Hydrogenation system of phytosterol and hydrogenation method thereof
By setting up a homogenization assembly, a heating plate, agitating assembly and temperature control assembly in the phytosterol hydrogenation reactor, the problem of heat inhomogeneity between phytosterol and reaction solvents is solved, the quality of hydrogenation reaction and the accuracy of temperature control are improved, and the difficulty of cleaning is reduced.
Patent Information
- Application Number
- CN202510772724.6
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Priority Date
- 2025-04-24
- Filing Date
- 2025-06-11
- Publication Date
- 2025-08-15
- Estimated Expiration
- Not applicable · inactive patent
AI Technical Summary
The existing phytosterol hydrogenation reactors have problems with heat inhomogeneity between phytosterols and reaction solvents, which affects the quality of the hydrogenation reaction.
The fixed sleeve is uniformly heated by a homogenizing component and a heating plate, combining the agitating component and the oscillating component to improve the mixing uniformity, and maintain an appropriate temperature through the temperature control component, and continuously inject hydrogen into the hydrogenation component for addition reaction.
It improves the heating uniformity and mixing uniformity of phytosterols, ensures the quality of hydrogenation reaction, and effectively reduces the difficulty of cleaning inside the reactor and the accuracy of temperature control.
Smart Images

Figure CN120479360A_ABST
Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of chemical agent manufacturing, in particular to a phytosterol hydrogenation system and a hydrogenation method thereof. Background Art
[0002] Phytosterols are a type of steroidal components present in plant cells. They can lower blood cholesterol, improve symptoms related to benign prostatic hyperplasia, and have anti-aging effects in the human body. Phytosterol hydrogenation is a chemical process that saturates the unsaturated bonds in phytosterols through hydrogenation reactions, which can improve the chemical stability of phytosterols.
[0003] When performing the phytosterol hydrogenation reaction, a dedicated hydrogenation reactor is required, and temperature is an important parameter affecting the hydrogenation reaction rate. Higher temperatures can accelerate the reaction rate. In actual operation, the temperature is usually controlled between 100-250°C. However, when the existing reactor performs the phytosterol hydrogenation reaction on the phytosterols, the phytosterols and solvent accumulate at the bottom of the reactor under the action of gravity. When the phytosterols and the reaction solvent are heated, the temperature of the phytosterols and the reaction solvent in direct contact with the inner wall of the reactor will be significantly higher than that of the sterols away from the reactor. Even if the sterols inside the reactor are stirred, the stirring blades cannot directly contact the inner wall of the reactor and can only stir in a single direction, which cannot improve the heating uniformity of the phytosterols. As a result, the quality of the hydrogenation reaction is adversely affected by the heating uniformity of the phytosterols and the reaction solvent. Summary of the Invention
[0004] The purpose of the present invention is to provide a plant sterol hydrogenation system and a hydrogenation method thereof, which uniformly heats the fixed sleeve through a heating plate to improve the heating uniformity of the sterols, thereby solving the problems raised in the above background technology.
[0005] To achieve the above object, the present invention provides the following technical solution: a phytosterol hydrogenation system, comprising a reactor, wherein a motor is fixedly connected to the outer surface of the left end of the reactor, a drive rod is fixedly connected to the right end of the motor output shaft, and a material distribution assembly is provided on the outer side of the drive rod; The material distribution assembly includes a pull rod fixedly connected to the outer surface of the driving rod, the pull rod is fixedly connected to a fixed sleeve at one end away from the driving rod, the fixed sleeve is rotatably connected to the left and right ends of the inner surface of the reactor, the inner surface of the fixed sleeve is fixedly connected to a baffle, the lower side of the inner surface of the reactor is fixedly connected to a thermal insulation pad, the outer surface of the upper end of the thermal insulation pad is fixedly connected to a heating plate, and the heating plate is in rotational contact with the outer surface of the fixed sleeve.
[0006] Preferably, the heating plate is arc-shaped, the number of the heating plates is several groups and distributed in a linear array, the driving rod extends to the outside of the reactor away from the end of the motor and is rotatably connected to the reactor, a material guide cavity is opened on the inside of the driving rod, the number of the pull rods is several groups and symmetrically distributed, and the outer surface of the baffle is arc-shaped and is equidistantly distributed on the inner wall of the fixed sleeve.
[0007] Preferably, a stirring assembly is provided on the outside of the driving rod, and the stirring assembly includes a rotating seat fixedly connected to the outer surface of the driving rod, a connecting plate fixedly connected to the outer surface of the rotating seat, and a flap fixedly connected to the end of the connecting plate away from the rotating seat, and the flap is arc-shaped. The number of the connecting plates and the flaps is several groups and distributed in a ring array.
[0008] Preferably, an oscillation component is provided on the outside of the connecting plate, and the oscillation component includes a slide groove opened on the outer surface of the connecting plate, a slide rod is slidably connected to the inside of the slide groove, and the two ends of the slide rod are respectively fixedly connected to stop wheels, and the stop wheels are symmetrically distributed on both sides of the flap.
[0009] Preferably, a feeding assembly is provided on the inner side of the driving rod, and the feeding assembly includes feeding holes opened on the outer surface of the driving rod, and the number of the feeding holes is several groups and distributed in a ring array, and the outer surface of the right end of the reactor is fixedly connected to a receiving hopper, and the upper end of the receiving hopper is open, and the right end of the driving rod passes through the inside of the receiving hopper, and the outer surface of the driving rod is provided with a feeding trough inside the receiving hopper, and the number of the feeding troughs is several groups and distributed in a ring array, and a feeding pipe is fixedly connected to the upper side of the outer surface of the reactor.
[0010] Preferably, a hydrogenation assembly is provided on the inner side of the material guide cavity, and the hydrogenation assembly includes a sealing plate fixedly connected to the inner surface of the material guide cavity, and an air guide pipe is fixedly connected to the outer surface of the sealing plate. The air guide pipe is located inside the material guide cavity, and the right end of the air guide pipe passes through the outside of the material receiving hopper and is rotatably connected to the material receiving hopper. A connecting pipe is embedded on the inner side of the rotating seat.
[0011] Preferably, an overflow groove is embedded on the inner side of the connecting plate, one end of the connecting pipe is fixedly connected to the inside of the air guide pipe and the other end is connected to the inside of the overflow groove, a nozzle is embedded and fixedly connected on the inner side of the slide groove, and the nozzle is connected to the inside of the overflow groove. The number of the nozzles is several groups and distributed in a parallel array.
[0012] Preferably, a temperature control component is provided between the fixed sleeve and the reactor, the temperature control component includes a through hole opened on the outer surface of the reactor, the through hole penetrates to the inner side of the reactor, the inner surface of the reactor is slidably connected with a movable plate, the movable plate is arc-shaped and is in sliding contact with the inner wall of the reactor, the outer surface of the lower end of the heating plate is fixedly connected with a fixed plate 1, the outer surface of the movable plate away from the through hole is fixedly connected with a fixed plate 2, a capsule is fixedly connected between the fixed plates 1 and 2, and the interior of the capsule is filled with thermal expansion gas.
[0013] Preferably, a vacuum tube is fixedly connected to the outer surface of the right end of the reactor, a base is fixedly connected to the outer surface of the lower end of the reactor, a through groove is opened through the outer surface of the base, and a discharge pipe is fixedly connected to the outer surface of the right end of the reactor, and the discharge pipe is located on the lower side of the vacuum tube.
[0014] A hydrogenation method applicable to a phytosterol hydrogenation system comprises the following steps: S1: injecting sterol and reaction solvent into the fixed sleeve through the feeding tube, and evenly adding the catalyst into the sterol and reaction solvent through the feeding component; S2: The hydrogen is then transported to the interior of the connecting tube through the gas guide tube and sprayed into the interior of the sterol and reaction solvent through the nozzle at a certain pressure; S3: The driving rod drives the connecting plate to rotate synchronously through the rotating seat. The rotation of the flip plate can flip the sterol and reaction solvent inside the fixed sleeve; S4: The sliding rod collides with the connecting plate through the notch, causing the connecting plate and the flap to vibrate to a certain extent, thereby accelerating the falling of the sterol on the surface of the connecting plate and the flap; S5: The driving rod drives the fixed sleeve to perform circular motion through the pull rod, so that the fixed sleeve can be evenly heated by the heating plate; S6: The through hole is opened so that external air can enter between the fixed sleeve and the reactor through the through hole, thereby ventilating and dissipating heat inside the reactor through the flow of air.
[0015] Compared with the prior art, the present invention has the following beneficial effects: 1. This solution uses a material distribution assembly to evenly heat the fixed sleeve using a heating plate, which helps improve the uniformity of sterol heating. The baffles can increase the friction between the fixed sleeve and the sterol, thereby disturbing the sterol through the baffles, further improving the uniformity of mixing of sterol, butanol and catalyst, and thus effectively improving the quality of the sterol hydrogenation reaction. 2. This solution uses an oscillation component. The grooves on the surface of the connecting plate can cause the sterol and reaction solvent to flow irregularly. The sliding rod collides with the connecting plate through the notch, causing the connecting plate and the flap to vibrate to a certain extent. This can accelerate the falling of the sterol on the surface of the connecting plate and the flap, helping to reduce the sterol residue on the surface of the connecting plate and the flap, thereby effectively reducing the difficulty of cleaning the interior of the reactor. 3. This solution sets a temperature control component to open the through hole according to the temperature change, so that the outside air can enter between the fixed sleeve and the reactor through the through hole, thereby ventilating and dissipating the heat inside the reactor through the flow of air, and then maintaining the internal temperature of the reactor within an appropriate range, thereby ensuring the quality of the sterol hydrogenation reaction. BRIEF DESCRIPTION OF THE DRAWINGS
[0016] In order to more clearly illustrate the specific embodiments of the present invention or the technical solutions in the prior art, the following briefly introduces the drawings required for use in the specific embodiments or the description of the prior art. Obviously, the drawings described below are some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.
[0017] Figure 1 It is a schematic diagram of the overall structure of the present invention; Figure 2 It is a top view of the overall structure of the present invention; Figure 3 For the present invention Figure 2 Middle AA section view; Figure 4 For the present invention Figure 2 Middle BB section view; Figure 5 For the present invention Figure 2 Middle CC section view; Figure 6 For the present invention Figure 4 The enlarged schematic diagram of point D in the middle; Figure 7 For the present invention Figure 4 The enlarged schematic diagram at E in the middle; Figure 8 For the present invention Figure 5 Enlarged schematic diagram at point F in the middle.
[0018] Description of reference numerals: 11. Base; 12. Through slot; 13. Reactor; 14. Motor; 15. Feeding pipe; 16. Vacuum tube; 17. Hopper; 18. Air guide tube; 19. Discharge pipe; 20. Through hole; 21. Drive rod; 22. Guide cavity; 23. Fixed sleeve; 24. Pull rod; 25. Rotating seat; 26. Baffle; 27. Heating plate; 28. Feeding hole; 29. Sealing plate; 30. Connecting plate; 31. Connecting pipe; 32. Overflow trough; 33. Nozzle; 34. Slide rod; 35. Slide; 36. Baffle wheel; 37. Fixed plate 1; 38. Capsule; 39. Fixed plate 2; 40. Movable plate; 41. Feed trough; 42. Insulation pad; 43. Flip plate. DETAILED DESCRIPTION
[0019] The following will clearly and completely describe the technical solutions in the embodiments of the present invention in conjunction with the accompanying drawings. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without making creative efforts are within the scope of protection of the present invention.
[0020] See also Figures 1 to 8 , the present invention provides a technical solution: A plant sterol hydrogenation system includes a reactor 13, a motor 14 is fixedly connected to the outer surface of the left end of the reactor 13, a drive rod 21 is fixedly connected to the right end of the output shaft of the motor 14, and a material distribution assembly is provided on the outer side of the drive rod 21; The material distribution assembly includes a pull rod 24 fixedly connected to the outer surface of the driving rod 21, and the pull rod 24 is fixedly connected to a fixed sleeve 23 at one end away from the driving rod 21. The fixed sleeve 23 is rotatably connected to the left and right ends of the inner surface of the reactor 13, and a baffle 26 is fixedly connected to the inner surface of the fixed sleeve 23. The lower side of the inner surface of the reactor 13 is fixedly connected to a thermal insulation pad 42, and the outer surface of the upper end of the thermal insulation pad 42 is fixedly connected to a heating plate 27, and the heating plate 27 is in rotational contact with the outer surface of the fixed sleeve 23.
[0021] The heating plate 27 is arc-shaped, and the number of the heating plates 27 is several groups and distributed in a linear array. The driving rod 21 extends to the outside of the reactor 13 at one end away from the motor 14 and is rotatably connected to the reactor 13. A material guide cavity 22 is opened on the inner side of the driving rod 21. The number of the pull rods 24 is several groups and is symmetrically distributed. The outer surface of the baffle 26 is arc-shaped and is equidistantly distributed on the inner wall of the fixed sleeve 23.
[0022] The outer surface of the right end of the reactor 13 is fixedly connected to a vacuum tube 16, the outer surface of the lower end of the reactor 13 is fixedly connected to a base 11, and a through groove 12 is opened through the outer surface of the base 11. The outer surface of the right end of the reactor 13 is fixedly connected to a discharge pipe 19, and the discharge pipe 19 is located on the lower side of the vacuum tube 16.
[0023] By adopting the above technical solution, when hydrogenating sterols, it is usually necessary to keep the sterols at an appropriate reaction temperature in order to increase the reaction speed. In order to keep the temperature of the sterols inside the reactor 13 consistent, a material equalization component is set. During operation, the base 11 supports the reactor 13. The fixed sleeve 23 inside the reactor 13 is used to place the reaction raw materials. Before the reaction raw materials are injected, the excess air inside the fixed sleeve 23 is extracted through the vacuum tube 16 to reduce the probability of oxidation reaction between the sterols and oxygen in the air. During the sterol hydrogenation reaction, the heating plate 27 generates heat and transfers it to the fixed sleeve 23. The heat is transferred to the reaction raw materials through the fixed sleeve 23, so that the temperature inside the fixed sleeve 23 is kept within an appropriate range. The output shaft of the motor 14 drives the drive rod 21 to rotate synchronously, and the drive rod 2 The fixed sleeve 23 is driven by the pull rod 24 to perform circular motion. Under the action of gravity, the sterol and reaction solvent (common reaction solvents include butanol, isopropanol, etc.) will always gather in the lower area inside the fixed sleeve 23. During the rotation process, the outer surface of the fixed sleeve 23 will rotate and contact with the heating plate 27, so that the fixed sleeve 23 can be evenly heated by the heating plate 27, which helps to improve the heating uniformity of the sterol. At the same time, during the rotation process, the internal baffles 26 of the fixed sleeve 23 can increase the friction between the fixed sleeve 23 and the sterol, so that the baffles 26 can disturb the sterol, thereby further improving the mixing uniformity of the sterol, butanol and catalyst, thereby effectively improving the quality of the sterol hydrogenation reaction. After the hydrogenation reaction is completed, the material is discharged to the outside of the reactor 13 through the discharge pipe 19.
[0024] Specifically, such as Figure 3 and Figure 4 As shown, a stirring assembly is provided on the outside of the driving rod 21, and the stirring assembly includes a rotating seat 25 fixedly connected to the outer surface of the driving rod 21, and a connecting plate 30 is fixedly connected to the outer surface of the rotating seat 25. The connecting plate 30 is fixedly connected to the end away from the rotating seat 25 with a flap 43, and the flap 43 is arc-shaped. The number of the connecting plates 30 and the flap 43 is several groups and distributed in a ring array.
[0025] By adopting the above technical solution, in order to further improve the mixing uniformity and heating uniformity between the sterols, reaction solvent and catalyst, a stirring assembly is provided. During operation, the driving rod 21 drives the connecting plate 30 to rotate synchronously through the rotating seat 25, and drives the flap 43 to perform circular motion inside the fixed sleeve 23 through the connecting plate 30. The rotation of the flap 43 can flip the sterols and reaction solvent inside the fixed sleeve 23, so that the sterols, reaction solvent and catalyst can be fully mixed and contacted, thereby increasing the reaction speed and further improving the quality of the sterol hydrogenation reaction.
[0026] Specifically, such as Figure 4 and Figure 7 As shown, an oscillation component is provided on the outside of the connecting plate 30, and the oscillation component includes a slide groove 35 opened on the outer surface of the connecting plate 30, and a slide rod 34 is slidably connected to the inside of the slide groove 35. The two ends of the slide rod 34 are respectively fixedly connected to the blocking wheels 36, and the blocking wheels 36 are symmetrically distributed on both sides of the flap 43.
[0027] By adopting the above technical solution, during the operation of the stirring component, in order to reduce the residue of the reaction raw materials on the surface of the flap 43 and the connecting plate 30, an oscillation component is set, and the slide groove 35 opened on the surface of the connecting plate 30 is used to guide and support the slide rod 34. When the driving rod 21 drives the connecting plate 30 to rotate to stir the sterol and the reaction solvent, the slide groove 35 on the surface of the connecting plate 30 can make the sterol and the reaction solvent flow irregularly, thereby further improving the mixing uniformity of the sterol and the reaction solvent. The blocking wheels 36 at both ends of the slide rod 34 can not only increase the counterweight of the slide rod 34, but also prevent the slide rod 34 from sliding When the connecting plate 30 is rotated to the upper side, the slide bar 34 and the stop wheel 36 will move toward the side of the rotating seat 25 under the action of gravity, and when the connecting plate 30 is rotated to the lower side of the driving rod 21, the slide bar 34 will slide toward the side of the flap 43, and the slide bar 34 will collide with the connecting plate 30 through the slot, thereby causing the connecting plate 30 and the flap 43 to vibrate to a certain extent, thereby accelerating the falling of sterols on the surfaces of the connecting plate 30 and the flap 43, helping to reduce the residual sterols on the surfaces of the connecting plate 30 and the flap 43, and thus effectively reducing the difficulty of cleaning the inside of the reactor 13.
[0028] Specifically, such as Figure 4 and Figure 6As shown, a feeding assembly is provided on the inner side of the driving rod 21, and the feeding assembly includes a feeding hole 28 opened on the outer surface of the driving rod 21, and the number of the feeding holes 28 is several groups and distributed in a ring array. The outer surface of the right end of the reactor 13 is fixedly connected to the receiving hopper 17, and the upper end of the receiving hopper 17 is open. The right end of the driving rod 21 passes through the inside of the receiving hopper 17, and the outer surface of the driving rod 21 is provided with a feeding trough 41 on the inner side of the receiving hopper 17. The number of the feeding troughs 41 is several groups and distributed in a ring array. The upper side of the outer surface of the reactor 13 is fixedly connected to the feeding pipe 15.
[0029] By adopting the above technical solution, sterols and reaction solvents are injected into the fixed sleeve 23 through the feeding pipe 15. During the sterol hydrogenation reaction, an appropriate amount of catalyst needs to be added to maintain the normal progress of the addition reaction. In order to improve the uniformity of catalyst feeding, a feeding assembly is set. During operation, the catalyst is injected into the receiving hopper 17. During the rotation of the driving rod 21, the catalyst will enter the guide cavity 22 through the feeding groove 41 on the surface of the driving rod 21. As the driving rod 21 continues to rotate, the catalyst will move inside the guide cavity 22, and then the catalyst will enter the fixed sleeve 23 through the feeding hole 28 on the surface of the driving rod 21. The sterol and reaction solvent are stirred along with the connecting plate 30 and the flap 43, so that the catalyst is evenly fed into the sterol and the reaction solvent, thereby improving the quality of the sterol hydrogenation reaction to a certain extent.
[0030] Specifically, such as Figure 4 、 Figure 6 and Figure 7 As shown, a hydrogenation assembly is provided inside the material guide cavity 22, and the hydrogenation assembly includes a sealing plate 29 fixedly connected to the inner surface of the material guide cavity 22, and an air guide pipe 18 is fixedly connected to the outer surface of the sealing plate 29. The air guide pipe 18 is located inside the material guide cavity 22, and the right end of the air guide pipe 18 passes through the outside of the material receiving hopper 17 and is rotatably connected to the material receiving hopper 17. A connecting pipe 31 is embedded in the inner side of the rotating seat 25.
[0031] An overflow groove 32 is embedded on the inner side of the connecting plate 30, one end of the connecting pipe 31 is fixedly connected to the inside of the air guide pipe 18 and the other end is connected to the inside of the overflow groove 32, and a nozzle 33 is embedded and fixedly connected on the inner side of the slide groove 35. The nozzle 33 is connected to the inside of the overflow groove 32, and the number of the nozzles 33 is several groups and distributed in a parallel array.
[0032] By adopting the above technical solution, when the sterols and the reaction solvent are stirred, hydrogen needs to be continuously injected into the reactor 13. For this purpose, a hydrogenation assembly is provided. During operation, hydrogen is injected into the air duct 18. The driving rod 21 fixes and supports the air duct 18 through the sealing plate 29. The hydrogen is then transported to the interior of the connecting pipe 31 through the air duct 18. The hydrogen is then transported to the nozzle 33 through the connecting pipe 31 and the overflow groove 32, and is sprayed into the interior of the sterols and the reaction solvent through the nozzle 33 at a certain pressure. Through the continuous injection of hydrogen, under the action of the catalyst, the hydrogen reacts with the unsaturated bonds in the sterols to improve the chemical stability of the sterols during storage and transportation.
[0033] Specifically, such as Figure 5 and Figure 8 As shown, a temperature control component is provided between the fixed sleeve 23 and the reactor 13. The temperature control component includes a through hole 20 opened on the outer surface of the reactor 13. The through hole 20 penetrates to the inner side of the reactor 13. The inner surface of the reactor 13 is slidably connected with a movable plate 40. The movable plate 40 is arc-shaped and is in sliding contact with the inner wall of the reactor 13.
[0034] A fixing plate 1 37 is fixedly connected to the outer surface of the lower end of the heating plate 27, and a fixing plate 2 39 is fixedly connected to the outer surface of the movable plate 40 away from the through hole 20. A capsule 38 is fixedly connected between the fixing plates 1 37 and 2 39, and the capsule 38 is filled with thermal expansion gas.
[0035] By adopting the above technical solution, during the sterol hydrogenation reaction, a suitable temperature can effectively increase the reaction speed. For this purpose, a temperature control component is set. The movable plate 40 is used to seal the through hole 20. When the temperature inside the fixed sleeve 23 rises, the heat will be transferred to the capsule 38 through the heating plate 27 and the fixed plate 1 37. At this time, the gas inside the capsule 38 will expand due to the heat, thereby gradually increasing the volume of the capsule 38. The capsule 38 will push the fixed plate 2 39, and the movable plate 40 will be driven by the fixed plate 2 39 to move along the inside of the reactor 13. As the movable plate 40 gradually moves, the movable plate 40 will be out of contact with the through hole 20, thereby opening the through hole 20, so that external air can enter between the fixed sleeve 23 and the reactor 13 through the through hole 20, so that the interior of the reactor 13 can be ventilated and heat-dissipated by the flow of air, so that the internal temperature of the reactor 13 can be maintained within an appropriate range, thereby ensuring the quality of the sterol hydrogenation reaction. Gate valves for controlling on and off are provided inside the feeding pipe 15 and the discharging pipe 18, so as to ensure the sealing of the interior of the reactor 13.
[0036] A hydrogenation method applicable to a phytosterol hydrogenation system comprises the following steps: S1: injecting sterol and reaction solvent into the fixed sleeve 23 through the feeding pipe 15, and evenly adding the catalyst into the sterol and reaction solvent through the feeding component; S2: The hydrogen is then transported to the interior of the connecting pipe 31 through the gas guide pipe 18 and ejected into the interior of the sterol and the reaction solvent through the nozzle 33 at a certain pressure; S3: The driving rod 21 drives the connecting plate 30 to rotate synchronously through the rotating seat 25, and the sterol and reaction solvent inside the fixed sleeve 23 can be flipped by the rotation of the flip plate 43; S4: The sliding rod 34 collides with the connecting plate 30 through the notch, causing the connecting plate 30 and the flap 43 to vibrate to a certain extent, thereby accelerating the falling of the sterol on the surface of the connecting plate 30 and the flap 43; S5: The driving rod 21 drives the fixing sleeve 23 to perform circular motion through the pull rod 24, so that the fixing sleeve 23 can be evenly heated by the heating plate 27; S6: The through hole 20 is opened so that external air can enter between the fixing sleeve 23 and the reactor 13 through the through hole 20 , thereby ventilating and dissipating heat inside the reactor 13 through the flow of air.
[0037] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit it. Although the present invention has been described in detail with reference to the above embodiments, those skilled in the art should understand that they can still modify the technical solutions described in the above embodiments, or replace some or all of the technical features therein with equivalents. However, these modifications or replacements do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of the present invention.
Claims
1. A phytosterol hydrogenation system, comprising a reactor (13), wherein a motor (14) is fixedly connected to the outer surface of the left end of the reactor (13), and a drive rod (21) is fixedly connected to the right end of the output shaft of the motor (14), characterized in that: A material distribution component is provided on the outside of the driving rod (21); The material distribution assembly includes a pull rod (24) fixedly connected to the outer surface of the driving rod (21), the pull rod (24) is fixedly connected to a fixed sleeve (23) at one end away from the driving rod (21), the fixed sleeve (23) is rotatably connected to the left and right ends of the inner surface of the reactor (13), the inner surface of the fixed sleeve (23) is fixedly connected to a blocking bar (26), the lower side of the inner surface of the reactor (13) is fixedly connected to a heat insulation pad (42), the outer surface of the upper end of the heat insulation pad (42) is fixedly connected to a heating plate (27), and the heating plate (27) is in rotational contact with the outer surface of the fixed sleeve (23).
2. A phytosterol hydrogenation system according to claim 1, characterized in that: The heating plate (27) is in an arc shape, and the number of the heating plates (27) is several groups and distributed in a linear array. The end of the driving rod (21) away from the motor (14) passes through the outside of the reactor (13) and is rotatably connected to the reactor (13). A material guide cavity (22) is opened through the inside of the driving rod (21). The number of the pull rods (24) is several groups and is symmetrically distributed. The outer surface of the blocking bar (26) is in an arc shape and is equidistantly distributed on the inner wall of the fixed sleeve (23).
3. A phytosterol hydrogenation system according to claim 2, characterized in that: A stirring assembly is provided on the outside of the driving rod (21), and the stirring assembly includes a rotating seat (25) fixedly connected to the outer surface of the driving rod (21), a connecting plate (30) fixedly connected to the outer surface of the rotating seat (25), and a flap (43) fixedly connected to one end of the connecting plate (30) away from the rotating seat (25), and the flap (43) is in an arc shape. The connecting plates (30) and the flap (43) are both provided in a plurality of groups and are distributed in a ring array.
4. A phytosterol hydrogenation system according to claim 3, characterized in that: An oscillating assembly is provided on the outside of the connecting plate (30), and the oscillating assembly includes a slide groove (35) provided on the outer surface of the connecting plate (30), a slide rod (34) is slidably connected to the inside of the slide groove (35), and blocking wheels (36) are fixedly connected to both ends of the slide rod (34), and the blocking wheels (36) are symmetrically distributed on both sides of the flap (43).
5. A phytosterol hydrogenation system according to claim 4, characterized in that: A feeding assembly is provided on the inner side of the driving rod (21), and the feeding assembly includes feeding holes (28) opened on the outer surface of the driving rod (21), and the number of the feeding holes (28) is several groups and distributed in a ring array. The outer surface of the right end of the reactor (13) is fixedly connected to a receiving hopper (17), and the upper end of the receiving hopper (17) is open. The right end of the driving rod (21) passes through the inside of the receiving hopper (17), and the outer surface of the driving rod (21) is provided with a feeding trough (41) located inside the receiving hopper (17). The number of the feeding troughs (41) is several groups and distributed in a ring array. The upper side of the outer surface of the reactor (13) is fixedly connected to a feeding pipe (15).
6. A phytosterol hydrogenation system according to claim 5, characterized in that: A hydrogenation assembly is provided inside the material guide cavity (22), and the hydrogenation assembly includes a sealing plate (29) fixedly connected to the inner surface of the material guide cavity (22). An air guide pipe (18) is fixedly connected to the outer surface of the sealing plate (29). The air guide pipe (18) is located inside the material guide cavity (22). The right end of the air guide pipe (18) passes through the outside of the receiving hopper (17) and is rotatably connected to the receiving hopper (17). A connecting pipe (31) is embedded inside the rotating seat (25).
7. A phytosterol hydrogenation system according to claim 6, characterized in that: An overflow groove (32) is embedded in the inner side of the connecting plate (30), one end of the connecting pipe (31) is fixedly connected to the inside of the air guide pipe (18) and the other end is connected to the inside of the overflow groove (32), and a nozzle (33) is embedded and fixedly connected to the inner side of the chute (35), and the nozzle (33) is connected to the inside of the overflow groove (32). The number of the nozzles (33) is several groups and is distributed in a parallel array.
8. A phytosterol hydrogenation system according to claim 7, characterized in that: A temperature control component is provided between the fixed sleeve (23) and the reactor (13), and the temperature control component includes a through hole (20) opened on the outer surface of the reactor (13), the through hole (20) penetrates to the inner side of the reactor (13), and the inner surface of the reactor (13) is slidably connected with a movable plate (40), the movable plate (40) is arc-shaped and is in sliding contact with the inner wall of the reactor (13), the outer surface of the lower end of the heating plate (27) is fixedly connected with a fixed plate 1 (37), the outer surface of the movable plate (40) away from the through hole (20) is fixedly connected with a fixed plate 2 (39), a capsule (38) is fixedly connected between the fixed plate 1 (37) and the fixed plate 2 (39), and the interior of the capsule (38) is filled with thermal expansion gas.
9. A phytosterol hydrogenation system according to claim 8, characterized in that: The outer surface of the right end of the reactor (13) is fixedly connected to a vacuum tube (16), the outer surface of the lower end of the reactor (13) is fixedly connected to a base (11), the outer surface of the base (11) is penetrated by a through groove (12), and the outer surface of the right end of the reactor (13) is fixedly connected to a discharge pipe (19), and the discharge pipe (19) is located on the lower side of the vacuum tube (16).
10. The hydrogenation method applicable to a phytosterol hydrogenation system according to claim 9, characterized in that: The steps include: S1: injecting sterol and reaction solvent into the interior of the fixed sleeve (23) through the feeding pipe (15), and evenly adding the catalyst into the sterol and reaction solvent through the feeding component; S2: The hydrogen is then transported to the interior of the connecting pipe (31) through the gas guide pipe (18) and ejected into the interior of the sterol and the reaction solvent through the nozzle (33) at a certain pressure; S3: The driving rod (21) drives the connecting plate (30) to rotate synchronously through the rotating seat (25), and the sterol and reaction solvent inside the fixed sleeve (23) can be flipped by the rotation of the flip plate (43); S4: The sliding rod (34) collides with the connecting plate (30) through the notch, thereby causing the connecting plate (30) and the flap (43) to vibrate to a certain extent, thereby accelerating the falling of the sterol on the surface of the connecting plate (30) and the flap (43); S5: The driving rod (21) drives the fixing sleeve (23) to perform circular motion via the pull rod (24), thereby uniformly heating the fixing sleeve (23) via the heating plate (27); S6: The through hole (20) is opened so that external air can enter between the fixed sleeve (23) and the reactor (13) through the through hole (20), thereby ventilating and dissipating heat inside the reactor (13) through the flow of air.