CN209188694U - A kind of processing conveying system of superfine powder engineering - Google Patents
A kind of processing conveying system of superfine powder engineering Download PDFInfo
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- CN209188694U CN209188694U CN201821337969.8U CN201821337969U CN209188694U CN 209188694 U CN209188694 U CN 209188694U CN 201821337969 U CN201821337969 U CN 201821337969U CN 209188694 U CN209188694 U CN 209188694U
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Abstract
The utility model system provides a kind of processing conveying system of superfine powder engineering, including the module that feeds intake, slurrying module and conveyor module；Conveyor module includes the first conveying channel, it is connected on first conveying channel and several stirs storage tank slowly, slowly stirring storage tank is connected with the second conveying channel by the first discharging channel, several feed storage tanks is connected on the second conveying channel, the output end for being fed storage tank is connected with the second discharging channel；Slowly it stirs and is equipped with the first deaeration filter mechanism between storage tank and the first conveying channel, it is fed between storage tank and the second discharging channel and is equipped with the second deaeration filter mechanism, the both ends in the first conveying channel are connected separately with the first cleaning dispatching station and the first recycle bin, and the both ends in the second conveying channel are connected separately with the second cleaning dispatching station and the second recycle bin.The slurry of the utility model preparation after stirring storage tank stable storing slowly by just putting into memory structure, it can be ensured that exports the performance of slurry, and deaeration filter structure can be improved the purity of slurry.
Description
Technical field
The utility model relates to superfine powder engineerings, specifically disclose a kind of processing conveying system of superfine powder engineering.
Background technique
Superfine powder refers to particle of the diameter less than 10 μm, and density is less than 1g/ml, is widely used in chemical industry, plastics, new energy
The fields such as source, new material, pharmacy, food, cosmetics, fine chemistry industry.
In the prior art, superfine powder engineering mainly includes feeding system and pulping system, and feeding system is by quantitative former material
In material input pulping system, material is stirred acquisition slurry by pulping system, under slurry is directly output to after completing
One processing link, slurry, there are more bubble, will affect the performance of slurry after completing, and for cell size, directly
It connects and is not stabilized slurry production battery pole piece using rigid prepare, the performance of battery can be made to have a greatly reduced quality.
Utility model content
Based on this, it is necessary to be directed to prior art problem, provide a kind of processing conveying system of superfine powder engineering, slurrying is complete
It is just come into operation at rear by stirring to stablize to handle slowly, can effectively ensure the performance of slurry.
To solve prior art problem, the utility model discloses a kind of processing conveying system of superfine powder engineering, including according to
The secondary connected module that feeds intake, slurrying module and conveyor module；
Conveyor module includes the first conveying channel, be connected on the first conveying channel it is several stir storage tank slowly, stir storage tank slowly
Speed of agitator is 5~40r/min, stirs storage tank slowly by the first discharging channel and is connected with the second conveying channel, on the second conveying channel
Several feed storage tanks are connected with, the output end for being fed storage tank is connected with the second discharging channel；
Slowly stir and be equipped with the first deaeration filter mechanism between storage tank and the first conveying channel, be fed storage tank and the second discharging channel it
Between be equipped with the second deaeration filter mechanism, the both ends in the first conveying channel be connected separately with the first cleaning dispatching station and first recycling
It stands, the both ends in the second conveying channel are connected separately with the second cleaning dispatching station and the second recycle bin.
Further, the module that feeds intake includes at least one feeding station, and the output end of feeding station is connected by dynamic measuring mechanism
Connect slurrying module.
Further, the module that feeds intake further includes anti-fugitive dust negative pressure generating mechanism, the output end of anti-fugitive dust negative pressure generating mechanism
Connect dynamic measuring mechanism and slurrying module.
Further, slurrying module includes field wetting mechanism, fluctuation mixed organization and the cladding pulping mechanism set gradually.
Further, the first cleaning dispatching station and the second cleaning dispatching station are dry ice dispatching station or rotating wash bowl dispatching station.
Further, the first deaeration filter mechanism and the second deaeration filter mechanism include centrifugal defoaming machine, evacuation and centrifugal degassing
The input terminal of machine is equipped with filter screen.
Further, the top for stirring storage tank slowly is connect by the first air pressure balance pipeline with the first discharging channel, and storage tank is fed
Top connect with the second discharging channel by the second air pressure balance pipeline.
The utility model has the following beneficial effects: the utility model discloses a kind of processing conveying system of superfine powder engineering, if
Set it is independent stir storage tank slowly, preparing the slurry of completion, just investment can be fed at any time after a certain period of time by stirring storage tank stable storing slowly
Memory structure in, and used within the regular hour, can effectively ensure the performance of slurry, the batch can setting of independent separate
It conveniently manages and maintains, can avoid exporting without the slurry that processing is stablized in stirring slow enough to subsequent processing, can effectively ensure
Export the performance of slurry, the deaeration that can effectively ensure the performance of battery pole piece for making cell size, and rationally be arranged
Filter structure can be improved the purity and performance of slurry, cleaning structure can storage tank to conveyor module and pipeline clean, and
Waste material is recycled by recycle bin, cleaning operation is convenient.
Detailed description of the invention
Fig. 1 is the structural schematic diagram that the utility model connects control centre.
Fig. 2 is the structural schematic diagram of the utility model.
Fig. 3 is the enlarged structure schematic diagram of conveyor module in the utility model.
Appended drawing reference are as follows: the module that feeds intake 10, feeding station 11, dynamic measuring mechanism 12, anti-fugitive dust generating mechanism 13, slurrying mould
Block 20, field wetting mechanism 21, fluctuation mixed organization 22, cladding pulping mechanism 23, conveyor module 30, the first conveying channel 31, the
One cleaning dispatching station 311, stirs storage tank 32, the first deaeration filter mechanism 321, the first air pressure balance pipeline at first recycle bin 312 slowly
322, the first discharging channel 33, the second conveying channel 34, second cleaning dispatching station 341, the second recycle bin 342, feed storage tank 35, the
Two deaeration filter mechanisms 351, the second air pressure balance pipeline 352, the second discharging channel 36.
Specific embodiment
For the feature, technological means and specific purposes achieved, function that can further appreciate that the utility model, below
The utility model is described in further detail in conjunction with attached drawing and specific embodiment.
Referring to figs. 1 to Fig. 3.
The utility model discloses a kind of processing conveying system of superfine powder engineering, including the module that feeds intake being sequentially connected
10, slurrying module 20 and conveyor module 30, as shown in Figure 1, Central Control Center by electrical connection respectively control feed intake module 10,
Slurrying module 20 and conveyor module 30；
As shown in Figure 2,3, conveyor module 30 includes the first conveying channel 31, is connected on the first conveying channel 31 several slow
Storage tank 32 is stirred, stirring storage tank 32 slowly is the internal storage tank for being equipped with stirring structure, and the speed of agitator for stirring storage tank 32 slowly is 5~40r/min,
Slowly the output end for stirring 32 bottom of storage tank is connected with the first discharging channel 33, stirs storage tank 32 slowly by the first discharging channel 33 and is connected with second
Conveying channel 34, several feed storage tanks 35 are connected on the second conveying channel 34, and the output end of feed storage tank 35 is connected with second
Discharging channel 36, slurry is made directly to be used ineffective afterwards, and slurry in stirring storage tank 32 with the low-rotate speed of 5~40r/min slowly
It is stirred after 20~60min of storage and is delivered to feed storage tank 35 again, the properties of slurry can be effectively improved, be fed storage tank
35 can provide slurry at any time for next processing stations, and two be independently arranged group storage tank conveniently manages and maintains；
Slowly it stirs and is equipped with the first deaeration filter mechanism 321 between storage tank 32 and the first conveying channel 31, be fed storage tank 35 and the
It is equipped with the second deaeration filter mechanism 351 between two discharging channels 36, the first deaeration filter mechanism 321 is set to slowly to stir storage tank 32 defeated
Enter end side, can effectively ensure to enter the slurry fine-stabilization for stirring storage tank 32 slowly, so as to effectively ensure to stir at stable slowly
Effect is managed, the performance of slurry is improved, the second deaeration filter mechanism 351 is set to the output end of feed storage tank 35, can be effective
Ensure the performance of the slurry of final output；
The both ends in the first conveying channel 31 are connected separately with the first cleaning dispatching station 311 and the first recycle bin 312, and second is defeated
The both ends in material channel 34 are connected separately with the second cleaning dispatching station 341 and the second recycle bin 342, and when cleaning, the first cleaning is sent
Storage tank 32, the first discharging channel 33 and the first conveying channel 31, the second cleaning hair are stirred in the cleaning medium cleaning that 311 send out of standing slowly
The 341 cleaning media that send out that see off clean the second conveying channels 34, and the waste material after cleaning enters the first recycle bin 312 and the
Two recycle bins 342 are simultaneously recycled by them.
A kind of processing conveying system of superfine powder engineering of the utility model, setting is independent to stir storage tank slowly, prepares completion
Slurry, which passes through, to be stirred slowly in the storage tank stable storing memory structure that just investment can be fed at any time after a certain period of time, and in the regular hour
It has inside used, can effectively ensure the performance of slurry, the batch can setting of independent separate is conveniently managed and maintained, be can avoid without foot
The slurry that processing is stablized in enough slow stirrings is exported to subsequent processing, can effectively ensure to export the performance of slurry, for making battery
Slurry can effectively ensure the performance of battery pole piece, and the deaeration filter structure being rationally arranged can be improved the purity and property of slurry
Can, cleaning structure can storage tank to conveyor module and pipeline clean, and pass through recycle bin recycling waste material, cleaning operation side
Just.
In the present embodiment, the module that feeds intake 10 includes at least one feeding station 11, and the output end of feeding station 11 passes through dynamic
Metrological service 12 connects slurrying module 20, and dynamic measuring mechanism 12 includes bracket, bracket down through the first Weighing module and
Second Weighing module is separately connected weight-loss metering storehouse and weight gain measuring chute, passes through metering between weight-loss metering storehouse and weight gain measuring chute
Screw rod connection.The investment speed of raw material can be precisely controlled by dynamic measuring mechanism 12, so that it is guaranteed that effects on slurry making.
Based on the above embodiment, the module that feeds intake 10 further includes anti-fugitive dust negative pressure generating mechanism 13, and machine occurs for anti-fugitive dust negative pressure
The output end connection dynamic measuring mechanism 12 and slurrying module 20 of structure 13, anti-fugitive dust negative pressure generating mechanism 13 mainly includes vacuum
Machine, vacuum machine is for vacuumizing by dynamic measuring mechanism 12 and slurrying module 20 before feeding intake and to form negative pressure state, thus in original
Fugitive dust can be effectively avoided during material conveying, can avoid waste of material, while can reduce the probability of dust explosion.
In the present embodiment, slurrying module 20 includes field wetting mechanism 21, fluctuation mixed organization 22 and the packet set gradually
Pulping mechanism 23 is covered, field soaks mechanism 21 and is located at close to the side of slurrying module 20, and it includes quantum field that field, which soaks mechanism 21,
Device, vibration field generator and field generator, fluctuation mixed organization 22 include wave device and fluidic device, coat pulping mechanism
23 be surface modification device, can realize that the slurrying of material is processed, and can effectively avoid the structure of material itself by low-shearing force
It is destroyed, so as to effectively improve the performance for preparing slurry.
In the present embodiment, the first cleaning dispatching station 311 and the second cleaning dispatching station 341 are dry ice dispatching station, dry ice
The temperature difference formed when cleaning can be such that different substances is detached under different contraction speeds, and cleaning effect is good；Or first
Cleaning dispatching station 311 and the second cleaning dispatching station 341 is rotating wash bowl dispatching station, and rotating wash bowl is easy to operate, the service life is long, consumption at
This is low.
In the present embodiment, the first deaeration filter mechanism 321 and the second deaeration filter mechanism 351 include evacuation and centrifugal degassing
The input terminal of machine, centrifugal defoaming machine is equipped with filter screen.Slurry by filter screen filtration can effectively go out iron impuritiess and other
Graininess foreign matter can be avoided non-large granular impurity into stirring storage tank 32 slowly or exporting from the second discharging channel 36, and filter screen is simultaneously
Pre- de-bubble processing can be carried out to slurry, filtered slurry is handled by the centrifugal thin-filmization of centrifugal defoaming machine, can be effective
Eliminate bubble；The pipeline for being provided with filter screen is externally provided with supersonic generator, or is equipped with connection in the pipeline for being equipped with strainer and drives
The strainer scraper plate of motivation structure, can effectively clean filter screen, so that it is guaranteed that filter efficiency and filter effect.
In the present embodiment, the top for stirring storage tank 32 slowly is connected by the first air pressure balance pipeline 322 and the first discharging channel 33
It connects, the top of feed storage tank 35 is connect by the second air pressure balance pipeline 352 with the second discharging channel 36, it can be ensured that stirs storage tank slowly
32 can smoothly export with the material for being fed storage tank 35, avoid can not be successfully output slurry due to there are draught head.
Above-described embodiments merely represent several embodiments of the utility model, the description thereof is more specific and detailed,
But it should not be understood as limiting the scope of the patent of the utility model.It should be pointed out that for the common of this field
For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to
In the protection scope of the utility model.Therefore, the scope of protection shall be subject to the appended claims for the utility model patent.
Claims (7)
1. a kind of processing conveying system of superfine powder engineering, which is characterized in that including be sequentially connected the module that feeds intake (10), slurrying
Module (20) and conveyor module (30)；
The conveyor module (30) includes the first conveying channel (31), is connected on first conveying channel (31) and several stirs slowly
Storage tank (32), the speed of agitator for stirring storage tank (32) slowly are 5~40r/min, and described stir slowly storage tank (32) pass through the first discharging
Road (33) is connected with the second conveying channel (34), and several feed storage tanks (35), institute are connected on second conveying channel (34)
The output end for stating feed storage tank (35) is connected with the second discharging channel (36)；
Described stir slowly is equipped with the first deaeration filter mechanism (321) between storage tank (32) and first conveying channel (31), described
It is fed between storage tank (35) and second discharging channel (36) and is equipped with the second deaeration filter mechanism (351), first conveying is logical
The both ends in road (31) are connected separately with the first cleaning dispatching station (311) and the first recycle bin (312), second conveying channel
(34) both ends are connected separately with the second cleaning dispatching station (341) and the second recycle bin (342).
2. a kind of processing conveying system of superfine powder engineering according to claim 1, which is characterized in that the module that feeds intake
It (10) include at least one feeding station (11), the output end of the feeding station (11) passes through described in dynamic measuring mechanism (12) connection
Slurrying module (20).
3. a kind of processing conveying system of superfine powder engineering according to claim 2, which is characterized in that the module that feeds intake
It (10) further include anti-fugitive dust negative pressure generating mechanism (13), the output end connection of the anti-fugitive dust negative pressure generating mechanism (13) is described dynamic
State metrological service (12) and the slurrying module (20).
4. a kind of processing conveying system of superfine powder engineering according to claim 1, which is characterized in that the slurrying module
It (20) include field wetting mechanism (21), fluctuation mixed organization (22) and cladding pulping mechanism (23) set gradually.
5. a kind of processing conveying system of superfine powder engineering according to claim 1, which is characterized in that first cleaning
Dispatching station (311) and second cleaning dispatching station (341) are dry ice dispatching station or rotating wash bowl dispatching station.
6. a kind of processing conveying system of superfine powder engineering according to claim 1, which is characterized in that first deaeration
Filter mechanism (321) and the second deaeration filter mechanism (351) include centrifugal defoaming machine, the input of the centrifugal defoaming machine
End is equipped with filter screen.
7. a kind of processing conveying system of superfine powder engineering according to claim 1, which is characterized in that described to stir storage tank slowly
(32) top is connect by the first air pressure balance pipeline (322) with first discharging channel (33), the feed storage tank (35)
Top connect with second discharging channel (36) by the second air pressure balance pipeline (352).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821337969.8U CN209188694U (en) | 2018-08-16 | 2018-08-16 | A kind of processing conveying system of superfine powder engineering |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821337969.8U CN209188694U (en) | 2018-08-16 | 2018-08-16 | A kind of processing conveying system of superfine powder engineering |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209188694U true CN209188694U (en) | 2019-08-02 |
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ID=67405053
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821337969.8U Active CN209188694U (en) | 2018-08-16 | 2018-08-16 | A kind of processing conveying system of superfine powder engineering |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209188694U (en) |
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2018
- 2018-08-16 CN CN201821337969.8U patent/CN209188694U/en active Active
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