A natural plant active ingredient extraction device based on supercritical fluid extraction

By setting up exhaust pipes, solenoid valves, gas pipes, moisture absorption chambers and recovery pipes in the supercritical fluid extraction device, the gas-like supercritical fluid is dried and recovered by molecular sieve, solving the problems of resource waste and environmental pollution in the existing devices, and achieving efficient resource recycling and environmentally friendly extraction processes.

CN222694039UActive Publication Date: 2025-04-01YUNNAN MILI BIOTECHNOLOGY CO LTD
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Patent Information

Application Number
CN202421267865.X
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-06-05
Publication Date
2025-04-01
Estimated Expiration
2034-06-05

AI Technical Summary

Technical Problem

The existing supercritical fluid extraction devices lack the function of drying and recycling supercritical fluids in the form of recovery gases, resulting in environmental pollution and waste of resources.

Method used

A device including an exhaust pipe, a solenoid valve, a gas pipe, a moisture absorbing box and a recovery tube is designed. After absorbing and drying in the moisture absorbing box using a molecular sieve, the dried supercritical fluid is stored through the recovery tube.

Benefits of technology

The drying recovery of supercritical fluids is achieved, reducing environmental pollution and resource waste, while improving the efficiency and sustainability of the extraction device.

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Abstract

The utility model relates to the technical field of extraction and extraction devices, specifically, to a natural plant effective component extraction device based on supercritical fluid extraction, comprising a supercritical fluid extraction cylinder, a top cover fixedly installed on the top of the supercritical fluid extraction cylinder, an exhaust pipe fixedly installed at the center of the top cover, an electromagnetic valve fixedly installed on the exhaust pipe, a gas pipe fixedly installed on the top of the exhaust pipe, a moisture absorption box fixedly installed at the end of the gas pipe, a recovery pipe fixedly installed on one side plate of the moisture absorption box, the recovery pipe and the gas pipe are located on the opposite side, a blocking net is fixedly installed on the inner wall of the end tube body of the recovery pipe and the gas pipe close to the moisture absorption box, a molecular sieve is arranged in the moisture absorption box, a raw material tube is fixedly installed on the top cylinder of the supercritical fluid extraction cylinder, and a pressurizing tube is also fixedly installed on the top cylinder of the supercritical fluid extraction cylinder. The utility model is convenient for extraction and supercritical fluid recovery operations and is convenient to use.
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Description

Technical Field

[0001] The utility model relates to the technical field of extraction devices, in particular to a natural plant effective component extraction device based on supercritical fluid extraction. Background Art

[0002] Supercritical fluid extraction is a new type of extraction and separation technology. It uses supercritical fluid, that is, a fluid in a thermodynamic state with a temperature higher than the critical temperature and a pressure higher than the critical pressure, as an extractant to extract specific components from liquids or solids to achieve the purpose of separation. With the rapid development of modern science and technology, the application of natural plant active ingredients in medicine, cosmetics, food and other fields is becoming more and more extensive. Traditional extraction methods such as solvent extraction, steam distillation, and pressing have problems such as low extraction efficiency, complex operation, and environmental pollution. In order to achieve efficient extraction effects, supercritical fluid extraction technology is usually used to replace traditional extraction technology.

[0003] When performing supercritical fluid extraction, it is usually carried out in the corresponding extraction device. Since supercritical fluid extraction requires the addition of supercritical fluid, and most supercritical fluids are liquid gases, the gas will return to gaseous state and be discharged to the outside as the pressure decreases. Most supercritical fluid extraction devices lack the defect of being able to dry and recycle the supercritical fluid that has returned to gaseous state. If this part of the gas is directly discharged to the outdoors, it will pollute the environment. At the same time, it will also cause waste. It needs to be re-prepared the next time it is used, wasting resources. In view of this, we propose a natural plant active ingredient extraction device based on supercritical fluid extraction. Utility Model Content

[0004] The purpose of the utility model is to provide a natural plant active ingredient extraction device based on supercritical fluid extraction to solve the defects mentioned in the above background technology.

[0005] In order to achieve the above purpose, the utility model provides the following technical solutions:

[0006] A natural plant effective component extraction device based on supercritical fluid extraction comprises a supercritical fluid extraction cylinder, a top cover is fixedly installed on the top of the supercritical fluid extraction cylinder, an exhaust pipe is fixedly installed at the center of the top cover, an electromagnetic valve is fixedly installed on the exhaust pipe, a gas pipe is fixedly installed on the top of the exhaust pipe, a moisture absorption box is fixedly installed on the end of the gas pipe, a recovery pipe is fixedly installed on a side plate of the moisture absorption box, the recovery pipe and the gas pipe are located on the opposite side, blocking nets are fixedly installed on the inner wall of the recovery pipe and the end of the gas pipe close to the moisture absorption box, a molecular sieve is arranged in the moisture absorption box, and the molecular sieve is used for moisture absorption operation.

[0007] Preferably, a raw material tube is fixedly mounted on the top cylinder of the supercritical fluid extraction cylinder, and a pressurizing tube is also fixedly mounted on the top cylinder of the supercritical fluid extraction cylinder, so that raw material adding operation can be performed using the raw material tube and pressurizing operation can be performed using the pressurizing tube.

[0008] Preferably, a supercritical fluid generator is provided on one side of the supercritical fluid extraction cartridge, and the supercritical fluid generator is connected to the supercritical fluid extraction cartridge via a delivery pipe, so that the supercritical fluid generator is used to generate supercritical fluid and deliver it to the supercritical fluid extraction cartridge for extraction operation.

[0009] Preferably, a discharge pipe is fixedly mounted on the bottom end of the supercritical fluid extraction cylinder, and a discharge valve is fixedly mounted on the discharge pipe, so that the discharge valve can be opened to perform a discharge operation.

[0010] Preferably, an electric heater is fixedly mounted on the body of the supercritical fluid extraction cartridge, and the electric heater is used for heating operation.

[0011] Preferably, an entrainer pump is provided on one side of the supercritical fluid extraction cartridge, a suction tube is fixedly installed at the liquid inlet end of the entrainer pump, a liquid tube is fixedly installed at the liquid outlet end of the entrainer pump, and the end of the liquid tube is fixedly installed on the supercritical fluid extraction cartridge, so as to facilitate the use of the entrainer pump to transport the entrainer and improve the solubility of the supercritical fluid.

[0012] Preferably, a conical cylinder is fixedly installed at the bottom end of the desiccant box, a drop pipe is fixedly installed at the bottom end of the conical cylinder, a first valve is fixedly installed on the drop pipe, an addition pipe is fixedly installed on the top surface of the desiccant box, and a second valve is fixedly installed on the addition pipe to facilitate the replacement operation of the molecular sieve.

[0013] Preferably, a dust cover is threadedly connected to the top tube body of the adding tube, and the dust cover is used for dust protection operation.

[0014] Compared with the prior art, the beneficial effects of the utility model are:

[0015] 1. The utility model ensures that after the extraction is completed, as the pressure decreases, the liquid supercritical fluid returns to a gaseous state through the exhaust pipe, so that it can enter the moisture absorption box through the exhaust pipe, absorb moisture through the molecular sieve in the moisture absorption box, and then be discharged outward along the recovery pipe to the corresponding storage device for storage operation, thereby achieving the effect of drying and recovering the supercritical fluid.

[0016] 2. The utility model can generate supercritical fluid through the supercritical fluid generator and transport it to the supercritical fluid extraction cylinder for extraction operation. In addition, the entrainer pump can transport the entrainer to improve the dissolving ability of the supercritical fluid. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] Figure 1 It is a schematic diagram of the overall structure of the utility model;

[0018] Figure 2 It is a schematic diagram of the explosion structure of the utility model;

[0019] Figure 3 This is one of the cross-sectional views of the moisture absorption box of the utility model;

[0020] Figure 4 This is the second cross-sectional view of the moisture absorption box of the utility model.

[0021] The meaning of each number in the figure is:

[0022] 1. Supercritical fluid extraction cartridge; 10. Top cover; 11. Exhaust pipe; 111. Solenoid valve; 12. Raw material pipe; 13. Pressurizing pipe; 14. Supercritical fluid generator; 141. Delivery pipe; 15. Discharge pipe; 151. Discharge valve; 16. Electric heater; 17. Entrainment agent pump; 171. Suction pipe; 172. Liquid pipe;

[0023] 2. Gas pipe; 20. Desiccant box; 21. Recovery pipe; 22. Barrier net; 23. Molecular sieve; 24. Conical cylinder; 25. Dropping pipe; 251. First valve; 26. Adding pipe; 261. Second valve; 27. Dust cover. DETAILED DESCRIPTION

[0024] The following will be combined with the drawings in the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.

[0025] See also Figure 1-Figure 4The utility model provides a technical solution: a natural plant active ingredient extraction device based on supercritical fluid extraction, comprising a supercritical fluid extraction cylinder 1, a top cover 10 is fixedly installed on the top of the supercritical fluid extraction cylinder 1, an exhaust pipe 11 is fixedly installed at the center of the top cover 10, an electromagnetic valve 111 is fixedly installed on the exhaust pipe 11, a gas pipe 2 is fixedly installed on the top of the exhaust pipe 11, a moisture absorption box 20 is fixedly installed at the end of the gas pipe 2, a recovery pipe 21 is fixedly installed on one side plate of the moisture absorption box 20, the recovery pipe 21 and the gas pipe 2 are located on the opposite side, a blocking net 22 is fixedly installed on the inner wall of the recovery pipe 21 and the end of the gas pipe 2 close to the moisture absorption box 20, a molecular sieve 23 is arranged in the moisture absorption box 20, and the molecular sieve 23 is used for moisture absorption operation to achieve the effect of drying and recycling the supercritical fluid restored to gas state.

[0026] In this embodiment, a raw material tube 12 is fixedly installed on the top cylinder of the supercritical fluid extraction cylinder 1, and a pressurizing tube 13 is also fixedly installed on the top cylinder of the supercritical fluid extraction cylinder 1, so that the raw material tube 12 can be used for raw material adding operation, and the pressurizing tube 13 can be used for pressurizing operation.

[0027] Specifically, a supercritical fluid generator 14 is provided on one side of the supercritical fluid extraction cartridge 1, and the supercritical fluid generator 14 is connected to the supercritical fluid extraction cartridge 1 through a delivery pipe 141, so that the supercritical fluid generator 14 is used to generate supercritical fluid and deliver it to the supercritical fluid extraction cartridge 1 for extraction operation.

[0028] Furthermore, a discharge pipe 15 is fixedly installed at the bottom end of the supercritical fluid extraction cylinder 1 , and a discharge valve 151 is fixedly installed on the discharge pipe 15 , so that the discharge valve 151 can be opened to perform a discharge operation.

[0029] In addition, an electric heater 16 is fixedly mounted on the body of the supercritical fluid extraction cartridge 1 , and the electric heater 16 is used for heating operation.

[0030] It is worth noting that an entrainer pump 17 is provided on one side of the supercritical fluid extraction cartridge 1, a suction tube 171 is fixedly installed at the liquid inlet end of the entrainer pump 17, a liquid tube 172 is fixedly installed at the liquid outlet end of the entrainer pump 17, and the end of the liquid tube 172 is fixedly installed on the supercritical fluid extraction cartridge 1, so as to facilitate the use of the entrainer pump 17 to transport the entrainer and improve the solubility of the supercritical fluid.

[0031] It is worth noting that a conical cylinder 24 is fixedly installed at the bottom end of the desiccant box 20, a drop pipe 25 is fixedly installed at the bottom end of the conical cylinder 24, a first valve 251 is fixedly installed on the drop pipe 25, an addition tube 26 is fixedly installed on the top surface of the desiccant box 20, a second valve 261 is fixedly installed on the addition tube 26, so as to facilitate the replacement operation of the molecular sieve 23; a dust cover 27 is threadedly connected to the top tube body of the addition tube 26, and the dust cover 27 is used for dust protection operation.

[0032] When the natural plant active ingredient extraction device based on supercritical fluid extraction of the utility model is used, the discharge valve 151 is closed, the raw material pipe 12 is connected to the external raw material delivery pipeline, the pressure pipe 13 is connected to the external pressure device, the solenoid valve 111 is closed, the raw material pipe 12 is used to deliver the raw material to the supercritical fluid extraction cylinder 1, and then the supercritical fluid generator 14 is used to generate the supercritical fluid and deliver it to the supercritical fluid extraction cylinder 1 for extraction operation. In addition, the suction pipe 171 is connected to the external entrainer delivery pipeline, the entrainer pump 17 is connected to the external power supply and made to work, and the entrainer pump 17 is operated to realize the delivery of the entrainer to the supercritical fluid extraction cylinder 1 to improve the solubility of the supercritical fluid. After the extraction is completed, the solenoid valve 111 is opened. At this time, the supercritical fluid restored to the gaseous state can enter the moisture absorption box 20 along the exhaust pipe 11, and after being dried by the molecular sieve 23, it is delivered to the external storage device from the end of the recovery pipe 21 to complete the recovery operation of the supercritical fluid.

[0033] The above shows and describes the basic principle, main features and advantages of the utility model. Those skilled in the art should understand that the utility model is not limited by the above embodiments. The above embodiments and descriptions are only preferred examples of the utility model and are not used to limit the utility model. Without departing from the spirit and scope of the utility model, the utility model may have various changes and improvements, which fall within the scope of the utility model to be protected. The scope of protection of the utility model is defined by the attached claims and their equivalents.

Claims

1. A natural plant active ingredient extraction device based on supercritical fluid extraction, comprising a supercritical fluid extraction cartridge (1), characterized in that: A top cover (10) is fixedly mounted on the top of the supercritical fluid extraction cartridge (1), an exhaust pipe (11) is fixedly mounted at the center of the top cover (10), a solenoid valve (111) is fixedly mounted on the exhaust pipe (11), a gas pipe (2) is fixedly mounted on the top of the exhaust pipe (11), a moisture absorption box (20) is fixedly mounted on the end of the gas pipe (2), a recovery pipe (21) is fixedly mounted on a plate body on one side of the moisture absorption box (20), the recovery pipe (21) and the gas pipe (2) are located on the opposite side, a blocking net (22) is fixedly mounted on the inner wall of the end tube body of the recovery pipe (21) and the gas pipe (2) close to the moisture absorption box (20), a molecular sieve (23) is arranged in the moisture absorption box (20), and the molecular sieve (23) is used for moisture absorption operation.

2. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 1, characterized in that: A raw material tube (12) is fixedly mounted on the top cylinder of the supercritical fluid extraction cylinder (1), and a pressure tube (13) is also fixedly mounted on the top cylinder of the supercritical fluid extraction cylinder (1).

3. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 1, characterized in that: A supercritical fluid generator (14) is provided on one side of the supercritical fluid extraction cartridge (1), and the supercritical fluid generator (14) is connected to the supercritical fluid extraction cartridge (1) via a delivery pipe (141).

4. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 1, characterized in that: A discharge pipe (15) is fixedly mounted on the bottom end of the supercritical fluid extraction cylinder (1), and a discharge valve (151) is fixedly mounted on the discharge pipe (15).

5. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 1, characterized in that: An electric heater (16) is fixedly mounted on the body of the supercritical fluid extraction cartridge (1), and the electric heater (16) is used for heating operation.

6. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 1, characterized in that: An entrainer pump (17) is provided on one side of the supercritical fluid extraction cartridge (1), a suction pipe (171) is fixedly mounted on the liquid inlet end of the entrainer pump (17), a liquid pipe (172) is fixedly mounted on the liquid outlet end of the entrainer pump (17), and the end of the liquid pipe (172) is fixedly mounted on the supercritical fluid extraction cartridge (1).

7. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 1, characterized in that: A conical cylinder (24) is fixedly mounted on the bottom end of the desiccant box (20), a drop pipe (25) is fixedly mounted on the bottom end of the conical cylinder (24), a first valve (251) is fixedly mounted on the drop pipe (25), and an addition pipe (26) is fixedly mounted on the top surface of the desiccant box (20), a second valve (261) is fixedly mounted on the addition pipe (26).

8. The natural plant active ingredient extraction device based on supercritical fluid extraction according to claim 7, characterized in that: A dust cover (27) is threadedly connected to the top tube body of the addition tube (26), and the dust cover (27) is used for dust protection operation.