CN205868559U - Whirl static microbubble flotation column step strengthening pipe flows section mineralize mineralization device - Google Patents
Whirl static microbubble flotation column step strengthening pipe flows section mineralize mineralization device Download PDFInfo
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- CN205868559U CN205868559U CN201620788863.4U CN201620788863U CN205868559U CN 205868559 U CN205868559 U CN 205868559U CN 201620788863 U CN201620788863 U CN 201620788863U CN 205868559 U CN205868559 U CN 205868559U
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Abstract
The utility model discloses a whirl static microbubble flotation column step strengthening pipe flows section mineralize mineralization device, including the body, characterized by: the body is divided into three sub - pipeline sections, is upper reaches pipeline section, middle pipeline section and low reaches pipeline section in proper order respectively, installation a plurality of cylindricality vortex generator in the pipeline section of the upper reaches, a plurality of toper vortex generator of installation in the middle pipeline section, the low reaches pipeline section is the fluorescent lamp section. Cylindricality vortex generator is cylinder or halfcylinder, and the top surface is bevel ellipsoid or bevel semiellipse face, and cylindricality vortex generator's bottom surface is fixed on the inner wall of upper reaches pipeline section, and its yuan of curved surface is for meeting the stream interface, top surface lateral inclination. This device, simple structure is practical, can show the turbulence intensity who improves whole duct flow section to the turbulence intensity distribution that can make duct flow section regional area presents difference evidently, thereby increases the fine grain mineral of different grades and the probability of collision between the bubble, improves the fine grain mineral rate of recovery.
Description
Technical field
This utility model relates to the pipe flow section flotation unit of a kind of Cyclonic-static fine-bubble flotation column, specifically one rotation
Stream-static microbubble floatation column step strengthening pipe flow section mineralization device, belongs to technical field of mineral processing.
Background technology
In prior art, Cyclonic-static fine-bubble flotation column, it is mainly used in the floating of coal, non-ferrous metal and non-non-ferrous metal
Choosing, mainly for particulate and the flotation of mineral particles.Its agent structure include flotation column section (or claim post segregation section dress
Put), eddy flow section (or claiming cyclonic separation section), bubble occur and pipe flow section (or general name flotation tube device) three parts.Described pipe flow
Section is the bubble generator downstream pipeline to eddy flow section entrance point of flotation column.Whole flotation column is a cylinder, its principle such as Fig. 1
Shown in.Post segregation section (post flotation) 11 is positioned at whole cylinder top；Cyclonic separation section 12 uses the aqueous medium eddy flow that post cone is connected
Device structure, and go to upper and lower the straight-through of structure with post segregation section and be connected.From rotational flow sorting angle, post segregation section is equivalent to be exaggerated
Cyclone overflow pipe.At the top of post segregation section, it is provided with spray header and froth concentrate storage tank；It is positioned at post minute to ore deposit point
From section middle and upper part, true tailings 13 is discharged by cyclonic separation section base opening.Bubble generator 14 is joined directly together into one with flotation pipeline section
Body, is individually arranged in flotation column cylinder external；It goes out to flow in tangential direction and is connected with cyclonic separation section cylinder, is equivalent to cyclone
Tangent line feed pipe.Airway is set on bubble generator.Flotation tube device 15 includes bubble generator and flotation tube section two parts.
Bubble generator is the critical component of flotation column, and it uses the internal structure being similar to jet pump, has dependence jet flow negative pressure certainly
Body introduces gas and gas is ground into the dual function (also known as self-suction microbubble generator) of bubble.Float at cyclone-static microbubble
In selecting post, the working media of bubble generator is the chats of circulation.Circulation ore pulp through pressurization enters bubble generator, introduces
Gas is also formed containing the gas of a large amount of micro air bubbles, solid, liquid three-phase system.Containing alveolate three-phase system height in flotation pipeline section
Degree turbulent flow mineralising, the most still keeps higher-energy state tangentially to enter at a high speed cyclonic separation section.So, flotation tube device is complete
While becoming flotation air inflation (self-suction microbubble generator) and highly turbulent mineralising (flotation pipeline section) function, again with tangential pan feeding
Mode defines the eddy flow field of force bottom flotation column.Flotation tube device is that all kinds of sortings of whole flotation column provide energy
Source, and substantially determine the energy state of flotation column.
This Cyclonic-static fine-bubble flotation column integrates adverse current, eddy flow and three kinds of mineralising modes of pipe flow, at fine-particle minerals
Sorting field is applied widely.Column-type floatation unit is for carrying out preliminary election to mineral, and the mineral that floatability is good can preferentially float
Choosing, obtains high-quality concentrate.Chats is sorted by eddy flow section separation unit further, obtains qualified tailings.In pipe flow section
Heterogeneous fluid tangentially enter at a high speed cyclonic separation section, separating further and edge for cyclonic separation with higher-energy state
Tangential and cyclonic separation is connected to form circulation.Pipe flow sorting environment is conducive to the recovery of strengthening fine fraction coal grain (-45 μm)；Countercurrently
Sorting environment is preferable for the recovering effect of coarse fraction coal grain (+250 μm).And rotational flow sorting advantage falls between, for
The recovering effect of middle sized coal grain (45-250 μm) is preferable.
Pipe flow section is the difficult fine mineral selected and bubble hit and adhesion during Mine By Cyclonic-static Micro-bubble Flotation Column
Main place, the turbulence intensity in this region decides the remineralization efficacy of fine-particle minerals, and is finally related to fine-particle minerals
The response rate.At present, the pipe flow segment structure employed in practice is light pipe, and turbulence intensity is less desirable, and whole pipe flow section
In turbulence intensity distribution more uniform, can only turbulence intensity required for adaption section grade mineral, thus can cause a large amount of
The Separate Fine-grained Minerals particle loss of monomer dissociation is in mine tailing.
Currently, improve pipe flow section turbulence intensity and currently mainly use two kinds of methods: one is, extend pipe flow segment length.Two are,
Use U-tube stream section.But both approaches is not notable for the increase of turbulence intensity, whole pipe flow section turbulence intensity is difficult to
Realize differentiation turbulent extent required for size fractionated scope mineral grain in adaptive mineral.In addition, U-tube stream section
Easily cause pipe flow section severely worn out, and extend pipe flow section and corresponding flotation column shell of column height can be made to increase, thus can increase
Equipment cost, reduces economic benefit.
Utility model content
For solving the problems referred to above, the utility model proposes a kind of Cyclonic-static fine-bubble flotation column step strengthening pipe flow section
Mineralization device, it is simple and practical, can significantly improve the turbulence intensity of whole pipe flow section, and can make pipe flow section partial zones
The turbulence intensity distribution in territory presents difference significantly, thus it is general to increase the collision between the fine-particle minerals of size fractionated and bubble
Rate, improves the fine-particle minerals response rate.
To achieve these goals, the technical solution adopted in the utility model is: Cyclonic-static fine-bubble flotation column step is strong
Change pipe flow section mineralization device, including body, it is characterized in that: described body is divided into three sub-pipeline sections, respectively be upstream pipeline section,
Middle pipeline section and downstream pipeline section；Several cylindricality vortex generators are installed in the pipeline section of described upstream, install some in middle pipeline section
Conical vortex flow-generator, downstream pipeline section is light pipe segment.
Vortex generator can be formed after each vortex generator in being arranged on pipeline section and flow to whirlpool a pair, and flowing to whirlpool can strengthen
Turbulence intensity in pipe flow, can significantly improve the Turbulent Kinetic in pipe flow and turbulence dissipation rate, it is thus possible to remarkably promote bubble-
Grain collision, makes remineralization efficacy be strengthened.
Preferably, at least installing five organ timbering shape vortex generators in the pipeline section of described upstream, adjacent two organ timbering shape eddy current are sent out
The position interlaced arrangement of raw device；At least installing row's conical vortex flow-generator in middle pipeline section, adjacent two row's taper eddy current are sent out
Raw device alignment.
Preferably, along flow direction, upstream tube segment length is 1.2～1.5 times of intervalve segment length.
Preferably, cylindricality vortex generator is cylinder or semicylinder, and end face is bevel ellipsoid or bevel semiellipse
Face, the bottom surface of cylindricality vortex generator is fixed on the inwall of upstream pipeline section, and its round surface is that fluoran stream surface is (in face of ore pulp flowing
To), end face lateral inclination.
Described conical vortex flow-generator is triangular pyramid structure, and a conical surface is in face of ore pulp flow direction, for fluoran stream surface, taper
The bottom surface of vortex generator is connected with the inwall of middle pipeline section.Preferably conical vortex flow-generator is right-angle prismatic cone, and two tiltedly
Rib with inclined-plane be fluoran stream surface.
Further, cylindricality vortex generator is in height H is pipeline section internal diameter 0.2 radially, and conical vortex flow-generator exists
Height h is pipeline section internal diameter 0.1 radially.The length of the oval cross section major axis of cylindricality vortex generator and upstream pipeline section internal diameter
Ratio be 0.2 ~ 0.4, the size of the bottom surface longest edge that conical vortex flow-generator is connected with pipeline section is 0.2 with the ratio of pipeline section internal diameter
~0.4。
Further, the inclined-plane of cylindricality vortex generator and the angle of the axis of pipeline section are at 15 °～20 °.Taper eddy current is sent out
The inclined-plane of raw device is fluoran stream surface, and inclined-plane is 40 °～60 ° with the angle of the axis of pipeline section.
Preferably, upstream tube intrasegmental part often arranges four cylindricality vortex generators of installation, and four cylindricality vortex generators are uniform
Ground is arranged.Intervalve intrasegmental part arranges four conical vortex flow-generators, and four conical vortex flow-generators are arranged equably, and adjacent two
Alignment between row.
Cylindricality vortex generator and conical vortex flow-generator can change the flow field of pipe flow intrasegmental part, and vortex generator has
The effect of raw whirlpool, the raw whirlpool effect of cylindricality vortex generator is better than conical vortex flow-generator, is staggeredly arranged and has compared to alignment
It is beneficial to flow to the development in whirlpool.Flow to whirlpool can periodically come off, thus form pulsating flow, pipe flow section turbulence intensity at pipe flow intrasegmental part
Being strengthened, due to the difference of three inner tube segment structures, turbulence intensity also has enhancing in various degree, streamwise
Three pipeline section turbulence intensities weaken successively.Three pipeline sections being respectively provided with varying level turbulence intensity are size fractionated mineral grains
Mineralising occur main place, i.e. upstream pipeline section is the main place of more fine-graded mineral grain generation mineralising in ore pulp,
Downstream pipeline section is the main place of more coarsely graded mineral grain generation mineralising, grade mineral grain in the middle of middle pipeline section correspondence
Mineralising.Therefore, the purpose of step strengthening mineral grain mineralising is achieved, and finally, enhances the recovery of fine-particle minerals.
This utility model Cyclonic-static fine-bubble flotation column step strengthening pipe flow section apparatus, simple and practical, can be notable
Improve the turbulence intensity of whole pipe flow section, and the turbulence intensity distribution of pipe flow section regional area can be made to present difference significantly,
Thus increase the collision probability between the fine-particle minerals of size fractionated and bubble, improve the fine-particle minerals response rate.
Accompanying drawing explanation
Fig. 1 is prior art Cyclonic-static fine-bubble flotation column structure and workflow schematic diagram.
Fig. 2 is this utility model Cyclonic-static fine-bubble flotation column step strengthening pipe flow section apparatus sectional view (vertical view).
Fig. 3 is the schematic perspective view of cylindricality vortex generator.
Fig. 4 is the schematic perspective view of conical vortex flow-generator.
Fig. 5 is Fig. 2 A-A profile.
Fig. 6 is Fig. 2 B-B profile.
Detailed description of the invention
The utility model is described in further detail below in conjunction with the accompanying drawings.
As in figure 2 it is shown, Cyclonic-static fine-bubble flotation column step strengthening pipe flow section mineralization device.Its body is divided into three sons
Pipeline section, respectively is upstream pipeline section 1, middle pipeline section 3 and downstream pipeline section 5.Several cylindricality eddy current are installed in the pipeline section of upstream send out
Raw device 2, installs some conical vortex flow-generators 4 in middle pipeline section, and downstream pipeline section 5 is light pipe segment.It is mounted with in the pipeline section of upstream
Five organ timbering shape vortex generators (described row, it is simply that along a week of the section of pipeline section, vortex generator was uniformly laid), adjacent two
The position front and back position interlaced arrangement of organ timbering shape vortex generator.In middle pipeline section 3, at least it is mounted with that two row's taper eddy current are sent out
Raw device 4, alignment before and after adjacent two row's conical vortex flow-generators.Along flow direction, upstream tube segment length is middle pipeline section
1.2～1.5 times of length.As it is shown on figure 3, cylindricality vortex generator is semicylinder, end face is bevel semiellipse face, cylindricality whirlpool
The bottom surface of flow-generator is fixed on the inwall of upstream pipeline section, its round surface be fluoran stream surface (in face of ore pulp flowing come to), top
Face lateral inclination.As shown in Figure 4, conical vortex flow-generator is triangular pyramid structure, and a conical surface is in face of ore pulp flow direction, for meeting
Stream interface, the bottom surface of conical vortex flow-generator is connected with the inwall of middle pipeline section.Preferably conical vortex flow-generator is right-angle prismatic
Cone, two slant edges with inclined-plane be fluoran stream surface.
Further, cylindricality vortex generator is in height H is pipeline section internal diameter 0.2 radially, and conical vortex flow-generator exists
Height h is pipeline section internal diameter 0.1 radially.The length of the oval cross section major axis of cylindricality vortex generator and upstream pipeline section internal diameter
Ratio be 0.2 ~ 0.4, the size of the bottom surface longest edge that conical vortex flow-generator is connected with pipeline section is 0.2 with the ratio of pipeline section internal diameter
~0.4.The angle of the inclined-plane of cylindricality vortex generator and the axis of pipeline section is at 15 °～20 °.The inclined-plane of conical vortex flow-generator is
Fluoran stream surface, inclined-plane is 40 °～60 ° with the angle of the axis of pipeline section.
Preferably, upstream tube intrasegmental part often arranges four cylindricality vortex generators of installation, and four cylindricality vortex generators are uniform
Ground is arranged.Intervalve intrasegmental part arranges four conical vortex flow-generators, and four conical vortex flow-generators are arranged equably, and adjacent two
Alignment between row.
Vortex generator can be formed after each vortex generator in being arranged on pipeline section and flow to whirlpool a pair, and flowing to whirlpool can strengthen
Turbulence intensity in pipe flow, can significantly improve the Turbulent Kinetic in pipe flow and turbulence dissipation rate, it is thus possible to remarkably promote bubble-
Grain collision, makes remineralization efficacy be strengthened.Cylindricality vortex generator and conical vortex flow-generator can change pipe flow intrasegmental part
Flow field, vortex generator has the effect of raw whirlpool, and the raw whirlpool effect of cylindricality vortex generator is better than conical vortex flow-generator, and stagger cloth
Put the development being conducive to flowing to whirlpool compared to alignment.Flow to whirlpool can periodically come off, thus form arteries and veins at pipe flow intrasegmental part
Dynamic stream, pipe flow section turbulence intensity is strengthened, and due to the difference of three inner tube segment structures, turbulence intensity also has in various degree
Enhancing, three pipeline section turbulence intensities of streamwise weaken successively.Three pipes being respectively provided with varying level turbulence intensity
Section is the main place of the mineralising generation of size fractionated mineral grain, i.e. upstream pipeline section is more fine-graded mineral grain in ore pulp
The main place of mineralising occurs, and downstream pipeline section is the main place of more coarsely graded mineral grain generation mineralising, middle pipeline section pair
The mineralising of grade mineral grain in the middle of should.Therefore, the purpose of step strengthening mineral grain mineralising is achieved, and finally, enhances
The recovery of fine-particle minerals.
Claims (9)
1. a Cyclonic-static fine-bubble flotation column step strengthening pipe flow section mineralization device, including body, is characterized in that: described pipe
Body is divided into three sub-pipeline sections, respectively is upstream pipeline section, middle pipeline section and downstream pipeline section；Install some in the pipeline section of described upstream
Individual cylindricality vortex generator, installs some conical vortex flow-generators in middle pipeline section, and downstream pipeline section is light pipe segment.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
At least installing five organ timbering shape vortex generators in the pipeline section of described upstream, the position of adjacent two organ timbering shape vortex generators interlocks cloth
Put；In middle pipeline section, row's conical vortex flow-generator, adjacent two row's conical vortex flow-generator alignment are at least installed.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
Described upstream tube segment length is 1.2～1.5 times of intervalve segment length.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
Described cylindricality vortex generator is cylinder or semicylinder, and end face is bevel ellipsoid or bevel semiellipse face, cylindricality eddy current
The bottom surface of generator is fixed on the inwall of upstream pipeline section, and its round surface is fluoran stream surface, end face lateral inclination.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
Described conical vortex flow-generator is triangular pyramid structure, and a conical surface is in face of ore pulp flow direction, and for fluoran stream surface, taper eddy current occurs
The bottom surface of device is connected with the inwall of middle pipeline section.
Cyclonic-static fine-bubble flotation column step the most according to claim 5 strengthening pipe flow section mineralization device, is characterized in that:
Described conical vortex flow-generator is right-angle prismatic wimble structure, two slant edges with inclined-plane be fluoran stream surface.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
Described cylindricality vortex generator is at height H is pipeline section internal diameter 0.2 times radially, conical vortex flow-generator height diametrically
H is 0.1 times of pipeline section internal diameter；The length of the oval cross section major axis of cylindricality vortex generator is 0.2 ~ 0.4 with the ratio of pipeline section internal diameter,
The size of the bottom surface longest edge that conical vortex flow-generator is connected with pipeline section is 0.2 ~ 0.4 with the ratio of pipeline section internal diameter.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
The angle of the inclined-plane of described cylindricality vortex generator and the axis of pipeline section is at 15 °～20 °；The fluoran stream surface of conical vortex flow-generator with
The angle of the axis of pipeline section is 40 °～60 °.
Cyclonic-static fine-bubble flotation column step the most according to claim 1 strengthening pipe flow section mineralization device, is characterized in that:
Upstream tube intrasegmental part often arranges four cylindricality vortex generators of installation, and four cylindricality vortex generators are arranged equably；Middle pipeline section
Four conical vortex flow-generators of internal arrangement, four conical vortex flow-generators are arranged equably.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620788863.4U CN205868559U (en) | 2016-07-26 | 2016-07-26 | Whirl static microbubble flotation column step strengthening pipe flows section mineralize mineralization device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620788863.4U CN205868559U (en) | 2016-07-26 | 2016-07-26 | Whirl static microbubble flotation column step strengthening pipe flows section mineralize mineralization device |
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|---|---|---|---|
| CN201620788863.4U Withdrawn - After Issue CN205868559U (en) | 2016-07-26 | 2016-07-26 | Whirl static microbubble flotation column step strengthening pipe flows section mineralize mineralization device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106040442A (en) * | 2016-07-26 | 2016-10-26 | 中国矿业大学 | Cyclone-static micro bubble flotation column step enhanced pipe flow section mineralization device |
| CN110773329A (en) * | 2019-09-19 | 2020-02-11 | 中国矿业大学 | Strong turbulence generating device suitable for micro-fine particle rapid sorting |
-
2016
- 2016-07-26 CN CN201620788863.4U patent/CN205868559U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106040442A (en) * | 2016-07-26 | 2016-10-26 | 中国矿业大学 | Cyclone-static micro bubble flotation column step enhanced pipe flow section mineralization device |
| CN106040442B (en) * | 2016-07-26 | 2019-01-01 | 中国矿业大学 | Cyclonic-static fine-bubble flotation column step enhanced tube stream section mineralization device |
| CN110773329A (en) * | 2019-09-19 | 2020-02-11 | 中国矿业大学 | Strong turbulence generating device suitable for micro-fine particle rapid sorting |
| WO2021051953A1 (en) * | 2019-09-19 | 2021-03-25 | 中国矿业大学 | Strong turbulent flow generation device suitable for rapid sorting of micro-fine particles |
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| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20170111 Effective date of abandoning: 20190101 |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20170111 Effective date of abandoning: 20190101 |