CN205367944U - Carry out filterable processing system to lake water - Google Patents
Carry out filterable processing system to lake water Download PDFInfo
- Publication number
- CN205367944U CN205367944U CN201620166236.7U CN201620166236U CN205367944U CN 205367944 U CN205367944 U CN 205367944U CN 201620166236 U CN201620166236 U CN 201620166236U CN 205367944 U CN205367944 U CN 205367944U
- Authority
- CN
- China
- Prior art keywords
- water
- layer
- siphon
- process system
- room
- 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 - Fee Related
Links
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model provides a carry out filterable processing system to lake water, including two the same filters, every filter includes the vessel, the U -shaped inlet tube, the siphon tedge, the siphon downtake, the siphon auxiliary tube, the siphon destroys pipe and water sealed tank, vessel inner chamber from the top down divide into the sparge water in order and holds the room greatly, filter chamber and collecting chamber, the sparge water holds greatly to be separated by tapered hood between room and the filter chamber, the tapered hood opening down, the tapered hood outer fringe is fixed in on the vessel, filter chamber and collecting chamber are separated by the perforated plate, the perforated plate outer fringe is fixed in on the vessel, the filtering layer is arranged on the perforated plate, the riser from the top down that the communication sparge water holds room and collecting chamber greatly passes tapered hood in order, filtering layer and perforated plate, the end of intaking of outlet pipe sets up in the sparge water holds the room greatly.
Description
Technical field
This utility model relates to water treatment field, is specifically related to a kind of process system Lake Water precipitated and filter.
Background technology
Lake refer to that depression, land hydrops is formed, flow water body slowly.Containing two class impurity in Lake Water, first kind impurity is float, and granule is maximum, and its diameter is about 1 × 10-4More than mm, this kind of impurity exists with unsure state in water, is easier to separate from water body；Equations of The Second Kind impurity is colloid, is in general that particle diameter is 1 × 10-6mm-1×10-4Between mm, it it is the aggregation of many molecules and ion.Relative well water compare with spring water Lake Water also have float and colloid relatively more.
Existing filter includes intake chamber, U-shaped water inlet pipe, filter chamber, collecting chamber, flush box, outlet pipe, siphon tedge, siphon down-comer, auxiliary siphon tube, siphon destructing tube and water sealed tank, pending water sequentially enters filter chamber via intake chamber and U-shaped water inlet pipe, then then through after being filtered by filtering layer, enter collecting chamber, water in collecting chamber enters flush box via gathering tube, the water of flush box is the water after filtering, and discharges from outlet pipe.This filtration system has automatic back-flushing function, namely periodically automatically filtering layer can be carried out back flush, with clean filter bed.The water of backwash filtering layer is from the water in flush box, and each backwash water amount is the water that flush box can contain appearance between siphon destructing tube lower end to outlet pipe top.
Summary of the invention
The technical problems to be solved in the utility model is to provide a kind of process system that Lake Water is filtered, so that Lake Water is carried out purified treatment.
In order to solve above-mentioned technical problem, the technical solution of the utility model is:
A kind of process system that Lake Water is filtered, including two identical filters；Each filter includes vessel, U-shaped water inlet pipe, siphon tedge, siphon down-comer, auxiliary siphon tube, siphon destructing tube and water sealed tank, vessel inner chamber is sequentially divided into flushing water to contain room from top to bottom, filter chamber and collecting chamber, flushing water is contained and is separated by cone-shaped hood between room and filter chamber, cone-shaped hood is opening down, cone-shaped hood outer rim is fixed on vessel, filter chamber and collecting chamber are separated by porous plate, porous plate outer rim is fixed on vessel, filtering layer is arranged on porous plate, link up flushing water and contain the standpipe of room and collecting chamber from top to bottom sequentially through cone-shaped hood, filtering layer and porous plate, the water inlet end of outlet pipe is arranged at flushing water and contains in room.
The above-mentioned process system that Lake Water is filtered, the flushing water of two filters is contained the bottom of room and is connected by communicating pipe.
The above-mentioned process system that Lake Water is filtered, the upper end of the U-shaped water inlet pipe of each filter connects an intake chamber, and two intake chambers are to be formed by dividing plate segmentation by the inner chamber of an inlet water tank.
The above-mentioned process system that Lake Water is filtered, the upstream of inlet water tank arranges accelerator.
The above-mentioned process system that Lake Water is filtered, the water sealed tank of two filters shares.
The above-mentioned process system that Lake Water is filtered, vessel and cone-shaped hood are reinforced concrete structure.
The above-mentioned process system that Lake Water is filtered, siphon down-comer lower end arranges the taper opening and closing element regulating siphon down-comer lower port aperture size, and upward, taper opening and closing element is connected on the elevating lever realizing the lifting of taper opening and closing element at taper opening and closing element tip.
The above-mentioned process system that Lake Water is filtered, siphon down-comer arranges the butterfly valve regulating siphon down-comer area of passage.
The above-mentioned process system that Lake Water is filtered, the water exit end of penstocks oliquely downward extends and is followed by auxiliary siphon tube upper end.
The above-mentioned process system that Lake Water is filtered, filtering layer includes ground floor thick for the 70cm that sequentially arranges from top to bottom, the second layer thick for 5cm, third layer thick for 5cm, thick for 5cm the 4th layer, layer 5 thick for 5cm and layer 6, ground floor is particle diameter is the natural stone diamond stone filter material layer of 0.5-1mm, the second layer is particle diameter is the gravel by nature layer of 2-4mm, third layer is particle diameter is the gravel by nature layer of 6-8mm, 4th layer is gravel by nature layer that particle diameter is 12-18mm, layer 5 is particle diameter is the gravel by nature layer of 20-25mm, and layer 6 is the 30 double-deck order Buddhist nun's floss nets.
Vessel inner chamber is sequentially divided into flushing water to contain room, filter chamber and collecting chamber from top to bottom, flushing water is contained and is separated by cone-shaped hood between room and filter chamber, filter chamber and collecting chamber are separated by porous plate, achieve flushing water and contain the compact conformation design of room, filter chamber and collecting chamber, make them all in vessel.The tip of cone-shaped hood is upward so that gas can converge in cone-shaped hood tip place, it is easy to drains gas before automatic backwash, does not affect follow-up backwash.Standpipe, from top to bottom sequentially through cone-shaped hood, filtering layer and porous plate, is linked up flushing water and is contained room and collecting chamber, it is achieved that inside vessel, the water of collecting chamber is sent into flushing water and contains in room.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, this utility model is described in further detail:
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of filter.
Fig. 3 is the top view of cone-shaped hood.
Fig. 4 is the schematic diagram of bar-mat reinforcement in part conic cover.
Fig. 5 is the schematic diagram of end toper opening and closing element under siphon down-comer.
Fig. 6 is the schematic diagram of inlet water tank.
Fig. 7 is the part-structure schematic diagram of filter.
Fig. 8 is A-A direction view in Fig. 7.
In figure: 1 filter, 2 filters, 3 communicating pipes, 4U shape water inlet pipe, 5 taper opening and closing elements, 6 siphon down-comers, 7 auxiliary siphon tubes, 8 water sealed tanks, 9 penstocks, 10 elevating levers, 11 outlet pipes, 12 siphon destructing tubes, 13 cone-shaped hoods, 14 standpipes, 15 siphon tedges, 16 vessels, 17 filtering layers, 18 porous plates.
Detailed description of the invention
As shown in Figures 1 to 8, a kind of process system that Lake Water is filtered, including two identical filters (1 and 2).Each filter includes vessel 16, U-shaped water inlet pipe 4, siphon tedge 15, siphon down-comer 6, auxiliary siphon tube 7, siphon destructing tube 12 and water sealed tank 8.Vessel inner chamber is sequentially divided into flushing water to contain room, filter chamber and collecting chamber from top to bottom, and flushing water is contained and separated by cone-shaped hood 13 between room and filter chamber, and cone-shaped hood is opening down, and cone-shaped hood outer rim is fixed on vessel.Filter chamber and collecting chamber are separated by porous plate 18, and porous plate outer rim is fixed on vessel, are used for supporting filtering layer.Filtering layer 17 is arranged on porous plate, links up flushing water and contains the standpipe 14 of room and collecting chamber from top to bottom sequentially through cone-shaped hood, filtering layer and porous plate, and the water inlet end of outlet pipe 11 is arranged at flushing water and contains in room.
The flushing water of two filters contains the bottom of room by connecting communicating pipe 3, when a Filter Back Washing, it is possible to introduces another filter flushing water and contains the water of room so that backwashing time is longer, and backwash effect is better.
The upper end of the U-shaped water inlet pipe of each filter connects an intake chamber, and two intake chambers are to be formed by dividing plate segmentation by the inner chamber of an inlet water tank.
The upstream of inlet water tank arranges accelerator so that first water carry out clarifying treatment at accelerator, is then filtered then through by single filter.
Specifically, the water sealed tank of two filters shares.
Vessel and cone-shaped hood are reinforced concrete structure, and long service life, expenditure of construction is low.
Siphon down-comer lower end arranges the taper opening and closing element 20 regulating siphon down-comer lower port aperture size, and upward, taper opening and closing element is connected on the elevating lever 19 realizing the lifting of taper opening and closing element, to regulate the intensity of backwash at taper opening and closing element tip.
The structure of the another kind of intensity regulating backwash is: arrange the butterfly valve regulating siphon down-comer area of passage on siphon down-comer.
The water exit end of penstocks 9 oliquely downward extends and is followed by auxiliary siphon tube upper end, it is possible to achieve force backwash, by the press water of penstocks by auxiliary siphon tube, by realizations pressure backwash.
Filtering layer includes ground floor thick for the 70cm that sequentially arranges from top to bottom, the second layer thick for 5cm, third layer thick for 5cm, thick for 5cm the 4th layer, layer 5 thick for 5cm and layer 6, ground floor is particle diameter is the natural stone diamond stone filter material layer of 0.5-1mm, the second layer is particle diameter is the gravel by nature layer of 2-4mm, third layer is particle diameter is the gravel by nature layer of 6-8mm, 4th layer is gravel by nature layer that particle diameter is 12-18mm, layer 5 is particle diameter is the gravel by nature layer of 20-25mm, and layer 6 is the 30 double-deck order Buddhist nun's floss nets.
Claims (10)
1. the process system that Lake Water is filtered by a kind, it is characterised in that: include two identical filters；Each filter includes vessel, U-shaped water inlet pipe, siphon tedge, siphon down-comer, auxiliary siphon tube, siphon destructing tube and water sealed tank, vessel inner chamber is sequentially divided into flushing water to contain room from top to bottom, filter chamber and collecting chamber, flushing water is contained and is separated by cone-shaped hood between room and filter chamber, cone-shaped hood is opening down, cone-shaped hood outer rim is fixed on vessel, filter chamber and collecting chamber are separated by porous plate, porous plate outer rim is fixed on vessel, filtering layer is arranged on porous plate, link up flushing water and contain the standpipe of room and collecting chamber from top to bottom sequentially through cone-shaped hood, filtering layer and porous plate, the water inlet end of outlet pipe is arranged at flushing water and contains in room.
2. the process system that Lake Water is filtered according to claim 1, it is characterised in that: the flushing water of two filters is contained the bottom of room and is connected by communicating pipe.
3. the process system that Lake Water is filtered according to claim 1 and 2, it is characterised in that: the upper end of the U-shaped water inlet pipe of each filter connects an intake chamber, and two intake chambers are to be formed by dividing plate segmentation by the inner chamber of an inlet water tank.
4. the process system that Lake Water is filtered according to claim 3, it is characterised in that: the upstream of inlet water tank arranges accelerator.
5. the process system that Lake Water is filtered according to claim 1 and 2, it is characterised in that: the water sealed tank of two filters shares.
6. the process system that Lake Water is filtered according to claim 1 and 2, it is characterised in that: vessel and cone-shaped hood are reinforced concrete structure.
7. the process system that Lake Water is filtered according to claim 1 and 2, it is characterized in that: siphon down-comer lower end arranges the taper opening and closing element regulating siphon down-comer lower port aperture size, upward, taper opening and closing element is connected on the elevating lever realizing the lifting of taper opening and closing element at taper opening and closing element tip.
8. the process system that Lake Water is filtered according to claim 1 and 2, it is characterised in that: siphon down-comer arranges the butterfly valve regulating siphon down-comer area of passage.
9. the process system that Lake Water is filtered according to claim 1 and 2, it is characterised in that: the water exit end of penstocks oliquely downward extends and is followed by auxiliary siphon tube upper end.
10. the process system that Lake Water is filtered according to claim 1 and 2, it is characterized in that: filtering layer includes the ground floor thick for 70cm sequentially arranged from top to bottom, the second layer that 5cm is thick, the third layer that 5cm is thick, thick for 5cm the 4th layer, the layer 5 of 5cm thickness and layer 6, ground floor is particle diameter is the natural stone diamond stone filter material layer of 0.5-1mm, the second layer is particle diameter is the gravel by nature layer of 2-4mm, third layer is particle diameter is the gravel by nature layer of 6-8mm, 4th layer is gravel by nature layer that particle diameter is 12-18mm, layer 5 is particle diameter is the gravel by nature layer of 20-25mm, layer 6 is the 30 double-deck order Buddhist nun's floss nets.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620166236.7U CN205367944U (en) | 2016-03-05 | 2016-03-05 | Carry out filterable processing system to lake water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620166236.7U CN205367944U (en) | 2016-03-05 | 2016-03-05 | Carry out filterable processing system to lake water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205367944U true CN205367944U (en) | 2016-07-06 |
Family
ID=56265655
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620166236.7U Expired - Fee Related CN205367944U (en) | 2016-03-05 | 2016-03-05 | Carry out filterable processing system to lake water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205367944U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107401209A (en) * | 2017-08-02 | 2017-11-28 | 徐文斌 | Rainwater-collecting purifies and is used for the equipment afforested in a kind of park |
-
2016
- 2016-03-05 CN CN201620166236.7U patent/CN205367944U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107401209A (en) * | 2017-08-02 | 2017-11-28 | 徐文斌 | Rainwater-collecting purifies and is used for the equipment afforested in a kind of park |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206473882U (en) | A kind of tandem type multi-stage filter | |
| CN203648255U (en) | Centrifugal filter-screen type sediment filtering device | |
| CN106310746A (en) | Tandem type multistage filtering device | |
| US20010022286A1 (en) | Filtration system including a back washable pre-filtration apparatus | |
| CN205367944U (en) | Carry out filterable processing system to lake water | |
| CN208561915U (en) | A kind of environmental protection self-loopa platemaking machine | |
| CN213555698U (en) | Water treatment is with having filtration jar of preventing blockking up function | |
| CN210613021U (en) | Metal film filter core, metal film filter and sewage treatment depth filtration system | |
| CN207811404U (en) | It is a kind of can auto-flushing ultrafiltration central purifier | |
| CN205886317U (en) | Valveless filter is tied to gas -tight | |
| CN207032456U (en) | One kind building rainwater treatment dirt separation | |
| CN203253216U (en) | Siphonic valveless filtering pool | |
| CN205627213U (en) | Vertical multicavity room sandstone filtration ware | |
| CN203208743U (en) | Separate bed automatic inverted filter device | |
| CN205886321U (en) | Valveless filter | |
| CN204079564U (en) | Novel tiny flocculation water purifier | |
| CN204569519U (en) | Poly-repelling crude oil storage tank sewage purification machinery | |
| CN104511188A (en) | Novel filter tank | |
| CN202605812U (en) | Horizontal type high speed filter tank | |
| CN103157308B (en) | Divide the automatic anti-filter device of bed | |
| CN216549883U (en) | Carbon sand filters jar | |
| CN209020200U (en) | A kind of filter using tube microfiltration membrane | |
| CN220714923U (en) | Pipeline arrangement structure of air-water backwashing filter tank | |
| CN208065858U (en) | A kind of sandstone filter device | |
| CN107583442A (en) | The automatic hydrogen sulphide removing device of petroleum tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160706 Termination date: 20170305 |