CN200967047Y - Fluidization gravity separating machine - Google Patents
Fluidization gravity separating machine Download PDFInfo
- Publication number
- CN200967047Y CN200967047Y CN 200620093244 CN200620093244U CN200967047Y CN 200967047 Y CN200967047 Y CN 200967047Y CN 200620093244 CN200620093244 CN 200620093244 CN 200620093244 U CN200620093244 U CN 200620093244U CN 200967047 Y CN200967047 Y CN 200967047Y
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- CN
- China
- Prior art keywords
- vallecular cavity
- fluidized
- ventilative cloth
- reseparator
- discharging opening
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Abstract
A fluidization gravity-flow concentrator is provided, which relates to an improvement of material separation equipment. The utility model provides a fluidization gravity-flow concentrator of wide application and large separation volume, which comprises a concentrator body, and is characterized in that: a slanting breathable cloth is positioned between an upper cavity and a lower cavity on the frame; wherein, the upper cavity top is provided with a feeding inlet and a venthole respectively; a bracket inside the lower cavity under the breathable cloth is provided with an electromagnet; the lower cavity is connected with an air tube of a fan; a discharge hole of the concentrator body is positioned at the lower end of the slanting breathable cloth.
Description
Technical field:
The utility model relates to the improvement of material screening installation.
Background technology:
In the industrial processes, need often utilize screening installation to separate, extract some valuable article by character, the proportion of material, for example, the separating etc. of the coal ash of ferrosilicon powder and iron content.Often use at present as the seperator of ferrous material and be used for different specific weight or the separator of variable grain.
The seperator of ferrous material is exactly the adhesive effect by magnet, the iron powder in the material is pull-in on around the magnet, and then scrapes the iron powder material with screeding device.But there is following shortcoming:
1, can not on-line operation: this confidential asking can not have wind regime etc., needs the external force feed way to enter, and therefore, this machine is not suitable for having on the equipment on the wind regime production line and uses;
2, inferior separating effect: material is short through this machine time, and it is less that magnet is inhaled the iron amount, so separating effect is also bad;
3, treating capacity is little: magnet is inhaled the iron material after a certain amount of, needs regularly scraper, i.e. this machine interruption work; Therefore, treating capacity is less.
Be used to contain the separator of different specific weight or variable grain, main equipment is cyclone dust collectors, by regulating wind speed, the different material of proportion difference or particle is discharged respectively, reaches the purpose of sorting.But there is following shortcoming:
1, use is limited: this machine is subjected to the restriction of wind regime, and the material that particle is big is difficult for entering cyclone dust collectors, can not carry out sorting, and therefore, the scope of application is very restricted;
2, handle the fine dust material and must add setting: sorting fine dust material also must add gas-solid separator, promptly gas is separated with solid, finally just can receive the fine dust material;
3, separating effect is poor: because the cyclone dust removal inefficiency, therefore, the separating effect of cyclone dust removal is also low.
The utility model content:
The utility model is exactly at the problems referred to above, provides a kind of applied widely, the fluidized reseparator that the sorting amount is big.
The utility model adopts following technical scheme: the utility model comprises body, is provided with the ventilative cloth of inclination between the last vallecular cavity of its structural feature body, the following vallecular cavity; The top of last vallecular cavity is respectively arranged with charging aperture, passage, and the support in the following vallecular cavity of ventilative cloth below is provided with electromagnet; Following vallecular cavity links to each other with the blast pipe of blower fan respectively, and the discharging opening of body is arranged on the low side of ventilative cloth.
The beneficial effects of the utility model:
1, applied widely:
Gravity concentrator of the present utility model can be used for the feed separation of the iron thing separation of ferrous material and different specific weight, variable grain; Structure of the present utility model can connect deduster, wind-force conveying etc. and have in the air supply system, and therefore, the scope of application is very wide, can be widely used in industries such as ore dressing, chemical industry, power plant, coal, metallurgy;
2, sorting amount is big:
Structure of the present utility model makes material flow along the surface of ventilative cloth, and the magnetic line of force that electromagnet produces passes material, absorbs the iron in the material; Because continuous operation is uninterrupted, therefore, sorting material that can be a large amount of;
3: simple in structure:
Gravity concentrator of the present utility model, its member is few, and simple in structure, is easy to popularize;
4, environmental protection:
The utility model is to make material carry out sorting at last vallecular cavity, and good airproof performance has been avoided the pollution to environment.
Description of drawings:
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is the left view of Fig. 1.
The specific embodiment:
The utility model comprises body 19, is provided with the ventilative cloth 9 of inclination between the last vallecular cavity 11 of body 19, the following vallecular cavity 13; The top of last vallecular cavity 11 is respectively arranged with charging aperture 16, passage 4, and the support 12 in the following vallecular cavity 13 of ventilative cloth 9 belows is provided with electromagnet 8; Following vallecular cavity 13 links to each other with the blast pipe 17 of blower fan 20 respectively, and the discharging opening 1 of body 19 is arranged on the low side of ventilative cloth 9.
Passage 4 can be arranged on the hood 7 on the body 19, and the body 19 of hood 7 belows is provided with ventilative cloth 6.
Discharging opening 1 is two, i.e. one-level discharging opening 5, secondary discharge port 3; The material that proportion is bigger, particle is bigger is then discharged from one-level discharging opening 5; Proportion is smaller, and particle is smaller then discharges from secondary discharge port 3.
Also can be provided with hopper 15, batcher 14 by charging aperture 16; Batcher 14 can be outsourcing, and its model is YJDXBI-16.Discharging opening 1 is provided with discharging machine 2, and its model is YJDXBZ-8.
For accelerating the speed of charging, discharging, the circuit in all right distribution box 18 of the utility model is implemented automation control, improves operating efficiency of the present utility model.
Below in conjunction with a description of drawings course of action of the present utility model:
At first, material is fallen in the vallecular cavity 11, is piled up on the ventilative cloth 9 by charging aperture 16; Blower fan 20 blows ventilative cloth 9 by blast pipe 17, following vallecular cavity 13 and shakes up and down, and the material of piling up on the ventilative cloth 9 is breathed freely the 9 proal whiles of cloth along inclination, and the iron material in the material is attracted on ventilative cloth 9 surfaces; The material that proportion is big, particle is bigger is discharged along one-level discharging opening 5; Proportion is less, and the less material of particle is then discharged from secondary discharge port 3.
Claims (6)
1, fluidized reseparator comprises body (19), it is characterized in that being provided with between the last vallecular cavity (11) of body (19), the following vallecular cavity (13) the ventilative cloth (9) of inclination; The top of last vallecular cavity (11) is provided with capable charging aperture (16), passage (4) respectively, and the support (12) in the following vallecular cavity (13) of ventilative cloth (9) below is provided with electromagnet (8); The blast pipe (17) of the same respectively blower fan of following vallecular cavity (13) (20) links to each other, and the discharging opening (1) of body (19) is arranged on the low side of ventilative cloth (9).
2, fluidized reseparator according to claim 1 is characterized in that passage (4) is arranged on the hood (7) on the body (19), and the body (19) of hood (7) below is provided with ventilative cloth (6).
3, fluidized reseparator according to claim 1 is characterized in that discharging opening (1) is two, i.e. one-level discharging opening (5), secondary discharge port (3).
4, fluidized reseparator according to claim 1 is characterized in that blast pipe (17) is set to two, respectively at eminence, lower corresponding to the ventilative cloth (9) that tilts.
5, fluidized reseparator according to claim 1 is characterized in that charging aperture (16) is provided with hopper (15), batcher (14).
6,, it is characterized in that discharging opening (1) is provided with discharging machine (2) according to claim 1 or 3 described fluidized reseparators.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620093244 CN200967047Y (en) | 2006-09-14 | 2006-09-14 | Fluidization gravity separating machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200620093244 CN200967047Y (en) | 2006-09-14 | 2006-09-14 | Fluidization gravity separating machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200967047Y true CN200967047Y (en) | 2007-10-31 |
Family
ID=38966618
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200620093244 Expired - Fee Related CN200967047Y (en) | 2006-09-14 | 2006-09-14 | Fluidization gravity separating machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200967047Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102553823A (en) * | 2011-12-30 | 2012-07-11 | 广州捷士多铝合金有限公司 | Sorting device for solid materials with different specific weights |
| CN107321496A (en) * | 2017-07-25 | 2017-11-07 | 安徽正丰再生资源有限公司 | A kind of gravity type silicon carbide micro-powder purifying plant |
-
2006
- 2006-09-14 CN CN 200620093244 patent/CN200967047Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102553823A (en) * | 2011-12-30 | 2012-07-11 | 广州捷士多铝合金有限公司 | Sorting device for solid materials with different specific weights |
| CN102553823B (en) * | 2011-12-30 | 2014-01-01 | 广州捷士多铝合金有限公司 | Sorting device for solid materials with different specific weights |
| CN107321496A (en) * | 2017-07-25 | 2017-11-07 | 安徽正丰再生资源有限公司 | A kind of gravity type silicon carbide micro-powder purifying plant |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |