A continuous production device for oil and fat hydrolysis reaction

Abstract

The utility model belongs to the technical field of oil hydrolysis, specifically discloses a kind of oil hydrolysis reaction continuous production device, including water bath cabinet and cross plate, the left and right between the upper inside of water bath cabinet is fixed with cross plate, and the inside of cross plate is provided with three groups of through slot, the both sides of water bath cabinet top are respectively fixed with supporting plate, and the side of supporting plate is fixed with vertical plate, the inside of vertical plate is longitudinally provided with vertical slot.The oil hydrolysis reaction continuous production device is longitudinally inserted and fixed with beaker in the slot, the beaker is fixedly installed in the slot, after injecting raw materials and reaction liquid into beaker by passing through left pipe orifice by injection pipe, open the cylinder one installed in vertical plate, along vertical slot moves up and down sliding plate and immerse beaker in water surface below water bath cabinet by passing through through slot, after opening electric heater, it can be rapidly heated, and the reaction of sample in beaker is catalyzed by water separation, after ending, raise and drain moisture, the problem of lacking lifting capacity is solved.

Description

Technical Field

[0001] This utility model relates to the field of oil and fat hydrolysis technology, specifically to a continuous production device for oil and fat hydrolysis reaction. Background Technology

[0002] Oil hydrolysis specifically refers to the process in which oils react with water using acid or alkali as a catalyst to produce glycerol or fatty acids. It requires weighing out a certain amount of raw materials and acid or alkali, then adding them in batches to a beaker and stirring them, in preparation for the subsequent reaction in a water bath.

[0003] To accelerate the reaction and improve production efficiency, large-scale equipment is often used to assist in the hydrolysis of oils. Although such equipment can quickly heat the liquid and catalyze the reaction, it lacks an auxiliary lifting mechanism. The outside of the beaker is still covered with liquid, and it still takes a certain amount of time to cool down. If it is operated manually by workers, it is not only dangerous, but also cannot guarantee that the internal materials will not splash out.

[0004] Now, a novel continuous production device for oil hydrolysis reaction is proposed to solve the above problems. Utility Model Content

[0005] The purpose of this invention is to provide a continuous production device for oil hydrolysis reaction to solve the problem of lack of lifting capacity mentioned in the background art.

[0006] To achieve the above objectives, this utility model provides the following technical solution: a continuous production device for oil hydrolysis reaction, comprising a water bath and a horizontal plate. The horizontal plate is fixed between the left and right sides of the upper part of the water bath, and the interior of the horizontal plate is provided with three sets of through grooves. Support plates are fixed on both sides of the top of the water bath, and vertical plates are fixed on the sides of the support plates. Vertical grooves are provided in the interior of the vertical plates, and cylinder 1 is fixed at the top of the vertical grooves. A sliding plate is fixed between the bottom of the piston rods of cylinder 1 on both sides, and the interior of the sliding plate is provided with three sets of slots. Beakers are inserted and fixed in the slots in a longitudinal direction, and a left pipe opening is provided at the front left of the top of the beaker, and a right pipe opening is provided at the rear right of the top of the beaker. A center plate is fixed above the vertical plates on both sides, and an electric heater is installed at the bottom of the interior of the water bath.

[0007] As a further technical solution of this utility model, the beaker is embedded between the slot and the through groove, and the slot, the through groove and the beaker are arranged in concentric circles.

[0008] As a further technical solution of this utility model, the cylinder is used to vertically lift the sliding plate along the vertical groove, and the beaker is used to vertically enter and exit the through groove.

[0009] As a further technical solution of this utility model, a liquid tank is fixed to the upper right corner of the outside of the water bath, and a lower liquid pump is fixed to the top of the liquid tank. A suction tube is fixed to the top of the lower liquid pump, and a three-way pipe is fixed to the lower left corner of the suction tube. The three-way pipe is fixedly embedded in the center plate.

[0010] As a further technical solution of this utility model, the lower liquid pump is connected between the liquid tank and the suction tube, and the bottom of the suction tube is connected to the three-way pipe.

[0011] As a further technical solution of this utility model, the center plate is provided with three sets of insertion holes. A cylinder two is fixed on the left side of the center plate, and a reinforcing rod is fixed on the top of the piston rod of the cylinder two. A liquid pump is fixed on the right side of the reinforcing rod, and a feeding pipe is fixed in the liquid pump. An injection pipe is fixed at the bottom of the feeding pipe.

[0012] As a further technical solution of this utility model, the piston rod top guide and reinforcing rod of the second cylinder is raised and lowered vertically, and the bottom of the feeding pipe is connected to the injection pipe.

[0013] As a further technical solution of this utility model, the three vertical tubes of the injection tube are all embedded in the insertion hole, and the injection tube enters and exits the insertion hole vertically.

[0014] Compared with the prior art, the beneficial effects of this utility model are: the continuous production device for oil hydrolysis reaction not only realizes the rapid lifting or settling of the beaker and the automatic suction of the reaction liquid, but also makes it easy to add liquid;

[0015] (1) A beaker is fixed in the slot by inserting it vertically. The beaker is fixed in the slot beforehand. After injecting the raw material and reaction liquid into the beaker through the injection tube through the left tube opening, the cylinder installed in the vertical plate is turned on. The slide plate is moved up and down along the vertical groove and the beaker is submerged in the water bath after passing through the groove. After turning on the electric heater, the temperature can be raised quickly and the reaction between the sample in the beaker and the acid or alkali solution is catalyzed in the water. After the reaction is completed, the beaker is raised again and the water is drained.

[0016] (2) By fixing a three-way tube in the lower left corner of the pipette, after the beaker rises to a certain height, the three tubes at the bottom of the three-way tube pass through the right pipe opening and enter the bottom of the beaker. Start the liquid pump and suck the hydrolyzed liquid into the liquid tank through the pipette and the three-way tube. There is no need to manually remove the beaker. The material can be automatically discharged after the hydrolysis reaction is completed. When the hydrolysis reaction is carried out, the three-way tube is separated from the beaker and will not cause mixed contamination.

[0017] (3) By fixing the injection pipe at the bottom of the feeding pipe, starting the cylinder two and vertically raising and lowering the reinforcing rod through the piston rod, the liquid pump and feeding pipe installed on the right side of the reinforcing rod can be guided to vertically raise and lower the three pipes of the injection pipe along the vertical groove inside the center plate. After the beaker rises and absorbs the internal hydrolysis reaction liquid, the injection pipe is then passed through the left pipe opening and pressed into the beaker to replenish the raw materials and catalyst, so as to achieve the purpose of automatic feeding and continuous catalytic reaction. Attached Figure Description

[0018] Figure 1 This is a frontal cross-sectional view of the present invention.

[0019] Figure 2 This is a front view cross-sectional structural diagram of the vertical plate of this utility model;

[0020] Figure 3 This is a front view structural diagram of the present utility model;

[0021] Figure 4 This is a front view schematic diagram of the injection tube of this utility model.

[0022] In the diagram: 1. Water bath; 2. Beaker; 3. Horizontal plate; 4. Vertical plate; 5. Support plate; 6. Cylinder 1; 7. Center plate; 8. Cylinder 2; 9. Reinforcing rod; 10. Feeding pipe; 11. Upper liquid pump; 12. Injection pipe; 13. Suction pipe; 14. T-connector; 15. Lower liquid pump; 16. Liquid tank; 17. Electric heater; 18. Slide plate; 19. Slot; 20. Through slot; 21. Left pipe opening; 22. Right pipe opening; 23. Vertical slot; 24. Insertion hole. Detailed Implementation

[0023] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.

[0024] Please see Figure 1-4An embodiment of this utility model provides a continuous production device for oil hydrolysis reaction, including a water bath 1 and a horizontal plate 3. The horizontal plate 3 is fixed between the left and right sides of the upper part of the water bath 1, and the horizontal plate 3 is provided with three sets of through grooves 20. Support plates 5 are fixed on both sides of the top of the water bath 1, and vertical plates 4 are fixed on the sides of the support plates 5. Vertical grooves 23 are provided in the vertical plate 4, and cylinder 6 is fixed at the top of the vertical groove 23. A sliding plate 18 is fixed between the bottom of the piston rods of cylinder 6 on both sides, and three sets of slots 19 are provided in the sliding plate 18. A beaker 2 is inserted and fixed in the slots 19 in the longitudinal direction. A left pipe opening 21 is provided at the front left of the top of the beaker 2, and a right pipe opening 22 is provided at the rear right of the top of the beaker 2. A center plate 7 is fixed above the vertical plates 4 on both sides. An electric heater 17 is installed at the bottom of the water bath 1.

[0025] Beaker 2 is embedded between slot 19 and through slot 20. Slot 19, through slot 20 and beaker 2 are arranged in concentric circles. Cylinder 6 vertically raises and lowers slide plate 18 along vertical slot 23, and beaker 2 vertically enters and exits through slot 20.

[0026] Specifically, such as Figure 1 and Figure 2 As shown, beaker 2 is pre-fixed in slot 19. After injecting raw materials and reaction liquid into beaker 2 through injection tube 12 and left port 21, cylinder 6 installed in vertical plate 4 is turned on. Slide plate 18 is moved up and down along vertical groove 23 and beaker 2 is submerged in water bath 1 through through groove 20. After turning on electric heater 17, the temperature can be raised quickly and the reaction between sample in beaker 2 and acid or alkali solution is catalyzed in water.

[0027] A liquid tank 16 is fixed to the upper right corner of the exterior of the water bath 1, and a lower liquid pump 15 is fixed to the top of the liquid tank 16. A suction tube 13 is fixed to the top of the lower liquid pump 15, and a three-way pipe 14 is fixed to the lower left corner of the suction tube 13. The three-way pipe 14 is fixedly embedded in the center plate 7. The lower liquid pump 15 is connected between the liquid tank 16 and the suction tube 13. The bottom of the suction tube 13 is connected to the three-way pipe 14.

[0028] Specifically, such as Figure 1 and Figure 3 As shown, after the beaker 2 rises to a certain height, the three tubes at the bottom of the three-way tube 14 all pass through the right tube opening 22 and enter the bottom of the beaker 2. The liquid pump 15 is started and the hydrolyzed liquid is drawn into the liquid tank 16 through the suction tube 13 and the three-way tube 14. There is no need to manually remove the beaker 2. The liquid can be discharged automatically after the hydrolysis reaction is completed.

[0029] The center plate 7 has three sets of insertion holes 24 inside. The left side of the center plate 7 is fixed with cylinder 2 8, and the piston rod of cylinder 2 8 is fixed with a reinforcing rod 9. The right side of the reinforcing rod 9 is fixed with a liquid pump 11, and the liquid pump 11 is fixed with a feeding pipe 10. The bottom of the feeding pipe 10 is fixed with an injection pipe 12.

[0030] The piston rod of cylinder 2 8 is guided and reinforced by the top of the rod 9, which moves vertically. The bottom of the feeding pipe 10 is connected to the injection pipe 12. The three vertical pipes of the injection pipe 12 are all embedded in the insertion hole 24. The injection pipe 12 moves vertically in and out of the insertion hole 24.

[0031] Specifically, such as Figure 1 and Figure 4 As shown, the cylinder 8 is started and the reinforcing rod 9 is raised and lowered vertically through the piston rod. The liquid pump 11 and the feed pipe 10 installed on the right side of the reinforcing rod 9 are guided to raise and lower the three tubes of the injection pipe 12 vertically along the vertical groove 23 inside the center plate 7. After the beaker 2 rises and absorbs the hydrolysis reaction liquid inside, the injection pipe 12 is then pushed into the beaker 2 through the left pipe opening 21 to replenish the raw materials and catalyst.

[0032] Working principle: In use, beaker 2 is pre-fixed in slot 19. After injecting raw materials and reaction solution into beaker 2 through injection tube 12 and left port 21, cylinder 6 installed in vertical plate 4 is turned on. Slide plate 18 moves up and down along vertical groove 23, immersing beaker 2 through through groove 20 below the water surface of water bath 1. After turning on electric heater 17, the temperature rises rapidly, catalyzing the reaction between the sample in beaker 2 and acid or alkali solution in water. After the reaction is completed, beaker 2 is raised again and drained. When beaker 2 rises to a certain height, the three tubes at the bottom of three-way tube 14 all pass through right port 2. 2. Insert the probe into the bottom of beaker 2, start the lower liquid pump 15 and suck the hydrolyzed liquid into the liquid tank 16 through the suction pipe 13 and the three-way pipe 14. There is no need to manually remove beaker 2. Finally, start cylinder 2 8 and vertically raise and lower the reinforcing rod 9 through the piston rod. Guide the upper liquid pump 11 and the feeding pipe 10 installed on the right side of the reinforcing rod 9. The three pipes of the injection pipe 12 can be vertically raised and lowered along the vertical groove 23 inside the center plate 7. After beaker 2 rises and absorbs the hydrolyzed reaction liquid inside, the injection pipe 12 is then pushed into beaker 2 through the left pipe opening 21 to replenish the raw materials and catalyst, so as to continuously carry out the oil hydrolysis reaction.

[0033] It will be apparent to those skilled in the art that this invention is not limited to the details of the exemplary embodiments described above, and that it can be implemented in other specific forms without departing from the spirit or essential characteristics of this invention. Therefore, the embodiments should be considered illustrative and non-limiting in all respects, and the scope of this invention is defined by the appended claims rather than the foregoing description. Thus, it is intended that all variations falling within the meaning and scope of equivalents of the claims be included within this invention. No reference numerals in the claims should be construed as limiting the scope of the claims.

Claims

1. A continuous production apparatus for oil hydrolysis reaction, comprising a water bath (1) and a horizontal plate (3), characterized in that: A horizontal plate (3) is fixed between the left and right sides of the upper part of the water bath (1), and three sets of through grooves (20) are provided inside the horizontal plate (3). Support plates (5) are fixed on both sides of the top of the water bath (1), and vertical plates (4) are fixed on the side of the support plates (5). Vertical grooves (23) are provided in the vertical plate (4) in the longitudinal direction. Cylinder 1 (6) is fixed at the top of the vertical groove (23). Slide plate (18) is fixed between the bottom of the piston rods of cylinder 1 (6) on both sides. Three sets of slots (19) are provided inside the slide plate (18). Beaker (2) is inserted and fixed in the slot (19) in the longitudinal direction. A left pipe opening (21) is provided at the front left of the top of the beaker (2). A right pipe opening (22) is provided at the rear right of the top of the beaker (2). A center plate (7) is fixed above the vertical plates (4) on both sides. An electric heater (17) is installed at the bottom of the water bath (1).

2. The continuous production apparatus for oil hydrolysis reaction according to claim 1, characterized in that: The beaker (2) is embedded between the slot (19) and the through slot (20), and the slot (19), the through slot (20) and the beaker (2) are arranged in concentric circles.

3. The continuous production apparatus for oil hydrolysis reaction according to claim 1, characterized in that: The cylinder (6) moves vertically up and down the slide plate (18) along the vertical groove (23), and the beaker (2) moves vertically in and out of the through groove (20).

4. The continuous production apparatus for oil hydrolysis reaction according to claim 1, characterized in that: A liquid tank (16) is fixed to the upper right corner of the outside of the water bath (1), and a lower liquid pump (15) is fixed to the top of the liquid tank (16). A suction tube (13) is fixed to the top of the lower liquid pump (15), and a three-way pipe (14) is fixed to the lower left corner of the suction tube (13). The three-way pipe (14) is fixedly embedded in the center plate (7).

5. The continuous production apparatus for oil hydrolysis reaction according to claim 4, characterized in that: The lower liquid pump (15) is connected between the liquid tank (16) and the suction pipe (13), and the bottom of the suction pipe (13) is connected to the three-way pipe (14).

6. The continuous production apparatus for oil hydrolysis reaction according to claim 1, characterized in that: The center plate (7) has three sets of insertion holes (24) inside. A cylinder two (8) is fixed on the left side inside the center plate (7), and a reinforcing rod (9) is fixed at the top of the piston rod of the cylinder two (8). A liquid pump (11) is fixed on the right side of the reinforcing rod (9), and a feeding pipe (10) is fixed in the liquid pump (11). An injection pipe (12) is fixed at the bottom of the feeding pipe (10).

7. A continuous production apparatus for oil hydrolysis reaction according to claim 6, characterized in that: The piston rod of cylinder 2 (8) is guided and reinforced by the top rod (9) which moves vertically up and down, and the bottom of the feeding pipe (10) is connected to the injection pipe (12).

8. A continuous production apparatus for oil hydrolysis reaction according to claim 6, characterized in that: The three vertical tubes of the injection tube (12) are all embedded in the insertion hole (24), and the injection tube (12) enters and exits the insertion hole (24) vertically.

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