Temperature control equipment for improving quality of epoxy-terminated silicone oil
By introducing dual temperature detection of armored platinum thermal resistance and K-type thermocouple in the temperature control equipment, combining the temperature control of the thermal conduction layer and the heat dissipation fins, the mixing structure of the stirring rod and the auxiliary rotary rod, the anti-blocking design of the filter net and the buffer structure, and the re-mixing of the circulating water pump solves the problems of inaccurate temperature control and uneven mixing in traditional temperature control equipment, and improves the production efficiency and product quality of end epoxy silicone oil.
Patent Information
- Application Number
- CN202510547000.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2025-04-28
- Publication Date
- 2025-07-08
AI Technical Summary
Traditional temperature control equipment cannot achieve accurate monitoring and dynamic adjustment of the temperature in the reactor, and the mixing uniformity is poor, resulting in low production efficiency of end epoxy silicone oil and unstable product quality.
The armored platinum thermal resistor and K-type thermocouple are used for dual temperature detection, combined with the thermal conduction layer and the heat dissipation fin for precise temperature control, and a stirring rod and auxiliary rotating rod are used for three-dimensional mixing, a filter net and a buffer structure are set to prevent impurities from being blocked, and the circulating water pump is used to stir and mix again.
It realizes precise control of the temperature in the reactor, improves the mixing uniformity and reaction efficiency, ensures stable product quality, reduces equipment wear and impact, and improves production efficiency and product qualification rate.
Smart Images

Figure CN120268351A_ABST
Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of temperature control equipment, and specifically to a temperature control equipment for improving the quality of terminal epoxy silicone oil. Background Art
[0002] Terminal epoxy silicone oil occupies a key position in high-end fields such as electronic packaging, aerospace, and medical materials due to its excellent high and low temperature resistance, electrical insulation, and chemical stability. With the continuous improvement of the performance requirements for terminal epoxy silicone oil in various industries, the quality control in its production process has become the focus of the industry. In the existing production process of terminal epoxy silicone oil, traditional temperature control equipment is difficult to meet the needs of fine production. On the one hand, the temperature control means are single, unable to achieve precise monitoring and dynamic adjustment of the temperature inside the reaction kettle, easily causing local temperature imbalance and resulting in product performance fluctuations. On the other hand, during the raw material mixing process, the conventional stirring device stirs and mixes the liquid surface, with poor mixing uniformity, and the liquid is prone to stratification effect, making the mixing efficiency of the lower and upper layers of the solution different, thereby affecting the overall quality of terminal epoxy silicone oil. At the same time, when the raw materials enter the reaction kettle, there is a large impact, which impacts the internal components of the equipment. These defects lead to low production efficiency and low product qualification rate of terminal epoxy silicone oil, seriously restricting industrial upgrading and the improvement of market competitiveness.
[0003] To solve the above problems, we hereby propose a temperature control equipment for improving the quality of terminal epoxy silicone oil. Summary of the Invention
[0004] In view of the deficiencies of the prior art, the present invention provides a temperature control equipment for improving the quality of terminal epoxy silicone oil, which solves the above problems.
[0005] To achieve the above object, the present invention provides the following technical solution: A temperature control equipment for improving the quality of terminal epoxy silicone oil, including a mounting plate, multiple supporting feet for support are fixedly installed at the lower end of the mounting plate, a reaction kettle for reaction is arranged at the center of the upper surface of the mounting plate, a feeding port for feeding is fixedly installed on one side of the upper end of the reaction kettle, and a discharging port for discharging is installed at the position corresponding to the feeding port at the lower end of the reaction kettle. It further includes: A temperature adjustment component, installed outside the reaction kettle, which is a structure for adjusting the temperature inside the reaction kettle; A temperature measurement component, installed at the upper end inside the reaction kettle, which is a structure for measuring the temperature inside the reaction kettle.
[0006] Preferably, the temperature adjustment component includes a heat preservation outer layer, a diversion pipe, a heat conduction layer, and heat dissipation fins. A heat preservation outer layer for protection is installed around the outside of the reaction kettle. The inside of the heat preservation outer layer is hollow. A heat conduction layer for heat conduction is installed inside the heat preservation outer layer. A diversion pipe for guiding is arranged inside the heat conduction layer. Both ends of the diversion pipe extend to the outside of the heat preservation outer layer. A plurality of heat dissipation fins for heat dissipation are evenly installed on the inner wall of the reaction kettle corresponding to the position of the heat conduction layer. One end of the heat dissipation fin penetrates the surface of the reaction kettle and is connected to the heat conduction layer. A sealing gasket for sealing is installed at the connection between the heat dissipation fin and the reaction kettle.
[0007] Preferably, a motor for control is installed at the center of the upper end of the mounting plate. The output end of the motor is connected to the central shaft. A plurality of stirring rods for stirring are evenly installed on the surface of the central shaft.
[0008] Preferably, a fixing ring for connection is fixedly installed on the surface of the central shaft corresponding to the side end of the stirring rod. A connecting rod for connection is fixedly installed on the side end of the fixing ring. A plurality of auxiliary rotating rods for assistance are evenly sleeved on the surface of the connecting rod. The other end of the connecting rod is fixedly connected to the limiting block. A circular limiting groove for sliding is arranged on the inner wall of the reaction kettle corresponding to the position of the limiting block. The limiting block is slidably installed inside the circular limiting groove.
[0009] Preferably, an upper mounting block for support is installed at the connection between the upper end of the reaction kettle and the central shaft. A limiting groove is arranged inside the upper mounting block. A limiting circular block for limiting is fixedly installed on the surface of the central shaft corresponding to the inside of the limiting groove.
[0010] Preferably, a lower mounting block for connection is installed at the center of the lower end of the reaction kettle. A first circulation pipe for collection is fixedly installed at the lower end of the lower mounting block. A circulation water pump for driving is fixedly installed on the surface of the first circulation pipe. The other end of the first circulation pipe is connected to a second circulation water pipe through a connecting flange. The other end of the second circulation water pipe is connected to a third circulation water pipe through a fixed flange.
[0011] Preferably, the temperature measurement component includes an annular pipe, a filter screen, and a rhombic plate. The feeding port and the lower end of the third circulation water pipe extend into the reaction kettle and are connected to the annular pipe. The annular pipe is fixedly installed on the inner wall surface of the reaction kettle. A filter screen for filtering is fixedly installed inside the reaction kettle corresponding to the lower end of the annular pipe. A rhombic plate for temperature measurement is arranged at the lower end of the filter screen.
[0012] Preferably, a plurality of auxiliary connecting pipes are fixedly installed at the inner end of the annular pipe, and a central ring is fixedly installed at the other end of the connecting pipe. The second circulating water pipe is arranged around the central axis. A plurality of leakage holes for flowing are uniformly arranged on the lower surfaces of the annular pipe and the connecting pipe. A buffer spring for buffering is fixedly installed inside the connecting pipe corresponding to the surface of the central ring. The other end of the buffer spring is connected to a baffle plate, and the baffle plate is arranged in a fitting manner with the inner wall of the connecting pipe.
[0013] Preferably, the surface of the filter screen is inclined upward from outside to inside. A plurality of filter holes are uniformly arranged on the surface of the filter screen, and the surface of the filter hole is arranged in a conical circular groove shape. The filter screen is composed of two parts inside and outside, and a fixing ring is installed at the connection of the two sections of the filter screen for connection.
[0014] Preferably, the surface of the rhombic plate is inclined downward from outside to inside. A plurality of thermal resistors for temperature measurement are uniformly installed on the upper surface of the rhombic plate. One end of the thermal resistor is connected to the upper temperature display screen, and the other end of the upper temperature display screen extends to the outside of the reaction kettle. A plurality of thermocouples for temperature measurement are uniformly installed on the lower surface of the rhombic plate. One end of the thermocouple is connected to the lower temperature display screen, and the other end of the lower temperature display screen extends to the outside of the reaction kettle.
[0015] Compared with the prior art, the present invention provides a temperature control device for improving the quality of terminal epoxy silicone oil, having the following beneficial effects: 1. For this temperature control device for improving the quality of terminal epoxy silicone oil, through the cooperation of the armored platinum thermal resistor and the K-type thermocouple in the temperature measurement component, the upper and lower double temperature detection of the terminal epoxy silicone oil in the reaction kettle can be carried out, the temperature data can be obtained in real time and visually presented through the upper and lower temperature display screens. Once the temperature exceeds the predetermined value, the cooling liquid in the diversion pipe can be quickly switched, and efficient heat dissipation can be carried out through the heat conduction layer and the heat dissipation fins, accurately controlling the reaction temperature to ensure that the terminal epoxy silicone oil reacts at an appropriate temperature and avoiding product quality instability caused by temperature fluctuations.
[0016] 2. For this temperature control device for improving the quality of terminal epoxy silicone oil, the motor drives the central shaft to rotate. While the stirring rod conventionally stirs the raw materials, the central shaft drives the connecting rod through the fixing ring, so that the limiting block moves in the ring limiting groove, enhancing the stability of the stirring. The flowing water flow drives the auxiliary rotating rod to rotate, assisting in mixing the raw materials from a three-dimensional perspective, effectively reducing the phenomenon of stirring stratification, and significantly improving the mixing uniformity and reaction efficiency of the terminal epoxy silicone oil.
[0017] 3. For the temperature control device for improving the quality of the terminal epoxy silicone oil, both the raw materials and the recycled terminal epoxy silicone oil need to pass through a filter screen. The surface of the filter screen is inclined and the filter holes are in the shape of conical circular grooves. It can not only effectively intercept impurities, but also prompt the impurities to flow along the inclined surface, preventing the impurities from clogging on the surface of the filter screen. At the same time, the filter screen plays a buffering role in the liquid pressure, reducing the impact on the temperature measuring component. While ensuring the accuracy of temperature measurement, it ensures the purity of the terminal epoxy silicone oil.
[0018] 4. For the temperature control device for improving the quality of the terminal epoxy silicone oil, the circulating water pump pumps out the preliminarily mixed terminal epoxy silicone oil for circulation, making it enter the annular pipe again to participate in the reaction. After being stirred and mixed again, the upper and lower stratification is further reduced, optimizing the product performance. The connecting flange and the fixed flange facilitate the replacement of the second circulating pipe, facilitating equipment maintenance and upgrading, and ensuring the stable operation of the circulation system.
[0019] 5. For the temperature control device for improving the quality of the terminal epoxy silicone oil, when the liquid flow rate in the annular pipe is too large, resulting in blockage and increased pressure, the baffle compresses the buffer spring under the action of the liquid pressure, and the auxiliary liquid flows out through the leakage holes on the lower surface of the connecting pipe to relieve the pressure. When the pressure decreases, the buffer spring pushes the baffle to reset, effectively avoiding damage to the equipment caused by excessive pressure, and enhancing the reliability and stability of the equipment operation.
[0020] 6. For the temperature control device for improving the quality of the terminal epoxy silicone oil, the mounting plate and the support feet firmly support the reaction kettle. Structures such as the upper mounting block, the limiting groove and the limiting circular block play a good limiting and supporting role for the central shaft, reducing the shaking and wear during the operation of the equipment. The heat preservation outer layer cooperates with the heat conduction layer and the diversion pipe, which can not only conduct heat efficiently but also reduce heat dissipation, reducing the loss of the equipment caused by temperature changes. BRIEF DESCRIPTION OF THE DRAWINGS
[0021] Figure 1 is a schematic structural diagram of the present invention; Figure 2 is a schematic diagram of the temperature control component of the present invention; Figure 3 is a schematic cross-sectional view of the reaction kettle of the present invention; Figure 4 is a schematic diagram of the stirring structure of the present invention; Figure 5 is a schematic diagram of the circulation structure of the present invention; Figure 6 is a schematic diagram of the temperature measuring component of the present invention; Figure 7 is of the present invention Figure 6 side end decomposition schematic diagram; Figure 8 is a schematic cross-sectional view of the annular pipe of the present invention; Figure 9 is of the present invention Figure 8 reset schematic diagram.
[0022] In the figure: 1. mounting plate; 2. support feet; 3. reactor; 4. feed inlet; 5. discharge outlet; 6. thermal insulation outer layer; 7. diversion pipe; 8. heat conduction layer; 9. heat dissipation fins; 10. annular limit groove; 11. motor; 12. central shaft; 13. stirring rod; 14. connecting rod; 15. auxiliary rotating rod; 16. limit block; 17. upper mounting block; 18. limit round block; 19. fixed flange; 20. lower mounting block; 21. first circulation pipe; 22. circulation water pump; 23. connecting flange; 24. second circulation water pipe; 25. third circulation water pipe; 26. annular pipe; 27. filter screen; 28. diamond-shaped plate; 29. thermal resistor; 30. upper temperature display screen; 31. thermocouple; 32. lower temperature display screen; 33. connecting pipe; 34. central ring; 35. buffer spring; 36. baffle plate. Specific implementation mode
[0023] The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. All other embodiments obtained by those of ordinary skill in the art based on the embodiments of the present invention without creative efforts shall fall within the protection scope of the present invention.
[0024] Please refer to Figures 1-9 , a temperature control device for improving the quality of terminal epoxy silicone oil, including a mounting plate 1. A plurality of support feet 2 for support are fixedly installed at the lower end of the mounting plate 1. A reactor 3 for reaction is arranged at the center of the upper surface of the mounting plate 1. A feed inlet 4 for feeding is fixedly installed on one side of the upper end of the reactor 3. A discharge outlet 5 for discharging is installed at a position corresponding to the feed inlet 4 at the lower end of the reactor 3. It is characterized in that it further includes: a temperature adjustment component, installed outside the reactor 3, a structure for adjusting the temperature inside the reactor 3; a temperature measurement component, installed at the upper end inside the reactor 3, a structure for measuring the temperature inside the reactor 3. The mounting plate 1 and the support feet 2 fixedly support the reactor 3 body. The raw material enters the inside of the reactor 3 from the feed inlet 4 and is discharged from the discharge outlet 5. The temperature inside the reactor is detected by the temperature measurement component, and the detected temperature data is transmitted to the temperature display screen for display. By comparing the temperature display screen with the temperature required by the current process, the temperature inside the reactor 3 is adjusted by the temperature adjustment component.
[0025] Furthermore, the temperature control component includes a heat-insulating outer layer 6, a diversion pipe 7, a heat-conducting layer 8, and heat-dissipating fins 9. A heat-insulating outer layer 6 for protection is installed around the outside of the reaction kettle 3. The inside of the heat-insulating outer layer 6 is hollow. A heat-conducting layer 8 for heat conduction is installed inside the heat-insulating outer layer 6. A diversion pipe 7 for guiding is arranged inside the heat-conducting layer 8. Both ends of the diversion pipe 7 extend to the outside of the heat-insulating outer layer 6. A plurality of heat-dissipating fins 9 for heat dissipation are evenly installed on the inner wall of the reaction kettle 3 corresponding to the position of the heat-conducting layer 8. One end of the heat-dissipating fin 9 penetrates the surface of the reaction kettle 3 and is connected to the heat-conducting layer 8. A sealing gasket for sealing is installed at the connection between the heat-dissipating fin 9 and the reaction kettle 3. The heat-insulating outer layer 6 protects the outside of the temperature control component. The heating liquid and the cooling liquid enter the inside of the heat-insulating outer layer 6 through the diversion pipe 7. The heat-conducting layer 8 and the heat-dissipating fins 9 transfer the temperature inside the heat-conducting pipe 7 to the inside of the reaction kettle 3.
[0026] Furthermore, a motor 11 for control is installed at the center of the upper end of the mounting plate 1. The output end of the motor 11 is connected to the central shaft 12. A plurality of stirring rods 13 for stirring are evenly installed on the surface of the central shaft 12. The composition of the stirring structure, the motor 11 is fixed at the center of the reaction kettle 3 through the mounting block 17.
[0027] Furthermore, a fixing ring for connection is fixedly installed on the surface of the central shaft 12 corresponding to the side end of the stirring rod 13. A connecting rod 14 for connection is fixedly installed on the side end of the fixing ring. A plurality of auxiliary rotating rods 15 for assistance are evenly sleeved on the surface of the connecting rod 14. The other end of the connecting rod 14 is fixedly connected to the limiting block 16. A ring limiting groove 10 for sliding is arranged on the inner wall of the reaction kettle 3 corresponding to the position of the limiting block 16. The limiting block 16 is slidably installed inside the ring limiting groove 10. The ring limiting groove 10 and the limiting block 16 support the central shaft 12. The auxiliary rotating rods 15 assist in mixing the liquid from the vertical direction.
[0028] Furthermore, an upper mounting block 17 for support is installed at the connection between the upper end of the reaction kettle 3 and the central shaft 12. A limiting groove is arranged inside the upper mounting block 17. A limiting circular block 18 for limiting is fixedly installed on the surface of the central shaft 12 corresponding to the inside of the limiting groove. The upper mounting block 17 and the limiting groove cooperate to limit the central shaft 12, so that the central shaft 12 is at the center point and prevent the central shaft 12 from tilting.
[0029] Furthermore, a lower mounting block 20 for connection is installed at the center of the lower end of the reactor 3. A first circulation pipe 21 for collection is fixedly installed at the lower end of the lower mounting block 20. A circulation water pump 22 for driving is fixedly installed on the surface of the first circulation pipe 21. The other end of the first circulation pipe 21 is connected to a second circulation water pipe 24 through a connecting flange 23. The other end of the second circulation water pipe 24 is connected to a third circulation water pipe 25 through a fixed flange 19. The combination of multiple circulation pipes extracts the liquid at the lower end inside the reactor 3, circulates it, and mixes it on the upper surface of the liquid. The first circulation pipe 21, the second circulation water pipe 24, and the third circulation water pipe 25 are connected through the lower mounting block 20, the connecting flange 23, and the fixed flange 19, and can be replaced when damaged.
[0030] Furthermore, the temperature measuring assembly includes a ring pipe 26, a filter screen 27, and a diamond-shaped plate 28. The feeding port 4 and the lower end of the third circulation water pipe 25 extend into the reactor 3 and are connected to the ring pipe 26. The ring pipe 26 is fixedly installed on the inner wall surface of the reactor 3. A filter screen 27 for filtering is fixedly installed inside the reactor 3 corresponding to the lower end of the ring pipe 26. A diamond-shaped plate 28 for temperature measurement is arranged below the filter screen 27. The circulating terminal epoxy silicone oil enters the inside of the ring pipe 26. The ring pipe 26 preliminarily intercepts and buffers the circulating terminal epoxy silicone oil. Part of the terminal epoxy silicone oil drains out to the surface of the filter screen 27 through the leakage holes. While the filter screen 27 filters, it buffers the terminal epoxy silicone oil to prevent the terminal epoxy silicone oil from contacting the diamond-shaped plate 28. The diamond-shaped plate 28 detects the temperature of the flowing terminal epoxy silicone oil. At the same time, the hot air flow generated on the upper surface of the liquid inside the reactor 3 rises and contacts the diamond-shaped plate 28, and the diamond-shaped plate 28 synchronously detects it.
[0031] Furthermore, a plurality of connecting pipes 33 for assistance are fixedly installed at the inner end of the ring pipe 26. The other end of the connecting pipe 33 is fixedly installed with a central ring 34. The second circulation water pipe 24 is arranged around the central axis 12. A plurality of leakage holes for flowing are uniformly arranged on the lower surfaces of the ring pipe 26 and the connecting pipe 33. A buffer spring 35 for buffering is fixedly installed on the surface of the central ring 34 corresponding to the inside of the connecting pipe 33. The other end of the buffer spring 35 is connected to a baffle 36. The baffle 36 is arranged in a fitting manner with the inner wall of the connecting pipe 33. The pressure generated by the terminal epoxy silicone oil inside the ring pipe 26 impacts the baffle 36. The terminal epoxy silicone oil pushes the baffle 36 to move inward, and the buffer spring 35 compresses. According to the pressure generated by the terminal epoxy silicone oil, the baffle 36 is pushed to move inward, and then it is assisted to flow out through the leakage holes on the lower surface of the connecting pipe 33. When the pressure generated by the terminal epoxy silicone oil decreases, the pressure received by the baffle 36 decreases, and the buffer spring 35 rebounds to reset the baffle 36.
[0032] Further, the surface of the filter net 27 is arranged in an upwardly inclined shape from the outside to the inside. A plurality of filter holes are evenly arranged on the surface of the filter net 27, and the surface of the filter holes is arranged in a conical circular groove shape. The filter net 27 is composed of an inner part and an outer part. A fixing ring is installed at the connection of the two sections of the filter net 27 for connection. The surface of the filter net 27 is inclined and the filter holes are in a conical circular groove shape. While ensuring the original function of intercepting impurities of the filter net 27, the impurities can move outward along the track of the filter net 27, preventing the impurities from remaining on the surface of the filter net 27 and reducing the blockage of the filter net 27. At the same time, the filter net 27 buffers the liquid discharged from the annular pipe 26, preventing the liquid discharged from the annular pipe 26 from impacting the temperature measuring component on the surface of the lower diamond-shaped plate 28. A height difference is provided between the two sections of the filter net 27, so that when the liquid flow rate is large, the dropped liquid can gradually diffuse outward while preventing the impurities from floating to the inside on the liquid surface.
[0033] Further, the surface of the diamond-shaped plate 28 is arranged in a downwardly inclined shape from the outside to the inside. A plurality of resistance thermometers 29 for temperature measurement are evenly installed on the upper surface of the diamond-shaped plate 28. One end of the resistance thermometer 29 is connected to the upper temperature display screen 30, and the other end of the upper temperature display screen 30 extends to the outside of the reaction kettle 3. A plurality of thermocouples 31 for temperature measurement are evenly installed on the lower surface of the diamond-shaped plate 28. One end of the thermocouple 31 is connected to the lower temperature display screen 32, and the other end of the lower temperature display screen 32 extends to the outside of the reaction kettle 3. The resistance thermometer 29 is an armored platinum resistance thermometer, which is installed on the upper surface of the diamond-shaped plate 28 and contacts with the terminal epoxy silicone oil, synchronously transmitting the temperature of the terminal epoxy silicone oil to the inside of the upper temperature display screen 30. The thermocouple 31 is a K-type thermocouple. The hot air flow generated after the liquid inside the reaction kettle 3 is heated rises and contacts with the K-type thermocouple. The K-type thermocouple synchronously transmits the temperature of the lower end air flow to the inside of the lower temperature display screen 32.
[0034] Instructions for Use Working Principle: The mounting plate 1 and the support feet 2 fixedly support the reaction kettle 3 body. The raw materials enter the reaction kettle 3 from the feeding port 4 and are discharged from the discharging port 5.
[0035] Example 1: Obtained according to Claims 1 to 5: The raw materials enter the interior of the annular pipe 26 from the feed inlet 4. The annular pipe 26 conducts preliminary buffering on the entering raw materials. The raw materials that pass through smoothly enter the surface of the filter screen 27 through the leakage holes at the lower end of the annular pipe 26. After being preliminarily filtered by the filter screen 27, they enter the interior of the diamond-shaped plate 28, and enter the interior of the reaction kettle 3 along the inwardly inclined arc of the diamond-shaped plate 28. The external heating liquid enters the interior of the protective outer layer 6 from one end of the diversion pipe 7. The heat conduction layer 8 diffuses the heat dissipated inside the diversion pipe 7 and transfers it to the interior of the reaction kettle 3 through the heat dissipation fins 9. The motor 11 is started, and the motor 11 drives the central shaft 12 to rotate. The stirring rods 13 on the surface of the central shaft 12 stir and mix the raw materials. At the same time, the central shaft 12 synchronously drives the connecting rod 14 to move through the fixed ring. The limiting block 16 at the other end of the connecting rod 14 moves inside the annular limiting groove 10. The annular limiting groove 10 and the limiting block 16 support the central shaft 12. When the stirring rods 13 stir the raw materials, the flowing water flow drives the auxiliary rotating rod 15 to rotate. The auxiliary rotating rod 15 assists in mixing the raw materials three-dimensionally, reducing the layering generated during stirring. The resulting terminal epoxy silicone oil after mixing is discharged from the discharge port 5.
[0036] Example 2: According to claims 6-10, it can be obtained that: The circulating water pump 22 is started, and the preliminarily mixed terminal epoxy silicone oil is extracted from the lower mounting block 20 at the lower end of the reaction kettle 3 into the interior of the first circulating pipe 22. The liquid after preliminary mixing enters the interior of the annular pipe 26 again along the first circulating pipe 21, the second circulating pipe 24, and the third circulating pipe 25. The connecting flange 23 and the fixed flange 19 can replace the second circulating pipe 24. The terminal epoxy silicone oil inside the annular pipe 26 falls through the leakage holes at the lower end of the annular pipe 26, and the filter screen 27 filters it again. The filtered impurities gradually move outward along the inclined angle of the filter screen 27. When the terminal epoxy silicone oil drips onto the surface of the diamond-shaped plate 28, the armored platinum thermal resistor on the upper surface of the diamond-shaped plate 28 detects the temperature carried by the terminal epoxy silicone oil. The preliminarily mixed terminal epoxy silicone oil enters above the liquid layer after circulation, and the stirring assembly stirs and mixes it again to reduce the upper and lower layering between the terminal epoxy silicone oils.
[0037] Example 3: According to claims 1-2 and claims 7-10, it can be obtained that: The terminal epoxy silicone oil transported through the circulation pipe falls downward from the leakage hole below the annular pipe 26 onto the filter screen 27. The filter screen 27 buffers the pressure of the terminal epoxy silicone oil, reducing the impact of the terminal epoxy silicone oil on the temperature measurement component. The terminal epoxy silicone oil falls downward and contacts the armored platinum thermal resistance on the surface of the diamond-shaped plate 28. The upper temperature display screen 30 displays the temperature of the terminal epoxy silicone oil. When the temperature exceeds the predetermined temperature of the current process, the heating liquid inside is discharged from the lower end of the diversion pipe 7, and the cooling liquid enters from the upper end of the diversion pipe 7. The cooling liquid cools down the heat conduction layer 8. At the same time, through the contact between the heat dissipation fins 9 and the liquid, the heat of the liquid is absorbed and transferred to the heat conduction layer 8 for heat exchange with the cooling liquid inside the diversion pipe 7. The K-type thermocouple on the lower surface of the diamond-shaped plate 28 detects the rising heat of the liquid and transmits the heat information to the lower temperature display screen 32. Through the cooperation of the armored platinum thermal resistance and the K-type thermocouple, the temperature of the terminal epoxy silicone oil inside the reaction kettle 3 is detected in real time, and then the liquid inside the diversion pipe 7 is replaced.
[0038] Example 4: Obtained according to Claim 8: Refer to the attached Figures 8-9 , attached Figure 9 is the original position of this structure. When the third circulation pipe 25 transports the mixed terminal epoxy silicone oil into the internal of the annular pipe 26, the amount of the mixed terminal epoxy silicone oil is relatively large, and the leakage holes on the lower surface of the annular pipe 28 cannot discharge the liquid in the first time, resulting in the blockage of the terminal epoxy silicone oil. The pressure generated by the terminal epoxy silicone oil inside the annular pipe 26 impacts the baffle 36. The terminal epoxy silicone oil pushes the baffle 36 to move inward, and the buffer spring 35 is compressed. According to the pressure generated by the terminal epoxy silicone oil, the baffle 36 is pushed to move inward, and then it flows out through the leakage holes on the lower surface of the connecting pipe 33, which can be used as a reference for the attached Figure 8 . When the pressure generated by the terminal epoxy silicone oil decreases, the pressure received by the baffle 36 decreases, and the buffer spring 35 rebounds, causing the baffle 36 to reset. The structure after reset can be referred to the attached Figure 9 .
[0039] Although the embodiments of the present invention have been shown and described, for those of ordinary skill in the art, it can be understood that various changes, modifications, substitutions, and variations can be made to these embodiments without departing from the principles and spirit of the present invention. The scope of the present invention is defined by the appended claims and their equivalents.
Claims
1. A temperature control device for improving the quality of terminal epoxy silicone oil, comprising a mounting plate (1), a plurality of supporting feet (2) for support are fixedly installed at the lower end of the mounting plate (1), a reaction kettle (3) for reaction is arranged at the center of the upper surface of the mounting plate (1), a feeding inlet (4) for feeding is fixedly installed on one side of the upper end of the reaction kettle (3), and a discharging outlet (5) for discharging is installed at a position corresponding to the feeding inlet (4) at the lower end of the reaction kettle (3), characterized in that, It also includes: A temperature regulating component, installed on the outer side of the reaction kettle (3), which is a structure for adjusting the temperature inside the reaction kettle (3); A temperature measuring component, installed at the upper end inside the reaction kettle (3), which is a structure for measuring the temperature inside the reaction kettle (3).
2. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 1, characterized in that: The temperature regulating component includes a heat preservation outer layer (6), a diversion pipe (7), a heat conducting layer (8) and heat dissipation fins (9). A heat preservation outer layer (6) for protection is installed around the outer side of the reaction kettle (3). The inside of the heat preservation outer layer (6) is hollow. A heat conducting layer (8) for heat conduction is installed inside the heat preservation outer layer (6). A diversion pipe (7) for guiding is arranged inside the heat conducting layer (8). Both ends of the diversion pipe (7) extend to the outside of the heat preservation outer layer (6). A plurality of heat dissipation fins (9) for heat dissipation are evenly installed on the inner wall of the reaction kettle (3) corresponding to the position of the heat conducting layer (8). One end of the heat dissipation fin (9) penetrates through the surface of the reaction kettle (3) and is connected to the heat conducting layer (8). A sealing gasket for sealing is installed at the connection between the heat dissipation fin (9) and the reaction kettle (3).
3. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 1, characterized in that: A motor (11) for control is installed at the center of the upper end of the mounting plate (1). The output end of the motor (11) is connected to the central shaft (12). A plurality of stirring rods (13) for stirring are evenly installed on the surface of the central shaft (12).
4. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 3, characterized in that: A fixing ring for connection is fixedly installed on the surface of the central shaft (12) corresponding to the side end of the stirring rod (13). A connecting rod (14) for connection is fixedly installed on the side end of the fixing ring. A plurality of auxiliary rotating rods (15) for assistance are evenly sleeved on the surface of the connecting rod (14). The other end of the connecting rod (14) is fixedly connected to the limiting block (16). A ring limiting groove (10) for sliding is arranged on the inner wall of the reaction kettle (3) corresponding to the position of the limiting block (16). The limiting block (16) is slidably installed inside the ring limiting groove (10).
5. A temperature control device for improving the quality of terminal epoxy silicone oil according to claim 1, characterized in that: An upper mounting block (17) for support is installed at the connection between the upper end of the reaction kettle (3) and the central shaft (12). A limiting groove is arranged inside the upper mounting block (17). A limiting circular block (18) for limiting is fixedly installed on the surface of the central shaft (12) corresponding to the inside of the limiting groove.
6. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 1, characterized in that: A lower mounting block (20) for connection is installed at the center of the lower end of the reaction kettle (3). A first circulation pipe (21) for collection is fixedly installed at the lower end of the lower mounting block (20). A circulation water pump (22) for driving is fixedly installed on the surface of the first circulation pipe (21). The other end of the first circulation pipe (21) is connected to a second circulation water pipe (24) through a connection flange (23). The other end of the second circulation water pipe (24) is connected to a third circulation water pipe (25) through a fixed flange (19).
7. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 1, characterized in that: The temperature measuring component includes an annular pipe (26), a filter screen (27) and a diamond-shaped plate (28). The feeding port (4) and the lower end of the third circulating water pipe (25) extend into the reactor (3) and are connected to the annular pipe (26). The annular pipe (26) is fixedly installed on the inner wall surface of the reactor (3). A filter screen (27) for filtering is fixedly installed inside the reactor (3) corresponding to the lower end of the annular pipe (26). A diamond-shaped plate (28) for temperature measurement is arranged at the lower end of the filter screen (27).
8. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 7, characterized in that: A plurality of connecting pipes (33) for assistance are fixedly installed at the inner end of the annular pipe (26). The other end of the connecting pipe (33) is fixedly installed with a central ring (34). The second circulating water pipe (24) is arranged around the central axis (12). A plurality of leakage holes for flowing are uniformly arranged on the lower surfaces of the annular pipe (26) and the connecting pipe (33). A buffer spring (35) for buffering is fixedly installed inside the connecting pipe (33) corresponding to the surface of the central ring (34). The other end of the buffer spring (35) is connected to a baffle plate (36). The baffle plate (36) is arranged in a fitting manner with the inner wall of the connecting pipe (33).
9. The temperature control device for improving the quality of terminal epoxy silicone oil according to claim 7, characterized in that: The surface of the filter screen (27) is inclined upward from outside to inside. A plurality of filter holes are uniformly arranged on the surface of the filter screen (27). The surface of the filter hole is arranged in a conical circular groove shape. The filter screen (27) is composed of two parts, an inner part and an outer part. A fixing ring is installed at the connection of the two sections of the filter screen (27) for connection.
10. A temperature control device for improving the quality of terminal epoxy silicone oil according to claim 7, characterized in that: The surface of the diamond-shaped plate (28) is inclined downward from outside to inside. A plurality of thermal resistors (29) for temperature measurement are uniformly installed on the upper surface of the diamond-shaped plate (28). One end of the thermal resistor (29) is connected to an upper temperature display screen (30). The other end of the upper temperature display screen (30) extends to the outside of the reactor (3). A plurality of thermocouples (31) for temperature measurement are uniformly installed on the lower surface of the diamond-shaped plate (28). One end of the thermocouple (31) is connected to a lower temperature display screen (32). The other end of the lower temperature display screen (32) extends to the outside of the reactor (3).