CN203565212U - Flocculation concentration whirlcone - Google Patents
Flocculation concentration whirlcone Download PDFInfo
- Publication number
- CN203565212U CN203565212U CN201320797765.3U CN201320797765U CN203565212U CN 203565212 U CN203565212 U CN 203565212U CN 201320797765 U CN201320797765 U CN 201320797765U CN 203565212 U CN203565212 U CN 203565212U
- Authority
- CN
- China
- Prior art keywords
- desilting
- port
- box
- desilting mouth
- whirlcone
- 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
Images
Landscapes
- Cyclones (AREA)
Abstract
The utility model relates to a flocculation concentration whirlcone, comprising a feed port, an overflow port, a desilting port and a thickening box, wherein one end of the thickening box is provided with the desilting port; the other end of the thickening box is provided with a spiral discharging mechanism; the thickening box is provided with a low concentration thick liquid outward discharging pipe between the desilting port and the spiral discharging mechanism; a desilting port straight pipe is arranged outside the desilting port; the desilting port straight pipe stretches into the thickening box. The flocculation concentration whirlcone also comprises a flocculating agent adding pipe which is arranged on the desilting port straight pipe, and stretches out of the box body of the thickening box, a proper amount of flocculating agent is added into the thickening box by the flocculating agent adding pipe, the settling velocity of thick liquid is increased, the desilting productive rate of the whirlcone is greatly increased, and the energy consumption is reduced.
Description
Technical field
The utility model relates to a kind of flocculation concentration cyclone, and it comprises charging aperture, overfall and desilting mouth.
Background technology
Hydrocyclone is a kind of centrifugal force field separation equipment, is widely used in the departments such as ore dressing, chemical industry, oil.Concentrated is one of very important purposes of cyclone.Existing cyclone as shown in Figure 2, comprises charging aperture 11, overfall 12 and desilting mouth 13, but relatively simple for structure, in order to improve the desilting concentration of cyclone, conventionally take to reduce the diameter of desilting mouth 13, but desilting productive rate has also reduced simultaneously, will sacrifice like this desilting productive rate of cyclone.So in order to improve desilting concentration and to improve desilting productive rate and constantly find reasonable approach.
Utility model content
Technical problem to be solved in the utility model is to provide a kind of flocculation concentration cyclone.
The technical scheme that the utility model solves the problems of the technologies described above is as follows: a kind of flocculation concentration cyclone, it comprises charging aperture, overfall and desilting mouth, also comprise board concentrating box, one end of described board concentrating box is provided with described desilting mouth, the other end of described board concentrating box is provided with screw unloading mechanism, and described board concentrating box is provided with comb outside low-concentration pulp between described desilting mouth and described screw unloading mechanism; The outside of described desilting mouth is provided with desilting mouth straight tube, and described desilting mouth straight tube stretches into the inside of described board concentrating box.
The beneficial effects of the utility model are: the utility model has increased slurry sinking speed, can greatly increase like this desilting productive rate of cyclone, have reduced energy consumption.
Further, also comprise flocculant adding tube, described flocculant adding tube is arranged on described desilting mouth straight tube, and described flocculant adding tube is stretched out outside the casing of described board concentrating box.
Further beneficial effect is: by flocculant adding tube, to board concentrating box, add flocculant, more improved the desilting productive rate of cyclone.
Accompanying drawing explanation
Fig. 1 is common hydrocyclone structure schematic diagram;
Fig. 2 is the utility model structural representation.
In accompanying drawing, the list of parts of each label representative is as follows:
1, cyclone, 11, charging aperture, 12, overfall, 13, desilting mouth, 14, flocculant adding tube, 15, desilting mouth straight tube, 2, board concentrating box, 21, the outer comb of low-concentration pulp, 22, screw unloading mechanism.
The specific embodiment
Below in conjunction with accompanying drawing, principle of the present utility model and feature are described, example, only for explaining the utility model, is not intended to limit scope of the present utility model.
Below in conjunction with Fig. 2, a kind of flocculation concentration cyclone of the utility model is described.
The utility model is below the desilting mouth 13 of cyclone 1, to increase a board concentrating box 2, and board concentrating box 2 bottoms increase screw unloading mechanism 22; In the outside of desilting mouth 13, increase desilting mouth straight tube 15 simultaneously, at desilting mouth straight tube 15, increase flocculant adding tube 14, and flocculant adding tube 14 is stretched out outside the casing of board concentrating box 2; Appropriate location at board concentrating box 2 increases comb 21 outside low-concentration pulp, and take between desilting Kou13He screw unloading mechanism 22 this example appropriate location.
When slurry enters after the charging aperture 11 of cyclone 1, high concentration and coarse granule ore pulp are discharged from desilting mouth 13, and fine grained is discharged from overfall 12; The slurry concentration of discharging from desilting mouth 13 when slurry when not bery high, adds appropriate flocculant by the flocculant adding tube 14 at desilting mouth straight tube 15, increases slurry sinking speed, can greatly increase like this desilting productive rate of cyclone 1, has reduced energy consumption; The ore pulp of low concentration is the outer row of comb 21 from low-concentration pulp regularly; After a large amount of slurry sedimentations, by screw unloading mechanism 22, discharge board concentrating box 2.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (2)
1. a flocculation concentration cyclone, it comprises charging aperture (11), overfall (12) and desilting mouth (13), it is characterized in that: also comprise board concentrating box (2), one end of described board concentrating box (2) is provided with described desilting mouth (13), the other end of described board concentrating box (2) is provided with screw unloading mechanism (22), and described board concentrating box (2) is provided with comb outside low-concentration pulp (21) between described desilting mouth (13) and described screw unloading mechanism (22); The outside of described desilting mouth (13) is provided with desilting mouth straight tube (15), and described desilting mouth straight tube (15) stretches into the inside of described board concentrating box (2).
2. a kind of flocculation concentration cyclone according to claim 1, it is characterized in that: also comprise flocculant adding tube (14), it is upper that described flocculant adding tube (14) is arranged on described desilting mouth straight tube (15), and described flocculant adding tube (14) is stretched out outside the casing of described board concentrating box (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320797765.3U CN203565212U (en) | 2013-12-04 | 2013-12-04 | Flocculation concentration whirlcone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320797765.3U CN203565212U (en) | 2013-12-04 | 2013-12-04 | Flocculation concentration whirlcone |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203565212U true CN203565212U (en) | 2014-04-30 |
Family
ID=50532976
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320797765.3U Expired - Fee Related CN203565212U (en) | 2013-12-04 | 2013-12-04 | Flocculation concentration whirlcone |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203565212U (en) |
-
2013
- 2013-12-04 CN CN201320797765.3U patent/CN203565212U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202876534U (en) | Tailing dry emission system | |
| CN204275574U (en) | A kind of anti-sewage precipitation device turning over mud | |
| CN203565212U (en) | Flocculation concentration whirlcone | |
| CN104225969A (en) | Method and device for concentrating molybdenum ore flotation tailing ore pulp | |
| CN205361690U (en) | Hydraulic classification desliming cylinder for bauxite | |
| CN103611637A (en) | Flocculation concentration hydrocyclone | |
| CN204121814U (en) | A kind of enrichment facility of molybdenum ore flotation tailing pulp | |
| CN203741185U (en) | Sewage treatment device for environmental protection | |
| CN204134756U (en) | A kind of novel deliming equipment | |
| CN206262174U (en) | A kind of atlapulgite slurry multifeed clarifier | |
| CN204182497U (en) | A kind of dense media concentrate cyclone | |
| CN204543666U (en) | Containing solid-liquid feeding buffer device | |
| CN204958419U (en) | Continuous densification jar of calcium carbonate | |
| CN203370391U (en) | Wastewater recycling device | |
| CN202892998U (en) | Inclined plate sedimentation tank with coagulation region | |
| CN201962159U (en) | Novel coal water comprehensive treatment device | |
| CN207025554U (en) | A kind of tailings glass system | |
| CN206262702U (en) | Process water solid-liquid separating equipment in a kind of wet-method sulfur forming device | |
| CN103230684A (en) | Double-feed-pipe flat-bottom settling tank | |
| CN205127486U (en) | Sludge discharging device | |
| CN204973951U (en) | Take centrifuging tube of cusp bottom | |
| CN204247405U (en) | With the thick overflow pipe of anti-race of sieve aperture | |
| CN203874916U (en) | Novel sand-discharging type hydraulic cyclone desander capable of automatically controlling interval | |
| CN103394214A (en) | Ore pulp thickening method in iron ore separation process | |
| CN206404384U (en) | A kind of concentrator with overflow collection groove |
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: 20140430 Termination date: 20161204 |