CN205461949U - Thick liquids mixing equipment - Google Patents
Thick liquids mixing equipment Download PDFInfo
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- CN205461949U CN205461949U CN201521108707.0U CN201521108707U CN205461949U CN 205461949 U CN205461949 U CN 205461949U CN 201521108707 U CN201521108707 U CN 201521108707U CN 205461949 U CN205461949 U CN 205461949U
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- uniform mixing
- feeding pipe
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Abstract
The utility model discloses a thick liquids mixing equipment belongs to the mixed technical field of material. It includes premixing device, blend device, mixes thick liquids feeding pipe, transition pipeline, backward flow feeding pipe, blend thick liquids feeding pipe, the pipeline of unloading, agitating unit in advance, mixes feeding pipe in advance through mixing slurry feed port and premixing device intercommunication in advance, the transition pipeline is used for communicateing mixing arrangement and blend device in advance, backward flow feeding pipe's one end is drawn forth from the transition pipeline, backward flow feeding pipe's the other end and premixing device intercommunication, blend thick liquids feeding pipe loads in mixture together through blend slurry feed port and puts the intercommunication, the discharge tube sweetgum fruit is crossed the discharge opening and is unloaded from the blend device, agitating unit is arranged in the stirring to be in the blend thick liquids of blend device. It can increase the mixing uniformity who preblends thick liquids, and then, after preblending thick liquids follow transition pipeline entering blend device, can mix through the stirring with the thick liquids that are in in the blend device for the uniformity of the blend thick liquids that obtain is better.
Description
Technical field
This utility model relates to material hybrid technology field, and particularly relating to one can be to power battery electrode
Slurry carries out the slurry uniform mixing equipment mixed.
Background technology
Lithium ion battery, as the important chemical cell of a class, has high voltage, high specific energy, discharge and recharge life-span long
Deng many advantages.Under the background that global energy and environmental problem become increasingly conspicuous, the application of lithium ion battery
Also by mobile phone, notebook computer, etc. small portable electrical equipment progressively to electric automobile field develop.Along with power
The fast development of lithium electricity industry, the requirement for performance of lithium ion battery and large-scale production is more and more higher.Even
Slurry process is as an important step in lithium electricity production technology, for follow-up coating quality or even whole battery
Concordance have significant impact.
In lithium battery production technology in the early stage, homogenization process is by entire solid matters i.e. active substance, conduction
Agent and binding agent add together with solvent homogenate tank in be stirred mixing, in this method solvent can be once or
Repeatedly add.In evolution subsequently, there is people that glue process is individually separated the work becoming independent
Sequence, other solid matter and solvent are blended in homogenate tank, once or be dividedly in some parts produced adhesive, as
CN101683594, CN103618063A disclosure of that.But positive and negative pole material active substance, conduction
Agent, binding agent and solvent composition molecular diffusion rate are relatively slow, only by the mode of mechanical mixture, and dividing of solid matter
Scattered effect is the most not ideal, directly affects the concordance of slurry.
Utility model content
In view of this, this utility model provides a kind of slurry uniform mixing equipment, its by pre-mixing apparatus and be blended and
The combination of device, it is possible to make Blending Efficiency of Blending more preferable, thus more suitable for practicality.
The slurry uniform mixing equipment that this utility model provides includes pre-mixing apparatus, intermingling apparatus, premix slurry feed pipe
Road, transition pipe, reflux entry pipeline, blended slurry feeding pipe, discharge pipelines, agitating device,
Described pre-mixed feeds pipeline is connected with described pre-mixing apparatus by premix slurry charging aperture；
Described transition pipe is used for connecting described pre-mixing apparatus and described intermingling apparatus；
One end of described reflux entry pipeline is drawn from described transition pipe, described reflux entry pipeline another
One end connects with described pre-mixing apparatus；
Described blended slurry charging aperture is connected with described intermingling apparatus by described blended slurry charging aperture；
Described discharge pipelines passes through discharge port from described intermingling apparatus discharging；
The blended slurry that described agitating device is in described intermingling apparatus for stirring.
As preferably, described premix slurry feeding pipe is multiple.
As preferably, the span of the angle between described premix slurry feeding pipe and horizontal plane is-
45 °～75 °.
As preferably, the span of the angle between described premix slurry feeding pipe and horizontal plane be 0 °～
60°。
As preferably, described slurry uniform mixing equipment also includes premixing slurry feed pump, described premix slurry feed pump
For slurry to be mixed is pumped into described pre-mixing apparatus.
As preferably, what described transition pipe was arranged at described premix slurry feeding pipe vertically divides equally on face.
As preferably, described slurry uniform mixing equipment also includes microchannel, described microchannel in described pre-mixing apparatus,
Arrange along premix pulp flow direction.
As preferably, the span of described microchannel quantity is 1～16.
As preferably, the span of the hydraulic diameter of described microchannel is 0.5mm～10mm.
As preferably, the shape selected from circles of the cross section of described microchannel, rectangle, and/or, trapezoidal, and/
Or, triangle.
As preferably, described microchannel includes straight channel, and/or, bending channel.
As preferably, described microchannel includes straight channel, and, bending channel, described straight channel and bending channel
Interval is arranged.
As preferably, the span of the length of single described microchannel is 1cm～50cm.
As preferably, the agitator arm of described agitating device is in planetary, anchor formula, frame, helical-ribbon type
A kind of.
As preferably, the span of the rotating speed of described agitating device is 10rpm～1000rpm.
As preferably, if the agitator arm of described agitating device is dried layer.
As preferably, described slurry uniform mixing equipment also includes that deflector, described deflector are arranged at described common
In mixing device, described deflector is for carrying out water conservancy diversion for described blended slurry.
As preferably, described slurry uniform mixing equipment also includes that baffle plate, described baffle plate are also disposed on described intermingling apparatus
In, described baffle plate is used for stoping described blended slurry to overflow described intermingling apparatus.
As preferably, described slurry uniform mixing equipment also includes batch (-type) valve, and described batch (-type) valve will be for treating
Mixed slurry is intermittently introduced in described pre-mixing apparatus.
As preferably, the span at the intermittent time interval of described batch (-type) valve is 0.5h～2h.
As preferably, described slurry uniform mixing equipment also includes chiller, and described chiller is for described common
Slurry material cools down.
As preferably, described chiller is circulating water cooling device.
As preferably, the span of the temperature of described recirculated water is 15 DEG C～30 DEG C.
As preferably, the span of the flow velocity of described recirculated water is 1mL/min～20mL/min.
As preferably, described slurry uniform mixing equipment is used for mixing power cell electrode slurry,
Described premix slurry feeding pipe includes the first feeding pipe, the second feeding pipe,
Described first feeding pipe is described for being delivered to by the first slurry being made up of adhesive particle and solvent
Pre-mixing apparatus；
Described second feeding pipe is for being delivered to institute by the second slurry being made up of solid conductive material and solvent
State pre-mixing apparatus；
Described pre-mixing apparatus, for mixing described first slurry and described second slurry, obtains premixing
Slurry；
Described transition pipe is for being delivered to described intermingling apparatus by described premixed slurries；
Described reflux entry pipeline is for refluxing the part in described premixed slurries from described transition pipe
To described pre-mixing apparatus；
Described blended slurry feeding pipe for being delivered to described intermingling apparatus by electrode active material；
Described intermingling apparatus, for mixing described premixed slurries, electrode active material, obtains mixing
Power cell electrode slurry；
Described discharge pipelines is used for drawing the power cell electrode slurry of described mixing from described intermingling apparatus,
Standby.
The slurry uniform mixing equipment that this utility model provides first passes through pre-mixing apparatus, to respectively from described pre-slurry
The slurry that material feeding pipe enters mixes, and obtains premixed slurries, and premixed slurries passes through transition pipe quilt
Being guided in the road of intermingling apparatus, some premixed slurries is introduced again into by reflux entry pipeline
To pre-mixing apparatus, in pre-mixing apparatus, this premixed slurries mixes with the slurry being in pre-mixing apparatus again
Close, so move in circles, it is possible to the slurry entered from premix slurry feeding pipe is mixed pre-mixing apparatus
More abundant, thus increase the mixing uniformity of premixed slurries.And then, when premixed slurries is from transition pipe
After entering intermingling apparatus, it is possible to after being mixed by stirring with the slurry being in intermingling apparatus, it is possible to make
The concordance of the blended slurry obtained is more preferable.
Accompanying drawing explanation
By reading the detailed description of hereafter preferred implementation, various other advantage and benefit for ability
Territory those of ordinary skill will be clear from understanding.Accompanying drawing is only used for illustrating the purpose of preferred implementation, and not
It is considered restriction of the present utility model.And in whole accompanying drawing, it is denoted by the same reference numerals identical
Parts.In the accompanying drawings:
Fig. 1 is used for mixing power battery electrode slurry for the slurry uniform mixing equipment that this utility model embodiment provides
Concrete structure schematic diagram when material mixes；
Fig. 2 is used for mixing power battery electrode slurry for the slurry uniform mixing equipment that this utility model embodiment provides
Material is when mixing, the first feeding pipe, position relationship schematic diagram between the second feeding pipe and pre-mixing apparatus.
Detailed description of the invention
This utility model is to solve the problem that prior art exists, it is provided that a kind of slurry uniform mixing equipment, and it is by pre-
The combination of mixing arrangement and altogether mixing apparatus, it is possible to make Blending Efficiency of Blending more preferable, thus more suitable for practicality.
By further illustrate technological means that this utility model taked by reaching predetermined utility model purpose and
Effect, below in conjunction with accompanying drawing and preferred embodiment, to according to the slurry uniform mixing equipment that the utility model proposes, its
Detailed description of the invention, structure, feature and effect thereof, after describing in detail such as.In the following description, different " one
Embodiment " or " embodiment " refer to be not necessarily same embodiment.Additionally, specific in one or more embodiment
Feature, structure or feature can be combined by any suitable form.
The terms "and/or", a kind of incidence relation describing affiliated partner, expression can exist
Three kinds of relations, such as, A and/or B, concrete is interpreted as: can include A and B, Ke Yidan simultaneously
Solely there is A, it is also possible to individualism B, it is possible to possess above-mentioned three kinds of any one situations.
This utility model embodiment only selects concrete structure when mixing mixing power cell electrode slurry
Illustrate, in practice, it is also possible to the slurry uniform mixing equipment provided this utility model according to demand is carried out specifically
, adaptive application.
Embodiment
Seeing accompanying drawing 1 and accompanying drawing 2, the slurry uniform mixing equipment that this utility model provides includes pre-mixing apparatus 1, is total to
(in the present embodiment, premix slurry feeding pipe includes the first charging for mixing device 12, premix slurry feeding pipe
Pipeline 2 and the second feeding pipe 3), transition pipe 5, reflux entry pipeline 7, be blended slurry feeding pipe
16, discharge pipelines 18, agitating device 13.Pre-mixed feeds pipeline (in the present embodiment, premixes slurry feed pipe
Road includes the first feeding pipe 2 and the second feeding pipe 3) by premix slurry charging aperture (in the present embodiment,
It is the first charging aperture 8 and the second charging aperture 9) connect with pre-mixing apparatus 1；Transition pipe 5 is used for connecting premix
Locking device 1 and intermingling apparatus 12；One end 6 of reflux entry pipeline 7 is drawn from transition pipe 5, backflow
The other end 10 of feeding pipe 7 connects with pre-mixing apparatus 1；Slurry feeding pipe 16 is blended by slurry is blended
Material charging aperture 15 connects with intermingling apparatus 12；Discharge pipelines 18 is unloaded from intermingling apparatus 12 by discharge port 17
Material；The blended slurry that agitating device 13 is in intermingling apparatus 12 for stirring.
The slurry uniform mixing equipment that this utility model embodiment provides first passes through pre-mixing apparatus 1, to respectively from premix
(in the present embodiment, premix slurry feeding pipe includes that the first feeding pipe 2 and second enters to slurry feeding pipe
Material pipeline 3) slurry that enters mixes, and obtains premixed slurries, and premixed slurries passes through transition pipe 5
Being guided in the road of intermingling apparatus 12, some premixed slurries passes through reflux entry pipeline 7 by again
Secondary be introduced to pre-mixing apparatus 1, in pre-mixing apparatus 1, this premixed slurries again be in pre-mixing apparatus 1
Slurry mix, so move in circles, it is possible to make from premix slurry feeding pipe (the present embodiment,
Premix slurry feeding pipe includes the first feeding pipe 2 and the second feeding pipe 3) slurry that enters loading in mixture in advance
Put in 1 and be more fully mixed, thus increase the mixing uniformity of premixed slurries.And then, work as premixed slurries
From transition pipe, (the present embodiment, premix slurry feeding pipe includes the first feeding pipe 2 and the second charging
Pipeline 3) enter after intermingling apparatus 12, it is possible to mixed by stirring with the slurry being in intermingling apparatus 12
After conjunction, it is possible to make the concordance of blended slurry obtained more preferable.
Wherein, premix slurry feeding pipe is multiple.Thus, by multiple premix slurry feeding pipes, it is possible to
Multiple slurry is mixed.
Wherein, the span of the angle between premix slurry feeding pipe and horizontal plane is-45 °～75 °.
In the present embodiment, premix slurry feeding pipe includes the first feeding pipe 2 and the second feeding pipe 3, is converted to
Angle α between them, then the span of angle α is 30 °～270 °.In this case, it is possible to
Slurry to be mixed is entered in pre-mixing apparatus 1 more easily.
Wherein, the span of the angle between premix slurry feeding pipe and horizontal plane is 0 °～60 °.This
In embodiment, premix slurry feeding pipe includes the first feeding pipe 2 and the second feeding pipe 3, is converted to him
Angle α between, then the span of angle α is 60 °～180 °.In this case, first enters
The inclination angle of material pipeline 2 and the second feeding pipe 3 is respectively the angle of depression, and a component of slurry gravity to be mixed is firm
Good identical with the direction of the first feeding pipe 2 and the second feeding pipe 3, therefore, it is possible to accelerate slurry to be mixed
Material enters the charging rate of pre-mixing apparatus 1.
Wherein, in the present embodiment, slurry uniform mixing equipment also includes premixing slurry feed pump (not shown),
Premix slurry feed pump (not shown) is for pumping into pre-mixing apparatus 1 by slurry to be mixed, when the first charging
The inclination angle of pipeline 2 and the second feeding pipe 3 is the elevation angle, or, when the first feeding pipe 2 and the second charging
Pipeline 3 be the angle of depression and angle less time, affected by slurry gravity to be mixed, it cannot enter into voluntarily
In pre-mixing apparatus 1, in this case, it is necessary to will treat by premix slurry feed pump (not shown)
Mixed slurry is incorporated in pre-mixing apparatus 1.
Wherein, transition pipe 1 is arranged at premix slurry feeding pipe and (in the present embodiment, premixes slurry feed pipe
Road includes the first feeding pipe 2 and the second feeding pipe 3) vertically divide equally on face.Thus so that it is in pre-
Premixed slurries in mixing device 1 is when entering transition pipe 5, and flow velocity is more stable.
Wherein, in the present embodiment, slurry uniform mixing equipment also includes microchannel (not shown), microchannel (figure
Not shown in) in pre-mixing apparatus 1, arrange along premix pulp flow direction.In this case, premixing
Slurry is in flow process, and can produce frictional force between the (not shown) wall of microchannel, thus, make
The mixing efficiency obtaining premixed slurries is higher.In the present embodiment, the value of microchannel (not shown) quantity
Scope is 1～16；The span of the hydraulic diameter of microchannel (not shown) is 0.5mm～10mm；
The shape selected from circles of the cross section of microchannel (not shown), rectangle, and/or, trapezoidal, and/or,
Triangle.Wherein, when cross section generally circular in shape, isotropism, it is possible to make the mixed of premixed slurries
Close efficiency to improve further.
Wherein, microchannel (not shown) includes straight channel, and/or, bending channel.Wherein, when micro-logical
When road (not shown) is bending channel, it is possible to extend the slurry to be mixed operation road in pre-mixing apparatus 1
Footpath, thus, it is also possible to improve the mixing efficiency of premixed slurries.
Wherein, microchannel (not shown) includes straight channel, and, bending channel, straight channel is logical with bending
Interval, road is arranged.In this case, through to ensure that the current speed of slurry to be mixed, bending channel
The mixing efficiency of premixed slurries can be improved.
Wherein, the span of the length of single microchannel (not shown) is 1cm～50cm.Single
The length of microchannel is the longest, and mixed effect is the best, and length is the shortest, and the current speed of mixed slurry is bigger.
In the present embodiment, the agitator arm 14 of agitating device 13 is selected from planetary, anchor formula, frame, helical-ribbon type
In one, the span of the rotating speed of agitating device 13 is 10rpm～1000rpm.
Wherein, if the agitator arm of agitating device is dried layer.If when the agitator arm of agitating device is dried layer,
The mixed effect of the blended slurry being in intermingling apparatus 12 can be improved.
In the present embodiment, slurry uniform mixing equipment also includes deflector (not shown), deflector (figure
Not shown in) be arranged in intermingling apparatus 12, deflector (not shown) is for entering for blended slurry
Row water conservancy diversion.Thus avoid that slurry is blended and be detained in intermingling apparatus 12.
In the present embodiment, slurry uniform mixing equipment also includes baffle plate (not shown), baffle plate (not shown)
Being also disposed in intermingling apparatus 12, baffle plate (not shown) is used for stoping blended slurry to overflow intermingling apparatus
12.When the agitator arm 14 of agitating device 13 is in and runs up, in intermingling apparatus 12, can be formed
Eddy current, this eddy current makes the apparent liquid level that slurry is blended raise, after setting up this baffle plate (not shown),
It can be avoided that the blended slurry after liquid level raises overflows from intermingling apparatus 12, cause slurry loss and environment dirty
Dye.
Wherein, in the present embodiment, slurry uniform mixing equipment also includes batch (-type) valve (not shown), intermittently
Formula valve (not shown) is for being intermittently introduced to slurry to be mixed in pre-mixing apparatus.By this batch (-type)
Valve (not shown), it is possible to make slurry to be mixed enter in pre-mixing apparatus 1 in batches so that with
The amount of the premix slurry being in one time in pre-mixing apparatus 1 is less, thus ensures to premix the mixing effect of slurry
Really.In the present embodiment, the span at intermittent time of batch (-type) valve (not shown) interval be 0.5h～
2h。
Wherein, in the present embodiment, slurry uniform mixing equipment also includes chiller (not shown), cooling dress
Put (not shown) for blended slurry is cooled down.Thus, it is to avoid slurry is blended at intermingling apparatus 12
In with agitator arm 14 high-speed friction after the heat that produces produce too much, and affect the reality of slurry is blended should
Use effect.In the present embodiment, chiller is circulating water cooling device, and circulating water cooling device is with low cost,
It is easily achieved.In the present embodiment, the span of the temperature of recirculated water is 15 DEG C～30 DEG C, thus so that
The temperature of the blended slurry being in intermingling apparatus 12 is constantly in close to 15 DEG C～the state of 30 DEG C, it is ensured that altogether
The practical application effect of slurry material.In the present embodiment, the span of the flow velocity of recirculated water is 1mL/min～20
ML/min, in this case, can either ensure cooling effect, also be unlikely to so that the pressure in chiller
Power is excessive, thus ensures the application security of the slurry uniform mixing equipment that the present embodiment provides.
When the embodiment of the present invention provides slurry uniform mixing equipment to be used for mixing power cell electrode slurry, pre-slurry
Material feeding pipe includes first feeding pipe the 2, second feeding pipe 3, and the first feeding pipe 2 is used for will be by gluing
First slurry of knot agent granule and solvent composition is delivered to pre-mixing apparatus 1；Second feeding pipe 3 is used for will be by solid
Second slurry of body conductive material and solvent composition is delivered to pre-mixing apparatus 1；Pre-mixing apparatus 1 is for the first slurry
Material and the second slurry mix, and obtain premixed slurries；Transition pipe 5 is for carrying premixed slurries
To intermingling apparatus 12；Reflux entry pipeline 7 for by the part in premixed slurries from transition pipe 5 times
It flow to pre-mixing apparatus 1；Slurry feeding pipe 16 is blended for electrode active material being delivered to intermingling apparatus 12；
Intermingling apparatus 12, for mixing premixed slurries, electrode active material, obtains the electrokinetic cell of mixing
Electrode slurry；Discharge pipelines 18 is used for drawing the power cell electrode slurry of mixing from intermingling apparatus 12,
Standby.
In prior art, in the technology mixing power cell electrode slurry, whole flow process is all at machine
Complete under tool stirring condition, and both positive and negative polarity active material, conductive agent and binding agent many kinds of substance are blended with batch
In the case of, to first realize the dispersed and then uniform with binding agent and solvent of active material and conductive agent
Hybrid extremely difficult, therefore, prior art is for the technology that mixes power cell electrode slurry also
It it is the root place affecting sizing agent consistency.It is used for the equipment that this utility model provides mixing electrokinetic cell electricity
During the slurry of pole, it is possible to the mixed effect of kind slurry and the duration of shortening homogenate technique, improve production efficiency.
Although having been described for preferred embodiment of the present utility model, but those skilled in the art once learning
Basic creative concept, then can make other change and amendment to these embodiments.So, appended right
Require to be intended to be construed to include preferred embodiment and fall into all changes and the amendment of this utility model scope.
Obviously, those skilled in the art this utility model can be carried out various change and modification without deviating from
Spirit and scope of the present utility model.So, if these amendments of the present utility model and modification belong to this practicality
Within the scope of novel claim and equivalent technologies thereof, then this utility model be also intended to comprise these change and
Including modification.
Claims (24)
1. a slurry uniform mixing equipment, it is characterised in that include pre-mixing apparatus, intermingling apparatus, premix slurry feeding pipe, transition pipe, reflux entry pipeline, slurry feeding pipe, discharge pipelines, agitating device are blended,
Described pre-mixed feeds pipeline is connected with described pre-mixing apparatus by premix slurry charging aperture；
Described transition pipe is used for connecting described pre-mixing apparatus and described intermingling apparatus；
One end of described reflux entry pipeline is drawn from described transition pipe, and the other end of described reflux entry pipeline connects with described pre-mixing apparatus；
Described blended slurry feeding pipe is connected with described intermingling apparatus by described blended slurry charging aperture；
Described discharge pipelines passes through discharge port from described intermingling apparatus discharging；
The blended slurry that described agitating device is in described intermingling apparatus for stirring.
Slurry uniform mixing equipment the most according to claim 1, it is characterised in that described premix slurry feeding pipe is multiple.
Slurry uniform mixing equipment the most according to claim 2, it is characterised in that the span of the angle between described premix slurry feeding pipe and horizontal plane is-45 °～75 °.
Slurry uniform mixing equipment the most according to claim 3, it is characterised in that the span of the angle between described premix slurry feeding pipe and horizontal plane is 0 °～60 °.
Slurry uniform mixing equipment the most according to claim 1, it is characterised in that also including premixing slurry feed pump, described premix slurry feed pump is for pumping into described pre-mixing apparatus by slurry to be mixed.
Slurry uniform mixing equipment the most according to claim 1, it is characterised in that what described transition pipe was arranged at described premix slurry feeding pipe vertically divides equally on face.
Slurry uniform mixing equipment the most according to claim 1, it is characterised in that also include microchannel, described microchannel, in described pre-mixing apparatus, is arranged along premix pulp flow direction.
Slurry uniform mixing equipment the most according to claim 7, it is characterised in that the span of described microchannel quantity is 1～16.
Slurry uniform mixing equipment the most according to claim 7, it is characterised in that the span of the hydraulic diameter of described microchannel is 0.5mm～10mm.
Slurry uniform mixing equipment the most according to claim 7, it is characterised in that the shape selected from circles of the cross section of described microchannel, and/or, rectangle, and/or, trapezoidal, and/or, triangle.
11. slurry uniform mixing equipments according to claim 7, it is characterised in that described microchannel includes straight channel, and/or, bending channel.
12. slurry uniform mixing equipments according to claim 11, it is characterised in that described microchannel includes straight channel, and, bending channel, described straight channel and bending channel interval are arranged.
13. slurry uniform mixing equipments according to claim 7, it is characterised in that the span of the length of single described microchannel is 1cm～50cm.
14. slurry uniform mixing equipments according to claim 1, it is characterised in that the agitator arm of described agitating device one in planetary, anchor formula, frame, helical-ribbon type.
15. slurry uniform mixing equipments according to claim 1, it is characterised in that the span of the rotating speed of described agitating device is 10rpm～1000rpm.
16. slurry uniform mixing equipments according to claim 14, it is characterised in that if the agitator arm of described agitating device is dried layer.
17. slurry uniform mixing equipments according to claim 1, it is characterised in that also include that deflector, described deflector are arranged in described intermingling apparatus, described deflector is for carrying out water conservancy diversion for described blended slurry.
18. slurry uniform mixing equipments according to claim 1, it is characterised in that also include that baffle plate, described baffle plate are also disposed in described intermingling apparatus, described baffle plate is used for stoping described blended slurry to overflow described intermingling apparatus.
19. slurry uniform mixing equipments according to claim 1, it is characterised in that also include batch (-type) valve, described batch (-type) valve is for being intermittently introduced to slurry to be mixed in described pre-mixing apparatus.
20. slurry uniform mixing equipments according to claim 19, it is characterised in that the span at the intermittent time interval of described batch (-type) valve is 0.5h～2h.
21. slurry uniform mixing equipments according to claim 1, it is characterised in that also include chiller, described chiller is for cooling down described blended slurry.
22. slurry uniform mixing equipments according to claim 21, it is characterised in that described chiller is circulating water cooling device.
23. slurry uniform mixing equipments according to claim 22, it is characterised in that the span of the temperature of described recirculated water is 15 DEG C～30 DEG C.
24. slurry uniform mixing equipments according to claim 22, it is characterised in that the span of the flow velocity of described recirculated water is 1mL/min～20mL/min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521108707.0U CN205461949U (en) | 2015-12-28 | 2015-12-28 | Thick liquids mixing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521108707.0U CN205461949U (en) | 2015-12-28 | 2015-12-28 | Thick liquids mixing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205461949U true CN205461949U (en) | 2016-08-17 |
Family
ID=56661669
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521108707.0U Active CN205461949U (en) | 2015-12-28 | 2015-12-28 | Thick liquids mixing equipment |
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| Country | Link |
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| CN (1) | CN205461949U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715774A (en) * | 2017-07-06 | 2018-02-23 | 东莞市创明电池技术有限公司 | Lithium battery closes paste-making method and solid powder premixing device |
| CN111111590A (en) * | 2019-12-27 | 2020-05-08 | 苏州清陶新能源科技有限公司 | Method for stirring anode slurry |
-
2015
- 2015-12-28 CN CN201521108707.0U patent/CN205461949U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715774A (en) * | 2017-07-06 | 2018-02-23 | 东莞市创明电池技术有限公司 | Lithium battery closes paste-making method and solid powder premixing device |
| CN111111590A (en) * | 2019-12-27 | 2020-05-08 | 苏州清陶新能源科技有限公司 | Method for stirring anode slurry |
| CN111111590B (en) * | 2019-12-27 | 2022-04-22 | 苏州清陶新能源科技有限公司 | Method for stirring anode slurry |
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