High-efficiency purification device for nervonic acid production

Abstract

The utility model discloses a kind of efficient purification devices for nervonic acid production, including separation bucket, the bottom end of separation bucket is clamped and is equipped with firm base, the inner wall of separation bucket is equipped with several guide vanes, the bottom end of separation bucket is penetrated firm base, the bottom end of firm base is equipped with purification box, the inner wall of purification box is equipped with distillation bucket, the outside of distillation bucket is equipped with several filter channels, the bottom end of distillation bucket is equipped with low-temperature crystallization bucket;From the primary interception of large-particle impurities of primary filter screen in the top end of separation bucket, to the accurate filtration of fine impurities by transition pipe inner filter ball surface separation filter screen, again to the depth purification of porous sieve plate in distillation bucket outside filter channel, different particle size impurities in material can be removed comprehensively, effectively avoid the influence of impurity residue on nervonic acid purity, compared with single filtration mode, the purity of product is improved, meet the strict requirement of biomedical, high-end health care product etc. to nervonic acid high purity.

Description

Technical Field

[0001] This utility model relates to the technical field of purification device ejection device, and in particular to a high-efficiency purification device for nervonic acid production. Background Technology

[0002] Nervonic acid, a core natural component of brain nerve cells and tissue, has a significant effect on promoting the repair and regeneration of damaged nerve tissue, and is widely in demand in biomedical applications, health product development, and nutritional supplement production. It is typically obtained from plant oils, such as Acer truncatum oil and Xanthoceras sorbifolium oil, requiring multiple complex processes including saponification, hydrolysis, acidification, distillation, and freeze-drying to produce a high-purity product. However, existing nervonic acid production and purification processes have many problems.

[0003] Traditional purification equipment relies on a relatively simple filtration process, making it difficult to comprehensively remove impurities of varying sizes from raw materials. This limits the purity of the final nervonic acid product, hindering its application in high-end fields. For example, relying solely on a simple filter cannot effectively intercept tiny particles and some organic impurities, potentially leaving residues that affect product quality. Furthermore, inadequate equipment design during critical steps such as distillation and crystallization leads to insufficient material separation. For instance, during distillation, steam may flow back into the raw materials, affecting purification accuracy. During crystallization, a lack of effective stirring and condensation control results in slow crystallization rates and low crystal purity, significantly reducing production efficiency and increasing costs.

[0004] Therefore, we propose a high-efficiency purification device for the production of nervonic acid. Utility Model Content

[0005] The purpose of this invention is to address the shortcomings of existing technologies by proposing a highly efficient purification device for the production of nervonic acid.

[0006] To achieve the above objectives, the present invention adopts the following technical solution: A high-efficiency purification device for nervonic acid production includes a separation tank with a stable base engaged at its bottom. Several guide vanes are arranged on the inner wall of the separation tank. The stable base extends through the bottom of the separation tank, and a purification chamber is located at the bottom of the stable base. A distillation tank is arranged on the inner wall of the purification chamber, and several filtration channels are arranged on the outer side of the distillation tank. A low-temperature crystallization tank is located at the bottom of the distillation tank. The guide vanes precisely guide the material to flow along a specific trajectory within the separation tank, preventing localized material accumulation and significantly enhancing the uniformity and efficiency of centrifugal separation, allowing for more thorough separation of impurities and active ingredients from the material.

[0007] As a further improvement of this utility model: a drive motor is provided at the top of the inner wall of the purification box, and the motor shaft of the drive motor is connected to the bottom of the separation tank through a coupling, thereby driving the separation tank to rotate.

[0008] As a further improvement of this utility model: the separation bucket is a tubular shell with an open top, and a primary filter screen is provided at the top of the inner side of the separation bucket.

[0009] As a further improvement of this utility model: a transition tube is provided between the outer side of the stable base and the distillation tank, and a number of filter balls are provided on the inner wall of the transition tube, and a number of separation filter screens are opened on the surface of the filter balls.

[0010] As a further improvement of this utility model: a flow divider is provided at the top of the distillation tank, the flow divider is connected to the filtration channel, and the distillation tank is connected to the flow divider. The inner wall of the filtration channel is provided with several porous sieve plates, and the outer side is provided with multiple filtration channels. With the flow divider at the top, the distilled material can be evenly introduced into each filtration channel for further filtration. This design greatly improves the separation accuracy, ensures higher purity of the material entering the subsequent crystallization stage, and can evenly distribute the material in the distillation tank to each filtration channel, avoiding the situation where some filtration channels are overloaded or idle due to uneven material distribution. This fully utilizes the function of each filtration channel and improves the overall filtration efficiency.

[0011] As a further improvement of this utility model: the low-temperature crystallization tank has a condensation function, and the bottom end of the filter channel is connected to the low-temperature crystallization tank.

[0012] As a further improvement of this utility model: a transmission rod is provided on the inner wall of the low-temperature crystallization tank, and several scrapers are provided at the top end of the transmission rod. A stepper motor is provided at the bottom end of the low-temperature crystallization tank, and the stepper motor is connected to the transmission rod. The scrapers are in close contact with the top end of the inner wall of the low-temperature crystallization tank, which ensures thorough scraping of crystals without leaving any residue. Furthermore, the scraper material should be a soft plastic structure that is moderately soft, which can effectively scrape off the crystals without damaging the inner wall of the tank, thus ensuring the service life of the equipment and the purity of the crystals.

[0013] Compared with the prior art, this utility model provides a high-efficiency purification device for nervonic acid production, which has the following beneficial effects: This invention employs a multi-stage filtration system. From the initial interception of large particles by the primary filter at the top of the separation tank, to the precise filtration of fine impurities by the filter ball separator in the transition tube, and finally to the deep purification by the porous sieve plate in the filtration channel outside the distillation tank, this design comprehensively removes impurities of different particle sizes from the material, effectively preventing residual impurities from affecting the purity of nervonic acid. Compared to traditional single-filtration methods, this significantly improves product purity, meeting the stringent requirements for high purity nervonic acid in biomedicine and high-end health products, thus laying a solid foundation for the widespread application of nervonic acid in these fields.

[0014] This invention utilizes the centrifugal force of the separation tank to reduce the burden on subsequent distillation. The distilled material is precisely diverted into the filtration channel, and finally crystallizes efficiently in a low-temperature crystallization tank. A drive motor rotates the separation tank, and a stepper motor controls the scraper operation, achieving automated operation of key processes. The intelligent control system can precisely regulate various parameters, such as the separation tank rotation speed, distillation temperature, and crystallization time. This not only greatly improves production efficiency and reduces errors caused by manual operation but also ensures a high degree of consistency in product quality, making nervonic acid production more efficient, stable, and reliable, significantly enhancing the company's production benefits and market competitiveness.

[0015] The parts of this device not covered herein are the same as or can be implemented using existing technologies. This utility model has a simple structure and is easy to operate. Attached Figure Description

[0016] Figure 1 This is a schematic diagram of the overall structure of a high-efficiency purification device for nervonic acid production proposed in this utility model. Figure 2 This is a cross-sectional structural diagram of the separation tank of a high-efficiency purification device for nervonic acid production proposed in this utility model; Figure 3 This is a schematic cross-sectional view of the distillation tank and the low-temperature crystallization tank of a high-efficiency purification device for nervonic acid production proposed in this utility model. Figure 4 This is a schematic diagram of the distribution structure of the transition tube and filter balls in a high-efficiency purification device for nervonic acid production proposed in this utility model.

[0017] In the diagram: 1. Separation tank; 2. Stable base; 3. Guide vanes; 4. Purification chamber; 5. Distillation tank; 6. Filtration channel; 7. Low-temperature crystallization tank; 8. Drive motor; 9. Primary filter screen; 10. Transition tube; 11. Filter ball; 12. Separation filter screen; 13. Diverter plate; 14. Porous sieve plate; 15. Transmission rod; 16. Scraper; 17. Stepper motor. Detailed Implementation

[0018] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present utility model. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments.

[0019] In the description of this utility model, it should be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model.

[0020] Example: A high-efficiency purification device for nervonic acid production, such as... Figures 1-4 As shown, the system includes a separation tank 1, a stable base 2 that engages with the bottom of the separation tank 1, several guide vanes 3 on the inner wall of the separation tank 1, the bottom of the separation tank 1 passing through the stable base 2, a purification chamber 4 at the bottom of the stable base 2, a distillation tank 5 on the inner wall of the purification chamber 4, several filter channels 6 on the outer side of the distillation tank 5, a low-temperature crystallization tank 7 at the bottom of the distillation tank 5, and a drive motor 8 at the top of the inner wall of the purification chamber 4. The motor shaft of the drive motor 8 is connected to the bottom of the separation tank 1 via a coupling, and drives the separation tank 1 to rotate. From the initial interception of large particles by the primary filter 9 at the top of the separation tank 1, to the precise filtration of fine impurities by the separation filter 12 on the surface of the filter balls 11 in the transition tube 10, and then to the deep purification by the porous sieve plate 14 in the filter channel 6 on the outer side of the distillation tank 5, this design can comprehensively remove impurities of different particle sizes from the material and effectively avoid the impact of impurity residues on the purity of nervonic acid. Compared to traditional single filtration methods, this method greatly improves the purity of the product, meeting the stringent requirements for high purity of nervonic acid in biomedicine, high-end health products, and other fields, thus laying a solid foundation for the widespread application of nervonic acid in these areas.

[0021] like Figures 1-4 As shown, the separation tank 1 is a tubular shell with an open top. A primary filter screen 9 is provided at the top of the inner side of the separation tank 1. A transition tube 10 is provided between the outer side of the stable base 2 and the distillation tank 5. A number of filter balls 11 are provided on the inner wall of the transition tube 10. A number of separation filter screens 12 are opened on the surface of the filter balls 11. A flow divider plate 13 is provided at the top of the distillation tank 5. The flow divider plate 13 is connected to the filter channel 6. The distillation tank 5 is connected to the flow divider plate 13. A number of porous sieve plates 14 are provided on the inner wall of the filter channel 6.

[0022] like Figures 1-3As shown, the low-temperature crystallization tank 7 has a condensation function. The bottom end of the filter channel 6 is connected to the low-temperature crystallization tank 7. A transmission rod 15 is installed on the inner wall of the low-temperature crystallization tank 7, and several scrapers 16 are installed at the top of the transmission rod 15. A stepper motor 17 is installed at the bottom of the low-temperature crystallization tank 7 and is connected to the transmission rod 15. The scrapers 16 are attached to the top of the inner wall of the low-temperature crystallization tank 7. The centrifugal action of the separation tank 1 reduces the burden on subsequent distillation. The distilled material is precisely diverted into the filter channel 6 and finally crystallizes efficiently in the low-temperature crystallization tank 7. The drive motor 8 drives the separation tank 1 to rotate, and the stepper motor 17 controls the scrapers 16 to work, realizing the automated operation of key links. The intelligent control system can precisely control various parameters, such as the rotation speed of the separation tank 1, the distillation temperature, and the crystallization time.

[0023] Working Principle: Material enters through the top opening of separation tank 1. The primary filter 9 first performs initial filtration, intercepting large particles of impurities. Then, the drive motor 8 rotates separation tank 1 at high speed. Under the combined action of centrifugal force and guide vanes 3, the material achieves initial separation and flows from the bottom of separation tank 1 into the stable base 2. Next, the material passes through transition pipe 10, where the separation filter 12 on the surface of filter balls 11 performs secondary filtration, further removing fine impurities. The filtered material enters distillation tank 5, where nervonic acid-related components are separated during distillation. The diverter plate 13 evenly guides the material into the outer filtration channel 6, where the porous sieve plate 14 performs further fine filtration. Finally, the filtered material enters a low-temperature crystallization tank 7 with a condensation function, where nervonic acid crystallizes upon cooling. The stepper motor 17 drives the transmission rod 15 and scraper 16 to rotate. The scraper 16 scrapes off the nervonic acid crystals crystallized at the top of the inner wall of the tank, completing the purification and collection of nervonic acid.

[0024] The above description is only a preferred embodiment of the present utility model, but the protection scope of the present utility model is not limited thereto. Any equivalent substitutions or changes made by those skilled in the art within the technical scope disclosed in the present utility model, based on the technical solution and the inventive concept of the present utility model, should be included within the protection scope of the present utility model.

Claims

1. A high-efficiency purification device for nervonic acid production, comprising a separation tank (1), characterized in that: The bottom of the separation tank (1) is fitted with a stable base (2). The inner wall of the separation tank (1) is provided with several guide vanes (3). The bottom of the separation tank (1) passes through the stable base (2). The bottom of the stable base (2) is provided with a purification box (4). The inner wall of the purification box (4) is provided with a distillation tank (5). The outer side of the distillation tank (5) is provided with several filter channels (6). The bottom of the distillation tank (5) is provided with a low-temperature crystallization tank (7).

2. The high-efficiency purification device for nervonic acid production according to claim 1, characterized in that: The purification chamber (4) is equipped with a drive motor (8) at the top of its inner wall. The motor shaft of the drive motor (8) is connected to the bottom of the separation tank (1) via a coupling, and drives the separation tank (1) to rotate.

3. The high-efficiency purification device for nervonic acid production according to claim 1, characterized in that: The separation tank (1) is a tubular shell with an open top, and a primary filter screen (9) is provided on the top inner side of the separation tank (1).

4. The high-efficiency purification device for nervonic acid production according to claim 3, characterized in that: A transition tube (10) is provided between the outer side of the stable base (2) and the distillation tank (5). A number of filter balls (11) are provided on the inner wall of the transition tube (10), and a number of separation filter screens (12) are opened on the surface of the filter balls (11).

5. The high-efficiency purification apparatus for nervonic acid production according to claim 4, characterized in that: The distillation tank (5) is provided with a flow divider plate (13) at the top. The flow divider plate (13) is connected to the filter channel (6). The distillation tank (5) is connected to the flow divider plate (13). The inner wall of the filter channel (6) is provided with a number of porous sieve plates (14).

6. The high-efficiency purification apparatus for nervonic acid production according to claim 5, characterized in that: The low-temperature crystallization tank (7) has a condensation function, and the bottom end of the filter channel (6) is connected to the low-temperature crystallization tank (7).

7. The high-efficiency purification apparatus for nervonic acid production according to claim 6, characterized in that: The low-temperature crystallization tank (7) is provided with a transmission rod (15) on its inner wall. The top of the transmission rod (15) is provided with several scrapers (16). The bottom of the low-temperature crystallization tank (7) is provided with a stepper motor (17). The stepper motor (17) is connected to the transmission rod (15). The scrapers (16) are attached to the top of the inner wall of the low-temperature crystallization tank (7).

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