CN204261657U - A kind of microballoon High-efficient Production system - Google Patents
A kind of microballoon High-efficient Production system Download PDFInfo
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- CN204261657U CN204261657U CN201420719875.2U CN201420719875U CN204261657U CN 204261657 U CN204261657 U CN 204261657U CN 201420719875 U CN201420719875 U CN 201420719875U CN 204261657 U CN204261657 U CN 204261657U
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- kettle
- emulsifying
- motor
- production system
- efficient production
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Abstract
The utility model discloses a kind of microballoon High-efficient Production system, comprise control centre, air compression plant and the dissolver connected successively, emulsifier unit, sedimentation device; Dissolver comprises still preheater and dissolution kettle, program heating and cooling fuel tank, peristaltic pump that emulsifier unit comprises emulsifying kettle and is connected with emulsifying kettle respectively; Sedimentation device comprises flow tank and connected intelligent output equipment, and air compression plant is for controlling the unlatching of still preheater, dissolution kettle and emulsifying kettle and closed, and control centre is for the conveying of the operation and material that control each device.This security of system, energy-saving and environmental protection, efficient, the automatic continuous production that can realize uniform particle diameter microballoon, have good economy, society and environmental benefit.
Description
Technical field
The utility model relates to microballoon production field, is specially a kind of microballoon High-efficient Production system.
Background technology
Microballoon is widely used in separating medium, pharmaceutical carrier and cosmetics.The microspheres of existing industrialization is all that a reactor has been stirred by common heating substantially, the deficiencies such as this mode of production life period and cost of labor is high, production efficiency is low, utilization rate of equipment and installations is low, energy consumption is high, seriously polluted, prepared microspheres quality difference.In view of the above circumstances, be necessary to design that a kind of automaticity is high, safety, energy-saving and environmental protection, efficient, uniform particle diameter microballoon continuous process system.
Utility model content
It is high that the purpose of this utility model is to provide a kind of automaticity, and quality is good, efficient, the microballoon production system of uniform particle diameter.
The technical scheme of this novel employing is as follows: a kind of microballoon High-efficient Production system, comprises control centre, air compression plant and the dissolver connected successively, emulsifier unit, sedimentation device; Described dissolver comprises still preheater and dissolution kettle, is respectively used to feed liquid preheating, dissolves heating; Described emulsifier unit is used for feed liquid emulsification to be frozen into spherical, it program heating and cooling fuel tank, peristaltic pump of comprising emulsifying kettle and being connected with emulsifying kettle respectively; Described sedimentation device comprises flow tank and connected intelligent output equipment, and described air compression plant is for controlling the unlatching of still preheater, dissolution kettle and emulsifying kettle and closed, and described control centre is for the conveying of the operation and material that control each device.
Preferably, be provided with implosion guard between described control centre and all the other devices and observe wall.
Wherein, described still preheater comprises kettle, far-infrared heater, kettle cover, motor, paddle, thermometer, baiting valve, kettle lower end is located at by described far-infrared heater, described kettle cover is positioned at kettle upper end, described kettle cover is provided with charge door, safety valve, column condenser and observation panel, described paddle is connected with motor and stretches in kettle, and described thermometer is positioned at kettle side and inserts kettle, and described baiting valve is positioned at kettle bottom.
Wherein, described dissolution kettle comprises kettle, far-infrared heater, kettle cover, motor, agitatortype, thermometer, baiting valve, kettle lower end is located at by described far-infrared heater, described kettle cover is positioned at kettle upper end, described kettle cover is provided with charge door, safety valve, column condenser and observation panel, described agitatortype is connected with motor and stretches in kettle, and described thermometer is positioned at kettle side and inserts kettle, and described baiting valve is positioned at kettle bottom.
Wherein, described emulsifying kettle comprises kettle, far-infrared heater, kettle cover, motor, emulsifying head, paddle, thermometer, baiting valve, kettle lower end is located at by described far-infrared heater, described kettle lower end is provided with an inlet chuck, described kettle cover is positioned at kettle upper end, described kettle cover is provided with charge door, safety valve, column condenser and observation panel, described emulsifying head combines with paddle and is connected with motor and stretches in kettle, described thermometer is positioned at kettle side and inserts kettle, and described baiting valve is positioned at kettle bottom.
Wherein, described flow tank comprises that the casing, the casing top that are provided with charge door and discharging opening are provided with starter motor and buoy, lower box is provided with the paddle be with and controlled motor, described buoy is provided with density inductor and height sensors.
Wherein, described air compression plant comprises some air compressor unit, Compressed Gas storage tank and pneulift, and described pneulift is for controlling the kettle cover lifting of still preheater, dissolution kettle and emulsifying kettle.
After adopting technique scheme, the utility model has following beneficial effect:
1. control centre control the turnover opening and closing automatically to control gas and liquid of the valve of each system and material conveying, control each systematic parameter and observe each system cloud gray model and stable state reaches safety automation object.
2. install still preheater additional according to the dissolver of material characteristic design and realize whole system contact production, dissolution kettle can realize the rapid solution of high concentration material; Emulsifying kettle realizes the object of High-efficient Production high-quality high homogeneity microballoon; Sedimentation device, the zero-emission formula realizing the collection of material nil waste and waste liquid recycles.Each device adopts Far-infrared Heating mode to realize energy-conservation, environmental protection.
3. the scientific and reasonable layout of whole technological process finally reaches the automatic continuous production of safety, energy-saving and environmental protection, efficient, uniform particle diameter microballoon, improves production efficiency and utilization rate of equipment and installations, has good economy, society and environmental benefit.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of still preheater;
Fig. 3 is the structural representation of dissolution kettle;
Fig. 4 is the structural representation of emulsifier unit;
Fig. 5 is the structural representation of flow tank.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.
As shown in Figure 1, the utility model discloses a kind of microballoon High-efficient Production system, comprise control centre 1, air compression plant 2 and the dissolver 3 connected successively, emulsifier unit 6, sedimentation device 8.Dissolver 3 comprises still preheater 4 and dissolution kettle 5.Emulsifier unit 6 comprises emulsifying kettle 7, heating and cooling fuel tank 61, peristaltic pump 62.Sedimentation device 8 comprises flow tank 9, intelligent output equipment.Be provided with implosion guard between control centre 1 and all the other devices and observe wall 11, operating personnel only need at wall outer side operational control center 1, observe by implosion guard the working condition that the inner each device of body of wall observed by wall 11, achieve the automation of height, and reach the object of safety in production.Below make introductions all round the setting of each device and operation principle:
Air compression plant 2 is for controlling the unlatching of still preheater 4, dissolution kettle 5 and emulsifying kettle 7 and closed, and it comprises some air compressor unit, Compressed Gas storage tank and pneulift 21, with still preheater 4, dissolution kettle 5 and emulsifying kettle 7 with the use of.
Dissolver 3 comprises still preheater 4 and dissolution kettle 5, as Fig. 2, shown in 3, still preheater 4 and dissolution kettle 5 are equipped with kettle 41, 51, far-infrared heater 42, 52, kettle cover 43, 53, motor 44, 54, paddle 45, 55, thermometer 46, 56, baiting valve 47, 57, far-infrared heater 42, 52 are located at kettle 41, 51 lower ends, kettle cover 43, 53 are positioned at kettle 41, 51 upper ends, kettle cover 43, 53 are provided with charge door 431, 531, safety valve 432, 532, column condenser 433, 533, and observation panel 434, 534, paddle 45, 55 with motor 44, 54 connect and stretch into kettle 41, in 51, thermometer 46, 56 are positioned at kettle 41, 51 sides insert kettle 41, in 51, baiting valve 47, 57 are positioned at valve body 41, 51 bottoms.
The operation principle of dissolver 3 is: the solvent of still preheater 4 is added by charge door 43, heat through far-infrared heater 42, starter motor 44, paddle 45 solvent stirred in kettle 41 makes its thermally equivalent, by thermometer 46, temperature feedback is gone back to control centre, thus realize temperature constant state, constant and the safety of solvent is ensured by safety valve 432, column condenser 433 condensing reflux and mechanical seal, by the liquid condition in observation panel 434 observable still, the magnetic valve be connected with control centre 1 by baiting valve 47 controls solvent flow rate at regular time and quantity.The charge door 531 entering dissolution kettle 5 through baiting valve 47 after the solvent process of still preheater 4 completes adds dissolution kettle 5, add powder material again and enter dissolution kettle 5, drive agitatortype 55 Stirring to realize powder material in a solvent dispersed through motor 54, its heating and feedback procedure identical with the principle of still preheater 4.
Program heating and cooling fuel tank 61, peristaltic pump 62 that emulsifier unit 6 comprises emulsifying kettle 7 and is connected with emulsifying kettle 7 respectively, as shown in Figure 4.Emulsifying kettle 7 comprises kettle 71, far-infrared heater 72, kettle cover 73, motor 74, emulsifying head 75, paddle 76, thermometer 77, baiting valve 78, kettle 71 lower end is located at by far-infrared heater 72, kettle 71 lower end is provided with an inlet chuck 79, kettle cover 73 is positioned at kettle 71 upper end, kettle cover 73 is provided with charge door 731, safety valve 732, column condenser 733 and observation panel 734, emulsifying head 75 combines with paddle 76 and is connected with motor 74 and stretches in kettle 71, thermometer 77 is positioned at kettle 71 side and inserts kettle 71, and baiting valve 78 is positioned at valve body bottom.
The operation principle of emulsifier unit 6 is: the feed liquid of dissolution kettle 5 controls through baiting valve 57 charge door 731 entering emulsifying kettle 7, thermal medium enters inlet chuck 79 from the solenoid control of program heating and cooling fuel tank 61 through being connected with control centre 1, fed back by thermometer 77 again and realize heating feed liquid program, when thermometer 77 reaches programmed values, other solvents add in emulsifying kettle 7 through charge door through peristaltic pump 62 at regular time and quantity, drive emulsifying head 75 and paddle 76 to combine to realize emulsifying materials and dispersed through motor 74, after reaching certain hour, program heating and cooling fuel tank 61 is switched to programmed cooling pattern from program heating mode, realize feed liquid in still and solidify balling-up, by safety valve 732, column condenser 733 condensing reflux and mechanical seal ensure constant and the safety of solvent, by the liquid condition in observation panel 734 observable still, the magnetic valve be connected with control centre 1 by baiting valve 78 controls solvent flow rate at regular time and quantity.
The kettle cover 43,53,73 of still preheater 4, dissolution kettle 5, emulsifying kettle 7 is all connected with pneulift 21, and control centre 1 can control air compression plant thus control pneulift 21 to be mentioned by kettle cover 43,53,73 and be convenient to still preheater 4, dissolution kettle 5, the cleaning of emulsifying kettle 7 and the replacing of paddle 45,55,76.
Sedimentation device 8 comprises flow tank 9 and connected intelligent output equipment, as shown in Figure 5, flow tank 9 comprises that the casing 91, casing 91 top that are provided with charge door 92 and discharging opening 93 are provided with starter motor 94 and buoy 95, casing 91 bottom is provided with the paddle 97 be with and controlled motor 96, buoy 95 is provided with density inductor and height sensors.
The operation principle of sedimentation device 8 is: the charge door 92 of flow tank 9 is connected with the drain hole magnetic valve of emulsifying kettle 7, feed liquid enters flow tank 9 through the control of emulsifying kettle 7 baiting valve 78, starter motor 94 is opened control buoy 95 and is declined, density inductor when buoy 95 arrives different liquids layer on buoy is to control centre 1 feedback information, control centre 1 sends instruction and suspends starter motor 94, liquids recovery bucket is placed with below discharging opening 93, after liquids recovery bucket below discharging opening 93 is changed, control centre 1 sends information command makes starter motor 94 work on, when buoy 95 reaches solid layer, density inductor feeds back to information, control centre 1 sends instruction makes starter motor 94 stop, liquid adds from charge door 92, buoy 95 rises, when arriving setting height, height sensors is to control centre 1 feedback information, control centre 1 sends instruction to controlling motor 96, control motor 96 and drive paddle 97, realize solid dispersal in liquid, finally by intelligent output equipment, realize the filling of dispersion liquid, the recycle and reuse of encapsulation and solvent.
The whole technological process of the utility model design is scientific and reasonable, finally reaches the automatic continuous production of safety, energy-saving and environmental protection, efficient, uniform particle diameter microballoon, improves production efficiency and utilization rate of equipment and installations, have good economy, society and environmental benefit.
The above; be only the utility model preferably detailed description of the invention; but protection domain of the present utility model is not limited thereto; anyly be familiar with those skilled in the art in the technical scope that the utility model discloses; the change that can expect easily or replacement, all should be encompassed within protection domain of the present utility model.
Claims (7)
1. a microballoon High-efficient Production system, is characterized in that: comprise control centre (1), air compression plant (2) and the dissolver (3) connected successively, emulsifier unit (6), sedimentation device (8);
Described dissolver (3) comprises still preheater (4) and dissolution kettle (5), is respectively used to feed liquid preheating, dissolves heating; Described emulsifier unit (6) for feed liquid emulsification is frozen into spherical, it program heating and cooling fuel tank (61), peristaltic pump (62) of comprising emulsifying kettle (7) and being connected with emulsifying kettle (7) respectively; Described sedimentation device (8) comprises flow tank (9) and connected intelligent output equipment, described air compression plant (2) is for controlling the unlatching of still preheater (4), dissolution kettle (5) and emulsifying kettle (7) and closed, and described control centre (1) is for the conveying of the operation and material that control each device.
2. microballoon High-efficient Production system as claimed in claim 1, is characterized in that: be provided with implosion guard between described control centre (1) and all the other devices and observe wall (11).
3. microballoon High-efficient Production system as claimed in claim 1 or 2, it is characterized in that: described still preheater (4) comprises kettle (41), far-infrared heater (42), kettle cover (43), motor (44), paddle (45), thermometer (46), baiting valve (47), kettle (41) lower end is located at by described far-infrared heater (42), described kettle cover (43) is positioned at kettle (41) upper end, described kettle cover (43) is provided with charge door (431), safety valve (432), column condenser (433) and observation panel (434), described paddle (45) is connected with motor (44) and stretches in kettle (41), described thermometer (46) is positioned at kettle (41) side and inserts kettle (41), described baiting valve (47) is positioned at kettle (41) bottom.
4. microballoon High-efficient Production system as claimed in claim 3, it is characterized in that: described dissolution kettle (5) comprises kettle (51), far-infrared heater (52), kettle cover (53), motor (54), agitatortype (55), thermometer (56), baiting valve (57), kettle (51) lower end is located at by described far-infrared heater (52), described kettle cover (53) is positioned at kettle (51) upper end, described kettle cover (53) is provided with charge door (531), safety valve (532), column condenser (533) and observation panel (534), described agitatortype (55) is connected with motor (54) and stretches in kettle (51), described thermometer (56) is positioned at kettle (51) side and inserts kettle (51), described baiting valve (57) is positioned at kettle (51) bottom.
5. microballoon High-efficient Production system as claimed in claim 4, it is characterized in that: described emulsifying kettle (7) comprises kettle (71), far-infrared heater (72), kettle cover (73), motor (74), emulsifying head (75), paddle (76), thermometer (77), baiting valve (78), kettle (71) lower end is located at by described far-infrared heater (72), described kettle (71) lower end is provided with an inlet chuck (79), described kettle cover (73) is positioned at kettle (71) upper end, described kettle cover (73) is provided with charge door (731), safety valve (732), column condenser (733) and observation panel (734), described emulsifying head (75) combines with paddle (76) and is connected with motor (74) and stretches in kettle (71), described thermometer (77) is positioned at kettle (71) side and inserts kettle (71), described baiting valve (78) is positioned at kettle (71) bottom.
6. microballoon High-efficient Production system as claimed in claim 5, it is characterized in that: described flow tank (9) comprises that the casing (91), casing (91) top that are provided with charge door (92) and discharging opening (93) are provided with starter motor (94) and buoy (95), casing (91) bottom is provided with the paddle (97) be with and controlled motor (96), and described buoy (95) is provided with density inductor and height sensors.
7. microballoon High-efficient Production system as claimed in claim 6, it is characterized in that: described air compression plant (2) comprises some air compressor unit, Compressed Gas storage tank and pneulift (21), described pneulift (21) is for controlling the kettle cover (43 of still preheater (4), dissolution kettle (5) and emulsifying kettle (7), 53,73) be elevated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420719875.2U CN204261657U (en) | 2014-11-27 | 2014-11-27 | A kind of microballoon High-efficient Production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420719875.2U CN204261657U (en) | 2014-11-27 | 2014-11-27 | A kind of microballoon High-efficient Production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204261657U true CN204261657U (en) | 2015-04-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420719875.2U Expired - Fee Related CN204261657U (en) | 2014-11-27 | 2014-11-27 | A kind of microballoon High-efficient Production system |
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| CN (1) | CN204261657U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109092195A (en) * | 2018-10-10 | 2018-12-28 | 红云红河烟草(集团)有限责任公司 | It is a kind of for cigarette sugar fragrance preparation, use process high shear homogeneous system |
-
2014
- 2014-11-27 CN CN201420719875.2U patent/CN204261657U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109092195A (en) * | 2018-10-10 | 2018-12-28 | 红云红河烟草(集团)有限责任公司 | It is a kind of for cigarette sugar fragrance preparation, use process high shear homogeneous system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150415 Termination date: 20171127 |