Ozonized oil production reactor

Abstract

The invention belongs to the technical field of ozonized oil preparation, and particularly relates to an ozonized oil production reactor which comprises a reaction tank, an oil inlet is formed in the middle of the reaction tank; a discharge hole is formed in the bottom of the reaction tank; the bottom of the reaction tank is fixedly connected with a gas conveyor; the top of the reaction tank is fixedly connected with a driving motor; the output end of the driving motor is fixedly connected with a rotating rod, and the rotating rod extends into the reaction tank; the end part of the rotating rod is rotationally connected with the gas conveyor; a gas cavity is formed in a rotating rod, a control switch of a driving motor is turned on, so that the driving motor drives the rotating rod to rotate, then a stirring rod stirs vegetable oil in the reaction tank, ozone gas is added while the vegetable oil is stirred, and the vegetable oil and the ozone gas can be mixed more sufficiently and quickly; the reaction speed between the vegetable oil and the ozone gas is increased, the preparation speed of the ozonized oil is increased, and meanwhile the production quality of the ozonized oil is improved.

Description

Technical Field

[0001] The invention belongs to the technical field of ozonated oil preparation, in particular to an ozonated oil production reactor. Background Art

[0002] Ozonated oil, also known as ozone oil or superoxygenated oil, is a remedy with multiple benefits.

[0003] It is a substance made by mixing ozone with a carrier oil (such as vegetable oil, mineral oil, etc.). Ozone O3 is a strong oxidant with broad-spectrum bactericidal, disinfectant, antiviral, deodorizing, antipruritic, wound healing and immune function enhancement functions. When ozone is mixed with oil, the ozone molecules will dissolve in the oil to form stable ozonated oil.

[0004] During the preparation process of ozonated oil, the vegetable oil and ozone gas are in a static state, which makes it difficult for the vegetable oil and ozone gas to mix effectively, affects the mixing reaction between the vegetable oil and ozone gas, and reduces the preparation effect.

[0005] To this end, the present invention provides an ozonated oil production reactor. Summary of the invention

[0006] In order to make up for the deficiencies of the prior art, at least one technical problem raised in the background technology is solved.

[0007] The technical solution adopted by the present invention to solve its technical problems is: an ozonated oil production reactor described in the present invention comprises a reaction tank; an oil inlet is provided in the middle of the reaction tank; a discharge port is provided at the bottom of the reaction tank; a gas conveyor is fixedly connected to the bottom of the reaction tank; a driving motor is fixedly connected to the top of the reaction tank; a rotating rod is fixedly connected to the output end of the driving motor, and the rotating rod extends into the reaction tank; the end of the rotating rod is rotatably connected to the gas conveyor; an air cavity is opened inside the rotating rod; the air cavity and the gas conveyor are interconnected; a plurality of stirring rods are installed in the middle of the rotating rod; the air cavity and the stirring rod are interconnected; an air hole is provided in the middle of the stirring rod. The above structure accelerates the reaction speed between vegetable oil and ozone gas, improves the preparation speed of ozonated oil, and improves the production quality of ozonated oil.

[0008] Preferably, the air hole comprises an air pipe, a first connecting pipe sleeve and a second connecting pipe sleeve; the end of the air pipe is fixedly connected to the rotating rod, and the air pipe and the air cavity are interconnected; the first connecting pipe sleeve and the second connecting pipe sleeve are both fixedly connected to the middle of the air pipe; the first connecting pipe sleeve is located on the air pipe near the rotating rod; the ends of the first connecting pipe sleeve and the second connecting pipe sleeve are hinged to each other; the air hole is opened on the second connecting pipe sleeve and the air pipe; a guide rail is fixedly connected inside the reaction tank; a baffle is rotatably connected to the middle of the guide rail; the rotating rod passes through the baffle and is fixedly connected to the baffle; the baffle is arranged above the air pipe; a plurality of electric push cylinders are fixedly connected to the top side wall of the baffle; the output end of the electric push cylinder passes through the baffle and is slidably connected to the baffle; a first sleeve is slidably connected to the middle of the first connecting pipe sleeve; the output end of the electric push cylinder and the first sleeve are hinged; the air pipe is arranged as a hose, and the above structure makes the mixing between the vegetable oil and the ozone gas more sufficient, thereby improving the mixing effect between the vegetable oil and the ozone gas.

[0009] Preferably, a second ring is fixedly connected to the middle of the second connecting pipe sleeve; a connecting rope is fixedly connected to the middle of the second ring; one end of the connecting rope away from the second ring is fixedly connected to the middle of the rotating rod. The above structure increases the stability of the second connecting pipe sleeve during the stirring process, and improves the protection effect of the reaction tank and the second connecting pipe sleeve.

[0010] Preferably, a water inlet pipe is fixedly connected to the bottom of the reaction tank; a cooling pipe is fixedly connected to the top of the water inlet pipe; a water outlet pipe is fixedly connected to the middle of the cooling pipe; the water outlet pipe and the reaction tank are fixedly connected; the water inlet pipe, cooling pipe and water outlet pipe are all interconnected. The above structure improves the stability during mixing and stirring, and improves the preparation quality of ozonated oil.

[0011] Preferably, a pair of slide grooves are provided on the inner side wall of the guide rail; the side wall of the baffle is symmetrically arranged and rotatably connected to multiple groups of ball bearings; the ball bearings are located inside the slide grooves and are arranged to roll with the slide grooves. The above structure reduces the friction loss between the guide rail and the baffle when the baffle rotates continuously driven by the rotating rod, thereby improving the service life of the guide rail and the baffle.

[0012] Preferably, heat dissipation holes are provided on the top of the reaction tank; there are multiple groups of heat dissipation holes, which are arranged in a circular array around the driving motor. The above structure reduces the loss of the electric push cylinder due to the difficulty in heat dissipation in a sealed environment, thereby improving the safety of the electric push cylinder.

[0013] Preferably, a plurality of groups of fan blades are fixedly connected to the middle portion of the rotating rod; the fan blades are arranged above the baffle, and the above structure accelerates the air flow, thereby achieving a better heat dissipation effect.

[0014] Preferably, a plurality of guide plates are fixedly connected to the top of the inner wall of the reaction tank; the guide plates are arranged at an angle; the guide plates are arranged close to the heat dissipation holes, and the stability of heat dissipation is increased through the above structure.

[0015] Preferably, a dustproof net is fixedly connected to the side wall of the heat dissipation hole, and the protection effect of the electric push cylinder is improved through the above structure.

[0016] Preferably, a shock-absorbing pad is fixedly connected to the driving motor; the shock-absorbing pad is arranged between the driving motor and the reaction tank. The above structure reduces vibration and improves the safety during the preparation of ozonated oil.

[0017] The beneficial effects of the present invention are as follows: 1. The ozonated oil production reactor described in the present invention, by turning on the control switch of the driving motor, makes the driving motor drive the rotating rod to rotate, and then makes the stirring rod stir the vegetable oil in the reaction tank. By stirring the vegetable oil while adding ozone gas, the vegetable oil and ozone gas can be mixed more fully and quickly, the reaction speed between the vegetable oil and ozone gas is accelerated, the preparation speed of the ozonated oil is increased, and the production quality of the ozonated oil is improved.

[0018] 2. The ozonated oil production reactor described in the present invention controls the electric push cylinder to move the second connecting pipe sleeve, thereby increasing the stirring range of the second connecting pipe sleeve, accelerating the flow rate of the vegetable oil, and making the mixing between the vegetable oil and the ozone gas more complete, thereby improving the mixing effect between the vegetable oil and the ozone gas. BRIEF DESCRIPTION OF THE DRAWINGS

[0019] The present invention will be further described below in conjunction with the accompanying drawings.

[0020] Figure 1 is a stereogram of the present invention; Figure 2 It is a structural schematic diagram of the reaction tank in the present invention; Figure 3 It is a structural schematic diagram of the transfer rod of the present invention; Figure 4 It is a schematic structural diagram of the stirring rod in the present invention; Figure 5 It is a structural schematic diagram of the chute in the present invention; In the figure: 1. reaction tank; 12. gas conveyor; 13. driving motor; 14. rotating rod; 15. air cavity; 16. stirring rod; 17. air hole; 18. oil inlet; 19. discharge port; 2. guide rail; 21. baffle; 22. electric push cylinder; 23. gas pipe; 24. first connecting pipe sleeve; 25. second connecting pipe sleeve; 26. first ring; 3. second ring; 31. connecting rope; 4. water inlet pipe; 41. cooling pipe; 42. water outlet pipe; 5. slide; 51. ball; 6. heat dissipation hole; 7. fan blade; 8. guide plate; 9. dust net; 10. shock pad. DETAILED DESCRIPTION

[0021] In order to make the technical means, creative features, objectives and effects achieved by the present invention easy to understand, the present invention is further explained below in conjunction with specific implementation methods.

[0022] like Figures 1 to 3 The ozonated oil production reactor described in the embodiment of the present invention comprises a reaction tank 1; an oil inlet 18 is provided in the middle of the reaction tank 1; a discharge port 19 is provided at the bottom of the reaction tank 1; a gas conveyor 12 is fixedly connected to the bottom of the reaction tank 1; a driving motor 13 is fixedly connected to the top of the reaction tank 1; a rotating rod 14 is fixedly connected to the output end of the driving motor 13, and the rotating rod 14 extends into the reaction tank 1; the end of the rotating rod 14 is rotatably connected to the gas conveyor 12; an air cavity 15 is provided inside the rotating rod 14; the air cavity 15 and the gas conveyor 12 are connected to each other; a plurality of stirring rods 16 are installed in the middle of the rotating rod 14; the air cavity 15 and the stirring rod 16 are connected to each other; an air hole 17 is provided in the middle of the stirring rod 16. When working, first The vegetable oil is put into the reaction tank 1 from the oil inlet 18, and then the valve is closed. The valve of the gas conveyor 12 is then opened to allow the ozone gas to be conveyed to the air cavity 15 through the gas conveyor 12. At this time, the ozone gas is sprayed into the vegetable oil through the air hole 17 through the connection between the air cavity 15 and the stirring rod 16. Then, the control switch of the driving motor 13 is turned on to allow the driving motor 13 to drive the rotating rod 14 to rotate, thereby allowing the stirring rod 16 to stir the vegetable oil in the reaction tank 1. By stirring the vegetable oil while adding ozone gas, the vegetable oil and the ozone gas can be mixed more fully and quickly, thereby accelerating the reaction speed between the vegetable oil and the ozone gas, increasing the preparation speed of the ozonated oil, and improving the production quality of the ozonated oil.

[0023] like Figures 2 to 4The air hole 17 comprises an air pipe 23, a first connecting pipe sleeve 24 and a second connecting pipe sleeve 25; the end of the air pipe 23 is fixedly connected to the rotating rod 14, and the air pipe 23 and the air cavity 15 are interconnected; the first connecting pipe sleeve 24 and the second connecting pipe sleeve 25 are both fixedly connected to the middle of the air pipe 23; the first connecting pipe sleeve 24 is located on the air pipe 23 near the rotating rod 14; the ends of the first connecting pipe sleeve 24 and the second connecting pipe sleeve 25 are hingedly arranged with each other; the air hole 17 is opened on the second connecting pipe sleeve 25 and the air pipe 23; a guide rail 2 is fixedly connected to the inside of the reaction tank 1; a baffle 21 is rotatably connected to the middle of the guide rail 2; the rotating rod 14 passes through the baffle 21 and is fixedly arranged with the baffle 21; the baffle 21 is arranged above the air pipe 23; a plurality of electric push cylinders 22 are fixedly connected to the top side wall of the baffle 21; the electric push cylinder 22 The output end passes through the baffle 21 and is slidably connected to the baffle 21; a first ring 26 is slidably connected to the middle of the first connecting pipe sleeve 24; the output end of the electric push cylinder 22 and the first ring 26 are hinged; the air supply pipe 23 is a hose setting. When working, by controlling the switch of the electric push cylinder 22, the output end of the electric push cylinder 22 pulls the first ring 26, so that the first ring 26 drives the first connecting pipe sleeve 24 to move upward. At this time, the second connecting pipe sleeve 25 is moved as a whole under the drive of the first connecting pipe sleeve 24. In the process of using the second connecting pipe sleeve 25 for stirring, the second connecting pipe sleeve 25 is moved by controlling the electric push cylinder 22, thereby increasing the stirring range of the second connecting pipe sleeve 25, accelerating the flow rate of the vegetable oil, and making the vegetable oil and ozone gas mixed more fully, thereby improving the mixing effect between the vegetable oil and the ozone gas.

[0024] like Figures 2 to 4 The second connecting pipe sleeve 25 is fixedly connected to a second ring 3 in the middle thereof; the second ring 3 is fixedly connected to a connecting rope 31 in the middle thereof; the end of the connecting rope 31 away from the second ring 3 is fixedly connected to the middle of the rotating rod 14. During operation, the position of the second connecting pipe sleeve 25 is limited by using the connecting rope 31, so that during the rotating stirring process of the second connecting pipe sleeve 25, the problem of the second connecting pipe sleeve 25 being thrown away due to excessive centrifugal force, resulting in the collision between the second connecting pipe sleeve 25 and the inner wall of the reaction tank 1, is reduced, and the connecting rope 31 limits the deviation angle of the second connecting pipe sleeve 25, thereby increasing the stability of the second connecting pipe sleeve 25 during the stirring process and improving the protection effect of the reaction tank 1 and the second connecting pipe sleeve 25.

[0025] like Figure 2The bottom of the reaction tank 1 is fixedly connected with a water inlet pipe 4; the top of the water inlet pipe 4 is fixedly connected with a cooling pipe 41; the middle of the cooling pipe 41 is fixedly connected with a water outlet pipe 42; the water outlet pipe 42 and the reaction tank 1 are fixedly connected; the water inlet pipe 4, the cooling pipe 41 and the water outlet pipe 42 are all interconnected. During operation, in the process of stirring and mixing the vegetable oil, heat will be generated due to the stirring heat phenomenon, resulting in an increase in the temperature of the vegetable oil. The ozone gas is easily decomposed after being heated, resulting in a decrease in the preparation quality of the ozonated oil. At this time, cold water is filled into the water inlet pipe 4, so that the cold water flows into the cooling pipe 41 through the water inlet pipe 4, and then flows out again through the water outlet pipe 42. When the cold water passes through the cooling pipe 41, the cold water absorbs the heat of the vegetable oil in the reaction tank 1, thereby reducing the problem of the vegetable oil, reducing the decomposition of the ozone gas, improving the stability during mixing and stirring, and improving the preparation quality of the ozonated oil.

[0026] like Figure 3 and Figure 5 As described, a pair of slide grooves 5 are provided on the inner side wall of the guide rail 2; the side wall of the baffle plate 21 is symmetrically arranged and rotatably connected to multiple groups of ball bearings 51; the ball bearings 51 are located inside the slide grooves 5, and are configured to roll with the slide grooves 5. During operation, by providing the slide grooves 5 and the ball bearings 51 between the guide rail 2 and the baffle plate 21, part of the sliding friction between the guide rail 2 and the baffle plate 21 can be converted into rolling friction, thereby reducing the friction loss between the guide rail 2 and the baffle plate 21 when the baffle plate 21 continuously rotates driven by the rotating rod 14, thereby improving the service life of the guide rail 2 and the baffle plate 21.

[0027] like Figure 2 The top of the reaction tank 1 is provided with heat dissipation holes 6; there are multiple groups of heat dissipation holes 6, which are arranged in a circular array around the driving motor 13. When working, by providing multiple groups of heat dissipation holes 6 on the reaction tank 1, the heat above the baffle 21 can be dissipated to the outside through the heat dissipation holes 6, thereby reducing the temperature above the baffle 21, making the working environment of the electric push cylinder 22 more stable, reducing the loss of the electric push cylinder 22 due to the difficulty in heat dissipation in the sealed environment, and improving the safety of the use of the electric push cylinder 22.

[0028] like Figure 2 The rotating rod 14 has a plurality of sets of fan blades 7 fixedly connected to the middle part thereof; the fan blades 7 are arranged above the baffle 21. When the rotating rod 14 is in operation, the fan blades 7 are arranged on the rotating rod 14. When the rotating rod 14 rotates, the fan blades 7 are driven to rotate by the rotating rod 14, thereby accelerating the air flow and achieving a better heat dissipation effect.

[0029] like Figure 2The top of the inner wall of the reaction tank 1 is fixedly connected with a plurality of guide plates 8; the guide plates 8 are arranged at an angle; the guide plates 8 are arranged close to the heat dissipation holes 6. When working, the air flow is guided by the guide plates 8, so that the hot air can flow out of the outside through the heat dissipation holes 6 faster, thereby increasing the stability of heat dissipation.

[0030] like Figure 2 The top of the inner wall of the reaction tank 1 is fixedly connected with a plurality of guide plates 8; the guide plates 8 are arranged at an angle; the guide plates 8 are arranged close to the heat dissipation holes 6. When working, the air flow is guided by the guide plates 8, so that the hot air can flow out of the outside through the heat dissipation holes 6 faster, thereby increasing the stability of heat dissipation.

[0031] like Figure 1 The drive motor 13 is fixedly connected with a shock-absorbing pad 10; the shock-absorbing pad 10 is arranged between the drive motor 13 and the reaction tank 1. When working, the shock-absorbing pad 10 is arranged on the drive motor 13, and the vibration generated when the drive motor 13 is working is reduced by the shock-absorbing pad 10, thereby reducing the problem of vibration being transmitted to the reaction tank 1 and causing loss of the reaction tank 1, thereby improving the safety of ozonated oil preparation by reducing vibration.

[0032] During operation, the vegetable oil is firstly put into the reaction tank 1 from the oil inlet 18, and then the valve is closed, and then the valve of the gas conveyor 12 is opened to allow the ozone gas to be conveyed to the inside of the air cavity 15 through the gas conveyor 12. At this time, through the connection between the air cavity 15 and the stirring rod 16, the ozone gas is sprayed into the vegetable oil through the air hole 17, and then the control switch of the driving motor 13 is turned on to allow the driving motor 13 to drive the rotating rod 14 to rotate, and then the stirring rod 16 stirs the vegetable oil in the reaction tank 1. By stirring the vegetable oil while adding ozone gas, the vegetable oil and the ozone gas can be mixed more fully and quickly, which speeds up the reaction speed between the vegetable oil and the ozone gas, improves the preparation speed of the ozonated oil, and improves the production quality of the ozonated oil.

[0033] By controlling the switch of the electric push cylinder 22, the output end of the electric push cylinder 22 pulls the first ring 26, so that the first ring 26 drives the first connecting pipe sleeve 24 to move upward. At this time, the second connecting pipe sleeve 25 is moved as a whole under the drive of the first connecting pipe sleeve 24. During the stirring process using the second connecting pipe sleeve 25, the second connecting pipe sleeve 25 is moved by controlling the electric push cylinder 22, thereby increasing the stirring range of the second connecting pipe sleeve 25, accelerating the flow rate of the vegetable oil, and making the vegetable oil and ozone gas mix more fully, thereby improving the mixing effect between the vegetable oil and the ozone gas.

[0034] By using the connecting rope 31 to limit the position of the second connecting tube sleeve 25, the problem of the second connecting tube sleeve 25 being thrown away due to excessive centrifugal force during the rotation and stirring, which causes the second connecting tube sleeve 25 to collide with the inner wall of the reaction tank 1, is reduced. The connecting rope 31 limits the deviation angle of the second connecting tube sleeve 25, increases the stability of the second connecting tube sleeve 25 during the stirring process, and improves the protection effect of the reaction tank 1 and the second connecting tube sleeve 25.

[0035] During the stirring and mixing process of the vegetable oil, heat is generated due to the stirring heat phenomenon, causing the temperature of the vegetable oil to rise. The ozone gas is easily decomposed after being heated, resulting in a decrease in the preparation quality of the ozonated oil. At this time, cold water is filled into the water inlet pipe 4, so that the cold water flows into the cooling pipe 41 through the water inlet pipe 4, and then flows out again through the water outlet pipe 42. When the cold water passes through the cooling pipe 41, the cold water absorbs the heat of the vegetable oil in the reaction tank 1, thereby reducing the problem of the vegetable oil, reducing the decomposition of the ozone gas, improving the stability during mixing and stirring, and improving the preparation quality of the ozonated oil.

[0036] By providing a slide groove 5 and a ball 51 between the guide rail 2 and the baffle 21, part of the sliding friction between the guide rail 2 and the baffle 21 can be converted into rolling friction, thereby reducing the friction loss between the guide rail 2 and the baffle 21 when the baffle 21 continuously rotates under the drive of the rotating rod 14, thereby improving the service life of the guide rail 2 and the baffle 21.

[0037] By providing a plurality of groups of heat dissipation holes 6 on the reaction tank 1, the heat above the baffle 21 can be dissipated to the outside through the heat dissipation holes 6, thereby reducing the temperature above the baffle 21, making the working environment of the electric push cylinder 22 more stable, reducing the loss of the electric push cylinder 22 caused by the difficulty in heat dissipation in the sealed environment, and improving the safety of the use of the electric push cylinder 22.

[0038] By arranging the fan blades 7 on the rotating rod 14, when the rotating rod 14 rotates, the fan blades 7 are driven to rotate by the rotating rod 14, thereby accelerating the air flow and achieving a better heat dissipation effect.

[0039] The guide plate 8 is provided to guide the air flow, so that the hot air can flow out of the outside through the heat dissipation holes 6 more quickly, thereby increasing the stability of heat dissipation.

[0040] By providing a dustproof net 9 on the heat dissipation hole 6, it is possible to reduce the amount of dust and impurities from the outside entering the reaction tank 1 through the heat dissipation hole 6 to cause corrosion to the electric push cylinder 22, thereby improving the protection effect of the electric push cylinder 22.

[0041] By providing a shock-absorbing pad 10 on the driving motor 13, the shock-absorbing pad 10 reduces the vibration generated when the driving motor 13 is working, thereby reducing the problem of vibration being transmitted to the reaction tank 1 and causing loss of the reaction tank 1, thereby improving the safety of ozonated oil preparation by reducing vibration.

[0042] The above shows and describes the basic principles, main features and advantages of the present invention. It should be understood by those skilled in the art that the present invention is not limited to the above embodiments. The above embodiments and descriptions are only for explaining the principles of the present invention. Without departing from the spirit and scope of the present invention, the present invention may have various changes and improvements, which fall within the scope of the present invention. The scope of protection of the present invention is defined by the attached claims and their equivalents.

Claims

1. An ozonated oil production reactor, comprising a reaction tank (1); an oil inlet (18) is provided in the middle of the reaction tank (1); a discharge port (19) is provided at the bottom of the reaction tank (1); the characteristics are: A gas conveyor (12) is fixedly connected to the bottom of the reaction tank (1); a driving motor (13) is fixedly connected to the top of the reaction tank (1); a rotating rod (14) is fixedly connected to the output end of the driving motor (13), and the rotating rod (14) extends into the interior of the reaction tank (1); an end of the rotating rod (14) is rotatably connected to the gas conveyor (12); an air cavity (15) is provided inside the rotating rod (14); the air cavity (15) and the gas conveyor (12) are interconnected; a plurality of groups of stirring rods (16) are installed in the middle of the rotating rod (14); the air cavity (15) and the stirring rod (16) are interconnected; and an air hole (17) is provided in the middle of the stirring rod (16).

2. The ozonated oil production reactor according to claim 1, characterized in that: The air hole (17) comprises an air supply pipe (23), a first connecting pipe sleeve (24) and a second connecting pipe sleeve (25); the end of the air supply pipe (23) is fixedly connected to the rotating rod (14), and the air supply pipe (23) and the air cavity (15) are communicated with each other; the first connecting pipe sleeve (24) and the second connecting pipe sleeve (25) are both fixedly connected to the middle of the air supply pipe (23); the first connecting pipe sleeve (24) is located on the air supply pipe (23) near the rotating rod (14); the ends of the first connecting pipe sleeve (24) and the second connecting pipe sleeve (25) are hingedly arranged with each other; the air hole (17) is opened on the second connecting pipe sleeve (25) and the air supply pipe (23); the reaction tank (1) A guide rail (2) is fixedly connected inside; a baffle (21) is rotatably connected in the middle of the guide rail (2); the rotating rod (14) passes through the baffle (21) and is fixedly connected to the baffle (21); the baffle (21) is arranged above the air supply pipe (23); a plurality of electric push cylinders (22) are fixedly connected to the top side wall of the baffle (21); the output end of the electric push cylinder (22) passes through the baffle (21) and is slidably connected to the baffle (21); a first sleeve (26) is slidably connected in the middle of the first connecting pipe sleeve (24); the output end of the electric push cylinder (22) and the first sleeve (26) are hingedly connected; the air supply pipe (23) is arranged as a hose.

3. An ozonated oil production reactor according to claim 2, characterized in that: A second ring (3) is fixedly connected to the middle of the second connecting sleeve (25); a connecting rope (31) is fixedly connected to the middle of the second ring (3); and one end of the connecting rope (31) away from the second ring (3) is fixedly connected to the middle of the rotating rod (14).

4. An ozonated oil production reactor according to claim 3, characterized in that: The bottom of the reaction tank (1) is fixedly connected to a water inlet pipe (4); the top of the water inlet pipe (4) is fixedly connected to a cooling pipe (41); the middle of the cooling pipe (41) is fixedly connected to a water outlet pipe (42); the water outlet pipe (42) and the reaction tank (1) are fixedly connected; and the water inlet pipe (4), the cooling pipe (41) and the water outlet pipe (42) are all interconnected.

5. An ozonated oil production reactor according to claim 4, characterized in that: The inner side wall of the guide rail (2) is provided with a pair of slide grooves (5); the side wall of the baffle (21) is symmetrically arranged and rotatably connected to a plurality of groups of balls (51); the balls (51) are located inside the slide grooves (5) and are arranged to roll with the slide grooves (5).

6. The ozonated oil production reactor according to claim 5, characterized in that: The top of the reaction tank (1) is provided with heat dissipation holes (6); a plurality of heat dissipation holes (6) are provided and arranged in a circular array around the drive motor (13).

7. An ozonated oil production reactor according to claim 6, characterized in that: A plurality of groups of fan blades (7) are fixedly connected to the middle portion of the rotating rod (14); the fan blades (7) are arranged above the baffle plate (21).

8. An ozonated oil production reactor according to claim 7, characterized in that: The top of the inner wall of the reaction tank (1) is fixedly connected with a plurality of groups of guide plates (8); the guide plates (8) are arranged at an angle; and the guide plates (8) are arranged close to the heat dissipation holes (6).

9. An ozonated oil production reactor according to claim 8, characterized in that: A dustproof net (9) is fixedly connected to the side wall of the heat dissipation hole (6).

10. An ozonated oil production reactor according to claim 9, characterized in that: A shock-absorbing pad (10) is fixedly connected to the driving motor (13); the shock-absorbing pad (10) is arranged between the driving motor (13) and the reaction tank (1).

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