CN203112564U - Vertical micro-vortex flocculation clarifier - Google Patents
Vertical micro-vortex flocculation clarifier Download PDFInfo
- Publication number
- CN203112564U CN203112564U CN 201220741915 CN201220741915U CN203112564U CN 203112564 U CN203112564 U CN 203112564U CN 201220741915 CN201220741915 CN 201220741915 CN 201220741915 U CN201220741915 U CN 201220741915U CN 203112564 U CN203112564 U CN 203112564U
- Authority
- CN
- China
- Prior art keywords
- seat
- shape
- place
- staving
- flocculator
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The utility model provides a vertical micro-vortex flocculation clarifier. The clarifier comprises a vertical bucket body and is characterized in that manholes are formed in the top surface and left side wall of the bucket body; supporting legs are uniformly distributed on the bottom surface of the peripheral wall of the bucket body; a water inlet pipe arranged in the center of the lower bottom surface; a sludge discharge pipe hole is formed at the left end of the lower bottom surface; a water outlet pipe hole is formed in the right side wall; a ring-shaped perforated pipe is arranged in the middle of the inner bottom surface; a sludge discharge pipe is communicated with the lower bottom surface at one end of the ring-shaped perforated pipe; a spherical micro-vortex flocculator seat on which water outlet holes are uniformly distributed is arranged in the center of the inner bottom surface; a hollow cylinder shaped partition is arranged on the micro-vortex flocculator seat; micro-vortex flocculators are filled in the partition; a #-shaped grid-like top plate is arranged on the upper end face of the partition; a ring-shaped water collecting tank is arranged on the peripheral wall of the partition; a ring-shaped net rack seat is arranged at the lower end of the peripheral wall of the partition; a tubular net rack is arranged on the edge of the net rack seat; a water outlet pipe is arranged on the bottom surface of the net rack seat; and a honeycomb inclined pipe is arranged between the notch of the water collecting tank and the net rack. The clarifier is suitable for clean water treatment.
Description
Technical field
The utility model relates to a kind of settler, particularly relates to a kind of vertical micro swirl flocculator-settler.
Background technology
In purification of water quality process in the past, use the equipment of traditional tank type usually, exist in its water purification process and take up an area of shortcomings such as big, that management is assorted, investment is many, cleaning water is low, loss is big.
In water purifying process, the clarification process of coagulating sedimentation adopts traditional dispensing, coagulation and depositing technology usually, and wherein most crucial technology is exactly coagulating treatment technology, and it directly has influence on the quality of water conditioning quality.Coagulation process is divided into waterpower and stirs and mechanical stirring two big classes, because the mechanical stirring energy is difficult to uniformly distributing, energy utilization efficiency is low, and the mechanical means maintenance workload is big in addition, and therefore, it is in the majority to use waterpower to stir coagulation process.The waterpower whipped form is varied, is nothing more than to make that former water and medicament are full and uniform to be mixed, and increases the velocity slope of current, increases the collision probability of taking off steady micelle.Prove that through a large amount of engineering practices waterpower or mechanical stirring form more little cohesion and the flocculation that more is conducive to the water-borne glue body of eddy current, it is best that the eddy current size approaches the diameter reaction effect that forms flco.The grid reaction pond of promoting the use of in recent years just is based on this theory.Along with being extensive use of of grid reaction pond, people recognize that the coagulation efficiency technology more in the past in grid reaction pond is significantly improved.Arrange that in the coagulating district grid, its purpose are exactly in order to form small vortex flow, micro swirl is conducive to the diffusion of particulate in the water, takes full advantage of fluid energy, increases the collision probability of taking off steady micelle.Yet, find that in engineering practice and production run grid reaction technology exists the making of grid and installation all to compare difficulty, secondly, when containing floating matter in the former water, mesh is easily blocked, needs periodic cleaning, in addition, grid generally adopts timber or bamboo wood to make, and work-ing life is shorter.
In sum, always in the traditional water treating processes many disadvantages that is difficult to overcome occur, especially also have long reaction time, the settling tank load is low, no mud concentrating function, and processing efficiency is low, and problem such as cost of water treatment height.
Summary of the invention
The purpose of this utility model is that a kind of improved vertical micro swirl flocculator-settler will be provided, it not only can concentrate micro swirl flocculation, tube settling and mud to organically combine effectively and be integral, but also improve water-purifying process coagulating efficient, improve water purification water quality, improve deposition efficiency and be conducive to mud and concentrate, floor space is few simultaneously.
Solution of the present utility model is to achieve the above object: vertical micro swirl flocculator-settler of the present utility model comprises a staving, described staving is vertical staving, described staving end face place establishes the manhole of a band top pressure closure, described staving left side wall place also establishes the manhole of a with closure, the place, bottom surface of described staving perisporium is evenly equipped with feet, the centre of described staving bottom surface is established the water-in pipe of a flanged seat, the left end place of described staving bottom surface establishes a mud discharging pore, described staving right side wall place is provided with a water outlet pore, the center of described staving inner bottom surface is established a shape perforated pipe ringwise, the bottom surface place of the described perforated pipe of shape ringwise one end is communicated with the mud discharging pipe of a flanged seat, the mud discharging pipe of described flanged seat and stretching out outside the mud discharging pore of the left end place of described staving bottom surface establishing, centre on the described staving inner bottom surface is established one and is micro swirl flocculator seat dome shape and that be evenly equipped with posticum on it, described being established a next door that is the hollow cylinder shape on micro swirl flocculator seat dome shape and that be evenly equipped with posticum on it, be filled with the micro swirl flocculator in the described next door that is the hollow cylinder shape, establish a top board that is the groined type grid on the described upper surface, next door that is the hollow cylinder shape, the described perisporium place that is the next door of hollow cylinder shape establishes the water leg of shape ringwise, the described lower end that is the next door perisporium of hollow cylinder shape is established the rack seat of shape ringwise, the rack seat edge of described shape ringwise establishes in a tubular form a rack, the place, bottom surface of the rack seat of described shape ringwise establishes the water outlet pipe of a flanged seat, the other end of the water outlet pipe of described flanged seat and stretching out outside the water outlet pore of establishing in described staving right side wall place is equipped with honeycomb inclined-tube between the notch place of the water leg of described shape ringwise and described in a tubular form the rack.
Also can set swash plate between the notch place of the water leg of described shape ringwise and described in a tubular form the rack.
Vertical micro swirl flocculator-settler of the present utility model mainly adopts vertical staving, and micro swirl flocculation, tube settling and mud are concentrated the synthetic stereoscopic-state in three districts.
Described micro swirl flocculation zone structure mainly is made of the top board that is the groined type grid that the centre on the described vertical staving inner bottom surface is on micro swirl flocculator seat dome shape and that be evenly equipped with posticum on it, the described micro swirl flocculator that is filling in the next door that is the hollow cylinder shape on micro swirl flocculator seat dome shape and that be evenly equipped with posticum on it, the described next door that is the hollow cylinder shape and the described upper surface, next door that is the hollow cylinder shape.
The honeycomb inclined-tube that sets between the notch place of the rack in a tubular form that the rack seat of the shape ringwise that the lower end of the water leg of the shape ringwise that described tube settling plot structure is mainly established by the described perisporium place that is the next door of hollow cylinder shape, the described next door perisporium that is the hollow cylinder shape is set, the rack seat edge of described shape ringwise are set and the water leg of described shape ringwise and described in a tubular form the rack constitutes.
The mud discharging pipe of the flanged seat that described mud enrichment region structure mainly is communicated with by the bottom surface place of the set perforated pipe of shape ringwise of the center of described staving, described staving inner bottom surface and the described perforated pipe of shape ringwise one end constitutes.
In the water treatment procedure of vertical micro swirl flocculator-settler of the present utility model, former water enters from the water-in pipe, be filled with in the next door that is the hollow cylinder shape of micro swirl flocculator in entering by uniform posticum on the set micro swirl flocculator seat that is dome shape of the centre on the described staving inner bottom surface, then be the top board that is the groined type grid set on the upper surface, next door of hollow cylinder shape and flow in the described staving from described, flow into the honeycomb inclined-tube import from a tubular form rack again, flowed out into the water leg of the shape of establishing in the described perisporium place that is the next door of hollow cylinder shape ringwise then by honeycomb inclined-tube outlet, at last the water outlet pipe output of the flanged seat of establishing from the place, bottom surface of the rack seat of described shape ringwise.
When being in the next door of hollow cylinder shape, water body flocculated by the micro swirl flocculator, mixed solution after the flocculation carries out mud-water separation through honeycomb inclined-tube again, the water that separates is exported through the water outlet pipe of the flanged seat that establish in the place, bottom surface of the rack seat of described shape ringwise, the bottom that mud enters described staving concentrates, and the mud discharging tube drainage of the flanged seat that the mud after concentrating regularly is communicated with through the bottom surface place of the set perforated pipe of shape ringwise of the center of described staving inner bottom surface and the described perforated pipe of shape ringwise one end goes out external.
Vertical micro swirl flocculator-settler of the present utility model has following advantage:
1, vertical micro swirl flocculator-settler of the present utility model will flocculate, depositing technology optimum combination, and the reaction times is short, the precipitation load is high, reliable, treatment effect is good.
2, selected the micro swirl flocculator for use in the micro swirl flocculation process that vertical micro swirl flocculator-settler of the present utility model adopts, the micro swirl flocculator is the hollow regular polygon of regular dodecahedron, and respectively establish five or six holes on each face, in each face, all has certain roughness on the outside surface, the micro-vortex energy of flow that the micro swirl flocculator forms promotes colloidal solid and suspended substance to condense in the micro swirl flocculator effectively, collision, three-dimensional contact flocculation, generate the alumen ustum of highly dense solidity, flocculating effect strengthens greatly, flocculation time only is 5～8 minutes, described micro swirl flocculator is difficult for stopping up, and can clean the back repeatedly and use.
3, the precipitation of vertical micro swirl flocculator-settler of the present utility model adopts tube settling technology, wetted perimeter is big, and hydraulic radius is little, and laminar flow regime is good, particles settling is not disturbed by turbulent flow, its processing power be rectangular sedimentation tank 3-5 doubly, accelerating purifying pool and plusator 2 times.
4, the sludge settling of vertical micro swirl flocculator-settler of the present utility model is located at the staving bottom of vertical micro swirl flocculator-settler, relies on the gravity thickened sludge, regularly carries out spoil disposal by the mud discharging pipe at last.
5, vertical micro swirl flocculator-settler of the present utility model is made as vertical staving shape, and compact construction, and volume is little, and floor space is few, takes full advantage of the space.
Description of drawings
Concrete structure of the present utility model is provided by following embodiment and accompanying drawing thereof.
Fig. 1 is the structural representation of vertical micro swirl flocculator-settler of the present utility model.
Embodiment
Below with reference to accompanying drawing vertical micro swirl flocculator-settler of the present utility model is described in further detail.
With reference to Fig. 1, the vertical micro swirl flocculator-settler of this utility model comprises a staving 1.
Described staving 1 is vertical staving, described staving 1 end face place establishes the manhole of a band top pressure closure, described staving 1 left side wall place also establishes the manhole of a with closure, described staving 1 right side wall place establishes a water outlet pore 4, the centre of described staving 1 bottom surface is established the water-in pipe 2 of a flanged seat, the left end place of described staving 1 bottom surface establishes a mud discharging pore 3, and the place, bottom surface of described staving 1 perisporium is evenly equipped with feet.
The center of described staving 1 inner bottom surface is established a shape perforated pipe 5 ringwise, the bottom surface place of the described perforated pipe of shape ringwise 5 one ends is communicated with the mud discharging pipe 6 of a flanged seat, the mud discharging pipe 6 of described flanged seat and stretching out outside the mud discharging pore of the left end place of described staving 1 bottom surface establishing 3.
Centre on described staving 1 inner bottom surface is established one and is micro swirl flocculator seat 8 dome shape and that be evenly equipped with posticum 7 on it, described being established a next door 9 that is the hollow cylinder shape on the micro swirl flocculator seat 8 dome shape and that be evenly equipped with posticum 7 on it, be filled with micro swirl flocculator 10 in the described next door 9 that is the hollow cylinder shape, establish a top board 11 that is the groined type grid on described 9 upper surfaces, next door that are the hollow cylinder shape.
The described perisporium place that is the next door 9 of hollow cylinder shape establishes the water leg 12 of shape ringwise, the described lower end that is next door 9 perisporiums of hollow cylinder shape is established the rack seat 13 of shape ringwise, rack seat 13 edges of described shape ringwise establish in a tubular form a rack 14, the place, bottom surface of the rack seat 13 of described shape ringwise establishes the water outlet pipe 15 of a flanged seat, the other end of the water outlet pipe 15 of described flanged seat and stretching out outside the water outlet pore of establishing in described staving 1 right side wall place 4 is equipped with honeycomb inclined-tube 16 between the notch place of the water leg 12 of described shape ringwise and described in a tubular form the rack 14.
Claims (2)
1. vertical micro swirl flocculator-settler, it comprises a staving (1), it is characterized in that described staving (1) is vertical staving, described staving (1) end face place establishes the manhole of a band top pressure closure, described staving (1) left side wall place also establishes the manhole of a with closure, the place, bottom surface of described staving (1) perisporium is evenly equipped with feet, the centre of described staving (1) bottom surface is established the water-in pipe (2) of a flanged seat, the left end place of described staving (1) bottom surface establishes a mud discharging pore (3), described staving (1) right side wall place is provided with a water outlet pore (4), the center of described staving (1) inner bottom surface is established a shape perforated pipe (5) ringwise, the bottom surface place of the described perforated pipe of shape ringwise (5) one ends is communicated with the mud discharging pipe (6) of a flanged seat, described mud discharging pipe (6) and stretching out outside the mud discharging pore of the left end place of described staving (1) bottom surface establishing (3), centre on described staving (1) inner bottom surface is established one and is micro swirl flocculator seat (8) dome shape and that be evenly equipped with posticum (7) on it, described being established a next door (9) that is the hollow cylinder shape on the micro swirl flocculator seat (8) dome shape and that be evenly equipped with posticum (7) on it, be filled with micro swirl flocculator (10) in the described next door (9) that is the hollow cylinder shape, establish a top board (11) that is the groined type grid on the described upper surface, next door (9) that is the hollow cylinder shape, the described perisporium place that is the next door (9) of hollow cylinder shape establishes a water leg of shape (12) ringwise, the described lower end that is next door (9) perisporium of hollow cylinder shape is established the rack seat (13) of shape ringwise, rack seat (13) edge of described shape ringwise establishes in a tubular form a rack (14), the place, bottom surface of the rack seat (13) of described shape ringwise establishes the water outlet pipe (15) of a flanged seat, the other end of the water outlet pipe (15) of described flanged seat and stretching out outside the water outlet pore of establishing in described staving (1) right side wall place (4) is equipped with honeycomb inclined-tube (16) between the notch place of the water leg of described shape ringwise (12) and described in a tubular form the rack (14).
2. a kind of vertical micro swirl flocculator-settler according to claim 1 is characterized in that being equipped with swash plate between the notch place of water leg (12) of described shape ringwise and described in a tubular form the rack (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220741915 CN203112564U (en) | 2012-12-31 | 2012-12-31 | Vertical micro-vortex flocculation clarifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220741915 CN203112564U (en) | 2012-12-31 | 2012-12-31 | Vertical micro-vortex flocculation clarifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203112564U true CN203112564U (en) | 2013-08-07 |
Family
ID=48892933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220741915 Expired - Lifetime CN203112564U (en) | 2012-12-31 | 2012-12-31 | Vertical micro-vortex flocculation clarifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203112564U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103850762A (en) * | 2014-01-16 | 2014-06-11 | 同济大学 | Diesel engine exhaust purification device adopting unconventional end surface carrier |
| CN104141347A (en) * | 2014-07-14 | 2014-11-12 | 江苏永钢集团有限公司 | Swirling well |
| CN109354246A (en) * | 2018-11-15 | 2019-02-19 | 山东科技大学 | A kind of high-concentration sewage quick treatment device and its processing method |
-
2012
- 2012-12-31 CN CN 201220741915 patent/CN203112564U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103850762A (en) * | 2014-01-16 | 2014-06-11 | 同济大学 | Diesel engine exhaust purification device adopting unconventional end surface carrier |
| CN104141347A (en) * | 2014-07-14 | 2014-11-12 | 江苏永钢集团有限公司 | Swirling well |
| CN109354246A (en) * | 2018-11-15 | 2019-02-19 | 山东科技大学 | A kind of high-concentration sewage quick treatment device and its processing method |
| CN109354246B (en) * | 2018-11-15 | 2023-09-26 | 山东科技大学 | High-concentration sewage rapid treatment device and treatment method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201890794U (en) | Novel high-efficiency physicochemical water treatment settling tank device | |
| CN202590444U (en) | Tube-in-tube clarification pool | |
| CN104230048A (en) | Integrated efficient precipitation equipment and application | |
| CN104941265A (en) | Rotational flow efficient separation silt clarifying basin and treatment technology | |
| CN203112564U (en) | Vertical micro-vortex flocculation clarifier | |
| CN108328786A (en) | A kind of water treatment facilities and method for treating water | |
| CN102145953A (en) | Combined sewage treatment system | |
| CN101530681A (en) | Seawater clarifier turbulence construction and clarifier thereof | |
| CN202844656U (en) | Vortex flocculation-clearing equipment | |
| CN102424488B (en) | Integrated-process rural water purifier based on micro-eddy flocculation | |
| CN104478080B (en) | The efficiently heavy stream aerobic reactor of honeycomb fashion | |
| CN203079732U (en) | U-shaped micro swirl flocculation sedimentation tank | |
| CN103990302B (en) | A kind of radial-flow type sedimentation device | |
| CN202526949U (en) | Integrated sedimentation clarification tank | |
| CN109293079B (en) | Low-energy-consumption aeration circulation clarification tank | |
| CN203108283U (en) | Micro-vortex flocculation clarifier | |
| CN201386049Y (en) | High turbidity water and waste water filtering and purifying system | |
| CN208684599U (en) | A kind of double-layer integrally water purification apparatus | |
| CN201694908U (en) | Combined sewage disposal system | |
| CN105858839B (en) | It is a kind of tangentially to enter ability of swimming clarifying basin | |
| CN204170466U (en) | A kind of inward eddy structure of New-type Swirl Flow settling vessel | |
| CN207412830U (en) | Sedimentation basin | |
| CN108147642A (en) | Highly effective sludge concentration basin | |
| CN204170464U (en) | A kind of New-type Swirl Flow settling vessel | |
| CN201713369U (en) | Coagulation reaction equipment and sewage treatment system provided with the same |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130807 |
|
| CX01 | Expiry of patent term |