CN206711966U - Pipeline cell size automatic production line - Google Patents
Pipeline cell size automatic production line Download PDFInfo
- Publication number
- CN206711966U CN206711966U CN201720105326.XU CN201720105326U CN206711966U CN 206711966 U CN206711966 U CN 206711966U CN 201720105326 U CN201720105326 U CN 201720105326U CN 206711966 U CN206711966 U CN 206711966U
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- China
- Prior art keywords
- tank
- raw material
- powder
- production line
- slurry
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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Abstract
The utility model discloses a kind of pipeline cell size automatic production line, include：Raw material feed system；Raw material quantitative add-on system；Material forming system；Slurry transferring system；Filter induction system；Control electric cabinet；Connecting pipeline, the connecting pipeline connect raw material feed system, raw material quantitative add-on system, material forming system, slurry transferring system, filtering induction system.Production line of the present utility model, whole oar process processed is supplied to from raw material, is that sealing is carried out, not with air contact, the quality of the slurry ensured well；And the production line is by under PLC control, it is added to after various splits and liquid weighing are quantified by raw material quantitative add-on system in blender, there are the various blenders that PLC is controlled to be processed by the requirement of technical recipe again, the uniformity for the slurry made is fine, meets the needs of market.
Description
Technical field
It the utility model is related to a kind of cell size production equipment, particularly automatic production line.
Background technology
In the making of lithium battery slurry, traditional approach is completed using vertical double-planet power mixer, working condition
Agitating paddle, dispersion impeller, which cooperate, to be completed, and vertical double-planet power mixer, stirring container are upper and lower bucket body structure, on
Staving is fixed, and lower barrel body rises closure, declines and open.Artificial plus when feeding intake and during finished product slurry, after staving is fallen, material is
It is open to be exposed in air ambient, because the particularity of lithium battery material, do not contacted with air preferably, otherwise can absorb sky
Moisture in gas, so that slurry quality reduces.And existing monomer mixer produces, turn in the addition of raw material and mixer
Speed, time, temperature, vacuum are all manual operations, plus quality of workers, personnel change etc. factor, the slurry worked it out viscosity,
Solid content, formula rate, in mobility, each pot of material is all different, has a strong impact on the quality of resultant battery.
Utility model content
The technical problems to be solved in the utility model is：A kind of full automatic lithium battery slurry production line is provided, ensures slurry
The Forming Quality of material.
The solution that the utility model solves its technical problem is：Wire type cell size automatic production line, includes：
Raw material feed system：Include powder supply device, fluid Supplying apparatus and SBR colloid feedways；The powder supply
Device includes loading hopper, fluffy device, powder discharge nozzle, vavuum pump and supply controller；The fluid Supplying apparatus includes
There are fluid reservoir, liquid pump and metering valve；The SBR colloids feedway includes colloid storage tank and colloid supply pump；
Raw material quantitative add-on system：Include powder weighing device, liquid metering device and colloid metering device, the powder is weighed
Device includes powder tank, weighing sensor, powder charge pipe, and the powder tank is connected with powder discharge nozzle；The level meter
Measuring device includes mass flowmenter, liquid addition pipe, and one end of the mass flowmenter is connected other end and liquid with fluid reservoir
Body charge pipe connects；The colloid metering device includes Measuring glass, pours out mechanism, and the Measuring glass connects with colloid supply pump
Connect, the Measuring glass, which is placed on, pours out mechanism；Material forming system：Include slurry mixer, pulp dilution device, high speed homogenization
Machine, the slurry mixer include blending tank, agitating paddle, and the powder charge pipe, liquid addition pipe connect with blending tank, institute
State blending tank and include delivery outlet；The pulp dilution device includes thinning tank, dispersion mixing device, the thinning tank and output
Mouth connection, the thinning tank are connected with pouring out mechanism；The high-shear homogenizer includes charging pump installation, staving, homogeneous head, institute
The one end for stating charging pump installation connects other end with thinning tank and connected with staving, and the homogeneous head is located in staving；In slurry
Transfer from one department to another to unite：Include three transfer tanks, the transfer tank includes temperature control device, and three transfer tanks are sequentially connected, described
First transfer tank connects with staving, the 3rd transfer tank connects with filtering induction system；Filter induction system：Include screen pack,
Magnetic filter, feeding engine and finished product discharge nozzle；Control electric cabinet：Include PLC, the PLC is and raw material
Feed system, raw material quantitative add-on system, material forming system, slurry transferring system, filtering induction system electrical connection；Communicating pipe
Road, the connecting pipeline convey feed system, raw material quantitative add-on system, material forming system, slurry transferring system, filtering
System connectivity.
As the further improvement of above-mentioned technical proposal, the powder supply device also includes pulse dust collector.
As the further improvement of above-mentioned technical proposal, the slurry mixer also include stirring motor, stirring main shaft,
Supervising device, shaft sealer, the agitating paddle are arranged in stirring main shaft, and the shaft sealer is arranged on stirring main shaft
Both ends, for the supervising device in blending tank, the supervising device includes temperature sensor, pressure sensor and vacuum
Sensor.
As the further improvement of above-mentioned technical proposal, the mechanism that pours out includes SBR memories, institute's SBR memories
It is connected with Measuring glass, the SBR memories are provided with atmospheric valve provided with liquid level sensor, pressure sensor, bottom.
As the further improvement of above-mentioned technical proposal, the homogenizer also includes cooling device, the cooling device
On the outside of staving.
As the further improvement of above-mentioned technical proposal, the transfer tank includes tank body, cover, is provided with the tank body
Rabbling mechanism.
The beneficial effects of the utility model are：Production line of the present utility model, whole oar mistake processed is supplied to from raw material
Journey, it is that sealing is carried out, not with air contact, the quality of the slurry ensured well；And the production line is by PLC control
Under, it is added to after various splits and liquid weighing are quantified by raw material quantitative add-on system in blender, then have what PLC was controlled
Various blenders set set rotating speed, time, temperature, vacuum are mixed, stirred with being divided by the requirement of technical recipe
Dissipate, the uniformity for the slurry made is fine, meets the needs of market.
Brief description of the drawings
, below will be to needed for embodiment description in order to illustrate more clearly of the technical scheme in the embodiment of the utility model
The accompanying drawing to be used is briefly described.Obviously, described accompanying drawing is part of the embodiment of the present utility model, rather than entirely
Portion's embodiment, those skilled in the art on the premise of not paying creative work, can also obtain it according to these accompanying drawings
His design and accompanying drawing.
Fig. 1 is front view of the present utility model；
Fig. 2 is top view of the present utility model.
Embodiment
Design, concrete structure and caused technique effect of the present utility model are carried out below with reference to embodiment and accompanying drawing
Clearly and completely describe, to be completely understood by the purpose of this utility model, feature and effect.Obviously, described embodiment
It is part of the embodiment of the present utility model, rather than whole embodiments, based on embodiment of the present utility model, the skill of this area
The other embodiment that art personnel are obtained on the premise of not paying creative work, belong to the model of the utility model protection
Enclose.In addition, all connection/annexations being previously mentioned in text, not singly refer to component and directly connect, and refer to can be according to specific reality
Situation is applied, by adding or reducing couple auxiliary, to form more excellent draw bail.Each technology in the invention is special
Sign, can be with combination of interactions on the premise of not conflicting conflict.
1~Fig. 2 of reference picture, wire type cell size automatic production line, includes：Raw material feed system 1：Include powder
Feedway, fluid Supplying apparatus and SBR colloid feedways；The powder supply device include loading hopper, fluffy device,
Powder discharge nozzle, vavuum pump and supply controller；The fluid Supplying apparatus includes fluid reservoir, liquid pump and metering
Valve；The SBR colloids feedway includes colloid storage tank and colloid supply pump；Raw material quantitative add-on system 2：Include
Powder weighing device, liquid metering device and colloid metering device, the powder weighing device includes powder tank, biography of weighing
Sensor, powder charge pipe, the powder tank are connected with powder discharge nozzle；The liquid metering device includes mass flowmenter, liquid
Body charge pipe, one end of the mass flowmenter are connected other end with fluid reservoir and are connected with liquid addition pipe；The colloid meter
Amount device includes Measuring glass, pours out mechanism, and the Measuring glass is connected with colloid supply pump, and the Measuring glass is placed on the machine of pouring out
Structure；Material forming system 3：Include slurry mixer, pulp dilution device, high-shear homogenizer, the slurry mixer includes
Blending tank, agitating paddle, the powder charge pipe, liquid addition pipe connect with blending tank, and the blending tank includes delivery outlet；Institute
State pulp dilution device and include thinning tank, dispersion mixing device, the thinning tank connects with delivery outlet, and the thinning tank is with pouring out
Mechanism connects；The high-shear homogenizer include charging pump installation, staving, homogeneous head, it is described charging pump installation one end with it is dilute
Release tank connection other end to connect with staving, the homogeneous head is in staving；Slurry transferring system 4：Include three transfers
Tank, the transfer tank include temperature control device, and three transfer tanks are sequentially connected, the first transfer tank connects with staving,
3rd transfer tank connects with filtering induction system 5, and middle cylinder is for inactive slurry so that the quality of slurry more has guarantor
Card；Filter induction system 5：Include screen pack, magnetic filter, feeding engine and finished product discharge nozzle；Control electric cabinet 6：Include
PLC, the PLC with raw material feed system 1, raw material quantitative add-on system 2, material forming system 3, slurry
Transferring system 4, filtering induction system 5 electrically connect；Connecting pipeline 7, the connecting pipeline 7 is by raw material feed system 1, raw material quantitative
Add-on system 2, material forming system 3, slurry transferring system 4, filtering induction system 5 connect.Meanwhile accounted for further save
Ground area, described raw material feed system, raw material quantitative the add-on system slurry mixer in material forming system, slurry
Diluter stacks successively from top to bottom, and the storage area of raw material can stack original material, by a feeding device by ground
Under raw material be supplied in the raw material feed system of the top.
Preferred embodiment is further used as, the powder supply device also includes pulse dust collector.Pass through pulse
Deduster, it is possible to reduce the accumulation of powder, not only save raw material, and make it that the precision of formula is more accurate.
Preferred embodiment is further used as, the slurry mixer also includes stirring motor, stirring main shaft, monitoring
Device, shaft sealer, the agitating paddle are arranged in stirring main shaft, and the shaft sealer is arranged on the two of stirring main shaft
End, in blending tank, the supervising device includes temperature sensor, pressure sensor and vacuum and passed the supervising device
Sensor.In order to ensure the forming quality of slurry, described main shaft prevents air from being altered from main shaft into material cylinder by sealing device
In, destroy the quality of slurry.
Preferred embodiment is further used as, the mechanism that pours out includes SBR memories, and institute's SBR memories are with determining
Measuring cup connects, and the SBR memories are provided with atmospheric valve provided with liquid level sensor, pressure sensor, bottom.
Preferred embodiment is further used as, the homogenizer also includes cooling device, and the cooling device is located at
On the outside of staving.Homogenizer easily produces high temperature in the course of the work, and high temperature can impact to the quality of slurry, therefore, leads to
Cross and cooling device is incorporated in homogenizer so that the quality of slurry is more guaranteed.
Be further used as preferred embodiment, the transfer tank includes tank body, cover, described first and the 3rd tank
Rabbling mechanism is provided with body.
Better embodiment of the present utility model is illustrated above, but the invention be not limited to it is described
Embodiment, those skilled in the art can also make a variety of equivalent changes on the premise of without prejudice to the utility model spirit
Type or replacement, these equivalent modifications or replacement are all contained in the application claim limited range.
Claims (6)
1. pipeline cell size automatic production line, it is characterised in that：Include：
Raw material feed system (1)：Include powder supply device, fluid Supplying apparatus and SBR colloid feedways；The powder
Body feeding includes loading hopper, fluffy device, powder discharge nozzle, vavuum pump and supply controller；The liquid supply dress
Put and include fluid reservoir, liquid pump and metering valve；The SBR colloids feedway includes colloid storage tank and colloid supplies
To pump；
Raw material quantitative add-on system (2)：Include powder weighing device, liquid metering device and colloid metering device, it is described
Powder weighing device includes powder tank, weighing sensor, powder charge pipe, and the powder tank is connected with powder discharge nozzle；Institute
Stating liquid metering device includes mass flowmenter, liquid addition pipe, and one end of the mass flowmenter is connected in addition with fluid reservoir
One end is connected with liquid addition pipe；The colloid metering device includes Measuring glass, pours out mechanism, and the Measuring glass supplies with colloid
Connected to pump, the Measuring glass, which is placed on, pours out mechanism；
Material forming system (3)：Include slurry mixer, pulp dilution device, high-shear homogenizer, the slurry mixer includes
There are blending tank, agitating paddle, the powder charge pipe, liquid addition pipe connect with blending tank, and the blending tank includes delivery outlet；
The pulp dilution device includes thinning tank, dispersion mixing device, and the thinning tank connects with delivery outlet, and the thinning tank is with falling
Go out mechanism connection；The high-shear homogenizer include charging pump installation, staving, homogeneous head, it is described charging pump installation one end with
Thinning tank connection other end connects with staving, and the homogeneous head is in staving；
Slurry transferring system (4)：Include three transfer tanks, the transfer tank includes temperature control device, three transfer tanks
It is sequentially connected, the first transfer tank connects with staving, the 3rd transfer tank connects with filtering induction system (5)；
Filter induction system (5)：Include screen pack, magnetic filter, feeding engine and finished product discharge nozzle；
Control electric cabinet (6)：Include PLC, the PLC is added with raw material feed system (1), raw material quantitative
System (2), material forming system (3), slurry transferring system (4), filtering induction system (5) electrical connection；
Connecting pipeline (7), the connecting pipeline (7) is by raw material feed system (1), raw material quantitative add-on system (2), material forming
System (3), slurry transferring system (4), filtering induction system (5) connection.
2. pipeline cell size automatic production line according to claim 1, it is characterised in that：The powder supply dress
Put and also include pulse dust collector.
3. pipeline cell size automatic production line according to claim 1, it is characterised in that：The slurry mixer
Also include stirring motor, stirring main shaft, supervising device, shaft sealer, the agitating paddle is arranged in stirring main shaft, described
Shaft sealer is arranged on the both ends of stirring main shaft, and for the supervising device in blending tank, the supervising device includes temperature
Spend sensor, pressure sensor and vacuum transducer.
4. pipeline cell size automatic production line according to claim 1, it is characterised in that：It is described to pour out mechanism bag
SBR memories are included, institute's SBR memories are connected with Measuring glass, and the SBR memories are provided with liquid level sensor, pressure sensing
Device, bottom are provided with atmospheric valve.
5. pipeline cell size automatic production line according to claim 1, it is characterised in that：The homogenizer also wraps
Cooling device is included, the cooling device is on the outside of staving.
6. pipeline cell size automatic production line according to claim 1, it is characterised in that：The transfer tank includes
Have tank body, a cover, described first and the 3rd tank body in be provided with rabbling mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720105326.XU CN206711966U (en) | 2017-01-23 | 2017-01-23 | Pipeline cell size automatic production line |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720105326.XU CN206711966U (en) | 2017-01-23 | 2017-01-23 | Pipeline cell size automatic production line |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206711966U true CN206711966U (en) | 2017-12-05 |
Family
ID=60472925
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720105326.XU Withdrawn - After Issue CN206711966U (en) | 2017-01-23 | 2017-01-23 | Pipeline cell size automatic production line |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206711966U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107068965A (en) * | 2017-01-23 | 2017-08-18 | 广州红尚机械制造有限公司 | Pipeline cell size automatic production line |
-
2017
- 2017-01-23 CN CN201720105326.XU patent/CN206711966U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107068965A (en) * | 2017-01-23 | 2017-08-18 | 广州红尚机械制造有限公司 | Pipeline cell size automatic production line |
| CN107068965B (en) * | 2017-01-23 | 2023-05-19 | 广州红尚机械制造有限公司 | Full-automatic production line of pipeline formula battery thick liquids |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20171205 Effective date of abandoning: 20230519 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20171205 Effective date of abandoning: 20230519 |