of air recoil and biochemical oxygen supply, improved the utilization ratio of oxygen in the treatment system, effectively lower the technology operation energy consumption, reduction has improved nitric efficiency to the requirement of carbon-nitrogen ratio.By test run data, additionally not using under the situation of chemical dephosphorization technology, for common town sewage, the total clearance of pollutent is: COD＞90%; BOD＞95%; SS＞99%; NH3-N＞95%; TN＞80%; TP＞70%.
[description of drawings]
Fig. 1 is a dicyclo ditch MBR Waste Water Treatment two dimensional structure synoptic diagram of the present utility model;
Fig. 2 is a dicyclo ditch MBR Waste Water Treatment cross-sectional view of the present utility model;
Wherein, 1, water inlet pipe; 2, outer channel; 3, interior channel; 4, impeller; 5, rotary aeration disc; 6, MBR membrane bioreactor; 7, central island; 8, overflow weir; 9, rising pipe; 10, intake pump; 11, gas blower; 12, go out water pump; 13 blast pipes.
[embodiment]
Following embodiment illustrates this dicyclo ditch MBR Waste Water Treatment in conjunction with the accompanying drawings without limitation.Those skilled in the art are under the situation that does not break away from spirit and scope of the present utility model; can also make variations and modifications to dicyclo ditch MBR Waste Water Treatment of the present utility model; but all equivalent technical schemes all belong to category of the present utility model, and the utility model protection domain is limited by claims.
Embodiment 1
One cover dicyclo ditch MBR Waste Water Treatment, as shown in Figure 1, 2, comprise water inlet pipe 1 (intake pump 12 is housed), rising pipe 9 and be provided with the water treatment zone of MBR membrane bioreactor 6 on pipeline, described water treatment zone comprises outer channel 2 and the interior channel 3 that is separated by pool wall, described water inlet pipe 1 communicates with outer channel 2, and described rising pipe 1 communicates with interior channel 3; In the channel 3, this MBR membrane bioreactor 6 was equipped with aerating apparatus in described MBR membrane bioreactor 6 was located at.Pool wall top outside described between channel 2 and the interior channel 3 has overflow weir 8, and is provided with 4 groups of impellers 4 and refluxing opening symmetrically; The straight way place of channel is provided with 4 groups of aeration devices 5 outside described; Channel central authorities are provided with central island 7 in described.The blast pipe 13 that also is provided with gas blower 11 and is attached thereto on rising pipe 9 is used for air is fed interior channel 3.
Wherein:
1, aeration device
Across raceway groove the aeration device group is installed in the channel 2 outside, installs 4 groups altogether in the straight way end symmetrically.
Changeing the butterfly diameter is 1.4m, specified speed 52rpm, the about 230mm of submergence depth of water place, its oxygen-supplying amount 0.94kg/h, dynamic efficiency 1.89kg O
2/ h, power of agitator reaches 0.5Kw, but the about 250m of plug-flow volume
3, promptly the unit power of agitator is by being not less than 2W/m
3Check.
Change butterfly group drive-motor and be furnished with the frequency-adjustable speed-adjustable device, speed adjustable range 35-52rpm.
Change butterfly group top and also establish splash guard, enough ventilation space are arranged between the splash guard and the water surface.Change butterfly group upstream and downstream and all do not establish flow deflector under water.
2, overflow weir
3, impeller
The impeller 4 of present embodiment is axial flow thruster under water, in the installation through walls of the end of direct current pool wall, with the mixed solution plug-flow of interior channel 3 to outer channel 2.
The installation direction of impeller 4 becomes miter angle with middle pool wall (tangent line), and the plug-flow component of formation is consistent with outer fissure flow velocity direction.The mounting height of impeller is that interior channel 3 waters surface are following, 1/2 place of the depth of water.
Impeller 4 is installed two groups altogether, also is symmetrical distribution, is installed in the upstream of aeration device 5.
The lift of impeller 4 is 200mm-500mm (maximum stage of considering outer fissure and septal fossula is poor), and the total plug-flow amount of impeller (being in the unit time, the ratio of the flooding quantity that impeller can be operated and the flooding quantity of outer channel) is 100-400%.Impeller is furnished with the frequency-adjustable speed-adjustable device.Impeller also is furnished with guide rail chain type lifting gear.
4, MBR membrane bioreactor assembly
The direct current zone of channel 3 in membrane module is installed in, uniform distribution.The water outlet of this MBR membrane bioreactor assembly is furnished with flow rate control device, and is basicly stable to keep the septal fossula water level.
Below membrane module, the uniform aeration tube in interior channel 3 bottoms, and be furnished with regulated valve, can regulate aeration rate, be used to adapt to the requirement of membrane module flushing
Concrete operation scheme of the present utility model is:
With treatment sewage through advance intake pump 10 send into outside channel 2, impeller 4 is sent the mud of interior channel 3 and the mixture backflow of water into outer channel 2 simultaneously, under the plug-flow effect of aeration device 5, the mixed solution of outer channel 2 mixes the back with the mud mixed liquid that refluxes from interior channel 3 and flows along annular outer fissure 2.
The hydraulic detention time of outer channel 2 is 70% of a total hrt, is in double oxygen condition.The clearance of 2 pairs of principal pollutant of outer channel is about 80% of total clearance, and wherein TN all removes in the channel 2 outside.
By this set outside in the channel 2, the same time is realized carbonization, ammonification, nitrated, denitrification, anoxic and aerobic comprehensive biochemical reactions such as poly-phosphorus.
By this set outside in the channel 2, the same time all is formed with aerobic, the anaerobic environment of certain gradient in level and vertical direction, comprises the microenvironment of microorganism flco inside.
Different with traditional theory and engineering design, outer channel 2 is as the main body structures of this technology, the not aerobic workshop section in zoning place, anoxic workshop section or operating mode on space or sequential, overwhelming majority pollutant removal is realized in outer fissure 2 simultaneously, and losing oxygen and finishing biochemical reaction under the admixture fully, reach higher removal, save energy consumption and reduction demand carbon source.
Outer channel 2 adopts oxidation ditch ditch type, has embodied complete blended hydromechanics advantage.Homogeneous media, sufficient reacting, strong shock resistance.In addition, change butterfly aeration 5 and possess good oxygen supply and plug-flow effect, stirring efficiency is higher, for complete hybrid reaction has been created condition.In addition, owing to follow-up aerobic workshop section arranged, avoided mixing fully to produce the quality problem that the short stream of water inlet brings.
Outer channel 2 is oxygen-supplying amount and oxygen-consumption balance generally, but oxygen supply intensity is distinguished to some extent.Change the butterfly aeration and have the characteristics of " pulse " oxygen supply, by changeing the moment of butterfly, aeration intensity is high at mixed solution, causes oxidation and nitrated generation simultaneously, and especially nitrification is obvious, far surpasses the bottom micro-pore aeration.
After changeing butterfly, dissolved oxygen consumes rapidly, and most of space is oxygen and the anoxic condition held concurrently, and former in addition water directly enters outer channel 2, farthest provides denitrification required carbon source, and denitrification effect is better.In addition, under interior channel 3 backflow effects, nitric efficiency can further provide.
Mud backflow and nitrate internal reflux are integrated to be the characteristics of system of the present utility model, the sludge concentration of interior channel 3 is the highest, and the nitrate that contains further nitrated formation, and outer channel 2 has the comprehensive function of oxidation, nitrification and denitrification, once backflow from interior channel 3 to outer channel 2 can satisfy that mud refluxes and the double requirements of nitrification liquid internal reflux.
Another effect that refluxes is that the outside channel 2 of the dissolved oxygen of interior channel 3 is shifted, and can reduce the oxygen supply energy consumption of outer channel 2.Utilize the oxygen supply of the additional aerobic section of dissolved oxygen of membrane cisterna, usually also be the method that other technology (as A2O) is taked, but the utlity model has three characteristics: 1. outer channel 2 is the high efficient mixed fluidised form, and the utilization ratio of backflow dissolved oxygen is better than other pulling flow type technology; 2. outer channel 2 main oxygen supply modes are surperficial mechanical aeration, and the backflow source of dissolved oxygen is in the bottom aeration, and different aeration modes can produce complementary effect preferably; 3. outer channel 2 totally is in oxygen condition thanks to, and the backflow dissolved oxygen is had the higher rate of transform.
Channel 3 in the mobile mixed solutions enter through overflow weirs 8 in the channel 2 outside, the hammer that interior channel 3 is used film is swept air, forms stronger aerobic environment, further to oxidation operation, and reinforcement nitrated to ammonia nitrogen.Simultaneously, by membrane filtration, further remove phosphorus and suspended substance, play the effluent quality effect of checking on, leading indicator reaches surface water 4 class standards.
Interior channel both as the membrane cisterna of Waste Water Treatment, also as the aerobic biochemical pond, can farthest improve the utilization ratio of oxygen with the air backwash and the biochemical efficient combination of oxygen supply of membrane module, lowered the energy consumption of membrane bioreactor from system-wide aspect.
The impeller under water that interior channel is provided with, with middle pool wall in angle of 45 degrees, existing backflow functionality also has the plug-flow and the stirring action of pair outer fissure.Simultaneously, impeller also makes septal fossula form circulation in the suction function of septal fossula, has mixed effect, helps the uniform distribution of film aeration dissolved oxygen.
The required sludge concentration of membrane bioreactor is higher, helps coming off of the outer sludge blanket of film.For biochemical process, improve sludge concentration, not only can reduce the pond and hold, reduce discharging mud, can also roll up the oxygen animalcule total amount of holding concurrently in the outer fissure, utilize its meta-bolites, for denitrogenation provides extra carbon source.
Significant parameter of the present utility model requires as follows:
Total hrt: 8-16h;
The outer fissure residence time accounts for the ratio of total residence time: 65%-70%;
Available depth: 3.8-4.2m;
Outer fissure sludge concentration: 7-9g/l;
Septal fossula (membrane cisterna) sludge concentration: 8g-10g/l;
Outer fissure dissolved oxygen (DO): 2m is 0mg/l after changeing butterfly;
Outer fissure redox potential (ORP) overwhelming majority is-30mv-+30mv
Septal fossula dissolved oxygen (DO): 1.5-4.0mg/l;
Septal fossula is to outer fissure reflux ratio: 100%-400%;
Membrane flux: 15-25l/m
2H;
Septal fossula (membrane cisterna) gas-water ratio (on average) 1: 15-1: 30.
Trial run
Go in in a big way in the sewage disposal of yellow village, influent quality is: CODcr content is 300-500mg/L, and total nitrogen content is 50-70mg/L, and total phosphorous is 5-8mg/L, and interior channel to outer channel reflux ratio is 300%.
Outer channel sludge concentration: 8.5g/l; Interior channel (membrane cisterna) sludge concentration: 9.5g/l; Total hrt: 14h.
Additionally do not using under the situation of chemical dephosphorization technology, final outflow water CODcr is less than 30mg/L, and total nitrogen is less than 8mg/L, and total phosphorus is less than 0.5mg/L.
Claims (5)
1. dicyclo ditch MBR Waste Water Treatment, described system comprises water inlet pipe, rising pipe and is provided with the water treatment zone of MBR membrane bioreactor, it is characterized in that described water treatment zone comprises outer channel and the interior channel that is separated by pool wall, described water inlet pipe communicates with outer channel, and described rising pipe communicates with interior channel; In the channel, have overflow weir in the pool wall outside described between channel and the interior channel in described MBR membrane bioreactor is located at, also be provided with many group impellers and refluxing opening on the pool wall outside described between channel and the interior channel symmetrically; Outside described, be provided with aeration device in the channel; Channel central authorities are provided with central island in described.
2. dicyclo ditch MBR Waste Water Treatment according to claim 1, the shape that it is characterized in that described outer channel and interior channel are circular, or two ends are semicircle, the middle ellipse of straight way that is.
3. dicyclo ditch MBR Waste Water Treatment according to claim 2 is characterized in that for described outer channel and interior channel be oval-shaped treatment system, and described impeller and refluxing opening are arranged on the straight way pool wall.
4. dicyclo ditch MBR Waste Water Treatment according to claim 2 is characterized in that for described outer channel and interior channel be oval-shaped treatment system, and described aeration device is arranged in the straight way of outer channel.
5. dicyclo ditch MBR Waste Water Treatment according to claim 1 is characterized in that described aeration device is arranged on 230mm-400mm place under water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020685005XU CN201914974U (en) | 2010-12-28 | 2010-12-28 | Dual-circular groove membrane bioreactor (MBR) waste water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201020685005XU CN201914974U (en) | 2010-12-28 | 2010-12-28 | Dual-circular groove membrane bioreactor (MBR) waste water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201914974U true CN201914974U (en) | 2011-08-03 |
Family
ID=44414782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201020685005XU Expired - Lifetime CN201914974U (en) | 2010-12-28 | 2010-12-28 | Dual-circular groove membrane bioreactor (MBR) waste water treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201914974U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010062A (en) * | 2010-12-28 | 2011-04-13 | 北京碧水源科技股份有限公司 | MBR wastewater treating system with double circular grooves |
| CN102539644A (en) * | 2011-12-29 | 2012-07-04 | 河海大学 | Generator for simulating pollution release process of aquatic plants to sediments and use method |
| CN110194524A (en) * | 2019-06-10 | 2019-09-03 | 凌志环保股份有限公司 | A kind of MBR sewage treatment pot having oxidation ditch function |
| CN114195255A (en) * | 2021-11-10 | 2022-03-18 | 新余市木林森线路板有限公司 | Method for removing total nitrogen from industrial sewage with high reflux ratio |
-
2010
- 2010-12-28 CN CN201020685005XU patent/CN201914974U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010062A (en) * | 2010-12-28 | 2011-04-13 | 北京碧水源科技股份有限公司 | MBR wastewater treating system with double circular grooves |
| CN102539644A (en) * | 2011-12-29 | 2012-07-04 | 河海大学 | Generator for simulating pollution release process of aquatic plants to sediments and use method |
| CN110194524A (en) * | 2019-06-10 | 2019-09-03 | 凌志环保股份有限公司 | A kind of MBR sewage treatment pot having oxidation ditch function |
| CN114195255A (en) * | 2021-11-10 | 2022-03-18 | 新余市木林森线路板有限公司 | Method for removing total nitrogen from industrial sewage with high reflux ratio |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110776099B (en) | Self-circulation efficient biological denitrification device and working method thereof | |
| CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
| CN101269882B (en) | Integrated oxidation ditch, construction and operation method | |
| CN103880248B (en) | A kind of coking wastewater processing system and treatment process | |
| CN205803249U (en) | A kind of anaerobic/anoxic/aerobic MBR sewage-treatment plant | |
| CN105330108B (en) | Utilize anaerobism-catalytic oxidation biofilm reactor processing sanitary sewage method and processing unit | |
| CN104512963B (en) | A kind of multistage simultaneous nitrification-denitrification biofilm system denitrogenation method of integral type and device | |
| CN205258127U (en) | Circulatory flow loop type multistage sludge -biofilm intergrowth combined type bioreactor | |
| CN201325908Y (en) | Improved sewage treatment system for oxidation ditch | |
| CN214781015U (en) | Integrated sewage treatment device with concentric structure | |
| CN102010062B (en) | MBR wastewater treating system with double circular grooves | |
| CN201914974U (en) | Dual-circular groove membrane bioreactor (MBR) waste water treatment system | |
| CN204588936U (en) | A kind of waste disposal plant of denitrogenation dephosphorizing | |
| CN210505759U (en) | Self-circulation efficient biological denitrification device | |
| CN105417871A (en) | Spiral-flow type integrated sewage treatment device provided with center return pipe | |
| CN209906446U (en) | Integrated sewage advanced treatment device based on circular tank body | |
| CN219689523U (en) | Treatment device for aged leachate of household garbage landfill | |
| CN202945124U (en) | Urban sewage treatment system with high efficiency and low energy consumption | |
| CN108996689B (en) | Solid carbon source micro-aeration device and wastewater treatment method thereof | |
| CN102050544B (en) | Treatment method for high-concentration organic wastewater and device used thereby | |
| CN214299767U (en) | Integrated sedimentation built-in deepwater aeration bioreactor | |
| CN101538085A (en) | Structure of spiral-flow aeration sedimentation sewage treatment tank and using method thereof | |
| CN110104776B (en) | Small-size sewage treatment integration equipment | |
| CN209890336U (en) | Device for enhancing gas stripping plug flow type oxidation ditch effect by using suspension carrier | |
| CN209507894U (en) | Integrated sewage treating apparatus based on tidal type biological aerated filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110803 Effective date of abandoning: 20120509 |