CN205461870U - Antigravity ore pulp agitator - Google Patents
Antigravity ore pulp agitator Download PDFInfo
- Publication number
- CN205461870U CN205461870U CN201521142177.1U CN201521142177U CN205461870U CN 205461870 U CN205461870 U CN 205461870U CN 201521142177 U CN201521142177 U CN 201521142177U CN 205461870 U CN205461870 U CN 205461870U
- Authority
- CN
- China
- Prior art keywords
- staving
- wall
- ore pulp
- helical feeder
- antigravity
- 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
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
Abstract
The utility model belongs to the mine equipment field relates to an ore pulp agitator, concretely relates to antigravity ore pulp agitator, including the staving, outer wall of the barrel body is provided with the support, and its characterized in that staving is inside to be provided with the ascending spiral feeder of opening, and it has feed hopper to lead to between spiral feeder lower extreme lateral part and the outer wall of the barrel body, and feed hopper and spiral feeder's junction upper portion has seted up the recycle feed mouth, is provided with the discharge opening bottom the staving. The utility model discloses the beneficial effect who has is: simple structure, work efficiency is high, has overcome the influence that material gravity brought, also can overcome some beneficiation reagent because self nature characteristic is difficult to the influence of dispersion in the ore pulp, and it is more even to make the material mix, has avoided the lamination.
Description
Technical field
This utility model belongs to mining equiment field, relates to a kind of flowsheet of slurry agitation bucket, is specifically related to a kind of bob-weight
Power flowsheet of slurry agitation bucket.
Background technology
In ore dressing especially in flotation, need before sorting to size mixing, generally make with the agitating device in agitator
Pulp flow, reaches material dispersion and the purpose of mixing.Due to the interfacial property of different minerals granule in Ore
Difference, occurs out-phase to assemble between granule agglomerating;Some beneficiation reagent added when sizing mixing is special due to self property
Point, it is not easy to disperse in ore pulp.
Tradition flowsheet of slurry agitation bucket is to be mixed by material under stirrer paddle drives.Material is different because of proportion, by oar
Leaf inclination can move between producing up and down mixing, but blade installation site is in middle and lower part, and blade stirs
Power is little to the staving bottom upper and lower active force of material, so heavy material will sink under the influence of gravity
Bottom staving, it is impossible to mix homogeneously.
Utility model content
According to above the deficiencies in the prior art, technical problem to be solved in the utility model is: provide one
Antigravity flowsheet of slurry agitation bucket, it is possible to material is sufficiently mixed.
A kind of antigravity flowsheet of slurry agitation bucket described in the utility model, including staving, bucket outer wall is provided with and props up
Frame, it is characterised in that staving is internally provided with the helical feeder of opening upwards, helical feeder lower end sidepiece
And lead to have cast hopper between bucket outer wall, and the top, junction of cast hopper and helical feeder offers and follows
Ring charging aperture, is provided with discharge port bottom staving.
Wherein, preferred version is as follows:
Bucket outer wall is provided with and the liquidometer that leads in staving, it is possible to the level condition in accurate observation staving.
Inner wall of barrel, the outer wall of helical feeder and inwall are coated with coat of silicon carbide, due to hardness of mineral
Height, easily causes abrasion to staving, is coated with coat of silicon carbide and can strengthen its wearability.
Work process of the present utility model is as follows: material is entered in helical feeder by cast hopper, arranges spiral shell
Screwing on the vertical speed of service of glassware and be not less than acceleration of gravity 9.8 meter per second, such material is in helical feeder
By upwards and the power of side-to-side movement, and it is in weightlessness, when running to helical feeder top end opening,
Material is in again free falling body state and falls in staving, enters helical feeder through recycle feed mouth the most again defeated
Send the circulation that goes round and begins again, finally flow out from discharge port.In the process, material whole process approximation weightlessness,
So overcoming gravity, lamination would not be produced because of material proportion difference, through certain time material just
Can be sufficiently mixed.
The had the beneficial effect that simple in construction of this utility model, work efficiency is high, overcomes material weight
The impact that power is brought, it is also possible to overcome some beneficiation reagent to be not easy in ore pulp due to self property feature
Scattered impact, makes material mixing more uniform, it is to avoid lamination.
Accompanying drawing explanation
Fig. 1 is operation principle schematic diagram of the present utility model;
In figure, 1, staving 2, cast hopper 3, helical feeder 4, discharge port 5, liquid level
Meter 6, support 7, recycle feed mouth.
Detailed description of the invention
Below in conjunction with drawings and Examples, this utility model is described further.
Embodiment 1:
As it is shown in figure 1, a kind of antigravity flowsheet of slurry agitation bucket, including staving 1, staving 1 outer wall is provided with support
6, staving 1 is internally provided with the helical feeder 3 of opening upwards, helical feeder 3 lower end sidepiece and staving
Lead to have cast hopper 2 between 1 outer wall, and the top, junction of cast hopper 2 and helical feeder 3 offers and follows
Ring charging aperture 7, is provided with discharge port 4 bottom staving 1.
Staving 1 outer wall is provided with and the liquidometer 5 that leads in staving 1, it is possible to the liquid in accurate observation staving 1
Position situation.
Staving 1 inwall, the outer wall of helical feeder 3 and inwall are coated with coat of silicon carbide, due to mineral
Hardness is high, easily staving 1 is caused abrasion, is coated with coat of silicon carbide and can strengthen its wearability.
Work process is as follows: material is entered in helical feeder 3 by cast hopper 2, arranges helical feeder 3
The vertical speed of service is not less than acceleration of gravity 9.8 meter per second, such material in helical feeder 3 by
Go up and the power of side-to-side movement, and be in weightlessness, when running to helical feeder 3 top end opening, thing
Material is in again free falling body state and falls in staving 1, enters helical feeder through recycle feed mouth 7 the most again
3 carry the circulation that goes round and begins again, and finally flow out from discharge port 4.In the process, material whole process approximation weightlessness
State, so overcoming gravity, would not produce lamination because of material proportion difference, through certain time
Material just can be sufficiently mixed.
Claims (1)
1. an antigravity flowsheet of slurry agitation bucket, including staving, bucket outer wall is provided with support, it is characterized in that staving is internally provided with the helical feeder of opening upwards, lead to there is cast hopper between helical feeder lower end sidepiece and bucket outer wall, and the top, junction of cast hopper and helical feeder offers recycle feed mouth, bottom staving, it is provided with discharge port;Bucket outer wall is provided with and the liquidometer that leads in staving;Inner wall of barrel is coated with coat of silicon carbide, and outer wall and the inwall of helical feeder are coated with coat of silicon carbide.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521142177.1U CN205461870U (en) | 2015-12-26 | 2015-12-26 | Antigravity ore pulp agitator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521142177.1U CN205461870U (en) | 2015-12-26 | 2015-12-26 | Antigravity ore pulp agitator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN205461870U true CN205461870U (en) | 2016-08-17 |
Family
ID=56663611
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201521142177.1U Expired - Fee Related CN205461870U (en) | 2015-12-26 | 2015-12-26 | Antigravity ore pulp agitator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN205461870U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114367212A (en) * | 2022-01-07 | 2022-04-19 | 湖南达诺智能机器人科技有限公司 | Particulate matter mixing device and method |
CN115814731A (en) * | 2022-12-07 | 2023-03-21 | 西北大学 | Micro-nano material sphericizing continuous shaping device and method |
-
2015
- 2015-12-26 CN CN201521142177.1U patent/CN205461870U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114367212A (en) * | 2022-01-07 | 2022-04-19 | 湖南达诺智能机器人科技有限公司 | Particulate matter mixing device and method |
CN115814731A (en) * | 2022-12-07 | 2023-03-21 | 西北大学 | Micro-nano material sphericizing continuous shaping device and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201862462U (en) | Vertical screw-stirring ore-grinding and floating integrated device | |
CN207521171U (en) | Jet stream micro-bubble flotation machine | |
CN108348927A (en) | System, method and apparatus for froth flotation | |
CN208894409U (en) | A kind of flotation device with air blower | |
CN106944264B (en) | Turbulence-regulated external particle fluidized bed mineralization flotation equipment with uniform turbulence | |
CN103831044A (en) | Rapid shunt mixing barrel | |
CN201921559U (en) | Steady flow type deep cone thickener | |
CN205461870U (en) | Antigravity ore pulp agitator | |
CN105080375B (en) | A kind of nitre sulfenyl depot fertilizer production emulsifier | |
CN207327294U (en) | A kind of tailing filling cementitious slurry agitating device of metal mine | |
CN107029895A (en) | Particulate coal stage flotation machine | |
CN105904589B (en) | A kind of agitating device and its stirring system | |
CN105537007B (en) | A kind of mineral floating system | |
CN113198619B (en) | Coarse particle flotation equipment and method adopting rotational flow and damping coupled fluidization | |
CN102660675A (en) | Cyanide leaching device for gold ore | |
CN212468476U (en) | Stable material feeder that divides of spiral chute | |
CN112691792B (en) | Quality-improving dissociation device and method for coarse-grained minerals | |
CN206526945U (en) | A kind of lead-zinc ore floating machine | |
CN210631720U (en) | Deep-cone dense sand silo with fluidized sand discharging device | |
CN205668325U (en) | A kind of agitating device and stirring system thereof | |
CN106079070B (en) | A kind of stirring system | |
CN204019732U (en) | A kind of colliery double-layer cement pulper | |
CN202527264U (en) | Conical hydraulic classifier | |
CN208583483U (en) | Flotation device | |
CN204566392U (en) | A kind of anti-airborne dust tailing cemented filling mixer |
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 |
Granted publication date: 20160817 Termination date: 20161226 |
|
CF01 | Termination of patent right due to non-payment of annual fee |