CN219941872U - Inclined tube sedimentation tank group - Google Patents
Inclined tube sedimentation tank group Download PDFInfo
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- CN219941872U CN219941872U CN202321565986.8U CN202321565986U CN219941872U CN 219941872 U CN219941872 U CN 219941872U CN 202321565986 U CN202321565986 U CN 202321565986U CN 219941872 U CN219941872 U CN 219941872U
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- sedimentation tank
- inclined tube
- sludge
- tank
- primary
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- 238000004062 sedimentation Methods 0.000 title claims abstract description 123
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 82
- 239000010802 sludge Substances 0.000 claims abstract description 80
- 239000000872 buffer Substances 0.000 claims abstract description 61
- 239000010865 sewage Substances 0.000 claims abstract description 13
- 238000007599 discharging Methods 0.000 claims abstract description 10
- 238000005189 flocculation Methods 0.000 claims description 8
- 230000016615 flocculation Effects 0.000 claims description 7
- 238000007689 inspection Methods 0.000 claims 3
- 238000005192 partition Methods 0.000 claims 2
- 238000000034 method Methods 0.000 abstract description 9
- 238000010992 reflux Methods 0.000 description 9
- 239000012528 membrane Substances 0.000 description 7
- 239000006228 supernatant Substances 0.000 description 6
- 238000012423 maintenance Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000001112 coagulating effect Effects 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000003631 expected effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 231100001240 inorganic pollutant Toxicity 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000001728 nano-filtration Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model discloses an inclined tube sedimentation tank group, which belongs to the technical field of sewage treatment, and comprises a buffer tank, a primary inclined tube sedimentation tank, a secondary inclined tube sedimentation tank, a water inlet pipeline, a water outlet pipeline and the like, wherein the inside of the buffer tank is equally divided into four buffer areas by a baffle plate in the buffer tank, one side of the primary sedimentation tank is adjacent to the buffer tank, the other side of the primary sedimentation tank is adjacent to the secondary inclined tube sedimentation tank, inclined tubes are arranged above the bottoms of the primary sedimentation tank and the secondary inclined tube sedimentation tank, and a sludge discharge pipeline is respectively communicated with the bottoms of the buffer tank, the primary sedimentation tank and the secondary inclined tube sedimentation tank and is used for discharging bottom sludge; the sludge return pipeline is connected to the sludge discharge pipeline and is used for timely and properly returning sludge to the biochemical tank. Compared with the prior art, the system is more stable in operation and better in adaptability to water quality and water quantity by arranging the two-stage inclined tube sedimentation tank, the sludge in the first-stage inclined tube sedimentation zone can automatically slide down and is not easy to adhere, the sludge is smoothly discharged, the impact on the rear-end process is reduced, and the occupied area is reduced.
Description
Technical Field
The utility model belongs to the technical field of sewage treatment, and particularly relates to an inclined tube sedimentation tank group.
Background
Main structures of the existing landfill leachate treatment station comprise an adjusting tank, a biochemical tank (UASB anaerobic zone-anoxic zone-aerobic zone), a membrane treatment room (MBR membrane+ultrafiltration+nanofiltration+reverse osmosis) and the like. Wherein, leachate is through directly entering membrane treatment room of sedimentation tank sediment supernatant after biochemical pond treatment, because current sedimentation tank volume is limited, and settling time is insufficient, mud-water separation is incomplete, contains a large amount of suspended solids in the supernatant, leads to follow-up membrane treatment stage load increase, and membrane module life-span reduces, and maintenance cost increases. Therefore, it is a technical problem in the field how to improve the above-mentioned state of the art without changing the production process of the leachate treatment station of the existing landfill.
The inclined tube sedimentation tank is mainly used for advanced treatment of coagulating sedimentation process sections or used as a secondary sedimentation tank when limited by the occupied area of a sewage treatment plant. However, the inclined tube sedimentation tank is not suitable for being used as a secondary sedimentation tank, because the activated sludge has high viscosity and is easy to adhere to the inclined tube, the sedimentation effect is affected, and even the inclined tube is likely to be blocked. Meanwhile, under the anaerobic condition, the gas generated by anaerobic digestion can interfere with the precipitation of the sludge when rising, and the sludge falling off from the plate is brought to the water surface to form a sludge layer. However, when the capacity of secondary sedimentation is required to be further enlarged in some sewage treatment plants, the treatment efficiency is improved by adopting a diagonal sedimentation tank due to the limitation of occupied area, so that a novel diagonal sedimentation tank is urgently needed to be designed to solve the problems.
Disclosure of Invention
Aiming at the technical problems, the utility model provides a pipe chute sedimentation tank group, which is characterized in that a two-stage pipe chute sedimentation tank is arranged in the equipment to ensure that the system is more stable in operation and better in adaptability to water quality and water quantity, and the sludge in a first-stage pipe chute sedimentation zone can automatically slide down, is not easy to adhere, is smooth in sludge discharge and reduces the impact on a rear-end process.
The utility model solves the problems by the following technical means:
the utility model provides a pipe chute sedimentation tank group, its characterized in that includes buffer tank, one-level sedimentation tank, second grade pipe chute sedimentation tank, water inlet pipeline, water outlet pipeline, mud pipeline and mud return line, wherein:
the inside of the buffer pool is provided with an inner baffle plate which is cross-shaped and equally divides the inside of the buffer pool into four buffer areas, the four buffer areas are communicated through a buffer area inner pipeline, the inside of the first buffer area is connected with a water inlet pipeline, the top of the fourth buffer area is communicated with a buffer area water outlet pipe, and sewage enters the buffer area from the water inlet pipeline, sequentially passes through the four buffer areas according to the S-shaped flow direction and then enters the first-stage sedimentation tank through the buffer area water outlet pipe;
one side of the primary sedimentation tank is adjacent to the buffer tank, the other side of the primary sedimentation tank is adjacent to the secondary inclined tube sedimentation tank, primary inclined tubes are closely and equidistantly arranged above a primary sedimentation area at the bottom of the primary sedimentation tank, a primary water outlet is formed in the top of one side, close to the secondary inclined tube sedimentation tank, of the primary sedimentation tank, and a primary water outlet weir is arranged on the inner side of the primary water outlet;
the upper part of a secondary sedimentation zone at the bottom of the secondary inclined tube sedimentation tank is closely and equidistantly provided with secondary inclined tubes, the top of one side of the secondary inclined tube sedimentation tank, which is far away from the primary sedimentation tank, is provided with a secondary water outlet, the inner side of the secondary water outlet is provided with a secondary water weir, the position, which is close to the primary water outlet, of the secondary inclined tube sedimentation tank is provided with a PAC dosing port, and a dosing tube is arranged in the PAC dosing port;
the water outlet pipeline is arranged on the secondary water outlet;
the sludge discharge pipeline is respectively communicated with the bottoms of the buffer tank, the primary sedimentation tank and the secondary inclined tube sedimentation tank and is used for discharging bottom sludge;
the sludge return pipeline is connected to the sludge discharge pipeline and is used for timely and properly returning sludge to the biochemical tank.
Preferably, the branch lines of the bottom parts of the sludge discharge pipeline connecting buffer tank, the primary sedimentation tank and the secondary inclined tube sedimentation tank are respectively provided with a flocculation sludge discharge valve, a primary sludge discharge valve and a secondary sludge discharge valve, and the output end of the sludge discharge pipeline is used for discharging sludge outwards through a sludge discharge pump.
Preferably, a control valve is arranged on the mud discharging pipeline and is used for closing or opening the mud discharging pipeline.
Preferably, a return pump and a return valve are arranged on the sludge return pipeline.
Preferably, the maintenance frame is further comprised, and the maintenance frame comprises a stair and a maintenance platform.
The inclined tube sedimentation tank set has the following beneficial effects:
1) The water flow trend of the buffer zone is designed into an S shape, and coagulation or flocculation can be performed in the precipitation process, so that suspended particles mutually collide and coagulate, the particle quality is gradually increased, the sedimentation speed is gradually increased, the stay time of muddy water is mainly increased, the sludge concentration effect is improved, and the sludge entering the inclined tube sedimentation zone is easy to sediment.
2) The utility model can be applied to the process section of a secondary sedimentation tank of a sewage treatment plant, and the sludge in the primary inclined tube sedimentation zone can automatically slide down through the primary inclined tube zone, so that the sludge is not easy to adhere and is smoothly discharged. The front end of the secondary sedimentation zone is provided with an automatic dosing system, PAC flocculant is added to further settle the micro suspended matters, so that the water suspended matters entering the rear-end process section are minimized. The dosing pump is controlled by frequency conversion, and the dosing amount is controlled according to the water quality refinement. The two-stage inclined tube sedimentation tank increases the residence time, so that the operation is stable, and the adaptability to water quality and water quantity is good. The implementation of the technical scheme achieves the expected effect.
Drawings
In order to more clearly illustrate the technical solutions of the present utility model, the drawings that are needed in the embodiments will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present utility model, and that other drawings can be obtained according to these drawings without inventive effort for a person skilled in the art.
FIG. 1 is a schematic view of the overall structure of the present utility model;
FIG. 2 is a schematic diagram of a buffer pool structure of the present utility model;
FIG. 3 is a schematic diagram of the structure of the sedimentation tank of the present utility model;
FIG. 4 is a schematic diagram of a piping structure of the present utility model;
fig. 5 is a schematic diagram of a chute layout of the present utility model.
Wherein, 1-buffer pool, 101-inner baffle, 102-buffer zone, 103-buffer zone inner pipeline, 104-buffer zone water outlet pipe, 2-first-stage sedimentation tank, 201-first-stage sedimentation zone, 202-first-stage inclined pipe, 203-first-stage water outlet, 204-first-stage water outlet weir, 3-second-stage inclined pipe sedimentation tank, 301-second-stage sedimentation zone, 302-second-stage inclined pipe, 303-second-stage water outlet port, 304-second-stage water outlet weir, 305-PAC dosing port, 306-dosing pipe, 4-water inlet pipeline, 5-water outlet pipeline, 6-mud discharge pipeline, 601-flocculation mud valve, 602-primary mud valve, 603-secondary mud valve, 604-mud pump, 605-control valve, 7-mud reflux pipeline, 701-reflux pump, 702-reflux valve and 8-maintenance frame.
Description of the embodiments
In the description of the present utility model, it should be understood that the terms "center," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like indicate orientations or positional relationships based on the orientation or positional relationships shown in the drawings, merely to facilitate describing the present utility model and simplify the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model. The terms "first," "second," and the like, are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defining "a first" or "a second" may explicitly or implicitly include one or more such feature. In the description of the present utility model, unless otherwise indicated, the meaning of "a plurality" is two or more.
The present utility model will be described in detail below with reference to the accompanying drawings.
As shown in fig. 1 to 5, the inclined tube sedimentation tank group comprises a buffer tank 1, a primary sedimentation tank 2, a secondary inclined tube sedimentation tank 3, a water inlet pipeline 4, a water outlet pipeline 5, a sludge discharge pipeline 6, a sludge return pipeline 7, an overhaul frame 8 and other structures, wherein in the figure, biochemical tank mixed liquor enters the buffer tank 1 through the water inlet pipeline 4, then enters the water outlet pipeline 5 through the primary sedimentation tank 2 and the secondary inclined tube sedimentation tank 3, and the sludge discharge pipeline 6 is respectively communicated with the bottoms of the buffer tank 1, the primary sedimentation tank 2 and the secondary inclined tube sedimentation tank 3 and is used for discharging bottom sludge; the sludge return pipeline 7 is connected to the sludge discharge pipeline 6, and the sludge return pipeline 7 is used for timely and properly returning sludge to the biochemical tank.
In the figure, the inside of buffer tank 1 is provided with interior baffle 101, interior baffle 101 becomes the cross and equally divide into four buffers 102 with buffer tank 1' S inside, communicate through buffer inner tube 103 between four buffers 102, the internal connection of first buffer 102 has inlet tube 4, the top intercommunication of fourth buffer 102 has buffer outlet pipe 104, after the sewage gets into buffer 102 by inlet tube 4, after four buffers 102 are passed through in proper order according to the S type flow direction again in entering first class sedimentation tank 2 through buffer outlet pipe 104, it is to say that, the top of buffer inner tube 103 intakes, the bottom goes out water, it is upper and lower S type to design the rivers trend to increase muddy water dwell time.
In the figure, one side of a primary sedimentation tank 2 is close to a buffer tank 1, the other side of the primary sedimentation tank 2 is close to a secondary inclined tube sedimentation tank 3, a primary inclined tube 202 is closely and equidistantly arranged above a primary sedimentation area 201 at the bottom of the primary sedimentation tank 2, a primary water outlet 203 is formed in the top of one side of the primary sedimentation tank 2 close to the secondary inclined tube sedimentation tank 3, a primary water outlet weir 204 is arranged on the inner side of the primary water outlet 203, and it is noted that after mixed liquor enters the primary sedimentation tank 2, inclined tube fillers are filled in the mixed liquor, water is fed in and discharged in a mode of lower feeding and upper discharging, suspended matters and supernatant in the mixed liquor are separated through the action of the inclined tube, sludge is discharged from the bottom, and supernatant is discharged from a water outlet weir to the secondary inclined tube sedimentation tank.
A second-stage inclined tube 302 is arranged above a second-stage sedimentation zone 301 at the bottom of the second-stage inclined tube sedimentation tank 3 in a close and equidistant manner, a second-stage water outlet 303 is formed in the top of one side, far away from the first-stage sedimentation tank 2, of the second-stage inclined tube sedimentation tank 3, a second-stage water outlet weir 304 is arranged on the inner side of the second-stage water outlet 303, a PAC dosing opening 305 is formed in the position, close to the first-stage water outlet 203, of the second-stage inclined tube sedimentation tank 3, and a dosing tube 306 is arranged in the PAC dosing opening 305; the water outlet pipeline 5 is arranged on the secondary water outlet 303; after the supernatant enters the secondary inclined tube sedimentation tank, a water inlet and outlet mode of lower inlet and upper outlet is adopted, and at the moment, fine suspended matters are further settled by the inner inclined tube and adding PAC flocculant, so that the water suspended matters entering the rear end membrane treatment process section are minimized.
In this embodiment, a plurality of dense inclined pipes are arranged in the sedimentation area, so that suspended impurities in water are precipitated in the inclined pipes, water flows upward along the inclined pipes, and separated sludge slides downwards to the bottom of the pond along the inclined pipes under the action of gravity and is discharged in a concentrated manner. The sedimentation efficiency can be improved by 50-60%, the treatment capacity can be improved by 3-5 times on the same area, and the water outlet pipe is arranged above the inclined pipe area so as to prevent the influence on the water outlet at the upper part. In addition, PAC flocculant is added to further settle the fine suspended matters so as to minimize the water suspended matters entering the back-end membrane treatment process section. The dosing pump is controlled by frequency conversion, and the dosing amount is controlled according to the water quality refinement.
Specifically, the primary inclined tube sedimentation adopts an upward flow inclined tube, the inclined angle is set to be 60-70 degrees, the aperture of the inclined tube adopts a large aperture, and the diameter of an inscribed circle is 100mm, so that the sludge in the primary inclined tube sedimentation zone can automatically slide down, is not easy to adhere and is smooth to discharge. The secondary sedimentation adopts an upward flow inclined tube, the installation angle of the inclined tube is 50-60 degrees, and the diameter of the inscribed circle is 80mm, which is different from that of the primary sedimentation. The front end of the secondary sedimentation zone is provided with an automatic dosing system, PAC flocculant is added to further settle the micro suspended matters, so that the water suspended matters entering the rear-end process section are minimized. The dosing pump is controlled by frequency conversion, and the dosing amount is controlled according to the water quality refinement.
In the figure, a flocculation sludge valve 601, a primary sludge valve 602 and a secondary sludge valve 603 are respectively arranged on branches of the sludge discharge pipeline 6 connected with the bottoms of the buffer tank 1, the primary sedimentation tank 2 and the secondary inclined tube sedimentation tank 3, and the output end of the sludge discharge pipeline 6 is used for discharging sludge outwards through a sludge discharge pump 604.
In this embodiment, the sludge discharge pipeline 6 is provided with a control valve 605, the control valve 605 is used for closing or opening the sludge discharge pipeline 6, it is to be noted that, because PAC is added at the front end of the buffer zone, the sludge in the buffer zone is chemical sludge, and in order not to affect the sludge activity of the biochemical tank, the sludge is directly discharged to the sludge tank, but the sludge in the flocculation zone and the primary sedimentation tank is directly returned to the biochemical tank, and the control valve 605 is closed at this time. If the sludge concentration in the biochemical tank is sufficient, the control valve 605 can be opened to directly discharge the sludge in the flocculation zone and the primary sedimentation tank to the sludge concentration tank without the need of sludge reflux. The control valve 605 is mainly used for controlling the sludge concentration of the biochemical tank and the sludge amount of the flocculation area and the primary sedimentation tank, in the figure, a reflux pump 701 and a reflux valve 702 are arranged on a pipeline of a sludge reflux pipeline 7, the reflux pump 701 is controlled by a frequency converter, and the sludge concentration of the biochemical tank can be ensured in a mode of feeding water and refluxing.
In actual operation, the inclined tube sedimentation tank can remove colloid and micro suspended organic and inorganic pollutants in sewage, and macroscopically, the chromaticity and turbidity of the sewage are removed. The coagulating sedimentation can also remove certain dissolved substances in the sewage, and can also effectively remove nitrogen, phosphorus and the like which can cause eutrophication of the slow-flowing water body. The inclined tube sedimentation tank is characterized in that coagulant with the quantity which is suitable for the action mechanism is put into sewage, and through full mixing and reaction, tiny suspended particles and colloid particles in the sewage are mutually aggregated to form larger particles, suspended matters are precipitated and sunk on an inclined plate while water flow rises, and supernatant fluid flows out of a water outlet through a water outlet weir groove.
Finally, it should be noted that: the above embodiments are only for illustrating the technical solution of the present utility model, and are not limiting; although the utility model has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical scheme described in the foregoing embodiments can be modified or some technical features thereof can be replaced by equivalents; such modifications and substitutions do not depart from the spirit and scope of the technical solutions of the embodiments of the present utility model.
Claims (5)
1. The utility model provides a pipe chute sedimentation tank group, its characterized in that, including buffer tank (1), one-level sedimentation tank (2), second grade pipe chute sedimentation tank (3), water inlet pipeline (4), outlet pipe way (5), mud discharging pipeline (6) and mud return line (7), wherein:
an inner partition plate (101) is arranged in the buffer tank (1), the inner partition plate (101) is in a cross shape and equally divides the interior of the buffer tank (1) into four buffer areas (102), the four buffer areas (102) are communicated through a buffer area inner pipeline (103), the interior of a first buffer area (102) is connected with a water inlet pipeline (4), the top of the fourth buffer area (102) is communicated with a buffer area water outlet pipe (104), and sewage enters the buffer area (102) from the water inlet pipeline (4) and then sequentially passes through the four buffer areas (102) according to an S-shaped flow direction and then enters the first-stage sedimentation tank (2) through the buffer area water outlet pipe (104);
one side of the primary sedimentation tank (2) is close to the buffer tank (1), the other side of the primary sedimentation tank (2) is close to the secondary inclined tube sedimentation tank (3), primary inclined tubes (202) are closely and equidistantly arranged above a primary sedimentation area (201) at the bottom of the primary sedimentation tank (2), a primary water outlet (203) is formed in the top of one side, close to the secondary inclined tube sedimentation tank (3), of the primary sedimentation tank (2), and a primary water outlet weir (204) is arranged on the inner side of the primary water outlet (203);
a second-stage inclined tube (302) is closely and equidistantly arranged above a second-stage sedimentation zone (301) at the bottom of the second-stage inclined tube sedimentation tank (3), a second-stage water outlet (303) is formed in the top of one side, far away from the first-stage sedimentation tank (2), of the second-stage inclined tube sedimentation tank (3), a second-stage water outlet weir (304) is arranged on the inner side of the second-stage water outlet (303), a PAC (programmable logic controller) dosing port (305) is formed in the position, close to the first-stage water outlet (203), of the second-stage inclined tube sedimentation tank (3), and a dosing tube (306) is arranged in the PAC dosing port (305);
the water outlet pipeline (5) is arranged on the secondary water outlet (303);
the sludge discharge pipeline (6) is respectively communicated with the bottoms of the buffer tank (1), the primary sedimentation tank (2) and the secondary inclined tube sedimentation tank (3) and is used for discharging sludge at the bottoms;
the sludge return pipeline (7) is connected to the sludge discharge pipeline (6), and the sludge return pipeline (7) is used for timely and properly returning sludge to the biochemical pond.
2. The inclined tube sedimentation tank set according to claim 1, wherein the sludge discharge pipeline (6) is connected with the branch paths at the bottoms of the buffer tank (1), the primary sedimentation tank (2) and the secondary inclined tube sedimentation tank (3), and is respectively provided with a flocculation sludge discharge valve (601), a primary sludge discharge valve (602) and a secondary sludge discharge valve (603), and the output end of the sludge discharge pipeline (6) discharges sludge outwards through a sludge discharge pump (604).
3. A pipe chute sedimentation tank group according to claim 1, characterized in that a control valve (605) is arranged on the sludge discharge pipe (6), and the control valve (605) is used for closing or opening the sludge discharge pipe (6).
4. A pipe chute sedimentation tank group according to claim 1, characterized in that the pipe of the sludge return pipe (7) is provided with a return pump (701) and a return valve (702).
5. A pipe chute sedimentation basin group as claimed in claim 1, further comprising an inspection rack (8), said inspection rack (8) comprising stairs and an inspection platform.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321565986.8U CN219941872U (en) | 2023-06-19 | 2023-06-19 | Inclined tube sedimentation tank group |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321565986.8U CN219941872U (en) | 2023-06-19 | 2023-06-19 | Inclined tube sedimentation tank group |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219941872U true CN219941872U (en) | 2023-11-03 |
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ID=88540244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321565986.8U Active CN219941872U (en) | 2023-06-19 | 2023-06-19 | Inclined tube sedimentation tank group |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219941872U (en) |
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2023
- 2023-06-19 CN CN202321565986.8U patent/CN219941872U/en active Active
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