Temperature control type propolis extraction machine
By designing a temperature-controlled propolis extractor, the combination of negative pressure filter set, reaction tank and stirrer is used to solve the problem of propolis extraction time in the prior art, and the effect of efficient extraction and high purity is achieved.
Patent Information
- Application Number
- CN202421888881.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-08-06
- Publication Date
- 2025-05-23
- Estimated Expiration
- 2034-08-06
AI Technical Summary
Existing honey extraction devices require a lot of time to separate alcohol and propolis, which affects production efficiency.
A temperature-controlled propolis extractor is designed, using a combination of a negative pressure filter group, a reaction tank and agitator. Through temperature control, stirring and negative pressure, the ethanol in the propolis solution is fully evaporated, thereby achieving efficient extraction and high purity effects.
It realizes efficient extraction and high purity output of propolis, improves production efficiency and reduces extraction time.
Smart Images

Figure CN222889528U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of honey processing, in particular to a temperature-controlled propolis extractor. Background Art
[0002] Honey is taken from the nectar or secretions with a water content of about 75% from the flowers of plants, and stored in its second stomach. Under the action of multiple transformations in the body, it takes about 15 days of repeated brewing when various vitamins, minerals and amino acids are enriched to a certain value. At the same time, the polysaccharides in the nectar are converted into monosaccharides glucose and fructose that can be directly absorbed by the human body. The water content is less than 23% and is stored in the nest hole, which is sealed with beeswax. Honey is a supersaturated solution of sugar, which will produce crystals at low temperatures. The crystals are glucose, and the part that does not produce crystals is mainly fructose.
[0003] Propolis needs to be extracted from honey. Propolis is a collection of animal and plant essences, containing more than 300 chemical components, including aromatics, flavonoids, organic acids, terpenes, vitamins, enzymes, etc. It has antioxidant, antibacterial, anti-inflammatory, antiviral, liver-protecting and anti-cancer effects. As a natural substance that can improve health and physical fitness, propolis is particularly attractive.
[0004] The existing honey extraction device takes a lot of time to separate alcohol and propolis, which affects production efficiency. Utility Model Content
[0005] The utility model aims to provide a temperature-controlled propolis extractor, which has the effects of efficient extraction and high purity.
[0006] The above technical purpose of the utility model is achieved through the following technical solutions: a temperature-controlled propolis extractor, comprising a mounting plate, a lower surface of the mounting plate fixedly connected to a supporting leg, an upper surface of one end of the mounting plate fixedly connected to a cooling tank, a vacuum tube fixedly connected above one side of the cooling tank, one end of the vacuum tube fixedly connected to a vacuum pump, a condenser fixedly connected to the upper surface of the cooling tank, one end of the condenser fixedly connected to a reaction tank, a controller fixedly connected to the front of the reaction tank, a heating layer fixedly connected to the inner wall of the reaction tank, a stirrer fixedly connected to the bottom of the inner wall of the reaction tank, a conduit fixedly connected to the upper surface of the reaction tank, and a negative pressure filter group fixedly connected to one end of the conduit.
[0007] By adopting the above technical scheme, through the setting of negative pressure filter group, reaction tank and agitator, the staff first passes the propolis solution through the negative pressure filter group, filters out impurities, and then passes it into the reaction tank. After temperature control, stirring by the agitator and negative pressure, the ethanol in the propolis solution is fully volatilized and passed from the condenser into the cooling tank. The propolis is discharged from the bottom of the reaction tank, and the ethanol is cooled by the condenser and becomes liquid and falls into the cooling tank, achieving the effect of efficient extraction and high purity.
[0008] The utility model is further configured as follows: a universal wheel is fixedly connected to the lower surface of the support leg, the number of the support legs is four, and the four support legs are fixedly connected to the lower surface of the mounting plate in the form of a rectangular array.
[0009] By adopting the above technical solution, the support legs and the universal wheels are arranged to ensure that the mounting plate can move while maintaining a stable state to prevent tipping.
[0010] The utility model is further configured as follows: an ethanol output pipe is fixedly connected to the bottom of the other side of the cooling tank, and a cooling tank observation port is fixedly connected to the upper part of the front side of the cooling tank.
[0011] By adopting the above technical solution, the setting of the ethanol output pipe makes it convenient to discharge the ethanol for recycling, and the setting of the cooling tank observation port makes it convenient to observe the cooling tank.
[0012] The utility model is further configured as follows: the lower surface of the vacuum pump is fixedly connected to the upper surface of the mounting plate, and a valve is fixedly connected below the vacuum tube.
[0013] By adopting the above technical solution, the setting of the vacuum pump strengthens the connectivity between devices to prevent them from falling apart, and the setting of the valve facilitates closing the vacuum pipeline to prevent back suction.
[0014] The utility model is further configured as follows: the condenser comprises a cooling shell, and an inner exchange tube is arranged on the inner wall of the cooling shell.
[0015] By adopting the above technical solution, the setting of the condenser can ensure the heat exchange effect and promote the stable progress of the condensation process.
[0016] The utility model is further configured as follows: one end of the upper surface of the cooling shell is fixedly connected with a cooling water inlet, and the other end of the upper surface of the condenser is fixedly connected with a cooling water drain.
[0017] By adopting the above technical solution, the setting of the cooling water inlet and the cooling water outlet can gradually cool the gas inside the condenser, ensuring that the formed liquid can fall into the cooling tank stably.
[0018] The utility model is further configured as follows: the reaction tank comprises an isolation shell, and a heat-insulating liner is fixedly connected to the inner wall of the isolation shell.
[0019] By adopting the above technical solution, the setting of the reaction tank can isolate the internal and external environments, protect the staff and improve the temperature control and ethanol volatilization effects.
[0020] The utility model is further configured as follows: a temperature gauge is fixedly connected to one side of the upper surface of the reaction tank, a vacuum gauge is fixedly connected to the other side of the upper surface of the reaction tank, and a glue discharge port is fixedly connected to the bottom of one side of the reaction tank.
[0021] By adopting the above technical solution, the setting of the temperature gauge and the vacuum gauge is convenient for monitoring the temperature and vacuum conditions inside the reaction tank, and the setting of the glue discharge port is convenient for discharging the extracted propolis.
[0022] The utility model is further configured as follows: the negative pressure filter group comprises a first negative pressure filter, and a second negative pressure filter is arranged at the bottom of the first negative pressure filter.
[0023] By adopting the above technical solution, the setting of the negative pressure filter group can filter the propolis solution multiple times, improve the purity, and then improve the purity of the extraction.
[0024] The utility model is further configured as follows: a filter screen is fixedly connected to the inner wall of the first negative pressure filter, and a filter element is arranged below the filter screen.
[0025] By adopting the above technical solution, the filter screen and filter element can be set up to filter step by step from large to small, reducing the pressure of filtration while ensuring the efficiency of filtration.
[0026] The beneficial effects of the utility model are as follows: through the arrangement of the negative pressure filter group, the reaction tank and the agitator, the staff first passes the propolis solution through the negative pressure filter group, filters out the impurities, and then passes it into the reaction tank; after temperature control, stirring by the agitator and the effect of negative pressure, the ethanol in the propolis solution is fully volatilized, and passed from the condenser into the cooling tank, the propolis is discharged from the bottom of the reaction tank, and the ethanol is cooled by the condenser and becomes liquid and falls into the cooling tank, thereby achieving the effect of efficient extraction and high purity. BRIEF DESCRIPTION OF THE DRAWINGS
[0027] In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings required for use in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without creative work.
[0028] Figure 1This is a schematic diagram of the shaft side structure of the utility model;
[0029] Figure 2 This is a schematic diagram of the cross-sectional structure of the first negative pressure filter of the utility model;
[0030] Figure 3 This is a schematic diagram of the cross-sectional structure of the reaction tank of the utility model;
[0031] Figure 4 This is a schematic diagram of the cross-sectional structure of the condenser of the utility model.
[0032] In the figure, 1. mounting plate; 2. supporting legs; 3. cooling tank; 4. vacuum tube; 5. vacuum pump; 6. condenser; 7. reaction tank; 8. controller; 9. heating layer; 10. agitator; 11. conduit; 12. negative pressure filter group; 13. universal wheel; 14. ethanol output pipe; 15. cooling tank observation port; 16. valve; 17. cooling water inlet; 18. cooling water outlet; 19. thermometer; 20. vacuum gauge; 21. glue discharge port; 22. filter screen; 23. filter element; 601. cooling shell; 602. internal exchange tube; 701. isolation shell; 702. thermal insulation liner; 1201. first negative pressure filter; 1202. second negative pressure filter. DETAILED DESCRIPTION
[0033] The technical solution of the utility model will be clearly and completely described below in conjunction with specific embodiments. Obviously, the described embodiments are only part of the embodiments of the utility model, rather than all of the embodiments. Based on the embodiments of 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.
[0034] Reference Figure 1-4A temperature-controlled propolis extractor comprises a mounting plate 1, a supporting leg 2 is fixedly connected to the lower surface of the mounting plate 1, a universal wheel 13 is fixedly connected to the lower surface of the supporting leg 2, there are four supporting legs 2, and the four supporting legs 2 are fixedly connected to the lower surface of the mounting plate 1 in the form of a rectangular array. The arrangement of the supporting legs and the universal wheel ensures that the mounting plate can be moved while maintaining a stable state to prevent tipping. A cooling tank 3 is fixedly connected to the upper surface of one end of the mounting plate 1, an ethanol output pipe 14 is fixedly connected to the bottom of the other side of the cooling tank 3, and a cooling tank observation port 15 is fixedly connected to the upper front of the cooling tank 3. The arrangement of the ethanol output pipe facilitates the discharge of ethanol for recycling, and the arrangement of the cooling tank observation port facilitates the observation of the cooling tank. A vacuum tube 4 is fixedly connected to the upper side of the cooling tank 3, one end of the vacuum tube 4 is fixedly connected to a vacuum pump 5, the lower surface of the vacuum pump 5 is fixedly connected to the upper surface of the mounting plate 1, a valve 16 is fixedly connected to the lower side of the vacuum tube 4, the setting of the vacuum pump strengthens the connectivity between the devices to prevent them from falling apart, the setting of the valve facilitates closing the vacuum pipeline to prevent back suction, a condenser 6 is fixedly connected to the upper surface of the cooling tank 3, the condenser 6 includes a cooling shell 601, the inner wall of the cooling shell 601 is provided with an inner exchange tube 602, the setting of the condenser can ensure the effect of cold and heat exchange and promote the stable progress of the condensation process, one end of the upper surface of the cooling shell 601 is fixedly connected to a cooling water inlet 17, the other end of the upper surface of the condenser 6 is fixedly connected to a cooling water outlet 18, the cooling The setting of the cooling water inlet and the cooling water drain port can gradually cool the gas inside the condenser to ensure that the formed liquid can stably fall into the cooling tank. One end of the condenser 6 is fixedly connected to the reaction tank 7, and the reaction tank 7 includes an isolation shell 701. The inner wall of the isolation shell 701 is fixedly connected to an insulation liner 702. The setting of the reaction tank can isolate the internal and external environments, protect the staff while improving the temperature control and ethanol volatilization effects. A thermometer 19 is fixedly connected to one side of the upper surface of the reaction tank 7, and a vacuum gauge 20 is fixedly connected to the other side of the upper surface of the reaction tank 7. A glue discharge port 21 is fixedly connected to the bottom of one side of the reaction tank 7. The setting of the thermometer and the vacuum gauge is convenient for monitoring the temperature and vacuum conditions inside the reaction tank, and the setting of the glue discharge port is convenient for discharging the extracted propolis. The front of the reaction tank 7 is fixedly connected with a controller 8, the inner wall of the reaction tank 7 is fixedly connected with a heating layer 9, the bottom of the inner wall of the reaction tank 7 is fixedly connected with an agitator 10, the upper surface of the reaction tank 7 is fixedly connected with a conduit 11, one end of the conduit 11 is fixedly connected with a negative pressure filter group 12, the negative pressure filter group 12 includes a first negative pressure filter 1201, and a second negative pressure filter 1202 is arranged at the bottom of the first negative pressure filter 1201. The arrangement of the negative pressure filter group can filter the propolis solution multiple times to improve the purity, thereby improving the purity of the extraction, the inner wall of the first negative pressure filter 1201 is fixedly connected with a filter screen 22, and a filter element 23 is arranged below the filter screen 22. The arrangement of the filter screen and the filter element can filter step by step from large to small to reduce the pressure of filtration.At the same time, the filtration efficiency is guaranteed.
[0035] In the utility model, the staff first passes the propolis solution through the negative pressure filter group 12 to filter out impurities, and then passes it into the reaction tank 7. After temperature control, stirring by the stirrer 10 and negative pressure, the ethanol in the propolis solution is fully volatilized and passed into the cooling tank 3 from the condenser 6. The propolis is discharged from the bottom of the reaction tank 7, and the ethanol is cooled by the condenser 6 and becomes liquid and falls into the cooling tank 3, thereby achieving the effect of efficient extraction and high purity.
[0036] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.
Claims
1. A temperature-controlled propolis extraction machine, comprising a mounting plate (1), characterized in that: The lower surface of the mounting plate (1) is fixedly connected to a supporting leg (2); the upper surface of one end of the mounting plate (1) is fixedly connected to a cooling tank (3); a vacuum tube (4) is fixedly connected above one side of the cooling tank (3); one end of the vacuum tube (4) is fixedly connected to a vacuum pump (5); the upper surface of the cooling tank (3) is fixedly connected to a condenser (6); one end of the condenser (6) is fixedly connected to a reaction tank (7); the front of the reaction tank (7) is fixedly connected to a controller (8); the inner wall of the reaction tank (7) is fixedly connected to a heating layer (9); the bottom of the inner wall of the reaction tank (7) is fixedly connected to an agitator (10); the upper surface of the reaction tank (7) is fixedly connected to a conduit (11); one end of the conduit (11) is fixedly connected to a negative pressure filter group (12).
2. A temperature-controlled propolis extractor according to claim 1, characterized in that: The lower surface of the support leg (2) is fixedly connected with a universal wheel (13), the number of the support legs (2) is four, and the four support legs (2) are fixedly connected to the lower surface of the mounting plate (1) in the form of a rectangular array.
3. A temperature-controlled propolis extractor according to claim 1, characterized in that: An ethanol output pipe (14) is fixedly connected to the bottom of the other side of the cooling tank (3), and a cooling tank observation port (15) is fixedly connected to the top of the front of the cooling tank (3).
4. A temperature-controlled propolis extractor according to claim 1, characterized in that: The lower surface of the vacuum pump (5) is fixedly connected to the upper surface of the mounting plate (1), and a valve (16) is fixedly connected below the vacuum tube (4).
5. The temperature-controlled propolis extractor according to claim 1, characterized in that: The condenser (6) comprises a cooling shell (601), and an inner exchange tube (602) is provided on the inner wall of the cooling shell (601).
6. A temperature-controlled propolis extractor according to claim 5, characterized in that: One end of the upper surface of the cooling shell (601) is fixedly connected to a cooling water inlet (17), and the other end of the upper surface of the condenser (6) is fixedly connected to a cooling water outlet (18).
7. The temperature-controlled propolis extractor according to claim 1, characterized in that: The reaction tank (7) comprises an isolation shell (701), and a heat-insulating inner container (702) is fixedly connected to the inner wall of the isolation shell (701).
8. The temperature-controlled propolis extractor according to claim 1, characterized in that: A temperature gauge (19) is fixedly connected to one side of the upper surface of the reaction tank (7), a vacuum gauge (20) is fixedly connected to the other side of the upper surface of the reaction tank (7), and a glue discharge port (21) is fixedly connected to the bottom of one side of the reaction tank (7).
9. The temperature-controlled propolis extractor according to claim 1, characterized in that: The negative pressure filter group (12) comprises a first negative pressure filter (1201), and a second negative pressure filter (1202) is arranged at the bottom of the first negative pressure filter (1201).
10. The temperature-controlled propolis extractor according to claim 9, characterized in that: A filter screen (22) is fixedly connected to the inner wall of the first negative pressure filter (1201), and a filter element (23) is arranged below the filter screen (22).