CN110002688A - It is a kind of efficiently to mention mark system - Google Patents

It is a kind of efficiently to mention mark system Download PDF

Info

Publication number
CN110002688A
CN110002688A CN201910365783.6A CN201910365783A CN110002688A CN 110002688 A CN110002688 A CN 110002688A CN 201910365783 A CN201910365783 A CN 201910365783A CN 110002688 A CN110002688 A CN 110002688A
Authority
CN
China
Prior art keywords
partition
circulation
activated sludge
partitions
opening
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.)
Granted
Application number
CN201910365783.6A
Other languages
Chinese (zh)
Other versions
CN110002688B (en
Inventor
张建飞
元西方
赵庆
刘丹丹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beckett Group Co Ltd
Original Assignee
Beckett Group Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beckett Group Co Ltd filed Critical Beckett Group Co Ltd
Priority to CN201910365783.6A priority Critical patent/CN110002688B/en
Publication of CN110002688A publication Critical patent/CN110002688A/en
Application granted granted Critical
Publication of CN110002688B publication Critical patent/CN110002688B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes

Abstract

Mark system is efficiently mentioned the present invention relates to a kind of, including at least conditioning tank, anoxic pond, aerobic tank, sedimentation basin and clear water reserviors, the downstream of sedimentation basin is arranged in clear water reserviors, the downstream of anoxic pond is arranged in aerobic tank, the downstream of conditioning tank is arranged in anoxic pond, circulation oxidation reactor is provided in the aerobic tank, aerobic tank inputs the water in anoxic pond in sedimentation basin after the circulation of circulation oxidation reactor aoxidizes;Wherein, circulation oxidation reactor includes several circulation partitions and several aerators, and aerator provides gas in the side of circulation partition, and activated sludge is allowed to form circulation around at least one piece of circulation separator flow.The present invention can preferably improve the oxygen transfer efficiency and dissolved oxygen performance efficiently mentioned in the aerobic tank of device for mark.

Description

It is a kind of efficiently to mention mark system
Technical field
The present invention relates to water treatment fields and ecological, environmental protective industry, especially water prevention and cure of pollution and Sewage advanced treatment, especially It is related to one kind and efficiently mentions mark system.
Background technique
Aerobic activated sludge process is a kind of biologic treating technique of relative maturity, using wide in current municipal sewage treatment General, in the processing of the industrial wastewater of some high concentrations, the stain disease by anaerobism will also be carried out by aerobic activated sludge process Processing.
In traditional aerobic activated sludge process sewage treatment process, dissolved oxygen aeration is to carry out simultaneously with biological oxidation process , but be to separate in different pond bodies from precipitation and separation, in order to ensure certain sludge concentration, it is necessary to carry out returning for big flow Stream, makes the precipitating sludge of secondary settling tank flow back into aeration tank by power and participates in bioprocesses again.
For example, the Chinese patent literature that Authorization Notice No. is CN202849149U discloses at a kind of microkinetic sanitary sewage Device is managed, it includes the closed tank body of integral type, which passes through first partition, second partition, third partition and the 4th partition It is separated out anaerobic pond, anoxic pond, aerobic tank, sludge reflux well and sedimentation basin, the anaerobic pond, anoxic pond, aerobic tank, sludge return It is respectively arranged with manhole at the top of stream well and sedimentation basin, combination is mounted in the anaerobic pond, anoxic pond and aerobic tank and fills out The front end of material, the anaerobic pond is equipped with water inlet.Its structure is simple, improves the effective rate of utilization of integration apparatus;It can mention Mobility and the tank intracorporal residence time of high sewage;It can promote muddy water contact enhancing treatment effect;And muddy water can be enhanced Separating effect.In this process, activated sludge can be circulated constantly between aerobic tank and sedimentation basin, on the one hand be expended a large amount of On the other hand the energy due to the continuous variation of microorganism growing environment, reduces its bioactivity, be unfavorable for biodegradable anti- The progress answered.
Therefore, circulation aoxidizes relevant device, for example, the Chinese patent literature that Authorization Notice No. is CN102815784B is public A kind of Aerobic three-phase separator is opened.Aerobic three-phase separator by end plate disposed in parallel, respectively it is vertical with end plate connect top It is folded respectively inwards for the deflector of rectangular cavities, two deflector bottom ends and vertical with end plate is connected as having sludge reflux to stitch The inclined plate of bottom pyramidal chambers, the overflow weir being arranged between two end plates of top rectangular cavity, two end plate are corresponding to overflow The position Liu Yan, which is opened up, to be symmetrically arranged with respectively between the outlet of overflow weir perforation, overflow weir and overflow weir two sides deflector along two ends Between the precipitating partition that overhangs downwards at the top of plate, precipitating partition between molding sludge settling area, precipitating partition and deflector at The guiding region of type the taper sludge bucket that inclined plate is constituted is folded inward by deflector forms.But the device does not carry out space It efficiently utilizes, circulation oxidation effectiveness is to be improved.Therefore, it is necessary to be improved to the prior art.
Summary of the invention
For the deficiencies of the prior art, the present invention provides one kind efficiently to mention mark system, this efficiently mentions the circulation of mark system Oxidation reactor can form the subring around second partition in the formation of oxidation pond around the main ring stream of first partition and in main ring stream Stream, compared with the prior art for, present invention greatly enhances the dissolved oxygen performances of circulation oxidation reactor.
According to a preferred embodiment, a kind of circulation oxidation reactor, including several circulation partitions and several aerators, Aerator provides gas in the side of circulation partition, allows at least partly activated sludge of the side of circulation partition to be stripped and upward Mobile, at least partly a part of activated sludge is under the action of behind the top edge of corresponding circulation partition in pressure difference from ring The side of stream partition is moved to the other side of circulation partition and is fallen based on gravity from the other side of circulation partition, from circulation partition A part of activated sludge for falling of the other side be stripped again behind the side for moving to circulation partition, to allow with active The sewage of sludge forms circulation around corresponding circulation separator flow.
According to a preferred embodiment, several circulation partitions include at least a pair of of first partition, several aerators Including at least the first aerator, two first partitions in each pair of first partition are intervally installed, and the first aerator is each pair of Lower section ventilation between first partition is to allow at least part in the sewage for having activated sludge can be around corresponding first partition Flowing forms circulation.Several circulation partitions further include at least one second partition, and several aerators further include at least one Second aerator, the second partition by with first partition at angle in a manner of intersect with each other, and each second partition is remote One end from corresponding first partition is in the lower section for the other end of each second partition intersected with corresponding first partition, The top of the position of first partition intersected with second partition is equipped with the first opening, in intersecting with second partition for first partition The lower section of position is equipped with the second opening, and each second partition is furnished at least one second aerator, and corresponding second aerator exists Ventilation below corresponding second partition, with allow in each pair of first partition the amount of activated sludge that flows by corresponding second every Second partition is moved to from the side of first partition by corresponding first opening under the action of pressure difference behind the top edge of plate The other side is simultaneously fallen based on gravity from the other side of second partition, one from the activated sludge that the other side of second partition falls The bubble air lift that amount of activated sludge is discharged by the second aerator again behind the side for moving to second partition is by corresponding Second opening enters the position between two first partitions, to allow the sewage for having activated sludge around corresponding second partition stream It is dynamic to form circulation.
According to a preferred embodiment, each first partition is equipped at least two intersecting therewith second partitions, and every At least two second partitions of a first partition intersection are spaced setting on different level height directions, are partially lived with allowing have The sewage of property sludge flows to form circulation in different level height sides upwards about corresponding second partition.
According to a preferred embodiment, at least two second partitions intersected with each first partition are thrown towards horizontal Shadow face project when with floor projection width different from each other, wherein at least two second intersected with each first partition every Floor projection width in second partition relatively above in plate is greater than the floor projection of the second partition in opposite lower section Width.
According to a preferred embodiment, corresponding with each second partition first be arranged in first partition is open big Small related to the floor projection width of the second partition, the second partition corresponding first with bigger floor projection width is opened Mouthful it is bigger;And/or the size and the second partition for the second opening corresponding with each second partition being arranged in first partition Floor projection width it is related, corresponding second opening of second partition with bigger floor projection width it is bigger.
According to a preferred embodiment, the lower edge of each second partition is extended downward into and corresponding second opening Lower edge flushes or the lower edge of each second partition extends downward into the lower edge of corresponding second opening or less.
According to a preferred embodiment, the first overthe openings of first partition are equipped with chock flap, the chock flap with First partition intersects with each other at the mode of angle, and one end far from corresponding first partition of each chock flap is in each The lower section for the other end of chock flap intersected with corresponding first partition, and the other end of corresponding chock flap extend to it is right The lower edge for the first opening answered flushes or the other end of corresponding chock flap extends to the corresponding first lower edge being open Below.
According to a preferred embodiment, one end far from corresponding first partition of chock flap is equipped with arc crimping, arc Shape crimping is having towards first after arc crimping according to allowing the following table along chock flap to face away from the bubble that first partition moves The mode of the trend of partition movement is arranged.
According to a preferred embodiment, one kind efficiently mentioning mark system, includes at least conditioning tank, anoxic pond, aerobic tank, sinks The downstream of sedimentation basin is arranged in shallow lake pond and clear water reserviors, clear water reserviors, and the downstream of anoxic pond is arranged in aerobic tank, and anoxic pond setting is being adjusted The downstream in pond is saved, circulation oxidation reactor is provided in the aerobic tank, aerobic tank aoxidizes the water in anoxic pond by circulation It is inputted in sedimentation basin after the circulation oxidation of reactor;Wherein, circulation oxidation reactor includes several circulation partitions and several aerations Device, aerator circulation partition side provide gas, allow at least partly activated sludge of the side of circulation partition be stripped and Move up, at least partly a part of activated sludge behind the top edge of corresponding circulation partition under the action of pressure difference The other side of circulation partition is moved to from the side of circulation partition and is fallen based on gravity from the other side of circulation partition, from circulation The a part for the activated sludge that the other side of partition falls is stripped again behind the side for moving to circulation partition, is had with allowing The sewage of activated sludge forms circulation around corresponding circulation separator flow.
According to a preferred embodiment, several circulation partitions include at least a pair of of first partition, several aerators Including at least the first aerator, two first partitions in each pair of first partition are intervally installed, and the first aerator is each pair of Lower section ventilation between first partition is to allow at least part in the sewage for having activated sludge can be around corresponding first partition Flowing forms circulation, and several circulation partitions further include at least one second partition, and several aerators further include at least one Second aerator, the second partition by with first partition at angle in a manner of intersect with each other, and each second partition is remote One end from corresponding first partition is in the lower section for the other end of each second partition intersected with corresponding first partition, The top of the position of first partition intersected with second partition is equipped with the first opening, in intersecting with second partition for first partition The lower section of position is equipped with the second opening, and each second partition is furnished at least one second aerator, and corresponding second aerator exists Ventilation below corresponding second partition, with allow in each pair of first partition the amount of activated sludge that flows by corresponding second every Second partition is moved to from the side of first partition by corresponding first opening under the action of pressure difference behind the top edge of plate The other side is simultaneously fallen based on gravity from the other side of second partition, one from the activated sludge that the other side of second partition falls The bubble air lift that amount of activated sludge is discharged by the second aerator again behind the side for moving to second partition is by corresponding Second opening enters the position between two first partitions, to allow the sewage for having activated sludge around corresponding second partition stream It is dynamic to form circulation.
Detailed description of the invention
Fig. 1 is the module connection diagram of a preferred embodiment for efficiently mentioning mark system of the invention;
Fig. 2 is the rough schematic view of first preferred embodiment of circulation oxidation reactor of the invention;
Fig. 3 is the rough schematic view of second preferred embodiment of circulation oxidation reactor of the invention;
Fig. 4 is the rough schematic view of the third preferred embodiment of circulation oxidation reactor of the invention;
Fig. 5 is the schematic diagram of a preferred embodiment of carbon fiber layer;With
Fig. 6 is the module connection diagram of another preferred embodiment for efficiently mentioning mark system of the invention.
Reference signs list
A: conditioning tank B: anoxic pond C: aerobic tank
D: sedimentation basin E: clear water reserviors F: anaerobic pond
G: device for mark H: sand filter 100: circulation partition is efficiently mentioned
110: 112: the second opening of the opening of first partition 111: the first
120: second partition 200: several 210: the first aerators of aerator
220: the second aerators 300: chock flap 400: overflow weir
500: drainage plate the Q2: the second acute angle of the Q1: the first acute angle
K1: guidance dog-ear K2: arc crimping X1: carbon fiber layer
LR: circulation oxidation reactor
Specific embodiment
It 1,2,3,4,5 and 6 is described in detail with reference to the accompanying drawing.
In the description of the present invention, it is to be understood that, if occur term " center ", " longitudinal direction ", " transverse direction ", " length ", " width ", " 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 the description present invention and simplify description, rather than the device or element of indication or suggestion meaning there must be specific side Position is constructed and operated in a specific orientation, therefore is not considered as limiting the invention.
In the description of the present invention, it is also necessary to which understanding is only used for retouching if there are the terms such as " first ", " second " Purpose is stated, relative importance is not understood to indicate or imply or implicitly indicates the quantity of indicated technical characteristic.By This defines " first ", the feature of " second " can explicitly or implicitly include one or more of the features.In this hair In bright description, if there are term " multiple ", it is meant that two or more, unless otherwise specifically defined.
In the description of the present invention, it is also necessary to understanding, if occur " installation ", " connected ", " connection ", " fixation ", " Gu Connect " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected;It can To be mechanical connection, it is also possible to be electrically connected;It can be directly connected, can also can be indirectly connected through an intermediary Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood as the case may be Concrete meaning in the present invention unless otherwise specific regulation and/or limits.
In the description of the present invention, it is also necessary to which understanding is unless specifically defined or limited otherwise, fisrt feature is The "upper" of two features or "lower" may include that the first and second features directly contact, also may include the first and second features not It is direct contact but by the other characterisation contact between them.Moreover, fisrt feature second feature " on ", " on Side " and " above " include fisrt feature right above second feature and oblique upper, or are merely representative of first feature horizontal height height In second feature.Fisrt feature under the second feature " below ", " below " and " below " include fisrt feature second feature just under Side and obliquely downward, or first feature horizontal height is merely representative of less than second feature.
Embodiment 1
Present embodiment discloses one kind efficiently to mention mark system, in other words a kind of water treatment system, in other words at a kind of waste water Reason system, in the case where not causing conflict or contradictory situation, in the entirety of the preferred embodiment of other embodiments and/or part Hold the supplement that can be used as the present embodiment.
According to a preferred embodiment, it may include conditioning tank A, anoxic pond B, aerobic tank that one kind, which efficiently mentioning mark system, C, at least one of sedimentation basin D and clear water reserviors E.Circulation oxidation reactor LR can be set in aerobic tank C.In conditioning tank A Water can enter in anoxic pond B by grid filtration.Aerobic tank C by the water in anoxic pond B can by efficiently mention mark after it is defeated Enter in sedimentation basin D.Meanwhile the sludge in the nitrification liquid and sedimentation basin D in aerobic tank C can be with circulating reflux into anoxic pond B.It is heavy Clear water reserviors E can be discharged into after clear water in the D of shallow lake pond is up to standard.Preferably, the oxidation of at least one circulation can be set in aerobic tank C Reactor LR.Preferably, several circulation oxidation reactors LR can be set in aerobic tank C.Several circulation oxidation reactions It can be one another in series between device LR or in parallel.
According to a preferred embodiment, if circulation oxidation reactor LR may include circulation partition 100 and/or dry gas Provider.Gas provider can provide gas in the side of circulation partition 100 and not provide in the other side of circulation partition 100 Gas.Thus the side solid-liquid-gas of circulation partition 100 is allowed to move up, the solid of 100 other side of circulation partition moves down shape At circulation.Gas provider for example can be aerator.
According to a preferred embodiment, circulation oxidation reactor LR may include several circulation partitions 100 and/or several Aerator 200.Aerator 200 can the side of circulation partition 100 provide gas, allow circulation partition 100 side at least Amount of activated sludge is stripped and moves up by the lower edge of circulation partition 100.At least partly a part of activated sludge It can be moved under the action of behind the top edge of corresponding circulation partition 100 in pressure difference from the side of circulation partition 100 The other side of circulation partition 100 is simultaneously fallen based on gravity from the other side of circulation partition 100.From the other side of circulation partition 100 The a part of of the activated sludge of whereabouts can be stripped again behind the side for moving to circulation partition 100, to allow with active The sewage of sludge forms circulation around the flowing of corresponding circulation partition 100.Preferably, the top of aerobic tank C can be to be open to incite somebody to action Gas in aerobic tank C is directly discharged to the external world.
According to a preferred embodiment, circulation oxidation reactor LR may include overflow weir 400 and/or drainage plate 500. Drainage plate 500 can be set between circulation partition 100 and overflow weir 400, to draw between circulation partition 100 and drainage plate 500 Activated sludge precipitating is led, the sewage at least partially through precipitating is allowed to flow out along overflow weir 400.Preferably, under drainage plate 500 End is bent towards 400 direction of overflow weir.
According to a preferred embodiment, several circulation partitions 100 may include a pair of of first partition 110.Several aerations Device 200 may include the first aerator 210.Two first partitions 110 in each pair of first partition 110, which can be spaced each other, to be set It sets.First aerator 210 can the lower section of each pair of first partition 110 ventilate with allow have activated sludge sewage at least A part can be flowed around corresponding first partition 110 forms circulation.
According to a preferred embodiment, several circulation partitions 100 may include a second partition 120.Several aerations Device 200 may include the second aerator 220.Second partition 120 can by with first partition 110 at angle in a manner of phase each other It hands over.One end far from corresponding first partition 110 of each second partition 120 may be at each second partition 120 with it is right The lower section for the other end that the first partition 110 answered intersects.In the upper of the position of first partition 110 intersected with second partition 120 Side can be equipped with the first opening 111.The can be equipped in the lower section for the position of first partition 110 intersected with second partition 120 Two openings 112.Each second partition 120 can be furnished at least one second aerator 220.Corresponding second aerator 220 exists It ventilates below corresponding second partition 120, to allow in each pair of first partition 110 the amount of activated sludge flowed by corresponding It is transported by corresponding first opening 111 from the side of first partition 110 under the action of pressure difference behind the top edge of second partition 120 It moves the other side of second partition 120 and is fallen based on gravity from the other side of second partition 120.From the another of second partition 120 A part of activated sludge in activated sludge that side falls can be again by second behind the side for moving to second partition 120 The bubble air lift that aerator 220 discharges enters the position between two first partitions 110 by corresponding second opening 112, To allow the sewage for having activated sludge to form circulation around the flowing of corresponding second partition 120.The present invention at least can using this mode Enough realize following advantageous effects: first, the present invention has better dissolved oxygen performance compared with the prior art;Second, this hair It is bright to have preferably mass-transfer performance, mixed performance more reasonable compared with the prior art;Third, the present invention is compared with the prior art With better heat transfer property, when needing temperature to adjust, by better heat transfer property, realization is fast and accurately adjusted, surely It is qualitative also more preferable.Preferably, the system can also include temperature control device, temperature control device be used for the fluid temperature in oxygen pond into Row regulation is to be maintained at corresponding temperature range.For example, 20 DEG C~30 DEG C, particularly preferred 24 DEG C~26 DEG C.Temperature control device can be with Including heater, heater can be embedded in around oxygen bottom of pond portion and/or side wall.Or heater can be placed in oxygen Inside pond.
According to a preferred embodiment, the upper surface of the first opening 111 and the first 111 lower surfaces of opening can be tilted Setting.The inclined direction of the upper and lower surfaces of first opening 111 can be opposite closer to resistance on its surface according to making There is the mode of lower height to be arranged for the position of gas plate 300.In other words, the upper surface of the first opening 111 can be according to making the Opposite tilt closer to the position of chock flap 300 with the mode of lower level height on the upper surface of one opening 111 sets It sets.It the lower surface of first opening 111 can be according to opposite closer to chock flap 300 on the lower surface for making the first opening 111 There is the mode of lower level height to be obliquely installed for position.The present invention at least can be realized following Advantageous using this mode Effect: the mode that is obliquely installed of the upper surface of the first, the first opening 111 helps to reduce the gas from 111 escape of the first opening Amount;The mode that is obliquely installed of the lower surface of the second, the first opening 111 facilitates the outflow of sludge.
According to a preferred embodiment, the lower surface of the upper surface of the second opening 112 and the second opening 112 can incline Tiltedly setting.It the upper surface of second opening 112 can be according to opposite closer to second partition on the upper surface for making the second opening 112 There is the mode of lower level height to be obliquely installed for 120 position.The lower surface of second opening 112 can be according to making second to open Closer to the position of second partition 120 there is the mode of higher level height to be obliquely installed relatively on the lower surface of mouth 112. The present invention at least can be realized following advantageous effects using this mode: the inclination of the upper surface of the first, the second opening 112 is set The mode of setting facilitates gas and activated sludge and flows into from the second opening 112;The inclination of the lower surface of the second, the second opening 112 is set The mode of setting facilitates activated sludge disposed thereon and more swimmingly enters two under the collective effect of weight component and external pressure Between block first partition 110, and the gas stripping for lodging the bubble between first partition 110 moves upwards.
According to a preferred embodiment, each first partition 110 can be equipped with the of at least one intersecting therewith setting Two partitions 120.
According to a preferred embodiment, each first partition 110 can be equipped with intersecting therewith at least two second every Plate 120.Between at least two second partitions 120 intersected with each first partition 110 can be on different level height directions Every setting, to allow the sewage for having amount of activated sludge to flow in different level height sides upwards about corresponding second partition 120 It is dynamic to form circulation.
According to a preferred embodiment, at least two second partitions 120 intersected with each first partition 110 are in direction Horizontal plane can have identical projection width when projecting.In other words, when being projected towards horizontal plane, with each The projection width in second partition 120 relatively above can wait at least two second partitions 120 of one partition 110 intersection In the projection width of the second partition 120 in opposite lower section.
According to a preferred embodiment, at least two second partitions 120 intersected with each first partition 110 are in direction Horizontal plane can have floor projection width different from each other when projecting, to allow from intersecting with each first partition 110 At least two second partitions 120 fall activated sludge plummet face different from each other lose the support of second partition 120 and after It is continuous to fall.The present invention at least can be realized following advantageous effects using this mode: first, it can be in different space planes The upper circulation for forming activated sludge;Second, it can allow amount of activated sludge quickly circulation.
According to a preferred embodiment, it is at least two second partitions 120 intersected with each first partition 110 The floor projection width of second partition 120 relatively above can be greater than the horizontal of the second partition 120 in opposite lower section and throw Shadow width.
According to a preferred embodiment, it is at least two second partitions 120 intersected with each first partition 110 The floor projection width of second partition 120 relatively above can be less than the horizontal of the second partition 120 in opposite lower section and throw Shadow width.Preferably, the size for first opening 111 corresponding with each second partition 120 being arranged in first partition 110 can be with It is related to the floor projection width of the second partition 120, the second partition 120 corresponding the with bigger floor projection width One opening 111 can be bigger.For example, in opposite at least two second partitions 120 intersected with each first partition 110 The floor projection width of the second partition 120 of top is greater than the floor projection width of the second partition 120 in opposite lower section In the case of, in second partition 120 relatively above at least two second partitions 120 that intersect with each first partition 110 Corresponding first opening 111 can be bigger than the opening of second partition 120 corresponding first 111 in opposite lower section.Preferably, The size of one opening 111 can refer to the opening section size of the first opening 111.
Preferably, the size for second opening 112 corresponding with each second partition 120 being arranged in first partition 110 can With related to the floor projection width of the second partition 120, the second partition 120 with bigger floor projection width is corresponding Second opening 112 can be bigger.For example, being in phase at least two second partitions 120 intersected with each first partition 110 It is greater than the floor projection width of the second partition 120 in opposite lower section to the floor projection width of the second partition 120 of top In the case where, in second partition relatively above at least two second partitions 120 that intersect with each first partition 110 120 corresponding second openings 112 can be bigger than the opening of second partition 120 corresponding second 112 in opposite lower section.It is preferred that The size on ground, the second opening 112 can refer to the opening section size of the second opening 112.
According to a preferred embodiment, it is at least two second partitions 120 intersected with each first partition 110 The level height of the top edge of the second partition 120 of opposite lower section can be lower than under second partition 120 relatively above The level height at edge.Preferably, at least two second partitions 120 intersected with each first partition 110 are towards plummet face Projection when projection can be overlapped.Preferably, at least two second partitions 120 intersected with each first partition 110 The top edge of second partition 120 in opposite lower section and lower edge in second partition 120 relatively above are in plummet side To distance range can be 0.4~2m, such as desirable 0.5m, 1m or 1.5m.Preferably, with each 110 phase of first partition The top edge of second partition 120 in opposite lower section at least two second partitions 120 handed over and in the relatively above Distance of the lower edge of two partitions 120 in plummet direction can be equal at least two second intersected with each first partition 110 The 0.5 of the sum of plate length in partition 120 in the second partition 120 of lower section relatively and in second partition 120 relatively above ~1.5 times.Preferably, the long linear distance that can be its top edge to its lower edge of the plate of single second partition 120.The present invention Following advantageous effects at least can be realized using this mode: first, it reduces between two pieces of adjacent second partitions 120 up and down The circulation of formation it is interfering with each other;Second, if there is incrustation, when clearing up incrustation, upper and lower two pieces adjacent second partitions 120 It does not block, is convenient to clean each other.
According to a preferred embodiment, 111 top of the first opening of first partition 110 can be equipped with chock flap 300.Resistance Gas plate 300 can by with first partition 110 at angle in a manner of intersect with each other.Separate corresponding the first of each chock flap 300 One end of partition 110 may be at the lower section for the other end of each chock flap 300 intersected with corresponding first partition 110.Or Person says that one end of corresponding chock flap 300 can connect in first partition 110.The other end of corresponding chock flap 300 can prolong It extends to and is flushed with the lower edge of corresponding first opening 111 or the other end of corresponding chock flap 300 extends to corresponding the Below the lower edge of one opening 111.Thus, it is possible to reduce and/or prevent the bubble within each pair of first partition 110 to open from first Mouth 111 escapes out and influences the air lift effect in each pair of first partition 110.
According to a preferred embodiment, the lower edge of each second partition 120 can be extended downward into and corresponding The lower edge of two openings 112 flushes or the lower edge of each second partition 120 extends downward into corresponding second opening 112 Below lower edge.The present invention at least can be realized following advantageous effects using this mode: first, it can reduce and/or hinder Only the bubble within each pair of first partition 110 escapes out from the second opening 112 and influences the air lift in each pair of first partition 110 Effect;The lower edge of the second, the second opening 112 opens to obtain the too deep formation that also will affect the circulation around second partition 120 and circulation Speed, therefore, the preferred embodiment also can help to be formed around second partition 120 circulation and guarantee around second partition The speed of 120 circulation improves oxygen transfer efficiency.
The first acute angle according to a preferred embodiment, between second partition 120 and corresponding first partition 110 Q1 can be 30 °~80 °, particularly preferred 40 °~70 °, most preferably 50~60 °.
The second acute angle Q2 according to a preferred embodiment, between chock flap 300 and corresponding first partition 110 It can be 30 °~80 °, particularly preferred 40 °~70 °, most preferably 50~60 °.Preferably, the size of the second acute angle Q2 and the The size of one acute angle Q1 is identical.
According to a preferred embodiment, one end far from corresponding first partition 110 of second partition 120 can be set There is guidance dog-ear K1.Guidance dog-ear K1 can be arranged in the way of one end bending downward for making second partition 120.Guide dog-ear The bending angle of K1 can be greater than 180 ° plus the sum of first acute angle Q1.The present invention use this mode at least and can be realized with Lower advantageous effects: first, which makes even if there are bendings, but second partition 120 of the invention is another One end will not be still hidden under the other parts of second partition 120, so that the activity in the upper direction of second partition 120 is dirty Mud quickly glides because of the change of pitch angle of seating surface after moving at guidance dog-ear K1 but is not directly in plummet direction diameter It directly falls, has guiding function to the activated sludge in opposite rear, activated sludge is enable quickly to glide;The second, the The bending part of two partitions 120 can also generate guiding function to the bubble of 120 lower section of second partition, reduce bubble from second partition A possibility that 120 edge outflow.
According to a preferred embodiment, guide at least part of the one side directed downwardly of dog-ear K1 that can be attached with and can use In providing the carbon fiber layer X1 for hanging attached place for microorganism.During carbon fiber layer X1 can be bolted, rivets and be bonded At least one mode is connected to second partition 120.The present invention at least can be realized following advantageous effects using this mode: the One, the presence of carbon fiber layer X1, allow guidance dog-ear K1 one side directed downwardly roughness with higher, there is no biofilm situation Under, preferable decelerating effect can be still played to the bubble moved to herein, reduce marginal flow of the bubble from second partition 120 Out a possibility that;Second, in the operation of water process, since material is covered with the presence of the carbon fiber layer X1 of micropore, surface meeting Microbial film is mounted, mycelia, which extends downwardly, to be hung from above, so that circulation waste water can be recycled via carbon during the circulation of second partition The microbial film mounted on fibrous layer X1 is aoxidized, and oxidation effectiveness is more preferable;Third, extending downwardly the mycelia hung from above also can be into One step reduces a possibility that bubble is flowed out from the edge of second partition 120.
According to a preferred embodiment, one end far from corresponding first partition 110 of chock flap 300 can be equipped with arc Shape crimping K2.Arc crimping K2 can exist according to allowing the following table along chock flap 300 to face away from the bubble that first partition 110 moves Have the tendency that the mode moved towards first partition 110 is arranged after arc crimping K2.The present invention at least can using this mode It realizes following advantageous effects: a possibility that bubble is escaped from from chock flap 300 can be further reduced.
Preferably, the arc crimping K2 of chock flap 300 can be based on according to that can allow in the activated sludge of arc crimping K2 The mode that gravity is flowed out out of arc crimping K2 is arranged.
According to a preferred embodiment, circulation oxidation reactor LR may include controller.Controller can be according to energy The mode of the independent aeration quantity for adjusting each first aerator 210 and the second aerator 220 is arranged.
Embodiment 2
The present embodiment can be the further improvement and/or supplement to embodiment 1, and duplicate content repeats no more.Not It causes in conflict or contradictory situation, the entirety and/or partial content of the preferred embodiment of other embodiments can be used as The supplement of the present embodiment.Present embodiment discloses one kind efficiently to propose mark method, in other words a kind of method for treating water, a kind of in other words Wastewater treatment method, this method can be realized by system of the invention and/or other alternative components.For example, by making Method of the invention is realized with each components in system of the invention.
According to a preferred embodiment, this method may include: to carry out water process using aforementioned system.
According to a preferred embodiment, this method may include: to be carried out at water using aforementioned circulation oxidation reactor LR Reason.
Embodiment 3
The present embodiment can be to embodiment 1,2 or its further improvement and/or supplement for combining, and duplicate content is not It repeats again.In the case where not causing conflict or contradictory situation, in the entirety of the preferred embodiment of other embodiments and/or part Hold the supplement that can be used as the present embodiment.
According to a preferred embodiment, referring to Fig. 6, which may include conditioning tank A, anoxic pond B, anaerobic pond F, good Oxygen pond C, sedimentation basin D, at least one of device for mark G, sand filter H and clear water reserviors E are efficiently mentioned.Clear water reserviors E can be set in sand The downstream filter H.Sand filter H, which can be set, is efficiently mentioning the downstream device for mark G.Efficiently mentioning device for mark G can be set at sedimentation basin D Trip.Aerobic tank C can be set in the downstream of anaerobic pond F.Anaerobic pond F can be set in the downstream of anoxic pond B.Anoxic pond B can be with The downstream of conditioning tank A is set, circulation oxidation reactor LR is provided in the aerobic tank C.Aerobic tank C will be in anoxic pond B Water inputs in sedimentation basin D after the oxidation of the circulation of circulation oxidation reactor LR.Circulation oxidation reactor LR may include several Circulation partition 100 and several aerators 200.Aerator provides gas in the side of circulation partition 100, allows activated sludge around at least One piece of circulation separator flow forms circulation.The present invention at least can be realized following advantageous effects using this mode: the present invention The oxygen transfer efficiency and dissolved oxygen performance efficiently mentioned in the aerobic tank of device for mark can be preferably improved, device for mark and sand filter are efficiently mentioned More effectively remove the organic matter and suspended matter in water removal.
Word " module " as used herein describes any hardware, software or combination thereof, is able to carry out and " mould The associated function of block ".
It should be noted that above-mentioned specific embodiment is exemplary, those skilled in the art can disclose in the present invention Various solutions are found out under the inspiration of content, and these solutions also belong to disclosure of the invention range and fall into this hair Within bright protection scope.It will be understood by those skilled in the art that description of the invention and its attached drawing are illustrative and are not Constitute limitations on claims.Protection scope of the present invention is defined by the claims and their equivalents.

Claims (10)

1. a kind of circulation oxidation reactor, which is characterized in that including several circulation partitions (100) and several aerators (200), expose Gas device circulation partition (100) side provide gas, allow circulation partition (100) side at least partly activated sludge by gas It mentions and moves up, at least partly a part of activated sludge is being pressed behind the top edge of corresponding circulation partition (100) Under the action of difference from the side of circulation partition (100) move to circulation partition (100) the other side and based on gravity from circulation every The other side of plate (100) falls, and a part of the activated sludge to fall from the other side of circulation partition (100) is moving to circulation It is stripped again behind the side of partition (100), to allow the sewage for having activated sludge to flow shape around corresponding circulation partition (100) At circulation.
2. circulation oxidation reactor as described in claim 1, which is characterized in that several circulation partitions (100) are at least wrapped It includes a pair of of first partition (110), several aerators (200) include at least the first aerator (210), each pair of first partition (110) In two first partitions (110) be intervally installed, under the first aerator (210) is between each pair of first partition (110) Fang Tongqi is to allow at least part in the sewage for having activated sludge that can form ring around corresponding first partition (110) flowing Stream,
Several circulation partitions (100) further include at least one second partition (120), several aerators (200) further include to Few second aerator (220), the second partition (120) by with first partition (110) at angle in a manner of intersect with each other, And each second partition (120) far from corresponding first partition (110) one end be in each second partition (120) with The lower section of the other end of corresponding first partition (110) intersection, in intersecting with second partition (120) for first partition (110) The top of position is equipped with the first opening (111), in the lower section for the position of first partition (110) intersected with second partition (120) Equipped with the second opening (112), each second partition (120) is furnished at least one second aerator (220), corresponding second aeration Device (220) is ventilated below the corresponding second partition (120), to allow in each pair of first partition (110) the amount of activated dirt flowed Mud under the action of behind the top edge of corresponding second partition (120) in pressure difference by it is corresponding first opening (111) from The side of first partition (110) moves to the other side of second partition (120) and is based on gravity from the another of second partition (120) Side fall, from the other side of second partition (120) fall activated sludge in a part of activated sludge move to second every The bubble air lift discharged again by the second aerator (220) behind the side of plate (120) enters by corresponding second opening (112) Position between two first partitions (110), to allow the sewage for having activated sludge to flow around corresponding second partition (120) Form circulation.
3. the circulation oxidation reactor as described in one of preceding claims, which is characterized in that each first partition (110) is equipped with Intersecting therewith at least two second partitions (120), at least two second partitions intersected with each first partition (110) (120) it is spaced setting, on different level height directions to make the sewage for having amount of activated sludge high in different levels Degree side forms circulation upwards about corresponding second partition (120) flowing.
4. the circulation oxidation reactor as described in one of preceding claims, which is characterized in that with each first partition (110) phase At least two second partitions (120) handed over when being projected towards horizontal plane with floor projection width different from each other, In, in second partition relatively above at least two second partitions (120) that intersect with each first partition (110) (120) floor projection width is greater than the floor projection width of the second partition (120) in opposite lower section.
5. the circulation oxidation reactor as described in one of preceding claims, which is characterized in that be arranged in first partition (110) The size of the first opening (111) corresponding with each second partition (120) and the floor projection width phase of the second partition (120) It closes, there is the bigger of corresponding first opening (111) of the second partition (120) of bigger floor projection width;And/or
Be arranged in first partition (110) it is corresponding with each second partition (120) second opening (112) size and this second The floor projection width of partition (120) is related, and the second partition (120) corresponding second with bigger floor projection width is opened Mouthful (112) it is bigger.
6. the circulation oxidation reactor as described in one of preceding claims, which is characterized in that under each second partition (120) Edge is extended downward into be flushed or the lower edge of each second partition (120) with the lower edge of corresponding second opening (112) Extend downward into the lower edge of corresponding second opening (112) or less.
7. the circulation oxidation reactor as described in one of preceding claims, which is characterized in that the first of first partition (110) opens Be equipped with chock flap (300) above mouthful (111), the chock flap (300) by with first partition (110) at angle in a manner of phase each other Hand over, and each chock flap (300) far from corresponding first partition (110) one end be in each chock flap (300) with The lower section of the other end of corresponding first partition (110) intersection, and the other end of corresponding chock flap (300) extend to it is right The lower edge for the first opening (111) answered flushes or the other end of corresponding chock flap (300) extends to corresponding first and opens Below the lower edge of mouth (111).
8. the circulation oxidation reactor as described in one of preceding claims, which is characterized in that the separate of chock flap (300) corresponds to First partition (110) one end be equipped with arc crimping (K2), arc crimping (K2) is according to the lower surface allowed along chock flap (300) Having the tendency that moving towards first partition (110) after arc crimping (K2) towards the bubble far from first partition (110) movement Mode be arranged.
9. a kind of efficiently mention mark system, which is characterized in that include at least conditioning tank (A), anoxic pond (B), aerobic tank (C), precipitating Pond (D) and clear water reserviors (E), clear water reserviors (E) setting are arranged at anoxic pond (B) in the downstream of sedimentation basin (D), aerobic tank (C) Trip, anoxic pond (B) setting are provided with circulation oxidation reactor, aerobic tank in the downstream of conditioning tank (A), the aerobic tank (C) (C) water in anoxic pond (B) is inputted in sedimentation basin (D) after the oxidation of the circulation of circulation oxidation reactor;
Wherein, circulation oxidation reactor includes several circulation partitions (100) and several aerators (200), aerator circulation every The side of plate (100) provides gas, and at least partly activated sludge of the side of circulation partition (100) is allowed to be stripped and Xiang Shangyi It is dynamic, at least partly a part of activated sludge behind the top edge of corresponding circulation partition (100) under the action of pressure difference The other side of circulation partition (100) is moved to from the side of circulation partition (100) and is based on gravity from the another of circulation partition (100) Side falls, and a part of the activated sludge to fall from the other side of circulation partition (100) is moving to circulation partition (100) It is stripped again behind side, to allow the sewage for having activated sludge to form circulation around the flowing of corresponding circulation partition (100).
10. efficiently mentioning mark system as claimed in claim 9, which is characterized in that several circulation partitions (100) include at least A pair of of first partition (110), several aerators (200) include at least the first aerator (210), in each pair of first partition (110) Two first partitions (110) be intervally installed, lower section of the first aerator (210) between each pair of first partition (110) It ventilates to allow at least part in the sewage for having activated sludge that can form circulation around corresponding first partition (110) flowing,
Several circulation partitions (100) further include at least one second partition (120), several aerators (200) further include to Few second aerator (220), the second partition (120) by with first partition (110) at angle in a manner of intersect with each other, And each second partition (120) far from corresponding first partition (110) one end be in each second partition (120) with The lower section of the other end of corresponding first partition (110) intersection, in intersecting with second partition (120) for first partition (110) The top of position is equipped with the first opening (111), in the lower section for the position of first partition (110) intersected with second partition (120) Equipped with the second opening (112), each second partition (120) is furnished at least one second aerator (220), corresponding second aeration Device (220) is ventilated below the corresponding second partition (120), to allow in each pair of first partition (110) the amount of activated dirt flowed Mud under the action of behind the top edge of corresponding second partition (120) in pressure difference by it is corresponding first opening (111) from The side of first partition (110) moves to the other side of second partition (120) and is based on gravity from the another of second partition (120) Side fall, from the other side of second partition (120) fall activated sludge in a part of activated sludge move to second every The bubble air lift discharged again by the second aerator (220) behind the side of plate (120) enters by corresponding second opening (112) Position between two first partitions (110), to allow the sewage for having activated sludge to flow around corresponding second partition (120) Form circulation.
CN201910365783.6A 2019-04-30 2019-04-30 Efficient label lifting system Active CN110002688B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910365783.6A CN110002688B (en) 2019-04-30 2019-04-30 Efficient label lifting system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910365783.6A CN110002688B (en) 2019-04-30 2019-04-30 Efficient label lifting system

Publications (2)

Publication Number Publication Date
CN110002688A true CN110002688A (en) 2019-07-12
CN110002688B CN110002688B (en) 2021-11-30

Family

ID=67175494

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910365783.6A Active CN110002688B (en) 2019-04-30 2019-04-30 Efficient label lifting system

Country Status (1)

Country Link
CN (1) CN110002688B (en)

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2011795A (en) * 1978-01-06 1979-07-18 Hartley Simon Ltd Aeration of Liquids
WO2004043866A1 (en) * 2002-11-13 2004-05-27 Jai-Hun Lee Apparatus for the biological treatment of wastewater
CN1807281A (en) * 2006-02-08 2006-07-26 江南大学 circulating type aerobe reactor for treating organic waste
CN1911835A (en) * 2006-08-29 2007-02-14 华南理工大学 Sequential air lifting circulation waste water biological treatment reactor and its process
CN101045581A (en) * 2007-04-27 2007-10-03 浙江大学 Treating device for sludge self-return aerobic bios
CN101062810A (en) * 2007-04-24 2007-10-31 张文虎 Biological cycle moving bed sewage treatment system and method thereof
CN201003003Y (en) * 2006-10-23 2008-01-09 深圳清华大学研究院 Reaction-deposition integral rectangle circulating bioreactor sludge treatment device
CN201045130Y (en) * 2007-04-27 2008-04-09 浙江大学 Sludge self-refluxing aerobic organisms processing unit
CN201605196U (en) * 2009-12-01 2010-10-13 王小华 Internal circulation AO bioreactor
CN105461166A (en) * 2015-11-26 2016-04-06 湖南万净环保科技有限公司 Enhanced biological treatment and reusing device and method for high-concentration refractory organic industrial wastewater
CN109607757A (en) * 2019-01-03 2019-04-12 深圳市深水水务咨询有限公司 A kind of self-loopa bio-contact oxidation High-rate sedimentation reactor

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2011795A (en) * 1978-01-06 1979-07-18 Hartley Simon Ltd Aeration of Liquids
WO2004043866A1 (en) * 2002-11-13 2004-05-27 Jai-Hun Lee Apparatus for the biological treatment of wastewater
CN1807281A (en) * 2006-02-08 2006-07-26 江南大学 circulating type aerobe reactor for treating organic waste
CN1911835A (en) * 2006-08-29 2007-02-14 华南理工大学 Sequential air lifting circulation waste water biological treatment reactor and its process
CN201003003Y (en) * 2006-10-23 2008-01-09 深圳清华大学研究院 Reaction-deposition integral rectangle circulating bioreactor sludge treatment device
CN101062810A (en) * 2007-04-24 2007-10-31 张文虎 Biological cycle moving bed sewage treatment system and method thereof
CN101045581A (en) * 2007-04-27 2007-10-03 浙江大学 Treating device for sludge self-return aerobic bios
CN201045130Y (en) * 2007-04-27 2008-04-09 浙江大学 Sludge self-refluxing aerobic organisms processing unit
CN201605196U (en) * 2009-12-01 2010-10-13 王小华 Internal circulation AO bioreactor
CN105461166A (en) * 2015-11-26 2016-04-06 湖南万净环保科技有限公司 Enhanced biological treatment and reusing device and method for high-concentration refractory organic industrial wastewater
CN109607757A (en) * 2019-01-03 2019-04-12 深圳市深水水务咨询有限公司 A kind of self-loopa bio-contact oxidation High-rate sedimentation reactor

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张玉魁: "高效分离生物流化复合反应器的研究", 《中国优秀博士学位论文全文数据库工程科技I辑》 *

Also Published As

Publication number Publication date
CN110002688B (en) 2021-11-30

Similar Documents

Publication Publication Date Title
JP5749731B2 (en) Sewage treatment equipment
JP5665307B2 (en) Organic waste water treatment apparatus and organic waste water treatment method
CN102659227A (en) Middle-set type high density sediment water purification tank and purification technology thereof
US5217609A (en) Combination sludge collector, aerator, and return pump
US3879285A (en) Aerobic sewage treatment system
CA1265266A (en) Method and apparatus for biological aerobic wastewater treatment
CN108328786A (en) A kind of water treatment facilities and method for treating water
CN105439286B (en) A kind of vertical current sewage ecological treatment system
CN100540486C (en) Synchronous denitrification and dephosphorization process for city sewage
JP2006075839A5 (en)
JP2006075839A (en) Method for primary treatment of organic sewage and device therefor
CN110002688A (en) It is a kind of efficiently to mention mark system
KR20080105445A (en) Improved secondary sedimentation basins of biological sewage and waste water treatment plant
CN214880824U (en) Integrated iron-carbon micro-electrolysis wastewater treatment device
CN207313243U (en) A kind of micro- oxygen-short-cut denitrification oxidation ditch
CN205419912U (en) Circulatingly oxygenate biochemical ware
CN113387425A (en) Air flotation device based on air-borne flocs
JP2523295B2 (en) Wastewater treatment device with side channel type fining tank
CN111777178A (en) Vertical oxidation ditch micro-power water treatment system
CN220788253U (en) SBR sewage treatment equipment
CN215756921U (en) Air-lift circulation reaction device
CN105668779A (en) Circular-oxygenation biochemical device
JP7178082B2 (en) Stirring tank
CN110002687A (en) One kind is circulating efficiently to mention mark system
KR200188801Y1 (en) A scum treatment structure for a septic tank

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant