CN209668887U - One kind being based on New oxidation ditch associated with MABR-MBR - Google Patents
One kind being based on New oxidation ditch associated with MABR-MBR Download PDFInfo
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- CN209668887U CN209668887U CN201920325549.6U CN201920325549U CN209668887U CN 209668887 U CN209668887 U CN 209668887U CN 201920325549 U CN201920325549 U CN 201920325549U CN 209668887 U CN209668887 U CN 209668887U
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Abstract
The utility model relates to technical field of sewage, more particularly to it is a kind of based on New oxidation ditch associated with MABR-MBR, it solves MABR technology in the prior art to be used alone, biological phosphor-removing effect is bad, and the problem that MBR technology energy consumption is high, including oxidation ditch ontology, the area MBR and the area MABR, space between partition wall body and wall frame is the area MBR, there are three aeration membrane module and three blenders close to the setting of the side of wall frame for oxidation ditch ontology, there are two aeration membrane module and two blenders close to the setting of the other side of wall frame for oxidation ditch ontology, and oxidation ditch ontology is provided with separating film module on the inside of partition wall body, the side of oxidation ditch ontology opens up inlet opening, and water inlet pipe is fixedly installed on the inside of inlet opening, most of pollutant in oxidation ditch is by the microorganism in MABR Film removal, wherein activated sludge is mainly used for biological phosphate-eliminating, therefore the more conventional MBR of activated sludge concentration can be reduced, and thus reduced the aeration intensity of MBR, reduced operating cost.
Description
Technical field
The utility model relates to technical field of sewage, more particularly to one kind is based on novel oxidized associated with MABR-MBR
Ditch.
Background technique
Oxidation ditch is a kind of modification of activated sludge process, and aeration tank is in closed irrigation canals and ditches type, so it is in hydraulic flow state
Upper to be different from traditional activated sludge process, it is a kind of end to end recycle stream aeration irrigation canals and ditches, and sewage infiltration wherein obtains net
Change, what earliest oxidation irrigation canals and ditches were not built up by armored concrete, it is subject to the native irrigation canals and ditches that slope protection is handled, is between intermittent water inflow
Have a rest aeration, from this point on for, oxidation ditch is with the technology of sequence batch mode processing sewage earliest.
The Chinese patent of number of patent application 201510320526.2 discloses a kind of " MABR and MBR combined type sewage treatment
Device and processing method ".The patent sets gradually pretreatment unit, MABR unit and MBR unit along drainage flow direction；MABR
Unit and MBR unit are completely separable, and the activated sludge of suspended state is present in MBR unit.Removal for total phosphorus, relies primarily on
The Denitrifying Phosphate Accumulating Organisms of MABR unit and the aerobic phosphorous accumulating bacterium of MBR unit.However the training of Denitrifying Phosphate Accumulating Organisms and aerobic polyP bacteria
It is more demanding to operator to support enrichment, apply in sewage treatment facility at present is the most easily traditional biological phosphate-eliminating mistake
Journey: even if conventional polyP bacteria in the system of anaerobic-aerobic alternate run, carries out anaerobic phosphorus release and aerobic excess inhales phosphorus, most
Achieve the purpose that remove total phosphorus by discharging the excess sludge containing polyP bacteria eventually, which is plug-flow configuration, in MBR unit
Preferably oxygen condition, suspended sludge can not be in anaerobic state, therefore be unfavorable for the enrichment and growth of conventional polyP bacteria.
And when MABR technology is used alone, although nitration denitrification, biological phosphor-removing effect can be synchronized
It is bad.MBR technology is to overcome running membrane pollution problem, needs to maintain higher aeration intensity, increases operation energy consumption；And
The conventional bubble type aeration coefficient of oxygen utilization that MBR is used is too low.
It is therefore proposed that a kind of solved the above problems based on New oxidation ditch associated with MABR-MBR.
Utility model content
Purpose of the utility model is to solve MABR technology existing in the prior art exclusive use, biological phosphate-eliminating effects
Fruit is bad, and the disadvantage that MBR technology energy consumption is high, and the one kind proposed is based on New oxidation ditch associated with MABR-MBR.
To achieve the goals above, the utility model adopts the technical scheme that
One kind being based on New oxidation ditch associated with MABR-MBR, including oxidation ditch ontology, the area MBR and the area MABR, the oxygen
Change and be provided with wall frame on the inside of ditch ontology, and the inner wall of the oxidation ditch ontology is also connected with and is provided with partition wall body, the partition wall
Space between body and the wall frame is the area MBR；
There are three aeration membrane module and three blenders, institutes close to the setting of the side of the wall frame for the oxidation ditch ontology
Stating oxidation ditch ontology, there are two be aerated membrane module and two blenders, and the oxidation close to the setting of the other side of the wall frame
Ditch ontology is provided with separating film module on the inside of the partition wall body, and the outside of the separating film module is connected by drainpipe
There are suction pump and outlet pipe；
The side of the oxidation ditch ontology opens up inlet opening, and is fixedly installed with water inlet pipe, the oxidation on the inside of inlet opening
The other side of ditch ontology offers injection hole, and is fixedly installed with sludge pipe on the inside of injection hole.
Preferably, there are five blenders for the inside setting of the oxidation ditch ontology, and blender is in arrangement clockwise
Installation, blender are fixedly connected with the output end of motor, and the inside of the oxidation ditch ontology is arranged in by support rod for motor.
Preferably, the oxidation ditch ontology opens up mounting hole far from the side of the water inlet pipe, and is provided in mounting hole
Drainpipe, one end of drainpipe are connected on the separating film module.
Preferably, the other end of the drainpipe is connected to the input end of suction pump, and the outlet end of suction pump is connected with
Outlet pipe.
Preferably, the oxidation ditch ontology external form in closing irrigation canals and ditches shape, and oxidation ditch ontology inside region be divided into the area MBR and
The area MABR, and the area MBR and the area MABR are mutually communicated.
The beneficial effects of the utility model are:
1, in the oxidation ditch in the utility model, activated sludge all experienced complete anaerobism, aerobic process, increase oxygen
Change the adequacy that sludge in ditch inhales phosphorus, improves the removal effect of total phosphorus.
2, the utility model, organic matter, ammonia nitrogen and the total nitrogen in oxidation ditch in sewage are in the higher MABR of coefficient of oxygen utilization
It is removed in area, the area MBR is only that Biological Phosphorus Removal Process provides aerobic environment, and energy consumption is lower.
3, the utility model, most of pollutant in oxidation ditch is removed by the microbial film in MABR, wherein living
Property sludge is mainly used for biological phosphate-eliminating, therefore the more conventional MBR of activated sludge concentration can be reduced, and thus reduce the aeration of MBR
Intensity reduces operating cost.
Detailed description of the invention
Fig. 1 be the utility model proposes it is a kind of based on New oxidation ditch associated with MABR-MBR plan structure signal
Figure；
Fig. 2 be the utility model proposes a kind of forward sight structural representation based on New oxidation ditch associated with MABR-MBR
Figure；
Fig. 3 be the utility model proposes a kind of backsight structural representation based on New oxidation ditch associated with MABR-MBR
Figure.
In figure: 1 oxidation ditch ontology, the area 2MBR, 3 separating film modules, 4 outlet pipes, 5 suction pumps, 6 drainpipes, 7 partition wall bodies, 8
Motor, 9 aeration membrane modules, 10 water inlet pipes, the area 11MABR, 12 blenders, 13 wall framves, 14 sludge pipes.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.
Embodiment: referring to Fig.1-3, one kind being based on New oxidation ditch associated with MABR-MBR, including oxidation ditch ontology 1, MBR
Area 2 and the area MABR 11, the inside of oxidation ditch ontology 1 is provided with wall frame 13, and the inner wall of oxidation ditch ontology 1 is also connected with and is provided with
Partition wall body 7, the space between partition wall body 7 and wall frame 13 is the area MBR 2, in the inner space of oxidation ditch, partition wall body 7 and wall
Space between the outside of frame 13 is the area MABR 11, and 1 external form of oxidation ditch ontology is in closing irrigation canals and ditches shape, and 1 medial area of oxidation ditch ontology
Domain is divided into the area MBR 2 and the area MABR 11, and the area MBR 2 and the area MABR 11 are mutually communicated, and aeration membrane module 9 is selected as film aeration life
Object reactor, and MABR membrane material surface formed microbial film, microbial film from inside to outside be respectively aerobic layer, and oxygen layer and
Anaerobic layer, separating film module 3 is selected as membrane bioreactor, and membrane bioreactor is membrane separation technique and bioreactor
In conjunction with；
Wherein, there are three aeration membrane module 9 and three blenders close to the setting of the side of wall frame 13 for oxidation ditch ontology 1
12, there are two aeration membrane module 9 and two blenders 12 close to the setting of the other side of wall frame 13 for oxidation ditch ontology 1, and aoxidize
Ditch ontology 1 is provided with separating film module 3 close to the inside of partition wall body 7, and the outside of separating film module 3 is connected with by drainpipe 6
Suction pump and outlet pipe 4, i.e. oxidation ditch ontology 1 open up mounting hole, and the row of being provided in mounting hole far from the side of water inlet pipe 10
Water pipe 6, one end of drainpipe 6 are connected on separating film module 3, and the other end of drainpipe 6 is connected to the input end of suction pump 5,
And the outlet end of suction pump 5 is connected with outlet pipe 4, and in the setting of the inside of oxidation ditch ontology 1, there are five blenders 12, and stir
It mixes device 12 to be fixedly connected with the output end of motor 8 in arrangement installation, blender 12 clockwise, motor 8 passes through support rod
The inside of oxidation ditch ontology 1 is set, the side of oxidation ditch ontology 1 opens up inlet opening, and be fixedly installed on the inside of inlet opening into
Water pipe 10, the other side of oxidation ditch ontology 1 offers injection hole, and is fixedly installed with sludge pipe 14 on the inside of injection hole.
Preferably, the membrane material surface of MABR can form microbial film, and the oxygen from the intracavitary side of membrane tube is out of biomembrane
Portion is spread to outside, and the substrate in sewage is then internally spread from the surface of biomembrane, due to the incorgruous biography of oxygen and substrate
Matter causes on membrane module microbial film to generate apparent layered structure, from inside to outside respectively aerobic layer and oxygen layer and anaerobic layer,
In MABR microbial film functionality layering, can make the oxidation of microbial film complete independently dirt organic pollutants with it is synchronous
Nitration denitrification reaction；
Membrane bioreactor (MBR) is the sewage treatment process for being combined into membrane separation technique and bioreactor, is
The secondary settling tank for replacing traditional activated sludge process with membrane separation device, can be efficiently separated by solid-liquid separation, and it is preferable to obtain water quality
Water outlet.
Specifically, oxidation ditch is in the continuous cycle type reaction tank of closing irrigation canals and ditches shape, due to special construction, oxidation ditch is same
When have that be thoroughly mixed can be in the guiding role of blender 12 after sewage enters oxidation ditch with two kinds of characteristics of fluid state of pulling flow type
Lower carry out one-way flow, but because mixed liquor will be completed repeatedly to recycle in oxidation ditch, and simultaneously because flow velocity is very fast, sewage is very
It can be oxidized a large amount of mixed liquor dilution in ditch gallery fastly, therefore again it is considered that fluidised form and process dynamics in oxidation ditch are special
Sign is to be thoroughly mixed formula, and the unique characteristics of fluid state of oxidation ditch is just utilized in the present apparatus, and the area MABR 11 and the area MBR 2 are placed in
In the same reaction tank, the area MBR 2 and the area MABR 11 are separated by partition wall body 7 and wall frame 13, make activated sludge alternately in the area MABR
It is circulated in the area 11 and MBR 2, improves the biological phosphor-removing effect of technique, and reduce operation difficulty；
Further, the area MBR 21 is made of separating film module 3, drainpipe 6, suction pump 5 and outlet pipe 4, is being located at MBR
The reaction pool bottom in area 2 is uniformly equipped with micro porous aeration head or aeration tube, and the area MBR 2 and aeration membrane module 9 are all made of air
Source is supplied oxygen by air blower, and sewage enters oxidation ditch by water inlet pipe 10, and water inlet pipe 10 is located above the pool wall in the area MABR 11, and
And sewage can enter the area MABR 11 by more water inlet pipes 10, wherein a water inlet pipe 10 is located at the outlet pipe 4 one in the area MBR 2
Side mitigates its influence to anaerobic state in the area MABR 11, the denitrogenation to oxidation ditch to consume the dissolved oxygen in the water outlet of the area MBR 2
Phosphorus removal functional is strengthened, and the water distribution quantity of each water inlet pipe 10 can distribute by a certain percentage according to water quality, and the area MBR 2 removes for biology
Phosphorus provides aerobic environment, therefore sludge concentration needed for oxidation ditch is lower, and the pool capacity in the area MBR 2 can also reduce, and reduce MBR
The aeration intensity in area 2 simultaneously thereby reduces energy consumption；
Further, the motor 8 for thering is aeration membrane module 9, blender 12 and control blender 12 to rotate in the area MABR 11,
Blender 12 plays the role of adjusting sewage fluidised form for making sludge keep suspended state, plays guiding to the flowing of sewage
Effect, due to that oxygen can be made on aeration 9 surface of membrane module by pressure in control film using aeration membrane module 9 in the area MABR 11
It is totally consumed in microbial film, therefore the sewage in the area MABR 11 is in anaerobic state, the activated sludge of sewage and suspension is in oxygen
Changing will complete repeatedly to recycle in ditch, need to replace and recycle in the area MBR 2 in the area MABR 11 in anaerobic state and in aerobic state
Flowing can carry out Biological Phosphorus Removal Process, and by the discharge of sludge pipe 14, (sludge pipe 14 is located under the pool wall in the area MABR 11 excess sludge
Side, the side diagonal positioned at water inlet pipe 10 can also serve as evacuated tube use, achieve the purpose that finally to remove total phosphorus, the biological phosphate-eliminating
Process is not necessarily to gathering denitrifying polyP bacteria and aerobic polyP bacteria, therefore operation is more simple, and phosphor-removing effect is more preferable, in sewage
Organic pollutant, ammonia nitrogen, total nitrogen etc. can be removed in the area MABR 11；
In conclusion sanitary sewage enters the area MABR 11 in oxidation ditch after pretreatment, through water inlet pipe 10, and stirring
It under the guiding role for mixing device 12, is sufficiently mixed with the activated sludge in oxidation ditch, the film surface of aeration membrane module 9 is attached with micro- life
Object film, some organic pollutants and ammonia nitrogen in sewage diffuse into aerobic layer inside microbial film, are decomposed and are converted into dioxy
Change carbon and nitrate, nitrate reversely diffuses to the organic pollutant outside microbial film and in oxygen layer and anaerobic layer, with sewage
Denitrification is carried out, N2 is formed and is escaped from water.
In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width
Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside",
The orientation or positional relationship of the instructions such as " clockwise ", " counterclockwise " be based on the orientation or positional relationship shown in the drawings, be only for
Convenient for description the utility model and simplify description, rather than the equipment of indication or suggestion meaning or element must have specifically
Orientation is constructed and operated in a specific orientation, therefore should not be understood as limiting the present invention.
In addition, term " first ", " second " are used for description purposes only, it is not understood to indicate or imply relatively important
Property or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Person implicitly includes one or more of the features.The meaning of " plurality " is two or two in the description of the present invention,
More than a, unless otherwise specifically defined.
The preferable specific embodiment of the above, only the utility model, but the protection scope of the utility model is not
It is confined to this, anyone skilled in the art is within the technical scope disclosed by the utility model, practical according to this
Novel technical solution and its utility model design are subject to equivalent substitution or change, should all cover the protection model in the utility model
Within enclosing.
Claims (5)
1. one kind is based on New oxidation ditch associated with MABR-MBR, including oxidation ditch ontology (1), the area MBR (2) and the area MABR
(11), which is characterized in that it is provided with wall frame (13) on the inside of the oxidation ditch ontology (1), and the oxidation ditch ontology (1)
Inner wall, which is also connected with, to be provided with partition wall body (7), and the space between the partition wall body (7) and the wall frame (13) is the area MBR (2)；
There are three aerations membrane module (9) and three to stir close to the setting of the side of the wall frame (13) for the oxidation ditch ontology (1)
Mix device (12), the oxidation ditch ontology (1) close to the wall frame (13) the other side setting there are two aeration membrane module (9) and
Two blenders (12), and the oxidation ditch ontology (1) is provided with separating film module (3) on the inside of the partition wall body (7),
The outside of the separating film module (3) is connected with suction pump and outlet pipe (4) by drainpipe (6)；
The side of the oxidation ditch ontology (1) opens up inlet opening, and is fixedly installed with water inlet pipe (10), the oxygen on the inside of inlet opening
The other side for changing ditch ontology (1) offers injection hole, and is fixedly installed with sludge pipe (14) on the inside of injection hole.
2. according to claim 1 a kind of based on New oxidation ditch associated with MABR-MBR, which is characterized in that the oxidation
There are five blender (12) for the inside setting of ditch ontology (1), and blender (12) is in arrangement installation clockwise, blender
(12) it is fixedly connected with the output end of motor (8), motor (8) is arranged by support rod in the interior of the oxidation ditch ontology (1)
Portion.
3. according to claim 1 a kind of based on New oxidation ditch associated with MABR-MBR, which is characterized in that the oxidation
Ditch ontology (1) opens up mounting hole far from the side of the water inlet pipe (10), and drainpipe (6), drainpipe are provided in mounting hole
(6) one end is connected on the separating film module (3).
4. according to claim 3 a kind of based on New oxidation ditch associated with MABR-MBR, which is characterized in that the draining
The other end of pipe (6) is connected to the input end of suction pump (5), and the outlet end of suction pump (5) is connected with outlet pipe (4).
5. according to claim 1 a kind of based on New oxidation ditch associated with MABR-MBR, which is characterized in that the oxidation
Ditch ontology (1) external form is in closing irrigation canals and ditches shape, and oxidation ditch ontology (1) inside region is divided into the area MBR (2) and the area MABR (11), and
And the area MBR (2) and the area MABR (11) are mutually communicated.
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| Application Number | Priority Date | Filing Date | Title |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109761354A (en) * | 2019-03-15 | 2019-05-17 | 沈阳环境科学研究院 | One kind being based on New oxidation ditch associated with MABR-MBR |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109761354A (en) * | 2019-03-15 | 2019-05-17 | 沈阳环境科学研究院 | One kind being based on New oxidation ditch associated with MABR-MBR |
| CN109761354B (en) * | 2019-03-15 | 2024-01-02 | 沈阳环境科学研究院 | Novel oxidation ditch based on MABR-MBR allies oneself with uses |
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