CN207175566U - Revolve plug-flow submerged aerobic biofilter - Google Patents
Revolve plug-flow submerged aerobic biofilter Download PDFInfo
- Publication number
- CN207175566U CN207175566U CN201721014924.2U CN201721014924U CN207175566U CN 207175566 U CN207175566 U CN 207175566U CN 201721014924 U CN201721014924 U CN 201721014924U CN 207175566 U CN207175566 U CN 207175566U
- Authority
- CN
- China
- Prior art keywords
- gas distribution
- pond body
- reaction zone
- perforated pipe
- sewage
- 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
Classifications
-
- 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
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
One kind rotation plug-flow submerged aerobic biofilter, pond body are followed successively by guiding region and rotation plug-flow reaction zone from front to back, and twoth area are separated by dividing plate, and dividing plate has gap with bottom of pond;It is provided with sewage inlet in guiding region, the gap of dividing plate and bottom of pond is outlet of sewer;Rotation plug-flow reaction zone is followed successively by aeration layer, reaction zone packing layer from the bottom to top;The bottom of aeration layer is provided with gas distribution perforated pipe, and several qi-emitting holes are offered on body;It is hung with elastic filler in reaction zone packing layer, intensive in elastic filler to be provided with more attachment filaments, the surface of attachment filament is attaching surface, and it is delivery port to adhere to propagation rear for aerobic bacteria.Compared to existing technologies, the utility model can produce density current effect, sewage is set to form eddy flow state, current iterate through reaction zone packing layer haptoreaction just as spiral shape promotes, double effects with biomembrance process and activated sludge process, not only to the high treating effect of sewage, and it is stable, and operational administrative is simple.
Description
Technical field
It the utility model is related to environment water treatment field, and in particular to one kind rotation plug-flow submerged aerobic biofilter, should
Filter tank is used to handle trade effluent or sanitary sewage.
Background technology
Submerged bacteria filter and the main difference in other biological filter tank are:It is submerged in filter tank full of sewage, filtrate
The neutralization of sewage uses artificial offering oxygen way.Specifically, submerged bacteria filter has the characteristics that:
(1)Among the filler grown for microorganism set is all submerged in sewage, it is immersed in equivalent to a kind of in sewage
Biofilter, hence obtain one's name " submerged bacteria filter ";
(2)Using the blast aeration method similar to aeration tank, there is provided microorganism(Aerobic bacteria, aerobic amphimicrobe)Oxidation has
Oxygen amount required for machine thing, and there is certain stirring and immixture, due to it equivalent to the addition of inhabited for microorganism it is numerous
The aeration tank for the filler grown, so the contact blast aeration tank that is otherwise known as;
(3)Purification sewage relies primarily on the effect of the biomembrane on filler, but activity similar in finite concentration is remained in pond
The biomembrance process processing structures of sludge feature, therefore it combines the effect of both aeration tank and biofilter.
Because submerged bacteria filter has These characteristics, therefore in the small-sized sanitary sewage in China and Industrial Wastewater Treatment
Application is obtained.Generally speaking, submerged bacteria filter have volumetric loading is high, the residence time is short, organic matter removal effect is good,
The advantages that operational management is simply and floor space is small, but if designing or running improper, easily causes filter clogging.
To sum up, blast aeration submerged bacteria filter, there is biomembrance process and activated sludge process double action and effect, but
There is also problems with:
First, in sewage disposal, current flow from bottom to top almost vertically, sewage water outlet after packing layer is flowed through.This
It is short current shape journey to be present in the traditional up flow type processing of kind(Generally only more than 3 meters), water outlet the problem of producing short circuit in the side in pond,
Adverse effect is brought to wastewater treatment efficiency;
2nd, blast aerator installation site is in larger distance with bottom of pond close to packing layer bottom, is easily caused bottom of pond deposition
Situation occur;
3rd, it is not perfect enough to flood biofilter structural form for up flow type, is applicable only to small-sized organic sewage processing,
It is difficult to promote in the sewage disposal of big-and-middle-sized scale.
Therefore, how to solve above-mentioned the shortcomings of the prior art, become as the problem of the invention to be researched and solved.
The content of the invention
The purpose of this utility model is to provide a kind of rotation plug-flow submerged aerobic biofilter.
To reach above-mentioned purpose, the technical solution adopted in the utility model is:
One kind rotation plug-flow submerged aerobic biofilter, including at least one unit for treating water, the unit for treating water bag
A pond body is included, the inner space that the pond body is formed is followed successively by guiding region and rotation plug-flow reaction from front to back along its length
Area, separated by a dividing plate between twoth area, and the dividing plate and the bottom of the pond body have a gap;Wherein,
It is provided with a sewage inlet in the guiding region, the gap of the dividing plate and the pond body bottom is the dirt of the guiding region
Water out;Sewage enters guiding region by the sewage inlet, is pushed backward into the rotation plug-flow via the outlet of sewer
The lower section of reaction zone;
Short transverse of the rotation plug-flow reaction zone along pond body divides into aeration layer successively from the bottom to top and reaction zone is filled out
The bed of material;The sewage is through pushing, by the outlet of sewer of the guiding region rearwards into the aeration layer for revolving plug-flow reaction zone, and
The reaction zone packing layer is flowed up through while continuing and flowing backward, the delivery port after processing above pond body rear end
Water outlet;Wherein,
Length direction of the bottom of the aeration layer along pond body is horizontally disposed an at least gas distribution perforated pipe;The gas distribution
Perforated pipe connects setting with an air intlet, the air containing oxygen is imported into the aeration layer;And the gas distribution is worn
It is spaced apart along its length on the body of hole pipe and is provided with several qi-emitting holes, each qi-emitting hole is perforated tube side part towards gas distribution
Obliquely downward opens up;When the gas distribution perforated pipe is one, gas distribution perforated pipe is located at the centre position of the pond body bottom, and away from
Side wall from pond body has with a distance from one, to form an eddy flow state mixing wastewater with air stream;When the gas distribution perforated pipe is more, each cloth
Gas perforated pipe is parallel and is arranged at intervals, and the gas distribution perforated pipe of both sides has a distance, the eddy flow state gas apart from the side wall of pond body
Water mixed flow is formed between adjacent two gas distributions perforated pipe and between gas distribution perforated pipe and the side wall of pond body;Work in filter tank
Under state, from the cross section angle of the pond body, mixing wastewater with air stream of the top formed with rising of the gas distribution perforated pipe,
And the mixing wastewater with air stream formed with decline between adjacent two gas distributions perforated pipe and between gas distribution perforated pipe and the side wall of pond body, on
For the mixing wastewater with air stream and the mixing wastewater with air stream of decline risen through the reaction zone packing layer and the aeration layer, both are common
With the composition eddy flow state mixing wastewater with air stream;
Elastic filler is hung with the reaction zone packing layer, the elastic filler is intensive to be filled in the reaction zone filler
In layer, and relatively described pond body positioning;Wherein, the elastic filler is made up of multiple strip fillers for being easy to mushroom to adhere to, should
Strip filler includes a strip main body, and along its length and intensive more attachments are provided with towards extending around in the strip main body
Silk, the surface of each attachment filament is attaching surface, and the aerobic bacteria attachment during attaching surface water supply is flowed is bred.
Relevant content in above-mentioned technical proposal is explained as follows:
1. in such scheme, " obliquely downward of each qi-emitting hole towards gas distribution perforation tube side part opens up ", form each described
The outlet air-flow of qi-emitting hole produces disturbance and gas-vapor mix to the current of the bottom of pond.
2. in such scheme, the trend of the gas distribution perforated pipe is consistent with pond body length direction, therefore is filled when in pond body
After water, worked by opening air blower, gas distribution perforated pipe is started outlet, the water in pond body will be produced due to density current effect
Multiple eddy flow state mixing wastewater with air streams;When pond body formally starts sewage treatment works, i.e. sewage is anti-into rotation plug-flow via guiding region
When answering area, the potential energy by sewage is kinetic energy, raw thrust of being miscarried to original eddy flow state mixing wastewater with air, forms rotation backward
The mixing wastewater with air stream of plug-flow state, until outlet water at tail end.
3. in such scheme, the dividing plate between guiding region and rotation plug-flow reaction zone has a gap apart from bottom of pond, passes through
The design in the gap, the sewage for revolving plug-flow reaction zone to entering produce a thrust, and the thrust contributes to sewage equably to pass
It is handed in whole rotation plug-flow reaction zone;
Simultaneously as the effect of the thrust, can be to being originally formed at the multiple eddy flow state gas revolved in plug-flow reaction zone
Water mixed flow plays plug-flow effect backward, and each eddy flow state mixing wastewater with air stream is affected by it can be while itself spins upside down
It is moved rearwards, so as to form the mixing wastewater with air stream of a rotation plug-flow state backward, so as to contribute to sewage, air and rotation plug-flow reaction
Elastic filler in area sufficiently contact, mixed.
4. in such scheme, the aeration layer extends forwardly into the bottom of the guiding region.It is unobstructed to be aerated the full pond of layer, is easy to
Bottom of pond Pipe installing is with safeguarding.
5. in such scheme, short transverse of the guiding region along pond body divide into successively from the bottom to top the aeration layer,
Guiding region packing layer and water conservancy diversion water-yielding stratum;The elastic filler is hung with the guiding region packing layer.Air water convection current passes through
Also there is biofilm contact reagentia during the packing layer of guiding region.
Elastic filler in guiding region can be positioned in active filler frame, it may be necessary to sling, made guiding region as perpendicular
To passage, it is easy to the drawing water of filter tank, Pipe installing and maintenance.
6. in such scheme, the positioning method of the relatively described pond body of the elastic filler can be suspended at the top of pond body,
Can also be fixedly arranged on pond body sidepiece etc..
7. in such scheme, by the design of more attachment filaments, the described attached of the single elastic filler can be significantly increased
Surface, is advantageous to produce more dense biomembrane, lifts biochemical reaction effect.
8. in such scheme, the air intlet can be opened at least in a side wall or from pond body of pond body
Top access a gas distribution supply air line gas outlet.
9. in such scheme, by " obliquely downward of each qi-emitting hole towards gas distribution perforation tube side part opens up ", set whereby
Count, the current of pond body bottom can be disturbed after air ejection qi-emitting hole, prevent sludge settling from accumulating;The qi-emitting hole tiltedly sets angle
Preferably 45 ° of degree, and each qi-emitting hole cross arrangement.
10. in such scheme, in addition to a gas distribution supply air line, the gas distribution supply air line is by a gas distribution house steward and Duo Gen cloth
Gas branch pipe connects and composes;
Wherein, the gas distribution house steward connects the air intlet, and horizontally disposed in the top of the pond body;Institute
Stating gas distributionbranch pipe has more, each gas distributionbranch pipe(By with gas control valve)The gas distribution house steward is connected, and each gas distributionbranch pipe is equal
The bottom for extending downwardly into the pond body connects with the gas distribution perforated pipe.
11. in such scheme, comprising two unit for treating water, two unit for treating water with the width of pond body it is horizontal and
It is bonded side by side, into being integral;Wherein, the binding face of two unit for treating water is a partition wall, the partition wall and the pond body
Bottom has a gap, and the aeration layer for forming the two unit for treating water pond bodies is interconnected.
12. in such scheme, aerobic biochemical of the present utility model belongs to a link of sewage disposal, the sewage disposal
Whole links include:Pretreatment, anaerobic biological, aerobic biochemical, materializing strategy and end advanced treating.
Operation principle of the present utility model is as follows:
A kind of rotation plug-flow submerged aerobic biofilter of the utility model, using aerobic treatment organic sewage, it is
Extremely important link in sewage treatment project.The active sludge of aerobic treatment and the class of biomembrance process two, different type,
Construct different, key of the present utility model is to construct good microorganism(Aerobic bacteria, aerobic amphimicrobe)Existence and procreation
Environment, there is provided the nutrient needed to Institute of Micro-biology(Organic matter in sewage), while provide needed for microorganism adsorption decomposing organic matter
Oxygen(By air blower force feed Lai air), good processing environment is built, obtains preferable treatment effect, is that this practicality is new
The target of type research and development.
When the utility model handles sewage, sewage from bottom to top, while flows from front to back, in the effect of ascending air
Under, form rotary-push type current;Therefore, the utility model can be accomplished in limited space, make lengthened stroke of the sewage in pond,
Will not be short-circuit, the mixing to sewage, oxygen and aerobic bacteria fully creates advantage;The utility model has activated sludge process concurrently
With both processing functions of biomembrance process, while the shortcomings that overcome two kinds of processing modes;Compared to traditional activated sludge process
Speech, because the activated sludge in filter tank will not go out pond body with a large amount of overflows of the process of processing, is retained activated sludge,
Also eliminate the backflow link of activated sludge(The link that flows back is without oxygen supply), therefore, aerobic microbiological(Aerobic bacteria)All the time in confession
Survive and multiply under conditions of oxygen abundance;For traditional biomembrance process, due in the form with submerged filter tank, and adopt
Intake with forward lower part, the water outlet of rear top, by producing the mixing wastewater with air stream of rotation plug-flow state backward, sewage and bubble are repeatedly
The problem of being contacted with filler, therefore overcoming short sewage stroke existing for protozoa embrane method, sewage flow direction easy " short circuit ";Due to this
Utility model has the advantages of activated sludge process and both processing methods of biomembrance process, therefore disposal ability of the present utility model concurrently
By force, large-scale sewage disposal can be carried out, sewage load is big in the unit interval, and the processing that same sewage load needs
Time is short;
The utility model installs gas distribution perforated pipe by the aeration layer in bottom of pond, 45 degree of qi-emitting hole on gas distribution perforated pipe to
Lower cross arrangement, and elastic filler is installed in reaction zone packing layer;After sewage is filled in pond, drive air blower and perforated to gas distribution
Pipe supplies, and due to the small rising of band air water fluid capacitance weight, the not sparkling water capacity is great to flowing down, therefore produces density current effect, is formed
Eddy flow state;When sewage enters rotation plug-flow reaction zone through guiding region Hou Chi bottoms, current iterate through just as spiral shape promotes
Reaction zone packing layer haptoreaction, until the muddy water mixed solution after overflow discharge processing, muddy water is carried out from secondary sedimentation tank is flowed into
Separation.
Major advantage of the present utility model:
1st, guiding region has the function that after sewage enters guiding region, the floating object in sewage is due to density uniformly with rectification
It is smaller, the spillwag chute of guiding region will be floated up to, can because the spillwag chute of guiding region and the spillwag chute of rotation plug-flow reaction zone are isolated
To prevent floating object from entering rotation plug-flow reaction zone.
2nd, resilient filler layer in plug-flow reaction zone is revolved, filler surface area is very big, is the good carrier of microorganism;When elasticity is filled out
It after the surface of material forms biomembrane, can be constantly updated under air water Swirl Condition, keep its bio-contact oxidation to decompose organic dirt
Contaminate the effect of thing;
Further, since pond body not overflow, activated sludge are retained, therefore without backflow link, i.e., in the absence of anoxic ring
Section, be advantageous to generation time it is longer nitrification mushroom existence procreation, make ammonia nitrogen in sewage nitrification for nitrite, nitrate, be
Biological denitrificaion creates conditions, and polyP bacteria therein has excessive adsorption phosphorus, there is biological phosphate-eliminating;
Revolving elastic filler in plug-flow reaction zone includes biomembrane, filler support etc., and shared pool volume is less than 10%, more than 90%
Volume be activated sludge cyclone reaction area, promote organic pollution catalytic oxidation and decompose.
To sum up, described the utility model has biomembrance process and the double effects of activated sludge process.
3rd, in the case where revolving plug-flow environment, volume effective rate of utilization is high, will not be short-circuit, downward using 45 degree of bottom of pond gas distribution perforated pipe
Cloth hole cross arrangement, when air-flow rises to reaction zone packing layer, bubble cuts filled silk repeatedly, improves the utilization of oxygen
Rate;Other gas distribution perforated pipe is easily installed, and is firmly installed, and is hardly damaged, typically need not maintenance;
4th, rotation pushes away the microorganism abundance of biofilter aggregation, it is not necessary to returned sludge, can save pump and pipeline;It is caused
Also specific activity sludge is few for surplus sludge volume, and the problem of activated sludge bulking will not occur and be lost in;
5th, stable, operational administrative specific activity sludge is easy.
The scope of application of the present utility model:
1st, sewage disposal scale is all suitable for, and small scale can use steel equipment, and scale can use greatly armored concrete knot
Structure;
2nd, can be built jointly side by side according to requirement of engineering progress is multiunit, specifically will be according to the scale and water quality shape of process object
Condition, calculate its BOD5 volumetric loading, the parameter such as pond shape construction and size, to meet handling process and the requirement of construction, and it is dirty
The requirement of the unified layout of water treatment plant;
3rd, using the structures of activated sludge process, if influenceing treatment effect because improving processing load, it may be considered that change
Make to revolve plug-flow submerged bacteria filter, improvement project amount is few.
Brief description of the drawings
Accompanying drawing 1 is the schematic top plan view of the utility model embodiment;
Accompanying drawing 2 be in Fig. 1 A-A to schematic cross-sectional view;
Accompanying drawing 3 is B-B direction schematic cross-sectional view in Fig. 1;
Accompanying drawing 4 be in Fig. 1 C-C to schematic cross-sectional view.
In the figures above:1. pond body;2. partition wall;3. guiding region;4. revolve plug-flow reaction zone;5. dividing plate;6. sewage inlet;
7. outlet of sewer;8. it is aerated layer;9. guiding region packing layer;10. water conservancy diversion water-yielding stratum;11. reaction zone packing layer;12. delivery port;
13. gas distribution perforated pipe;14. qi-emitting hole;15. eddy flow state mixing wastewater with air stream;The 151. mixing wastewater with air streams risen;152. gas declined
Water mixed flow;16. gas distribution house steward;17. gas distributionbranch pipe;18. tooth form water outlet conduit;19. outlet pipe;20. revolve the air water of plug-flow state
Mixed flow.
Embodiment
Below in conjunction with the accompanying drawings and embodiment is further described to the utility model:
Embodiment:Referring to shown in accompanying drawing 1~4, one kind revolves plug-flow submerged aerobic biofilter, including two water process lists
Member, two unit for treating water include a pond body 1, and two unit for treating water paste with the width level in filter tank and side by side
Close, into being integral.Wherein, the binding face of two unit for treating water is a partition wall 2, and the partition wall 2 and the bottom of pond body 1 have
One gap, the bottom of pond body 1 for forming two unit for treating water are interconnected.
The inner space that the pond body 1 of each unit for treating water is formed is followed successively by water conservancy diversion from front to back along its length
Area 3 and rotation plug-flow reaction zone 4, separated by a dividing plate 5 between twoth area, and the dividing plate 5 is same with the bottom of the pond body 1 has
One gap;
Wherein, the top of the guiding region 3 is provided with sewage inlet 6, and the dividing plate 5 and the gap of the bottom of pond body 1 are
The outlet of sewer 7 of the guiding region 3;Sewage enters guiding region 3 by the sewage inlet 6, via the outlet of sewer 7 to pusher
It is fed into the lower section of the rotation plug-flow reaction zone 4.Short transverse of the guiding region 3 along pond body 1 is divided into successively from the bottom to top
It is aerated layer 8, guiding region packing layer 9 and water conservancy diversion water-yielding stratum 10.
The rotation plug-flow reaction zone 4 divides into aeration layer 8 and reaction zone successively from the bottom to top along the short transverse of pond body 1
Packing layer 11;The aeration layer 8 of the guiding region 3 connects integrally with the aeration layer 8 of the rotation plug-flow reaction zone 4;The sewage
Through push, by the outlet of sewer of the guiding region 3 rearwards into the aeration layer 8 for revolving plug-flow reaction zone 4, and continuing backward
The reaction zone packing layer 11 is flowed up through while flowing, the water outlet of a delivery port 12 after processing above the rear end of pond body 1;
Wherein,
Length direction of the bottom of the aeration layer 8 along pond body 1 is horizontally disposed an at least gas distribution perforated pipe 13;It is described
Gas distribution perforated pipe 13 connects setting with an air intlet, the air containing oxygen is imported into the aeration layer 8;It is and described
It is spaced apart along its length on the body of gas distribution perforated pipe 13 and is provided with several qi-emitting holes 14, each qi-emitting hole 14 is towards gas distribution
The obliquely downward of the sidepiece of perforated pipe 13 opens up;When the gas distribution perforated pipe 13 is one, gas distribution perforated pipe 13 is located at the pond body 1
The centre position of bottom, and have a distance apart from the side wall of pond body 1, to form an eddy flow state mixing wastewater with air stream 15;When described
When gas distribution perforated pipe 13 is more, each gas distribution perforated pipe 13 is parallel and is arranged at intervals, and the gas distribution perforated pipe 13 of both sides is apart from pond
The side wall of body 1 has a distance, and the eddy flow state mixing wastewater with air stream 15 is formed between adjacent two gas distributions perforated pipe 13 and gas distribution
Between the side wall of perforated pipe 13 and pond body 1;It is described from the cross section angle of the pond body 1 under the working condition in filter tank
Mixing wastewater with air stream 151 of the top of gas distribution perforated pipe 13 formed with rising, and between adjacent two gas distributions perforated pipe 13 and gas distribution
Mixing wastewater with air stream 152 formed with decline between the side wall of perforated pipe 13 and pond body 1.The mixing wastewater with air stream 151 of the rising exists
During close to 1 top of pond body, wherein the air included is released, after releasing air, because accommodating change is big therefore continues to decline
Turn into the mixing wastewater with air stream 152 of the decline into pond body;Therefore, the mixing wastewater with air stream 152 of the decline due to comprising sky
Gas is few, not even containing air, its accommodating mixing wastewater with air stream 151 more than the rising, and then is produced by both bulk density differences
Density current effect.The mixing wastewater with air stream 151 of rising and the mixing wastewater with air stream 152 of decline are through the reaction zone packing layer 11
And the aeration layer 8, both collectively form the eddy flow state mixing wastewater with air stream 15.
For the guiding region packing layer 9 with being hung with elastic filler in the reaction zone packing layer 11, the elastic filler is close
Collection is filled in the guiding region packing layer 9 and the reaction zone packing layer 11, and relatively described pond body 1 positions;Wherein, it is described
Elastic filler is made up of multiple strip fillers for being easy to mushroom to adhere to, and the strip filler includes a strip main body, the strip main body
On along its length and towards extend around it is intensive be provided with more attachment filaments, the surface of each attachment filament is attaching surface,
Aerobic bacteria attachment propagation in attaching surface water supply stream.
Wherein, in addition to a gas distribution supply air line, the gas distribution supply air line is by a gas distribution house steward 16 and Duo Gen gas distributionbranch pipes
17 connect and compose;The gas distribution house steward 16 connects the air intlet, and horizontally disposed in the top of the pond body 1;
The gas distributionbranch pipe 17 has more, and each gas distributionbranch pipe 17 connects the gas distribution house steward 16, and each gas distributionbranch pipe 17 is stretched downwards
The bottom for entering the pond body 1 connects with the gas distribution perforated pipe 13.
Wherein, the top rear of the reaction zone water-yielding stratum 12 is provided with the delivery port 12, and the delivery port 12 connects a tooth
Shape water outlet conduit 18, the tooth form water outlet conduit 18 are connected with an outlet pipe 19.
Wherein, there is a gap apart from bottom of pond by the dividing plate 5 between guiding region 3 and rotation plug-flow reaction zone 4, by this
The design in gap, for producing a thrust to the sewage for entering rotation plug-flow reaction zone 4, the thrust contributes to sewage Transmit evenly
Into whole rotation plug-flow reaction zone 4;
Simultaneously as the effect of the thrust, can be to being originally formed at the multiple eddy flow state gas revolved in plug-flow reaction zone 4
Water mixed flow 16 plays plug-flow effect backward, and each eddy flow state mixing wastewater with air stream 15 is affected by it what can be spun upside down at itself
It is moved rearwards simultaneously, so as to form the mixing wastewater with air stream 20 of a rotation plug-flow state backward.
The utility model in the aeration layer 8 of bottom of pond by installing gas distribution perforated pipe 13, the qi-emitting hole on gas distribution perforated pipe 13
14 be in 45 degree of downward cross arrangements, and at least installs elastic filler in reaction zone packing layer 11;After sewage is filled in pond, open
Air blower supplies to gas distribution perforated pipe 13, and due to the small rising of band air water fluid capacitance weight, the not sparkling water capacity is great to flowing down, therefore produces
Raw density current effect, forms eddy flow state;When sewage behind guiding region 3 pond bottom enter rotation plug-flow reaction zone 4 when, current just as
Spiral shape promotes and iterates through the haptoreaction of reaction zone packing layer 11, until the muddy water mixed solution after overflow discharge processing, gravity flow
Enter secondary sedimentation tank and carry out mud-water separation.
For above-described embodiment only to illustrate technical concepts and features of the present utility model, its object is to allow be familiar with technique
Personage can understand content of the present utility model and implement according to this, the scope of protection of the utility model can not be limited with this.
All equivalent change or modifications made according to the utility model Spirit Essence, should all cover the scope of protection of the utility model it
It is interior.
Claims (5)
1. one kind rotation plug-flow submerged aerobic biofilter, it is characterised in that:
Including at least one unit for treating water, the unit for treating water includes a pond body, the inner space edge that the pond body is formed
Its length direction is followed successively by guiding region and rotation plug-flow reaction zone from front to back, is separated between twoth area by a dividing plate, and the dividing plate
There is a gap with the bottom of the pond body;Wherein,
A sewage inlet is provided with the guiding region, the dividing plate and the gap of the pond body bottom go out for the sewage of the guiding region
Mouthful;Sewage enters guiding region by the sewage inlet, is pushed backward via the outlet of sewer into the rotation plug-flow reaction
The lower section in area;
Short transverse of the rotation plug-flow reaction zone along pond body divides into aeration layer and reaction zone packing layer successively from the bottom to top;
The sewage through push, by the guiding region outlet of sewer rearwards into it is described rotation plug-flow reaction zone aeration layer, and after
The reaction zone packing layer is flowed up through while continuous flowing backward, the delivery port after processing above pond body rear end goes out
Water;Wherein,
Length direction of the bottom of the aeration layer along pond body is horizontally disposed an at least gas distribution perforated pipe;The gas distribution perforation
The connection of Guan Yuyi air intlets is set, the air containing oxygen is imported into the aeration layer;And the gas distribution perforated pipe
Body on be spaced apart be provided with several qi-emitting holes along its length, each qi-emitting hole towards gas distribution perforate tube side part it is oblique under
Fang Kaishe;When the gas distribution perforated pipe is one, gas distribution perforated pipe is located at the centre position of the pond body bottom, and apart from pond
The side wall of body has a distance, to form an eddy flow state mixing wastewater with air stream;When the gas distribution perforated pipe is more, each gas distribution is worn
Hole pipe is parallel and is arranged at intervals, and the gas distribution perforated pipe of both sides has a distance apart from the side wall of pond body, and the eddy flow state air water mixes
Interflow is formed between adjacent two gas distributions perforated pipe and between gas distribution perforated pipe and the side wall of pond body;Working condition in filter tank
Under, from the cross section angle of the pond body, mixing wastewater with air stream of the top formed with rising of the gas distribution perforated pipe, and phase
Mixing wastewater with air stream formed with decline between adjacent two gas distribution perforated pipes and between gas distribution perforated pipe and the side wall of pond body, rising
Mixing wastewater with air stream and the mixing wastewater with air stream of decline are through the reaction zone packing layer and the aeration layer, both common structures
Into the eddy flow state mixing wastewater with air stream;
Elastic filler is hung with the reaction zone packing layer, the elastic filler is intensive to be filled in the reaction zone packing layer
In, and relatively described pond body positioning;Wherein, the elastic filler is made up of multiple strip fillers for being easy to mushroom to adhere to, this
Shape filler includes a strip main body, and along its length and intensive more attachments are provided with towards extending around in the strip main body
Silk, the surface of each attachment filament is attaching surface, and the aerobic bacteria attachment during attaching surface water supply is flowed is bred.
2. aerobic biofilter according to claim 1, it is characterised in that:The aeration layer extends forwardly into the water conservancy diversion
The bottom in area.
3. aerobic biofilter according to claim 2, it is characterised in that:Short transverse of the guiding region along pond body by
Under supreme divide into the aeration layer, guiding region packing layer and water conservancy diversion water-yielding stratum successively;Hang and set in the guiding region packing layer
There is the elastic filler.
4. aerobic biofilter according to claim 1, it is characterised in that:Also include a gas distribution pipeline, the gas distribution pipeline
Connected and composed by a gas distribution house steward and Duo Gen gas distributionbranch pipes;
Wherein, the gas distribution house steward connects the air intlet, and horizontally disposed in the top of the pond body;The cloth
Gas branch pipe has more, and each gas distributionbranch pipe connects the gas distribution house steward, and each gas distributionbranch pipe extends downwardly into the bottom of the pond body
Portion connects with the gas distribution perforated pipe.
5. aerobic biofilter according to claim 1, it is characterised in that:Comprising two unit for treating water, at two water
Reason unit is horizontal and be bonded side by side with the width of pond body, into being integral;Wherein, the binding face of two unit for treating water is one
The bottom of partition wall, the partition wall and the pond body has a gap, forms the aeration layer phase of the two unit for treating water pond bodies
It is intercommunicated.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721014924.2U CN207175566U (en) | 2017-08-14 | 2017-08-14 | Revolve plug-flow submerged aerobic biofilter |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201721014924.2U CN207175566U (en) | 2017-08-14 | 2017-08-14 | Revolve plug-flow submerged aerobic biofilter |
Publications (1)
Publication Number | Publication Date |
---|---|
CN207175566U true CN207175566U (en) | 2018-04-03 |
Family
ID=61741029
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201721014924.2U Active CN207175566U (en) | 2017-08-14 | 2017-08-14 | Revolve plug-flow submerged aerobic biofilter |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN207175566U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107500403A (en) * | 2017-08-14 | 2017-12-22 | 谢绍舜 | Revolve plug-flow submerged aerobic biofilter |
CN109354335A (en) * | 2018-12-14 | 2019-02-19 | 谢绍舜 | The optimum organization technique of town domestic sewage processing |
-
2017
- 2017-08-14 CN CN201721014924.2U patent/CN207175566U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107500403A (en) * | 2017-08-14 | 2017-12-22 | 谢绍舜 | Revolve plug-flow submerged aerobic biofilter |
CN109354335A (en) * | 2018-12-14 | 2019-02-19 | 谢绍舜 | The optimum organization technique of town domestic sewage processing |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102180543B (en) | Highly-efficient stable bio-doubling sewage treatment device | |
CN104528932B (en) | A kind of advanced treatment of wastewater denitrification bio-filter apparatus system and process technique | |
CN105084650B (en) | Micro- aeration cycle integrated sewage water biological and ecological processing system and method | |
CN102583736A (en) | Sewage biochemical treatment process and device utilizing active sludge and biological membrane combined circulating flow | |
CN206512058U (en) | A kind of efficient villages and small towns waste water treating and reutilizing device | |
CN105923906A (en) | Structure and method for treating sewage through coupling multi-point water inlet biological membrane with phosphorus adsorption device | |
CN103435220B (en) | Coupled A[2]O suspended filler process and cloth media filter integrated nitrogen and phosphorus removal device and method | |
CN207175566U (en) | Revolve plug-flow submerged aerobic biofilter | |
CN110683658B (en) | Efficient biological denitrification process for sewage treatment | |
CN102285715A (en) | Compound membrane bioreactor for treating tuber mustard waste water | |
CN109354336A (en) | The optimum organization system of town domestic sewage processing | |
CN206970300U (en) | Nitrification liquid reflux and biological reaction pool for biological reaction pool | |
CN112479368A (en) | Sewage treatment device of biofilm reactor and treatment method thereof | |
CN114906986B (en) | Integrated sewage treatment device and method with adjustable process | |
CN107500403A (en) | Revolve plug-flow submerged aerobic biofilter | |
CN110713256A (en) | Biological pipe culvert reaction unit | |
CN106186548A (en) | A kind of marine culture wastewater processing system and processing method | |
CN201999827U (en) | High-efficiency stable sewage treatment device with bio-doubling process | |
CN208617486U (en) | A kind of high-performance bio integrated sewage treatment unit | |
CN211712878U (en) | Sewage treatment equipment | |
CN203295322U (en) | Nitrogen and phosphorus removal water-treatment device | |
CN210001737U (en) | Flotation advanced treatment equipment for extracellular enzymes | |
CN114014492A (en) | Low carbon nitrogen ratio sewage treatment system | |
CN209619000U (en) | A kind of high strength domestic sewage processing unit | |
CN103241901B (en) | Nitrogen and phosphorus removal water treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |