CN203494231U - Concentration tank - Google Patents
Concentration tank Download PDFInfo
- Publication number
- CN203494231U CN203494231U CN201320546855.5U CN201320546855U CN203494231U CN 203494231 U CN203494231 U CN 203494231U CN 201320546855 U CN201320546855 U CN 201320546855U CN 203494231 U CN203494231 U CN 203494231U
- Authority
- CN
- China
- Prior art keywords
- pool body
- tank body
- nozzle
- flocculation
- foam
- 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
- 239000006260 foam Substances 0.000 claims abstract description 19
- 238000005189 flocculation Methods 0.000 claims abstract description 15
- 230000016615 flocculation Effects 0.000 claims abstract description 15
- 239000010865 sewage Substances 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 238000005507 spraying Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000002245 particle Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 238000005457 optimization Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000003311 flocculating Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000006011 modification reaction Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
Abstract
The utility model discloses a concentration tank. The concentration tank comprises an upper tank body and a lower tank body, wherein an overflow port is arranged on the edge of the upper tank body; both the upper tank body and the lower tank body are conical; the taper of the upper tank body is greater than that of the lower tank body; a flocculation bridge frame is arranged on the top of the upper tank body and provided with a nozzle and a submerged pump which is connected with the nozzle; a foam check ring is arranged below the flocculation bridge frame; the nozzle is arranged inside the foam check ring; and a drain outlet is arranged at the bottom of the lower tank body and connected with a siphon pipe. The concentration tank overcomes the shortage of the prior art; by virtue of the upper and lower conical tank body differing in taper, the concentration rate is enhanced without increasing the depth of the tank body; foam can be eliminated by spraying water downward through the nozzle; and sewage is discharged from the drain outlet at the bottom of the tank based on a siphon principle, so that energy is saved.
Description
Technical field
The utility model relates to a kind of mill water treatment facility, especially a kind of concentration basin.
Background technology
In ore-dressing technique, concentration basin is that the sewage that is mixed with suspended particulate is carried out to flocculating setting, obtains the equipment of recycled recirculated water.At present, the enrichment factor of domestic concentration basin is only 60%～70%, and concentrated effect is not good enough.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of concentration basin, can solve the deficiencies in the prior art, by designing the different two terminal circle conical tank body of upper and lower tapering, do not increasing under the prerequisite of the pond body degree of depth, improved enrichment factor, by nozzle, spray current downwards, play the effect of eliminating foam.Sewage draining exit at the bottom of pond utilizes siphon principle blowdown, saves the energy.
For solving the problems of the technologies described above, technical solution adopted in the utility model is as follows.
A concentration basin, comprises upper pool body and lower pool body, at the edge of upper pool body, is provided with overfall, and described upper pool body and lower pool body are taper shape, and the tapering of described upper pool body is greater than the tapering of described lower pool body; At the top of described upper pool body, be provided with flocculation crane span structure, flocculation crane span structure is provided with nozzle and the immersible pump being connected with nozzle, below flocculation crane span structure, is provided with foam back-up ring, and nozzle is in the inside of foam back-up ring; Bottom at lower pool body is provided with sewage draining exit, and sewage draining exit is connected with siphon pipe.
As preferably, the tapering of described upper pool body is 4.5, and the tapering of described lower pool body is 2.5.
As preferably, on described siphon pipe, be provided with switch valve.
As preferably, described upper pool body and lower pool body inner side are equipped with watertight composition.
The beneficial effect that adopts technique scheme to bring is: upper pool body and lower pool body adopt the design of different taperings, can under the prerequisite that does not increase the concentration basin degree of depth, improve the dischargeable capacity of concentration basin, have increased hydraulic detention time, have improved enrichment factor.In addition, this design is applicable to concentrated mechanical maximization more.It is inner that foam back-up ring can be limited in foam back-up ring the foam producing, and by immersible pump, constantly extracted water and sprayed by nozzle, effectively reduced the foam in concentration basin.Sewage draining exit adopts siphon principle, saves the energy.The switch valve arranging on siphon pipe can be controlled siphonal break-make.The watertight composition of upper pool body and lower pool body inner side can effectively stop seepage, extends the service life of concentration basin.Through above-mentioned optimization, thickening efficiency can be increased to 88.2%.
accompanying drawing explanation
Fig. 1 is the schematic diagram of a specific embodiment of the utility model.
In figure: 1, upper pool body; 2, lower pool body; 3, overfall; 4, flocculation crane span structure; 5, nozzle; 6, immersible pump; 7, foam back-up ring; 8, sewage draining exit; 9, siphon pipe; 10, switch valve; 11, watertight composition.
The specific embodiment
With reference to Fig. 1, the utility model comprises upper pool body 1 and lower pool body 2, at the edge of upper pool body 1, is provided with overfall 3, and described upper pool body 1 and lower pool body 2 are taper shape, and the tapering of described upper pool body 1 is greater than the tapering of described lower pool body 2; At the top of described upper pool body 1, be provided with flocculation crane span structure 4, flocculation crane span structure 4 is provided with nozzle 5 and the immersible pump 6 being connected with nozzle 5, below flocculation crane span structure 4, is provided with foam back-up ring 7, and nozzle 5 is in the inside of foam back-up ring 7; In the bottom of lower pool body 2, be provided with sewage draining exit 8, sewage draining exit 8 is connected with siphon pipe 9.
Tapering that it should be noted that described upper pool body 1 is 4.5, and the tapering of described lower pool body 2 is 2.5.
It should be noted that: on described siphon pipe 9, be provided with switch valve 10.
In addition, described upper pool body 1 and lower pool body 2 inner sides are equipped with watertight composition 11.
Operation principle of the present utility model is: silt particle suspension is after cyclone classification, and the thin mud suspension of granularity-0.045mm enters in concentration basin.Meanwhile, according to set regime of agent, add flocculant, make the particle generation Flocculation Settling Process in suspension.In Flocculation Settling Process, thin mud particle forms large floc sedimentation under the effect of flocculation bridge formation 4, at the bottom of sinking to pond, forms concentrated underflow, by sewage draining exit 8, discharges; The few water of solid content is discharged by overfall 3, becomes recirculated water.Reached the object of mud-water separation.
The design of upper pool body 1 and the different taperings of lower pool body 2 employing can improve the dischargeable capacity of concentration basin under the prerequisite that does not increase the concentration basin degree of depth, has increased hydraulic detention time, has improved enrichment factor.In addition, this design is applicable to concentrated mechanical maximization more.Foam back-up ring 7 can be limited in foam back-up ring 7 inside the foam producing, and by immersible pump 6, is constantly extracted water and is sprayed by nozzle 5, has effectively reduced the foam in concentration basin.Sewage draining exit 8 adopts siphon principle, saves the energy.The switch valve 10 arranging on siphon pipe 9 can be controlled the break-make of siphon pipe 9.The watertight composition 11 of upper pool body 1 and lower pool body 2 inner sides can effectively stop seepage, extends the service life of concentration basin.Through above-mentioned optimization, thickening efficiency can be increased to 88.2%.
More than show and described basic principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; that in above-described embodiment and description, describes just illustrates principle of the present utility model; do not departing under the prerequisite of the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (4)
1. a concentration basin, comprise upper pool body (1) and lower pool body (2), at the edge of upper pool body (1), be provided with overfall (3), it is characterized in that: described upper pool body (1) and lower pool body (2) are taper shape, and the tapering of described upper pool body (1) is greater than the tapering of described lower pool body (2); At the top of described upper pool body (1), be provided with flocculation crane span structure (4), flocculation crane span structure (4) is provided with nozzle (5) and the immersible pump (6) being connected with nozzle (5), below at flocculation crane span structure (4) is provided with foam back-up ring (7), and nozzle (5) is in the inside of foam back-up ring (7); In the bottom of lower pool body (2), be provided with sewage draining exit (8), sewage draining exit (8) is connected with siphon pipe (9).
2. concentration basin according to claim 1, is characterized in that: the tapering of described upper pool body (1) is 4.5, and the tapering of described lower pool body (2) is 2.5.
3. concentration basin according to claim 1, is characterized in that: on described siphon pipe (9), be provided with switch valve (10).
4. concentration basin according to claim 1, is characterized in that: described upper pool body (1) and lower pool body (2) inner side are equipped with watertight composition (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320546855.5U CN203494231U (en) | 2013-09-04 | 2013-09-04 | Concentration tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320546855.5U CN203494231U (en) | 2013-09-04 | 2013-09-04 | Concentration tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203494231U true CN203494231U (en) | 2014-03-26 |
Family
ID=50325239
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320546855.5U Expired - Fee Related CN203494231U (en) | 2013-09-04 | 2013-09-04 | Concentration tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203494231U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104474747A (en) * | 2014-11-04 | 2015-04-01 | 攀枝花钢城集团瑞矿工业有限公司 | Micro-fine particle grade titanium ore recovery apparatus |
-
2013
- 2013-09-04 CN CN201320546855.5U patent/CN203494231U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104474747A (en) * | 2014-11-04 | 2015-04-01 | 攀枝花钢城集团瑞矿工业有限公司 | Micro-fine particle grade titanium ore recovery apparatus |
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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: 20140326 Termination date: 20150904 |
|
| EXPY | Termination of patent right or utility model |