CN208032410U - Blender and dispersal device for high-viscosity material dispersal device - Google Patents
Blender and dispersal device for high-viscosity material dispersal device Download PDFInfo
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- CN208032410U CN208032410U CN201721891058.5U CN201721891058U CN208032410U CN 208032410 U CN208032410 U CN 208032410U CN 201721891058 U CN201721891058 U CN 201721891058U CN 208032410 U CN208032410 U CN 208032410U
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Abstract
The utility model discloses a kind of blender and dispersal device for high-viscosity material dispersal device, dispersal device includes cylinder, and accommodating chamber is limited in cylinder, and the lower end of cylinder is equipped with discharge port, and blender is located in accommodating chamber, and blender includes：At least part of height-adjustable agitating shaft, agitating shaft is located in accommodating chamber, and the lower end of agitating shaft extends close to the inner bottom wall of cylinder straight down；Multiple stirrer paddles, multiple stirrer paddles are connected with agitating shaft, the free end of each stirrer paddle extends close to the madial wall of cylinder, the stirrer paddle for being wherein located at sustained height with the junction of agitating shaft is divided into one group, along agitating shaft be axially arranged with multigroup stirrer paddle and multigroup stirrer paddle along agitating shaft axially spaced arrangement.Blender according to the present utility model for high-viscosity material dispersal device avoids the occurrence of stirring wall built-up phenomenon, while reducing cylinder body bottom stirring blind area, stirs more uniform, improves the working efficiency of stirring.
Description
Technical field
The utility model is related to dispersing apparatus technical fields, more particularly, to one kind for high-viscosity material dispersion dress
The blender and dispersal device set.
Background technology
The application of lithium battery is very extensive at present, and wherein electrocondution slurry is the necessary adding ingredient of positive and negative anodes in lithium battery,
Electrocondution slurry is generated by sand mill, fixed in material prescription, and different dispersions and sand milling technology are to electrocondution slurry
Performance influences very big.
Dispersing apparatus in the related technology is that less and shorter diameter metal dispersion blade is equipped in conical shell, is led
High solid content is constantly pursued in the research and development of plasma-based material, and slurry viscosity is higher in experimentation, therefore the bottom of conical shell is in and stirs
Blind area is mixed, and plugging phenomenon easily occurs, while with the tenor for increasing slurry and stirring wall built-up phenomenon occurs, is thus produced
Raw dispersion unevenness so that working efficiency is relatively low.
Utility model content
The utility model aims to solve at least one of the technical problems existing in the prior art.
For this purpose, the utility model proposes a kind of blender for high-viscosity material dispersal device, the blender will not
There is stirring wall built-up phenomenon, while reducing cylinder body bottom stirring blind area, work efficiency is high.
The utility model also proposes a kind of dispersal device with above-mentioned blender.
According to the blender for high-viscosity material dispersal device of the utility model first aspect, the dispersal device packet
Cylinder is included, accommodating chamber is limited in the cylinder, the lower end of the cylinder is equipped with discharge port, and the blender is located at the receiving
Intracavitary, the blender include：At least part of height-adjustable agitating shaft, the agitating shaft is located at the accommodating chamber
Interior, the lower end of the agitating shaft extends close to the inner bottom wall of the cylinder straight down；Multiple stirrer paddles, it is multiple described to stir
Blade to be mixed to be connected with the agitating shaft, the free end of each stirrer paddle extends close to the madial wall of the cylinder,
The stirrer paddle for being wherein located at sustained height with the junction of the agitating shaft is divided into one group, along the axis of the agitating shaft
To the axially spaced arrangement equipped with multigroup stirrer paddle and multigroup stirrer paddle along the agitating shaft.
Blender according to the present utility model for high-viscosity material dispersal device, the free end of stirrer paddle extend to
Close to the madial wall of the cylinder, and it is axially arranged with multigroup stirrer paddle in agitating shaft, can both avoids the occurrence of stirring wall built-up
Phenomenon, but can stir more uniformly, reduce cylinder body bottom stir blind area, improve the working efficiency of stirring.
One embodiment according to the present utility model, free end and the cylinder madial wall of each stirrer paddle
Distance is L, wherein 2mm≤L≤55mm.
Another embodiment according to the present utility model, multigroup stirrer paddle include：Splashproof stirrer paddle group, it is described
Splashproof stirrer paddle group is arranged close to the upper end of the agitating shaft；Intermediate agitation blade group, the intermediate agitation blade group are located at
The middle part of the agitating shaft；Push stirrer paddle group, it is described that stirrer paddle group is pushed to be located at the lower end of the agitating shaft and described
Push the downside of stirrer paddle group concordant with the lower end of the agitating shaft.
According to one optional example of the utility model, each paddle-shaped of the splashproof stirrer paddle group becomes wing.
Another optional example according to the utility model, each blade of the splashproof stirrer paddle group are stirred along described
The direction of rotation for mixing axis tilts extension upwards；Each blade of the splashproof stirrer paddle group and the angle of horizontal plane are k, wherein
0°≤k≤90°。
Another optional example according to the utility model, each paddle-shaped for pushing stirrer paddle group become square
Shape, the principal plane for pushing each blade of stirrer paddle group is parallel with the axis of the agitating shaft and the promotion agitating paddle
The horizontally extending setting of each blade of leaf group.
Each paddle-shaped of another optional example according to the utility model, the intermediate agitation blade group becomes square
Shape.Another optional example according to the utility model, each blade of the intermediate agitation blade group is along the agitating shaft
Direction of rotation tilt down extension；Each blade of the intermediate agitation blade group and the angle of horizontal plane are e, wherein 20 °
≤e≤90°。
Further, the intermediate agitation blade group is multigroup, remaining group includes at least one and the splashproof agitating paddle
The identical blade group of leaf shape and/or at least one blade group identical with the promotion stirrer paddle group shape.
According to the dispersal device of the utility model second aspect, including：Cylinder limits between the inner wall and outer wall of the cylinder
Make cylindrical cavity, the thickness D of the cylindrical cavity, wherein 10mm≤D≤120mm accommodate cycle in the cylindrical cavity
Water is plane with the material in the cooling cylinder, the cylinder inner bottom wall, and the discharge port is located at the side wall of cylinder bottommost
Or the non-central place of cylinder body bottom；The blender for high-viscosity material dispersal device according to above-described embodiment, institute
Blender is stated to be located in the cylinder.
Dispersal device according to the present utility model, the free end of stirrer paddle extend close to the madial wall of the cylinder,
And it is axially arranged with multigroup stirrer paddle in agitating shaft, stirring wall built-up phenomenon can be not only avoided the occurrence of, but also can stir more
Uniformly, reduce cylinder body bottom and stir blind area, improve the working efficiency of stirring.
The additional aspect and advantage of the utility model will be set forth in part in the description, partly will be from following description
In become apparent, or recognized by the practice of the utility model.
Description of the drawings
The above-mentioned and/or additional aspect and advantage of the utility model will in the description from combination following accompanying drawings to embodiment
Become apparent and is readily appreciated that, wherein：
Fig. 1 is the schematic diagram according to the blender for high-viscosity material dispersal device of the utility model embodiment.
Reference numeral：
100：Blender；
10：Agitating shaft；
20：Stirrer paddle；21：Splashproof stirrer paddle group；211：Outer rim；212：Inner edge；
22：Intermediate agitation blade group；23：Push stirrer paddle group；
30：Fixing piece.
Specific implementation mode
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning
Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng
The embodiment for examining attached drawing description is exemplary, and is only used for explaining the utility model, and should not be understood as to the utility model
Limitation.
In the description of the present invention, it should be understood that term "center", " longitudinal direction ", " transverse direction ", " length ", " width
Degree ", " thickness ", "upper", "lower", "vertical", "horizontal", "top", "bottom" "inner", "outside", " clockwise ", " counterclockwise ", " axis
To ", " radial direction ", the orientation or positional relationship of the instructions such as " circumferential direction " be to be based on the orientation or positional relationship shown in the drawings, be only for
Described convenient for description the utility model and simplifying, do not indicate or imply the indicated device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.In addition, define " the
One ", the feature of " second " can explicitly or implicitly include one or more this feature.In the description of the utility model
In, unless otherwise indicated, the meaning of " plurality " is two or more.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " is pacified
Dress ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integrally
Connection；It can be mechanical connection, can also be electrical connection；Can be directly connected, can also indirectly connected through an intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, it can understand above-mentioned art with concrete condition
The concrete meaning of language in the present invention.
Below with reference to Fig. 1 descriptions according to the blender for high-viscosity material dispersal device of the utility model embodiment
100。
As shown in Figure 1, the blender 100 for high-viscosity material dispersal device according to the utility model embodiment includes
Agitating shaft 10 and multiple stirrer paddles 20.
Wherein, dispersal device includes cylinder, and accommodating chamber is defined in cylinder, and the lower end of cylinder is equipped with discharge port, accommodates
Chamber is connected with discharge port, and blender 100 is located in accommodating chamber, blender 100 in the operating condition, to the slurry in accommodating chamber
It is stirred, is discharged outside dispersal device by discharge port after being stirred.
Further, at least part of agitating shaft 10 is located in accommodating chamber, and the lower end of agitating shaft 10 extends straight down
Until at the inner bottom wall of cylinder, multiple stirrer paddles 20 are connected with agitating shaft 10, the free end of each stirrer paddle 20
The madial wall of cylinder is extended close to, i.e., on the madial wall of the free end infinite approach cylinder of stirrer paddle 20, in this way, can have
Avoid to effect stirring wall built-up phenomenon.
The stirrer paddle 20 for being wherein located at sustained height with the junction of agitating shaft 10 is divided into one group, along agitating shaft 10
Be axially arranged with multigroup stirrer paddle 20, and multigroup stirrer paddle 20 is along the axially spaced arrangement of agitating shaft 10, i.e., multigroup
Stirrer paddle 20 is being respectively at different height from the junction of agitating shaft 10, and multigroup stirrer paddle 20 is respectively provided with different
Function.
According to the blender 100 for high-viscosity material dispersal device of the utility model embodiment, stirrer paddle 20
Free end extends close to the madial wall of cylinder, and is axially arranged with multigroup stirrer paddle 20 in agitating shaft 10, both can be effective
Ground avoid the occurrence of stirring wall built-up phenomenon, and can stir more uniformly, improve the working efficiency of stirring.
Wherein, it is d at a distance from cylinder inner bottom surface to be located at the lowermost blade on agitating shaft 10, wherein 2mm≤d≤
50mm, for example, can be 2mm, 8mm, 14mm, 20mm, 26mm, 32mm, 38mm, 45mm or 50mm, specifically can be according to reality
Border needs to set the distance between the blade of bottommost and cylinder inner bottom surface, by the blade and cylinder by bottommost
The distance between bottom surface is limited within above range, can minimize stirring blind area.
It is used at a distance from cylinder madial wall the free end of one embodiment according to the present utility model, each stirrer paddle 20
L indicates, wherein 2mm≤L≤55mm, for example, L can be 2mm, 8mm, 15mm, 20mm, 25mm, 30mm, 35mm, 40mm,
45mm, 50mm or 55mm can specifically set L according to actual demand, by by each stirrer paddle 20
It is limited within above-mentioned zone of reasonableness at a distance from free end and cylinder madial wall, can not only avoid the occurrence of stirring wall built-up phenomenon, but also
It can flexibly be chosen according to actual conditions.
Another embodiment according to the present utility model, multigroup stirrer paddle 20 include splashproof stirrer paddle group 21, centre
Stirrer paddle group 22 and promotion stirrer paddle group 23, splashproof stirrer paddle group 21 is arranged close to the upper end of agitating shaft 10, i.e., and first
Group stirring blade arranges that intermediate agitation blade group 22 is located at the middle part of agitating shaft 10, intermediate agitation paddle close to the open end of cylinder
Between leaf group 22 is located at splashproof stirrer paddle group 21 and pushes stirrer paddle group 23, stirrer paddle group 23 is pushed to be located at agitating shaft 10
Lower end, and push the downside of stirrer paddle group 23 concordant with the lower end of agitating shaft 10, blind area stirred to prevent, by cylinder
Slurry stirring in bottom is abundant, further, it is also possible to push slurry outside discharge port discharge dispersal device.
Pass through the mutual cooperation of three groups of stirrer paddles 20 so that stirring is more full and uniform, further improves stirring effect
Rate has prevented stirring blind area occur, while having ensured that the ingredient of same layer and each layer is uniformly distributed in dispersal device.
As shown in Figure 1, an optional example according to the present utility model, each paddle-shaped of splashproof stirrer paddle group 21
As wing, i.e., each blade of splashproof stirrer paddle group 21 is in wing-shaped, increases the area of stirrer paddle, prevent due to from
The heart acts on and the effect that turns over of second group of stirrer paddle causes liquid level excessively high or the case where slurries splash.
As shown in Figure 1, another optional example according to the present utility model, each blade of splashproof stirrer paddle group 21
Extension is tilted upwards along the direction of rotation of agitating shaft 10, when such as being rotated clockwise with agitating shaft 10, splashproof stirrer paddle group
21 each blade is configured to tilt extension upwards along the clockwise direction of agitating shaft 10, i.e. the inner edge of each blade at this time
212 is lower with the height of the junction of agitating shaft 10 than the outer rim 211 of each blade with the junction of agitating shaft 10, such as with stirring
When axis 10 rotates counterclockwise, each blade of splashproof stirrer paddle group 21 be configured to the counter clockwise direction along agitating shaft 10 to
Upper inclination extends, i.e. the outer rim 211 of the inner edge 212 of each blade and the junction of agitating shaft 10 than each blade and stirring at this time
The height of the junction of axis 10 is low, to achieve the purpose that can to cover the material that intermediate agitation blade group is dug, further expands
Big blade area, realization avoid the occurrence of that slurries splash.
Further, such as along the direction that rotates clockwise of agitating shaft 10, each blade of splashproof stirrer paddle group 21 with
The angle of horizontal plane is k, wherein 20 °≤k≤90 °, such as k can be 20 °, 30 °, 40 °, 50 °, 60 °, 70 °, 80 ° or
It 90 °, can specifically be set based on actual conditions, by by the folder of each blade and horizontal plane of splashproof stirrer paddle group 21
Angle is set within above range, has not only increased the area of stirrer paddle 20, but may be implemented to avoid due to centrifugation force effect and
Lower layer's stirrer paddle turns over the case where effect causes liquid level excessively high or slurries splashing.
It is at least one in intermediate agitation blade group 22 to be as shown in Figure 1, an optional example according to the present utility model
The blade of intermediate agitation rectangle blade group, the intermediate agitation rectangle blade group is rectangle, in this way, due to intermediate agitation rectangle blade
The width of the free end of the blade of group is larger, while the free end infinite approach cylinder of the blade of intermediate agitation rectangle blade group
Madial wall, the phenomenon that slurry wall built-up can be effectively prevented from.
Another optional example according to the present utility model, each blade of intermediate agitation blade group 22 is along agitating shaft
10 direction of rotation tilts down extension, i.e., the height of each blade both sides is inconsistent, each paddle of intermediate agitation blade group 22
When leaf is rotated clockwise along agitating shaft 10, each blade tilts down extension along the clockwise direction of agitating shaft 10, with
When agitating shaft 10 rotates clockwise, each blade of intermediate agitation blade group 22 can dig material, intermediate agitation blade upwards
When each blade of group 22 rotates counterclockwise along agitating shaft 10, each blade is downward along the counter clockwise direction of agitating shaft 10
It tilts and extends, with when agitating shaft 10 rotates counterclockwise, each blade of intermediate agitation blade group 22 can dig material upwards,
So that slurry is uniformly mixed, fully in all directions.
Further, each blade of intermediate agitation blade group 22 and the angle of horizontal plane are indicated with e, wherein 20 °≤e
≤ 90 °, such as e can be 20 °, 30 °, 40 °, 50 °, 60 °, 70 °, 80 ° or 90 °, can specifically be based on actual conditions and carry out
Setting, by by the angle of each blade of intermediate agitation blade group 22 and horizontal plane be set in it is above-mentioned it is rational within the scope of,
The phenomenon that can ensureing to dig slurry upwards in agitation, avoid the occurrence of slurry same layer uniformly but being layered so that slurry
It is uniformly mixed in all directions, fully, achievees the purpose that meet demand.
In addition, the free end of each blade of intermediate agitation blade group 22 relative to agitating shaft 10 axis tilt extend or
Person's horizontal extension can tilt upward extension in the blade of intermediate agitation blade group 22, can also extend obliquely downward, specifically
The extending direction of the free end of each blade of intermediate agitation blade group 22 can be set according to actual production requirement, with
Preferably meet actual requirement.
Further, intermediate agitation blade group 22 is multigroup, remaining group includes at least one and splashproof stirrer paddle group 21
The identical blade group of shape and/or at least one blade group identical with 23 shape of stirrer paddle group is pushed.
As shown in Figure 1, push the width of the free end of the blade of stirrer paddle group 23 larger, it is smaller to account for cylinder volume, has
Conducive to pushing slurry to be sufficiently mixed, stirring blind area is avoided the occurrence of, furthermore, help that slurry is pushed to enter discharge port, prevents slurry
It omits.
Another optional example according to the present utility model, push the principal plane of each blade of stirrer paddle group 23 with
The axis of agitating shaft 10 is arranged in parallel, that is, the principal plane of each blade of stirrer paddle group 23 is pushed to be arranged with horizontal plane,
Ensure blade and slurry contact area maximum in the axial direction, when blender 100 works, pushes the every of stirrer paddle group 23
A blade can the parallel impeller material in strong and maximum ground, be conducive to the mixing of slurry same layer.
Another optional example according to the present utility model, push the principal plane of each blade of stirrer paddle group 23 with
The axis of agitating shaft 10 is arranged in parallel, that is, the principal plane of each blade of stirrer paddle group 23 is pushed to be arranged with horizontal plane,
And each madial wall for pushing 23 horizontally extending to unlimited close cylinder of stirrer paddle group, when blender 100 works,
It pushes stirrer paddle group 23 that can stir the slurry of cylinder body bottom, cylinder body bottom is avoided stirring blind area occur.In addition, ensureing blade
Push each blade of stirrer paddle group 23 can when blender 100 works with slurry contact area maximum in the axial direction
With strong and maximum parallel impeller material is conducive to the mixing of slurry same layer.
Further, minimum range of each blade of promotion stirrer paddle group 23 apart from cylinder body bottom described in bottommost is
H, wherein 2mm≤H≤50mm.Such as H can be 5mm, 10mm, 20mm, 30mm, 40mm or 50mm, can specifically be based on real
Border situation is set, and pushes minimum range of each blade of stirrer paddle group 23 apart from cylinder body bottom to set by bottommost
Within the scope of above-mentioned rational, it is ensured that the slurry of cylinder bottom fully participates in mixing, and reduces stirring blind area.
Another embodiment according to the present utility model, stirrer paddle 20 are macromolecule material part, such as stirrer paddle and are stirred
It mixes axis 10 and uses macromolecule material, avoid introducing metal impurities, while avoiding the condensed water generated on metal material to influence slurry
Item matter has enough hardness and corrosion resistance, improves the service life of blender 100, while not interfering with slurry product
Matter.
Further embodiment according to the present utility model, every group of stirrer paddle 20 along agitating shaft 10 circumferential uniform intervals
Arrangement is opened, in this way, multiple stirrer paddles 20 can be stirred simultaneously to slurry in the circumferential direction along agitating shaft 10, improves and stirs
Mix the stirring efficiency of device 100.
The upper end of blender 100 is equipped with fixing piece 30, and fixing piece 30 is connected by connector with agitating shaft 10, for fixing
Blender 100 so that stable structure, it is ensured that the working performance of blender 100.
It is divided into according to the stirrer paddle of the blender 100 for high-viscosity material dispersal device of the utility model embodiment
2-4 groups, such as can be 2 groups, 3 groups and 4 groups, and the radius long enough of stirrer paddle, infinite approach cylinder madial wall, effectively
Ground prevents slurry wall built-up phenomenon, stirrer paddle is designed as three functional layers, the promotion stirrer paddle group 23 of bottom is responsible for promotion
Slurry, avoids the occurrence of stirring blind area, and the intermediate agitation blade group 22 in middle level is responsible for digging slurry, the splashproof stirrer paddle group on upper layer
21 push down slurry, prevent slurries from splashing, by the way that the stirrer paddle 20 of rectangle and wing stirrer paddle 20 to be used cooperatively so that
Slurry mixing is abundant, is evenly distributed.
The dispersion gained slurry quality of blender 100 for high-viscosity material dispersal device in the utility model is uniform,
It can effectively shorten and the time is sanded, improve production efficiency, reduce energy consumption, when same sand mill in the related technology is with sand milling under technique
Between be 8-10 hour, after the blender 100, be sanded the time be 6-8 hours, greatly improve work efficiency.
According to the dispersal device of the utility model second aspect, including cylinder and according in above-described embodiment for high viscous
The blender 100 of material dispersing device is spent, blender 100 is located in cylinder, and tubular is limited between the inner wall and outer wall of cylinder
Cavity, so-called cylindrical cavity refers to has cavity between the madial wall and lateral wall of cylinder, in the inner bottom surface and outer bottom of cylinder
Also there is cavity between face, the thickness of cylindrical cavity be D, wherein 10mm≤D≤120mm, such as D can be 10mm, 20mm,
30mm, 50mm, 70mm, 100mm or 120mm, by by the thickness limit of cylindrical cavity within above range so that structure
Small volume is occupied, and can make to accommodate recirculated water in cylindrical cavity again, is cooled down in this way to the material in cylinder.
It is plane that cylinder, which is inner bottom surface, and discharge port be located at cylinder the lowermost cylinder lateral wall or cylinder body bottom it is non-in
Heart position, in this way, helping that stirrer paddle group 23 is pushed to release the material of cylinder body bottom outside cylinder from discharge port.
The free end of dispersal device according to the present utility model, stirrer paddle 20 extends close to the madial wall of cylinder, and
It is axially arranged with multigroup stirrer paddle in agitating shaft 10, can have not only avoided the occurrence of stirring wall built-up phenomenon, but also can stir more
Uniformly, reduce cylinder body bottom and stir blind area, improve the working efficiency of stirring.
According to the utility model embodiment for high-viscosity material dispersal device blender 100 and dispersal device its
He is constituted and operation is all for those of ordinary skills known, is not detailed herein.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " illustrative examples ",
The description of " example ", " specific example " or " some examples " etc. means specific features described in conjunction with this embodiment or example, knot
Structure, material or feature are contained at least one embodiment or example of the utility model.In the present specification, to above-mentioned art
The schematic representation of language may not refer to the same embodiment or example.Moreover, description specific features, structure, material or
Person's feature can be combined in any suitable manner in any one or more of the embodiments or examples.
While there has been shown and described that the embodiments of the present invention, it will be understood by those skilled in the art that：
Can these embodiments be carried out with a variety of variations in the case where not departing from the principles of the present invention and objective, modification, replaced
And modification, the scope of the utility model are limited by claim and its equivalent.
Claims (10)
1. a kind of blender for high-viscosity material dispersal device, which is characterized in that the dispersal device includes cylinder, described
Accommodating chamber is limited in cylinder, the lower end of the cylinder is equipped with discharge port, and the blender is located in the accommodating chamber, described to stir
Mixing device includes：
At least part of height-adjustable agitating shaft, the agitating shaft is located in the accommodating chamber, under the agitating shaft
End extends close to the inner bottom wall of the cylinder straight down；
Multiple stirrer paddles, multiple stirrer paddles are connected with the agitating shaft, the free end of each stirrer paddle
The madial wall of the cylinder is extended close to, wherein being located at the stirrer paddle of sustained height with the junction of the agitating shaft
Be divided into one group, along the agitating shaft be axially arranged with multigroup stirrer paddle and multigroup stirrer paddle is stirred along described
Mix the axially spaced arrangement of axis.
2. the blender according to claim 1 for high-viscosity material dispersal device, which is characterized in that stirred described in each
The free end for mixing blade is L, wherein 2mm≤L≤55mm at a distance from the cylinder madial wall.
3. the blender according to claim 2 for high-viscosity material dispersal device, which is characterized in that stirred described in multigroup
Mixing blade includes：
Splashproof stirrer paddle group, the splashproof stirrer paddle group are arranged close to the upper end of the agitating shaft；
At least one set of intermediate agitation blade group, the intermediate agitation blade group are located at the middle part of the agitating shaft；
Stirrer paddle group, the promotion stirrer paddle group is pushed to be located at the lower end of the agitating shaft and the promotion stirrer paddle group
Downside it is concordant with the lower end of the agitating shaft.
4. the blender according to claim 3 for high-viscosity material dispersal device, which is characterized in that the splashproof stirs
Mixing each paddle-shaped of blade group becomes wing.
5. the blender according to claim 3 for high-viscosity material dispersal device, which is characterized in that the splashproof stirs
The each blade for mixing blade group tilts extension upwards along the direction of rotation of the agitating shaft；The splashproof stirrer paddle group it is every
The angle of a blade and horizontal plane is k, wherein 0 °≤k≤90 °.
6. the blender according to claim 3 for high-viscosity material dispersal device, which is characterized in that the promotion is stirred
Mixing each paddle-shaped of blade group becomes rectangle, the principal plane and the agitating shaft of each blade of the promotion stirrer paddle group
Axis it is parallel and it is described push stirrer paddle group the horizontally extending setting of each blade.
7. the blender according to claim 3 for high-viscosity material dispersal device, which is characterized in that the centre is stirred
It is intermediate agitation rectangle blade group to mix at least one in blade group, and the blade of the intermediate agitation rectangle blade group is rectangle.
8. the blender according to claim 3 for high-viscosity material dispersal device, which is characterized in that the centre is stirred
The each blade for mixing blade group tilts down extension along the direction of rotation of the agitating shaft；The intermediate agitation blade group it is every
The angle of a blade and horizontal plane is e, wherein 20 °≤e≤90 °.
9. the blender according to claim 7 for high-viscosity material dispersal device, which is characterized in that the centre is stirred
It is multigroup, including at least one blade group identical with the splashproof stirrer paddle group shape and/or at least one to mix blade group
Blade group identical with the promotion stirrer paddle group shape.
10. a kind of dispersal device, which is characterized in that including：
Cylinder limits cylindrical cavity between the inner wall and outer wall of the cylinder, the thickness of the cylindrical cavity is D, wherein
10mm≤D≤120mm, recirculated water is accommodated in the cylindrical cavity with the material in the cooling cylinder, bottom in the cylinder
Wall is plane, and discharge port is located at the side wall of cylinder bottommost or the non-central place of cylinder body bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721891058.5U CN208032410U (en) | 2017-12-28 | 2017-12-28 | Blender and dispersal device for high-viscosity material dispersal device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721891058.5U CN208032410U (en) | 2017-12-28 | 2017-12-28 | Blender and dispersal device for high-viscosity material dispersal device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109822714A (en) * | 2019-03-29 | 2019-05-31 | 河北科技大学 | It is a kind of using gypsum slurries as the 3D pattern forming device of material |
| CN110169230A (en) * | 2018-12-28 | 2019-08-27 | 河南科技学院 | A kind of cotton seeds species test stirrer paddle |
| CN110180241A (en) * | 2019-05-25 | 2019-08-30 | 禹涵（上海）环保科技有限公司 | A kind of oil particles U-shaped coupling dispersal device |
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2017
- 2017-12-28 CN CN201721891058.5U patent/CN208032410U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110169230A (en) * | 2018-12-28 | 2019-08-27 | 河南科技学院 | A kind of cotton seeds species test stirrer paddle |
| CN109822714A (en) * | 2019-03-29 | 2019-05-31 | 河北科技大学 | It is a kind of using gypsum slurries as the 3D pattern forming device of material |
| CN109822714B (en) * | 2019-03-29 | 2023-12-12 | 河北科技大学 | Use 3D pattern forming device of gypsum thick liquid as material |
| CN110180241A (en) * | 2019-05-25 | 2019-08-30 | 禹涵（上海）环保科技有限公司 | A kind of oil particles U-shaped coupling dispersal device |
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