CN203235547U - Flotation feed preprocessing device - Google Patents
Flotation feed preprocessing device Download PDFInfo
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- CN203235547U CN203235547U CN 201320260707 CN201320260707U CN203235547U CN 203235547 U CN203235547 U CN 203235547U CN 201320260707 CN201320260707 CN 201320260707 CN 201320260707 U CN201320260707 U CN 201320260707U CN 203235547 U CN203235547 U CN 203235547U
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- flotation
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- mixing chamber
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Abstract
The utility model belongs to the technical field of flotation equipment and discloses a flotation feed preprocessing device which is used for preprocessing feed ore pulp before the feed ore pulp enters a flotation machine. According to the technical scheme, a feeding pipe is installed on one side of a feeding chamber of the flotation feed preprocessing device, a mixing chamber is connected below the feeding chamber, and a discharging chamber is connected below the mixing chamber; a closed push plate is arranged at the connection position of the feeding chamber and the mixing chamber, a plurality of nozzles are installed on the push plate, the inlets of the nozzles are located in the feeding chamber, and jet spouts of the nozzles are located in the mixing chamber; an atomizer is installed on the side wall of the mixing chamber, and a discharging port is formed in the lower portion of the discharging chamber. The flotation feed preprocessing device achieves the flotation feed preprocessing process integrating pre-mineralization before flotation, flotation reagent atomizing, flotation feeding and air even-mixing of flotation feed with the granularity smaller than 0.50mm in a wet process coal preparation plant, achieves the purposes of improving flotation feed separation selectivity, reducing flotation cleans ash, promoting cleans yield and reducing flotation reagent consumption, and has the advantages of being simple in structure, small in occupied area and good in flotation effect.
Description
Technical field
The utility model relates to a kind of pan feeding ore pulp and carry out pretreated device before entering flotation device, belongs to the floatation equipment technical field.
Background technology
The coal preparation plant of China all is wet coal preparation more than 95%, and flotation device is wet coal preparation factory sorting granularity＜the most ripe effective screening installation of 0.5mm coal slime technology.Coal slime needs the pan feeding ore pulp is carried out preliminary treatment before entering flotation device, namely before coal slime enters flotation device, with ore pulp, medicament, the abundant disperse of air and mixing, reaches and reduces optionally purpose of floating agent consumption, raising sorting.Therefore the preliminary treatment of floatation feed is an important step of coal slime flotation.Up to now, domestic floatation feed pre-processing device has kaskad apparatus for pre-flotation pulp conditioning, ore pulp preprocessor, agitator, falls case etc.These existing equipment or function singlenesses, or complex structure, cost of manufacture are high, otherwise floor space large, increase civil engineering cost, can not be applicable to the various newly-built or coal preparation plants that transform fully.
The utility model content
Technical problem to be solved in the utility model provides a kind of floatation feed pretreatment unit, and this device medicament that can atomize ore pulp, medicament, air are fully mixed, and floor space is little.
The technical scheme that solves the problems of the technologies described above is:
A kind of floatation feed pre-processor unit, it is comprised of pan feeding chamber, mixing chamber, discharge chamber, nozzle, vertebral plate, atomizer, one side of pan feeding chamber is installed feeding pipe, and mixing chamber is connected to the below of pan feeding chamber, and discharge chamber is connected to the below of mixing chamber, the junction of pan feeding chamber and mixing chamber is the push pedal of sealing, a plurality of nozzles are installed in the push pedal, and the import of nozzle is indoor at pan feeding, and the spout of nozzle is in mixing chamber, atomizer is installed on the sidewall of mixing chamber, and discharging opening is arranged at the bottom of discharge chamber.
Above-mentioned floatation feed pre-processor unit, described push pedal are sphere, have a plurality of equally distributed circular holes at the push pedal sphere, and a plurality of nozzles are installed in respectively in the circular hole, and each nozzle tilts to the central axis of mixing chamber respectively.
Above-mentioned floatation feed pre-processor unit, described nozzle are conical nozzle, and the spout of nozzle is along the axis direction of nozzle, and the extended line of the axis of a plurality of nozzles intersects on the mixing chamber central axis.
The beneficial effects of the utility model are:
Floatation feed forms high-pressure spray through nozzle, and in mixing chamber, form negative pressure, air and floating agent enter mixing chamber through atomizer under suction function, through jet high-speed cutting, pulverizing, become bubble, floating agent to be atomized into trickle elaioleucite air dispersion, floatation feed, air, vaporific floating agent enter in mixing chamber and the discharge chamber and fully mix and diffusion, finish the preliminary treatment of ore pulp, enter the flotation device cell body by discharging opening again.The utility model has realized that the pre-mineralising of the front collection of wet coal preparation factory granularity＜0.50mm floatation feed flotation, floating agent atomizing and floatation feed, air evenly are mixed in the floatation feed preprocessing process of one, reach and improve the purpose that the floatation feed sorting is selective, reduce floatation clean coal ash content, raising clean coal yield, reduction floating agent consumption, has advantage simple in structure, that floor space is little, floating agent is atomized on one is effective, cost of manufacture is low, the coal preparation plant's adapted that is applicable to the newly-built of various scales and transforms.
Description of drawings
Fig. 1 is the utility model overall structure schematic diagram;
Fig. 2 is the top view of Fig. 1.
Number in the figure is as follows: pan feeding chamber 1, feeding pipe 2, nozzle 3, mixing chamber 4, vertebral plate 5, atomizer 6, discharge chamber 7, discharging opening 8.
The specific embodiment
The utility model is comprised of pan feeding chamber 1, mixing chamber 4, discharge chamber 7, nozzle 3, vertebral plate 5, atomizer 6.
Show among the figure that a side of pan feeding chamber 1 is installed feeding pipe 2, mixing chamber 4 is connected to the below of pan feeding chamber 1, and discharge chamber 7 is connected to the below of mixing chamber 4, and discharging opening 8 is arranged at the bottom of discharge chamber 7, and discharging opening 8 is communicated with flotation head groove.
Show among the figure, pan feeding chamber 1 is the push pedal 5 of sealing with the junction of mixing chamber 4, push pedal 5 is sphere, have a plurality of equally distributed circular holes at push pedal 5 spheres, a plurality of nozzles 3 are installed in respectively in the circular hole, the import of nozzle 3 is in pan feeding chamber 1, and the spout of nozzle 3 is in mixing chamber 4, and nozzle 3 is connected pan feeding chamber 1 and mixing chamber 4 cavity space.
Show among the figure that each nozzle 3 tilts to the central axis of mixing chamber 4 respectively, nozzle 3 is conical nozzle, and the spout of nozzle 3 is along the axis direction of nozzle 3, and the extended line of the axis of a plurality of nozzles 3 intersects on mixing chamber 4 central axis.
Show among the figure that atomizer 6 is installed on the sidewall of mixing chamber 4,
The course of work of the present utility model is as follows:
Floatation feed enters pan feeding chamber 1 with 0.06-0.2MPa pressure through feeding pipe 2, forms high-pressure spray through pan feeding nozzle 3; Be negative pressure this moment in the mixing chamber 4, and air and floating agent are by in the atomizer 6 moments suction mixing chamber 4, and floating agent is the trickle elaioleucite of the shape that atomizes under suction function, air then by the jet high-speed cutting, be ground into minute bubbles; Floatation feed, vaporific floating agent, air are finished the preliminary treatment of ore pulp in mixing chamber 4 and discharge chamber 7 interior abundant mixing and diffusions, enter the flotation device cell body by discharging opening 8 again.
Claims (3)
1. floatation feed pre-processor unit, it is characterized in that: it is by pan feeding chamber (1), mixing chamber (4), discharge chamber (7), nozzle (3), vertebral plate (5), atomizer (6) forms, one side of pan feeding chamber (1) is installed feeding pipe (2), mixing chamber (4) is connected to the below of pan feeding chamber (1), discharge chamber (7) is connected to the below of mixing chamber (4), pan feeding chamber (1) is the push pedal (5) of sealing with the junction of mixing chamber (4), a plurality of nozzles (3) are installed in the push pedal (5), the import of nozzle (3) is in pan feeding chamber (1), the spout of nozzle (3) is in mixing chamber (4), atomizer (6) is installed on the sidewall of mixing chamber (4), and discharging opening (8) is arranged at the bottom of discharge chamber (7).
2. floatation feed pre-processor unit according to claim 1, it is characterized in that: described push pedal (5) is sphere, have a plurality of equally distributed circular holes at push pedal (5) sphere, a plurality of nozzles (3) are installed in respectively in the circular hole, and each nozzle (3) tilts to the central axis of mixing chamber (4) respectively.
3. floatation feed pre-processor unit according to claim 2, it is characterized in that: described nozzle (3) is conical nozzle, the spout of nozzle (3) is along the axis direction of nozzle (3), and the extended line of the axis of a plurality of nozzles (3) intersects on mixing chamber (4) central axis.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320260707 CN203235547U (en) | 2013-05-15 | 2013-05-15 | Flotation feed preprocessing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320260707 CN203235547U (en) | 2013-05-15 | 2013-05-15 | Flotation feed preprocessing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203235547U true CN203235547U (en) | 2013-10-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320260707 Expired - Fee Related CN203235547U (en) | 2013-05-15 | 2013-05-15 | Flotation feed preprocessing device |
Country Status (1)
| Country | Link |
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| CN (1) | CN203235547U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104624356A (en) * | 2015-01-09 | 2015-05-20 | 天地（唐山）矿业科技有限公司 | Solution microbubble strong surface modification machine |
| CN105642450A (en) * | 2016-02-25 | 2016-06-08 | 江西稀有稀土金属钨业集团有限公司 | Method for increasing flotation molybdenite recovery rate |
| CN106391327A (en) * | 2016-10-25 | 2017-02-15 | 武汉工程大学 | Ore pulp flowing film type agent atomizing feeder |
| CN108246516A (en) * | 2018-03-28 | 2018-07-06 | 中国矿业大学 | A kind of intensified Daqu medicament and the system and method for mineral grain mixing |
-
2013
- 2013-05-15 CN CN 201320260707 patent/CN203235547U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104624356A (en) * | 2015-01-09 | 2015-05-20 | 天地（唐山）矿业科技有限公司 | Solution microbubble strong surface modification machine |
| CN104624356B (en) * | 2015-01-09 | 2017-02-22 | 天地（唐山）矿业科技有限公司 | Solution microbubble strong surface modification machine |
| CN105642450A (en) * | 2016-02-25 | 2016-06-08 | 江西稀有稀土金属钨业集团有限公司 | Method for increasing flotation molybdenite recovery rate |
| CN106391327A (en) * | 2016-10-25 | 2017-02-15 | 武汉工程大学 | Ore pulp flowing film type agent atomizing feeder |
| CN106391327B (en) * | 2016-10-25 | 2019-10-18 | 武汉工程大学 | Flow of slurry membrane type is atomized doser |
| CN108246516A (en) * | 2018-03-28 | 2018-07-06 | 中国矿业大学 | A kind of intensified Daqu medicament and the system and method for mineral grain mixing |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 063012 Hebei province Tangshan City Xinhua West Road No. 21 Patentee after: TANGSHAN RESEARCH INSTITUTE OF CHINA COAL TECHNOLOGY & ENGINEERING GROUP Address before: 063012 Hebei province Tangshan City Xinhua West Road No. 21 Patentee before: Tangshan Branch of China Coal Research Institute |
|
| 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: 20131016 Termination date: 20180515 |