CN207605410U - Integral cyclone separator for mud and water - Google Patents
Integral cyclone separator for mud and water Download PDFInfo
- Publication number
- CN207605410U CN207605410U CN201721518717.0U CN201721518717U CN207605410U CN 207605410 U CN207605410 U CN 207605410U CN 201721518717 U CN201721518717 U CN 201721518717U CN 207605410 U CN207605410 U CN 207605410U
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- CN
- China
- Prior art keywords
- mud
- separator
- water
- injection well
- area
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- 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.)
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 230000008021 deposition Effects 0.000 claims abstract description 18
- 238000002347 injection Methods 0.000 claims abstract description 13
- 239000007924 injection Substances 0.000 claims abstract description 13
- 230000000694 effects Effects 0.000 abstract description 8
- 238000000926 separation method Methods 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 abstract description 4
- 238000001514 detection method Methods 0.000 abstract description 2
- 238000012856 packing Methods 0.000 abstract description 2
- 239000002245 particle Substances 0.000 description 18
- 238000004062 sedimentation Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 3
- 238000005352 clarification Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Abstract
The utility model is related to Integral cyclone separator for mud and water, separator sets gradually injection well downhole flow regulator, sloping plate deposition district and taper mud collection area from top to bottom, sloping plate deposition district is two, it is symmetrically distributed in the left and right of separator interior, the top of separator is equipped with catch basin, injection well downhole flow regulator is arranged in the middle and upper part of separator, and injection well downhole flow regulator is made of multiple water distribution lattice.This equipment uses middle part water distribution manner, sewage is after injection well downhole flow regulator, it quickly enters Disengagement zone and carries out mud-water separation, dedicated novel inclined plate packing is arranged in Disengagement zone, effectively improve the effect of mud-water separation, mud collector is arranged in separator bottom, by online mud-water interface apparatus detection mud position, according to mud place value automatic mud removing.
Description
Technical field
The utility model is related to field of sewage treatment equipment, specially Integral cyclone separator for mud and water.
Background technology
Tube settler used at present, the defect being primarily present have：Mud amount on unit area is high, holds when spoil disposal is unsmooth
It is also easy to produce anti-mud phenomenon, makes water outlet water quality deterioration；Water residence time in pond is short, when change of water quality is larger, anti impulsion load
Energy force difference；Inclined plate（Pipe）Spacing（Caliber）It is small, it is easy between plate（Caliber）Deposition, inclined plate（Pipe）Spacing（Caliber）Size and row
The unobstructed of mud more difficult is taken into account；It is low for the suspended matter removal efficiency of proportion 1 or so.
Invention content
In order to make up drawbacks described above, the utility model provides Integral cyclone separator for mud and water, solves inclined plate high load capacity
Shorten particle settling height using special construction inclined plate with the contradiction of rapid effectively spoil disposal, greatly improve treatment effeciency and resistance to punching
Load-bearing capacity is hit, for the suspended matter of proportion 1 or so, optimization water distribution, captation ensure treatment effect.
The technical solution of the utility model is：Integral cyclone separator for mud and water, separator is set gradually from top to bottom matches
Hydrophone, sloping plate deposition district and taper mud collection area, sloping plate deposition district are two, are symmetrically distributed in the left and right of separator interior, are detached
The both sides of device are equipped with water outlet, and injection well downhole flow regulator is arranged in the middle and upper part of separator, and injection well downhole flow regulator is made of multiple water distribution lattice, water distribution lattice
It is inside provided with sparge pipe, sparge pipe is passed into the sloping plate deposition district at both ends in the middle part of separator, and the inner wall of separator is equipped with
Holder for fixing inclined plate, inclined plate setting is multiple, is axially arranged in parallel on bottom plate, inclined plate and horizontal angle
It it is 60 °, the other side of bottom plate is equipped with the fin being axially arranged in parallel, and fin is 135 ° with horizontal angle.
It is divided into sloping plate deposition district described in the utility model close to bottom plate main flow area, close to the vortex of fin and fin
Between circulating-area, the flow velocity of the circulating-area is the 1/5-1/4 of main flow area.
The utility model 40~60mm of fin height, 60~75mm of spacing.
The utility model settling zone uses intermediate water distribution, the lateral flow mode flowed to pond body both ends.It is identical as sectional area
Pond body comparison, cloth water area increase by 1 times, water velocity reduce by 50%.
The utility model increases vertical fin on novel all-in-one double-cyclone separator for mud and water（Fin height 40~
60mm, 60~75mm of spacing）, along the advance of main flow area direction, another part then enters main flow area and has a common boundary with fin a part
The eddy flow area at place.It on the one hand travels forward in the particle of main flow area movement, is on the one hand deposited to the partial particulate in eddy flow area with rotation
Stream is another to play movement, these particles in eddy flow area are transported to eddy flow near the fin of downstream, when eddy flow and the fin
When top and top collide, which part particle enters in inclined plate area, and partial particulate flows to next oblique grid together with mainstream
Plate area, the particle being transported in inclined plate are slowly moved with interior circulation, are concentrated on bottom inclined plate, are slided into mud-removing bucket, into inclined plate
Interior superfine little particle, or cannot precipitate in slow circulation movement, or bottom inclined plate has been touched, then again by ring
Stream rushes, then may flow out this oblique grid plate area.Flowing of the circulation energy from main flow area in inclined plate, eddy flow collide the downstream wing
When piece, the energy that is transmitted maintains its cycle.Circulating-area flow velocity, substantially 1/4~1/5 or so of main flow area, thus slowly
Flow velocity make circulation close to laminar condition be conducive to particle sedimentation.And under circulation centrifugal force effect, particle precipitates on one side
It is thrown toward four wall of inclined plate on one side, as long as so general particle just can precipitate into inclined plate, this low speed ring of novel inclined plate
Stream causes well to precipitate environment and inclined plate reactor is made to have High-rate sedimentation effect.After inclined plate, sediment is in inclined plate bottom side
Surface is accumulated into thin mud layer, and bucket is slided to by gravity sludge, and the water after clarification is discharged from catch basin is flow to.
The beneficial effects of the utility model are：This equipment use middle part water distribution manner, sewage after injection well downhole flow regulator, rapidly into
Enter Disengagement zone and carries out mud-water separation.Dedicated novel inclined plate packing is arranged in Disengagement zone, effectively improves the effect of mud-water separation, point
Mud collector is set from device bottom, by online mud-water interface apparatus detection mud position, according to mud place value automatic mud removing；The utility model inclined plate
The surface loading of settling zone reaches 15m3/m2.h, it is 2.5~5 times of common process.Residence time is short, and sedimentation effect is high, processing
It is efficient；Mud, water flowing be not in the same direction, avoids and interferes with each other, and reduces the generation for running mud phenomenon；Inclined plate water flow inside runner is logical
Freely, no sidewise restraint, more conducively alumen ustum sedimentation separation are not easy deposition folder mud；Lateral flow designs, and short flow phenomenon, cloth will not occur
Water catchments uniformly, stable, easy to operate；The utility model is simple in structure, take up an area province, small investment, it is efficient, without rapid wear
Part, durable, maintenance cost is low.
Description of the drawings
Fig. 1 is the overall structure diagram of the utility model.
Fig. 2 is the utility model sloping plate deposition district schematic diagram.
Fig. 3 is the utility model sloping plate deposition district operation principle structural schematic diagram.
Fig. 4 is the utility model water distribution lattice structural schematic diagram.
Specific implementation mode
The present embodiment is further described below in conjunction with the accompanying drawings：
Integral cyclone separator for mud and water, separator set gradually injection well downhole flow regulator 1, sloping plate deposition district 2 and taper from top to bottom
Mud collection area 3, sloping plate deposition district 2 are two, are symmetrically distributed in the left and right of separator interior, and the top of separator is equipped with catch basin 4,
Injection well downhole flow regulator 1 is arranged in the middle and upper part of separator, and injection well downhole flow regulator is made of multiple water distribution lattice 13, and sparge pipe 5 is provided in water distribution lattice 13,
Sparge pipe 5 is passed into the sloping plate deposition district 2 at both ends in the middle part of separator, and the inner wall of separator is equipped with for fixing inclined plate
Holder 6, the inclined plate 7 are arranged multiple, axial direction and are arranged in parallel on bottom plate 8, and inclined plate 7 and horizontal angle are 60 °, bottom plate
8 other side is equipped with the fin 9 being axially arranged in parallel, and fin 9 and horizontal angle are 135 °.
It is divided into sloping plate deposition district described in the utility model close to bottom plate main flow area 10, close to the vortex 11 of fin 9
Circulating-area 12 between fin 9, the flow velocity of the circulating-area are the 1/5-1/4 of main flow area.
The utility model fin 9 height 40~60mm, 60~75mm of spacing.
The utility model Integral cyclone separator for mud and water major function is high-turbidity sewage of the clarification after flocculation, this sets
It is standby to be suitable for coal mine high concentrtion mine water, mine wastewater, abrasive waste water etc. containing sticking containing solid class waste water.Dirt containing particle
Water is after flocculation reaction, and after water distributor special, into novel inclined plate, a part is advanced along main flow area direction, another part
Then enter the vortex of main flow area and fin intersection.It on the one hand travels forward in the particle of main flow area movement, it is on the one hand heavy
The partial particulate to form sediment to vortex plays movement with vortex is another, these particles in vortex are transported to downstream with vortex
Near fin, when vortex collides at the top of the fin and top, which part particle enters in inclined plate area, partial particulate
With next oblique grid plate area is flowed to together with mainstream, the particle being transported in inclined plate slowly moves with interior circulation, it is oblique to concentrate on bottom
Plate slides into mud-removing bucket, into the superfine little particle in inclined plate, or cannot precipitate in slow circulation movement, or connect
It contacts bottom inclined plate, is then rushed again by circulation, then may flow out this oblique grid plate area.
Flowing of the circulation energy from main flow area in inclined plate, when vortex collides downstream fin, the energy transmitted comes
Maintain its cycle.Circulating-area flow velocity, substantially 1/4~1/5 or so of main flow area, thus slow flow velocity make circulation close to layer
Stream mode is conducive to particle sedimentation.And under circulation centrifugal force effect, particle is thrown toward four wall of inclined plate, institute while precipitating
As long as just can be precipitated into inclined plate with general particle, this low speed circulation of novel inclined plate causes well to precipitate environment to be oblique
Novel inclined plate has one of the reason of High-rate sedimentation effect.
Claims (3)
1. Integral cyclone separator for mud and water, it is characterised in that：Separator sets gradually injection well downhole flow regulator, sloping plate deposition district from top to bottom
With taper mud collection area, sloping plate deposition district is two, is symmetrically distributed in the left and right of separator interior, and the top of separator, which is equipped with, catchments
Slot, injection well downhole flow regulator are arranged in the middle and upper part of separator, and injection well downhole flow regulator is made of multiple water distribution lattice, is provided with sparge pipe in water distribution lattice, matches
Water pipe is passed into the sloping plate deposition district at both ends in the middle part of separator, and the inner wall of separator is equipped with the branch for fixing inclined plate
Frame, inclined plate setting is multiple, it is axial be arranged in parallel on bottom plate, inclined plate and horizontal angle are 60 °, bottom plate it is another
Side is equipped with the fin being axially arranged in parallel, and fin and horizontal angle are 135 °.
2. Integral cyclone separator for mud and water according to claim 1, it is characterised in that：Divide in the sloping plate deposition district
Flow velocity for the circulating-area between the vortex and fin of bottom plate main flow area, close fin, the circulating-area is mainstream
The 1/5-1/4 in area.
3. Integral cyclone separator for mud and water according to claim 1 or 2, it is characterised in that：40~60mm of fin height,
60~75mm of spacing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721518717.0U CN207605410U (en) | 2017-11-15 | 2017-11-15 | Integral cyclone separator for mud and water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721518717.0U CN207605410U (en) | 2017-11-15 | 2017-11-15 | Integral cyclone separator for mud and water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207605410U true CN207605410U (en) | 2018-07-13 |
Family
ID=62795375
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721518717.0U Expired - Fee Related CN207605410U (en) | 2017-11-15 | 2017-11-15 | Integral cyclone separator for mud and water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207605410U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113101705A (en) * | 2021-04-17 | 2021-07-13 | 开封国安供水设备有限公司 | Pressure type horizontal flow vertical sludge discharge accelerated precipitation device |
-
2017
- 2017-11-15 CN CN201721518717.0U patent/CN207605410U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113101705A (en) * | 2021-04-17 | 2021-07-13 | 开封国安供水设备有限公司 | Pressure type horizontal flow vertical sludge discharge accelerated precipitation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180713 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |