CN208229453U - Downflow system high-efficiency coagulative precipitation tank - Google Patents
Downflow system high-efficiency coagulative precipitation tank Download PDFInfo
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- CN208229453U CN208229453U CN201820445731.0U CN201820445731U CN208229453U CN 208229453 U CN208229453 U CN 208229453U CN 201820445731 U CN201820445731 U CN 201820445731U CN 208229453 U CN208229453 U CN 208229453U
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Abstract
The utility model discloses a kind of downflow system high-efficiency coagulative precipitation tanks, belong to water-treatment technology field, including eddy current type coagulation area, cloth sink area, and waterpower mixes area under control, vertical plate flocculation zone, sloping plate deposition district, horizontal tube settling zone, perforated plate exhalant region and mud collection area；Eddy current type coagulation area is connected with cloth sink area, cloth sink area is connected with waterpower mixing area under control, waterpower mixing area under control is connected with vertical plate flocculation zone, vertical plate flocculation zone is connected with sloping plate deposition district, sloping plate deposition district is connected with horizontal tube settling zone, horizontal tube settling zone is connected with perforated plate exhalant region again, and the lower part of sloping plate deposition district is equipped with mud collection area.The utility model downflow system high-efficiency coagulative precipitation tank, which can effectively shorten, precipitates the time used, deposition efficiency is improved, heavy mud is effectively reduced and turns over and emerges in large numbers as coagulation, flocculation, multiple precipitating functions combine, space occupied not only can be effectively saved, more can effectively improve the efficiency of sedimentation basin.
Description
Technical field
The utility model relates to a kind of coagulative precipitation tank, in particular to a kind of downflow system highly effective coagulation for cement separation
Sedimentation basin belongs to water-treatment technology field.
Background technique
Currently, the most of sedimentation basins applied in water process are up flow type inclined-plate clarifying basin, water flow and inclined plate are at certain
Angle flows up, and needs the coagulated particles precipitated that gravity is then relied on to settle downwards, leads to water (flow) direction and flocculation in this way
Grain the direction of motion on the contrary, increase particle reach inclined plate time, greatly reduce the efficiency of sedimentation basin.
It is found according to investigation, up flow type inclined-plate clarifying basin, which often will appear coagulated particles and turn over, to be emerged in large numbers as mainly due to upward
Water flow drives coagulated particles to cause.And downflow system sedimentation basin not only can effectively improve the efficiency of sedimentation basin, can also effectively drop
Low coagulated particles turn over emerge in large numbers as.Most of precipitating pool process are relatively simple, only have sloping plate deposition simple function, and deposition efficiency
Not high, coagulation is separated with precipitating, and space occupied is relatively large.
Therefore it provides one kind effectively shortens the precipitating time used, improve deposition efficiency, be effectively reduced heavy mud turn over emerge in large numbers as,
The downflow system high-efficiency coagulative precipitation tank that coagulation, flocculation, multiple precipitating functions combine just becomes the technical field and is badly in need of solving
Technical problem.
Summary of the invention
It is effectively shortened the purpose of the utility model is to provide one kind and precipitates the time used, improved deposition efficiency, be effectively reduced
Heavy mud, which turns over, to be emerged in large numbers as the downflow system high-efficiency coagulative precipitation tank that coagulation, flocculation, multiple precipitating functions combine.
The above-mentioned purpose of the utility model reaches by the following technical programs:
Downflow system high-efficiency coagulative precipitation tank, it is characterised in that: including eddy current type coagulation area, cloth sink area, waterpower mixing tube
Area, vertical plate flocculation zone, sloping plate deposition district, horizontal tube settling zone, perforated plate exhalant region and mud collection area；Eddy current type coagulation area and cloth
Sink area is connected, and cloth sink area is connected with waterpower mixing area under control, and waterpower mixing area under control is connected with vertical plate flocculation zone, erects
Straight panel flocculation zone is connected with sloping plate deposition district, and sloping plate deposition district is connected with horizontal tube settling zone, horizontal tube settling zone again with
Perforated plate exhalant region is connected, and the lower part of sloping plate deposition district is equipped with mud collection area.
Preferably, eddy current type coagulation area includes: eddy current type coagulating basin, and blender is equipped in eddy current type coagulating basin and is added
Medicine device.
Preferably, the eddy current type coagulating basin is cylindrical shape, and eddy current type coagulating basin is equipped with and eddy current type coagulating basin pond body
Tangent inlet passage.
Preferably, the cloth sink area includes several cloth sinks arranged side by side, and cloth sink is welded using steel plate,
Positioned at the upper left side of sedimentation tank body, the surrounding of cloth sink is uniformly arranged multiple rectangular water outlets.
Preferably, waterpower mixing area under control includes several waterpower mixing tubes.
Preferably, the inner wall of the waterpower mixing tube is equipped with barrier.
Preferably, the vertical plate flocculation zone is provided with several risers, places in vertical, and the lower end of riser is equipped with steel
Slot.
Preferably, the sloping plate deposition district is located at the lower section of vertical plate flocculation zone, and sloping plate deposition district is tiltedly installed with interval
The lower end of uniform inclined plate, inclined plate is equipped with steel tank.
Preferably, the mud collection area is located at the lower part of the sloping plate deposition district, and mud collection area includes several sludge hoppers, collects mud
The bottom of bucket is equipped with sludge pipe.
Preferably, the horizontal tube settling zone is located at the right of downflow system high-efficiency coagulative precipitation tank, with sloping plate deposition district phase
Connection, horizontal tube settling zone are equipped with several transversely arranged horizontal tubes, and lower end is equipped with the steel tank being connected with the horizontal tube.
Preferably, the perforated plate exhalant region is equipped with several perforated plates, and the perforated plate is connected with drainpipe.
The utility model has the advantages that
The utility model downflow system high-efficiency coagulative precipitation tank is a kind of new coprecipitation mode, can be effectively shortened used in precipitating
Time improves deposition efficiency, heavy mud is effectively reduced and turns over and emerges in large numbers as coagulation, flocculation, multiple precipitating functions combine, and not only may be used
Effectively to save space occupied, the efficiency of sedimentation basin more can effectively improve, be a kind of suitable for railway tunnel construction waste water water
The high-efficient treatment device of amount and water quality characteristics.
Below by the drawings and specific embodiments, the present invention will be further described, but is not meant to protect the present invention
Protect the limitation of range.Implementation condition and device in embodiment unless otherwise, be this field routine implementation condition and
The conventional device that can be purchased in the market.
Detailed description of the invention
Fig. 1 is the longitudinal profile structure schematic of the utility model downflow system high-efficiency coagulative precipitation tank.
Fig. 2 is the planar structure schematic diagram of the utility model downflow system high-efficiency coagulative precipitation tank.
Fig. 3 is the B-B section structure diagram of the utility model downflow system high-efficiency coagulative precipitation tank.
Main parts size title:
1 eddy current type coagulating basin, 2 blender
3 doser, 4 waterpower mixing tube
5 cloth sink, 6 riser
7 inclined plate, 8 steel tank
9 horizontal tube, 10 perforated plate
11 drainpipe, 12 sludge hopper
The total sludge pipe of 13 sludge pipe 14
Specific embodiment
As shown in Figure 1, being the longitudinal profile structure schematic of the utility model downflow system high-efficiency coagulative precipitation tank, such as Fig. 2
It is shown, it is the planar structure schematic diagram of the utility model downflow system high-efficiency coagulative precipitation tank, as shown in figure 3, being the utility model
The B-B section structure diagram of downflow system high-efficiency coagulative precipitation tank；Wherein, 1 is eddy current type coagulating basin, and 2 be blender, and 3 be to add
Medicine device, 4 be waterpower mixing tube, and 5 be cloth sink, and 6 be riser, and 7 be inclined plate, and 8 be steel tank, and 9 be horizontal tube, and 10 be perforated plate, 11
It is sludge hopper for drainpipe, 12,13 be sludge pipe, and 14 be total sludge pipe；The utility model downflow system high-efficiency coagulative precipitation tank packet
It includes: eddy current type coagulating basin 1, blender 2, doser 3, waterpower mixing tube 4, cloth sink 5, riser 6, inclined plate 7, steel tank 8, horizontal tube
9, perforated plate 10, drainpipe 11, sludge hopper 12 and sludge pipe 13；Blender 2, eddy current type coagulation are equipped in eddy current type coagulating basin 1
Pond 1 is connected with doser 3, and eddy current type coagulating basin 1 is connected with cloth sink 5, and cloth sink 5 is connected with waterpower mixing tube 4, water
Power mixing tube 4 is connected with riser 6, and 6 lower end of riser is equipped with steel tank 8, and riser 6 is connected with inclined plate 7, and 7 lower end of inclined plate is equipped with steel
Slot 8, inclined plate 7 are connected with horizontal tube 9, and 9 lower end of horizontal tube is equipped with steel tank 8, and horizontal tube 9 is connected with perforated plate 10, perforated plate
10 lower ends are equipped with steel tank 8, and perforated plate 10 is connected with drainpipe 11, and sludge hopper 12 is connected with sludge pipe 13, sludge pipe 13 and
Total sludge pipe 14 is connected；
The utility model downflow system high-efficiency coagulative precipitation tank successively includes: eddy current type coagulation area, connected water distribution
Slot area, the waterpower mixing area under control being connected with cloth sink area, waterpower mixing area under control are connected with vertical plate flocculation zone, vertical plate wadding
Coagulation zone is connected with sloping plate deposition district, and sloping plate deposition district is connected with horizontal tube settling zone, horizontal tube settling zone again with perforated plate
Exhalant region is connected, and the lower part of sloping plate deposition district is equipped with mud collection area；
The working principle of the utility model downflow system high-efficiency coagulative precipitation tank: water flow first passes through eddy current type coagulation area, dosing
After being stirred, after cloth sink area is evenly arranged, mixed into the waterpower mixing laggard step in area under control using waterpower, vertical
Plate flocculation zone flocculates, and coagulated particles increase, and carries out quick mud-water separation in sloping plate deposition district rapid precipitation, heavy in horizontal tube
Shallow lake area further removes fine particle, improves deposition efficiency, eventually passes through perforated plate exhalant region main road and stablizes water outlet.
Eddy current type coagulation area includes: the eddy current type coagulating basin 1 of cylindrical shape, equipped with tangent with eddy current type coagulating basin pond body
Inlet passage makes to enter pond body formation vortex into water, blender 2 and doser 3, mixing direction and vortex direction one is equipped in pond
It causes, by quickly stirring and 3 dosing of doser of blender 2, realizes in the short time and come into full contact with mixing；
Water inlet is after eddy current type coagulating basin, and into cloth sink area, cloth sink area includes five cloth sinks arranged side by side
5, cloth sink 5 is welded using steel plate, and positioned at the upper left side of sedimentation tank body, the surrounding of cloth sink 5 is uniformly arranged multiple rectangular
Water outlet guarantees that the water quality for entering waterpower mixing area under control is uniform；
It intakes by the homogeneous of cloth sink, water flow is downwardly into waterpower mixing area under control；Waterpower mixes area under control by multiple inner walls
Rectangular tube equipped with barrier, that is, waterpower mixing tube 4 forms, and when water inlet is by the rectangular tube, forms turbulent flow, keeps medicament and water mixed
It closes more abundant；
Water inlet mixes area under control in waterpower, after being sufficiently mixed with medicament, wads a quilt with cotton into vertical plate flocculation zone, and in vertical plate
Coagulation zone is flocculated；Vertical plate flocculation zone is provided with several risers 6, places in vertical, and the lower end of riser 6 is equipped with steel tank 8, erects
Spacing is smaller between plate 6 (partition), prevents turbulent flow and makes to flow into water direction in stratified flow straight down, has longer waterpower
Residence time, coagulated particles are formed and are constantly grown up；
Water inlet is further processed after the processing of vertical plate flocculation zone into sloping plate deposition district, and sloping plate deposition district is located at perpendicular
The lower section of straight panel flocculation zone, sloping plate deposition district are tiltedly installed with evenly spaced inclined plate 7, and the lower end of inclined plate 7 is equipped with steel tank 8, tiltedly
The setting of plate settling zone has the characteristics that rapid precipitation and high efficiency precipitating；According to precipitating formula, the water flow by riser 6 be to
Lower flowing, coagulated particles are moved downward with the effect for pushing down on power and gravity of water, and the acceleration of particle sedimentation increases, because
This particle can quickly reach inclined plate 7 and be precipitated, to achieve the purpose that rapid precipitation；
Sludge after precipitating enters the mud collection area processing of sloping plate deposition district lower part, and mud collection area includes four sludge hoppers 12, collection
The bottom of bucket 12 is equipped with sludge pipe 13；
Water inlet is further processed after sloping plate deposition district is handled into horizontal tube settling zone；Horizontal tube precipitates position
In the right of whole device, it is connected with sloping plate deposition district, horizontal tube settling zone is equipped with several transversely arranged horizontal tubes 9, under
End is equipped with the steel tank 8 being connected with the horizontal tube 9；Setting can make water (flow) direction be staggered with precipitating direction in this way, be orthogonal
State, the two do not interfere with each other, to achieve the effect that mud-water separation；
Water inlet is further processed after the processing of horizontal tube settling zone into perforated plate exhalant region；Perforated plate exhalant region
Equipped with several perforated plates 10, the perforated plate 10 is connected with drainpipe 11；It is discharged using 10 submerged of perforated plate, it can be effective
Swabbing is prevented, from reaching more preferable more steady outlet effect.
Coagulation, flocculation, multiple precipitating functions are combined together by the downflow system high-efficiency coagulative precipitation tank of the utility model,
Space occupied not only can be effectively saved, more can effectively improve the efficiency of sedimentation basin, suitable for railway tunnel construction waste water
Efficient process.
The downflow system high-efficiency coagulative precipitation tank of the utility model is one designed based on shallow pool theory and particle sedimentation theory
The efficient device for separating mud and water of kind；Including two parts of coagulation and precipitating, water inlet first passes through gallery and enters eddy current type coagulating basin, coagulation
Pond is equipped with chemicals dosing plant and blender, adds after quickly stir after appropriate coagulant by blender, medicament with intake with respect to filling
Divide mixing, is mixed again into waterpower mixing area under control, then water flow flows downward into vertical plate flocculation zone, particle flocculation
After increase, flowing downward enters back into sloping plate deposition district and carries out a rapid precipitation, in water outlet not by separation little particle floccule body with
Water flow flows up into horizontal tube depositing separation area and carries out secondary separation, and water outlet is discharged using submerged perforated plate；Downflow system
High-efficiency coagulative precipitation tank uses reinforced concrete structure on the whole, and part-structure uses steel plate and channel steel material.
Claims (10)
1. downflow system high-efficiency coagulative precipitation tank, it is characterised in that: including eddy current type coagulation area, cloth sink area, waterpower mixes area under control,
Vertical plate flocculation zone, sloping plate deposition district, horizontal tube settling zone, perforated plate exhalant region and mud collection area；Eddy current type coagulation area and water distribution
Slot area is connected, and cloth sink area is connected with waterpower mixing area under control, and waterpower mixing area under control is connected with vertical plate flocculation zone, vertically
Plate flocculation zone is connected with sloping plate deposition district, and sloping plate deposition district is connected with horizontal tube settling zone, horizontal tube settling zone again with wear
Orifice plate exhalant region is connected, and the lower part of sloping plate deposition district is equipped with mud collection area.
2. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: eddy current type coagulation area packet
Include: eddy current type coagulating basin, eddy current type coagulating basin is interior to be equipped with blender and doser.
3. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the eddy current type coagulating basin is circle
Bar shape, eddy current type coagulating basin are equipped with the inlet passage tangent with eddy current type coagulating basin pond body.
4. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the cloth sink area includes side by side
Several cloth sinks being arranged, cloth sink is welded using steel plate, and positioned at the upper left side of sedimentation tank body, the surrounding of cloth sink is equal
The even multiple rectangular water outlets of setting.
5. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: waterpower mixing area under control includes
Several waterpower mixing tubes.
6. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the inner wall of the waterpower mixing tube
Equipped with barrier.
7. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the vertical plate flocculation zone setting
There are several risers, placed in vertical, the lower end of riser is equipped with steel tank.
8. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the sloping plate deposition district is located at perpendicular
The lower section of straight panel flocculation zone, sloping plate deposition district are tiltedly installed with evenly spaced inclined plate, and the lower end of inclined plate is equipped with steel tank.
9. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the mud collection area is located at described oblique
The lower part of plate settling zone, mud collection area include several sludge hoppers, and the bottom of sludge hopper is equipped with sludge pipe.
10. downflow system high-efficiency coagulative precipitation tank according to claim 1, it is characterised in that: the horizontal tube precipitates position
In the right of downflow system high-efficiency coagulative precipitation tank, it is connected with sloping plate deposition district, horizontal tube settling zone is equipped with several transversely arranged
Horizontal tube, lower end is equipped with the steel tank that is connected with the horizontal tube；The perforated plate exhalant region is equipped with several perforated plates, institute
Perforated plate is stated to be connected with drainpipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820445731.0U CN208229453U (en) | 2018-03-31 | 2018-03-31 | Downflow system high-efficiency coagulative precipitation tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820445731.0U CN208229453U (en) | 2018-03-31 | 2018-03-31 | Downflow system high-efficiency coagulative precipitation tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208229453U true CN208229453U (en) | 2018-12-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820445731.0U Expired - Fee Related CN208229453U (en) | 2018-03-31 | 2018-03-31 | Downflow system high-efficiency coagulative precipitation tank |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110540268A (en) * | 2019-04-18 | 2019-12-06 | 贵州民族大学 | Electric field algae removal structure |
| CN111847774A (en) * | 2020-07-10 | 2020-10-30 | 珠海九通水务股份有限公司 | Application method of mud-water separation tank |
| CN113387423A (en) * | 2021-07-15 | 2021-09-14 | 南通华新环保科技股份有限公司 | High-efficiency energy-saving coagulation reactor |
| CN113860454A (en) * | 2021-11-09 | 2021-12-31 | 温华环境科技（北京）有限公司 | Circulation clarification equipment |
| WO2022007525A1 (en) * | 2020-07-10 | 2022-01-13 | 珠海九通水务股份有限公司 | Multifunctional tank-based sewage treatment process |
-
2018
- 2018-03-31 CN CN201820445731.0U patent/CN208229453U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110540268A (en) * | 2019-04-18 | 2019-12-06 | 贵州民族大学 | Electric field algae removal structure |
| CN111847774A (en) * | 2020-07-10 | 2020-10-30 | 珠海九通水务股份有限公司 | Application method of mud-water separation tank |
| WO2022007525A1 (en) * | 2020-07-10 | 2022-01-13 | 珠海九通水务股份有限公司 | Multifunctional tank-based sewage treatment process |
| CN111847774B (en) * | 2020-07-10 | 2022-05-03 | 珠海九通水务股份有限公司 | Application method of mud-water separation tank |
| CN113387423A (en) * | 2021-07-15 | 2021-09-14 | 南通华新环保科技股份有限公司 | High-efficiency energy-saving coagulation reactor |
| CN113860454A (en) * | 2021-11-09 | 2021-12-31 | 温华环境科技（北京）有限公司 | Circulation clarification equipment |
| CN113860454B (en) * | 2021-11-09 | 2024-02-06 | 温华环境科技（北京）有限公司 | Circulation clarification plant |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181214 Termination date: 20200331 |
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| CF01 | Termination of patent right due to non-payment of annual fee |