CN204841063U - Hierarchical concentrated machine of tailing pulp material - Google Patents
Hierarchical concentrated machine of tailing pulp material Download PDFInfo
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- CN204841063U CN204841063U CN201520568278.9U CN201520568278U CN204841063U CN 204841063 U CN204841063 U CN 204841063U CN 201520568278 U CN201520568278 U CN 201520568278U CN 204841063 U CN204841063 U CN 204841063U
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- rotating shaft
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- material room
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Abstract
The utility model discloses a hierarchical concentrated machine of tailing pulp material, include the support frame, place hopper, material grading plant, agitating unit, back flow and overflow launder on the support frame in, separates to become hierarchical chamber and storage cavity through the baffle in the hopper, material grading plant arranges hierarchical intracavity in, and this material grading plant is including expecting room, second grade material room, drop pressure chamber and circulation dish elementarily, and second grade material room is arranged elementary material in and indoor and pass through screen cloth UNICOM with elementary material room, elementary material room top is arranged in to the drop pressure chamber, the circulation is coiled drop pressure outdoor wall and is set up, circulation dish inner bottom passes through the flocculating agent and adds pipe and hierarchical chamber UNICOM, agitating unit includes first pivot, second pivot and stuff pump, first pivot one end is connected with motor drive, the other end stretches into in the storage cavity, first pivot inner space is equipped with the opening of expecting room UNICOM with the second grade, second pivot suit and first pivot, this second pivot bottom is stretched into in the storage cavity, second pivot inner space is equipped with and expects elementarily the opening of room UNICOM.
Description
Technical field
The utility model relates to a kind of tailings disposal plant, particularly a kind of mine tailing slurry graded concentrator.
Background technology
Adopting concentrator to improve the concentration of mine tailing is method conventional at present, current thickener adopt by be suspended in concentration basin ore pulp by flocculant, solid particle is united after sedimentation under natural gravity effect, top then becomes primary water, and solid-liquid is separated.The sludge be deposited on bottom concentration basin is scraped central row mine mouth at the bottom of collection to pond continuously by rake scraper plate and is discharged, and primary water is then overflowed by edge on concentration basin.Because the solid particle be suspended in concentration basin in ore pulp relies on flocculant to unite, whether flocculant evenly mixes with slurry directly affects solid particle and unites, flocculant usage is large, concentration basin cannot continuous concentration material, cause solid-liquid separation effect poor, use cost is high, muddy along the water overflowed on concentration basin, uses inconvenience.
Utility model content
The technical problems to be solved in the utility model be to provide a kind of easy to use, good effect of separating solid from liquid, use cost are low, can the mine tailing slurry graded concentrator of continuous concentration material.
In order to solve the problems of the technologies described above, mine tailing slurry graded concentrator of the present utility model, comprise bracing frame, the hopper be placed on bracing frame, stock grading device, agitating device, return duct and overflow launder, become classification chamber and storage cavity by baffle for separating in described hopper, bottom described storage cavity, be provided with discharge valve; Described stock grading device is placed in described classification chamber, and this stock grading device comprises elementary material room, secondary material room, head pressure room and circulation dish, described elementary material room and material Ru Guan UNICOM; It is indoor and with elementary material room by screen cloth UNICOM that described secondary material room is placed in elementary material; Described head pressure room is placed in above elementary material room, this head pressure room with secondary Liao Shi UNICOM and outer wall contact with secondary material chamber interior walls and connect; Described circulation coiling head pressure chamber outer wall arrange and in circulation dish the end lower than the indoor liquid level of head pressure; In described circulation dish, the end, is by flocculant adding tube and classification chamber UNICOM; Described agitating device comprises the first rotating shaft, the second rotating shaft and stock pump; Described first rotating shaft, the second rotary shaft hollow, form cylindrical body; Described first rotating shaft one end is connected with motor-driven, the other end successively through head pressure room, secondary material room and elementary material room stretch in storage cavity; In described first rotating shaft, space is provided with the opening with secondary Liao Shi UNICOM, for by the material transferring of secondary material room in storage cavity; Described second shaft set and the first rotating shaft, this second rotating shaft bottom is stretched in storage cavity; In described second rotating shaft, space is provided with the opening with elementary Liao Shi UNICOM, for by the material transferring of elementary material room in storage cavity; UNICOM bottom the entrance of described stock pump and classification chamber, to export and discharge region UNICOM; Described return duct bottom and storage cavity UNICOM, top to be placed in above circulation dish and lower than top, differential pressure room; Described overflow launder be fixed on classification cavity wall top and overfall less than or equal to the height at the end in circulation dish.
Described return duct top is lower than head pressure room top 10-20cm.
Described return duct top is lower than head pressure room top 15cm.
Described agitating device also comprises impeller, and described impeller to be placed in bottom classification chamber, below elementary material room and to be connected with the second rotating shaft transmission, for stirring the concentrated material be deposited on bottom classification chamber.
Described agitating device also comprises harrow frame, and described harrow frame to be placed in below elementary material room, above impeller and to be connected with the second rotating shaft transmission, for breaing up the concentrated material be deposited on bottom classification chamber.
Described first rotating shaft and secondary material room are in transmission connection, and when rotating for the first rotating shaft, interlock secondary material room rotates.
Adopt structure of the present utility model, owing to comprising bracing frame, the hopper be placed on bracing frame, stock grading device, agitating device, return duct and overflow launder.During use, after material enters elementary material room, the deposition of solid that particle is larger is delivered to storage cavity in elementary material indoor by the second rotating shaft, and the less solid mixture of particle to enter secondary material through screen cloth indoor, be delivered in storage cavity by the first rotating shaft, preliminary classification carried out to material, the larger deposition of solid of particle is bottom storage cavity, the solid that particle is larger contacts few with flocculant, namely flocculant usage is little, and use cost is low.The completely rear mixed material liquid level of pulp-water mixture aggregation in storage cavity rises to head pressure room, when the indoor liquid level of head pressure is higher than return duct top, pulp-water mixture in storage cavity flows in circulation dish through return duct, flocculant adding tube again through circulation tray bottom enters in classification chamber, pulp-water mixture is united and is deposited on bottom classification chamber under the effect of flocculant, classification chamber is extracted out by stock pump, and the water separated is discharged through overflow launder, can continuous concentration material, easy to use, good effect of separating solid from liquid, use cost is low.
Again because agitating device also comprises impeller, described impeller to be placed in bottom classification chamber, below elementary material room and to be connected with the second rotating shaft transmission, for stirring the concentrated material be deposited on bottom classification chamber.Stirred the concentrated material be deposited on bottom classification chamber by impeller, to make, stock pump is easier to pump concentrated material, uses more convenient.
Because agitating device also comprises harrow frame, described harrow frame to be placed in below elementary material room, above impeller and to be connected with the second rotating shaft transmission, for breaing up the concentrated material be deposited on bottom classification chamber, after the concentrated material be deposited on bottom classification chamber is broken up by harrow frame, to make, stock pump is easier to pump concentrated material, uses more convenient.
Because the first rotating shaft and secondary material room are in transmission connection, when rotating for the first rotating shaft, interlock secondary material room rotates, and secondary material room rotates with the first rotating shaft, and secondary material locular wall upper screen cloth is not parked in spin rinse in pulp-water mixture, prevents screen cloth to block, uses more convenient.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the partial enlarged drawing of Fig. 1.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail:
As shown in Figure 1 and Figure 2, mine tailing slurry graded concentrator of the present utility model, comprises bracing frame 6, the hopper 7 be placed on bracing frame 6, stock grading device, agitating device, return duct 2 and overflow launder 9.Become classification chamber 8 and storage cavity 5 by baffle for separating in hopper 7, bottom storage cavity 5, be provided with discharge valve 3.Stock grading device is placed in described classification chamber 8, and this stock grading device comprises elementary material room 11, secondary material room 16, head pressure room 10 and circulation dish 1.Elementary material room 11 and material Ru Guan UNICOM.Secondary material room 16 to be placed in elementary material room 11 and with elementary material room 11 by screen cloth UNICOM.Head pressure room 10 is placed in above elementary material room 11, this head pressure room 10 with secondary Liao Shi 16 UNICOM and outer wall be tightly connected with secondary material room 16 inwall, elementary material room 11 contact internal walls respectively.Circulation dish 1 around head pressure room 10 outer wall arrange and in circulation dish 1 end lower than liquid level in head pressure room 10.In circulation dish 1, the end, is by flocculant adding tube 17 and classification chamber 8 UNICOM.Agitating device comprises the first rotating shaft 13, second rotating shaft 12 and stock pump 4.First rotating shaft 13, second rotating shaft 12 hollow, forms cylindrical body.First rotating shaft 13 one end is connected with motor-driven, the other end successively through head pressure room 10, secondary material room 16 and elementary material room 11 stretch in storage cavity 5.In first rotating shaft 13, space is provided with the opening with secondary Liao Shi 16 UNICOM, for by the material transferring of secondary material room 16 in storage cavity 5.Second rotating shaft 12 is set with and the first rotating shaft 13, and this second rotating shaft 12 bottom is stretched in storage cavity 5.In second rotating shaft 12, space is provided with the opening with elementary Liao Shi 11 UNICOM, for by the material transferring of elementary material room 11 in storage cavity 5.UNICOM bottom the entrance of stock pump 4 and classification chamber 8, to export and discharge region UNICOM.Return duct 2 bottom and storage cavity 5 UNICOM, top to be placed in above circulation dish 1 and lower than top, head pressure room 10.Overflow launder 9 be fixed on classification chamber 8 upper inside wall and overfall less than or equal to the height at the end in circulation dish 1.
The top of return duct 2 of the present utility model, preferably lower than top, head pressure room 10, is preferred value 10-20cm lower than top, head pressure room 10, preferably 15cm.
More convenient in order to use, agitating device also comprises impeller 14.Impeller 14 to be placed in bottom classification chamber 8, below elementary material room 11 and to be in transmission connection with the second rotating shaft 12, for stirring the concentrated material be deposited on bottom classification chamber 8.Stirred the concentrated material be deposited on bottom classification chamber by impeller, to make, stock pump is easier to pump concentrated material, uses more convenient.
More convenient in order to use, agitating device also comprises harrow frame 15.Harrow frame 15 to be placed in below elementary material room 11, above impeller 14 and to be in transmission connection with the second rotating shaft 12, for breaing up the concentrated material be deposited on bottom classification chamber 8.After the concentrated material be deposited on bottom classification chamber is broken up by harrow frame, to make, stock pump is easier to pump concentrated material, uses more convenient.
In order to prevent screen cloth from blocking, use more convenient, the first rotating shaft 13 is in transmission connection with secondary material room 16, and secondary material room 16 of linking when rotating for the first rotating shaft 13 rotates.Secondary material room rotates with the first rotating shaft, and secondary material locular wall upper screen cloth is not parked in spin rinse in pulp-water mixture, prevents screen cloth to block, uses more convenient.
Claims (6)
1. a mine tailing slurry graded concentrator, is characterized in that: comprise bracing frame (6), the hopper (7) be placed on bracing frame (6), stock grading device, agitating device, return duct (2) and overflow launder (9),
Become classification chamber (8) and storage cavity (5) by baffle for separating in described hopper (7), described storage cavity (5) bottom is provided with discharge valve (3);
Described stock grading device is placed in described classification chamber (8), and this stock grading device comprises elementary material room (11), secondary material room (16), head pressure room (10) and circulation dish (1), described elementary material room (11) and material Ru Guan UNICOM; Described secondary material room (16) to be placed in elementary material room (11) and with elementary material room (11) by screen cloth UNICOM; Described head pressure room (10) is placed in elementary material room (11) top, and this head pressure room (10) and secondary material room (16) UNICOM and outer wall are tightly connected with secondary material room (16) inwall, elementary material room (11) contact internal walls respectively; Described circulation dish (1) around head pressure room (10) outer wall arrange and in circulation dish (1) end lower than liquid level in head pressure room (10); Described circulation dish (1) the interior end, is by flocculant adding tube (17) and classification chamber (8) UNICOM;
Described agitating device comprises the first rotating shaft (13), the second rotating shaft (12) and stock pump (4); Described first rotating shaft (13), the second rotating shaft (12) hollow, form cylindrical body; Described first rotating shaft (13) one end is connected with motor-driven, the other end stretches in storage cavity (5) through head pressure room (10), secondary material room (16) and elementary material room (11) successively; The interior space of described first rotating shaft (13) is provided with the opening with secondary material room (16) UNICOM, for by the material transferring of secondary material room (16) in storage cavity (5); Described second rotating shaft (12) suit and the first rotating shaft (13), this second rotating shaft (12) bottom is stretched in storage cavity (5); The interior space of described second rotating shaft (12) is provided with the opening with elementary material room (11) UNICOM, for by the material transferring of elementary material room (11) in storage cavity (5); The entrance of described stock pump (4) and classification chamber (8) bottom UNICOM, export and discharge region UNICOM; Described return duct (2) bottom and storage cavity (5) UNICOM, top be placed in circulation dish (1) top and lower than head pressure room (10) top;
Described overflow launder (9) be fixed on classification chamber (8) upper inside wall and overfall less than or equal to the height at circulation dish (1) the interior end.
2. mine tailing slurry graded concentrator according to claim 1, is characterized in that: described return duct (2) top is lower than head pressure room (10) top 10-20cm.
3. mine tailing slurry graded concentrator according to claim 1, is characterized in that: described return duct (2) top is lower than head pressure room (10) top 15cm.
4. mine tailing slurry graded concentrator according to claim 1, it is characterized in that: described agitating device also comprises impeller (14), described impeller (14) be placed in classification chamber (8) bottom, elementary material room (11) below and be in transmission connection with the second rotating shaft (12), for stir be deposited on classification chamber (8) bottom concentrated material.
5. mine tailing slurry graded concentrator according to claim 4, it is characterized in that: described agitating device also comprises harrow frame (15), described harrow frame (15) be placed in elementary material room (11) below, impeller (14) top and be in transmission connection with the second rotating shaft (12), for break up be deposited on classification chamber (8) bottom concentrated material.
6. mine tailing slurry graded concentrator according to claim 1, is characterized in that: described first rotating shaft (13) and secondary material room (16) are in transmission connection, and secondary material room (16) of linking when rotating for the first rotating shaft (13) rotates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520568278.9U CN204841063U (en) | 2015-07-31 | 2015-07-31 | Hierarchical concentrated machine of tailing pulp material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520568278.9U CN204841063U (en) | 2015-07-31 | 2015-07-31 | Hierarchical concentrated machine of tailing pulp material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204841063U true CN204841063U (en) | 2015-12-09 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520568278.9U Expired - Fee Related CN204841063U (en) | 2015-07-31 | 2015-07-31 | Hierarchical concentrated machine of tailing pulp material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204841063U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237578A (en) * | 2019-06-20 | 2019-09-17 | 安徽中能矿机制造有限公司 | A kind of thickener handling high-concentration ore slurry |
-
2015
- 2015-07-31 CN CN201520568278.9U patent/CN204841063U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237578A (en) * | 2019-06-20 | 2019-09-17 | 安徽中能矿机制造有限公司 | A kind of thickener handling high-concentration ore slurry |
| CN110237578B (en) * | 2019-06-20 | 2021-10-15 | 安徽中能矿机制造有限公司 | Can handle concentrated machine of high concentration ore pulp |
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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: 20151209 Termination date: 20170731 |