CN2224031Y - Stirring-separating-separated bubble floatation cell - Google Patents
Stirring-separating-separated bubble floatation cell Download PDFInfo
- Publication number
- CN2224031Y CN2224031Y CN 95215313 CN95215313U CN2224031Y CN 2224031 Y CN2224031 Y CN 2224031Y CN 95215313 CN95215313 CN 95215313 CN 95215313 U CN95215313 U CN 95215313U CN 2224031 Y CN2224031 Y CN 2224031Y
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- China
- Prior art keywords
- impeller
- separates
- separate
- trap tube
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Abstract
The utility model relates to a flotation machine for separating mineral particles. An upper impeller with a plurality of radial straight blades is arranged above the rotary shaft of a vertical stirrer, and a plurality of lower impellers which are arranged at intervals and are provided with a plurality of radial oblique blades. Vertical trapping pipes for containing the upper and the lower impellers are arranged on the peripheries of the upper and the lower impellers on the rotary shaft of the vertical stirrer, and the bottoms of the trapping pipes are provided with communicated distributors which are hung in separating tanks. As a result, the mineral particles separating precision is high (such as coal particles, etc.), and the power for stirring is reduced.
Description
The utility model relates to the flotation device that a kind of ore particle separates, and especially refers to the bubble floatation machine of Fine Coal Flotation.
At present, the agitation impeller flotator of widespread usage comparatively, be with rotor or impeller directly fill a large amount of ore pulps (Gu, the liquid mixed flow) in the container (flotation cell), directly stir ore pulp, make it produce strong vorticla motion, because the shear action of vortex, the air that sucks flotation device is dispersed into the bubble that diameter does not wait, at this moment, because it is hydrophobic in the ore pulp, the solid particle (as: duff grain) of parent's gas sticks to the bubble surface come-up and collects, and it is hydrophilic, dredge the solid particle (as: iron sulfide of gas, clay, sandstone and lime stone etc.), flow out down with mixed current direction, it is simple in structure, processing ease, still, since stirring rotator or impeller directly stir ore pulps a large amount of in the flotation cell (Gu, the liquid mixed flow) and be stored in bubble in the ore pulp, it is very high to stir required drive.When stirring is short of power, can not produce enough micro-bubbles again, and reduce the probability of solid particle and bubble hit and adhesion, flotation rate is reduced.In addition, because the disturbance that stirring action produces in the flotation cell, the mixed flow come-up is easily carried in the space between the bubble secretly, makes part solid particle hydrophilic, that dredge gas enter froth pulp, reduces its purity (being commonly called as mechanical entrapment).Therefore, there is the high and low major defect of separation accuracy of power consumption in traditional agitation impeller flotator.
In view of this, the purpose of this utility model provides a kind of stirring and separates the bubble floatation machine that separates.The a plurality of impellers that are built in upper and lower arrangement in a VERTICAL TUBE stir the solid, liquid mixed flow, mix the liquid-solid-gas three-phase mixed flow of formation with air, and form minute bubbles through cutting, extruding, the three-phase mixed flow floatingly selects the foam of hydrophobic close aerated particle in separating tank through distributor; Not only improve the purity of froth pulp, but also reduce the consumption of stirring power greatly.
The purpose of this utility model is achieved in that it comprises separating tank and agitator, the rotating shaft top of agitator has the last impeller of a multi-disc straight radial blade and have the radially following impeller of oblique blade of several multi-discs at interval below the impeller on this, upper and lower impeller outer on rotating shaft of stirrer is arranged with the trap tube that contains upper and lower impeller, and the trap tube bottom has a distributor and this distributor of connection and is suspended in the separating tank.
Above-mentioned trap tube inwall has the cutting plate of projection.
Offer solid, liquid mixed flow inlet and air intake on the above-mentioned trap tube sidewall of position above or below the above-mentioned upward impeller.
Above-mentioned trap tube places the separating tank outside.
Above-mentioned trap tube is suspended in the separating tank.
Above-mentioned distributor is that multitube radial radiation pipe and every pipe sidewall is offered level at interval and gone out the foam hole.
Above-mentioned cutting plate be radially, the cone sheets of axially spaced-apart projection.
Owing to adopt such scheme: sorting ore particle (as: coal grain) precision height, stir the power that consumes and reduce greatly.
Below in conjunction with drawings and Examples the utility model is further specified.
Fig. 1 the utility model first example structure schematic diagram.
Fig. 2 the utility model second embodiment schematic diagram
Among the figure: 1, trap tube 11, cutting plate 12, solid, liquid mixed flow inlet 13, air intake 14, distributor 141, go out foam hole 2, agitator 21, go up impeller 22, down impeller 23, rotating shaft 24, motor 3, separating tank 31, scrape bubble device 32, foam outlet 33, wake flow outlet
First embodiment, as shown in Figure 1, it mainly comprises trap tube 1, agitator 2 and separating tank 3, wherein: trap tube 1 is the metal tube of vertical or level, its madial wall has radially, axial all pyramidal projections cutting plates 11 at interval, form wedge shape between the adjacent cutting plate 11, be convenient to push bubble and bubble is cut; Side above this trap tube 1 also is provided with solid-liquid mixed flow inlet 12 and one air intake 13, its bottom has a distributor 14 of connection, the top has centre bore, supports motor 24 in this top outer rim, and above-mentioned centre bore (band hermetically-sealed construction) rotating shaft 23 of passing agitator 2; Wherein, distributor 14 is the multitube structure of radial radiation, and every pipe sidewall is offered level at interval and gone out foam hole 141, removes distributor 14 and puts in inside and outside the separating tank 3, and the other parts of trap tube 1 all outside separating tank 3, are convenient to manipulate.
Vertical or the horizontal device that agitator 2 is made up of a last impeller 21, a plurality of impeller 22, rotating shaft 23 and motor 24 thereof down; Wherein, motor 24 is supported on trap tube 1 top, trap tube 1 top centre bore is passed in rotating shaft 23, near below solid, liquid mixed flow inlet 12 and the air intake 13 or above rotating shaft 23 on fixedly connected on impeller 21, and the below fixed interval that goes up impeller 21 connects a plurality of impellers 22 (among Fig. 1 being two) in rotating shaft 23.Wherein going up impeller 21 is that the multi-disc straight radial blade constitutes, stir solid, liquid mixed flow and air, and impeller 22 is that the radially oblique blade of multi-disc constitutes down, when stirring solid, liquid mixed flow and air, the guiding foam cooperates cutting downwards and with cutting plate 11 or pushes bubble, make it form the micro-bubble that becomes floc sedimentation with the coal particle shape, enter the distributor 14 of trap tube 1 bottom.
Separating tank 3 has scrapes bubble device 31, foam outlet 32 and wake flow outlet 33 (genus prior aries).Go out foam hole 141 foam of emerging from what be in distributor 14 in the separating tank 3, scrape scraping of bubble device 31 (on transport tape) formation through the interval that is supported in separating tank 3 tops, can move continuously and steep device 31, froth pulp is pushed foam outlet 32, and the wake flow product flows out (the mixed current of hydrophilic thin gas-solid body particle)
Second embodiment, as shown in Figure 2, trap tube 1 whole being suspended in the separating tank 3, wherein the center line of distributor 14 overlaps with tube hub, compact equipment, all the other structures are identical with first embodiment, so repeated description not.
Claims (7)
1, a kind of stirring with separate the bubble floatation machine that separates and comprise separating tank and agitator, it is characterized in that: the rotating shaft top of agitator has the last impeller of a multi-disc straight radial blade and have the radially following impeller of oblique blade of several multi-discs at interval below the impeller on this, be arranged with in the containing at the upper and lower impeller outer on the rotating shaft of stirrer, the trap tube of following impeller is suspended in the separating tank and the trap tube bottom has a distributor and this distributor of connection.
2, by the described stirring of claim 1 with separate the bubble floatation machine that separates, it is characterized in that: above-mentioned trap tube inwall has the cutting plate of projection.
3, by the described stirring of claim 1 with separate the bubble floatation machine that separates, it is characterized in that: offer solid, liquid mixed flow inlet and air intake on the above-mentioned above-mentioned trap tube sidewall of going up position above or below the impeller.
4, by the described stirring of claim 1 with separate the bubble floatation machine that separates, it is characterized in that: above-mentioned trap tube places separating tank outside.
5, by the described stirring of claim 1 with separate the bubble floatation machine that separates, it is characterized in that: above-mentioned trap tube is suspended in the separating tank.
6, by the described stirring of claim 1 with separate the bubble floatation machine that separates, it is characterized in that: above-mentioned distributor is that multitube radial radiation pipe and every pipe sidewall is offered level at interval and gone out the foam hole.
7, by the described stirring of claim 2 with separate the bubble floatation machine that separates, it is characterized in that: above-mentioned cutting plate be radially, the cone sheets of axially spaced-apart projection.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 95215313 CN2224031Y (en) | 1995-07-07 | 1995-07-07 | Stirring-separating-separated bubble floatation cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 95215313 CN2224031Y (en) | 1995-07-07 | 1995-07-07 | Stirring-separating-separated bubble floatation cell |
Publications (1)
Publication Number | Publication Date |
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CN2224031Y true CN2224031Y (en) | 1996-04-10 |
Family
ID=33864700
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 95215313 Expired - Fee Related CN2224031Y (en) | 1995-07-07 | 1995-07-07 | Stirring-separating-separated bubble floatation cell |
Country Status (1)
Country | Link |
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CN (1) | CN2224031Y (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103313796A (en) * | 2010-11-03 | 2013-09-18 | 西门子公司 | Flotation apparatus and flotation process |
CN104841571A (en) * | 2015-05-29 | 2015-08-19 | 武汉工程大学 | Novel flotation column and flotation method thereof |
CN111974746A (en) * | 2020-08-21 | 2020-11-24 | 中国石油大学(华东) | Device for cleaning filler by flotation bubbles and cleaning method |
-
1995
- 1995-07-07 CN CN 95215313 patent/CN2224031Y/en not_active Expired - Fee Related
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103313796A (en) * | 2010-11-03 | 2013-09-18 | 西门子公司 | Flotation apparatus and flotation process |
CN103313796B (en) * | 2010-11-03 | 2015-12-16 | 西门子公司 | Flotation device and method for floating |
US9475066B2 (en) | 2010-11-03 | 2016-10-25 | Primetals Technologies Germany Gmbh | Flotation apparatus and flotation method |
CN104841571A (en) * | 2015-05-29 | 2015-08-19 | 武汉工程大学 | Novel flotation column and flotation method thereof |
CN111974746A (en) * | 2020-08-21 | 2020-11-24 | 中国石油大学(华东) | Device for cleaning filler by flotation bubbles and cleaning method |
CN111974746B (en) * | 2020-08-21 | 2021-09-24 | 中国石油大学(华东) | Device for cleaning filler by flotation bubbles and cleaning method |
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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 |