CN205518165U - Thick concentrate washup selectivity separator of bauxite beneficiation - Google Patents
Thick concentrate washup selectivity separator of bauxite beneficiation Download PDFInfo
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- CN205518165U CN205518165U CN201620292774.0U CN201620292774U CN205518165U CN 205518165 U CN205518165 U CN 205518165U CN 201620292774 U CN201620292774 U CN 201620292774U CN 205518165 U CN205518165 U CN 205518165U
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- separation chamber
- particulate
- gape
- level sensor
- driving motor
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- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model discloses a thick concentrate washup selectivity separator of bauxite beneficiation, including the separation chamber, separation chamber upper end open -ended center department is equipped with driving motor, driving motor is fixed on the inner wall of separation chamber by the support, and driving motor's below is equipped with the agitator, separation chamber upper end opening part still is equipped with the inlet pipe, be equipped with a plurality of particulate ore discharge mouths on the lateral wall of separation chamber, particulate ore discharge mouth and particulate ore discharge union coupling, still be equipped with a level sensor and the 2nd level sensor on the lateral wall of separation chamber, the lower extreme of separation chamber is equipped with coarse grain ore discharge mouth, and coarse grain ore discharge mouth and coarse grain ore discharge union coupling. The utility model discloses in, quick effectually separate low -grade mineral of separation coarse grain and thin granule high -grade mineral, in addition, liquid level information through ground paste in the real -time monitoring separation chamber of level sensor that sets up to the electromagnetic valves who sets up on the cooperation feed inlet to carry out automatic control to installing the feeding, has improved the degree of automation of device.
Description
Technical field
This utility model relates to benficiation machinery field, particularly relates to a kind of ore concentration of bauxite rough concentrate
Washup Selective Separation device.
Background technology
Bauxite actually refers to industrial can utilize, with gibbsite, boehmite or
The general designation of the Ore that diaspore is formed by essential mineral.The self-built grind grading in ore dressing plant enters
Row transformation the most mostly uses second cyclone classification, second cyclone underflow conduct later
Rough concentrate becomes final concentrate product with flotation concentrate after mixing again after being directly entered dashpot, and two
Level cyclone underflow alumina silica ratio is 4.0-4.5, but due to rough concentrate grade mineral products on the low side, coarse-fine
Rate is high, causes final concentrate product alumina silica ratio on the low side, does not reaches the demand of the quality of production, at this
In the case of Zhong, two grades of classification flow processs are forced to disable or be interrupted use.
Although ore dressing rough concentrate washup Selective Separation device of the prior art can be low by coarse grain
Grade mineral and fine grained high-grade mineral separate, but in the operating process of reality, due to
Ore often blocks the conveyance conduit of slip, and has to interrupt separation process, goes to expend greatly
The time of amount removes dredging pipeline；Additionally, the charging rate of segregation apparatus and discharging speed balance are
The maximal efficiency separated can be reached, but conventional separating apparatus charging and discharging cannot be accomplished automatically
Controlling, need to expend substantial amounts of manpower and materials and go supervision, the production significantly increasing enterprise becomes
This.
To this end, it is proposed that a kind of ore concentration of bauxite rough concentrate washup Selective Separation device solves
Certainly the problems referred to above.
Utility model content
The purpose of this utility model is to solve shortcoming present in prior art, and proposes
A kind of ore concentration of bauxite rough concentrate washup Selective Separation device.
To achieve these goals, this utility model adopts the technical scheme that
A kind of ore concentration of bauxite rough concentrate washup Selective Separation device, including separation chamber, described
Separation chamber is formed by connecting by cylindrical section and conical section, the center of described separation chamber upper end open
Place is provided with driving motor, and described driving motor is fixed on the inwall of separation chamber by support, and drives
The lower section of galvanic electricity machine is provided with agitator, and described agitator is positioned in separation chamber, and agitator with drive
The output shaft of galvanic electricity machine connects, and is additionally provided with feed pipe at described separation chamber upper end open, described point
Sidewall from room is provided with multiple particulate gape being symmetrical set, described particulate gape with
Particulate ore discharge pipe connects, and described particulate gape is provided with filtration with the junction of particulate ore discharge pipe
Net, the sidewall of described separation chamber is additionally provided with the first liquid level sensor and the second liquid level sensor,
Described first liquid level sensor is positioned at the lower section of particulate gape, described second liquid level sensor position
In the top of particulate gape, the lower end of described separation chamber is provided with coarse grain gape, and coarse grain row
Mine mouth is connected with coarse grain ore discharge pipe, described driving motor, the first liquid level sensor and the second liquid level
Sensor is all electrically connected with the controller.
Preferably, described driving motor is connected with agitator by decelerator.
Preferably, at described feed pipe, it is provided with electromagnetic valve, and electromagnetic valve is electrically connected with controller
Connect.
Preferably, the bore of described particulate gape is 50-150mm.
In this utility model, by the driving motor arranged, utilize and drive driven by motor agitator
Rotate so that the slip in separation chamber is in good dispersity, utilizes the coarse grain in slip
Low-grade mineral are different and then the most right with the sedimentation velocity of fine grained high-grade mineral
Separating coarse-grained low-grade mineral and fine grained high-grade mineral separate；Additionally, by arranging
The real-time detection separation chamber of liquid level sensor in the liquid level information of slip, and coordinate on charging aperture
The electromagnetic valve arranged, automatically controls device charging, improves the automatization of device
Degree, reduces the production cost of enterprise.
Accompanying drawing explanation
Fig. 1 is that a kind of ore concentration of bauxite rough concentrate washup selectivity that the utility model proposes divides
Structural representation from device.
In figure: 1 separation chamber, 2 drive motors, 3 supports, 4 agitators, 5 feed pipes, 6
Coarse grain ore discharge pipe, 7 particulate ore discharge pipes, 8 drainage screens, 9 first liquid level sensors, 10 second
Liquid level sensor.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, in this utility model embodiment
Technical scheme be clearly and completely described, it is clear that described embodiment be only this
The a part of embodiment of utility model rather than whole embodiments.Based in this utility model
Embodiment, those of ordinary skill in the art are obtained under not making creative work premise
Every other embodiment, broadly falls into the scope of this utility model protection.
With reference to Fig. 1, a kind of ore concentration of bauxite rough concentrate washup Selective Separation device, including dividing
From room 1, separation chamber 1 is formed by connecting by cylindrical section and conical section, and separation chamber 1 opens upper end
The center of mouth is provided with driving motor 2, drives motor 2 to be fixed on separation chamber 1 by support 3
On inwall, and driving the lower section of motor 2 to be provided with agitator 4, agitator 4 is positioned at separation chamber 1
In, agitator 4 is connected to by decelerator drive on the output shaft of motor 2, can be by controlling
Control the mixing speed of agitator, at separation chamber 1 upper end open, be additionally provided with feed pipe 5, charging
It is provided with electromagnetic valve at pipe 5, and electromagnetic valve is electrically connected with the controller, the sidewall of separation chamber 1
Being provided with multiple particulate gape being symmetrical set, the bore of particulate gape is
50-150mm, and particulate gape is connected with particulate ore discharge pipe 7, particulate gape is arranged with particulate
The junction of pipe 7 is provided with drainage screen 8, and drainage screen 8 is used for preventing ore particles from blocking particulate
Gape, the sidewall of separation chamber 1 is additionally provided with the first liquid level sensor 9 and the second level sensing
Device 10, the liquid level information of slurry, the first liquid level sensor 9 in detecting separation chamber 1
In the lower section of particulate gape, the second liquid level sensor 10 is positioned at the top of particulate gape,
The lower end of separation chamber 1 is provided with coarse grain gape, and coarse grain gape is connected with coarse grain ore discharge pipe 6,
Drive motor the 2, first liquid level sensor 9 and the second liquid level sensor 10 all electric with controller
Connect.
In this utility model, by setting centrally-mounted driving 2 at the top of separation chamber 1, utilization is driven
Galvanic electricity machine 2 drives agitator 4 to rotate so that the slip in separation chamber 1 does centrifugal motion, and
Slip is made to be in good dispersity in separation chamber 1；Meanwhile, the low-grade mineral of coarse grain
Heavy speed is very fast, discharges by coarse grain ore discharge pipe 6 through coarse grain gape after sedimentation, returns grinding machine and regrinds；
Fine grained high-grade mineral are relatively slow due to heavy speed, discharge by particulate ore discharge pipe 7 through particulate gape
As rough concentrate, as final product concentrate after mixing with flotation concentrate.
The above, only this utility model preferably detailed description of the invention, but this utility model
Protection domain be not limited thereto, any those familiar with the art is in this practicality
In the technical scope of novel exposure, according to the technical solution of the utility model and utility model structure thereof
Think equivalent or change in addition, all should contain within protection domain of the present utility model.
Claims (4)
1. an ore concentration of bauxite rough concentrate washup Selective Separation device, including separation chamber (1),
Described separation chamber (1) is formed by connecting by cylindrical section and conical section, it is characterised in that institute
The center stating separation chamber (1) upper end open is provided with driving motor (2), described driving motor
(2) it is fixed on the inwall of separation chamber (1) by support (3), and drives motor (2)
Lower section is provided with agitator (4), and described agitator (4) is positioned in separation chamber (1), and stirs
Mixing device (4) to be connected with the output shaft driving motor (2), described separation chamber (1) upper end is opened
Be additionally provided with feed pipe (5) at Kou, the sidewall of described separation chamber (1) be provided with multiple symmetrically
The particulate gape arranged, described particulate gape is connected with particulate ore discharge pipe (7), described
Particulate gape is provided with drainage screen (8), described separation with the junction of particulate ore discharge pipe (7)
The first liquid level sensor (9) and the second liquid level sensor (10) it is additionally provided with on the sidewall of room (1),
Described first liquid level sensor (9) is positioned at the lower section of particulate gape, and described second liquid level passes
Sensor (10) is positioned at the top of particulate gape, and the lower end of described separation chamber (1) is provided with slightly
Grain gape, and coarse grain gape is connected with coarse grain ore discharge pipe (6), described driving motor (2),
First liquid level sensor (9) and the second liquid level sensor (10) are all electrically connected with the controller.
A kind of ore concentration of bauxite rough concentrate washup selectivity the most according to claim 1 divides
From device, it is characterised in that described driving motor (2) is by decelerator and agitator (4)
Connect.
A kind of ore concentration of bauxite rough concentrate washup selectivity the most according to claim 1 divides
From device, it is characterised in that described feed pipe (5) place is provided with electromagnetic valve, and electromagnetic valve
Door is electrically connected with the controller.
A kind of ore concentration of bauxite rough concentrate washup selectivity the most according to claim 1 divides
From device, it is characterised in that the bore of described particulate gape is 50-150mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620292774.0U CN205518165U (en) | 2016-03-30 | 2016-03-30 | Thick concentrate washup selectivity separator of bauxite beneficiation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620292774.0U CN205518165U (en) | 2016-03-30 | 2016-03-30 | Thick concentrate washup selectivity separator of bauxite beneficiation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205518165U true CN205518165U (en) | 2016-08-31 |
Family
ID=56790135
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620292774.0U Expired - Fee Related CN205518165U (en) | 2016-03-30 | 2016-03-30 | Thick concentrate washup selectivity separator of bauxite beneficiation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205518165U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108262150A (en) * | 2018-01-03 | 2018-07-10 | 茂名市茂南嘉泥科技发展有限公司 | A kind of grogs particle size separating apparatus |
| CN112827663A (en) * | 2020-12-31 | 2021-05-25 | 新巴尔虎右旗荣达矿业有限责任公司 | Flotation cell liquid level regulating device |
-
2016
- 2016-03-30 CN CN201620292774.0U patent/CN205518165U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108262150A (en) * | 2018-01-03 | 2018-07-10 | 茂名市茂南嘉泥科技发展有限公司 | A kind of grogs particle size separating apparatus |
| CN112827663A (en) * | 2020-12-31 | 2021-05-25 | 新巴尔虎右旗荣达矿业有限责任公司 | Flotation cell liquid level regulating device |
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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: 20160831 Termination date: 20180330 |