CN104857887B - A kind of auto feed of high viscosity coating fluid, dispensing, feeding system - Google Patents
A kind of auto feed of high viscosity coating fluid, dispensing, feeding system Download PDFInfo
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- CN104857887B CN104857887B CN201510211236.4A CN201510211236A CN104857887B CN 104857887 B CN104857887 B CN 104857887B CN 201510211236 A CN201510211236 A CN 201510211236A CN 104857887 B CN104857887 B CN 104857887B
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Abstract
The invention discloses a kind of auto feed of high viscosity coating fluid, dispensing, feeding system, including silicone oil high-level storage groove, it is characterized in that the input port of the silicone oil high-level storage groove is connected by the viscous pump of height with silicone oil tank car, the delivery outlet of the silicone oil high-level storage groove is connected with the first input port of silicone oil dissolving tank, second input port of silicone oil dissolving tank is also connected with gasoline cistern and recovery gasoline cistern, the delivery outlet of silicone oil dissolving tank is connected with reacting the silicone oil input port of agitator tank, reaction agitator tank also sets up reagent input port and is connected with reagent pot, the delivery outlet of reaction agitator tank is connected with intermediate buffer tank, the delivery outlet of intermediate buffer tank is connected by flowmeter with coating pan, agitating device is all provided with silicone oil dissolving tank and reaction agitator tank.The advantage of the invention is that overcome manually is wasted time and energy with spoon charging, high viscosity liquid automatic charging is fully achieved.Because prosthetic operates, overcome and electrostatic is produced in manual operation, eliminate safe hidden trouble.
Description
Technical field
The present invention relates to mould release membrance coating apparatus, relate in particular to a kind of auto feed of high viscosity coating fluid, dispensing,
Feeding system.
Background technology
Mould release membrance is coated with industry, and silicone oil, solvent and reaction promoter oil need to by a certain percentage be configured, is then placed in by coating fluid
In coating chute, used for coating machine.Industry common practice is to use 200L barreled silicone oil, after opening, after being dug out with spoon, is put
Enter container, then extracted from 200L drummed gasolines gasoline out with air pump, then add and the auxiliary agent weighed up is added into container, start
Agitator stirs.After mixing time arrives, before the material for preparing shifts coater head onto with dolly, with pipe or manually coating fluid hopper is sent to
In, used for coating machine.Manually operation is completed substantially for this feeding, dispensing, feed, and workload is big, wastes time and energy.Dispensing ring
Border is poor, and ground oil stain is more, and solvent volatilization directly affects enterprise employee health.Raw material availability is low, is manually dug with spoon, and bottom has residual
Stay, using incomplete.Proportioning accuracy is poor, and manual weighing is affected by human factors, and unavoidable error is big, and it is linear poor to repeat again, causes
Coating quality is unstable, directly affects product quality.Artificial dispensing is because electrostatic etc. acts on, and there is also potential safety hazard.
The content of the invention
It is an object of the invention to provide a kind of auto feed of high viscosity coating fluid, dispensing, feeding system.
To achieve the above object, technical scheme is as follows：A kind of auto feed of high viscosity coating fluid, dispensing,
Feeding system, including silicone oil high-level storage groove, it is characterised in that the input port of the silicone oil high-level storage groove passes through the viscous pump of height and silicone oil
Tank car connects, and the delivery outlet of the silicone oil high-level storage groove is connected with the first input port of silicone oil dissolving tank, and the of silicone oil dissolving tank
Two input ports are also connected with gasoline cistern and recovery gasoline cistern, the silicone oil input port of the delivery outlet and reaction agitator tank of silicone oil dissolving tank
Connection, reaction agitator tank also set up reagent input port and are connected with reagent pot, and the delivery outlet and intermediate buffer tank for reacting agitator tank connect
Connect, the delivery outlet of intermediate buffer tank is connected by flowmeter with coating pan, is respectively provided with and is stirred in silicone oil dissolving tank and reaction agitator tank
Mix device.Silicon oil mixing tank and reagent pot are respectively provided with electronic scale.
The bottom of the silicone oil high-level storage groove passes sequentially through ball valve, first flowmeter and the first magnetic valve and silicone oil dissolving tank
Connection, the first flowmeter connect with the first quantitative controller, the control of first quantitative controller and the first magnetic valve
End connection.The gasoline cistern passes sequentially through stop valve, pneumatic diaphragm pump, second flowmeter and second solenoid valve and silicone oil dissolving tank
Connection, the second flowmeter connect with the second quantitative controller, the control of second quantitative controller and second solenoid valve
End connection.The recovery gasoline cistern passes sequentially through oil mixing with water alarm, stop valve, pneumatic diaphragm pump, the 3rd flowmeter and the
Three magnetic valves are connected with silicone oil dissolving tank, the 3rd flowmeter and the 3rd the quantitative controller connection, the described 3rd quantitative control
Device is connected with the control terminal of the 3rd magnetic valve.The delivery outlet of the silicon oil mixing tank passes sequentially through stop valve, pneumatic diaphragm pump,
Four flowmeters and the 4th magnetic valve are connected with reaction agitator tank, the 4th flowmeter and the 4th the quantitative controller connection, described
4th quantitative controller is connected with the control terminal of the 4th magnetic valve.Reagent pot passes through stop valve, the 5th flowmeter and the 5th electromagnetism
Valve connects, wherein the 5th flowmeter and the connection of the 5th quantitative controller, the 5th quantitative controller and the 5th magnetic valve
Control terminal connection.
The auto feed of coating machine high viscosity coating fluid of the present invention, dispensing, feeding system have advantages below：
1 overcome manually with spoon charging waste time and energy, fully achieve high viscosity liquid automatic charging;
2 flow measurement automatic control systems, metering is accurate, and automatic degree is high；Electronic scale review monitoring, is corrected in time.
3 dissolving tank predissolves act on, and make concentration evenly, overcome reaction dead angle.
4 PLC control systems realize reaction metering, charging sequence, the control of the computer program in reaction time, dispensing accuracy
Height, it is good to repeat again property, the shortcomings of the dispensing reproducibility difference for overcoming manual operation to bring.
5 by drummed gasoline and barreled silicone oil, is changed to tank car dress and uses, overcomes because barreled seeps water, influence quality, and raw material
Use, in the absence of every barrel of residue, save raw material, packaging is saved.
6 dispensing environment improve at all, favourable enterprise employee health.
7, because prosthetic operates, overcome and electrostatic are produced in manual operation, eliminate safe hidden trouble.
Brief description of the drawings
Fig. 1 is the structural representation of one embodiment of the invention.
Fig. 2 is the structural representation of auto feed unit in Fig. 1.
Fig. 3 is the structural representation of dosing in Fig. 1.
Fig. 4 is the structural representation of feed unit in Fig. 1.
Embodiment
A kind of auto feed of high viscosity coating fluid, dispensing, feeding system, including the dosage unit set gradually, dispensing
Unit and feed unit, the dosage unit include silicone oil high-level storage groove 1, it is characterised in that the silicone oil high-level storage groove 1 it is defeated
Entrance is connected by the viscous pump 2 of height with silicone oil tank car, the delivery outlet of the silicone oil high-level storage groove 1 and the first of silicone oil dissolving tank 3 defeated
Entrance connects, the second input port of silicone oil dissolving tank 3 also with gasoline cistern 4 and reclaiming gasoline cistern 5 and being connected, silicone oil dissolving tank 3 it is defeated
Export and be connected with reacting the silicone oil input port of agitator tank 6, reaction agitator tank 6 also sets up reagent input port and is connected with reagent pot 7, instead
The delivery outlet of agitator tank 6 is answered to be connected with intermediate buffer tank 8, the delivery outlet of intermediate buffer tank 8 is connected by flowmeter 9 and coating tank 10
Connect, agitating device is all provided with silicone oil dissolving tank and reaction agitator tank.Silicon oil mixing tank and reagent pot are respectively provided with electronic scale 13.Apply
Cloth tank 10 is also connected by pneumatic diaphragm pump 11 with circulating tank 12.
Fig. 2 is the structural representation of auto feed unit in Fig. 1.As shown in Fig. 2 the auto feed unit of the present invention includes
Silicone oil high-level storage groove 1, the bottom of the silicone oil high-level storage groove 1 pass sequentially through ball valve 14, the magnetic valve of first flowmeter 15 and first
16 are connected with silicone oil dissolving tank 3, and the quantitative controller 17 of first flowmeter 15 and first connects, first quantitative controller
17 are connected with the control terminal of the first magnetic valve 16.The gasoline cistern 4 passes sequentially through stop valve 18, pneumatic diaphragm pump 11, second
Gauge 19 and second solenoid valve 20 are connected with silicone oil dissolving tank 3, and the quantitative controller 21 of second flowmeter 19 and second connects,
Second quantitative controller 21 is connected with the control terminal of second solenoid valve 20.The recovery gasoline cistern 5 passes sequentially through profit and mixed
Alarm 22, stop valve 18, pneumatic diaphragm pump 11, the 3rd flowmeter 23 and the 3rd magnetic valve 24 is closed to be connected with silicone oil dissolving tank 3,
3rd flowmeter 23 and the 3rd quantitative controller 25 connect, the control of the 3rd quantitative controller 25 and the 3rd magnetic valve 24
End connection processed.The delivery outlet of the silicon oil mixing tank passes sequentially through stop valve 18, pneumatic diaphragm pump 11, the 4th flowmeter 26 and
Four magnetic valves 27 are connected with reaction agitator tank 6, and the 4th flowmeter 26 and the 4th quantitative controller 28 connect, and the described 4th is fixed
Amount controller 28 is connected with the control terminal of the 4th magnetic valve 27.
The input port of the gasoline cistern 4 conveys the 120# gasoline of solvent tank car by pneumatic diaphragm pump 11, and reclaims vapour
The input port of oil tank 5 then conveys solvent recovery gasoline by pneumatic diaphragm pump 11.
Viscous silicone fluid conveys to exist for viscosity（25℃ CS）：High viscous pump, enters in the conveying of 1000000~500 all creation materials
Row automatic pumping.Silicone oil in tank car is transported to silicone oil high-level storage groove by the viscous pump of height, overcomes what barreled silicone oil was manually fed with spoon
Mode, manpower is saved, avoids waste of material.
Silicone oil, 120# gasoline, the conveying of solvent recovery gasoline, metering, dispensing are by electronic scale, flowmeter, flow quantitative
Device processed, magnetic valve, ball valve, stainless steel pipes, dissolving tank diameter composition.
Agitating device is set in silicone oil dissolving tank, and silicone oil dissolving tank plays predissolve effect, silicone oil and gasoline is had enough
Dissolution time, overcome that conventional silicone oil and gasoline dissolution time is short, and concentration distribution is uneven, cause silicone oil reaction unbalanced, apply
The problem of dry silicon amount of cloth is uneven.
Fig. 3 is the structural representation of dosing in Fig. 1.As illustrated, dosing includes two reaction agitator tanks, instead
Answer and agitating device is set in agitator tank 6, the bottom of reaction agitator tank 6 sets delivery outlet, and the delivery outlet passes through pneumatic diaphragm pump 11
It is connected with intermediate buffer tank 8, the top of reaction agitator tank 6 is provided with silicone oil input port and reagent input port, reaction agitator tank 6
Silicone oil input port receives the silicone oil raw material from silicone oil dissolving tank 3, and the reagent input port of reaction agitator tank 6 is then received from reagent
The reagent of tank 7, reagent pot 7 set electronic scale 13, and the bottom of reagent pot 7 sets outlet, and the outlet passes through stop valve the 18, the 5th
The magnetic valve 30 of flowmeter 29 and the 5th connects, wherein the 5th flowmeter 29 and the 5th quantitative controller 31 connect, described
Five quantitative controllers 31 are connected with the control terminal of the 5th magnetic valve 30.
Dosing is by reaction agitator tank, reagent pot, flowmeter, stop valve, magnetic valve, flow controller, pneumatic stirring
Device, membrane pump, stainless steel pipes composition.Three reagent pots are set in the present invention altogether, are respectively configured to provide three kinds of reagents.Dissolve
Silicone oil adds reaction tank diameter by membrane pump and measurement controller, and three kinds of reaction reagents sequentially add reaction tank diameter, described anti-
Answer each input port of agitator tank that stop valve is set, the dosing also sets up PLC control unit 32, and the PLC controls are single
Member 32 is connected with the agitator air in the stop valve 18, electronic scale 13 and reaction agitator tank, for controlling addition programs
And mixing time, electronic scale carry out dosage review, prevent measuring error.
Fig. 4 is the structural representation of feed unit in Fig. 1.The feed unit includes intermediate buffer tank 33, and the centre is slow
The top for rushing tank 33 sets input port to be connected with dosing, and the bottom of intermediate buffer tank 33 is discharging opening, and upper end sets an overflow
Mouthful, bottom discharge mouth is connected by flowmeter 35 with coating pan 34.As liquid is excessive, by upper end overfall, pass through flowmeter
35 are connected with coating pan 34, and overfall effect in upper end is after liquid such as fills surge tank, can be dredged by overfall and flowmeter
To coating pan, and spillway discharge can be measured.The side of coating pan 34 sets a circulating tank 36, the coating pan set a delivery outlet and
One input port, circulated between delivery outlet and input port by circulating tank 36 and pneumatic diaphragm pump 11, prevent local precuring.
The silicone oil configured gets to intermediate buffering groove by membrane pump, and each coating line is assigned to by intermediate buffering groove
Coating line use device, coating line use device is by flowmeter, stop valve, circulating tank, pneumatic diaphragm valve, stainless steel pipes group
Into.Operating personnel can record from flowmeter and often roll up silicon oil dosage, and calculate the dry silicon amount of every square meter, overcome conventional one
The dry silicon amount usage amount that class can just count.
Claims (7)
1. a kind of auto feed of high viscosity coating fluid, dispensing, feeding system, including silicone oil high-level storage groove, it is characterised in that institute
The input port for stating silicone oil high-level storage groove is connected by the viscous pump of height with silicone oil tank car, the delivery outlet and silicone oil of the silicone oil high-level storage groove
The first input port connection of dissolving tank, the second input port of silicone oil dissolving tank are also connected with gasoline cistern and recovery gasoline cistern, silicone oil
The delivery outlet of dissolving tank is connected with reacting the silicone oil input port of agitator tank, and reaction agitator tank also sets up reagent input port and reagent pot
Connection, the delivery outlet for reacting agitator tank are connected with intermediate buffer tank, and the delivery outlet of intermediate buffer tank passes through flowmeter and coating pan
Agitating device is all provided with connection, silicone oil dissolving tank and reaction agitator tank.
2. auto feed as claimed in claim 1, dispensing, feeding system, it is characterised in that silicon oil mixing tank and reagent pot are equal
Electronic scale is set.
3. auto feed as claimed in claim 1, dispensing, feeding system, it is characterised in that the bottom of the silicone oil high-level storage groove
Portion passes sequentially through ball valve, first flowmeter and the first magnetic valve and is connected with silicone oil dissolving tank, and the first flowmeter and first is determined
Amount controller is connected, and first quantitative controller is connected with the control terminal of the first magnetic valve.
4. auto feed as claimed in claim 1, dispensing, feeding system, it is characterised in that the gasoline cistern, which passes sequentially through, to be cut
Only valve, pneumatic diaphragm pump, second flowmeter and second solenoid valve are connected with silicone oil dissolving tank, and the second flowmeter and second is determined
Amount controller connects, and the control terminal of second quantitative controller and second solenoid valve connects.
5. auto feed as claimed in claim 1, dispensing, feeding system, it is characterised in that the recovery gasoline cistern leads to successively
Cross oil mixing with water alarm, stop valve, pneumatic diaphragm pump, the 3rd flowmeter and the 3rd magnetic valve to be connected with silicone oil dissolving tank, institute
The 3rd flowmeter and the connection of the 3rd quantitative controller are stated, the 3rd quantitative controller is connected with the control terminal of the 3rd magnetic valve.
6. auto feed as claimed in claim 1, dispensing, feeding system, it is characterised in that the output of the silicon oil mixing tank
Mouth passes sequentially through stop valve, pneumatic diaphragm pump, the 4th flowmeter and the 4th magnetic valve and is connected with reaction agitator tank, the 4th stream
Gauge and the connection of the 4th quantitative controller, the 4th quantitative controller are connected with the control terminal of the 4th magnetic valve.
7. auto feed as claimed in claim 1, dispensing, feeding system, it is characterised in that reagent pot passes through stop valve, the 5th
Flowmeter and the connection of the 5th magnetic valve, wherein the 5th flowmeter and the connection of the 5th quantitative controller, the 5th quantitative
Device processed is connected with the control terminal of the 5th magnetic valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510211236.4A CN104857887B (en) | 2015-04-29 | 2015-04-29 | A kind of auto feed of high viscosity coating fluid, dispensing, feeding system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510211236.4A CN104857887B (en) | 2015-04-29 | 2015-04-29 | A kind of auto feed of high viscosity coating fluid, dispensing, feeding system |
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| CN104857887A CN104857887A (en) | 2015-08-26 |
| CN104857887B true CN104857887B (en) | 2018-01-30 |
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| CN201510211236.4A Active CN104857887B (en) | 2015-04-29 | 2015-04-29 | A kind of auto feed of high viscosity coating fluid, dispensing, feeding system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106244360B (en) * | 2016-09-18 | 2019-06-04 | 广州立白企业集团有限公司 | A kind of liquid detergent serialization process of flexible production and equipment |
| EP3511683B1 (en) * | 2018-01-10 | 2022-04-20 | ABB France | Method for controlling a metering installation |
| CN110010918B (en) * | 2019-05-06 | 2023-05-16 | 中国华能集团清洁能源技术研究院有限公司 | PET silicone oil membrane recycling device and method for producing molten carbonate fuel cell membrane |
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| EP0482579B1 (en) * | 1990-10-22 | 1997-01-08 | Reinhardt-Technik GmbH & Co. | Method and device for proportioning in particular a high viscous mixture with one or more components |
| JP2002514971A (en) * | 1998-02-13 | 2002-05-21 | レナー ド ポント ティンタス オートモーティバス エ インダストリアイズ エスエイ | Manufacture of paints for automobiles |
| JP3980953B2 (en) * | 2001-07-12 | 2007-09-26 | タツモ株式会社 | Liquid feeding device for high viscosity fluid using pressurized tank |
| CN201395507Y (en) * | 2009-05-09 | 2010-02-03 | 叶舟 | Silicone oil automatic quantitative priming device |
| EP2163314A2 (en) * | 2008-09-15 | 2010-03-17 | Nordson Corporation | Liquid material dispenser |
| CN102513271A (en) * | 2011-12-14 | 2012-06-27 | 奇瑞汽车股份有限公司 | Automatic feeding system and coating machine |
| CN204724117U (en) * | 2015-04-29 | 2015-10-28 | 江苏优珀斯材料科技有限公司 | A kind of auto feed of high viscosity coating fluid, batching, feeding system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW590795B (en) * | 2002-04-17 | 2004-06-11 | Rohm & Haas | An automated system and process for the preparation of a high viscosity fluid formulation |
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2015
- 2015-04-29 CN CN201510211236.4A patent/CN104857887B/en active Active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0482579B1 (en) * | 1990-10-22 | 1997-01-08 | Reinhardt-Technik GmbH & Co. | Method and device for proportioning in particular a high viscous mixture with one or more components |
| JP2002514971A (en) * | 1998-02-13 | 2002-05-21 | レナー ド ポント ティンタス オートモーティバス エ インダストリアイズ エスエイ | Manufacture of paints for automobiles |
| JP3980953B2 (en) * | 2001-07-12 | 2007-09-26 | タツモ株式会社 | Liquid feeding device for high viscosity fluid using pressurized tank |
| EP2163314A2 (en) * | 2008-09-15 | 2010-03-17 | Nordson Corporation | Liquid material dispenser |
| CN201395507Y (en) * | 2009-05-09 | 2010-02-03 | 叶舟 | Silicone oil automatic quantitative priming device |
| CN102513271A (en) * | 2011-12-14 | 2012-06-27 | 奇瑞汽车股份有限公司 | Automatic feeding system and coating machine |
| CN204724117U (en) * | 2015-04-29 | 2015-10-28 | 江苏优珀斯材料科技有限公司 | A kind of auto feed of high viscosity coating fluid, batching, feeding system |
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| CN104857887A (en) | 2015-08-26 |
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