CN212712935U - Circular integrated vertical flow labyrinth structure and sewage treatment device and system - Google Patents
Circular integrated vertical flow labyrinth structure and sewage treatment device and system Download PDFInfo
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- CN212712935U CN212712935U CN202022192992.6U CN202022192992U CN212712935U CN 212712935 U CN212712935 U CN 212712935U CN 202022192992 U CN202022192992 U CN 202022192992U CN 212712935 U CN212712935 U CN 212712935U
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Abstract
The utility model provides a circular integration vertical current labyrinth structure and sewage treatment plant, system, this structure include circular shape processing tank, be located the vertical baffle in the processing tank and be used for controlling sewage and be in processing tank medium mobile control system, vertical baffle will anaerobic zone, anoxic zone, aerobic zone and settling zone are cut apart into to the processing tank, anaerobic zone front end extremely be equipped with the baffling passageway between the aerobic zone front end. The utility model provides a circular integration vertical current labyrinth structure has structurally prolonged the dwell time in anaerobic zone and anoxic zone greatly, through the control backward flow, has guaranteed the high concentration activated sludge in anaerobic zone, anoxic zone. In the flow state environment, the activated sludge particles are fully utilized to carry out biochemical reaction, and the aim of efficiently removing nitrogen and phosphorus is fulfilled.
Description
Technical Field
The utility model relates to an environmental protection technology field, concretely relates to circular integrated vertical current labyrinth structure and sewage treatment plant, system.
Background
China is a large water-consuming country, but the water pollution is also very serious. At present, most local sewage is collected and treated in a centralized collection and treatment mode, but residential areas such as residential districts and rural gathering areas built by remote industrial and mining enterprises and towns are far away, and domestic sewage generated by the urban sewage treatment plant can only adopt simple sewage treatment modes such as septic tanks and the like and cannot reach stricter and stricter sewage discharge standards because the urban sewage treatment plant is far away. Especially, the construction of sewage treatment facilities and pipe networks in vast rural areas and small towns in China is seriously lagged, a large amount of sewage is incompletely treated, even the treated domestic sewage is not directly discharged, and great burden is caused to the ecological environment of local water resources.
The biochemical method for treating sewage is a common sewage treatment method, and the method utilizes the metabolism function of microorganisms to decompose and oxidize organic matters in a dissolved or colloidal state into stable inorganic substances so as to purify the sewage. The activated sludge needs to be kept suspended in the treatment process and cannot be settled to the bottom of the tank. In most sewage treatment processes by a biochemical method, submersible mixers are arranged at the bottoms of an anaerobic zone and an anoxic zone, the submersible mixers usually run continuously to prevent activated sludge from depositing, an aeration device is arranged at the bottom of the aerobic zone, aeration is provided by a fan, the aeration fan usually runs continuously, a nitrifying liquid reflux pump is arranged at the bottom, sludge in the aerobic zone flows back to the anoxic zone, sludge and water are separated in a settling zone, and a sludge reflux pump is arranged at the bottom of a pool to flow back the settled sludge to the anaerobic zone. For guaranteeing normal operation, the traditional integrated sewage treatment equipment needs 2 submersible mixers, 1 fan and 2 reflux pumps at least.
However, above-mentioned sewage treatment device is because aeration pipe and dive agitator motor install in the pond for sewage treatment device construction cost risees, needs unscheduled maintenance to it simultaneously, and first-selected needs will shift out the activated sludge in each pond during overhaul and maintenance of equipment, perhaps take out dive agitator motor from the pond in, maintain again, and the maintenance operation is complicated, and has increased the maintenance cost of equipment, has seriously reduced sewage treatment device's rate of utilization. Meanwhile, the maintenance of the sewage treatment facility needs professional technical management personnel, and the problems of low management level, large fluctuation of sewage treatment effect, difficult maintenance and the like are caused by the lack of the professional technical management personnel and the like.
SUMMERY OF THE UTILITY MODEL
The present invention is made to solve the above problems, and an object of the present invention is to provide a circular integrated vertical flow labyrinth structure.
Realize the utility model discloses the technical scheme of purpose as follows: the utility model provides a circular integrated vertical flow labyrinth structure, which comprises a circular treatment tank, a vertical clapboard positioned in the treatment tank and a control system used for controlling the sewage to flow in the treatment tank, the vertical clapboard divides the treatment tank into an anaerobic zone, an anoxic zone, an aerobic zone and a sedimentation zone, a baffling channel is arranged between the front end of the anaerobic zone and the front end of the aerobic zone, wherein the baffling channel is provided with a plurality of guide plates which are divided into an upper guide plate and a lower guide plate, the upper guide plate and the lower guide plate are arranged at intervals, the upper guide plate and the lower guide plate divide the baffling channel into a plurality of baffling tanks which are communicated in sequence, the upper guide plate is fixedly connected with the bottom and the side wall of the treatment tank, the height of the upper guide plate is lower than that of the side wall of the treatment tank, and the upper guide plate and the side wall of the treatment tank form an upper overthrow channel for sewage to pass through; the lower guide plate is fixedly connected with the side wall of the treatment tank, and a lower channel through which sewage passes is formed between the lower end of the lower guide plate and the bottom of the guide wall; the top heights of the adjacent upper guide plate and the lower guide plate are gradually reduced from the front end of the anaerobic zone to the front end of the aerobic zone, and the distance between the lower end of the lower guide plate and the bottom of the treatment tank is 5-500 mm.
The utility model provides a circular integrated vertical flow maze structure can also have such characteristic: the guide plate between the aerobic zone and the anoxic zone is an upper guide plate.
The utility model provides a circular integrated vertical flow maze structure can also have such characteristic: the control system includes: the aeration unit is arranged in the aerobic zone and is used for aeration of the aerobic zone; the reflux unit is used for carrying out multi-point reflux among the anaerobic zone, the anoxic zone, the aerobic zone and the precipitation zone; the online monitoring unit is arranged in the aerobic zone and used for monitoring the working data of the aerobic zone; and the control unit is connected with the aeration unit, the backflow unit and the online monitoring unit and used for generating a working command for controlling the aeration unit and the backflow unit according to the received working data monitored by the online monitoring unit.
The utility model provides a circular integrated vertical flow maze structure can also have such characteristic: the reflux unit comprises one or more selected from the following reflux pipes, a first reflux pipe is arranged between the anoxic zone and the anaerobic zone and is used for refluxing from the tail end of the anoxic zone to the front end of the anaerobic zone; the second return pipe is arranged in the anoxic zone and is used for returning from the bottom of the rear end of the anoxic zone to the front end of the anoxic zone; the third return pipe is arranged between the aerobic zone and the anoxic zone and is used for returning from the aerobic zone to the front end of the anoxic zone; the fourth return pipe is arranged between the sedimentation zone and the anoxic zone and is used for returning from the bottom of the sedimentation zone to the front end of the anoxic zone; and the fifth return pipe is arranged between the settling zone and the aerobic zone and is used for returning from the bottom of the settling zone to the aerobic zone.
The utility model provides a circular integrated vertical flow maze structure can also have such characteristic: the backflow unit further comprises a fan, and the fan is used for providing backflow power of the backflow unit.
The utility model provides a circular integrated vertical flow maze structure can also have such characteristic: the control system also comprises a solenoid valve group box, and the solenoid valve group box is connected with the aeration unit, the backflow unit and the control unit and is used for executing the working command sent by the control unit.
The utility model provides a circular integrated vertical flow maze structure can also have such characteristic: the control unit controls the aeration intensity and the aeration time of the aeration unit and the reflux intensity and the reflux time of the reflux unit.
Another object of the present invention is to provide a sewage treatment apparatus having the above-mentioned features, wherein the sewage treatment apparatus comprises any of the above-mentioned circular integrated vertical flow labyrinth systems.
An object of the utility model is also to provide a sewage treatment system, have such characteristic, sewage treatment system includes foretell sewage treatment plant.
Compared with the prior art, the beneficial effects of the utility model are that:
1. the utility model provides a circular integrated vertical flow maze structure has structurally prolonged the flow in anaerobic zone and anoxic zone greatly, eliminates the adverse effect of backward flow activated sludge to anaerobic zone and anoxic zone to improve its denitrogenation efficiency by a wide margin, be favorable to the dephosphorization simultaneously, control and adaptation anaerobic zone, anoxic zone are to the utilization of carbon source.
2. The utility model provides a circular integration vertical current labyrinth structure, the operation process is whole to be accomplished according to online check out test set collection data automatic control by the control unit, and operation process full automation need not artificial interference, at equipment operation in-process, need not to be equipped with professional technical personnel and carries out manual operation, has saved the manual work, has reduced the running cost.
3. The utility model provides a circular integration vertical current labyrinth structure's operation mode is program control, and aeration intensity and duration through the continuous adjustment operation procedure of on-line measuring equipment detection numerical value carry out intermittent type procedure operation according to on-line measuring equipment detection data in equipment operation, and many power equipment continuous operation in the non-conventional equipment, energy saving and consumption reduction more.
4. The utility model provides a circular integrated vertical current labyrinth structure need not to set up the equalizing basin, vertical current labyrinth structure is optimized from pool type structure and operation management two aspects, entire system is the operation under high sludge concentration, possess impact load resistance's ability completely, saved the civil engineering investment that dwell time is 8-12 hours' equalizing basin, the field occupation of land is nervous, the time limit for a project is short, the material can reuse, civil engineering accounts for a short time, civil engineering professional expense can reduce, the time limit for a project is less by the civil engineering restriction.
5. The utility model provides a short and the mud performance height of acclimatization time are cultivateed to technology mud of circular integration vertical current labyrinth structure, and the specially adapted is influenced by the vacation like school, hotel etc. and the crisscross condition in busy season. When the school learns again and the hotel enters the busy season, the normal time from starting to running of the vertical flow maze structure system is short.
Drawings
FIG. 1 is a reaction flow diagram of a vertical flow labyrinth arrangement provided by the present invention;
FIG. 2 is a schematic view of a circular integrated vertical flow labyrinth structure provided in an embodiment of the present invention;
fig. 3 is an expanded view of a baffle channel provided in an embodiment of the present invention;
wherein, 1: a treatment tank; 2: a vertical partition plate; 3: an aerobic zone; 4: a deflection channel; 5: a baffle; 51: a lower deflector; 52: an upper deflector; 6: a precipitation zone.
Detailed Description
The invention will be further described with reference to the accompanying drawings and specific embodiments, and the advantages and features of the invention will become more apparent as the description proceeds. These examples are merely illustrative and do not limit the scope of the invention in any way. It will be understood by those skilled in the art that various changes in form and details may be made therein without departing from the spirit and scope of the invention, and that such changes and modifications are intended to be included within the scope of the invention.
In the description of the present embodiments, it should be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", etc. indicate orientations or positional relationships based on those shown in the drawings, and are only for convenience of describing the present invention and simplifying the description, but do not indicate or imply that the device or element referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the invention.
Furthermore, the terms "first," "second," "third," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicit to a number of indicated technical features. Thus, a feature defined as "first," "second," etc. may explicitly or implicitly include one or more of that feature. In the description of the invention, unless otherwise specified, "a plurality" means two or more.
As shown in fig. 1, the vertical flow labyrinth process is a reaction flow diagram of an integrated vertical flow labyrinth structure, and is characterized in that vertical guide plates are arranged in an anaerobic zone and an anoxic zone, the anaerobic zone and the anoxic zone are divided into a plurality of reaction chambers connected in series with vertical flow, and each reaction chamber is a relatively independent up-down flow type sludge bed system. The principle of the process is that the structures of the anaerobic zone and the anoxic zone adopt a vertical flow labyrinth structure, and a plurality of downflow and upflow sludge beds are connected in series at intervals. The water inlet mode of the VFL combined tank is pulse type water inlet, so that in the upward-flowing cells, sludge forms a suspended sludge bed due to the upward flow velocity of sewage when water enters, part of sludge enters the next downward-flowing cell along with the water flow, and most of sludge is remained in the cells due to the action of gravity in the state of stopping water inlet, so that the structure ensures that the anaerobic anoxic zone keeps high sludge concentration, and the reaction efficiency of the unit tank volume is greatly improved. Particularly, the high-concentration sludge system can take the high-concentration sludge system as a supplementary carbon source under the condition of low water temperature in the northeast in winter, and overcomes the difficulty of sludge activity reduction at low temperature. The structure furthest prolongs the residence time of the anaerobic zone and the anoxic zone under the condition of the same tank capacity, not only avoids the short flow of sewage in the reaction tank, but also ensures that the sewage is fully contacted and mixed with microorganisms, and prolongs the effective reaction time. It has a unique sludge circulation route. A part of activated sludge in the sludge bucket of the settling zone flows back to the front end of the anoxic zone, the part of sludge has dissolved oxygen, and due to the characteristic of a vertical flow structure, the water flows to the second grid and the third grid of the anoxic zone, the concentration of the dissolved oxygen is rapidly reduced, denitrification is completely carried out in a longer anoxic flow, a carbon source (BOD5) in sewage is fully utilized, and the denitrification rate is far higher than that of denitrification carried out by depending on endogenous respiration. The sludge in the middle of the anoxic zone continuously flows back to the foremost end of the labyrinth grid, and simultaneously the sludge in the anaerobic zone, the anoxic zone and the aerobic zone can all flow back to the front end of the zone from the tail end of the zone, generally, the sludge is continuously conveyed to the front end of the labyrinth grid, the sludge keeps fluidity along the labyrinth grid, and the high sludge concentration is kept due to the upward and downward turning structure of the labyrinth, the sludge concentration of the labyrinth part is 7-8g/L, and the aerobic part is 3-4 g/L.
In the embodiment of the present invention, as shown in fig. 2, the present invention is a circular integrated vertical flow labyrinth structure, which comprises a circular processing tank 1, a vertical partition plate 2 located in the processing tank, and a control system for controlling sewage flowing in the processing tank, wherein the processing tank is divided into an anaerobic zone, an anoxic zone, an aerobic zone 3, and a settling zone 6, which are connected in sequence, by the vertical partition plate 2, a baffling channel 4 is provided between the front end of the anaerobic zone and the front end of the aerobic zone 3, as shown in fig. 3, the baffling channel 4 is provided with a plurality of baffle plates 5, the baffle plates are divided into an upper baffle plate 52 and a lower baffle plate 51, the upper baffle plate 52 and the lower baffle plate 51 divide the baffling channel 4 into a plurality of baffling tanks which are connected in sequence, the upper baffle plate 52 is fixedly connected with the bottom and the side wall of the processing tank 1, and the height of the upper baffle plate 52 is lower than the side wall of the processing tank 1, the upper guide plate 52 and the side wall of the treatment tank 1 form an upper overthrow channel for sewage to pass through; the lower guide plate 51 is fixedly connected with the side wall of the treatment tank 1, and a lower passage for passing sewage is formed between the lower end of the lower guide plate 51 and the bottom of the treatment tank 1. The guide plate between the aerobic zone 3 and the anoxic zone is an upper guide plate 52.
The control system comprises an aeration unit, a reflux unit, an online monitoring unit and a control unit;
an aeration unit provided in the aerobic zone 3 for aeration of the aerobic zone 3;
the reflux unit (comprising 1 or more than one) comprises a first reflux pipe, a second reflux pipe, a third reflux pipe, a fourth reflux pipe and a fifth reflux pipe, and is used for refluxing the sewage among the anaerobic zone, the anoxic zone, the aerobic zone 3 and the sedimentation zone; the first reflux pipe is arranged between the anoxic zone and the anaerobic zone and is used for refluxing from the tail end of the anoxic zone to the front end of the anaerobic zone; the second return pipe is arranged in the anoxic zone and is used for returning from the bottom of the rear end of the anoxic zone to the front end of the anoxic zone; the third return pipe is arranged between the aerobic zone 3 and the anoxic zone and is used for returning the aerobic zone 3 to the front end of the anoxic zone; the fourth return pipe is arranged between the sedimentation zone and the anoxic zone and is used for returning from the bottom of the sedimentation zone to the front end of the anoxic zone; and the fifth return pipe is arranged between the settling zone and the aerobic zone 3 and is used for returning from the bottom of the settling zone to the aerobic zone 3.
The online monitoring unit is arranged in the aerobic zone 3 and used for monitoring the working data of the aerobic zone 3;
and the control unit is connected with the aeration unit, the backflow unit and the online monitoring unit and used for generating a working command for controlling the aeration unit and the backflow unit according to the received working data monitored by the online monitoring unit, and the control unit controls the aeration intensity and the aeration time of the aeration unit and the backflow intensity and the backflow time of the backflow unit.
The working process is as follows:
the sewage to be treated sequentially enters an anaerobic zone, an anoxic zone, an aerobic zone 3 and a settling zone to be subjected to biological deamination and dephosphorization treatment. The sewage is baffled and passed through the baffling channel 4 and sequentially passes through the upper cross-over channel and the lower cross-over channel. Multiple downflow and upflow sludge beds are spaced in series within the deflection channel 4. In the grid which flows upwards, sludge forms a suspended sludge bed due to the upward flow velocity of the sewage, a small part of sludge enters the next grid which flows downwards along with the sewage, most of sludge is remained in the grid due to the action of gravity, the microorganisms convert ammonia nitrogen in the sewage into nitrate nitrogen or nitrite nitrogen under the aerobic condition of the aerobic zone 3, the microorganisms convert the nitrate nitrogen and the nitrite nitrogen into nitrogen under the anoxic condition of the anoxic zone, and the nitrogen is escaped from the water surface to finish denitrification. The dissolved oxygen in water in the anaerobic zone is less than 0.2mg/L, the dissolved oxygen in water in the anoxic zone is less than 0.5mg/L, and the dissolved oxygen in water in the aerobic zone 3 is more than 2 mg/L. An online monitoring unit arranged in the aerobic zone 3 monitors ORP value, namely oxidation-reduction potential, and after transmitting the ORP value to the control unit, the control unit generates different working commands to control the work of the first return pipe, the second return pipe, the third return pipe, the fourth return pipe and the fifth return pipe. The reflux of the first reflux pipe from the tail end of the anoxic zone to the front end of the anaerobic zone, the reflux of the second reflux pipe from the bottom of the rear end of the anoxic zone to the front end of the anoxic zone, the reflux of the third reflux pipe from the aerobic zone 3 to the front end of the anoxic zone, the reflux of the fourth reflux pipe from the bottom of the sedimentation zone to the front end of the anoxic zone and the reflux of the fifth reflux pipe from the bottom of the sedimentation zone to the aerobic zone 3 are controlled. 1 or more of the above refluxes are contained in the sewage treatment device and system.
In the above embodiment, the circular treatment tanks can be reused, the circular structure is stable, the number of equipment is small, and under the condition of large treatment scale, the connection among the circular treatment tanks can be selected for use, so that the circular treatment tank is more suitable for large-scale sewage treatment. The structure ensures that the anaerobic anoxic zone keeps high sludge concentration, generally 6000-8000 mg/L, and greatly improves the reaction efficiency of the treatment tank. Meanwhile, the structure prolongs the flow of the anaerobic zone and the anoxic zone to the maximum extent under the condition of the same tank capacity, not only avoids short flow of sewage in the reaction tank, but also ensures that the sewage is fully contacted and mixed with microorganisms, and prolongs the effective reaction time. Especially, the grid with the ascending flow state eliminates the adverse effect of nitrate in the returned sludge on the environmental states of the anaerobic zone and the anoxic zone, greatly improves the sewage treatment efficiency and the shock resistance, greatly improves the denitrification efficiency, is beneficial to dephosphorization, and controls and adapts to the utilization of carbon sources in the anaerobic zone and the anoxic zone. The control unit is arranged, the operation program is automatically controlled and completed by the control unit according to the data collected by the online detection equipment, the whole operation process is automatic, manual interference is not needed, and in the operation process of the equipment, professional technicians are not needed to perform manual operation, so that the labor is saved, and the operation cost is reduced. The aeration intensity and duration of the automatic operation program are continuously adjusted by detecting the numerical value through the online detection equipment, manual operation of personnel is not needed during the operation of the equipment, and the automation degree is high. And the running period among the programs is calculated by the working data obtained by on-line monitoring, and different programs are carried out in different time, so that the energy consumption is saved.
In another embodiment of the present invention, on the basis of the above embodiment, the backflow unit further includes a fan, and the fan is used for providing a backflow power of the backflow unit.
In the above embodiment, the fan is as the backward flow power supply of backward flow unit, the equipment such as the aeration pipe of installation at the bottom of the pool and dive agitator motor that still needs among the prior art has been solved, still need shift out the activated sludge in each pond when having avoided overhauing the equipment, perhaps take out dive agitator motor from the pond, the complicated operation of maintaining again has reduced the cost of maintaining the maintenance, the while has been solved among the prior art to the required professional technical staff's of maintenance problem, the further cost is reduced.
In another embodiment of the present invention, the control system further comprises a solenoid valve set box, wherein the solenoid valve set box is connected to the aeration unit, the backflow unit and the control unit, and is used for executing the work order sent by the control unit. The electromagnetic valve group box controls the backflow valve group box to execute a backflow program through the control cabinet by means of measurement data of the online measurement equipment, the backflow program controls the first backflow pipe, the second backflow pipe, the third backflow pipe, the fourth backflow pipe and the fifth backflow pipe, and the backflow comprises 1 or more types. The aeration program controls the aeration film at the bottom of the aerobic zone and the aeration film in the sludge zone.
In the above-mentioned embodiment, the utility model provides an inside operation procedure that is equipped with of circular integration vertical current labyrinth structure detects aeration intensity and the duration of numerical value continuous adjustment automatic operation procedure through on-line measuring equipment, need not personnel manually operation in equipment operation, and degree of automation is high.
In another embodiment of the present invention, the settling zone is provided with a mud-water separator and a water outlet tank. The mud-water separator is in an inverted cone shape, the bottom of the mud-water separator faces upwards, the conical top of the mud-water separator is connected with the bottom of the pool, a trapezoidal hole is formed in the side wall of one side of the mud-water separator, a baffle is arranged outside the hole, and a certain angle is formed between the baffle and the side wall for sludge in the aerobic zone 3 to enter. The mud-water separator can be made by welding PP plates or carbon steel plates. The effluent trough is arranged at the upper part of the mud-water separator, the collecting trough is in a long strip shape, and the periphery of the collecting trough is provided with a saw-tooth effluent weir.
In the above embodiment, the end of the settling zone is provided with the mud-water separator, so that the activated sludge and water in the sewage are separated, the water is discharged out of the sewage treatment equipment through the collecting tank, the activated sludge sinks, and the separator is arranged in the inverted cone shape, so that the total backflow of the activated sludge is ensured, and the activated sludge cannot be accumulated in the mud-water separator. The angle of baffle and lateral wall has controlled volume, entering angle and the speed that mud-water mixture got into for sewage can carry out effectual separation in mud-water separator, can not take place the velocity of flow and hang down the import pollution that leads to, perhaps the velocity of flow is too fast produces the torrent, influences sludge sedimentation.
The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modifications, equivalents, improvements and the like made within the spirit and principles of the present invention are intended to be included within the scope of the present invention. The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications and variations can be made without departing from the technical principle of the present invention, and these modifications and variations should also be regarded as the protection scope of the present invention.
Claims (9)
1. The circular integrated vertical flow labyrinth structure is characterized by comprising a circular treatment tank, a vertical partition plate positioned in the treatment tank and a control system for controlling sewage to flow in the treatment tank, wherein the treatment tank is divided into an anaerobic zone, an anoxic zone, an aerobic zone and a sedimentation zone by the vertical partition plate, a baffling channel is arranged between the front end of the anaerobic zone and the front end of the aerobic zone,
wherein,
the baffling channel is provided with a plurality of guide plates which are divided into an upper guide plate and a lower guide plate, the upper guide plate and the lower guide plate are arranged at intervals, the upper guide plate and the lower guide plate divide the baffling channel into a plurality of baffling tanks which are communicated in sequence,
the upper guide plate is fixedly connected with the bottom and the side wall of the treatment tank, the height of the upper guide plate is lower than that of the side wall of the treatment tank, and an upper overthrow channel for passing sewage is formed by the upper guide plate and the side wall of the treatment tank; the lower guide plate is fixedly connected with the side wall of the treatment tank, and a lower channel through which sewage passes is formed between the lower end of the lower guide plate and the bottom of the treatment tank;
the top heights of the adjacent upper guide plate and the lower guide plate are gradually reduced from the front end of the anaerobic zone to the front end of the aerobic zone, and the distance between the lower end of the lower guide plate and the bottom of the treatment tank is 5-500 mm.
2. The round integrated vertical flow labyrinth structure as recited in claim 1, wherein the flow guide plate between the aerobic zone and the anoxic zone is an upper flow guide plate.
3. The circular integrated vertical flow labyrinth structure as recited in claim 1, wherein the control system comprises:
the aeration unit is arranged in the aerobic zone and is used for aeration of the aerobic zone;
a reflux unit for refluxing at multiple points among the anaerobic zone, the anoxic zone, the aerobic zone and the settling zone;
the online monitoring unit is arranged in the aerobic zone and used for monitoring the working data of the aerobic zone;
and the control unit is connected with the aeration unit, the backflow unit and the online monitoring unit and used for generating a working command for controlling the aeration unit and the backflow unit according to the received working data monitored by the online monitoring unit.
4. The circular integrated vertical flow labyrinth structure according to claim 3, characterized in that the backflow unit comprises one or more selected from the following backflow pipes:
the first reflux pipe is arranged between the anoxic zone and the anaerobic zone and is used for refluxing from the tail end of the anoxic zone to the front end of the anaerobic zone;
the second return pipe is arranged in the anoxic zone and is used for returning from the bottom of the rear end of the anoxic zone to the front end of the anoxic zone;
the third return pipe is arranged between the aerobic zone and the anoxic zone and is used for returning from the bottom of the aerobic zone to the anoxic zone;
the fourth return pipe is arranged between the sedimentation zone and the anoxic zone and is used for returning from the bottom of the sedimentation zone to the front end of the anoxic zone;
and the fifth return pipe is arranged between the settling zone and the aerobic zone and is used for returning from the bottom of the settling zone to the front end of the aerobic zone.
5. The circular integrated vertical flow labyrinth structure as recited in claim 4, wherein the flow back unit further comprises a fan for providing flow back power to the flow back unit.
6. The circular integrated vertical flow labyrinth structure according to claim 3, characterized in that the control system further comprises a solenoid valve assembly box connected with the aeration unit, the backflow unit and the control unit for executing the work orders issued by the control unit.
7. The circular integrated vertical flow labyrinth structure according to claim 3, wherein the control unit controls the aeration intensity and the aeration time of the aeration unit and the reflux intensity and the reflux time of the reflux unit.
8. A wastewater treatment plant characterized in that it comprises a circular integrated vertical flow labyrinth system according to any of claims 1 to 7.
9. A wastewater treatment system, characterized in that it comprises the wastewater treatment apparatus of claim 8.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115925118A (en) * | 2022-12-29 | 2023-04-07 | 安徽中源锦天环境科技股份有限公司 | Baffling type sewage biological treatment system and treatment process thereof |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115925118A (en) * | 2022-12-29 | 2023-04-07 | 安徽中源锦天环境科技股份有限公司 | Baffling type sewage biological treatment system and treatment process thereof |
| CN115925118B (en) * | 2022-12-29 | 2023-09-12 | 安徽中源锦天环境科技股份有限公司 | Baffling type sewage biological treatment system and treatment process thereof |
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