CN207680106U - A kind of slurries concentration agitating device - Google Patents
A kind of slurries concentration agitating device Download PDFInfo
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- CN207680106U CN207680106U CN201721573793.1U CN201721573793U CN207680106U CN 207680106 U CN207680106 U CN 207680106U CN 201721573793 U CN201721573793 U CN 201721573793U CN 207680106 U CN207680106 U CN 207680106U
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Abstract
The utility model is related to slurries to concentrate agitating device, including stirred tank, sloping plate unit and distributing trough；Stirring trench bottom has discharge port, thereon end opening；Stirred tank inner bottom wall is equipped with rabbling mechanism；Rabbling mechanism is sequentially connected with mixer drive；Sloping plate unit is mounted in the open end of stirred tank；Distributing trough is arranged above stirred tank, and bottom is equipped with blanking channel, and feed control mechanism is equipped at blanking channel；Blanking channel, which is respectively communicated with to be equipped with, divides pipe；Every is divided pipe lower end to be evenly equipped with multiple tremie pipes respectively, and corresponding level is equipped with drapery panel between sloping plate unit upper end and each tremie pipe, and multiple throttle orifices are evenly equipped on drapery panel；Stirred tank open end is equipped with downflow weir, and the level height of drapery panel is higher than the upper end level height of downflow weir；It is equipped with overflow launder on the open end lateral wall of stirred tank.Advantage：Sloping plate unit combines together with stirred tank, and floor space is few, at low cost, and thickening efficiency is high, and operation and maintenance cost is low.
Description
Technical field
The utility model is related to slurries concentration technique, more particularly to a kind of slurries concentrate agitating device.
Background technology
At present in Proccessing technology, common thickener is mostly used to the concentration of ore pulp or lamella thickener carries out
Concentration, slurry after concentration are sent into Tailings Dam or large-scale stirred tank storage by pump and pipeline, then are carried out by pipeline defeated
It send to next procedure, the adjustment of concentration is completed by independent water systems and detecting system.This technique is widely used in iron
In concentrate pipe-line transportation system, used common thickener and lamella thickener are both needed to be independently arranged and take up a large area,
It is fed and discharge needs, by pump and pipeline, to invest big, high energy consumption.
In addition, lamella thickener is widely used in tailings glass and Treatment of Sludge, CN102228750B discloses one
Kind efficient tilting plate thickener is made of the box cone of top sloping plate unit, lower part with agitating device, and feed is direct from top
Feed, into sloping plate unit in concentrate, the slurry after concentration accumulates in cone, is discharged by lower part discharge port, this equipment
Concentration slurry concentration in cone cannot be controlled and be adjusted, can not meet subsequent process to stable slurry concentration requirement,
So this equipment has the function of that concentrating function does not have concentration control adjustment.
In addition, the feed-type that inclined plate thickener uses at present include top feed (CN102228750B,
CN203634873U), middle part feed (CN203724821U), lower part feed (《Metal mine》7th phase in 2010《In oblique narrow flow
Solid particless deposit the research with landing on inclined plate face》It is mentioned in one text " to slurry by the lower part of each oblique narrow flow monomer side, edge
Horizontal direction ... enters ") three kinds of modes, these three feed-types disturb to fine grain sedimentation generation is larger in ore pulp
It is dynamic, it is unfavorable for the sedimentation of subparticle, reduces concentrated effect and overflow water quality.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of slurries to concentrate agitating device, effectively overcomes existing
There is the defect of technology.
The technical solution that the utility model solves above-mentioned technical problem is as follows：A kind of slurries concentration agitating device, including stir
Mix slot, sloping plate unit and distributing trough；
Above-mentioned stirred tank is the cylinder-like structure of inner hollow and upper end opening, and bottom has discharge port；
Multiple rabbling mechanisms are uniformly provided in the interior bottom wall of above-mentioned stirred tank；Multiple above-mentioned rabbling mechanism difference one are a pair of
That answers is sequentially connected with mixer drive；
Above-mentioned sloping plate unit be with the above-mentioned matched cylindrical structure in stirred tank open end, and be coaxially mounted to above-mentioned stirred tank
Open end in；
Above-mentioned distributing trough is arranged above the middle part of above-mentioned stirred tank open end, and bottom is equipped with multiple its blankings of connection
Channel each is correspondingly provided with to control the feed control mechanism of its blanking state at above-mentioned blanking channel；
Each above-mentioned blanking channel is connected to and in communication with to be equipped with respectively correspondingly divides pipe；
Every above-mentioned point of pipe lower end is evenly equipped with multiple tremie pipes, above-mentioned sloping plate unit upper end and each above-mentioned blanking respectively
One-to-one level is equipped with drapery panel between pipe, and multiple throttle orifices are evenly equipped on above-mentioned drapery panel；
The open end of above-mentioned stirred tank is equipped with downflow weir, and the level height of above-mentioned drapery panel is upper higher than above-mentioned downflow weir
Hold level height；
It is equipped with overflow launder on the open end lateral wall of above-mentioned stirred tank.
The utility model has the beneficial effects that：Apparatus structure is simple, and sloping plate unit organically combines together with stirred tank, makes
Slurry concentrating, storage, concentration control are completed in set of device, are eliminated common thickener, are reduced the techniques ring such as pump, pipeline
Section, construction land area reduce 50%, and construction investment reduces 50%；It takes subregion and recycles feed-type stage by stage, improve
Thickening efficiency reduces the expense of day-to-day operation and maintenance.
Based on the above technical solution, the utility model can also do following improvement.
Further, matched circular upper skeleton, above-mentioned upper bone are coaxially installed in the open end of above-mentioned stirred tank
Frame is located at the top of above-mentioned sloping plate unit；Above-mentioned drapery panel is arranged in the top of above-mentioned upper skeleton；Above-mentioned distributing trough is fixed on
Above the middle part for stating upper skeleton.
The arrangement of distributing trough and drapery panel is easy for using the advantageous effect of above-mentioned further scheme, it is ensured that whole device
Structure is than stronger.
Further, it is vertically equipped with respectively close to the position of each above-mentioned rabbling mechanism to prevent on above-mentioned stirred tank inner wall
Slurry forms the first spoiler of circulation in whipping process.
Advantageous effect using above-mentioned further scheme is that slurry whipping process in stirred tank is avoided to generate rotary motion,
Prevent the rotary motion of slurry from causing harmful effect to the structure of sloping plate unit.
Further, above-mentioned distributing trough is cylindrical groove body, and is coaxially fixed in above-mentioned upper skeleton by support column
Above portion, multiple above-mentioned blanking channels are evenly distributed respectively in the bottom of above-mentioned distributing trough, and more above-mentioned point of pipes are circumferentially
It is uniformly distributed, one end is connected to and in communication with corresponding above-mentioned blanking channel respectively, and the other end is respectively diagonally downward and towards upper
The upper end edge for stating upper skeleton extends.
Advantageous effect using above-mentioned further scheme is reasonable design, is conducive to uniform distribution, and it is heavy to particle to reduce feed
The disturbance of drop.
Further, multiple second spoilers, multiple above-mentioned second choked flows are equipped in the interior bottom wall of above-mentioned stirred tank vertically
The upper end level height of plate be higher than above-mentioned rabbling mechanism upper end level height, and be distributed on two neighboring above-mentioned rabbling mechanism it
Between, to prevent slurry in whipping process from forming circulation.
Advantageous effect using above-mentioned further scheme is to further avoid slurry whipping process in stirred tank to generate back
Transhipment is dynamic, prevents the rotary motion of slurry from causing harmful effect to the structure and sedimentation effect of sloping plate unit.
Further, the lower end of above-mentioned sloping plate unit is coaxially provided with matched circular lower skeleton, above-mentioned first choked flow
The upper end of plate extends upwardly to respectively to offset with the lower end of above-mentioned lower skeleton.
Advantageous effect using above-mentioned further scheme is that the design plays supporting role to sloping plate unit, it is ensured that inclined plate
Device having good stability in use.
Further, above-mentioned feed control mechanism includes cone valve, cone valve axis and cone valve motor, and above-mentioned cone valve is arranged at above-mentioned point
In slot allocation, and positioned at the top of corresponding blanking channel and above-mentioned distributing trough connectivity part, above-mentioned cone valve axis is vertically arranged, lower end
It being connect with above-mentioned cone valve upper end, the upper end passes through the upper end of above-mentioned distributing trough and is connect with the driving end of above-mentioned cone valve motor, on
State cone valve motor can by drive end drive cone valve axis drive cone valve move up and down, open or close above-mentioned distribution trench bottom with it is upper
State the passway of blanking channel connection.
Advantageous effect using above-mentioned further scheme is that feed control mechanism is simple in structure, easy for operation.
Description of the drawings
Fig. 1 is that the slurries of the utility model concentrate the structural schematic diagram of agitating device；
Fig. 2 is that the slurries of the utility model concentrate the structure top view that rabbling mechanism is distributed in agitating device；
Fig. 3 concentrates the structure that feed control mechanism coordinates with distributing trough in agitating device for the slurries of the utility model and shows
Meaning.
In attached drawing, parts list represented by the reference numerals are as follows：
1, stirred tank, 2, sloping plate unit, 3, distributing trough, 4, rabbling mechanism, 5, mixer drive, 6, drapery panel, 7, overflow
Flow weir, 8, overflow launder, the 11, first spoiler, the 12, second spoiler, 21, upper skeleton, 22, lower skeleton, 31, blanking channel, 32,
Point pipe, 33, feed control mechanism, 321, tremie pipe, 331, cone valve, 332, cone valve axis, 333, cone valve motor.
Specific implementation mode
The principles of the present invention and feature are described below in conjunction with attached drawing, example is served only for explaining this practicality
It is novel, it is not intended to limit the scope of the utility model.
Embodiment：As shown in Figures 1 to 3, the slurries concentration agitating device of the present embodiment includes stirred tank 1,2 and of sloping plate unit
Distributing trough 3；
Above-mentioned stirred tank 1 is the cylinder-like structure of inner hollow and upper end opening, and bottom has discharge port；
Multiple rabbling mechanisms 4 are uniformly provided in the interior bottom wall of above-mentioned stirred tank 1；Multiple difference of above-mentioned rabbling mechanism 4 one
The one corresponding and drive connection of mixer drive 5；
Above-mentioned sloping plate unit 2 be with the matched cylindrical structure in 1 open end of above-mentioned stirred tank, and be coaxially mounted to above-mentioned stirring
In the open end of slot 1；
Above-mentioned distributing trough 3 is arranged above the middle part of 1 open end of above-mentioned stirred tank, and bottom is equipped with multiple be connected under it
Expect channel 31, to be correspondingly provided with to control the feed control mechanism 33 of its blanking state at each above-mentioned blanking channel 31；
Each above-mentioned blanking channel 31 is connected to and in communication with to be equipped with respectively correspondingly divides pipe 32；
Every above-mentioned point of 32 lower end of pipe is evenly equipped with multiple tremie pipes 321 respectively, 2 upper end of above-mentioned sloping plate unit with it is each on
One-to-one level is equipped with drapery panel 6 between stating tremie pipe 321, and multiple throttle orifices are evenly equipped on above-mentioned drapery panel 6；
The open end of above-mentioned stirred tank 1 is equipped with downflow weir 7, and the level height of above-mentioned drapery panel 6 is higher than above-mentioned downflow weir 7
Upper end level height；
It is equipped with overflow launder 8 on the open end lateral wall of above-mentioned stirred tank 1.
During use, slurry is distributed from each blanking channel 31 in distributing trough 3 to each point of pipe 32, then by every
A tremie pipe 321 divided on pipe 32 flows in blanking to corresponding drapery panel 6 respectively, is passed through after uniformly being spread out on drapery panel 6
The throttle orifice of drapery panel 6, which uniformly flows into, carries out sedimentation concentration operation in sloping plate unit 2, be deposited on the inclined plate of sloping plate unit 2
Concentration ore pulp is dropped into along inclined plate downslide in stirred tank 1, and stirred tank 1 drives as storage ore chimney, later mixer drive 5 at this time
Corresponding rabbling mechanism 4 rotates the slurry agitation to lower part in stirred tank 1, in normal operation, due to the stirring of rabbling mechanism 4
Effect, stirred tank 1 is interior to form a transition region, and the following slurry of transition region is in agitated conditions, more than transition region is in relatively quiet
Only state, in favor of the sedimentation of particle, the height of transition region can be lifted with the mixing speed of rabbling mechanism 4, but highest
No more than the lower end level height of sloping plate unit 2, when concentration reaches requirement, over time, the wash on upper layer
(water contains the diluter liquid of slurry) is spilled over to by the zigzag mouth of 7 upper end of downflow weir in overflow launder 8, then by 8 row of overflow launder
Go out, has the discharge port of opening stirred tank 1 after a certain amount of ore pulp in stirred tank 1, the ore pulp after concentration is with stable concentration
Into next road pipeline conveying operation；It should be strongly noted that above-mentioned blanking channel 31 should be by being fed control mechanism 33
Control, makes multiple blanking channels 31 select one opening by turns by certain sequencing, to realize that subregion recycles cloth stage by stage
Material, the purpose for the arrangement is that by ore pulp between the inclined plate of sloping plate unit 2 particle settle disturbance be preferably minimized, and other regions by
It is disturbed in no cloth, ore pulp particle is in free settling state, and settling efficiency is high.
It should be noted that above-mentioned sloping plate unit 2 is sloping plate unit traditional on the market, put down by multiple inclinations and mutually
Capable inclined plate composition, can also be inclined tube filler, main purpose is to be settled, concentrated to slurry here.
Preferably, being coaxially installed in the open end of above-mentioned stirred tank 1, matched (matching refers to opening for stirred tank 1
Mouthful end diameter should diameter equal with the diameter of upper skeleton 21 or upper skeleton 21 the open end that should be slightly larger than stirred tank 1 it is straight
Diameter, it is ensured that upper skeleton 21 can be firmly installed in the open end of stirred tank 1) circular upper skeleton 21, above-mentioned upper skeleton 21
Positioned at the top of above-mentioned sloping plate unit 2；Above-mentioned drapery panel 6 is arranged in the top of above-mentioned upper skeleton 21；Above-mentioned distributing trough 3 is fixed on
Above the middle part of above-mentioned upper skeleton 21, make the purpose for the arrangement is that preferable support can be played to distributing trough 3 by upper skeleton 21
With avoiding distributing trough 3 from being directly installed on the top of sloping plate unit 2 and the sedimentation to sloping plate unit 2 and concentration is caused to cause certain journey
The influence of degree, and promote the structural strength of whole device.
It should be noted that above-mentioned drapery panel 6 is by supporting rack or support column or other connectors and upper skeleton 21
Upper end is connected and fixed, to ensure the top for being hung on upper skeleton 21 that drapery panel 6 can be stablized.
Minimum range between multiple above-mentioned drapery panels 6 and downflow weir 7 is 1.5-2.5 meters, in drapery panel 6 and this overflow
Sedimentation operation is only carried out in region between weir 7, without cloth, to ensure overflow water quality.
Preferably, be vertically equipped with respectively close to the position of each above-mentioned rabbling mechanism 4 on 1 inner wall of above-mentioned stirred tank with to prevent
Only slurry forms the first spoiler 11 of circulation in whipping process, as shown in Fig. 2, by taking four rabbling mechanisms 4 as an example, four stirrings
The line centered on the axis of stirred tank 1 of mechanism 4 is uniformly distributed circumferentially, and the first spoiler 11 is equipped with eight, wherein four difference
Close to corresponding rabbling mechanism 4, four additional is in order to preferably prevent slurry in whipping process from forming circulation, eight the first choked flows
Plate is evenly distributed on the madial wall of above-mentioned stirred tank 1.
Preferably, above-mentioned distributing trough 3 is cylindrical groove body, and above-mentioned upper skeleton 21 is coaxially fixed on by support column
Above middle part, multiple above-mentioned blanking channels 31 are evenly distributed respectively in the bottom of above-mentioned distributing trough 3, more above-mentioned point of pipes 32
It is uniformly distributed circumferentially, one end is connected to and in communication with corresponding above-mentioned blanking channel 31 respectively, and other end difference is diagonally downward
And extend towards the upper end edge of above-mentioned upper skeleton 21, this is rationally distributed, can ensure that the uniform of 3 sub-material of distributing trough.
Preferably, multiple second spoilers 12 are equipped in the interior bottom wall of above-mentioned stirred tank 1 vertically, multiple above-mentioned second resistances
The upper end level height of flowing plate 12 is above the upper end level height of above-mentioned rabbling mechanism 4, and is distributed on two neighboring above-mentioned stir
Between mixing mechanism 4, to prevent slurry in whipping process from forming circulation, as shown in Fig. 2, each above-mentioned rabbling mechanism 4 is respectively provided with
Second spoiler 12 forms the independent zones that can accommodate a rabbling mechanism 4 between second spoiler 12 and the inner wall of stirred tank 1
Domain so that slurry will not be disturbed mutually when being stirred between two neighboring rabbling mechanism 4.
Preferably, the lower end of above-mentioned sloping plate unit 2 is coaxially provided with matched circular lower skeleton 22, above-mentioned first resistance
The upper end of flowing plate 11 extends upwardly to respectively to offset with the lower end of above-mentioned lower skeleton 22, is risen to sloping plate unit 2 by lower skeleton 22
It plays a supporting role to lower skeleton 22 to preferable supporting role, then by multiple first spoilers 11, inclined plate is enabled to fill
Set 2 can stablize mounted on the open end of stirred tank 1, it is ensured that the stability of whole device.
It should be noted that above-mentioned upper skeleton 21 and lower skeleton 22 are welded to each other by crisscross crossbeam and are made,
There are multiple equally distributed void regions in it, be convenient for the blanking of slurry.
Preferably, above-mentioned feed control mechanism 33 includes cone valve 331, cone valve axis 332 and cone valve motor 333, above-mentioned cone valve
331 are arranged in above-mentioned distributing trough 3, and positioned at the top of corresponding blanking channel 31 and 3 connectivity part of above-mentioned distributing trough, above-mentioned cone
Valve shaft 332 is vertically arranged, and lower end is connect with 331 upper end of above-mentioned cone valve, the upper end pass through above-mentioned distributing trough 3 upper end and with it is upper
The driving end connection of cone valve motor 333 is stated, above-mentioned cone valve motor 333 can be by driving end that cone valve axis 332 is driven to drive cone valve 331
It moves up and down, opens or closes the passway that 3 bottom of above-mentioned distributing trough is connected to above-mentioned blanking channel 31, be fed control mechanism 33
It is simple in structure, cone valve axis 332 can be driven by cone valve motor 333 and cone valve 331 is moved downward to and blocks blanking channel 31
Upper passage mouth (closed state) moves upwardly away from 31 Upper passage mouth (opening state) of blanking channel.
Above-mentioned rabbling mechanism 4 is made of the agitating shaft being vertically arranged and the impeller being arranged on agitating shaft, under agitating shaft
End drives end to be sequentially connected across the cylinder bottom of stirred tank 1 with corresponding mixer drive 5, and above-mentioned mixer drive 5 drives
The speed of agitating shaft rotation is adjustable, that is, being exactly the rotating speed of impeller can be adjusted according to concentration requirement, after controlling concentration
Pulp density is stablized within a certain range.
Above-mentioned mixer drive 5 includes motor and reduction box, and the drive shaft of above-mentioned motor and the input terminal of reduction box connect
It connects, the output end of above-mentioned reduction box is connected with the lower end of above-mentioned corresponding agitating shaft, flexible and convenient operation.
In some embodiments, further include controller, above-mentioned rabbling mechanism 4 is equipped with to measure the biography of agitator shaft speed
Sensor, the sensor on each rabbling mechanism 4 are electrically connected with the controller, and to transmit rotary speed information to controller, are each stirred
The motor for mixing 4 corresponding mixer drive 5 of mechanism is electrically connected with the controller, and controller can control the operating status of motor,
Also can (be exactly turn for driving agitating shaft to rotate according to the output power of the rational regulation motor of rotary speed information of sensor feedback
Speed).
Compared with the prior art, the technological merit of the utility model is：Since sloping plate unit 2 and stirred tank 1 is organic
It combines together, takes subregion and recycle feed-type stage by stage, improve thickening efficiency, make slurry concentrating, storage, concentration control
It is completed in set of device, eliminates common thickener, reduce the process procedures such as pump, pipeline, floor space is made to reduce 50%,
Investment reduces 50%.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all in this practicality
Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model
Within the scope of shield.
Claims (7)
1. a kind of slurries concentrate agitating device, it is characterised in that：Including stirred tank (1), sloping plate unit (2) and distributing trough (3)；
The stirred tank (1) is the cylinder-like structure of inner hollow and upper end opening, and bottom has discharge port；
It is uniformly provided with multiple rabbling mechanisms (4) in the interior bottom wall of the stirred tank (1)；Multiple rabbling mechanisms (4) are respectively
It is sequentially connected correspondingly with mixer drive (5)；
The sloping plate unit (2) be with the matched cylindrical structure in the stirred tank (1) open end, and be coaxially mounted to the stirring
In the open end of slot (1)；
The distributing trough (3) is arranged above the middle part of the stirred tank (1) open end, and bottom is equipped with multiple be connected under it
Expect channel (31), is correspondingly provided with to control the feed control mechanism of its blanking state at each blanking channel (31)
(33)；
Each blanking channel (31) is connected to and in communication with to be equipped with respectively correspondingly divides pipe (32)；
Divide pipe (32) lower end to be evenly equipped with multiple tremie pipes (321) respectively described in every, sloping plate unit (2) upper end with it is each
One-to-one level is equipped with drapery panel (6) between the tremie pipe (321), and multiple sections are evenly equipped on the drapery panel (6)
Discharge orifice；
The open end of the stirred tank (1) is equipped with downflow weir (7), and the level height of the drapery panel (6) is higher than the overflow
The upper end level height on weir (7)；
It is equipped with overflow launder (8) on the open end lateral wall of the stirred tank (1).
2. a kind of slurries according to claim 1 concentrate agitating device, it is characterised in that：The opening of the stirred tank (1)
Matched circular upper skeleton (21) is coaxially installed in end, the upper skeleton (21) is located at the sloping plate unit (2)
Top；Top of drapery panel (6) setting in the upper skeleton (21)；The distributing trough (3) is fixed on the upper skeleton
(21) above middle part.
3. a kind of slurries according to claim 2 concentrate agitating device, it is characterised in that：On stirred tank (1) inner wall
It is vertically equipped with respectively close to the position of each rabbling mechanism (4) to prevent slurry in whipping process from forming the first of circulation
Spoiler (11).
4. a kind of slurries according to claim 3 concentrate agitating device, it is characterised in that：The distributing trough (3) is cylinder
The groove body of shape, and be coaxially fixed on above the middle part of the upper skeleton (21) by support column, multiple blanking channels (31)
It is evenly distributed the bottom in the distributing trough (3) respectively, pipe (32) is divided to be uniformly distributed circumferentially described in more, one end point
It is not connected to and in communication with the corresponding blanking channel (31), the other end is respectively diagonally downward and towards the upper skeleton (21)
Upper end edge extends.
5. a kind of slurries according to claim 3 or 4 concentrate agitating device, it is characterised in that：The stirred tank (1) it is interior
Multiple second spoilers (12) are equipped on portion's bottom wall vertically, the upper end level height of multiple second spoilers (12) is above
The upper end level height of the rabbling mechanism (4), and be distributed between the two neighboring rabbling mechanism (4), to prevent from stirring
Slurry forms circulation during mixing.
6. a kind of slurries according to claim 3 or 4 concentrate agitating device, it is characterised in that：The sloping plate unit (2)
Lower end is coaxially provided with matched circular lower skeleton (22), and the upper end of first spoiler (11) extends upwardly to respectively
It offsets with the lower end of the lower skeleton (22).
7. a kind of slurries according to any one of claims 1 to 4 concentrate agitating device, it is characterised in that：The feed control
Mechanism (33) processed includes cone valve (331), cone valve axis (332) and cone valve motor (333), and the cone valve (331) is arranged at described point
In slot allocation (3), and positioned at the top of corresponding blanking channel (31) and the distributing trough (3) connectivity part, the cone valve axis (332)
Be vertically arranged, lower end is connect with the cone valve (331) upper end, the upper end pass through the distributing trough (3) upper end and with it is described
The driving end of cone valve motor (333) connects, and the cone valve motor (333) can be by driving end to drive cone valve axis (332) band mantle
Valve (331) moves up and down, and opens or closes the passway that the distributing trough (3) bottom is connected to the blanking channel (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721573793.1U CN207680106U (en) | 2017-11-22 | 2017-11-22 | A kind of slurries concentration agitating device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721573793.1U CN207680106U (en) | 2017-11-22 | 2017-11-22 | A kind of slurries concentration agitating device |
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| Publication Number | Publication Date |
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| CN207680106U true CN207680106U (en) | 2018-08-03 |
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ID=62998881
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107823920A (en) * | 2017-11-22 | 2018-03-23 | 黄双智 | A kind of slurries concentrate agitating device |
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2017
- 2017-11-22 CN CN201721573793.1U patent/CN207680106U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107823920A (en) * | 2017-11-22 | 2018-03-23 | 黄双智 | A kind of slurries concentrate agitating device |
| CN107823920B (en) * | 2017-11-22 | 2023-12-12 | 黄双智 | Slurry concentration stirring device |
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