CN206069515U - For the bioreactor of sewage disposal - Google Patents
For the bioreactor of sewage disposal Download PDFInfo
- Publication number
- CN206069515U CN206069515U CN201621038399.3U CN201621038399U CN206069515U CN 206069515 U CN206069515 U CN 206069515U CN 201621038399 U CN201621038399 U CN 201621038399U CN 206069515 U CN206069515 U CN 206069515U
- Authority
- CN
- China
- Prior art keywords
- cavity
- chamber
- aerobic
- dividing plate
- bioreactor
- 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.)
- Active
Links
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses a kind of bioreactor for sewage disposal, its drip irrigation device is, including tank body, dividing plate is provided with tank body, dividing plate tank interior space is divided into be sequentially communicated preposition chamber, anoxic zone, the first aerobic cavity, the second aerobic cavity, precipitation chamber, preposition chamber is communicated with water inlet pipe, precipitation chamber is communicated with outlet pipe, dividing plate between first aerobic cavity and the second aerobic cavity its upper and lower ends are equipped with the throughput circulated between the first aerobic cavity and the second aerobic cavity for current, and the first aerobic intracavity is provided with aerating pipelines.In sewage disposal process, using cyclic process between two aerobic units, simple structure, degradation effect substantially, and can reduce the quantity that space is divided in whole tank body in a large number, reduce the cost of production, with the stronger market competitiveness.
Description
Technical field
This utility model is related to sewage treatment area, more particularly to a kind of bioreactor for sewage disposal.
Background technology
With the progress that vast rural toilet is transformed, the phenomenon that Excreta and sewage are arbitrarily discharged before changing is substantial amounts of
Rural toilet construction is got up, and sanitary sewage is received bank of tubes and put, in terms of the process to country sewage, substantial amounts of with small-sized in field
Change the change excrement equipment of integration so that the sewage being disposed disclosure satisfy that discharging standards directly can be discharged.
Existing notification number discloses a kind of nido synchronization AO biofilm reactors for CN205133239U's, includes annular
1 ~ 6 groove of distribution, sewage pass sequentially through 6 grooves, complete the process of water quality lifting.But which is during sewage disposal,
Current are chain type flowings successively up and down staggeredly, and current need to flow through 6 grooves and carry out water quality lifting, and the amplitude that water quality is lifted
It is consistent, adjustability is poor, and is required for laying corresponding aerating pipelines in each of which groove, so easily causes structure multiple
It is miscellaneous.
Utility model content
In view of the shortcomings of the prior art, the purpose of this utility model is to provide a kind of biology for sewage disposal
Reactor, by the first aerobic cavity, the circular response of the second aerobic cavity, optimizes oxidation reaction, simplifies overall structure.
Above-mentioned technical purpose of the present utility model technical scheme is that：It is a kind of to be used for sewage disposal
Bioreactor, including tank body is provided with dividing plate in the tank body, tank interior space is divided into and is sequentially communicated by the dividing plate
Preposition chamber, anoxic zone, the first aerobic cavity, the second aerobic cavity, precipitation chamber, preposition chamber is communicated with water inlet pipe, and precipitation chamber is communicated with
Outlet pipe, dividing plate its upper and lower ends between first aerobic cavity and the second aerobic cavity are equipped with for current in the first aerobic cavity
The throughput circulated between the second aerobic cavity, the first aerobic intracavity are provided with aerating pipelines.
By above-mentioned technical proposal, in the processing procedure to sewage, aerating pipelines are in the sewage to the first aerobic intracavity
During carrying out aeration, bubble constantly rises, and the liquid of the first aerobic intracavity can be disturbed, drive which to rise,
So, the liquid of the first aerobic intracavity just can be entered in the second aerobic zone from throughput above.First aerobic cavity
After interior fluid loss, the throughput that the liquid in the second aerobic zone also can be below the liquid runs down of some flow back into first
Aerobic intracavity.The water circulation of a stable annular can be formed between such first aerobic cavity and the second aerobic cavity, in reaction
During, substantial amounts of sewage moves in circles between the first aerobic cavity and the second aerobic cavity and is degraded, and a small amount of sewage can be from
Anoxic zone fills into, while a small amount of degraded finishes sewage because the reason for liquid level maintains an equal level in tank body is flowed into precipitation intracavity.Sewage
Sufficiently can be contacted with filler by circulation, carry out aerobic reaction, more sufficient drop is carried out to the Organic substance in sewage
Solution, improves the degradation capability of overall bioreactor.In sewage disposal process, added using circulation between two aerobic units
Work, simple structure, degradation effect substantially, and can reduce the quantity that space is divided in whole tank body in a large number, reduce production
Cost, with the stronger market competitiveness.
This utility model is further arranged to：The inner tank wall and bulkhead sides wall are provided with the card that multiple confession dividing plates are plugged together
Groove, the dividing plate is by plugging together preposition chamber or anoxic zone or the first aerobic cavity or the second aerobic cavity or precipitation in different draw-in grooves
Chamber is divided into different sizes.
By above-mentioned technical proposal, dividing plate insertion slot is realized fixing, it is also possible to realize dismounting by extracting slot, and
Plate is inserted in the slot of diverse location, and dividing plate has detachability.Have without mark the water to emitting is needed
When alignment request, rate request, the height of dividing plate, position etc. can be adjusted, allow preposition chamber, anoxic zone, first good
Oxygen chamber, the second aerobic cavity, precipitation chamber etc. form different ratios, and the time of staying that can be to sewage in different regions meets
Corresponding standard, improves the internal adjustable of whole reactor, increases the range of application of reactor.
This utility model is further arranged to：It is the preposition chamber and anoxic zone, anoxic zone and the first aerobic cavity, second aerobic
The baffle pipe for connecting is equipped between chamber and precipitation chamber, one end of baffle pipe is located at the bottom of previous cavity, baffle pipe
The other end is through the top of dividing plate.
By above-mentioned technical proposal, the structure of baffle pipe between cavity and cavity, is increased, if had in previous cavity
New liquid is filled into into, and the liquid level in previous cavity can be raised, and thus above a cavity can be with latter one cavity
Formation liquid level is poor, and the bottom liquid in previous cavity will be from the baffle pipe nozzle position stream positioned at bottom to next cavity
Interior surface location, the just directly staggeredly flowing of the liquid between such chamber and chamber, it is to avoid sludge occur within each cavity residual
Situation about staying, eliminates and draws the loaded down with trivial details of mud in the future.
This utility model is further arranged to：First aerobic cavity and the second aerobic intracavity are provided with filler.
By above-mentioned technical proposal, filler plays the parasitic environment of an offer degrading microorganism, using filler to dirt
Sewage more clean can be kept when water process, is being allowed in sewage in inorganization degradation process, the sludge in sewage is protected
A relatively low level is held, the water quality of water outlet is improved.
This utility model is further arranged to：The anoxic zone includes anaerobic cavity, the anoxia chamber being sequentially communicated, anaerobic cavity
Connect with preposition chamber, anoxia chamber is connected with the first aerobic cavity, and separated by dividing plate between anaerobic cavity and anoxia chamber.
By above-mentioned technical proposal, anoxic zone is formed into anaerobism, two cavitys of anoxia, whole bioreactor is allowed in reaction
Process use the biodegradation technique of A2/O, anaerobic cavity its major function is release phosphorus, while carrying out to partial organic substances
Ammonification, and its premiere feature of anoxia chamber is denitrogenation, is that follow-up aerobic reaction carries out place mat, improves the water quality requirement of sewage, is allowed
The sewage that the bioreactor for treatment is finished meets higher water standard.
This utility model is further arranged to：Anaerobic cavity is aerobic with first with preposition chamber, anaerobic cavity and anoxia chamber, anoxia chamber
The baffle pipe for connection is provided between chamber, one end of baffle pipe is located at the bottom of previous cavity, and the baffle pipe other end runs through
The top of dividing plate.
By above-mentioned technical proposal, after allowing sewage to flow into anaerobic cavity, liquid level goes up, and the liquid of anaerobic cavity bottom can be from
The surface in anoxia chamber is entered into using the structure of baffle pipe, the liquid of anaerobism intracavity more sufficiently can be flowed, be slow down
Occurs the situation of sludge extruding during effluent cycle in anoxic zone.
This utility model is further arranged to：Sludge reflux mechanism, the dirt are provided between the preposition chamber and precipitation chamber
Mud backflow mechanism includes mud return line, and mud return line one end insertion precipitation bottom of chamber portion, the other end are located at preposition top of chamber.
By above-mentioned technical proposal, the additional designs of mud return line can allow sludge that precipitation intracavity is deposited again
The effluent cycle entered in tank body in the middle of, on the one hand increase the handling rate to sludge in sewage disposal, reduce sludge quantity, separately
On the one hand the residual of sludge can be reduced as far as possible, it is to avoid mud is frequently taken out to the sludge in tank body subsequently.
This utility model is further arranged to：One section of upper and aerating pipelines of precipitation intracavity are located on the mud return line
Connection, and on mud return line, on peak, offer the dispelling the stagnated QI pipe discharged for inner air.
This utility model is further arranged to：The lid for opening is sealed, the lid are provided with the top of the tank body
Manhole is offered on body.
By above-mentioned technical proposal, the structure of lid realizes the sealing at the top of tank body, and the split of tank body and lid
Arrange, allow tank body convenience also more when processing, directly be injected separately out.Manhole above lid, it is convenient
People are observed to inside, it is also possible to be convenient for people to inside can be carried out taking out the operation such as sludge.
This utility model is further arranged to：The gas being provided with for supplying to aerating pipelines is installed on the lid inwall
Pump.
By above-mentioned technical proposal, the effect of air pump is that aerating pipelines are ventilated, and air pump is arranged in lid
Portion, on the one hand can simplify the structure inside bioreactor, make full use of the space of inside, on the other hand also allow air pump to be in
One relatively reasonable position, dismounting when disposably can directly take apart with lid, be easy to follow-up maintenance with
Change.
In sum, this utility model having the beneficial effect that in contrast to prior art：1st, whole structure of reactor is simple,
Split is arranged, and processing cost is low；2nd, inside reactor can form interior circulation in aerobic reaction, reduce the area of aerobic reaction
Domain quantity, improves the efficiency of aerobic reaction；3rd, reactor controllability is high, wide adaptability, and internal different cavity can pass through
Dividing plate is plugged in different positions, and then adjusts the size relation between different cavitys.
Description of the drawings
Structure charts of the Fig. 1 for embodiment one；
Fig. 2 is one internal structure schematic diagram of embodiment；
Fig. 3 is the structure chart at one baffle pipe of embodiment；
Structure charts of the Fig. 4 for embodiment two.
Reference：1st, lid；11st, manhole；2nd, tank body；21st, draw-in groove；22nd, dividing plate；221st, throughput；23rd, water inlet pipe；
24th, outlet pipe；23rd, baffle pipe；31st, preposition chamber；32nd, anoxic zone；321st, anaerobic cavity；322nd, anoxia chamber；33rd, the first aerobic cavity；
34th, the second aerobic cavity；35th, precipitate chamber；351st, downflow weir；4th, mud return line；41st, dispelling the stagnated QI pipe；5th, aerating pipelines；51st, air pump；
6th, filler.
Specific embodiment
This utility model is described in further detail below in conjunction with accompanying drawing.
Embodiment one,
As shown in figure 1, a kind of bioreactor for sewage disposal, tank body 2 and lid 1, lid 1 can buckle fix
On tank body 2, by 2 inner sealing of tank body, and lid 1 is provided with manhole 11 above, is easy to people to carrying out inside tank body 2
Safeguard, operate.Tank body 2 is internally provided with multiple dividing plates 22, and dividing plate 22 can be by 2 inside division of tank body into how big and small sky
Chamber, preposition chamber 31 which is respectively sequentially communicated in the following order, anoxic zone 32, the first aerobic cavity 33, the second aerobic cavity 34,
Precipitation chamber 35, preposition chamber 31 are connected with water inlet pipe 23 above, sewage make from stream in preposition chamber 31 come in subsequently into anoxic zone
Hypoxia response is carried out in 32, the first aerobic cavity 33 and the second aerobic cavity 34 is being sequentially entered afterwards, is being carried out in the two intracavity
Aerobic reaction in biological respinse, final sewage are flowed in precipitation chamber 35 and are clarified, and clarify the liquid for finishing from precipitation chamber
Drain through outlet pipe 24 in 35.
Wherein, separated using dividing plate 22 between the first aerobic cavity 33 and the second aerobic cavity 34, this every
The top and bottom of plate 22, is provided with interconnecting part, and the effect of interconnecting part is to allow current that dividing plate 22 both can have been flow through from above,
Dividing plate 22 is flow through from below can.Interconnecting part can be at the top of perforate, or dividing plate 22 and at the top of tank body 2 between fall
Difference, can also be the communicating pipe for connection certainly, as long as realizing that current pass through.In the present embodiment, interconnecting part be every
Drop gap at the top of plate 22 and between the sewage water surface, also the drop gap between 22 bottom of dividing plate and ground, at this every
22 relative altitude of plate is less, and current can be flow through from the top of dividing plate 22 and lower section.
Such as Fig. 1 and Fig. 2, aerating pipelines 5 are provided with the first aerobic cavity 33, aerating pipelines 5 are arranged on the first aerobic cavity
33 bottom, aerating pipelines 5 are connected with air pump 51, and air pump 51 is arranged on the inwall of lid 1, can be conveniently follow-up to air pump 51
Safeguard.Aerating pipelines 5 are provided with multiple gas outlets above, gas can constantly from above gas outlet out, increase internal containing
Oxygen amount.Meanwhile, gas can constantly stir current in the process for rising, and allow current the situation for floating, the water for floating out occur
Stream enters interconnecting part by liquid level stream and is flowed in the second aerobic cavity 34, and during current float, the second aerobic cavity 34
Interior sewage can be entered in the first aerobic cavity 33 by the interconnecting part of 22 bottom of dividing plate, and such current are in the first aerobic cavity 33
The structure of aerating pipelines 5 can just be passed through with the second aerobic cavity 34 and then the state of a water circulation is defined, it is anti-in circulation
Should during, the aerobic reaction time can be allowed more long, reaction more abundant is carried out to the Organic substance in sewage more efficient
Degraded, improve sewage effluent quality.And aerating pipelines 5 can be allowed to be simplified under this structure, only to first
In aerobic cavity 33, aeration can be realized as being circulated reaction in the first aerobic cavity 33 and the second aerobic cavity 34, it is to avoid pipeline exists
Extra lays pipeline and the complex situation of structure occurs.
It is in the first aerobic cavity 33 and the second aerobic cavity 34 and is provided with filler 6, filler 6 refers to larger surface area
Solid particle, liquid can have on 6 surface of filler and be preferably uniformly distributed, and microorganism can be bred in 6 superficial growth of filler, greatly
That what is measured grows, and in the first aerobic cavity 33 and the second aerobic cavity 34, filler 6 can allow aerobic bacteria implantation above, in sewage
Organic substance carries out quickly inorganization process.And in anoxic zone 32, filler 6 can be placed and can not also be placed, according to water
Depending on matter process needs.During use, filler 6 can also adopt floating stuffing 6 etc. using solid packing 6.
Whole tank body 2, lid 1, dividing plate 22 are all made of plastics, and the side wall that 2 inwall of tank body also has dividing plate 22 is arranged
There are multiple draw-in grooves 21, draw-in groove 21 is made with 2 integrated injection molding of tank body out, and dividing plate 22 is inserted into draw-in groove 21 when installing
The inside, carries out clamping so as to keep stable in use.The feasible degeneration of plastic construction is stronger, is inserted into card in dividing plate 22
When groove 21, the inwall of draw-in groove 21 is fitted with the outer wall of dividing plate 22, hinders current to pass through, and then can allow the dividing plate 22 can be by
Segmented state is kept between different chambers, is flowed above 22 gap of dividing plate that current will not be between different chamber, is met
Independence on each chamber.There is the structure of draw-in groove 21, dividing plate 22 can be inserted on different draw-in grooves 21, so by people
The magnitude relationship each other of the multiple cavitys in tank body 2 just has difference.Cavity of different sizes also represents, in same speed
Under the inflow of current, existence time of the current in different cavitys is just different, and so each current is corresponding in the cavity
Regulation to sewage quality is also different.People can need water quality to be processed, the speed of also corresponding water inlet to insert plate
To in the draw-in groove 21 of diverse location, whole bioreactor is adjusted.
Between preposition chamber 31 and anoxic zone 32, anoxic zone 32 and the first aerobic cavity 33, the second aerobic cavity 34 and precipitation chamber 35
All it is attached using baffle pipe 23, baffle pipe 23 is a kind of plastic bend tube of L shape, and the mounting structure of baffle pipe 23 is such as
Shown in Fig. 3,23 one end of baffle pipe is inserted into the bottom of previous cavity, and 23 other end of baffle pipe is located at latter one cavity
Top.Dividing plate 22 of the baffle pipe 23 between two cavitys, realize that baffle pipe 23 is fixed by running through.In current flowing
During, when liquid is flowed into previous cavity, the liquid level of previous cavity raises a part, produces certain liquid level
Difference, then the liquid in previous cavity can be pressed into the liquid of previous cavity bottom in next cavity.By folding
After flow tube 23, the liquid flowing between two cavitys is exactly the bottom that the bottom liquid of previous cavity is pumped to next cavity
Portion, it is to avoid the contrast of the sludge of bottom, what is flowed in keeping drainage flow are thorough, and long-time can be accomplished substantially without taking out dirt
Mud.
Such as Fig. 2, the process process of circulation of sewage are as follows：Sewage is flowed into inside tank body 2, by baffle pipe from water inlet pipe 23
23 successively stream enter preposition chamber 31, anoxic zone 32, the first aerobic cavity 33, the second aerobic cavity 34, precipitation chamber 35, then from precipitation chamber 35
Outlet pipe 24 go out.In whole tank body 2, the sewage highly of each intracavity is all consistent, and the water surface is high below or equal to dividing plate 22
Degree, how many current of coming in water inlet pipe 23, outlet pipe 24 just go out how much sewage, and whole interior circulation keeps balance.Sewage is preposition
Buffering in chamber 31, stands, and then into hypoxia response is carried out in anoxic zone 32, enters back into the first aerobic cavity 33 aerobic with second
The aerobic reaction being circulated in chamber 34, enters finally into remaining a small amount of sludgd deposition in sedimentation tank in sedimentation tank bottom,
The water on top layer is discharged from outlet pipe 24.And a downflow weir 351 is provided with sedimentation tank, downflow weir 351 and outlet pipe 24
Connection, highest top surface and the water surface in whole tank body 2 of downflow weir 351 are consistent, and the current in sedimentation tank are crossed excessive
Substantial amounts of sludge can be blocked in sedimentation tank when stream 351 peak of weir, sludge in reduction water outlet to the full extent
Content.
Meanwhile, it is also extra between precipitation chamber 35 and preposition chamber 31 to be provided with sludge reflux mechanism, sludge reflux mechanism
Be for by the sludge of the residual in precipitation chamber 35 to releasing again so as to be back in preposition chamber 31, can allow sludge weight
The new drainage flow entered in tank body 2 is further thoroughly degraded.
Sludge reflux mechanism includes mud return line 4, and 4 one end of mud return line insertion precipitation 35 bottom of chamber, the other end are inserted
Enter at the top of preposition chamber 31, meanwhile, position of the mud return line 4 in precipitation chamber 35 is in vertical shape, is had with aerating pipelines 5 above
One connectivity points, connectivity points position is about in 1/3 position of vertical height.And the peak of whole mud return line 4 is less than
The liquid level of current is flush with it, and so, mud return line 4 is just in a water-filling state all the time, and aerating pipelines 5 are continuous
Inflation in past mud return line 4, constantly rising further can drive the liquid in mud return line 4 toward in preposition chamber 31 to air-flow
Flowing, as mud return line 4 is inserted into precipitation 35 bottom of chamber, is preferably inserted into apart from the position of ground 10cm or so, sludge
Return duct 4 can drive the sludge of bottom to flow back in preposition chamber 31.One is opened up on the peak of mud return line 4 simultaneously
Individual dispelling the stagnated QI pipe 41, air-flow are directly walked from the release of dispelling the stagnated QI pipe 41 after rising to peak, prevent substantial amounts of air-flow from entering into preposition
In chamber 31, anaerobic reaction in anoxic zone 32 is had influence on.
Embodiment two,
As shown in figure 4, a kind of bioreactor for sewage disposal, embodiment two with the difference of embodiment one is,
Anoxic zone 32 is divided into anaerobic cavity 321 and anoxia chamber 322 by one dividing plate 22 of the setting in anoxic zone 32.Anaerobic cavity 321 with it is front
Put chamber 31 to connect, and the connection anaerobic cavity 321 of anoxia chamber 322 and the first aerobic cavity 33.Increasing an anaerobic cavity 321 more can have
The discharging the phosphorus inside sewage of effect, while carrying out ammonification to partial organic substances, is easy to subsequently more add in aerobic reaction
The dephosphorization of one step.And current flowing between anaerobic cavity 321 and anoxia chamber 322 and by baffle pipe 23, is guided, allow
The liquid of 321 inner bottom part of anaerobic cavity is flowed in anoxia chamber 322.
The above is only exemplary embodiment of the present utility model, not for restriction protection model of the present utility model
Enclose, protection domain of the present utility model is determined by appended claim.
Claims (10)
1. a kind of bioreactor for sewage disposal, including tank body (2), is characterized in that：Dividing plate is provided with the tank body (2)
(22), the dividing plate (22) tank body (2) inner space is divided into be sequentially communicated preposition chamber (31), anoxic zone (32), first
Aerobic cavity (33), the second aerobic cavity (34), precipitation chamber (35), preposition chamber (31) are communicated with water inlet pipe (23), and precipitation chamber (35) is even
Outlet pipe (24) is connected with, dividing plate (22) its upper and lower ends between first aerobic cavity (33) and the second aerobic cavity (34) are all provided with
There are the throughput (221) circulated between the first aerobic cavity (33) and the second aerobic cavity (34) for current, first aerobic cavity
(33) aerating pipelines (5) are provided with.
2. the bioreactor for sewage disposal according to claim 1, is characterized in that：Tank body (2) inwall and
Dividing plate (22) side wall is provided with the draw-in groove (21) that multiple confession dividing plates (22) plug together, and the dividing plate (22) is by plugging together in different draw-in grooves
(21) by preposition chamber (31) or anoxic zone (32) or the first aerobic cavity (33) or the second aerobic cavity (34) or precipitation chamber (35) point in
It is cut into different sizes.
3. the bioreactor for sewage disposal according to claim 1, is characterized in that：The preposition chamber (31) with lack
It is equipped with for connecting between oxygen area (32), anoxic zone and the first aerobic cavity (33), the second aerobic cavity (34) and precipitation chamber (35)
Baffle pipe (23), one end of baffle pipe (23) is located at the bottom of previous cavity, and baffle pipe (23) other end runs through dividing plate
(22) top.
4. the bioreactor for sewage disposal according to claim 1, is characterized in that：First aerobic cavity (33)
Filler (6) is provided with the second aerobic cavity (34).
5. the bioreactor for sewage disposal according to claim 1, is characterized in that：The anoxic zone (32) includes
Have anaerobic cavity (321), anoxia chamber (322) being sequentially communicated, anaerobic cavity (321) is connected with preposition chamber (31), anoxia chamber (322) with
First aerobic cavity (33) is connected, and is separated by dividing plate (22) between anaerobic cavity (321) and anoxia chamber (322).
6. the bioreactor for sewage disposal according to claim 5, is characterized in that：Anaerobic cavity (321) with it is preposition
Chamber (31), anaerobic cavity (321) and it is provided between anoxia chamber (322), anoxia chamber (322) and the first aerobic cavity (33) for connecting
Baffle pipe (23), one end of baffle pipe (23) are located at the bottom of previous cavity, and baffle pipe (23) other end runs through dividing plate (22)
Top.
7. the bioreactor for sewage disposal according to claim 1, is characterized in that：The preposition chamber (31) with it is heavy
Sludge reflux mechanism is provided between shallow lake chamber (35), the sludge reflux mechanism includes mud return line (4), mud return line (4)
One end insertion precipitation chamber (35) bottom, the other end are located at the top of preposition chamber (31).
8. the bioreactor for sewage disposal according to claim 7, is characterized in that：The mud return line (4)
It is upper to be above connected with aerating pipelines (5) positioned at one section precipitated in chamber (35), and confession is offered on peak on mud return line (4)
The dispelling the stagnated QI pipe (41) that inner air is discharged.
9. the bioreactor for sewage disposal according to claim 1, is characterized in that：The top of the tank body (2)
The lid (1) for opening is sealed is provided with, on the lid (1), manhole (11) is offered.
10. the bioreactor for sewage disposal according to claim 9, is characterized in that：On lid (1) inwall
Installation is provided with the air pump (51) for supplying to aerating pipelines (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621038399.3U CN206069515U (en) | 2016-09-06 | 2016-09-06 | For the bioreactor of sewage disposal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621038399.3U CN206069515U (en) | 2016-09-06 | 2016-09-06 | For the bioreactor of sewage disposal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206069515U true CN206069515U (en) | 2017-04-05 |
Family
ID=58437003
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621038399.3U Active CN206069515U (en) | 2016-09-06 | 2016-09-06 | For the bioreactor of sewage disposal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206069515U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106242057A (en) * | 2016-09-06 | 2016-12-21 | 山东文远建材科技股份有限公司 | Bioreactor for sewage disposal |
| CN110921969A (en) * | 2019-07-25 | 2020-03-27 | 重庆潜灵科技有限公司 | Multifunctional sewage treatment device |
-
2016
- 2016-09-06 CN CN201621038399.3U patent/CN206069515U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106242057A (en) * | 2016-09-06 | 2016-12-21 | 山东文远建材科技股份有限公司 | Bioreactor for sewage disposal |
| CN110921969A (en) * | 2019-07-25 | 2020-03-27 | 重庆潜灵科技有限公司 | Multifunctional sewage treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105668950B (en) | The back-washing method of floatation type comprehensive water treatment device, method for treating water and the equipment | |
| US20090065412A1 (en) | Apparatus for waste water treatment | |
| CN110294531A (en) | A kind of water treatment system and method based on ecological core wetland | |
| CN106116045A (en) | A kind of efficiently villages and small towns waste water treating and reutilizing device and technique thereof | |
| CA2965076C (en) | Water treatment reactor | |
| CN204474503U (en) | A kind of country sewage drips the ecological canal treatment system of filter | |
| CN107585974A (en) | A kind of sewage water treatment method based on MBBR techniques | |
| CN206069515U (en) | For the bioreactor of sewage disposal | |
| CN102874971B (en) | Baffling anaerobic reactor and sewage treatment unit applying same | |
| CN204661512U (en) | A kind of country sewage microkinetic ecological treatment system | |
| CN106242057A (en) | Bioreactor for sewage disposal | |
| CN100500593C (en) | Combined type wastewater treatment method and equipment | |
| CN206828325U (en) | Septic tank+A20 processing units | |
| CN2832804Y (en) | Composite sewage treatment equipment | |
| CN109987791A (en) | A kind of variable sewage-treatment plant of modular process | |
| CN206318767U (en) | Electroplating wastewater activated sludge process denitrification system | |
| CN106698659A (en) | Expressway service area sewage comprehensive treatment device | |
| CN211338961U (en) | Sewage treatment device adopting down-flow type anaerobic biological filter combined process | |
| CN114014492A (en) | Low carbon nitrogen ratio sewage treatment system | |
| CN203346179U (en) | Oxygen-increasing device, self-flow oxygen-increasing biological filter, self-flow oxygen-enriching ecological bed and sewage treatment system | |
| CN208327523U (en) | A kind of biologic purifying pot for sewage treatment | |
| CN107814439B (en) | Novel rural domestic sewage denitrification and dephosphorization purification wetland system | |
| CN207243671U (en) | A kind of integration distributing rural domestic sewage treating device | |
| CN205575780U (en) | Sewage treatment system | |
| CN205473194U (en) | Bury power that declines and purify groove sewage treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 255400 Linzi City, Zibo Province Jin Ling Hui Hui town Patentee after: Shandong Wen Yuan environmental Polytron Technologies Inc Address before: 255400 Linzi City, Zibo Province Jin Ling Hui Hui town Patentee before: SHANDONG WENYUAN PLASTIC CO., LTD. |