CN207756087U - Nano-powder decentralized system - Google Patents
Nano-powder decentralized system Download PDFInfo
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- CN207756087U CN207756087U CN201721838592.XU CN201721838592U CN207756087U CN 207756087 U CN207756087 U CN 207756087U CN 201721838592 U CN201721838592 U CN 201721838592U CN 207756087 U CN207756087 U CN 207756087U
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Abstract
The utility model is related to a kind of nano-powder decentralized systems, including slightly mixing bucket and solvent tank, slightly mixed bucket is equipped with feeding port and is internally provided with blender, the outlet of solvent tank connects main pipeline, main pipeline is divided into two-way, the first via is connected to the top of thick mixed bucket by first pipe, and the second tunnel is connected with the first buffer barrel by second pipe；The outlet of thick mixed bucket is connected to the first buffer barrel top by third pipeline；The outlet of first buffer barrel is connected to the entrance of high-speed emulsifying machine by the 4th pipeline；The outlet of high-speed emulsifying machine is connected to the top of the second buffer barrel by the 6th pipeline；Second buffer barrel is connected to by the 7th pipeline and is filtered on unit.After using above system, under the premise of ensureing that nano-powder is evenly dispersed, it can realize that continous way production improves the degree of automation of nano-powder dispersion production, reduce time and the cost of labor of nano-powder dispersion, whole system is easy to operate, it is convenient and efficient, improve production efficiency.
Description
Technical field
The utility model is related to the production of nanometer film and manufacturing fields, more particularly, to a kind of nano-powder decentralized system.
Background technology
Nano-powder is also nano particle, refers generally to ultrafine particle of the size between 1~100nm, person it be super
Particulate, its scale are more than cluster and are less than general particle.Nano-powder material due to its head it is smaller have than
Larger specific surface area, absorption is easy to happen agglomeration mutually between them, and at present when using nano-powder material,
It needs to carry out decentralized processing to it.Currently, need to use nano-dispersed equipment when producing nano material, and existing equipment
There are many defects, operates excessively complexity in use and the time disperseed is also longer, it is relatively low so as to cause production efficiency,
So cost is accordingly higher；It is discontinuous production, and to again increase time cost, this significantly limits a nanometer material
Expect the extensive use in production field.
Invention content
The technical problem to be solved by the utility model is to provide a kind of production of continous way and nano-powders easy to operate
Decentralized system, it can save a large amount of time, reduce time cost.
The technical solution adopted by the utility model to solve its technical problems is that：A kind of nano-powder decentralized system, including
Slightly mixed bucket and solvent tank, the thick mixed bucket are equipped with feeding port and are internally provided with blender, the outlet of the solvent tank
Main pipeline is connected, the main pipeline is divided into two-way, and the first via is connected to the top of thick mixed bucket by first pipe, and the second tunnel is logical
It crosses second pipe and is connected with the first buffer barrel；The outlet of the thick mixed bucket is connected to by third pipeline in the first buffer barrel
Portion；The outlet of first buffer barrel is connected to the entrance of high-speed emulsifying machine by the 4th pipeline；The high speed emulsification
The outlet of machine is connected to the top of the second buffer barrel by the 6th pipeline；Second buffer barrel is connected to by the 7th pipeline
It filters on unit.
Further specifically, the main pipeline is equipped with the first valve and the first metering pump, the first pipe
Be equipped with the second valve, the second pipe be equipped with third valve, the third pipeline be equipped with the 4th valve and
Second metering pump, the 4th pipeline are equipped with the 5th valve, and the 6th pipeline is equipped with the 7th valve, and described the
Seven pipelines are equipped with the 8th valve and the 9th valve, and measuring tank is equipped between the 8th valve and the 9th valve.
Further specifically, the first valve, the 4th valve, the 5th valve and the 8th valve are manually-operated gate,
Second valve, third valve, the 7th valve and the 9th valve is automatic valve.
Further specifically, the outlet of the high-speed emulsifying machine is connected to the upper of the first buffer barrel by the 5th pipeline
Portion, is equipped with check valve on the 5th pipeline, and the check valve is logical to the flow direction of the first buffer barrel from high-speed emulsifying machine
Road.
Further specifically, being equipped with the 6th valve on the 5th pipeline, the 6th valve is automatic valve.
Further specifically, the system comprises for controlling the control that automatic valve opens and closes and metering pump acts
Unit processed.
Further specifically, the automatic valve uses pneumatic control valve.
Further specifically, being equipped with the low liquid level sensor being connect with control unit in the bottom of the thick mixed bucket.
Further specifically, being equipped with the high liquid level sensor being connect with control unit in second buffer barrel.
Further specifically, being equipped with leakage fluid dram in the thick mixed bottom of the barrel.
The utility model has the beneficial effects that：After using above system, before ensureing that nano-powder is evenly dispersed
It puts, can realize that continous way production improves the degree of automation of nano-powder dispersion production, reduce nano-powder dispersion
Time and cost of labor, whole system is easy to operate, convenient and efficient, improves production efficiency.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
In figure：1, solvent tank；2, bucket is slightly mixed；3, feeding port；4, blender；5, main pipeline；6, first pipe；7, the second pipe
Road；8, the first buffer barrel；9, third pipeline；10, the 4th pipeline；11, high-speed emulsifying machine；12, the 6th pipeline；13, the second buffering
Bucket；14, the 7th pipeline；15, the first valve；16, the first metering pump；17, the second valve；18, third valve；19, the 4th valve；
20, the second metering pump；21, the 5th valve；22, the 7th valve；23, the 8th valve；24, the 9th valve；25, measuring tank；26,
Five pipelines；27, check valve；28, the 6th valve；29, low liquid level sensor；30, high liquid level sensor；31, leakage fluid dram.
Specific implementation mode
The utility model is explained in detail below in conjunction with the accompanying drawings.
A kind of nano-powder decentralized system as shown in Figure 1, including bucket 2 and solvent tank 1 are slightly mixed, the thick mixed bucket 2 is set
There is feeding port 3 and be internally provided with blender 4, the outlet of the solvent tank 1 connects main pipeline 5, and the main pipeline 5, which divides, is
Two-way, the first via are connected to the top of thick mixed bucket 2 by first pipe 6, and the second tunnel is connected with the first buffering by second pipe 7
Bucket 8；The outlet of the thick mixed bucket 2 is connected to 8 top of the first buffer barrel by third pipeline 9；First buffer barrel 8
Outlet is connected to the entrance of high-speed emulsifying machine 11 by the 4th pipeline 10；The outlet of the high-speed emulsifying machine 11 passes through the 6th
Pipeline 12 is connected to the top of the second buffer barrel 13；Second buffer barrel 13 is connected to suction filtration unit by the 7th pipeline 14
On.
Solvent in solvent tank 1 is entered by main pipeline 5 and first pipe 6 in slightly mixed bucket 2, and nano-powder passes through
Feeding port 3 is put into slightly mixed bucket 2, is mixed solvent for the first time with nano-powder by slightly mixing the blender 4 inside bucket 2, is prepared
As the solution of high concentration；The solution of high concentration is entered by third pipeline 9 in the first buffer barrel 8, and solvent continues through second
Pipeline 7 enters in the first buffer barrel 8 to be continued to keep in after mixing with the solution of high concentration；Mixed solution passes through the 4th pipeline 10
Enter high-speed emulsifying machine 11, solution carries out final evenly dispersed in high-speed emulsifying machine 11, and solution after dispersion passes through the
Six pipelines 12 enter in the second buffer barrel 13 keep in, later by the 7th pipeline 14 enter filter unit in pressurization filter at
Film.
Based on above system, for the control of more convenient carry out solution concentration, increase on its corresponding pipeline
Add various valves and metering pump.The main pipeline 5 be equipped with the first valve 15 and the first metering pump 16, described first
Pipeline 6 is equipped with the second valve 17, and the second pipe 7 is equipped with third valve 18, and the third pipeline 9 is equipped with the
Four valves 19 and the second metering pump 20, the 4th pipeline 10 is equipped with the 5th valve 21, on the 6th pipeline 12
Equipped with the 7th valve 22, the 7th pipeline 14 is equipped with the 8th valve 23 and the 9th valve 24, in the 8th valve
Measuring tank 25 is equipped between door 23 and the 9th valve 24.In use, pass through solution after valve and metering pump control mixing
Concentration.
Further, the first valve 15, the 4th valve 19, the 5th valve 21 and the 8th valve 23 are hand-operated valve
Door, the second valve 17, third valve 18, the 7th valve 22 and the 9th valve 24 are automatic valve and automatic valve
Using pneumatic type.The system comprises for controlling the control unit that automatic valve opens and closes and metering pump acts.Together
When, can low liquid level sensor 29 be set in thick mixed bucket 2, setting high liquid level sensor 30, low liquid in the second buffer barrel 13
Liquid level signal is passed to control unit by level sensor 29 with high liquid level sensor 30, and control unit controls automatic valve and meter
Amount pump.Main pipeline 5 is opened by opening the first valve 15 manually, the second valve 17 and third valve are opened by control unit
18, solvent enters thick mixed bucket 2 by the second valve 17 and enters the first buffer barrel 8 from the third valve 18 on second pipe 7 simultaneously；
Slightly mixed solution enters the first buffer barrel 8 by the 4th valve 19 (opening manually) with the second metering pump 20 in mixed bucket 2
Interior mixing, the solution in the first buffer barrel 8 enters high-speed emulsifying machine 11 by the 5th valve 21 (opening manually), later from height
The outlet of fast mulser 11 enters the second buffer barrel 13 by the 7th valve 22, and the solution of the second buffer barrel 13 passes sequentially through the 8th valve
Door 23 (opening manually), measuring tank 25 and the 9th valve 24, which enter, to be filtered in unit.It is thick to mix the low of bucket 2 while operating
When liquid level sensor 29 senses that liquid level is relatively low, the throwing of solvent is increased by controlling the second valve 17 and the first metering pump 16
Enter；When solution in the second buffer barrel 13 is higher than high liquid level sensor 30, control unit controls the 7th valve 22 and closes, and stops
Convey solution.The first buffer barrel 8, the second buffer barrel 13 can also be given and slightly mixed bucket 2 is interior while adding high liquid level and low liquid level
Sensor, can preferably be controlled.
After above-mentioned stopping conveys solution to the second buffer barrel 13, the solution in pipeline will not flow, and be easy to make score
Nano-powder after dissipating is reunited again, therefore the outlet of high-speed emulsifying machine 11 is connected to the first buffer barrel 8 by the 5th pipeline 26
Top, is equipped with check valve 27 on the 5th pipeline 26, and the check valve 27 is buffered from high-speed emulsifying machine 11 to the first
Bucket flows to access；The 6th valve 28 is equipped on the 5th pipeline 26, the 6th valve 28 is automatic valve.When
When control unit controls the closing of the 7th valve 22, while opening the 6th valve 28 so that the outlet of high-speed emulsifying machine 11 passes through list
It is entered in the first buffer barrel 8 to valve 27 and the 6th valve 28, the solution in the first buffer barrel 8 is again introduced into high-speed emulsifying machine 11
Interior forming circuit so that solution ensures that the solution after dispersion will not reunite always in the process for carrying out dispersion storage, and
It can be used at any time.
It needs to clear up slightly mixing bucket 2 after a longer time of use, it will be remaining by the leakage fluid dram 31 that its bottom is arranged
After liquid discharge, shutdown can be facilitated to clear up.
Automatic valve replacement may be used in above-mentioned manually-operated gate, while can also carry out accurate control with control unit is crossed
System, can fully achieve automated production, save a large amount of man power and materials.Control unit can be real using PLC control program
It is existing.
The evenly dispersed of nano-powder not only can guarantee using the set decentralized system, but also the degree of automation can be improved,
Improve production efficiency.
It is emphasized that：The above is only the preferred embodiment of the present utility model, not appoints to the utility model
What formal limitation, any simple modification made by the above technical examples according to the technical essence of the present invention, etc.
With variation and modification, it is still within the scope of the technical solutions of the present invention.
Claims (10)
1. a kind of nano-powder decentralized system, including bucket (2) and solvent tank (1) are slightly mixed, the thick mixed bucket (2), which is equipped with, to feed intake
Mouthful (3) and it is internally provided with blender (4), which is characterized in that the outlet connection main pipeline (5) of the solvent tank (1), it is described
Main pipeline (5) be divided into two-way, the first via is connected to the top of thick mixed bucket (2) by first pipe (6), and the second tunnel passes through second
Pipeline (7) is connected with the first buffer barrel (8)；The outlet of the thick mixed bucket (2) is connected to the first buffering by third pipeline (9)
Bucket (8) top；The outlet of first buffer barrel (8) is connected to the import of high-speed emulsifying machine (11) by the 4th pipeline (10)
Place；The outlet of the high-speed emulsifying machine (11) is connected to the top of the second buffer barrel (13) by the 6th pipeline (12)；It is described
The second buffer barrel (13) by the 7th pipeline (14) be connected to filter unit on.
2. nano-powder decentralized system according to claim 1, which is characterized in that the main pipeline (5) is equipped with the
One valve (15) and the first metering pump (16), the first pipe (6) are equipped with the second valve (17), the described second pipe
Road (7) is equipped with third valve (18), and the third pipeline (9) is equipped with the 4th valve (19) and the second metering pump
(20), the 4th pipeline (10) is equipped with the 5th valve (21), and the 6th pipeline (12) is equipped with the 7th valve
(22), the 7th pipeline (14) is equipped with the 8th valve (23) and the 9th valve (24), in the 8th valve
(23) measuring tank (25) is equipped between the 9th valve (24).
3. nano-powder decentralized system according to claim 2, which is characterized in that first valve (15), the 4th
Valve (19), the 5th valve (21) and the 8th valve (23) are manually-operated gate, second valve (17), third valve
(18), the 7th valve (22) and the 9th valve (24) are automatic valve.
4. nano-powder decentralized system according to claim 1, which is characterized in that high-speed emulsifying machine (11) go out
Mouth is connected to the top of the first buffer barrel (8) by the 5th pipeline (26), and check valve is equipped on the 5th pipeline (26)
(27), the check valve (27) flows to access from high-speed emulsifying machine (11) to the first buffer barrel (8).
5. nano-powder decentralized system according to claim 4, which is characterized in that set on the 5th pipeline (26)
It is automatic valve to have the 6th valve (28), the 6th valve (28).
6. the nano-powder decentralized system according to claim 3 or 5, which is characterized in that the system comprises for controlling
Automatic valve opens and closes and the control unit of metering pump action.
7. the nano-powder decentralized system according to claim 3 or 5, which is characterized in that the automatic valve uses gas
Dynamic control valve.
8. nano-powder decentralized system according to claim 6, which is characterized in that in the bottom of the thick mixed bucket (2)
Equipped with the low liquid level sensor (29) being connect with control unit.
9. nano-powder decentralized system according to claim 6, which is characterized in that in second buffer barrel (13)
Equipped with the high liquid level sensor (30) being connect with control unit.
10. nano-powder decentralized system according to claim 1, which is characterized in that set in described thick mixed bucket (2) bottom
There is leakage fluid dram (31).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721838592.XU CN207756087U (en) | 2017-12-25 | 2017-12-25 | Nano-powder decentralized system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721838592.XU CN207756087U (en) | 2017-12-25 | 2017-12-25 | Nano-powder decentralized system |
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| Publication Number | Publication Date |
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| CN207756087U true CN207756087U (en) | 2018-08-24 |
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| CN201721838592.XU Active CN207756087U (en) | 2017-12-25 | 2017-12-25 | Nano-powder decentralized system |
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| CN (1) | CN207756087U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875961A (en) * | 2017-12-25 | 2018-04-06 | 苏州擎动动力科技有限公司 | Nano-powder decentralized system |
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2017
- 2017-12-25 CN CN201721838592.XU patent/CN207756087U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107875961A (en) * | 2017-12-25 | 2018-04-06 | 苏州擎动动力科技有限公司 | Nano-powder decentralized system |
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