CN207203871U - A kind of solid-liquid mixing device - Google Patents
A kind of solid-liquid mixing device Download PDFInfo
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- CN207203871U CN207203871U CN201720911409.8U CN201720911409U CN207203871U CN 207203871 U CN207203871 U CN 207203871U CN 201720911409 U CN201720911409 U CN 201720911409U CN 207203871 U CN207203871 U CN 207203871U
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Abstract
The utility model provides a kind of solid-liquid mixing device, include liquid distribution module, powder dispersed modules, solid-liquid mixing module and discharge module, liquid distribution module, liquid to be mixed is delivered to mixing module, powder dispersed modules by it, it is used for after powder to be mixed is disperseed and/or crushed, into solid-liquid mixing module；Liquid to be mixed is mixed in solid-liquid mixing module with powder to be mixed and quickly rotated, and is then discharged by discharge module.The utility model, in powder dispersed modules, after first powder to be mixed is tentatively broken up, contacted with specific inclination angle with liquid to be mixed, preliminary quick moistening is carried out, using screw feed, it is not necessary to independent Valve controlling, there is stronger dispersibility.In mixing module, atwirl agitator, accelerate the moistening process of powder and liquid, in discharge module, highly viscous slurry can be discharged, while produce vacuum.
Description
Technical field
Powder slurrying, solid-liquid mixing or nano-powder material rapid dispersion field are the utility model is related to, specifically, is
Refer to a kind of solid-liquid mixing device.
Background technology
Solid powder disperses basic process in a liquid to be divided into：(1) wetting of powder：The sky that will attach on powder
Gas is substituted with liquid medium.A kind of powder will disperse in a liquid it may first have to which wetted, the wettability of the surface of solids is changed by it
Learn composition and microstructure determines.(2) particle agglomeration ruptures, disperseed, break up agglomerates：Mainly there are three kinds of active forces：Squeeze
Pressure, impact and shearing force.This scattered step is necessarily required to the auxiliary of plant equipment, the above-mentioned three kinds of active forces of different equipment
Size and ratio be different.(3) stabilisation of suspended dispersed liquid, in order to which the particle for preventing to be dispersed through occurs reuniting, point
Scattered stabilization has electrostatic stabilization, space stability ultimate load.
All powder dispersion processes are above-mentioned basic process.At present, the moistening of first step powder is all scattered streams
The starting of journey, its effect is particularly significant, if the effect of first step moistening process is good, the scattered strength or energy subsequently needed
Consumption will be low, and coarse granule can also be reduced, and the stability of slurry can be higher.
At present, the first step (wetting) and the 3rd step (stabilization) can be optimized by auxiliary agent such as Ricinate.Due to existing
Can have a negative impact in moistening auxiliary agent to subsequent technique or product, such as the slurrying flow in Lithium Battery Industry field, it is desirable to
The additive of reference can not produce infringement to electrical property, strongly limit the range of choice of moistening auxiliary agent, and this is current lithium electricity
The place that pulping process has been ignored.How to accelerate the moistening of powder surface using the energy of machinery, avoid using moistening auxiliary agent,
Accelerate powder surface moistening, a upper industry problem anxious to be resolved using physical mechanical method.
In addition, with the development of nano material and superfine powder, because it is bigger than surface, the substantial amounts of gas of adsorption,
It is difficult infiltration in a liquid to cause these superfine powdery materials, and difficulty is mixed with liquid, causes powder disperseing in a liquid
Cheng Sudu is slow, high energy consumption, inefficient.And traditional equipment only has single 26S Proteasome Structure and Function, can not adapt to wide variety of
The material characteristic of powder and liquid.
Utility model content
The utility model provides a kind of solid-liquid mixing device and the mixed method using the equipment, and it can overcome big at present
Surface area material moistening it is difficult, devise the equipment combination of difference in functionality module, the moistening of powder surface can be accelerated, with
Liquid is sufficiently mixed.
To achieve the above object, the utility model adopts the following technical scheme that：
A kind of solid-liquid mixing device, it includes liquid distribution module, powder dispersed modules, solid-liquid mixing module and discharge
Module, described liquid distribution module, liquid to be mixed is delivered to described mixing module by it, and described powder disperses mould
Block, it is used for after powder to be mixed is disperseed and/or crushed, into solid-liquid mixing module；Liquid to be mixed mixes with waiting
Close powder to be mixed in described solid-liquid mixing module and quickly rotated, then discharged by described discharge module.
Above-mentioned liquid dispersion module, it is by one or more pumps and the liquid feed pipe being correspondingly arranged with pump, by liquid
Body is delivered in narrow annular channel, after making liquid by narrow annular channel, vertically downward.
Above-mentioned powder dispersed modules, it is that the powder of impact type disperses reducing mechanism.
Above-mentioned powder dispersed modules, it includes powder dispersing chamber and the helicon being located therein impact module, described
Helicon impact module include conical body and be arranged on conical body surface, the upward cutting sheet of spiral.
Above-mentioned powder dispersed modules, it includes powder dispersing chamber and the taper being located therein impact module, described cone
Shape impact module includes conical body, and described conical body surface is provided with hard alloy coating or ceramic coating, described
Conical body be provided with groove.
Above-mentioned powder dispersed modules, its rod pin impact module for including powder dispersing chamber and being located therein are described
Rod pin impact module includes conical body and one group of stirring rod located at conical body surface.
Above-mentioned powder dispersed modules, its wing formula impact module for including powder dispersing chamber and being located therein, the described wing
Formula impact module includes conical body and one group of impact component located at conical body surface, and described impact component includes one
Connecting rod and impact block, described connecting rod one end are connected with described conical body surface, and the other end is connected with impact block.
Above-mentioned powder dispersed modules, powder can be made with certain angle of inclination and liquid vertically downward by still further comprising
Body collides, the powder discharge structure for making powder tentatively moisten.
Above-mentioned powder discharge structure, it disperses between reducing mechanism and mixing module located at described powder, and it shapes
To be a disc-shaped component, circumference offers grooving.
At least one side wall of above-mentioned grooving is with respect to disk body centerline dip.
Above-mentioned solid-liquid mixing module, it includes stainless steel and in stainless steel, make liquid to be mixed with
Powder to be mixed is mixed and carries out atwirl agitator.
The inner surface that above-mentioned powder disperses outdoor face and described stainless steel forms narrow annular channel.
Above-mentioned agitator, it includes agitator body and sets the blade of body circumference.
Above-mentioned upright blade is arranged on described body circumference.
Above-mentioned blade lean is arranged on described body circumference.
Above-mentioned agitator, it includes the container of both ends open and the transverse slat in the middle part of container, described container table
Face is provided with small opening, and described transverse slat is provided with groove.
Above-mentioned discharge module, it includes discharge container and the dispersion impeller in discharge container, described discharge
Container side wall is provided with discharge line.
Above-mentioned discharge line is provided with the pump of regulation discharge flow rate of slurry.
Above-mentioned dispersion impeller, it includes disc body and is respectively arranged on disc body upper and lower surface, with described circle
The vertical blade of disk upper and lower surface.
Above-mentioned dispersion impeller, it is configured to flabellum shape, and it includes center contiguous block and integrally formed with contiguous block
Fan blades, at least one side of described fan blades, upper and lower both sides at least side is provided with stirring bar.
After adopting the above technical scheme, by the technical program, after its elder generation tentatively breaks up powder to be mixed, with specific
Inclination angle contacted with liquid to be mixed, carry out preliminary quick moistening, in powder dispersed modules, it uses screw feed, no
With Valve controlling, there is stronger mixing power.Meanwhile in mixing module, quick rotation agitator, accelerate powder and liquid
Moistening process, finally in module is discharged, the impeller for carrying out discharge opeing produces vacuum, can discharge highly viscous slurry, produce simultaneously
Raw vacuum.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model embodiment one；
Fig. 2 is Fig. 1 partial enlarged drawing；
Fig. 3 is the schematic perspective view of the utility model embodiment one；
Fig. 4 is the schematic perspective view of powder discharge structure embodiment one；
Fig. 4 A are Fig. 4 partial enlarged drawing；
Fig. 5 is the floor map of powder discharge structure embodiment one；
Fig. 5 B are Fig. 5 partial enlarged drawing；
Fig. 6 is the structural representation of the agitator of the utility model embodiment one；
Fig. 7 is the structural representation of the dispersion impeller of the utility model embodiment one；
Fig. 8 is the schematic perspective view of the utility model embodiment three；
Fig. 9 is the floor map of the utility model embodiment three；
Figure 10 is the structural representation of the agitator of the utility model embodiment three；
Figure 11 is the schematic perspective view of the utility model embodiment four；
Figure 12 is the floor map of the utility model embodiment four；
Figure 13 is the structural representation of the agitator of the utility model embodiment four；
Figure 14 is the structural representation that module is impacted in the taper of the utility model embodiment five；
Figure 15 is the structural representation that the rod pin of the utility model embodiment six impacts module；
Figure 16 is the structural representation that the wing formula of the utility model embodiment seven impacts module；
Figure 17 is the structural representation of the dispersion impeller of the utility model embodiment eight；
Figure 17 C are Figure 17 partial enlarged drawing.
Embodiment
In order that the purpose of this utility model, technical scheme and advantage are more clearly understood, below in conjunction with accompanying drawing and implementation
Example, the utility model is further elaborated.It should be appreciated that specific embodiment described herein is only explaining this
Utility model, it is not used to limit the utility model.
Embodiment one：
With reference to shown in figure 1,2,3, it discloses a kind of solid-liquid mixing device, includes powder dispersed modules 1, liquid distribution
Module 2, solid-liquid mixing module 3 and discharge module 4, wherein：
In the present embodiment, powder dispersed modules 1, it is that the powder of impact type disperses reducing mechanism.It includes powder and disperseed
Room 11, the helicon being located therein impact module 12 and powder discharge structure 13, wherein：
Powder dispersing chamber 11, it is configured to the tubbiness of upper and lower opening, and gear wall 111 is provided with the middle part of its outer wall, keeps off on wall 111 and setting
There is positioning hole 112.
Helicon impact module 12 includes conical body 121 and is arranged on conical body surface, and spiral is upward to be cut
Pitch cutting 122.By this structure setting, touch opportunity or the collision that can increase powder and helicon impact module 12 are general
Rate.So as to reach preferable dispersion effect.
With reference to shown in figure 4,4A, 5 and 5B, powder discharge structure 13, it is located at the lower section of helicon impact module 12, its energy
Powder is collided with certain angle of inclination and liquid vertically downward, powder is tentatively moistened；It is configured to be one
Disc-shaped component, circumference offer grooving 131 and form tooth-shape structure.Grooving 131, its include three side walls 1311,1312,
1313, these three at least one side walls of side wall 1311,1312,1313 tilt with respect to disk body axle center.In the present embodiment, side wall
1311st, 1313 is are obliquely installed, side wall 1312 and disk body axis parallel.The center of powder discharge structure 13 is provided with the axle of keyway arrangements
Heart hole 132.
When implementing, by scattered powder, discharged downwards by the grooving 131 of the powder discharge structure 13, due to grooving
131 is are obliquely installed, and therefore, the powder discharged downwards is also downward with incline direction, so as to be collided with liquid vertically downward,
Reach the effect for making powder tentatively be moistened.Due to the powder of many battery materials, its size is in several microns, by abundant
After moistening, it is easy to be just dispersed into single particle, the requirement of cell size can be met.It can mitigate to follow-up mixing module
It is required that when subsequently mixing, it is not necessary to very big power of agitator.It can not only powder is easily mixed, and save.
With reference to shown in figure 1,2,3, solid-liquid mixing module 3, include stainless steel 31 and in stainless steel 31, make
Liquid to be mixed is mixed with powder to be mixed and carries out atwirl agitator 32.
Stainless steel 31, it includes vertical component 311 and horizontal component 312, and horizontal component 312 is located at vertical component 311
Bottom, and vertical component 311 and horizontal component 312 are integrally formed, and the upper surface of vertical component 311 corresponds to powder dispersing chamber 11
At positioning hole 112, provided with corresponding positioning hole 313, positioning hole 112 is configured to counterbore with positioning hole 313.That is stainless steel 31
Vertical component 311, partially overlapped with the gear wall of powder dispersing chamber 11 below 111, therefore, in the appearance of powder dispersing chamber 11
Face, the inner surface with the vertical component 311 of stainless steel 31, form narrow annular channel 23.Horizontal component 312 is configured to annular shape,
It is provided with positioning hole 314 close to circumferential position.
In the present embodiment, agitator 32, it includes the vessel 321 of both ends open and located at vessel 321
The transverse slat 322 at middle part, the surface of vessel 321 are provided with small opening 323, and transverse slat 322 is provided with groove 324.The center of transverse slat 322 is provided with
Axle center hole 325.
With reference to shown in figure 1,2,3, liquid dispersion module 2, it is entered by multiple pumps 21 and the liquid being correspondingly arranged with pump 21
Expects pipe 22, liquid is delivered in narrow annular channel 23, after making liquid by narrow annular channel 23, vertically downward.Liquid feed pipe 22,
It is arranged on the vertical component 311 of stainless steel 31, and vertical component 311 at liquid feed pipe 22 to that should be provided with charging aperture；
By the setting of pump 21, to fluid pressure to be mixed, pressure to be mixed can be made downward with certain acceleration, it is preferable that can be with
The linear velocity of 1-2 rice per second is to bottom offset.
With reference to shown in figure 1,2,3, module 4 is discharged, it includes discharge container 41 and the scattered leaf in discharge container
Wheel 42, the side wall of discharge container 41 are provided with discharge line 43, and discharge line 43 is provided with the pump 44 of regulation discharge flow rate of slurry.
Discharge container 41 is configured to U-shaped structure, and the position that its upper surface corresponds to positioning hole 314 also is provided with positioning hole 411, fixed
Position hole 314 is configured to counterbore with positioning hole 411.
With reference to shown in figure 7, dispersion impeller 42, it includes disc body 421 and is respectively arranged on disc body upper and lower surface,
The blade 422,423 vertical with the upper and lower surface of disc body 421.The center of dispersion impeller 42 is provided with axle center hole 424.
During implementation, after liquid to be mixed mixes with powder to be mixed in mixing module 3, the slurry of formation falls into discharge mould
Block 4, in module 4 is discharged, by dispersion impeller 42, after further being sufficiently mixed it, discharged through discharge line 43, it is arranged
Go out the flow velocity of slurry, determined by pump 44.
By the technical program, after its elder generation tentatively breaks up powder to be mixed, with specific inclination angle and liquid to be mixed
Body contacts, and carries out preliminary quick moistening, and in powder dispersed modules 1, it uses screw feed, without Valve controlling, has more
Strong mixing power.Meanwhile in mixing module 3, quick rotation agitator 32, accelerate the moistening process of powder and liquid, finally
In module 4 is discharged, the impeller 42 for carrying out discharge opeing produces vacuum, can discharge highly viscous slurry, while produce vacuum.
Embodiment two：
The utility model, also discloses a kind of mixed method using above-mentioned solid-liquid mixing device, and it includes following step
Suddenly：
Step 1, first by liquid to be mixed, by liquid distribution module 2, it is delivered to mixing module 3；
Liquid to be mixed, is the collective effect for first passing through pump 21 and liquid feed pipe 22, and liquid is delivered into narrow annular channel
In 23, so that after liquid is by narrow annular channel 23, with certain acceleration vertically downward.The size of this acceleration, depending on pump
21 pressure for treating mixing liquid inputted.
In the specific implementation, the total cross-sectional area of liquid feed pipe 22 is greater than the area of passage equal to narrow annular channel 23.
Step 2, powder to be mixed, after disperseing and/or crush by described powder dispersed modules, with certain inclination
Angle is collided with liquid to be mixed vertically downward, powder is tentatively moistened；
Step 3, the powder tentatively moistened are mixed into solid-liquid mixing module together with liquid to be mixed and carried out fast
Speed rotation, it is rear to enter described discharge module；
Step 4, the slurry that preliminary mixed solid-liquid mixes are discharged after further disperseing wherein.
By adjusting the pump on discharge line, the velocity of discharge of slurry is set to be greater than equal to liquid to be mixed in step 1
Charging rate.To avoid slurry from overstocking in a reservoir.
In use, by power set, band moving axis 5 rotates, and axle 5 is through whole device, so as to drive powder to disperse mould
1 helicon of block impacts module 12 and powder discharge structure 13 is rotated, the agitator of solid-liquid mixing module 3 32 is rotated, arranged
The dispersion impeller 42 for going out module 4 rotates.
Embodiment three：
With reference to shown in figure 8,9,10, it is the structural representation of the utility model embodiment three；Its compared with embodiment one,
Difference is：
The ˊ of agitator 32 in the present embodiment, it includes the ˊ of agitator body 321 and sets the blade 326 of body circumference.Leaf
Piece 326 is uprightly arranged on the ˊ of agitator body 321 circumference.The ˊ centers of agitator body 321 are provided with the ˊ of axle center hole 325.
Example IV：
With reference to shown in figure 11,12,13, it is the structural representation of the utility model embodiment four；Itself and embodiment three-phase
Than difference is：
Blade 326 is obliquely installed on the ˊ of agitator body 321 circumference.
Embodiment five：
With reference to shown in figure 14, compared with embodiment one, difference is for it：
Powder dispersed modules 1, it includes the vacant room 11 of powder and the taper being located therein impact module 14, taper impact mould
Block 14 includes conical body 141, and the surface of conical body 141 is provided with hard alloy coating or ceramic coating, conical body 141
It is provided with groove 142.The setting of groove 142, it can prevent powder from sliding, the setting of hard alloy coating or ceramic coating can
Preferably powder is disperseed.The center of conical body 141 is provided with axle center hole 143.
Embodiment six：
With reference to shown in figure 15, compared with embodiment one, difference is for it：
Powder dispersed modules 1, its rod pin impact module 15 for including powder dispersing chamber 11 and being located therein, the punching of rod pin
Hit module 15 and include conical body 151 and one group of stirring rod 152 located at the surface of conical body 151.By stirring rod 152,
Powder preferably can be disperseed.
Embodiment seven：
With reference to shown in figure 16, compared with embodiment one, difference is for it：
Powder dispersed modules 1, its wing formula impact module 16 for including powder dispersing chamber 11 and being located therein, wing formula impact mould
Block 16 includes conical body 161 and one group of impact component 162 located at the surface of conical body 161, and impact component 162 includes one
Connecting rod 1621 and impact block 1622, the one end of connecting rod 1621 are connected with the surface of conical body 161, the other end and impact block 1622
It is connected.By increasing contact area, reaching makes the finely dispersed effect of powder.
Embodiment eight：
With reference to shown in figure 17,17C, compared with embodiment one, difference is for it：
The ˊ of dispersion impeller 42, it is configured to flabellum shape, its include the ˊ of center contiguous block 421 and with the ˊ of contiguous block 421 one into
The ˊ of fan blades 422 of shape, the ˊ of fan blades 422 are provided with two ˊ of side 4221 and 4222 ˊ, and in the present embodiment, both sides are equal up and down by its side 4221 ˊ
Provided with stirring bar 425,426.
It is described above, the only preferable embodiment of the utility model, but the scope of protection of the utility model is not
This is confined to, any one skilled in the art can readily occur in the technical scope that the utility model discloses
Change or replacement, should all cover within the scope of protection of the utility model.Therefore, the scope of protection of the utility model should
It is defined by scope of the claims.
Claims (20)
- A kind of 1. solid-liquid mixing device, it is characterised in that：It includes liquid distribution module, powder dispersed modules, solid-liquid mixing Module and discharge module, described liquid distribution module, liquid to be mixed is delivered to described mixing module by it, described Powder dispersed modules, it is used for after powder to be mixed is disperseed and/or crushed, into solid-liquid mixing module；It is to be mixed Liquid is mixed in described solid-liquid mixing module with powder to be mixed and quickly rotated, then by described discharge Module is discharged.
- 2. solid-liquid mixing device as claimed in claim 1, it is characterised in that：Described liquid distribution module, it passes through one Or multiple pumps and with the liquid feed pipe that pump is correspondingly arranged, liquid is delivered in narrow annular channel, liquid is passed through narrow annular channel Afterwards, vertically downward.
- 3. solid-liquid mixing device as claimed in claim 1, it is characterised in that：Described powder dispersed modules, it is impact type Powder disperses reducing mechanism.
- 4. solid-liquid mixing device as claimed in claim 3, it is characterised in that：Described powder dispersed modules, it includes powder Dispersing chamber and the helicon impact module being located therein, described helicon impact module include conical body and setting On conical body surface, the upward cutting sheet of spiral.
- 5. solid-liquid mixing device as claimed in claim 3, it is characterised in that：Described powder dispersed modules, it includes powder Dispersing chamber and the taper impact module being located therein, described taper impact module include conical body, described taper sheet Body surface face is provided with hard alloy coating or ceramic coating, and described conical body is provided with groove.
- 6. solid-liquid mixing device as claimed in claim 3, it is characterised in that：Described powder dispersed modules, it includes powder Dispersing chamber and the rod pin impact module being located therein, described rod pin impact module include conical body and located at taper One group of stirring rod of body surface.
- 7. solid-liquid mixing device as claimed in claim 3, it is characterised in that：Described powder dispersed modules, it includes powder Dispersing chamber and the wing formula impact module being located therein, described wing formula impact module include conical body and located at conical body One group of impact component on surface, described impact component include a connecting rod and impact block, described connecting rod one end with it is described Conical body surface be connected, the other end is connected with impact block.
- 8. the solid-liquid mixing device as described in claim 1-7 is any, it is characterised in that：Described powder dispersed modules, also enter One step includes making powder with certain angle of inclination and liquid making contact vertically downward, the powder for making powder tentatively moisten Discharge structure.
- 9. solid-liquid mixing device as claimed in claim 8, it is characterised in that：Described powder discharge structure, it is located at described Powder it is scattered between reducing mechanism and mixing module, it is configured to be a disc-shaped component, and circumference offers grooving.
- 10. solid-liquid mixing device as claimed in claim 9, it is characterised in that：At least one side wall of described grooving is with respect to disk Body centerline dip.
- 11. the solid-liquid mixing device as described in claim 1 or 4, it is characterised in that：Described solid-liquid mixing module, it includes There is stainless steel and in stainless steel, liquid to be mixed is mixed and is carried out atwirl with powder to be mixed Agitator.
- 12. solid-liquid mixing device as claimed in claim 11, it is characterised in that：Described powder disperse outdoor face with it is described Stainless steel inner surface formed narrow annular channel.
- 13. solid-liquid mixing device as claimed in claim 11, it is characterised in that：Described agitator, it includes agitator Body and the blade for setting body circumference.
- 14. solid-liquid mixing device as claimed in claim 13, it is characterised in that：Described upright blade is arranged at described sheet On body circumference.
- 15. solid-liquid mixing device as claimed in claim 13, it is characterised in that：Described blade lean is arranged at described sheet On body circumference.
- 16. solid-liquid mixing device as claimed in claim 11, it is characterised in that：Described agitator, it includes both ends and opened The container and the transverse slat in the middle part of container, described vessel surface of mouth are provided with small opening, and described transverse slat is provided with groove.
- 17. solid-liquid mixing device as claimed in claim 1, it is characterised in that：Described discharge module, it includes discharge and held Device and the dispersion impeller in discharge container, described discharge container side wall are provided with discharge line.
- 18. solid-liquid mixing device as claimed in claim 17, it is characterised in that：Described discharge line is provided with regulation and discharged The pump of flow rate of slurry.
- 19. solid-liquid mixing device as claimed in claim 18, it is characterised in that：Described dispersion impeller, it includes disk sheet Body and disc body upper and lower surface is respectively arranged on, the blade vertical with described disk upper and lower surface.
- 20. solid-liquid mixing device as claimed in claim 18, it is characterised in that：Described dispersion impeller, it is configured to flabellum Shape, it includes center contiguous block and the fan blades integrally formed with contiguous block, and at least one side of described fan blades, upper and lower both sides are extremely Few side is provided with stirring bar.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720911409.8U CN207203871U (en) | 2017-07-25 | 2017-07-25 | A kind of solid-liquid mixing device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201720911409.8U CN207203871U (en) | 2017-07-25 | 2017-07-25 | A kind of solid-liquid mixing device |
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| CN207203871U true CN207203871U (en) | 2018-04-10 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108393008A (en) * | 2018-04-26 | 2018-08-14 | 无锡先导智能装备股份有限公司 | Rabbling mechanism and pulping device |
| CN108465388A (en) * | 2017-07-25 | 2018-08-31 | 深圳市尚水智能设备有限公司 | A kind of solid-liquid mixing device and the mixed method using the equipment |
| WO2024008095A1 (en) * | 2022-07-05 | 2024-01-11 | 宁德时代新能源科技股份有限公司 | Slurry preparation device and solid-liquid mixing apparatus |
-
2017
- 2017-07-25 CN CN201720911409.8U patent/CN207203871U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108465388A (en) * | 2017-07-25 | 2018-08-31 | 深圳市尚水智能设备有限公司 | A kind of solid-liquid mixing device and the mixed method using the equipment |
| CN108393008A (en) * | 2018-04-26 | 2018-08-14 | 无锡先导智能装备股份有限公司 | Rabbling mechanism and pulping device |
| WO2024008095A1 (en) * | 2022-07-05 | 2024-01-11 | 宁德时代新能源科技股份有限公司 | Slurry preparation device and solid-liquid mixing apparatus |
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Address after: 518118 Pingzhi main plant 201, Huakong SEG plant, No. 6, Lanzhu East Road, Zhukeng community, Longtian street, Pingshan District, Shenzhen, Guangdong Patentee after: Shenzhen Shangshui Intelligent Co.,Ltd. Address before: 518000 Room 101, building 5, No.3 Industrial Zone, Kwai Chung office, Dapeng New District, Shenzhen City, Guangdong Province Patentee before: SHENZHEN SHANGSHUI INTELLIGENT EQUIPMENT Co.,Ltd. |
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