A device for extracting nervonic acid from malania acephala

CN224793031UActive Publication Date: 2026-09-25NAOYIKANG (HEBEI PROVINCE) BIOTECHNOLOGY CO LTD
View PDF 1 Cites 0 Cited by

Patent Information

Application Number
CN202522325413.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-11-03
Publication Date
2026-09-25
Estimated Expiration
2035-11-03

AI Technical Summary

Technical Problem

[0002]从蒜头果中提取神经酸,需要一套系统的生产设备,其中对其纯化提纯的现有技术,例如申请号为CN202321026613.3,该现有技术中通过挤压的方式对其进行提纯,该挤压方式较为落后,该方式不能够通过重复挤压来提高纯度,提高纯度的能力有限;需要设计一种新型的提纯方式

Benefits of technology

[0011]本实用新型的有益效果是:采用低温结晶的方式,利用不同物质在特定溶剂中的溶解度随温度降低而下降的速率不同的物理原理;神经酸(顺-15-二十四碳烯酸)和它的主要杂质(如芥酸,顺-13-二十二碳烯酸)在分子结构上非常相似,仅碳链长度和双键位置略有不同;这种微小的差异导致它们在特定有机溶剂(如丙酮、乙醇、正己烷、正戊醇等)中,低温下的溶解度行为不同,在降温时神经酸会优先析出;

✦ Generated by Eureka AI based on patent content.

Smart Images

  • Figure CN224793031U_ABST
    Figure CN224793031U_ABST
Patent Text Reader

Abstract

The utility model discloses a kind of garcinia indica extraction nervonic acid purification devices, including stirring shaft and stirring fin, stirring shaft and stirring fin are communicated with refrigeration system, refrigeration medium moves from stirring shaft upper end to lower end, pass through the stirring fin in the way, crystallizing kettle is communicated with filter jar;Crystal filter plate, the crystal and impurity mixed together are separated, crystal filter plate is located in filter jar;Circulating pump, after separation, crystal is transported to crystallizing kettle and is mixed with new solution repeatedly crystallization, repeatedly above-mentioned process can extract high-purity crystal.The utility model has the beneficial effect that, the crystal obtained first time is dissolved with fresh solvent, then the above-mentioned cooling crystallization process is carried out again.Each time of repetition, the purity of product is promoted once;Through the effect of scraper, crystal can be avoided to adhere on crystal filter plate, effectively avoid that crystal filter plate is blocked.
Need to check novelty before this filing date? Find Prior Art

Description

Technical Field

[0001] This utility model relates to the field of nervonic acid purification technology, and more specifically, to a device for purifying nervonic acid extracted from garlic fruit. Background Technology

[0002] Extracting nervonic acid from garlic fruit requires a systematic production equipment. Existing purification techniques, such as those in application number CN202321026613.3, involve purification through extrusion. This extrusion method is outdated and cannot improve purity through repeated extrusion, thus limiting its ability to increase purity. A novel purification method needs to be designed. Utility Model Content

[0003] To address the above deficiencies, this invention provides a device for purifying nervonic acid extracted from garlic fruit, thus solving the aforementioned problems.

[0004] To achieve the above objectives, the present invention adopts the following technical solution: A purification apparatus for extracting nervonic acid from garlic fruit includes a new solution, crystals, impurities, a crystallization vessel, a filter tank, a refrigeration system, and a recovery tank; and also includes: The stirring shaft and stirring blades are connected to the refrigeration system, which includes a refrigeration medium. The refrigeration medium moves from the upper end to the lower end of the stirring shaft, passing through the stirring blades along the way. The crystallization vessel is connected to the filter tank. Crystallization filter plates separate the mixed crystals and impurities. The crystallization filter plates are placed inside the filter tank. A circulating pump transports the separated crystals to a crystallization vessel for repeated crystallization. Repeating this process allows for the extraction of high-purity crystals.

[0005] Furthermore, sealed bearings are installed at both the upper and lower ends of the crystallization vessel, and the stirring shaft is installed inside the sealed bearings. The stirring shaft has openings at both ends and rotary sealing joints at both ends. The rotary sealing joints are connected to the refrigeration system. The stirring blades are U-shaped, fit the outline of the crystallization vessel, and are connected to the stirring shaft. The refrigeration medium moves from top to bottom. A drive mechanism is installed at the upper end of the crystallization vessel, and the drive mechanism drives the stirring shaft to rotate.

[0006] Furthermore, the crystallization filter plate is installed at the lower part of the filter tank, and a reflux pipe is installed on one side of the filter tank. The circulation pump is installed on the reflux pipe, with the upper end of the reflux pipe connected to the crystallization kettle and the lower end connected to the filter tank.

[0007] Furthermore, the crystallization filter plate is placed horizontally.

[0008] Furthermore, the crystallizing filter plate is placed at an angle, and a telescopic rod is installed on the side wall of the filter tank. A scraper is installed at the telescopic end of the telescopic rod, and the scraper contacts the crystallizing filter plate. The scraper is hinged to the telescopic end of the telescopic rod.

[0009] Furthermore, temperature sensors are installed on the inner wall of the crystallization vessel and on the stirring shaft.

[0010] Furthermore, the frame, crystallizing vessel, and filter tank are fixedly connected to the frame, with the crystallizing vessel and filter tank arranged vertically.

[0011] The beneficial effects of this invention are as follows: It employs a low-temperature crystallization method, utilizing the physical principle that the solubility of different substances in specific solvents decreases at different rates with decreasing temperature; nervonic acid (cis-15-tetracosenoic acid) and its main impurities (such as erucic acid, cis-13-tetracosenoic acid) are very similar in molecular structure, differing only slightly in carbon chain length and double bond position; this minute difference leads to different solubility behaviors at low temperatures in specific organic solvents (such as acetone, ethanol, n-hexane, n-pentanol, etc.), with nervonic acid preferentially precipitating upon cooling; The crystals obtained in the first step are redissolved in fresh solvent, and then the above-described cooling crystallization process is repeated. Each repetition increases the purity of the product. The scraper prevents crystals from adhering to the crystallization filter plate, effectively preventing the crystallization filter plate from clogging. Attached Figure Description

[0012] Figure 1 This is a schematic diagram of the structure of the garlic fruit extraction and purification device described in this utility model; Figure 2 This is a top view of the stirring blades; Figure 3 This is a schematic diagram of a crystallization filter plate; In the diagram, 1. New solution; 2. Crystals; 3. Impurities; 4. Crystallization vessel; 5. Filter tank; 6. Refrigeration system; 7. Recovery tank; 8. Stirring shaft; 9. Stirring blades; 10. Crystallization filter plate; 11. Circulation pump; 12. Sealed bearing; 13. Rotary sealing joint; 14. Drive mechanism; 15. Return pipe; 17. Telescopic rod; 18. Scraper; 19. Temperature sensor; 20. Frame. Detailed Implementation

[0013] To make the above-mentioned objectives, features and advantages of this utility model more apparent and understandable, the specific embodiments of this utility model will be described in detail below with reference to the accompanying drawings.

[0014] This application provides a device for purifying nervonic acid extracted from garlic fruit. Please refer to the following: Figures 1-3 It includes: 1. New solution; 2. Crystals; 3. Impurities; 4. Crystallization vessel; 5. Filter tank; 6. Refrigeration system; and 7. Recovery tank; and also includes: The stirring shaft 8 and stirring blades 9 are connected to the refrigeration system 6. The refrigeration system 6 includes a refrigeration medium. The refrigeration medium moves from the upper end to the lower end of the stirring shaft 8 and flows through the stirring blades 9. The crystallization vessel 4 is connected to the filter tank 5. Crystallization filter plate 10 separates the mixed crystals 2 and impurities 3. Crystallization filter plate 10 is installed inside filter tank 5. The circulating pump 11 transports the separated crystals 2 to the crystallization vessel 4 for repeated crystallization. Repeating the above process can extract high-purity crystals 2.

[0015] In practical applications, during operation, the new solution 1 and crude nervonic acid are transported into the crystallization vessel 4. Then, the drive mechanism 14 is controlled to rotate the stirring shaft 8 and stirring blades 9. At the same time, the refrigeration system 6 delivers the cooling medium to the stirring shaft 8 and stirring blades 9 for stable cooling. During the cooling process, the physical principle that the solubility of different substances in specific solvents decreases at different rates with decreasing temperature is utilized. Nervonic acid (cis-15-tetracosenoic acid) and its main impurities (such as erucic acid and cis-13-tetracosenoic acid) are very similar in molecular structure, with only slight differences in carbon chain length and double bond position. This slight difference leads to different solubility behaviors at low temperatures in specific organic solvents (such as acetone, ethanol, n-hexane, n-pentanol, etc.). During cooling, nervonic acid will preferentially precipitate out. After crystallization has occurred for a certain period of time, the drive mechanism 14 stops rotating, and the valve between the crystallization vessel 4 and the filter tank 5 opens, allowing the crystallized mixture to be transported into the filter tank 5. Through the action of the crystallization filter plate 10, crystal 2 (high-purity nervonic acid) is filtered onto the filter plate 10. Then, the crystal 2 is returned to the crystallization vessel 4 by the circulation pump 11. At this point, the bottom of the filter tank 5 contains the old solution, which is discharged to the recovery tank 7 for recycling. New solution 1 (such as acetone, ethanol, n-hexane, n-pentanol, etc.) is then transported into the crystallization vessel 4 for re-crystallization. By repeating the above process, high-purity nervonic acid can be obtained.

[0016] Reference Figure 1 , Figure 2 , Figure 3 The crystallizing vessel 4 is equipped with sealed bearings 12 at both ends. The stirring shaft 8 is installed inside the sealed bearings 12. The stirring shaft 8 has openings at both ends and is equipped with rotary sealing joints 13 at both ends. The rotary sealing joints 13 are connected to the refrigeration system 6. The stirring fins 9 are U-shaped and fit the contour of the crystallizing vessel 4 and are connected to the stirring shaft 8. The refrigeration medium moves from top to bottom. The upper end of the crystallizing vessel 4 is equipped with a drive mechanism 14, which drives the stirring shaft 8 to rotate.

[0017] In practical applications, the sealed bearing 12 facilitates the stable rotation of the stirring shaft 8, the rotary sealing joint 13 facilitates the flow of the refrigerant medium, and the stirring shaft 8 can rotate stably. The stirring fins 9 facilitate stirring and can quickly exchange heat with the new solution, thereby reducing the temperature of the new solution.

[0018] Reference Figure 1 , Figure 2 , Figure 3 The crystallization filter plate 10 is installed at the lower position of the filter tank 5. A return pipe 15 is installed on one side of the filter tank 5. The circulation pump 11 is installed on the return pipe 15. The upper end of the return pipe 15 is connected to the crystallization vessel 4, and the lower end is connected to the filter tank 5.

[0019] In practical applications, the crystals 2 (high-purity nervonic acid) can be filtered above the crystal filter plate 10 through the action of the crystal filter plate 10. Then, the crystals 2 are returned to the crystallization vessel 4 through the action of the circulation pump 11. At this time, the bottom of the filter tank 5 is the old solution, which is discharged to the recovery tank 7 for recycling.

[0020] Reference Figure 1 , Figure 2 , Figure 3 The crystallization filter plate 10 is placed horizontally.

[0021] In practical applications, placing the crystallization filter plate 10 horizontally can optimize the structure, reduce maintenance frequency, and lower production costs.

[0022] Reference Figure 1 , Figure 2 , Figure 3 The crystallizing filter plate 10 is placed at an angle, and a telescopic rod 17 is installed on the side wall of the filter tank 5. A scraper 18 is installed at the telescopic end of the telescopic rod 17. The scraper 18 is in contact with the crystallizing filter plate 10, and the scraper 18 is hinged to the telescopic end of the telescopic rod 17.

[0023] In practical applications, the inclined placement of the crystallization filter plate 10 facilitates the flow of crystals 2 toward the circulation pump 11. The extension of the telescopic rod 17 can scrape the crystals 2 adhering to the surface of the crystallization filter plate 10 to the position of the return pipe 15, thereby minimizing the residue of crystals 2.

[0024] Reference Figure 1 , Figure 2 , Figure 3 Temperature sensors 19 are installed on the inner wall of the crystallization vessel 4 and on the stirring shaft 8.

[0025] In practical applications, the temperature sensor 19 helps staff understand the working conditions inside the crystallization vessel 4.

[0026] Reference Figure 1 , Figure 2 , Figure 3It includes a frame 20, a crystallizing vessel 4 and a filter tank 5, which are fixedly connected to the frame 20. The crystallizing vessel 4 and the filter tank 5 are arranged vertically.

[0027] In practical applications, arranging the crystallization vessel 4 and the filter tank 5 vertically is beneficial for the flow of crystals 2 and impurities 3.

Claims

1. A purification apparatus for extracting nervonic acid from garlic fruit, comprising a fresh solution (1), crystals (2), impurities (3), a crystallization vessel (4), a filter tank (5), a refrigeration system (6), and a recovery tank (7), characterized in that, Also includes; The stirring shaft (8) and stirring blades (9) are connected to the refrigeration system (6). The refrigeration system (6) includes a refrigeration medium. The refrigeration medium moves from the upper end to the lower end of the stirring shaft (8) and flows through the stirring blades (9) along the way. The crystallizing vessel (4) is connected to the filter tank (5). Crystallization filter plate (10) separates the mixed crystals (2) and impurities (3). Crystallization filter plate (10) is installed inside filter tank (5). The circulating pump (11) transports the separated crystals (2) to the crystallization vessel (4) for repeated crystallization. Repeating the above process can extract high-purity crystals (2).

2. The garlic fruit extraction and purification device according to claim 1, characterized in that, The crystallizer (4) is equipped with sealed bearings (12) at both ends. The stirring shaft (8) is installed inside the sealed bearings (12). The stirring shaft (8) is open at both ends. Rotary sealing joints (13) are installed at both ends of the stirring shaft (8). The rotary sealing joints (13) are connected to the refrigeration system (6). The stirring fins (9) are U-shaped and fit the outline of the crystallizer (4) and are connected to the stirring shaft (8). The refrigeration medium moves from top to bottom. The crystallizer (4) is equipped with a drive mechanism (14) at the top. The drive mechanism (14) drives the stirring shaft (8) to rotate.

3. The garlic fruit extraction and purification device according to claim 2, characterized in that, The crystallization filter plate (10) is installed at the lower position of the filter tank (5). A reflux pipe (15) is installed on one side of the filter tank (5). The circulation pump (11) is installed on the reflux pipe (15). The upper end of the reflux pipe (15) is connected to the crystallization vessel (4), and the lower end is connected to the filter tank (5).

4. The apparatus for purifying nervonic acid extracted from garlic fruit according to claim 3, characterized in that, The crystallization filter plate (10) is placed horizontally.

5. The apparatus for purifying nervonic acid extracted from garlic fruit according to claim 3, characterized in that, The crystallization filter plate (10) is placed at an angle, and a telescopic rod (17) is installed on the side wall of the filter tank (5). A scraper (18) is installed at the telescopic end of the telescopic rod (17). The scraper (18) contacts the crystallization filter plate (10), and the scraper (18) is hinged to the telescopic end of the telescopic rod (17).

6. A garlic fruit extraction and purification device according to claim 4 or 5, characterized in that, Temperature sensors (19) are installed on the inner wall of the crystallization vessel (4) and on the stirring shaft (8).

7. The apparatus for purifying nervonic acid extracted from garlic fruit according to claim 6, characterized in that, The frame (20), crystallizer (4) and filter tank (5) are fixedly connected to the frame (20), and the crystallizer (4) and filter tank (5) are arranged vertically.

Citation Information

Patent Citations

  • Automatic nervonic acid purification device

    CN219730862U