CN202876730U - High-efficiency on-line stirring system - Google Patents
High-efficiency on-line stirring system Download PDFInfo
- Publication number
- CN202876730U CN202876730U CN 201220458953 CN201220458953U CN202876730U CN 202876730 U CN202876730 U CN 202876730U CN 201220458953 CN201220458953 CN 201220458953 CN 201220458953 U CN201220458953 U CN 201220458953U CN 202876730 U CN202876730 U CN 202876730U
- Authority
- CN
- China
- Prior art keywords
- slurry
- bearing block
- frequency converter
- granularity
- viscosity
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Colloid Chemistry (AREA)
Abstract
The utility model relates to a high-efficiency on-line stirring system for stirring and mixing materials. The high-efficiency on-line stirring system comprises a planetary dispersion vacuum stirring machine, a control system and a centrifugal emulsifying device equipped with a cooling system, wherein the planetary dispersion vacuum stirring machine is communicated with the centrifugal emulsifying device through a conveying pipeline, a conveying pump I, a return pipeline and a conveying pump II to form a circulation system; a thermocouple, a viscosity sensor and a granularity sensor are respectively arranged on the return pipeline and are respectively used for monitoring temperature, viscosity and granularity signals of slurry in the return pipeline and transmitting the signals to the control system; and the control system is used for carrying out data processing on the received signals and sends instructions to control running of the planetary dispersion vacuum stirring machine, the centrifugal emulsifying device, the conveying pump I, the conveying pump II and the cooling system. The high-efficiency on-line stirring system can monitor the viscosity, the granularity and the temperature of the slurry on line, so as to realize outer circulation deep homogenizing and emulsifying; the high-efficiency on-line stirring system has a good mixing effect; and the energy consumption and the equipment cost are greatly reduced.
Description
Technical field
The utility model relates to a kind of stirring system, particularly mixes the efficient online stirring system of usefulness in the industries such as a kind of chemical industry, electric slurry, lubricating grease, pharmacy, food.
Background technology
Planet disperses Zhen Kongjiaobanji ﹠amp; The emulsification vacuum mixer is applicable to mix all kinds of medium-high viscosity materials, is widely used in numerous industries such as chemical industry, electric slurry, lithium battery diaphragm slurry, coating, adhesive, cosmetics, lubricating grease, pharmacy, food.Above-mentioned mixed stirring device all can not be realized to slurry the monitoring of online granularity and viscosity, all be after waiting the slurry mixing to finish, just slurry is detected, can't grasp the variation of every theory index of material in the system, can't adjust according to the variation of actual conditions simultaneously the operational factor of equipment, when the material index changes the value of surpassing the expectation, can't monitor the process progress that goes wrong.Tend to like this occur the undesirable situation of mixing resultant, need to again do over again and carry out again the mix and blend operation, reduced operating efficiency, also increased energy consumption simultaneously.Because the difference of stirring material to be mixed, planet disperses Zhen Kongjiaobanji ﹠amp; Solid-liquid is carried out wetting, dispersion to the emulsification vacuum mixer and viscosity, the granularity that mixed slurry does not reach user's request can appear in emulsifying effectiveness, the slurries layering, the user has to increase the material mix and blend time, to reach its necessary requirement, increase work energy consumption and cost (directly, the indirectly) expense of equipment.
Summary of the invention
The technical problems to be solved in the utility model is: a kind of monitoring that realizes online viscosity, granularity and the temperature of slurry is provided, realize the efficient online stirring system of outer circulation degree of depth emulsifying, be somebody's turn to do efficient online stirring system good mixing effect, greatly reduce energy consumption and equipment cost, solved above-mentioned problems of the prior art.
The technical scheme that solves the problems of the technologies described above is: a kind of efficient online stirring system, comprise that planet disperses de-airing mixer, centrifugal emulsifier unit and control system, planet disperses the de-airing mixer discharge nozzle to be communicated with centrifugal emulsifier unit feed pipe by conveyance conduit and delivery pump I, centrifugal emulsifier unit discharge nozzle disperses the de-airing mixer feed pipe to be communicated with by Returning pipe and delivery pump II with planet, described centrifugal emulsifier unit is the supporting cooling system that is provided with also, be separately installed with thermocouple on the described Returning pipe, viscosity sensor and granularity sensor, thermocouple is used for the temperature signal of slurry in the monitoring Returning pipe, thermocouple is sent to control system by temperature controller with temperature signal, viscosity sensor and granularity sensor are respectively applied to monitor viscosity signal and the granularity signal of slurry in the Returning pipe, and viscosity signal and granularity signal be sent to control system, control system is used for the temperature signal to receiving, viscosity signal and granularity signal carry out data to be processed, send instruction control planet and disperse de-airing mixer, centrifugal emulsifier unit, the operation of delivery pump I and delivery pump II, the operation of sending simultaneously the instruction Controlled cooling system.
Described centrifugal emulsifier unit is vertical structure, comprise power set, transmission device, power transmission shaft, frame, the bearing block of jacket type, the slurry can of emulsification assembly and jacket type, described bearing block side is provided with the bearing block chuck, the bottom of bearing block chuck and top are respectively arranged with cooling liquid inlet I and cooling liquid outlet I, described slurry can side and bottom surface are provided with the slurry can chuck, slurry can chuck bottom surface and top, side are respectively arranged with cooling liquid inlet II and cooling liquid outlet II, cooling liquid inlet I, the cooling liquid outlet I, cooling liquid inlet II and cooling liquid outlet II are communicated with cooling system respectively; Described power transmission shaft is connected with power set by transmission device, bearing block is installed on the frame, slurry can is connected with bearing block, power transmission shaft passes bearing block and extends in the slurry can, described emulsification assembly is positioned at slurry can, the emulsification assembly comprises rotor and stator, stator is fixed on the bearing block, rotor is installed on the power transmission shaft and is positioned at stator, seal by being provided with sealing ring between stator lower end and the slurry can, form feed cavity between stator bottom and the slurry can, feed cavity is communicated with the feed pipe that passes the slurry can bottom, gap between stator side and the slurry can forms the discharging chamber, and stator side has the emulsifying homogeneous that is communicated with the discharging chamber discharging elongated hole of holding concurrently, and the discharging chamber is communicated with the discharge nozzle that passes the bearing block side and partly be positioned at the bearing block chuck.
Be provided with the spiral guiding plate I in the described bearing block chuck, be provided with the spiral guiding plate II in the slurry can chuck of described slurry can side.
Described control system comprises touch-screen, the PLC system, the frequency converter I, the frequency converter II, the frequency converter III, the water-cooled electromagnetic valve that is used for Controlled cooling system that is subjected to the magnetic valve I of PLC system control and controlled by the PLC system, described magnetic valve I and delivery pump I, the delivery pump II is electrically connected, described frequency converter I, the frequency converter II is disperseed respectively the revoluting motor of de-airing mixer with planet, disperse motor to be electrically connected, described frequency converter III is electrically connected with centrifugal emulsifier unit motor, described frequency converter I, the frequency converter II, the frequency converter III is connected described viscosity sensor with PLC system output interface respectively, the granularity sensor, temperature controller and touch-screen all link to each other with PLC system corresponding ports.
The efficient online stirring system of the utility model owing to adopt said structure, has following beneficial effect.
1. the utility model is realized the emulsifying of outer circulation type secondary deep, its process is online circulation, at Returning pipe thermocouple, viscosity sensor and granularity sensor are installed, the operator can realize the monitoring of online temperature, viscosity and granularity on the pulp flow pipeline, shorten material homogeneous incorporation time, enhance productivity, greatly reduce planet and disperse Zhen Kongjiaobanji ﹠amp; Work energy consumption and the equipment cost of centrifugal emulsifier unit have indirectly prolonged planet and have disperseed Zhen Kongjiaobanji ﹠amp; In the service life of centrifugal emulsifier unit, market prospects are wide, have the extremely strong market competitiveness.According to the numerical value of on-line monitoring, in real time the equipment operational factor is adjusted, thereby improved the equipment operating efficiency, shorten incorporation time, greatly reduce energy consumption and equipment cost.
2. the utility model has designed centrifugal emulsifier unit according to viscosity, the granularity requirements needs of enterprise to the mix and blend material.Powerful motor carries out High Rotation Speed to be made and turns, forms vacuum between the stator, and material sucks from rotor, stator bottom.Powerful kinetic energy makes rotor produce high linear velocity, make material between rotor, stator slotting through flying away after strong bump, fragmentation, centrifugal extruding, liquid layer friction, the strong shear, under the effect of multiple different directions power, produce powerful turbulent flow.Material produces stable emulsion through the depolymerization of certain hour iterative cycles, homogeneous, refinement, shearing under an amount of emulsifying agent and maturation process.The centrifugal emulsifier unit emulsify well of the utility model the slurries lamination can not occur.The user does not need to increase in addition the material mix and blend time, just can reach its required requirement, has further reduced work energy consumption and the cost of equipment.
3. the efficient online stirring system overall structure of the utility model is simple, and layout is succinctly reasonable, and occupation area of equipment is few.
Below, in conjunction with the accompanying drawings and embodiments the efficient online technical characterictic of stirring system of the utility model is further described.
Description of drawings
Fig. 1: the efficient online stirring system schematic diagram of the utility model.
Fig. 2: the control flow schematic diagram of the utility model control system.
Fig. 3: the utility model control system schematic diagram.
Fig. 4: the centrifugal emulsifier unit structural representation of the utility model.
Fig. 5: the member connection structure schematic diagrames such as the power transmission shaft of the centrifugal emulsifier unit of the utility model, bearing block, emulsification assembly and slurry can.
Fig. 6～Fig. 7: the stator structure schematic diagram of the centrifugal emulsifier unit of the utility model.
Fig. 6: upward view, Fig. 7: the main cutaway view of looking.
Fig. 8～Fig. 9: the rotor structure schematic diagram of the centrifugal emulsifier unit of the utility model.
The A-A cutaway view of Fig. 8: Fig. 9, Fig. 9: top view.
Figure 10～Figure 11: the bearing block structure schematic diagram of the centrifugal emulsifier unit of the utility model.
Figure 10: the main cutaway view, Figure 11 looked: top view.
Figure 12～Figure 13: the slurry can structural representation of the centrifugal emulsifier unit of the utility model.
Figure 12: the main cutaway view, Figure 13 looked: top view.
Figure 14～Figure 15: the ring structure schematic diagram of the centrifugal emulsifier unit of the utility model.
Figure 14: the main cutaway view, Figure 15 looked: top view.
Among the figure: the 1-planet disperses de-airing mixer, the 101-revoluting motor, and 102-disperses motor, the 2-control system, 21-touch-screen, 22-PLC system, 23-frequency converter I, 24-frequency converter II, 25-frequency converter III, 26-magnetic valve I, 27-magnetic valve II, 28-water-cooled electromagnetic valve, 3-delivery pump I, 4-conveyance conduit, 5-cooling system, the centrifugal emulsifier unit of 6-, the centrifugal emulsifier unit motor of 61-, 7-delivery pump II, 8-viscosity sensor, 9-granularity sensor, the 10-thermocouple, 11-temperature controller, 12-Returning pipe, 13-petrol station motor, the 14-vaccum pump motor.
The 61-power set, 62-transmission device, 63-power transmission shaft, 64-frame, the 65-bearing block, 651-cooling liquid outlet I, 652-bearing block chuck, 653-cooling liquid inlet I, 654-spiral guiding plate I, 66-emulsification assembly, 661-stator, the 6611-emulsifying homogeneous discharging elongated hole of holding concurrently, the 662-rotor, 67-sealing ring, 68-slurry can, 681-slurry can chuck, 682-cooling liquid outlet II, 683-spiral guiding plate II, 684-cooling liquid inlet II, 69-feed pipe, 610-discharge nozzle.
The specific embodiment
Embodiment one: a kind of efficient online stirring system, as shown in Figure 1, comprise that planet disperses de-airing mixer 1, centrifugal emulsifier unit 6 and control system 2, planet disperses the de-airing mixer discharge nozzle to be communicated with centrifugal emulsifier unit feed pipe by conveyance conduit 4 and delivery pump I 3, centrifugal emulsifier unit discharge nozzle disperses the de-airing mixer feed pipe to be communicated with by Returning pipe 12 and delivery pump II 7 with planet, described centrifugal emulsifier unit is the supporting cooling system 5 that is provided with also, be separately installed with thermocouple 10 on the described Returning pipe 12, viscosity sensor 8 and granularity sensor 9, thermocouple is used for the temperature signal of slurry in the monitoring Returning pipe, thermocouple is sent to control system by temperature controller 11 with temperature signal, viscosity sensor and granularity sensor are respectively applied to monitor viscosity signal and the granularity signal of slurry in the Returning pipe, and viscosity signal and granularity signal be sent to control system, control system is used for the temperature signal to receiving, viscosity signal and granularity signal carry out data to be processed, control system is sent instruction control planet dispersion de-airing mixer according to viscosity signal and granularity signal, centrifugal emulsifier unit, the operation of instruction Controlled cooling system is sent in the operation of delivery pump I and delivery pump II, control system simultaneously according to temperature signal.
Described centrifugal emulsifier unit 6 is that vertical structure is (referring to Fig. 4-Figure 15), comprise power set 61(motor), transmission device 62(shaft coupling), power transmission shaft 63, frame 64, the bearing block 65 of jacket type, the slurry can 68 of emulsification assembly 66 and jacket type, described bearing block side is provided with bearing block chuck 652, be provided with spiral guiding plate I 654 in the described bearing block chuck, the bottom of bearing block chuck and top are respectively arranged with cooling liquid inlet I 653 and cooling liquid outlet I 651, described slurry can side and bottom surface are provided with slurry can chuck 681, be provided with spiral guiding plate II 683 in the slurry can chuck of described slurry can side, slurry can chuck bottom surface and top, side are respectively arranged with cooling liquid inlet II 684 and cooling liquid outlet II 682, cooling liquid inlet I 653, cooling liquid outlet I 651, cooling liquid inlet II 684 and cooling liquid outlet II 682 are communicated with cooling system 5 respectively.Described power transmission shaft 63 is connected with power set 61 by transmission device, bearing block 65 is installed on the frame 64, slurry can 68 is connected with bearing block, and power transmission shaft passes bearing block and extends in the slurry can, and bearing and outside framework oil seal also are installed between power transmission shaft and the bearing block; Described emulsification assembly 66 is positioned at slurry can, and the emulsification assembly comprises rotor 662 and stator 661, and stator is fixed on the bearing block, and rotor is installed on the power transmission shaft 63 and is positioned at stator.Rotor drives by power transmission shaft and carries out High Rotation Speed.Seal by being provided with sealing ring 67 between stator lower end and the slurry can, form feed cavity between stator bottom and the slurry can, feed cavity is communicated with the feed pipe 69 that passes the slurry can bottom, gap between stator side and the slurry can forms the discharging chamber, sealing ring is isolated feed cavity and discharging chamber, prevents that the material after the high speed shear from producing backflow.Stator side has the emulsifying homogeneous that is communicated with the discharging chamber discharging elongated hole 6611 of holding concurrently, and the discharging chamber is communicated with the discharge nozzle 610 that passes bearing block side and part and be positioned at the bearing block chuck.
Can lead to circulating cooling liquid by cooling system in the slurry can chuck of slurry can, the slurry that cooling is stirred.But in the bearing block chuck of bearing block also cooling system can lead to circulating cooling liquid, cooling and stirring evenly after the slurry of output, but simultaneously bearing and the outside framework oil seal of High Rotation Speed cooled off.The emulsifying homogeneous that stator the has discharging elongated hole of holding concurrently is suitable for the rapid pulverizing of medium solid and the mixing of medium-viscosity liquid, for surface shear provides maximum area and good circulation.
The described frame of present embodiment is formed by section welded, and is simple in structure, prepares easy.Present embodiment can also supporting purging system.
The described control system of present embodiment comprises touch-screen 21, PLC system 22, frequency converter I 23, frequency converter II 24, frequency converter III 25, the water-cooled electromagnetic valve 28 that is used for Controlled cooling system that is subjected to the magnetic valve I 26 of PLC system control and controlled by the PLC system, described magnetic valve I and delivery pump I, the delivery pump II is electrically connected, described frequency converter I, the frequency converter II is disperseed respectively the revoluting motor 101 of de-airing mixer with planet, disperse motor 102 to be electrically connected, described frequency converter III is electrically connected with centrifugal emulsifier unit motor 61, described frequency converter I 23, frequency converter II 24, frequency converter III 25 is connected described viscosity sensor 8 with PLC system output interface respectively, granularity sensor 9, temperature controller 11 and touch-screen 21 all link to each other with PLC system corresponding ports.
In the present embodiment, also be provided with the petrol station motor 13 that is used for the control hydraulic system that is subjected to the control of PLC system, hydraulic system is used for the lifting that the control planet disperses the de-airing mixer hoist cylinder, realizes that planet disperses the lifting of de-airing mixer crossbeam.In addition, present embodiment also is provided with the magnetic valve II 27 that is subjected to the control of PLC system, and the magnetic valve II is electrically connected with the vaccum pump motor 14 that is used for the control vavuum pump, and vavuum pump is used for disperseing the charging basket of de-airing mixer to vacuumize to planet.
Touch-screen disperses the opening time of numerical value that de-airing mixer required running time, rotating speed, temperature of charge, viscosity, granularity, vacuum sets and centrifugal emulsifier unit required running time, rotating speed, pipeline to pass to the PLC system in the mode of communication in planet, when the actual read number of viscosity, granularity, temperature exceeded setting numerical value, the PLC system sent alarm signal.The PLC system is with the given frequency converter I of the mode of communication, frequency converter II, frequency converter III action command and frequency, and read working voltage and the running current of frequency converter, frequency converter is directly controlled revoluting motor, dispersion motor, the centrifugal emulsifier unit motor that planet disperses de-airing mixer, realizes that planet disperses de-airing mixer and the operation of centrifugal emulsifier unit.When reached the touch-screen setting-up time running time, the PLC system sent stop signal to corresponding frequency converter, made corresponding motor out of service.After obtaining the lifting instruction on the touch-screen, be transmitted in the PLC system with communication modes, the PLC control system is sent switching value signal controlling hydraulic system petrol station motor action, realizes that the control planet disperses the lifting of de-airing mixer hoist cylinder.After inputting the vacuum startup command on the touch-screen, instruction is moved simultaneously by PLC system control vavuum pump and magnetic valve II, the magnetic valve II makes outside gas circuit commutation, thereby the commutation of control pneumatic operated valve II promotes to start ball valve and opens, opening vaccum pump motor begins to vacuumize, when the pressure within planet disperses the de-airing mixer charging basket reaches the force value that sets, close and close barrel ball valve and vacuum pump switch, make charging basket be in vacuum state.The magnetic valve I of PLC system control delivery pump I and delivery pump II, magnetic valve I make outside gas circuit commutation so that the action of delivery pump I and delivery pump II is controlled in the commutation of pneumatic operated valve I, makes whole mass transport chain action.Thermocouple is directly monitored temperature of charge, and by the signal of telecommunication value of feedback temperature value is presented on the temperature controller, temperature controller is passed to the PLC system with signal, the PLC system judges through program whether actual temperature of charge surpasses the temperature that touch-screen sets, open the water-cooled magnetic valve when temperature surpasses and open cooling system, the slurry can of centrifugal emulsifier unit is cooled off.
A kind of conversion as present embodiment, described control system can also adopt other versions, receive temperature signal, viscosity signal and granularity signal as long as can be used in, and carry out data and process, send instruction control planet according to corresponding signal and disperse the operation of de-airing mixer, centrifugal emulsifier unit, delivery pump I, delivery pump II and cooling system to get final product.
Planet described in the utility model disperses de-airing mixer and existing planet to disperse the de-airing mixer structure identical, and described cooling system and purging system are also same as the prior art, repeat no more herein.
The course of work of the present utility model: raw material join planet disperse de-airing mixer tentatively to stir, disperse after, enter into centrifugal emulsifier unit by conveyance conduit and carry out degree of depth dispersion, shearing, emulsifying homogeneous, getting back to planet by Returning pipe again disperses in the de-airing mixer, at Returning pipe viscosity sensor, granularity sensor and thermocouple are installed, viscosity, granularity, the temperature of slurry detected in real time.Be lower than setting value when detecting temperature, system normally moves; When temperature is higher than setting value, opens cooling system the slurry in the centrifugal emulsifier unit is lowered the temperature.When the viscosity that detects slurry, granularity, temperature all meet setting value, shut down from planet and disperse discharging the de-airing mixer; When having an index improper in the viscosity that detects slurry, the granularity, slurry is recycled to planet to be disperseed in the de-airing mixer charging basket, and corresponding modify wet end furnish, namely revise the various numerical value that need to add raw material in the slurry, slurry carries out mix and blend within planet disperses de-airing mixer, and then be circulated to and carry out further degree of depth dispersion, shearing, emulsifying homogeneous in the centrifugal emulsifier unit, so circulation is until till each index of slurry meets the requirements.
Characteristics of the present utility model are:
1. conventional planet disperses de-airing mixer that solid-liquid is carried out wetting and preliminary dispersion (2-3h);
2. then slurry is input to centrifugal emulsifier unit and carries out degree of depth dispersion shearing/emulsifying homogeneous, its process is the on-line continuous circulation;
3. on the pulp flow pipeline, can realize online viscosity, granularity and temperature detection;
4. corollary system has cooling system, purging system etc.;
5. omnidistance PLC man-machine interface monitoring, and can disperse de-airing mixer to carry out exchanges data with planet.
Claims (4)
1. efficient online stirring system, it is characterized in that: comprise that planet disperses de-airing mixer (1), centrifugal emulsifier unit (6) and control system (2), planet disperses the de-airing mixer discharge nozzle to be communicated with centrifugal emulsifier unit feed pipe by conveyance conduit (4) and delivery pump I (3), centrifugal emulsifier unit discharge nozzle disperses the de-airing mixer feed pipe to be communicated with by Returning pipe (12) and delivery pump II (7) with planet, described centrifugal emulsifier unit is the supporting cooling system (5) that is provided with also, be separately installed with thermocouple (10) on the described Returning pipe (12), viscosity sensor (8) and granularity sensor (9), thermocouple is used for the temperature signal of slurry in the monitoring Returning pipe, thermocouple is sent to control system by temperature controller (11) with temperature signal, viscosity sensor and granularity sensor are respectively applied to monitor viscosity signal and the granularity signal of slurry in the Returning pipe, and viscosity signal and granularity signal be sent to control system, control system is used for the temperature signal to receiving, viscosity signal and granularity signal carry out data to be processed, send instruction control planet and disperse de-airing mixer, centrifugal emulsifier unit, the operation of delivery pump I and delivery pump II, the operation of sending simultaneously the instruction Controlled cooling system.
2. efficient online stirring system according to claim 1, it is characterized in that: described centrifugal emulsifier unit (6) is vertical structure, comprise power set (61), transmission device (62), power transmission shaft (63), frame (64), the bearing block of jacket type (65), the slurry can (68) of emulsification assembly (66) and jacket type, described bearing block side is provided with bearing block chuck (652), the bottom of bearing block chuck and top are respectively arranged with cooling liquid inlet I (653) and cooling liquid outlet I (651), described slurry can side and bottom surface are provided with slurry can chuck (681), slurry can chuck bottom surface and top, side are respectively arranged with cooling liquid inlet II (684) and cooling liquid outlet II (682), cooling liquid inlet I (653), cooling liquid outlet I (651), cooling liquid inlet II (684) and cooling liquid outlet II (682) are communicated with cooling system (5) respectively; Described power transmission shaft (63) is connected with power set (61) by transmission device, bearing block (65) is installed on the frame (64), slurry can (68) is connected with bearing block, power transmission shaft passes bearing block and extends in the slurry can, described emulsification assembly (66) is positioned at slurry can, the emulsification assembly comprises rotor (662) and stator (661), stator is fixed on the bearing block, rotor is installed in power transmission shaft (63) upward and is positioned at stator, seal by being provided with sealing ring (67) between stator lower end and the slurry can, form feed cavity between stator bottom and the slurry can, feed cavity is communicated with the feed pipe that passes the slurry can bottom (69), gap between stator side and the slurry can forms the discharging chamber, stator side has the emulsifying homogeneous that is communicated with the discharging chamber discharging elongated hole (6611) of holding concurrently, and the discharging chamber is communicated with the discharge nozzle (610) that passes bearing block side and part and be positioned at the bearing block chuck.
3. efficient online stirring system according to claim 2 is characterized in that: be provided with spiral guiding plate I (654) in the described bearing block chuck, be provided with spiral guiding plate II (683) in the slurry can chuck of described slurry can side.
4. according to claim 1,2 or 3 described efficient online stirring systems, it is characterized in that: described control system comprises touch-screen (21), PLC system (22), frequency converter I (23), frequency converter II (24), frequency converter III (25), the water-cooled electromagnetic valve (28) that is used for Controlled cooling system that is subjected to the magnetic valve I (26) of PLC system control and controlled by the PLC system, described magnetic valve I and delivery pump I, the delivery pump II is electrically connected, described frequency converter I, the frequency converter II is disperseed respectively the revoluting motor (101) of de-airing mixer with planet, disperse motor (102) to be electrically connected, described frequency converter III is electrically connected with centrifugal emulsifier unit motor (61), described frequency converter I (23), frequency converter II (24), frequency converter III (25) is connected described viscosity sensor (8) with PLC system output interface respectively, granularity sensor (9), temperature controller (11) and touch-screen (21) all link to each other with PLC system corresponding ports.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220458953 CN202876730U (en) | 2012-09-11 | 2012-09-11 | High-efficiency on-line stirring system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220458953 CN202876730U (en) | 2012-09-11 | 2012-09-11 | High-efficiency on-line stirring system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202876730U true CN202876730U (en) | 2013-04-17 |
Family
ID=48068196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220458953 Expired - Fee Related CN202876730U (en) | 2012-09-11 | 2012-09-11 | High-efficiency on-line stirring system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202876730U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102824873A (en) * | 2012-09-11 | 2012-12-19 | 柳州市豪杰特化工机械有限责任公司 | Efficient online mixing system |
| CN103268931A (en) * | 2013-05-24 | 2013-08-28 | 佛山市金银河智能装备股份有限公司 | Production process and system of positive and negative electrode paste of lithium battery |
| CN106964298A (en) * | 2015-11-18 | 2017-07-21 | 刘操 | A kind of circulating dual device for dispersing paint |
| CN109647270A (en) * | 2019-01-23 | 2019-04-19 | 江西蒙山乳业有限公司 | A kind of continuous circulation material system |
-
2012
- 2012-09-11 CN CN 201220458953 patent/CN202876730U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102824873A (en) * | 2012-09-11 | 2012-12-19 | 柳州市豪杰特化工机械有限责任公司 | Efficient online mixing system |
| CN103268931A (en) * | 2013-05-24 | 2013-08-28 | 佛山市金银河智能装备股份有限公司 | Production process and system of positive and negative electrode paste of lithium battery |
| CN103268931B (en) * | 2013-05-24 | 2015-06-10 | 佛山市金银河智能装备股份有限公司 | Production process and system of positive and negative electrode paste of lithium battery |
| CN106964298A (en) * | 2015-11-18 | 2017-07-21 | 刘操 | A kind of circulating dual device for dispersing paint |
| CN109647270A (en) * | 2019-01-23 | 2019-04-19 | 江西蒙山乳业有限公司 | A kind of continuous circulation material system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102824873A (en) | Efficient online mixing system | |
| CN202876730U (en) | High-efficiency on-line stirring system | |
| CN102327757B (en) | Shear dispersion system for high-efficiency mixing of sticky materials, and application thereof | |
| CN203342723U (en) | Combined vacuum planetary mixer for ultrasonic dispersion | |
| CN108180181A (en) | A kind of hydraulic system, the control system based on the hydraulic system and forced stirrer | |
| CN111169158B (en) | Intelligent special thick liquid device that gives of foam stamp | |
| CN2873838Y (en) | Size cooking device special for Textile sizing | |
| CN101259389B (en) | High shearing thinning homogenizing machine | |
| CN214330590U (en) | Split type electric well cementing truck | |
| CN214287964U (en) | Reaction system for preparing water-based strippable coating | |
| CN213254859U (en) | Dispersion equipment for paint production | |
| CN208229829U (en) | Integrated mulser | |
| CN109213052B (en) | Control system applied to drilling plug pumping | |
| CN201643994U (en) | High efficient liquid-powder homogenization and emulsification device for vacuum emulsifying mixer | |
| CN206027840U (en) | A multi -functional horizontal sand mill for paint produce usefulness | |
| CN2188420Y (en) | In-line mixing emolsifing machine | |
| CN209451660U (en) | A kind of material-stirring device | |
| CN208529430U (en) | Stone breaking machine is used in a kind of production of hilllock stone | |
| CN214439548U (en) | Basket type grinding machine for producing large motor insulation coating liquid | |
| CN202376945U (en) | Liquid powder mixer with ultrasonic flow controller | |
| CN215848960U (en) | Electrically-driven slurry mixing equipment | |
| CN210613404U (en) | Enzymolysis high-speed stirring emulsification system | |
| CN213761612U (en) | Material mixing device | |
| CN216630555U (en) | Automatic energy-conserving mixed unit of batching | |
| CN211445038U (en) | Pressure plate type online proportioning and conveying device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP02 | Change in the address of a patent holder |
Address after: 545005 the Guangxi Zhuang Autonomous Region Liuzhou City Industrial Zone No. E-02-05 Lowe Patentee after: Liuzhou Hugest Chemical Machinery Co., Ltd. Address before: 545005 No. 6-1, nine mountain road, the Guangxi Zhuang Autonomous Region, Liuzhou Patentee before: Liuzhou Hugest Chemical Machinery Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130417 Termination date: 20190911 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |