CN203018213U - Three-section type flotation mineralizing equipment set - Google Patents
Three-section type flotation mineralizing equipment set Download PDFInfo
- Publication number
- CN203018213U CN203018213U CN 201320022954 CN201320022954U CN203018213U CN 203018213 U CN203018213 U CN 203018213U CN 201320022954 CN201320022954 CN 201320022954 CN 201320022954 U CN201320022954 U CN 201320022954U CN 203018213 U CN203018213 U CN 203018213U
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- China
- Prior art keywords
- mineralizing
- bubble mixer
- bubble
- mineralising
- turbulent chamber
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Abstract
The utility model discloses a three-section type flotation mineralizing equipment set which is characterized by consisting of a material inlet connection pipe (1), a bubble mixer (2), an upper turbulent flow cavity (3), a flow control nozzle (4), a lower turbulent flow cavity (5), a mineralizing pipe (6) and a release head (7), wherein one end of the bubble mixer (2) is connected with the material inlet connection pipe (1), and the other end of the bubble mixer (2) is connected with the upper turbulent flow cavity (3); the flow control nozzle (4) is arranged between the upper turbulent flow cavity (3) and the lower turbulent flow cavity (5); and the lower turbulent flow cavity (5), the mineralizing pipe (6) and the release head (7) are sequentially connected with one another. The three-section type flotation mineralizing equipment set can be widely applied to a quick flotatation slot and a flotataion column and has the advantages of high mineralizing efficiency and long service life.
Description
Technical field
Syllogic floatation mineralizing device group is applicable to the Mineral Processing Industry of metallic ore and nonmetallic mineral, is used for the inflation mineralization process of floatation process ore pulp.The inflation mineralising of especially applicable fast-flotation groove and flotation column ore pulp.
Background technology
in ore dressing process, the ore pulp process pH value adjustment that grinds mixes with floating agent, contain adjusting agent in floating agent, collecting agent and foaming agent, collecting agent is comprised of the organic matter that contains hydrophilic radical and hydrophobic grouping, the hydrophobic grouping of collecting agent can combine with foaming agent, in the direct flotation process, the hydrophilic radical of collecting agent with electric charge and the particle of valuable mineral combine by electrostatic attraction, when having gas to be filled with, foaming agent just can form bubble, bubble just can be with the particle floating of valuable mineral, thereby realize the FLOTATION SEPARATION of mineral.
Syllogic floatation mineralizing device group be fast-flotation groove and flotation column ore pulp inflation mineralising must fitting mechanism.Flotation pulp mixes with compressed air in mineralizer, mixed inflation mineralising ore pulp is with certain pressure, these mineralising ore pulps with certain pressure are released in flotation cell by the earth pressure release head again, and bubble carries the ore particle of valuable mineral and realizes separating in flotation cell with hydrophilic gangue particle.Thereby in the mineralization process of ore pulp the mixability of ore pulp and bubble and the wear control of ore pulp overcurrent part, be the key of mineralization device successful Application.Flotation column and gas tube mineralising fast-flotation groove have been widely used in the floatation process of mineral, as of paramount importance inflation mineralising mechanism, there is the mineralizer of a lot of forms to be applied, mainly contain heterogeneous turbulent flow type inflation mineralizer, two bushing type aperture inflation mineralizer, two bushing type micropore inflation mineralizer etc., but most air consumptions are large, bubble diameter is inhomogeneous, disperses badly, and the ore dressing effect is formed very large impact; The earth pressure release head also has the application of various ways, mainly contains cone type release head and porous spiral-flow type release head.Syllogic floatation mineralizing device group adopts the bundled tube bubble mixer, and bubble is little and Uniform Dispersion is good, and adopts the mode of flow control shower nozzle and release head two-stage earth pressure release, effectively reduces overcurrent wearing and tearing partly.
The content of utility model
The purpose of invention
The utility model is for the flotation efficiency that improves quick mineralising pipe mineralising flotation cell and flotation column and reduces the wearing and tearing partly of ore pulp overcurrent and invent.Application of the present utility model has extended the service life of mineralising assembly greatly, has widened the application of quick mineralising pipe mineralising flotation cell and flotation column.
Technical scheme
The utility model syllogic floatation mineralizing device group is comprised of charging tube connector, bubble mixer, upper turbulent chamber, flow control nozzle, lower turbulent chamber, mineralising pipe, release head; One end of bubble mixer is connected with the charging tube connector, the other end of bubble mixer is connected with upper turbulent chamber; Between upper turbulent chamber and lower turbulent chamber, the flow control nozzle is installed; Lower turbulent chamber, mineralising pipe, release head are connected successively; Bubble mixer is the bundled tube bubble mixer, and compressed air inlet is installed on bubble mixer; Release head is equipped with a plurality of nozzles.
During application, the flotation pulp after medicament is combined enters bubble mixer from the charging tube connector, and compressed air passes into bubble mixer by compressed air inlet, and bubble and ore pulp are inflated mineralising in bubble mixer; After mineralising, ore pulp enters turbulent chamber, then enters lower turbulent chamber with the pressure that reduces the mineralising ore pulp and the energy that absorbs the mineralising ore pulp by the flow control nozzle ejection, enters flotation cell through post-decompression mineralising ore pulp through mineralising pipe, release head, nozzle ejection.
Beneficial effect
1, syllogic floatation mineralizing device group adopts the micropore inflation, and bubble is little, and good dispersion, the favourable ore pulp flash that Rapid Flow is crossed in microtubule are combined and even, forms inflation mineralising ore pulp, is conducive to reduce air consumption, improves the ore dressing effect.
2, syllogic floatation mineralizing device group adopts the mode of flow control nozzle and release head two-stage earth pressure release, effectively reduces the wearing and tearing of overcurrent part, has extended the service life of mineralising assembly.
Description of drawings
Accompanying drawing 1 is the generalized section of the utility model syllogic floatation mineralizing device group;
The utility model syllogic floatation mineralizing device group is comprised of charging tube connector 1, bubble mixer 2, upper turbulent chamber 3, flow control nozzle 4, lower turbulent chamber 5, mineralising pipe 6, release head 7; One end of bubble mixer 2 is connected with charging tube connector 1, the other end of bubble mixer 2 is connected with upper turbulent chamber 3; Between upper turbulent chamber 3 and lower turbulent chamber 5, flow control nozzle 4 is installed; Lower turbulent chamber 5, mineralising pipe 6, release head 7 are connected successively; Bubble mixer 1 is the bundled tube bubble mixer; Compressed air inlet 9 is installed on bubble mixer 1; Release head 7 is equipped with a plurality of nozzles 8.
Flotation pulp after medicament is combined enters bubble mixer 2 from charging tube connector 1, and compressed air passes into bubble mixer 2 by compressed air inlet 9, and bubble and ore pulp are inflated mineralising in bubble mixer 2; After mineralising, ore pulp enters turbulent chamber 3, then sprays by flow control nozzle 4 to enter lower turbulent chamber 5 with the pressure that reduces the mineralising ore pulp and the energy that absorbs the mineralising ore pulp, sprays and enters flotation cell through mineralising pipe 6, release head 7, nozzle 8 through post-decompression mineralising ore pulp.
Embodiment
The embodiment of syllogic floatation mineralizing device group the best is that syllogic floatation mineralizing device group is comprised of charging tube connector 1, bubble mixer 2, upper turbulent chamber 3, flow control nozzle 4, lower turbulent chamber 5, mineralising pipe 6, release head 7; One end of bubble mixer 2 is connected with charging tube connector 1, the other end of bubble mixer 2 is connected with upper turbulent chamber 3; Between upper turbulent chamber 3 and lower turbulent chamber 5, flow control nozzle 4 is installed; Lower turbulent chamber 5, mineralising pipe 6, release head 7 are connected successively; Bubble mixer 1 is the bundled tube bubble mixer; Compressed air inlet 9 is installed on bubble mixer 1; Release head 7 is equipped with a plurality of nozzles 8.
Claims (4)
1. syllogic floatation mineralizing device group, is characterized in that syllogic floatation mineralizing device group is comprised of charging tube connector (1), bubble mixer (2), upper turbulent chamber (3), flow control nozzle (4), lower turbulent chamber (5), mineralising pipe (6), release head (7); One end of bubble mixer (2) is connected with charging tube connector (1), the other end of bubble mixer (2) is connected with upper turbulent chamber (3); Between upper turbulent chamber (3) and lower turbulent chamber (5), flow control nozzle (4) is installed; Lower turbulent chamber (5), mineralising pipe (6), release head (7) are connected successively.
2. syllogic floatation mineralizing device group according to claim 1, it is characterized in that: bubble mixer (2) is the bundled tube bubble mixer.
3. syllogic floatation mineralizing device group according to claim 1, is characterized in that: compressed air inlet (9) is installed on bubble mixer (2).
4. syllogic floatation mineralizing device group according to claim 1, it is characterized in that: release head (7) is equipped with a plurality of nozzles (8).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320022954 CN203018213U (en) | 2013-01-10 | 2013-01-10 | Three-section type flotation mineralizing equipment set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320022954 CN203018213U (en) | 2013-01-10 | 2013-01-10 | Three-section type flotation mineralizing equipment set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203018213U true CN203018213U (en) | 2013-06-26 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320022954 Expired - Lifetime CN203018213U (en) | 2013-01-10 | 2013-01-10 | Three-section type flotation mineralizing equipment set |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203018213U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108273668A (en) * | 2018-03-28 | 2018-07-13 | 中国矿业大学 | A kind of fast-flotation system and method for floating mixing mineralising based on strong turbulence |
| CN109759242A (en) * | 2019-01-31 | 2019-05-17 | 中国矿业大学 | A kind of high ash fine slime screening installation and method |
-
2013
- 2013-01-10 CN CN 201320022954 patent/CN203018213U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108273668A (en) * | 2018-03-28 | 2018-07-13 | 中国矿业大学 | A kind of fast-flotation system and method for floating mixing mineralising based on strong turbulence |
| CN108273668B (en) * | 2018-03-28 | 2024-03-01 | 中国矿业大学 | Rapid flotation system and flotation method based on high-turbulence mixed mineralization |
| CN109759242A (en) * | 2019-01-31 | 2019-05-17 | 中国矿业大学 | A kind of high ash fine slime screening installation and method |
| CN109759242B (en) * | 2019-01-31 | 2019-11-29 | 中国矿业大学 | A kind of high ash fine slime screening installation and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130626 |