Purifying and crystallizing device for essence production

Abstract

The utility model relates to the technical field of essence production, and discloses a purification and crystallization device for essence production, which comprises a crystallization bin, a feeding cylinder, a purification bin, a stepping motor and a bin cover, the feeding cylinder is fixedly connected to the top end of the crystallization bin, and the purification bin is fixedly connected to the top end of the feeding cylinder. According to the purification and crystallization device for essence production, stirring, flow guiding and anti-blocking functions are achieved through the feeding cylinder, the purification bin and the crystallization bin in combination with the rotating rod driven by the stepping motor, and the essence production efficiency and purity are remarkably improved. Raw materials can be conveniently added through the feeding cylinder, the raw materials are finely filtered through the multi-layer and multi-stage screening plates and the sealing bin door in the purification bin, impurity mixing is reduced, and the essence quality is guaranteed. The anti-blocking scraping rod is attached to the upper surface of the screening plate, and material blocking is prevented. The transverse feeding pipe, the feeding bin, the driving motor and the feeding propeller achieve automatic conveying of materials, the labor intensity is reduced, and the production efficiency is improved.

Description

Technical Field

[0001] This utility model relates to the field of fragrance production technology, specifically a purification and crystallization device used in fragrance production. Background Technology

[0002] In the vast field of fragrance production, purification and crystallization play a crucial role. Fragrance, a product skillfully blended from various natural or synthetic flavorings, directly affects the aroma profile, taste, and stability of the final product.

[0003] In existing technologies, the purification process of fragrances mainly relies on some traditional processes, such as simple physical filtration. This method can only remove larger particles of impurities and is ineffective against tiny particles. While chemical precipitation can handle some specific types of impurities, it may introduce new chemical substances, affecting the purity and safety of the fragrance. Distillation, when separating components with different boiling points, often requires high-temperature operation, which is not only energy-intensive but may also lead to the loss of some heat-sensitive components in the fragrance.

[0004] In the crystallization stage, existing equipment typically only involves improvements to a simple cooling system, lacking precise control over the crystallization process. For example, the stirring device may not provide uniform stirring force and speed, leading to localized overcooling or oversaturation of the fragrance during crystallization, thus affecting crystal size and purity. Regarding temperature control, most equipment can only achieve coarse temperature regulation and cannot meet the precise temperature change curves required for fragrance crystallization.

[0005] Therefore, it is necessary to propose a purification and crystallization apparatus for fragrance production. Utility Model Content

[0006] To address the shortcomings of existing technologies, this invention provides a purification and crystallization device for flavor production, which has the advantages of improving flavor quality and production efficiency, and solves the problems mentioned in the background technology.

[0007] This utility model provides the following technical solution: a purification and crystallization device for flavor production, comprising a crystallization chamber, a feed cylinder, a purification chamber, a stepper motor, and a chamber cover:

[0008] The feed cylinder is fixedly connected to the top of the crystallization chamber, and the purification chamber is fixedly connected to the top of the feed cylinder. The chamber cover is located at the top of the purification chamber and fixedly installed at the bottom of the crystallization chamber. A rotating rod is fixedly connected to the output end of the stepper motor. The rotating rod passes through the crystallization chamber and the feed cylinder sequentially, extending into the interior of the purification chamber. From bottom to top, a stirring paddle, a guide plate, and an anti-clogging scraper are fixedly connected to the surface of the rotating rod. An exhaust valve is fixedly installed on the surface of the chamber cover. The stirring paddle rotates at a speed of 50-200 rpm. The guide plate has an inclination angle of 30-60 degrees. The contact pressure between the anti-clogging scraper and the multi-stage sieve plate is 0.5-1.5 N / cm². 2 .

[0009] Preferably, the bottom end of the crystallization chamber is fixedly connected with a support leg.

[0010] Preferably, the bottom of the crystallization chamber is fixedly connected to a discharge port, and a valve is fixedly installed on the discharge port.

[0011] Preferably, a horizontal feed pipe is fixedly connected to the upper surface of the chamber cover. The diameter of the horizontal feed pipe is 10-20cm and the length is 50-100cm. A feed chamber is fixedly connected to one end of the horizontal feed pipe. A drive motor is fixedly connected to the side of the feed chamber. A feeding propeller is fixedly connected to the output end of the drive motor. The feeding propeller is located inside the horizontal feed pipe. One end opening of the horizontal feed pipe corresponds to the feed inlet of the purification chamber. The power of the drive motor is 0.5-1.5kW, and the rotational speed of the feeding propeller is 100-300rpm.

[0012] Preferably, the inner wall of the purification chamber is fixedly connected with multiple multi-level sieve plates, and the side wall of the purification chamber is provided with multiple sealed chamber doors, the sealed chamber doors are positioned corresponding to the multi-level sieve plates, and the bottom end of the anti-clogging scraper is attached to the upper surface of the multi-level sieve plates.

[0013] Preferably, a sector-shaped valve plate is movably installed inside the feed cylinder.

[0014] Preferably, the guide plate and the stirring paddle are both located inside the crystallization chamber, the guide plate is located directly below the inlet of the crystallization chamber, and a cooling coil is provided inside the side wall of the crystallization chamber.

[0015] Compared with the prior art, the present invention has the following beneficial effects:

[0016] This purification and crystallization device for flavor production utilizes a feed cylinder, purification chamber, and crystallization chamber, combined with a stepper motor-driven rotor to achieve stirring, flow guidance, and anti-clogging functions, significantly improving flavor production efficiency and purity. The feed cylinder facilitates raw material addition, while the purification chamber features multi-layered, multi-stage sieve plates and a sealed door for fine filtration, reducing impurities and ensuring flavor quality. An anti-clogging scraper adheres to the upper surface of the sieve plates to prevent material blockage. A horizontal feed pipe, feed chamber, drive motor, and feeding propeller automate material transport, reducing labor intensity and increasing production efficiency. During crystallization, the guide plate and stirring paddle promote material flow and mixing, while the cooling coil precisely controls the crystallization temperature, ensuring uniform and pure flavor crystal growth. An exhaust valve on the chamber cover releases gas, preventing excessive internal pressure and ensuring safe operation. The overall design is highly efficient, automated, and precisely controlled, greatly improving flavor quality and production efficiency, demonstrating significant beneficial effects. Attached Figure Description

[0017] To more clearly illustrate the technical solutions of the embodiments of this utility model, the accompanying drawings used in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0018] Figure 1 This is a schematic diagram of the overall structure of the device of this utility model;

[0019] Figure 2 This is a cross-sectional structural diagram of the crystallization chamber and purification chamber of this utility model;

[0020] Figure 3 This is a cross-sectional view of the compartment cover of this utility model.

[0021] The attached diagram lists the components represented by each number as follows:

[0022] 100. Crystallization chamber; 101. Support leg; 102. Discharge port; 103. Valve; 104. Cooling coil;

[0023] 200. Feed cylinder; 201. Sector valve plate;

[0024] 300. Purification chamber; 301. Multi-stage sieve plate; 302. Sealed chamber door;

[0025] 400. Stepper motor; 401. Rotating rod; 402. Agitator; 403. Guide plate; 404. Anti-clogging scraper;

[0026] 500. Bin cover; 501. Exhaust valve; 502. Horizontal feed pipe; 503. Feed bin; 504. Drive motor; 505. Feed propeller. Detailed Implementation

[0027] 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.

[0028] Reference Figures 1-3 As shown, a purification and crystallization device for flavor production includes a crystallization chamber 100, a feed cylinder 200, a purification chamber 300, a stepper motor 400, and a chamber cover 500. The feed cylinder 200 is fixedly connected to the top of the crystallization chamber 100, allowing raw materials to be directly added from above, facilitating material transport. The purification chamber 300 is fixedly connected to the top of the feed cylinder 200, further ensuring smooth material flow from the feed cylinder 200 to the purification chamber 300. The chamber cover 500 is simultaneously located at the top of the purification chamber 300 and fixedly installed at the bottom of the crystallization chamber 100, forming a closed production environment that effectively prevents the entry of external impurities and ensures the purity of the internal materials. The stepper motor 400 serves as a power source, with a rotating rod 401 fixedly connected to its output end. This rotating rod 401 passes sequentially through the crystallization chamber 100, the feed cylinder 200, and extends into the purification chamber 300, enabling comprehensive stirring and control of the entire device. From bottom to top, the surface of the rotating rod 401 is sequentially connected to a stirring paddle 402, a guide plate 403, and an anti-clogging scraper 404. These components work together to ensure uniform mixing and effective flow of materials within the device, preventing clogging. An exhaust valve 501 is fixedly installed on the surface of the silo cover 500 to discharge gases generated during purification, maintaining stable internal pressure and ensuring production safety. The stirring paddle 402 rotates at a speed of 50-200 rpm, the guide plate 403 has an inclination angle of 30-60 degrees, and the contact pressure between the anti-clogging scraper 404 and the multi-stage screening plate 301 is 0.5-1.5 N / cm². 2 .

[0029] Preferably, the bottom of the crystallization chamber 100 is fixedly connected to a support leg 101. The design of the support leg 100 not only provides a stable support structure, but also ensures the distance between the device and the ground, making it easy to maintain and clean.

[0030] Preferably, the bottom of the crystallization chamber 100 is fixedly connected to a discharge port 102, the design of which allows the crystallized material to be easily discharged. A valve 103 is fixedly installed on the discharge port 102, the presence of which can control the discharge speed and timing of the material, ensuring the continuity and stability of production.

[0031] Preferably, a horizontal feed pipe 502 is fixedly connected to the upper surface of the hopper cover 500. This design allows raw materials to be conveniently added to the device through the horizontal feed pipe 502. One end of the horizontal feed pipe 502 is fixedly connected to a feed hopper 503, which serves as a temporary storage area for the raw materials, ensuring a stable supply. A drive motor 504 is fixedly connected to the side of the feed hopper 503, providing power to the feeding propeller 505. The feeding propeller 505 is located inside the horizontal feed pipe 502 and pushes the raw materials to the purification chamber for purification treatment through rotation. One end opening of the horizontal feed pipe 502 corresponds to the inlet position of the purification chamber 300, ensuring that the raw materials can accurately enter the purification chamber 300. The power of the drive motor 504 is 0.5-1.5kW, and the speed range of the feeding propeller 505 is 100-300rpm.

[0032] Furthermore, the inner wall of the purification chamber 300 is fixedly connected with multiple layers of multi-stage sieve plates 301. The design of the multi-layer, multi-stage sieve plates 301 enables multi-stage screening of raw materials, improving purification efficiency. Multiple sealing doors 302 are provided on the side walls of the purification chamber 300. The presence of the sealing doors 302 allows the sieve plates to be cleaned and maintained independently, while ensuring the airtightness of the purification chamber 300. The sealing doors 302 correspond to the positions of the multi-stage sieve plates 301, facilitating operation and maintenance. The bottom end of the anti-clogging scraper 404 is abutted against the upper surface of the multi-stage sieve plate 301. This design effectively prevents material from clogging the sieve plates during the screening process, ensuring the smooth progress of the purification process.

[0033] In a further preferred embodiment, a sector valve plate 201 is movably installed inside the feed cylinder 200. The presence of the sector valve plate 201 can regulate the flow rate and velocity of the material in the feed cylinder 200, ensuring that the material can enter the purification chamber 300 for purification treatment as needed.

[0034] Preferably, both the guide plate 403 and the agitator 402 are located inside the crystallization chamber 100, with the guide plate 403 positioned directly below the feed inlet of the crystallization chamber 100. This design ensures that the material entering the crystallization chamber can be immediately guided by the guide plate 403 to a suitable position for crystallization. A cooling coil 104 is installed inside the side wall of the crystallization chamber 100. The presence of the cooling coil 104 regulates the temperature inside the crystallization chamber 100, providing suitable temperature conditions for the crystallization process and ensuring the crystallization effect.

[0035] In the description of this utility model, it should be understood that the terms "coaxial", "bottom", "one end", "top", "middle", "other end", "upper", "side", "top", "inner", "front", "center", "both ends", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the 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.

[0036] In this utility model, unless otherwise explicitly specified and limited, the terms "installation", "setting", "connection", "fixing", "screw connection", etc., should be interpreted broadly. For example, they can refer to a fixed connection, a detachable connection, or an integral part; they can refer to a mechanical connection or an electrical connection; they can refer to a direct connection or an indirect connection through an intermediate medium; they can refer to the internal connection of two components or the interaction between two components. Unless otherwise explicitly limited, those skilled in the art can understand the specific meaning of the above terms in this utility model according to the specific circumstances.

[0037] Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present invention, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A purification crystallization device for essence production, comprising a crystallization bin (100), a feeding cylinder (200), a purification bin (300), a stepping motor (400) and a bin cover (500), characterized in that: The feeding cylinder (200) is fixedly connected to the top end of the crystallization bin (100), the purification bin (300) is fixedly connected to the top end of the feeding cylinder (200), the bin cover (500) is arranged at the top end of the purification bin (300), the bin cover (500) is fixedly installed at the bottom end of the crystallization bin (100), the output end of the stepping motor (400) is fixedly connected with a rotating rod (401), the rotating rod (401) extends to the inside of the purification bin (300) through the crystallization bin (100) and the feeding cylinder (200) in sequence, the surface of the rotating rod (401) is fixedly connected with a stirring paddle (402), a flow guide plate (403) and a anti-blocking scraping rod (404) in sequence from bottom to top, the surface of the bin cover (500) is fixedly installed with an exhaust valve (501), the rotating speed of the stirring paddle (402) ranges from 50 rpm to 200 rpm, the inclination angle of the flow guide plate (403) ranges from 30 degrees to 60 degrees, and the contact pressure between the anti-blocking scraping rod (404) and the multi-stage screening plate (301) ranges from 0.5 N / cm to 1.5 N / cm 2 .

2. A purification crystallization apparatus for use in the production of fragrances according to claim 1, characterized in that: The bottom end of the crystallization bin (100) is fixedly connected with a supporting leg (101).

3. A purification crystallization apparatus for use in the production of fragrances according to claim 2, characterized in that: The bottom of the crystallization bin (100) is fixedly connected with a discharge port (102), and the discharge port (102) is fixedly installed with a valve (103).

4. A purification and crystallization apparatus for use in the production of fragrances as claimed in claim 1, characterized in that: The upper surface of the bin cover (500) is fixedly connected with a transversely placed feeding pipe (502), the diameter of the transversely placed feeding pipe (502) is 10-20 cm, the length is 50-100 cm, one end of the transversely placed feeding pipe (502) is fixedly connected with a feeding bin (503), the side surface of the feeding bin (503) is fixedly connected with a driving motor (504), the output end of the driving motor (504) is fixedly connected with a feeding propeller (505), the feeding propeller (505) is located inside the transversely placed feeding pipe (502), one end opening of the transversely placed feeding pipe (502) corresponds to the feeding port position of the purification bin (300), the power of the driving motor (504) is 0.5-1.5 kW, and the rotating speed range of the feeding propeller (505) is 100-300 rpm.

5. A purification and crystallization apparatus for use in the production of fragrances as claimed in claim 2, characterized in that: The inner wall of the purification bin (300) is fixedly connected with a plurality of multilayer and multistage screening plates (301), the side wall of the purification bin (300) is provided with a plurality of sealing bin doors (302), the sealing bin doors (302) correspond to the positions of the multistage screening plates (301), and the bottom end of the anti-blocking scraping rod (404) is attached to the upper surface of the multistage screening plates (301).

6. A purification crystallization apparatus for use in the production of fragrances as claimed in claim 1, characterized in that: The inside of the feeding cylinder (200) is movably installed with a sector valve plate (201).

7. A purification and crystallization apparatus for use in the production of fragrances as claimed in claim 1, characterized in that: The guide vane (403) and the stirring paddle (402) are both located inside the crystallization bin (100), the guide vane (403) is located directly below the feeding port of the crystallization bin (100), and the side wall of the crystallization bin (100) is provided with a cooling coil (104).

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