Feeding device for production and synthesis of dodecanol glycidyl ether
By designing a synthetic feed device for dodecyl glycidyl ether production with automatic proportioning and rapid mixing functions, the problem that existing devices cannot automatically achieve the dosage ratio of stock liquid is solved, and process efficiency and product quality are improved.
Patent Information
- Application Number
- CN202421917126.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-08-08
- Publication Date
- 2025-06-10
- Estimated Expiration
- 2034-08-08
AI Technical Summary
The existing synthetic feeding device for dodecanol glycidyl ether production cannot automatically realize the proportional feeding of the stock solution dose, resulting in low process efficiency and unstable product quality.
A feeding device including a support base, a processing bucket, a sealing cover, an auxiliary synthesis mechanism, a premixed hedging mechanism and a temperature control mechanism are designed. By setting up a partition plate and a variable speed water pump in the storage tank, the automatic proportioning of dodecanol stock solution and glycerol ether stock solution is achieved; at the same time, the design of stirring leaves and limit filter plates is achieved to achieve rapid mixing and dispersion of the stock solution.
The automatic proportioning of dodecanol stock solution and glycerol ether stock solution is realized, which improves process efficiency and product quality and simplifies the operation process.
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Figure CN222956404U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of dodecyl glycidyl ether production, and particularly relates to a dodecyl glycidyl ether production and synthesis feeding device. Background Art
[0002] Dodecyl glycidyl ether is a cosmetic raw material with the effects of moisturizing and softening the skin. It is a compound formed by the combination of dodecyl alcohol and glycerol ether, which can play the roles of moisturizing, moistening and softening the skin in cosmetics. Adding dodecyl glycidyl ether to the formula can improve the water content of the skin, making the skin more moist and smooth. At the same time, it also has certain emulsifying and thickening properties, which can play the roles of adjusting the emulsification stability and increasing the texture in the formula. Therefore, it is widely used in skin care products and cosmetics;
[0003] The "feeding mechanism and its catalyst synthesis device" disclosed in the patent number "CN220803116U" can add different catalyst synthesis raw materials into the reaction kettle in a specified order by connecting the suction pipe to multiple bins on the arc-shaped slide rail in sequence through the setting mode of the forward feeding component, avoiding the phenomenon of incorrect addition order of raw materials or over-addition or under-addition of a single raw material; however, since it is difficult for workers to accurately control the dosage ratio of raw materials during manual operation, once the dosage ratio is incorrect, it will directly affect the normal use of the final synthesized product. However, the above device cannot automatically achieve the effect of proportioning and feeding the original liquid dosage during use, and the overall practical effect needs to be strengthened. Content of the Utility Model
[0004] The purpose of the utility model is to provide a dodecyl glycidyl ether production and synthesis feeding device to solve the above problems, improving the problem that the existing dodecyl glycidyl ether production and synthesis feeding device cannot automatically achieve proportioning and feeding of the original liquid dosage during use.
[0005] A production and synthesis feeding device for dodecyl glycidyl ether, comprising a support base, a processing barrel and a sealing cover: a processing barrel is arranged on the outer wall of the top end of the support base, a sealing cover is installed on the outer wall of the top end of the processing barrel, an auxiliary synthesis mechanism is arranged inside the processing barrel, a premixing and counteracting mechanism is arranged on the side of the processing barrel, and a temperature control mechanism is arranged on the side of the premixing and counteracting mechanism. The auxiliary synthesis mechanism includes a positioning support frame, a driving motor, a transmission shaft, stirring blades, support rods and a limiting filter plate. A positioning support frame is arranged on the outer wall of the top end of the sealing cover, a driving motor is arranged on the outer wall of the top end of the positioning support frame, the driving motor is connected to the outer wall of the top end of the transmission shaft, the outer wall of the bottom end of the transmission shaft is rotatably installed on the inner wall of the bottom end of the processing barrel, stirring blades are arranged outside the transmission shaft inside the processing barrel, support rods are arranged on the outer wall of the side of the transmission shaft at equal intervals in a circumferential manner, the support rods are arranged in a "[-]" shape, and a limiting filter plate is arranged on the outer wall of the side of the support rods.
[0006] Preferably, the stirring blades are arranged in a spiral structure, and the limiting filter plate is arranged in a porous plate structure.
[0007] Preferably, the premixing and counteracting mechanism includes a feed hopper, a liquid storage tank, a limiting partition plate and a first variable-speed water pump. A feed hopper is installed on the outer wall of the top end of the sealing cover in a conducting manner, a liquid storage tank is arranged on the outer wall of the top end of the support base, a limiting partition plate is arranged on the inner wall of the bottom end of the liquid storage tank at the middle position, the limiting partition plate divides the inside of the liquid storage tank into two complete closed spaces, and a first variable-speed water pump is arranged on the inner wall of the bottom end of the first space of the liquid storage tank.
[0008] Preferably, a second variable-speed water pump is arranged on the inner wall of the bottom end of the second space of the liquid storage tank, one end of the first variable-speed water pump is connected to one end of a first diversion pipe, and the other end of the first diversion pipe is installed on the outer wall of one side of the feed hopper in a conducting manner.
[0009] Preferably, one end of the second variable-speed water pump is connected to one end of a second diversion pipe, and the other end of the second diversion pipe is installed on the outer wall of the other side of the feed hopper in a conducting manner.
[0010] Preferably, the top end of the feed hopper is arranged in a sealed structure, and two liquid injection pipes are symmetrically installed on the outer wall of the top end of the liquid storage tank in a conducting manner.
[0011] Preferably, the temperature control mechanism includes a heating base, a power supply component, a controller and a protective cover. A heating base is arranged on the outer wall of the top end of the support base, the outer wall of the top end of the heating base is connected to the outer wall of the bottom end of the processing barrel, a power supply component and a controller are arranged on the outer wall of the top end of the support base, and a protective cover is arranged outside the power supply component and the controller.
[0012] Preferably, the bottom outer wall of the protective cover is connected to the top outer wall of the supporting base, the top outer wall of the protective cover is provided with a temperature monitoring sensor, and a temperature conducting rod is connected and installed between the temperature monitoring sensor and the side outer wall of the processing barrel.
[0013] The beneficial effects of the utility model are:
[0014] 1. When the dodecanol glycidyl ether production and synthesis feeding device is used, a partition is set inside the liquid storage tank to store the dodecanol stock solution and the glycerol ether stock solution separately and two variable speed water pumps are provided. When the dodecanol stock solution and the glycerol ether stock solution need to be proportioned and fed, it is only necessary to adjust the corresponding variable speed water pumps to a suitable speed ratio. The operation is simple, and the rapid proportioning and feeding of the dodecanol stock solution and the glycerol ether stock solution can be completed in a portable manner. Furthermore, the two guide pipes are both set inside the feed hopper. The two stock solutions can achieve the effect of premixing and hedging during the feeding process, thereby accelerating the efficiency of the subsequent mixing process of the dodecanol stock solution and the glycerol ether stock solution. The overall structural design is simple and the practical effect is good.
[0015] 2. When the dodecanol glycidyl ether production and synthesis feeding device is in use, the design of synchronously driving the stirring blade and the limiting filter plate to rotate synchronously through the mechanism transmission, the stirring blade is set to a spiral structure so that it can transport the raw liquid in the device up and down when rotating, and the surrounding raw liquid will immediately replenish to the center, thereby realizing the turning effect of the raw liquid and realizing the longitudinal mixing of the raw liquid. The limiting filter plate is set to a porous plate structure so that it can complete the mixing effect of the raw liquid horizontally when rotating. With the porous structure of the limiting filter plate, it can also disperse the raw liquid in the barrel when rotating, thereby accelerating the mixing effect of the raw liquid. The overall structural design is simple and the practical effect is excellent. BRIEF DESCRIPTION OF THE DRAWINGS
[0016] Figure 1 It is a schematic diagram of the overall three-dimensional structure of the utility model;
[0017] Figure 2 It is a schematic diagram of the overall sectional three-dimensional structure of the utility model;
[0018] Figure 3 It is a three-dimensional structural schematic diagram of the auxiliary synthesis mechanism of the utility model;
[0019] Figure 4 It is a three-dimensional structural schematic diagram of the premixing hedging mechanism of the utility model;
[0020] Figure 5 It is a three-dimensional structural schematic diagram of the temperature control mechanism of the utility model.
[0021] In the figure: 1, support base; 2, processing barrel; 3, sealing cover; 4, auxiliary synthesis mechanism; 41, positioning support frame; 42, drive motor; 43, transmission shaft; 44, stirring blade; 45, support rod; 46, limiting filter plate; 5, premixing and counteracting mechanism; 51, feed hopper; 52, liquid storage tank; 53, limiting partition plate; 54, first variable-speed water pump; 55, second variable-speed water pump; 56, first guide pipe; 57, second guide pipe; 6, temperature control mechanism; 61, heating base; 62, power supply component; 63, controller; 64, protective cover; 65, temperature monitoring sensor; 66, heat conduction rod. Detailed implementation manner
[0022] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with 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. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative work shall fall within the protection scope of the present invention.
[0023] During specific implementation: As Figures 1-5 shown, a production and synthesis feeding device for dodecyl alcohol glycidyl ether includes a support base 1, a processing barrel 2 and a sealing cover 3: The processing barrel 2 is provided on the outer wall of the top end of the support base 1, the sealing cover 3 is installed on the outer wall of the top end of the processing barrel 2, an auxiliary synthesis mechanism 4 is provided inside the processing barrel 2, a premixing and counteracting mechanism 5 is provided on the side of the processing barrel 2, and a temperature control mechanism 6 is provided on the side of the premixing and counteracting mechanism 5. The auxiliary synthesis mechanism 4 includes a positioning support frame 41, a drive motor 42, a transmission shaft 43, a stirring blade 44, a support rod 45 and a limiting filter plate 46. The positioning support frame 41 is provided on the outer wall of the top end of the sealing cover 3, the drive motor 42 is provided on the outer wall of the top end of the positioning support frame 41, the drive motor 42 is connected to the outer wall of the top end of the transmission shaft 43, the bottom end of the transmission shaft 43 is rotatably installed on the inner wall of the bottom end of the processing barrel 2, the stirring blade 44 is provided outside the transmission shaft 43 inside the processing barrel 2, the support rods 45 are arranged at equal intervals around the outer wall of the side of the transmission shaft 43, the support rod 45 is set in the shape of "[", and the limiting filter plate 46 is provided on the outer wall of the side of the support rod 45; When it is necessary to accelerate the mixing speed of dodecyl alcohol stock solution and glycidyl ether stock solution in the device, first, the drive motor 42 needs to be turned on. Here, the setting of the positioning support frame 41 plays an auxiliary supporting effect on the drive motor 42. When the drive motor 42 is turned on, it will automatically drive the transmission shaft 43 to rotate and then drive the stirring blade 44 to rotate. When the transmission shaft 43 rotates, it will also synchronously drive the support rod 45 to rotate and then drive the limiting filter plate 46 to rotate.
[0024] The stirring blade 44 is set to a spiral structure, and the limiting filter plate 46 is set to a porous plate structure; here, the stirring blade 44 is set to a spiral structure so that it can transport the raw liquid in the device up and down when it rotates, and at the same time, the surrounding raw liquid will immediately replenish to the center, thereby achieving the flipping effect of the raw liquid and achieving the longitudinal mixing of the raw liquid. The limiting filter plate 46 is set to a porous plate structure so that it can complete the horizontal mixing effect of the raw liquid when it rotates. Combined with the porous structure of the limiting filter plate 46, it can also disperse the raw liquid in the barrel when it rotates, thereby accelerating the mixing effect of the raw liquid.
[0025] The premixing and hedging mechanism 5 includes a feed hopper 51, a liquid storage tank 52, a limiting baffle 53 and a first variable speed water pump 54. The top outer wall of the sealing cover 3 is connected to the feed hopper 51, the top outer wall of the supporting base 1 is provided with a liquid storage tank 52, and the bottom inner wall of the liquid storage tank 52 located in the middle position is provided with a limiting baffle 53. The limiting baffle 53 divides the inside of the liquid storage tank 52 into two complete closed spaces. The bottom inner wall of the first space of the liquid storage tank 52 is provided with a first variable speed water pump 54, and the bottom inner wall of the second space of the liquid storage tank 52 is provided with a second variable speed water pump 55. The water pump 54 is connected to one end of the first guide pipe 56, and the other end of the first guide pipe 56 is connected to the outer wall of one side of the feed hopper 51. The second variable speed water pump 55 is connected to one end of the second guide pipe 57, and the other end of the second guide pipe 57 is connected to the outer wall of the other side of the feed hopper 51. The liquid storage tank 52 is divided into two closed spaces by the limiting partition 53, one for storing dodecanol stock solution and the other for storing glycerol ether stock solution. When the dodecanol stock solution and the glycerol ether stock solution need to be fed in a specified ratio, it is only necessary to mix the two. The first variable speed water pump 54 and the second variable speed water pump 55 are adjusted to a suitable speed ratio, and the faster the speed, the faster the pumping speed, and the slower the speed, the slower the pumping speed, so as to achieve the effect of proportional liquid inlet. When the first variable speed water pump 54 and the second variable speed water pump 55 are adjusted to a suitable speed ratio, the first variable speed water pump 54 and the second variable speed water pump 55 are turned on synchronously. When the first variable speed water pump 54 is turned on, the dodecanol stock solution in the liquid storage tank 52 will be automatically pumped into the first guide pipe 56 and transported to the inside of the feed hopper 51 through the drainage of the first guide pipe 56. After the second variable speed water pump 55 is turned on, it will automatically pump the glycerol ether stock solution in the liquid storage tank 52 into the second guide pipe 57 and transport it to the inside of the feed hopper 51 through the drainage of the second guide pipe 57. When the dodecanol stock solution and the glycerol ether stock solution are fed into the feed hopper 51 against each other, the effect of hedging premixing is achieved. It is noted here that both the first guide pipe 56 and the second guide pipe 57 are provided with a one-way valve on the outside, and the output ends of the two one-way valves are both facing the feed hopper 51. This arrangement avoids the problem of stock solution backflow, and further ensures the accuracy of subsequent stock solution ratio.
[0026] The top end of the feed hopper 51 is provided with a sealed structure, and two liquid injection pipes are symmetrically and conductively installed on the outer wall of the top end of the liquid storage tank 52; setting the top end of the feed hopper 51 as a sealed structure facilitates the counter-flow feeding of the dodecanol stock solution and the glycerol ether stock solution, and the setting of the two liquid injection pipes facilitates the subsequent separate injection of the dodecanol stock solution and the glycerol ether stock solution into the liquid storage tank 52.
[0027] The temperature control mechanism 6 includes a heating base 61, a power supply member 62, a controller 63 and a protective cover 64. The heating base 61 is provided on the outer wall of the top end of the support base 1, and the outer wall of the top end of the heating base 61 is connected to the outer wall of the bottom end of the processing barrel 2. The power supply member 62 and the controller 63 are provided on the outer wall of the top end of the support base 1, and the protective cover 64 is provided outside the power supply member 62 and the controller 63. The outer wall of the bottom end of the protective cover 64 is connected to the outer wall of the top end of the support base 1, and a temperature monitoring sensor 65 is provided on the outer wall of the top end of the protective cover 64. A temperature conduction rod 66 is connected and installed between the temperature monitoring sensor 65 and the side outer wall of the processing barrel 2; when it is necessary to control the temperature inside the device to facilitate the synthesis reaction of the dodecanol stock solution and the glycerol ether stock solution, first, the temperature monitoring sensor 65 needs to be adjusted to a suitable temperature monitoring range according to the synthesis reaction temperature of the two raw materials. After adjustment, the temperature monitoring sensor 65 is turned on. Here, the setting of the temperature conduction rod 66 facilitates the timely transfer of the real-time temperature of the outer wall of the processing barrel 2 to the temperature monitoring sensor 65. Once the processing temperature inside the processing barrel 2 is lower than the monitoring range of the temperature monitoring sensor 65, the temperature monitoring sensor 65 will automatically transmit the information to the controller 63. It should be noted here that an electric heating tube is pre-installed inside the heating base 61. Subsequently, the controller 63 will automatically control the power supply member 62 to turn on and energize the electric heating tube inside the heating base 61. Then, the heating of the electric heating tube will heat the stock solution inside the processing barrel 2 by heat transfer. When the temperature inside the processing barrel 2 is higher than the monitoring range of the temperature monitoring sensor 65, the temperature monitoring sensor 65 will also transmit the information to the controller 63. Subsequently, the controller 63 will automatically control the power supply member 62 to turn off and stop power supply. In this way, the effect of controlling the temperature inside the processing barrel 2 is achieved through the above working process, providing a good synthesis reaction temperature environment for the dodecanol stock solution and the glycerol ether stock solution.
[0028] When the utility model is in use, the liquid storage tank 52 is divided into two closed spaces by the limiting partition 53, one for storing the dodecanol stock solution, and the other for storing the glycerol ether stock solution. When the dodecanol stock solution and the glycerol ether stock solution need to be fed in accordance with a specified ratio, it is only necessary to adjust the first variable speed water pump 54 and the second variable speed water pump 55 corresponding to the two to a suitable speed ratio, and then the faster the speed, the faster the pumping speed, and the slower the speed, the slower the pumping speed, so as to achieve the effect of proportioned liquid feeding. When the first variable speed water pump 54 and the second variable speed water pump 55 are adjusted to a suitable speed ratio, The first variable speed water pump 54 and the second variable speed water pump 55 are started synchronously. When the first variable speed water pump 54 is started, the dodecanol stock solution in the liquid storage tank 52 is automatically pumped into the first guide pipe 56 and transported to the inside of the feed hopper 51 through the drainage of the first guide pipe 56. When the second variable speed water pump 55 is started, the glycerol ether stock solution in the liquid storage tank 52 is automatically pumped into the second guide pipe 57 and transported to the inside of the feed hopper 51 through the drainage of the second guide pipe 57. When the dodecanol stock solution and the glycerol ether stock solution are fed into the feed hopper 51 in a counter-balancing manner, the counter-balancing premixing effect is achieved.
[0029] When the proportioned dodecanol stock solution and glycerol ether stock solution enter the processing barrel 2, the driving motor 42 is turned on. When the driving motor 42 is turned on, it will automatically drive the transmission shaft 43 to rotate and then drive the stirring blade 44 to rotate. When the transmission shaft 43 rotates, it will also synchronously drive the support rod 45 to rotate and then drive the limiting filter plate 46 to rotate. Here, the stirring blade 44 is set to a spiral structure so that it can transport the stock solution in the device up and down when it rotates, and the surrounding stock solution will immediately replenish the center, thereby achieving the turning effect of the stock solution and achieving the longitudinal mixing of the stock solution. The limiting filter plate 46 is set to a porous plate structure so that it can complete the mixing effect of the stock solution horizontally when it rotates. With the porous structure of the limiting filter plate 46, it can also disperse the stock solution in the barrel when it rotates, thereby accelerating the mixing effect of the stock solution.
[0030] When it is necessary to control the temperature inside the device to facilitate the synthesis reaction of dodecanol stock solution and glycerol ether stock solution, first, the temperature monitoring sensor 65 needs to be adjusted to a suitable temperature monitoring range according to the synthesis reaction temperature of the two raw materials. After adjustment, the temperature monitoring sensor 65 is turned on. Here, the setting of the heat conduction rod 66 facilitates timely transmission of the real-time temperature on the outer wall of the processing barrel 2 to the temperature monitoring sensor 65. Once the processing temperature inside the processing barrel 2 is lower than the monitoring range of the temperature monitoring sensor 65, the temperature monitoring sensor 65 will automatically transmit the information to the controller 63. It should be noted here that an electric heating tube is pre-installed inside the heating base 61. Subsequently, the controller 63 will automatically control the power supply component 62 to turn on and supply power to the electric heating tube inside the heating base 61. Then, the heating of the electric heating tube will raise the temperature of the stock solution inside the processing barrel 2 through heat transfer. When the temperature inside the processing barrel 2 is higher than the monitoring range of the temperature monitoring sensor 65, the temperature monitoring sensor 65 will also transmit the information to the controller 63. Subsequently, the controller 63 will automatically control the power supply component 62 to turn off and stop power supply. In this way, the effect of controlling the temperature inside the processing barrel 2 is achieved through the above working process, providing a good synthesis reaction temperature environment for the dodecanol stock solution and glycerol ether stock solution.
[0031] The subsequent cooling process and crystallization process can be operated according to the existing technical means, which do not fall within the scope of the device description and will not be elaborated here; it should be noted here that the above driving motor 42 can be powered according to the existing operation means, whether it is powered by a power supply component or an external wire, which are both existing conventional operation technical means and will not be described in detail here.
[0032] In addition, it should be understood that although this specification is described according to embodiments, not every embodiment only contains an independent technical solution. This narrative way of the specification is only for clarity. Those skilled in the art should regard the specification as a whole, and the technical solutions in each embodiment can also be appropriately combined to form other embodiments that can be understood by those skilled in the art.
Claims
1. A feed device for producing and synthesizing dodecanol glycidyl ether, characterized in that: The invention comprises a supporting base (1), a processing barrel (2) and a sealing cover (3): the top outer wall of the supporting base (1) is provided with a processing barrel (2), the top outer wall of the processing barrel (2) is installed with a sealing cover (3), an auxiliary synthesis mechanism (4) is provided inside the processing barrel (2), a premixing and hedging mechanism (5) is provided on the side of the processing barrel (2), a temperature control mechanism (6) is provided on the side of the premixing and hedging mechanism (5), the auxiliary synthesis mechanism (4) comprises a positioning support frame (41), a driving motor (42), a transmission shaft (43), a stirring blade (44), a supporting rod (45) and a limiting filter plate (46), the sealing cover (3) is provided on the top outer wall of the processing barrel (2), an auxiliary synthesis mechanism (4) is provided inside the processing barrel (2), a premixing and hedging mechanism (5) is provided on the side of the premixing and hedging mechanism (5), the auxiliary synthesis mechanism (4) comprises a positioning support frame (41), a driving motor (42), a transmission shaft (43), a stirring blade (44), a supporting rod (45) and a limiting filter plate (46), the sealing cover (44) is provided on the top outer wall of the processing barrel (2), the auxiliary synthesis mechanism (4) comprises a positioning support frame (41), a driving motor (42), a transmission shaft (43), a stirring blade (44), a supporting rod (45) and a limiting filter plate (46), the sealing cover (46 ... A positioning support frame (41) is arranged on the top outer wall of the cover (3), a driving motor (42) is arranged on the top outer wall of the positioning support frame (41), the driving motor (42) is connected to the top outer wall of the transmission shaft (43), the bottom outer wall of the transmission shaft (43) is rotatably mounted on the bottom inner wall of the processing barrel (2), a stirring blade (44) is arranged outside the transmission shaft (43) inside the processing barrel (2), and support rods (45) are arranged around the side outer wall of the transmission shaft (43) at equal intervals, the support rods (45) are arranged in a "[" shape, and a limiting filter plate (46) is arranged on the side outer wall of the support rod (45).
2. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 1, characterized in that: The stirring blade (44) is configured as a spiral structure, and the limiting filter plate (46) is configured as a porous plate structure.
3. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 1, characterized in that: The premixing and hedging mechanism (5) comprises a feed hopper (51), a liquid storage tank (52), a limiting partition (53) and a first variable speed water pump (54); the top outer wall of the sealing cover (3) is connected to and installed with the feed hopper (51); the top outer wall of the supporting base (1) is provided with a liquid storage tank (52); the bottom inner wall of the liquid storage tank (52) at the middle position is provided with a limiting partition (53); the limiting partition (53) divides the inside of the liquid storage tank (52) into two complete closed spaces; the bottom inner wall of the first space of the liquid storage tank (52) is provided with a first variable speed water pump (54).
4. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 3, characterized in that: A second variable-speed water pump (55) is disposed on the inner wall at the bottom end of the second space of the liquid storage tank (52); the first variable-speed water pump (54) is connected to one end of a first flow guide pipe (56); and the other end of the first flow guide pipe (56) is connected to an outer wall of one side of the feed hopper (51) and installed.
5. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 4, characterized in that: The second variable speed water pump (55) is connected to one end of the second flow guide pipe (57), and the other end of the second flow guide pipe (57) is connected to the outer wall of the other side of the feed hopper (51) and installed.
6. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 5, characterized in that: The top of the feed hopper (51) is provided with a sealing structure, and the top outer wall of the liquid storage tank (52) is symmetrically connected with two liquid injection pipes.
7. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 1, characterized in that: The temperature control mechanism (6) comprises a heating base (61), a power supply (62), a controller (63) and a protective cover (64); the top outer wall of the support base (1) is provided with a heating base (61); the top outer wall of the heating base (61) is connected to the bottom outer wall of the processing barrel (2); the top outer wall of the support base (1) is provided with a power supply (62) and a controller (63); and a protective cover (64) is provided outside the power supply (62) and the controller (63).
8. A feed device for producing and synthesizing dodecanol glycidyl ether according to claim 7, characterized in that: The bottom outer wall of the protective cover (64) is connected to the top outer wall of the support base (1), and the top outer wall of the protective cover (64) is provided with a temperature monitoring sensor (65). A temperature conducting rod (66) is connected and installed between the temperature monitoring sensor (65) and the side outer wall of the processing barrel (2).
Citation Information
Patent Citations
Feeding mechanism and catalyst synthesis device thereof
CN220803116U