CN206286065U - A kind of novel injection air-breathing agitated flotation cell - Google Patents
A kind of novel injection air-breathing agitated flotation cell Download PDFInfo
- Publication number
- CN206286065U CN206286065U CN201621385209.5U CN201621385209U CN206286065U CN 206286065 U CN206286065 U CN 206286065U CN 201621385209 U CN201621385209 U CN 201621385209U CN 206286065 U CN206286065 U CN 206286065U
- Authority
- CN
- China
- Prior art keywords
- deflector
- support
- ore pulp
- flotation
- flotation cell
- 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
Abstract
The utility model belongs to mineral separation technical field, specifically related to a kind of novel injection air-breathing agitated flotation cell, this flotation device replaces the agitator arm of agitation impeller flotator using deflector, the interior energy loss that the friction energy loss between impeller and axle and impeller stirring ore pulp bring is reduced, flotation energy loss is reduced.Stationary baffles carry out water conservancy diversion to submerged jets pan feeding in three times, with the volume seat to ore pulp in groove and stirring, ore pulp is sufficiently mixed in wider interval in groove with medicament, bubble.Stationary baffles are by the achievable control to ore pulp mixing circulation region of induction on flow of slurry direction simultaneously, so as to avoid ore pulp mixing circulation region from disturbing the traffic zone and froth bed of mineral laden bubble, form good flotation environment and deflector repeatedly cut by air pocket in ore pulp, impact grinding, form the bubble of smaller particle, and each interval in groove is sufficiently uniformly distributed in along deflector, realize abundant mineralising.
Description
Technical field
The utility model belongs to mineral separation technical field, and in particular to a kind of novel injection air-breathing agitated flotation cell.
Background technology
Conventional flotation device is broadly divided into mechanical flotation device and air jet flotation machine, for the air jet flotation machine commonly used
Because being not provided with agitating device, when pulp density is higher, it is impossible to provide enough power to realize ore pulp, bubble, floating agent
Be sufficiently mixed dispersion；And the energy consumption of the rotating speed high needs of the agitating device of agitation impeller flotator is higher, and rotating speed is low
The flow field that can not be formed and inspiratory capacity, and new injection air-breathing rabbling mechanism connects because the ore pulp of jet segment floods injection stream
Plume is bordering on, injection energy major part is consumed by ore pulp, therefore ejection efficiency subtracts greatly so that stirring efficiency subtracts greatly, and interference is stirred
Mix flow field.
Utility model content
The purpose of this utility model is to provide a kind of novel injection air-breathing agitated flotation cell.Stationary baffles control is set
Ore pulp race way, makes the ore pulp of various concentrations that the enough air-breathings of uniform offer can be sufficiently mixed under deflector guide functions
Amount, reducing energy consumption improves flotation efficiency.
To achieve the above object, the utility model employs following technical scheme：A kind of novel injection air-breathing stirs flotation
Machine includes air-breathing mixed organization, flotation cell, first support, ore pulp traffic zone；
The air-breathing mixed organization includes material feeding region, stirs mixed zone.
The material feeding region is located at first support upside, by blending bunker, circulates feeding mouth, and air intake duct is constituted；The blending bunker
Be arranged at first support upper end, for holding flotation circuit ore pulp, the circulation feeding mouth is arranged at blending bunker top, it is described enter
Expects pipe is arranged at the lower end of blending bunker, and is communicated with blending bunker；
The stirring mixed zone includes feeding pipe, air intake duct, annular space fluid jet nozzle, stationary baffles, second support, the 3rd
Support；The stationary baffles by the first deflector, the second deflector, circulation deflector composition, the air intake duct upper end with it is big
Gas phase is led to, and lower end is connected with annular space fluid jet nozzle, and the feeding pipe upper end communicates with blending bunker bottom, and lower end is sprayed with annular space jet
Head is connected, and is nested in air intake duct；The annular space fluid jet nozzle is set to multiple and is uniformly fixed in pan feeding pipe outer wall,
And be connected with feeding pipe；First deflector is presented " circular arc " shape, is set to four and mutually in 90 degree of uniform fixations
In pan feeding pipe outer wall；Second deflector is presented " circular arc " shape, is set to four and is in mutually 90 degree uniform by second support
It is fixed on false bottom, and the end of the second deflector is relative with the first deflector end, level height is higher than the first deflector；
The circulation deflector is presented " hemisphere " shape, is likewise provided as four and in 90 degree is uniformly fixed on false bottom by the 3rd support mutually
On, and it is relative with the second deflector end, stagger certain angle, and level height is higher than the second deflector；First water conservancy diversion
Plate, the second deflector, circulation deflector is highly below the height of first support.The circulation discharging opening is placed in flotation cell bottom
Portion, the side under vacation；Region between the circulation deflector outside and flotation cell inwall is the secondary enrichment region of concentrate.
Scraper plate, feeding mouth and discharging opening are respectively equipped with the flotation cell cell body；Is provided with the upside of the flotation cell
One support, the scraper plate is arranged in first support, positioned at the secondary enrichment region upside of concentrate.
A kind of novel injection air-breathing agitated flotation cell of the present utility model, its advantage shows：
1st, novel injection air-breathing agitated flotation cell described in the utility model replaces mechanical agitation type using stationary baffles
The agitator arm of flotation device, reduces the friction energy loss between impeller and axle, and the interior energy that impeller stirring ore pulp brings
Loss, reduces flotation energy loss.
2nd, the stationary baffles that the utility model is used carry out water conservancy diversion to submerged jets pan feeding in three times, with to ore deposit in groove
The volume seat of slurry and stirring, make ore pulp sufficiently be mixed in wider interval in groove with medicament, bubble, it is to avoid to occur floating
The dead angle area of choosing.
3rd, the stationary baffles that the utility model is used are capable of achieving to ore pulp mixing by the induction on flow of slurry direction
The control of race way, so as to avoid ore pulp mixing circulation region from disturbing the traffic zone and froth bed of mineral laden bubble, forms good
Good flotation environment.
4th, the stationary baffles of the utility model use repeatedly cut by air pocket in ore pulp, impact cutting
It is broken, the bubble of smaller particle is formed, and each interval in groove is sufficiently uniformly distributed in along deflector, realize abundant ore deposit
Change, beneficial to flotation.
Brief description of the drawings
Fig. 1 is structural representation front view of the present utility model.
Fig. 2 is structural representation top view of the present utility model.
Reference implication is as follows in figure：
The secondary enrichment region 4- first supports 5- ore pulps traffic zone 6- material feeding regions of 1- air-breathing mixed organization 2- flotation cell 3- concentrate
7- stirrings mixed zone 8- blending bunkers 9- circulation feeding mouth 10- feeding pipe 11- air intake duct 12- annular space fluid jet nozzles 13- static state water conservancy diversion
Support 16- the first deflector the second deflectors of the 17- 18- of plate 14- second supports 15- the 3rd circulation deflector 19- vacations bottom 20- circulations
Discharging opening 21- scraper plate 22- feeding mouth 23- discharging opening 24- flow of slurry trajectories
Specific embodiment
As illustrated, to achieve the above object, the utility model employs following technical scheme：
A kind of novel injection air-breathing agitated flotation cell include air-breathing mixed organization (1), flotation cell (2), first support (4),
Ore pulp traffic zone (5)；
The air-breathing mixed organization (1) includes material feeding region (6), stirs mixed zone (7).
The material feeding region (6), by blending bunker (8), circulates feeding mouth (9), air intake duct (10) positioned at first support (4) upside
Constitute；The blending bunker (8) is arranged at first support (4) upper end, for holding flotation circuit ore pulp, the circulation feeding mouth
(9) blending bunker (8) top is arranged at, the feeding pipe (10) is arranged at the lower end of blending bunker (8), and is communicated with blending bunker (8)；
The stirring mixed zone (7) includes feeding pipe (10), air intake duct (11), annular space fluid jet nozzle (12), static water conservancy diversion
Plate (13), second support (14), the 3rd support (15)；The stationary baffles (13) are by the first deflector (16), the second water conservancy diversion
Plate (17), circulation deflector (18) composition, air intake duct (11) upper end communicates with air, lower end and annular space fluid jet nozzle
(12), feeding pipe (10) upper end communicates with blending bunker (8) bottom, and lower end is connected with annular space fluid jet nozzle (12), and embedding
It is placed in air intake duct (11)；The annular space fluid jet nozzle (12) is set to multiple and is uniformly fixed on feeding pipe (10) outer wall,
And be connected with feeding pipe (10)；First deflector (16) is presented " circular arc " shape, is set to four and mutually in 90 degree
Uniformly it is fixed on feeding pipe (10) outer wall；Second deflector (17) is presented " circular arc " shape, is set to four and is in mutually
90 degree are uniformly fixed on false bottom (19) by second support (14), and the second deflector (17) end and the first deflector (16)
End is relative, and level height is higher than the first deflector (16)；Circulation deflector (18) is presented " hemisphere " shape, same to set
Uniformly be fixed on false bottom (19) by the 3rd support (15) for four and mutually in 90 degree, and with the second deflector (17) end phase
Right, stagger certain angle, and level height is higher than the second deflector (17)；First deflector (16), the second deflector
(17), circulation deflector (18) is highly below the height of first support (4).Circulation discharging opening (20) is placed in flotation cell bottom
Portion, the side under vacation；Region between circulation deflector (18) outside and flotation cell (2) inwall is the secondary enrichment of concentrate
Area (3).
Scraper plate (21), feeding mouth (22) and discharging opening (23) are respectively equipped with flotation cell (2) cell body；The flotation cell
(2) first support (4) is provided with the upside of, the scraper plate (21) is arranged in first support (9), positioned at the secondary enrichment region of concentrate
Upside (3).
The course of work of the present utility model is described further with reference to Fig. 1-2：
Ore pulp enters participation flotation in flotation cell (2) from ore pulp feeding mouth (22), and flotation cell (2) bottom cycle ore pulp is passed through
Underflow pump is pumped out from bottom cycle discharging opening (20), has pressure to be injected into blending bunker (8), and mixed ore pulp is penetrated through annular space
Stream shower nozzle (12) sprays, and sucks a large amount of gases through air intake duct (11) at annular space fluid jet nozzle (12) place, by annular space fluid jet nozzle
(12) ore pulp for spraying impacts the first deflector (16), and ore pulp is moved along the first deflector (16), from the first deflector (16)
One edge water conservancy diversion is to another edge.Flotation mineralized froth is discharged from the edge of the first deflector (16), then impacts second
Deflector (17), flotation mineralized froth is moved along the second deflector (17), from an edge water conservancy diversion of the second deflector (17) to
Another edge.Flotation mineralized froth discharges again then impact cycle deflector (18) from the outward flange of the second deflector (17),
Flotation mineralized froth is moved along circulation deflector (18), from an edge water conservancy diversion of circulation deflector (18) to another side
Edge, makes ore pulp be scattered in bottom land regional, while low side of the ore pulp again from circulation deflector (18) rises to along arc-shaped side
The upper end of deflector is circulated, ore pulp forms circulation loop after injection.Flotation mineralized froth from circulation deflector (18) outward flange
Throw away at backward ore pulp traffic zone (5) the top liquid level for floating up to flotation cell, fully accumulated on ore pulp traffic zone (5) top, and
Flotation cell (2) is scraped by scraper plate (21), and the mineralized froth not scraped is then deposited downwards to the secondary enrichment region of concentrate (3), two
The mineralized froth sunk in the secondary enrichment region of the concentrate (3) of side is then sunk down under second support (14) and the 3rd support (15)
End, and second support (14) and false bottom (19) to flotation area are crossed respectively, to realize flotation again；It is settled down to flotation cell (2) bottom
The ore pulp in portion then enters next flotation cell (2) through discharging opening (23) carries out flotation again.
Claims (3)
1. a kind of novel injection air-breathing agitated flotation cell it is characterized in that：Including air-breathing mixed organization, flotation cell, first support,
Ore pulp traffic zone；
The air-breathing mixed organization includes material feeding region and stirring mixed zone；
The material feeding region is located at first support upside, by blending bunker, circulates feeding mouth, and air intake duct is constituted；The blending bunker is set
In first support upper end, for holding flotation circuit ore pulp, the circulation feeding mouth is arranged at blending bunker top, the feeding pipe
The lower end of blending bunker is arranged at, and is communicated with blending bunker；The stirring mixed zone includes feeding pipe, air intake duct, the spray of annular space jet
Head, stationary baffles, second support, the 3rd support；
2. novel injection air-breathing agitated flotation cell according to claim 1, it is characterised in that：The stationary baffles are by first
Deflector, the second deflector, circulation deflector composition, the air intake duct upper end communicates with air, lower end and annular space fluid jet nozzle
Connection, the feeding pipe upper end communicates with blending bunker bottom, and lower end is connected with annular space fluid jet nozzle, and is nested in air intake duct
It is interior；The annular space fluid jet nozzle is uniformly fixed in pan feeding pipe outer wall, and is connected with feeding pipe；First deflector is presented
" circular arc " shape, is set to four and in 90 degree is uniformly fixed on pan feeding pipe outer wall mutually；Second deflector is presented " circle
Arc " shape, is set to four and is uniformly fixed on false bottom by second support in 90 degree mutually, and the end of the second deflector and the
One deflector end is relative, and level height is higher than the first deflector；The circulation deflector is presented " hemisphere " shape, same to set
Uniformly it is fixed on false bottom by the 3rd support for four and mutually in 90 degree, and, level height relative with the second deflector end
Higher than the second deflector；First deflector, the second deflector, circulation deflector is highly below the height of first support
Degree；The circulation discharging opening is placed in flotation trench bottom, the side under vacation；Circulation deflector outside and flotation cell inwall it
Between region be the secondary enrichment region of concentrate.
3. novel injection air-breathing agitated flotation cell according to claim 1, it is characterised in that：On the flotation cell cell body respectively
It is provided with scraper plate, feeding mouth and discharging opening；First support is provided with the upside of the flotation cell, the scraper plate is arranged on first support
On, positioned at the secondary enrichment region upside of concentrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621385209.5U CN206286065U (en) | 2016-12-16 | 2016-12-16 | A kind of novel injection air-breathing agitated flotation cell |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621385209.5U CN206286065U (en) | 2016-12-16 | 2016-12-16 | A kind of novel injection air-breathing agitated flotation cell |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206286065U true CN206286065U (en) | 2017-06-30 |
Family
ID=59103757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621385209.5U Expired - Fee Related CN206286065U (en) | 2016-12-16 | 2016-12-16 | A kind of novel injection air-breathing agitated flotation cell |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206286065U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106694237A (en) * | 2016-12-16 | 2017-05-24 | 安徽理工大学 | Novel injection suction stirring flotation machine |
-
2016
- 2016-12-16 CN CN201621385209.5U patent/CN206286065U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106694237A (en) * | 2016-12-16 | 2017-05-24 | 安徽理工大学 | Novel injection suction stirring flotation machine |
| CN106694237B (en) * | 2016-12-16 | 2022-06-28 | 安徽理工大学 | Jet air suction stirring flotation machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202715484U (en) | Self-injection rotary agitation type flotation machine with impeller | |
| CN205462756U (en) | Counterattack formula annular space sprays stirring formula flotation device of breathing in | |
| CN111570100B (en) | Jet atomization flotation equipment | |
| CN204841962U (en) | Connecting rod jet agitation flotation unit of breathing in | |
| CN209005951U (en) | It is a kind of to realize highly purified quartz sand flotation machine | |
| CN207822942U (en) | A kind of efficient ore pulp modifying machine | |
| CN205868554U (en) | Ration adds reverse stirring center of medicine integral type flotation equipment that sizes mixing | |
| CN103601285A (en) | Jet aerator | |
| CN111570099A (en) | Jet atomization device and flotation device with same | |
| CN105642451B (en) | A kind of reaction type annular space injection air-breathing agitation type flotation machine for carrying fairing | |
| CN211914195U (en) | Jet type short column flotation machine | |
| CN204564358U (en) | A kind of injection stream is impacted vane rotary and is stirred self-induced aeration floatation | |
| CN206286065U (en) | A kind of novel injection air-breathing agitated flotation cell | |
| CN104772231B (en) | A kind of pre- de slime flotation complete set of equipments | |
| CN102583720A (en) | Deep-water type down-umbrella aerator impeller | |
| CN106694237A (en) | Novel injection suction stirring flotation machine | |
| CN105562217A (en) | Mixed flow field flotation system based on jet flow drive | |
| CN203972155U (en) | The air-breathing agitation type flotation machine of a kind of injection | |
| CN111389599A (en) | Jet type short column flotation machine | |
| CN202741248U (en) | Jetting and stirring flotation machine | |
| CN206286064U (en) | A kind of novel injection air-breathing agitating device | |
| CN110614168B (en) | Stirring type flotation machine with jet impeller | |
| CN210815739U (en) | High-efficient flotation column | |
| CN105289389B (en) | Equipment of deeply slurry mixing and modifying for coal slime | |
| CN206051675U (en) | A kind of gas-liquid mixed solid stirring system under the conditions of anaerobic reaction |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170630 Termination date: 20171216 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |