CN207430206U - A kind of continuous dispersal device of pulp of lithium ion battery - Google Patents
A kind of continuous dispersal device of pulp of lithium ion battery Download PDFInfo
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- CN207430206U CN207430206U CN201721224134.7U CN201721224134U CN207430206U CN 207430206 U CN207430206 U CN 207430206U CN 201721224134 U CN201721224134 U CN 201721224134U CN 207430206 U CN207430206 U CN 207430206U
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Abstract
The utility model discloses a kind of continuous dispersal devices of pulp of lithium ion battery, it includes at least one powder substance holding vessel, at least at least one solvent holding vessel, the first decentralized institution of level-one and at least first-stage centrifugal decentralized institution, the bottom discharge mouth of each powder substance holding vessel and the bottom discharge mouth of each solvent holding vessel are connected by pipeline with the first decentralized institution of at least level-one, the discharge port connection at least first-stage centrifugal decentralized institution of the first decentralized institution of afterbody.The utility model launches powder substance and liquid substance respectively, and uses spray mode liquid delivery substance, by carrying out scattered and Centrifugal dispersion for the first time to material, can improve dispersion effect；By the way that first decentralized institution is arranged to three-level, Centrifugal dispersion mechanism is arranged to two-stage, it can be achieved that slurry is worked continuously, output slurry, improves dust dispersion quality and production efficiency incessantly.
Description
Technical field
The utility model belongs to pulp of lithium ion battery manufacturing technology field, and in particular to a kind of pulp of lithium ion battery
Continuous dispersal device.
Background technology
Lithium ion battery is a kind of environmentally protective high-energy rechargeable battery, in portable electric appts, electric vehicle, energy
The fields such as source deposit and national defense industry have a wide range of applications.The mixing of pulp of lithium ion battery disperses to be lithium-ion electric
Very important link in the entire production process in pond, the quality of slurry dust dispersion quality will directly influence follow-up lithium ion battery life
The performance of the quality of production and products thereof.With the continuous progress of lithium ion battery material, raw materials particles grain size is less and less, this
The performance of lithium ion battery is not only increased, is also easily created two level aggregate, so as to add mixing dispersing technology
Difficulty.In currently available technology, lithium ion battery plus-negative plate slurry agitation disperses mostly double-planet and is dispersed with stirring, and there is stirring
Scattered the shortcomings of taking longer, dispersion effect lack of homogeneity.
Utility model content
The purpose of this utility model is to provide a kind of continuous dispersal device of pulp of lithium ion battery, solves in the prior art
Double-planet is dispersed with stirring the problem of device dispersion effect is bad used by scattered pulp of lithium ion battery.
Technical solution is used by the utility model：A kind of continuous dispersal device of pulp of lithium ion battery, including
At least one powder substance holding vessel, at least at least one solvent holding vessel, the first decentralized institution of level-one and at least first-stage centrifugal
The bottom discharge mouth of decentralized institution, the bottom discharge mouth of each powder substance holding vessel and each solvent holding vessel passes through pipeline
It is connected with the first decentralized institution of at least level-one, the discharge port connection at least first-stage centrifugal of the first decentralized institution of afterbody is disperseed
Mechanism.
The utility model is also characterized by：
Lead to the pipe of the first decentralized institution in each powder substance holding vessel and each solvent holding vessel
Road is both provided with meter.
The first decentralized institution include for the first time scattered tank body, high speed disperser, the first driver, solvent spray thrower and
Screw extruding device；The upper end feed inlet and the bottom discharge mouth of each powder substance holding vessel of the first scattered tank body lead to
Cross pipeline connection；The high speed disperser is provided in the first dispersion tank body, first driver is arranged on described first
It the upper end of secondary scattered tank body and is connected by transmission shaft with the high speed disperser, the solvent spray thrower is arranged on described first
At lower end position, the bottom discharge mouth of the solvent spray thrower and each solvent holding vessel leads to the outer wall of scattered tank body
Cross pipeline connection；The screw extruding device is connected with the lower end discharge port of the first scattered tank body.
The meter includes the first level-one meter, the second level-one meter and two level meter, in each powder
Material matter holding vessel, which leads on the pipeline of the first scattered tank body in the first decentralized institution of the first order, is respectively provided with one for measuring
First level-one meter of each powder substance total amount；Solvent spray thrower in per level-one first decentralized institution with it is each described
The bottom discharge mouth of solvent holding vessel leads to the first decentralized institution by pipeline connection in each solvent holding vessel
One is respectively provided on main pipe rail for measuring the second level-one meter of each liquid substance total amount, the second level-one meter with
Be respectively provided with a two level meter on the pipeline between solvent spray thrower in per level-one first decentralized institution, be used to measuring into
Enter the liquids quality in the solvent spray thrower in the first decentralized institution of every level-one.
When the first decentralized institution sets more than two-stage, the screw extruding device in the first decentralized institution of afterbody is
Twin-screw extruder device.
The Centrifugal dispersion mechanism includes Centrifugal dispersion tank body, Centrifugal dispersion device, centrifugation crash panel, the first material scraper, the
Two drivers, the discharge port of the screw extruding device in first decentralized institution described in afterbody are upper with the Centrifugal dispersion tank body
Endfeed mouth connects, and is provided with the Centrifugal dispersion device in the Centrifugal dispersion tank body, and the centrifugation crash panel sets two, and two
A centrifugation crash panel is symmetricly set on two outsides of the Centrifugal dispersion device, and first material scraper is a pair of of inverted L shape structure,
It is symmetricly set between the Centrifugal dispersion device and the centrifugation crash panel and coordinates with centrifugation crash panel；Second driving
Device is connected by transmission shaft with the Centrifugal dispersion device and the first material scraper.
The lower end of the Centrifugal dispersion device is provided with the second material scraper, and second material scraper includes one end and the transmission
The crossbeam of axis connection and the Curved beam with Centrifugal dispersion inner tank wall cooperation, one end of the Curved beam and crossbeam it is another
One end connects.
The Centrifugal dispersion device is made of two different cylindrical tubes of diameter, wherein the cylindrical tube being relatively large in diameter is coaxial
It is socketed in outside the smaller cylindrical tube of diameter, and the periphery of described two cylindrical tubes is both provided with for dispersed paste
Hollow out.
When the Centrifugal dispersion mechanism sets more than two-stage, the Centrifugal dispersion tank body lower end of previous stage Centrifugal dispersion mechanism
Discharge port is connected with the Centrifugal dispersion tank body upper end feed inlet of rear stage Centrifugal dispersion mechanism by pipeline, in the pipeline by nearby
The Centrifugal dispersion tank body lower end discharge outlet of first-stage centrifugal decentralized institution is provided with diaphragm pump.
The Centrifugal dispersion tank body upper end one side of Centrifugal dispersion mechanism described in afterbody is offered for the true of slurry deaeration
It eats dishes without rice or wine.
Compared with prior art, the continuous dispersal device of a kind of pulp of lithium ion battery of the utility model, by powder substance
And liquid substance is launched respectively, and spray mode liquid delivery substance is used, by carrying out for the first time disperseing and centrifuging to material
It is scattered, dispersion effect can be improved；By the way that first decentralized institution is arranged to three-level, Centrifugal dispersion mechanism is arranged to two-stage,
Working continuously for slurry can be achieved, incessantly output slurry, improve dust dispersion quality and production efficiency.
Description of the drawings
Fig. 1 is a kind of overall structure signal of the continuous dispersal device embodiment 1 of pulp of lithium ion battery of the utility model
Figure；
Fig. 2 shows for the structure of first decentralized institution in a kind of continuous dispersal device of pulp of lithium ion battery of the utility model
It is intended to；
Fig. 3 is a kind of overall structure signal of the continuous dispersal device embodiment 2 of pulp of lithium ion battery of the utility model
Figure；
Fig. 4 shows for the structure of Centrifugal dispersion mechanism in a kind of continuous dispersal device of pulp of lithium ion battery of the utility model
It is intended to；
Fig. 5 is the side view of Centrifugal dispersion device in Fig. 4.
In figure, 1. powder substance holding vessels, 2. solvent holding vessels, 3. first decentralized institutions, 31. first scattered tank bodies, 32.
High speed disperser, 33. first drivers, 34. solvent spray throwers, 35. screw extruding devices, 4. Centrifugal dispersion mechanisms, 41. centrifugations point
Scattered tank body, 42. Centrifugal dispersion devices, 43. centrifugation crash panels, 44. first material scrapers, 45. second drivers, 46. second material scrapers,
47. diaphragm pump, 48. vacuum ports, 5. first level-one meters, 6. second level-one meters, 7. two level meters.
Specific embodiment
The utility model is described in further detail with specific embodiment below in conjunction with the accompanying drawings：
Embodiment 1：
As shown in Figure 1, a kind of continuous dispersal device of pulp of lithium ion battery of the utility model, including at least one powder
Material matter holding vessel 1, at least one solvent holding vessel 2, the first decentralized institution 3 of level-one and first-stage centrifugal decentralized institution 4, each powder
The bottom discharge mouth of the bottom discharge mouth of material matter holding vessel 1 and each solvent holding vessel 2 passes through pipeline and first dispersion machine
Structure 3 is connected, the discharge port connection Centrifugal dispersion mechanism 4 of first decentralized institution 3；Powder in each powder substance holding vessel 1
Liquid substance in substance and each solvent holding vessel 2 initially enters to be disperseed for the first time in first decentralized institution 3, then again into
Enter and Centrifugal dispersion is carried out in Centrifugal dispersion mechanism 4.Preferably, it is logical in each powder substance holding vessel 1 and each solvent holding vessel 2
Meter is both provided on the pipeline of first decentralized institution 3, is respectively used to the amount of metering powder substance and liquid substance.
As shown in Fig. 2, first decentralized institution 3 include for the first time scattered tank body 31, high speed disperser 32, the first driver 33,
Solvent spray thrower 34 and screw extruding device 35；The upper end feed inlet and each powder substance holding vessel 1 of first scattered tank body 31
Bottom discharge mouth pass through pipeline connection；High speed disperser 32 is provided in scattered tank body 31 for the first time, the first driver 33 is set
It with high speed disperser 32 is connected in the upper end of first scattered tank body 31 and by transmission shaft, solvent spray thrower 34 is arranged on first point
The outer wall of tank body 31 is dissipated at lower end position, and solvent spray thrower 34 and the bottom discharge mouth of each solvent holding vessel 2 pass through pipe
Road connects；Screw extruding device 35 is connected with the lower end discharge port of first scattered tank body 31.
Embodiment 2：
The preferred embodiment of the utility model is illustrated in figure 3, wherein, first decentralized institution 3 is provided with three-level：Wherein
The upper end feed inlet of first scattered tank body 31 in the first decentralized institution 3 of level-one and the bottom of each powder substance holding vessel 1 go out
Material mouth by pipeline connection, leads to the first dispersion tank in the first decentralized institution 3 of the first order in each powder substance holding vessel 1
It is both provided with to measure the first level-one meter 5 of each powder substance total amount on the pipeline of body 31；The first order is disperseed for the first time
The upper end of the discharge port of screw extruding device 35 in mechanism 3 and the first scattered tank body 31 in the first decentralized institution 3 in the second level into
Material mouth connects；In the discharge port of screw extruding device 35 in the first decentralized institution 3 in the second level and the first decentralized institution 3 of the third level
The upper end feed inlet connection of first scattered tank body 31；The discharge port of screw extruding device 35 in the first decentralized institution 3 of the third level with
The feed inlet connection of Centrifugal dispersion mechanism 4；Solvent spray thrower 34 in per level-one first decentralized institution 3 with solvent holding vessel 2
Bottom discharge mouth by pipeline connection, lead in each solvent holding vessel 2 on the main pipe rail of first decentralized institution 3 and be respectively provided with one
A the second level-one meter 6 for being used to measure each liquid substance total amount, disperses for the first time in the second level-one meter 6 and per level-one
Two level meter 7 is both provided on the pipeline between solvent spray thrower 34 in mechanism 3, is divided for the first time for measuring into per level-one
Dissipate the liquids quality in the solvent spray thrower 34 in mechanism 3.Preferably, the screw extruding in the 3rd extremely first decentralized institution 3
Device 35 is twin-screw extruder device.
As shown in figure 4, Centrifugal dispersion mechanism 4 include Centrifugal dispersion tank body 41, Centrifugal dispersion device 42, centrifugation crash panel 43,
First material scraper 44, the second driver 45, discharge port and the centrifugation point of the screw extruding device 35 in the first decentralized institution 3 of the third level
The upper end feed inlet connection of tank body 41 is dissipated, is provided with Centrifugal dispersion device 42 in Centrifugal dispersion tank body 41, centrifugation crash panel 43 is set
Two, two centrifugation crash panels 43 are symmetricly set on two outsides of Centrifugal dispersion device 42, and the first material scraper 44 is a pair of of inverted L shape knot
Structure is symmetricly set between Centrifugal dispersion device 42 and centrifugation crash panel 43 and coordinates with centrifugation crash panel 43；Second driving
Device 45 is connected by transmission shaft with 42 and first material scraper 44 of Centrifugal dispersion device.
Preferably, be provided with the second material scraper 46 in the lower end of Centrifugal dispersion device 42, the second material scraper 46 include one end with
Be driven the crossbeam of axis connection and the Curved beam with the cooperation of 41 inner wall of Centrifugal dispersion tank body, one end of Curved beam and crossbeam it is another
End connection.
As shown in figure 5, Centrifugal dispersion device 42 is made of two different cylindrical tubes of diameter, wherein the cylinder being relatively large in diameter
Cylinder is coaxially socketed in outside the smaller cylindrical tube of diameter, and the periphery of two cylindrical tubes is both provided with for dispersion pulp
The hollow out of material.
Preferably, Centrifugal dispersion mechanism 4 is provided with two-stage；The wherein Centrifugal dispersion tank body of first order Centrifugal dispersion mechanism 4
41 lower end discharge ports are connected with the 41 upper end feed inlet of Centrifugal dispersion tank body of second level Centrifugal dispersion mechanism 4 by pipeline, at this
Pipeline is provided with diaphragm pump 47 close to the 41 lower end discharge outlet of Centrifugal dispersion tank body of first order Centrifugal dispersion mechanism 4.Also, the
The 41 upper end one side of Centrifugal dispersion tank body of two-stage centrifugal decentralized institution 4 offers the vacuum port 48 for slurry deaeration.
The operation principle of the utility model is as follows：
First, the powder substance of required input is added in powder substance holding vessel 1, by the liquid substance of required input
It is put into solvent holding vessel 2；The quantity of powder substance holding vessel 1 and solvent holding vessel 2 can be according to the kind of actually used material
Class is increased and decreased.Then the ratio added in required for each material is set.Next, according to the proportioning of each material, utilize
First level-one meter 5 measures each powder substance, while using the second level-one meter 6 to the total amount of liquid substance
It is measured.Then powder substance flows into the feed inlet of the first scattered tank body 31 of first decentralized institution 3 by pipeline, enters back into
High speed dispersion is carried out into high speed disperser 32, high speed disperser 32 is driven by the first driver 33, in powder substance from a high speed
While 32 lower end of disperser is flowed out, the spray that liquid substance is carried out using solvent spray thrower 34 is launched；It is above-mentioned to disperse what is obtained
Slurry, which is entered in screw extruding device 35, to be disperseed and is transmitted again.When being preferably provided with the first decentralized institution 3 of three-level, from
Slurry in level-one screw extruding device 35 out, which enters, carries out second of high speed dispersion in second level high speed disperser 32, together
While slurry is flowed out from 32 lower end of second level high speed disperser, liquids are carried out using second level solvent spray thrower 34 for sample
The spray of matter is launched, and then slurry enters in second level screw extruding device 35 and disperseed and transmitted；From the second level, screw rod squeezes
Slurry in depressor 35 out enters in third level high speed disperser 32 progress third time high speed dispersion, in slurry from the third level
While 32 lower end of high speed disperser is flowed out, the spray that liquid substance is carried out using third level solvent spray thrower 34 is launched, then
Slurry, which is entered in third level screw extruding device 35, to be disperseed and is transmitted；Wherein, per level-one, the liquids quality of input passes through
Two level meter 7 is measured.Slurry from third level screw extruding device 35 out, which is entered in Centrifugal dispersion mechanism 4, to carry out
Centrifugal dispersion, detailed process are as follows：
The feed inlet of slurry from Centrifugal dispersion tank body 41 is entered in Centrifugal dispersion device 42, and Centrifugal dispersion device 42 passes through centrifugation
The slurry being transferred to is thrown away Centrifugal dispersion device 42 by power, the slurry through throwing away strike centrifugation crash panel 43 on after due to self gravitation
Effect flows to the lower section of Centrifugal dispersion tank body 41；The leftover slurry impinged upon on centrifugation crash panel 43 will using the first material scraper 44
Its whole scrapes the lower section for flowing to Centrifugal dispersion tank body 41；It will be remained again by the second material scraper 46 on 41 inner wall of Centrifugal dispersion tank body
Slurry scrape.When being preferably provided with two-stage centrifugal decentralized institution 4, come out from 41 lower end discharge port of first order Centrifugal dispersion tank body
Slurry pumped by diaphragm pump 47 above-mentioned centrifugation point repeated in the upper end feed inlet for entering second level Centrifugal dispersion tank body 41
The process of dissipating, the slurry disperseed carry out deaeration processing by vacuum port 48；Finally obtained slurry is detected, detection is qualified
After can directly upper coating machine coating.The dispersion process of above-mentioned whole slurry is continuous action, and wherein first-stage centrifugal is disperseed and two level
It is scattered that Centrifugal dispersion can carry out Xun Huan according to the effect of slurry；Its rate of dispersion reaches 10m~20m/ when pulp centrifuged scattered
s。
Claims (10)
1. the continuous dispersal device of a kind of pulp of lithium ion battery, which is characterized in that it includes at least one powder substance storage
Tank, at least at least one solvent holding vessel, the first decentralized institution of level-one and at least first-stage centrifugal decentralized institution, each powder
The bottom discharge mouth of the bottom discharge mouth of substance holding vessel and each solvent holding vessel passes through pipeline and described at least one
The first decentralized institution of grade is connected, at least first-stage centrifugal dispersion machine described in the discharge port connection of the first decentralized institution of afterbody
Structure.
2. the continuous dispersal device of a kind of pulp of lithium ion battery according to claim 1, which is characterized in that in each institute
It states powder substance holding vessel and each solvent holding vessel leads on the pipeline of the first decentralized institution and is both provided with metering
Device.
3. the continuous dispersal device of a kind of pulp of lithium ion battery according to claim 2, which is characterized in that described first
Decentralized institution includes scattered tank body, high speed disperser, the first driver, solvent spray thrower and screw extruding device for the first time；It is described
The upper end feed inlet and the bottom discharge mouth of each powder substance holding vessel of first scattered tank body pass through pipeline connection；It is described
The high speed disperser is provided in first dispersion tank body, first driver is arranged on the upper end of the first scattered tank body
And be connected by transmission shaft with the high speed disperser, the outer wall that the solvent spray thrower is arranged on the first scattered tank body leans on
At nearly lower end position, the bottom discharge mouth of the solvent spray thrower and each solvent holding vessel passes through pipeline connection；It is described
Screw extruding device is connected with the lower end discharge port of the first scattered tank body.
A kind of 4. continuous dispersal device of pulp of lithium ion battery according to claim 3, which is characterized in that the metering
Device includes the first level-one meter, the second level-one meter and two level meter, leads in each powder substance holding vessel
One is respectively provided with for measuring each powder substance total amount on the pipeline of first scattered tank body in the first decentralized institution of the first order
The first level-one meter；Per bottom of the solvent spray thrower in the first decentralized institution of level-one with each solvent holding vessel
Discharge port leads on the main pipe rail of the first decentralized institution in each solvent holding vessel by pipeline connection and is respectively provided with one
A the second level-one meter for being used to measure each liquid substance total amount, in the second level-one meter and the first dispersion machine of every level-one
A two level meter is respectively provided on the pipeline between solvent spray thrower in structure, is used to measure and disperse for the first time into per level-one
The liquids quality in solvent spray thrower in mechanism.
5. the continuous dispersal device of a kind of pulp of lithium ion battery according to claim 3, which is characterized in that when described first
When secondary decentralized institution is set more than two-stage, the screw extruding device in the first decentralized institution of afterbody is twin-screw extruder device.
A kind of 6. continuous dispersal device of pulp of lithium ion battery according to claim 3, which is characterized in that the centrifugation
Decentralized institution includes Centrifugal dispersion tank body, Centrifugal dispersion device, centrifugation crash panel, the first material scraper, the second driver, afterbody
The discharge port of screw extruding device in the first decentralized institution is connected with the upper end feed inlet of the Centrifugal dispersion tank body, described
The Centrifugal dispersion device is provided in Centrifugal dispersion tank body, the centrifugation crash panel sets two, and two centrifugation crash panels are symmetrical
Be arranged on two outsides of the Centrifugal dispersion device, first material scraper is a pair of of inverted L shape structure, be symmetricly set on it is described from
Coordinate between heart disperser and the centrifugation crash panel and with centrifugation crash panel；Second driver passes through transmission shaft and institute
State Centrifugal dispersion device and the connection of the first material scraper.
A kind of 7. continuous dispersal device of pulp of lithium ion battery according to claim 6, which is characterized in that the centrifugation
The lower end of disperser is provided with the second material scraper, second material scraper include one end and the transmission axis connection crossbeam and
With the Curved beam of Centrifugal dispersion inner tank wall cooperation, one end of the Curved beam and the other end of crossbeam connect.
A kind of 8. continuous dispersal device of pulp of lithium ion battery according to claim 7, which is characterized in that the centrifugation
Disperser is made of two different cylindrical tubes of diameter, wherein to be coaxially socketed in diameter smaller for the cylindrical tube being relatively large in diameter
Outside cylindrical tube, and the periphery of described two cylindrical tubes is both provided with the hollow out for dispersed paste.
9. a kind of continuous dispersal device of pulp of lithium ion battery according to any one of claim 6-8, feature exist
In, when the Centrifugal dispersion mechanism sets more than two-stage, the Centrifugal dispersion tank body lower end discharging of previous stage Centrifugal dispersion mechanism
Mouth is connected with the Centrifugal dispersion tank body upper end feed inlet of rear stage Centrifugal dispersion mechanism by pipeline, in the pipeline close to previous stage
The Centrifugal dispersion tank body lower end discharge outlet of Centrifugal dispersion mechanism is provided with diaphragm pump.
10. a kind of continuous dispersal device of pulp of lithium ion battery according to claim 9, which is characterized in that last
The Centrifugal dispersion tank body upper end one side of the grade Centrifugal dispersion mechanism offers the vacuum port for slurry deaeration.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721224134.7U CN207430206U (en) | 2017-09-22 | 2017-09-22 | A kind of continuous dispersal device of pulp of lithium ion battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721224134.7U CN207430206U (en) | 2017-09-22 | 2017-09-22 | A kind of continuous dispersal device of pulp of lithium ion battery |
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| Publication Number | Publication Date |
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| CN207430206U true CN207430206U (en) | 2018-06-01 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201721224134.7U Active CN207430206U (en) | 2017-09-22 | 2017-09-22 | A kind of continuous dispersal device of pulp of lithium ion battery |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108816136A (en) * | 2018-06-07 | 2018-11-16 | 山东奥冠新能源科技有限公司 | A kind of continuous production device and technique for lithium battery slurry |
-
2017
- 2017-09-22 CN CN201721224134.7U patent/CN207430206U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108816136A (en) * | 2018-06-07 | 2018-11-16 | 山东奥冠新能源科技有限公司 | A kind of continuous production device and technique for lithium battery slurry |
| CN108816136B (en) * | 2018-06-07 | 2021-02-26 | 山东奥冠新能源科技有限公司 | Continuous production device and process for lithium battery slurry |
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