Flavored syrup production and concentration system
By designing a flavored syrup production and concentration system that uses a rotating scraper barrel and an arc-shaped corrugated plate, the problems of poor film formation, low concentration efficiency, and insufficient cleaning during the flavored syrup concentration process in the existing technology are solved, and high efficiency is achieved. , stable syrup concentration and equipment cleaning.
Patent Information
- Application Number
- CN202421157887.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-05-27
- Publication Date
- 2025-01-21
- Estimated Expiration
- 2034-05-27
AI Technical Summary
In the prior art, the flavor syrup concentration process has poor film formation effect, low concentration efficiency, and inadequate cleaning can easily cause cross-contamination, affecting the stability between batches.
A flavor syrup production and concentration system is designed, which uses a concentrator body with a jacket on the outside, a feed port and an arc-shaped flow distributor on the top, and a rotating scraper barrel and arc-shaped corrugated plate inside. The combination of plate tube and curved corrugated plate achieves uniform film formation and efficient evaporation of syrup. At the same time, the system is equipped with a steam inlet and a sewage outlet, which can automatically adjust the steam flow to ensure that the syrup is concentrated at a suitable temperature. The system is also equipped with a water supply device and a spray nozzle, which can automatically clean the concentrator to prevent syrup residue.
Through this system, flavor syrup can form a thin film with uniform texture, improve evaporation efficiency, shorten concentration time, and prevent sugar flavor substances from thermal decomposition and syrup discoloration. At the same time, the automatic cleaning function ensures the cleanliness of the equipment, prevents cross-contamination, and ensures stability between batches.
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Figure CN222368363U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of syrup production, in particular to a flavor syrup production and concentration system. Background Art
[0002] The concentration of flavored syrup has always been the most important part of the flavored syrup production process. If the concentration time of flavored syrup is too long, it will lead to problems such as thermal decomposition of sugar flavor substances and discoloration of syrup. Therefore, in the production process, the concentration efficiency is generally improved as much as possible, the concentration temperature is lowered, and the concentration time is shortened to ensure the quality of flavored syrup production.
[0003] In the prior art, a scraper evaporator is usually used to concentrate flavored syrups. This evaporator uses a straight scraper. The disadvantage is that as the concentration process of the flavored syrup progresses, the concentration increases, and the syrup cannot be uniformly filmed on the inner wall of the evaporator, which affects the concentration efficiency. In addition, directly pouring the flavored syrup also makes it difficult to stir the scraper, which is not conducive to film formation. In addition, after the production is completed, the cleaning of the equipment is not in place, which easily causes contamination of the next batch. Therefore, a dedicated flavored syrup concentration system is urgently needed to ensure the smooth progress of the concentration process and ensure the quality of the product. Utility Model Content
[0004] The technical problem to be solved by the utility model is to provide a flavor syrup production and concentration system, aiming to solve the technical problems existing in the prior art of poor film-forming effect, low concentration efficiency, and inadequate cleaning that easily causes cross contamination and affects the stability between batches.
[0005] The technical scheme of the utility model is: a flavor syrup production and concentration system, comprising a concentrator body with a jacket on the outside, a feed port on the top of the concentrator body, an arc flow distributor connected to the feed port, a rotating scraper cylinder on the inside of the concentrator body, a circle of inclined arc corrugated plates around the outer wall of the rotating scraper cylinder, the rotating scraper cylinder is driven to rotate by a hollow shaft, the syrup is sprayed uniformly on the inner wall of the concentrator body through the arc flow distributor from the feed port, and the rotating scraper cylinder uses the arc corrugated plates to continuously and uniformly smear the flowing syrup into a thin film under the drive of the hollow shaft; a steam inlet is provided on the upper part of the jacket and a sewage outlet is provided on the bottom, steam is passed from the steam inlet into the jacket to evaporate and concentrate the syrup and then discharged from the sewage outlet; a discharge port is provided at the bottom of the concentrator body and a condenser is connected to the top, the condenser is also connected to a receiving tank, the concentrated syrup is discharged from the discharge port, and the evaporated solvent is cooled by the condenser and collected in the receiving tank;
[0006] The hollow shaft is connected to a water supply device, and a spray nozzle is provided on the upper part of the hollow shaft. The water supply device can draw water into the hollow shaft and spray it out through the spray nozzle. The feed port can be used to add cleaning water into the concentrator body, and the concentrator body can be fully cleaned in cooperation with the spray nozzle, and the washing water is discharged from the discharge port.
[0007] Furthermore, the arc flow distributor described in the utility model is provided with an intermediate connecting port in the middle, which is connected to the feed port through a connecting pipe, and a plurality of outlets are respectively provided on both sides of the arc flow distributor. The arc of the arc flow distributor is arranged along the inner wall of the concentrator body, and the outlet is arranged toward the inner wall of the concentrator body.
[0008] Furthermore, the outlet in the utility model is connected with a conical discharge pipe.
[0009] Furthermore, the arc-shaped corrugated plates in the utility model have a plurality of pieces and are distributed at equal intervals.
[0010] Furthermore, the concentrator body of the utility model is provided with a thermometer socket for assembling a thermometer to detect the concentrating temperature.
[0011] Furthermore, the condenser described in the utility model is provided with a refrigerant inlet, a refrigerant outlet, an evaporative solvent inlet, and a coolant outlet. The evaporative solvent inlet is connected to the concentrator body through a circulation pipe, and the coolant outlet is connected to a receiving tank. The condenser is also provided with a vacuum interface, and the vacuum interface is connected to a vacuum pump for extracting air.
[0012] Furthermore, the water supply device in the utility model comprises a water pipe rotatably and sealably connected to the bottom of the hollow rotating shaft, and the water pipe is connected to an external water source through a water pump.
[0013] Furthermore, the injection nozzles described in the utility model are uniformly arranged in a plurality around the hollow rotating shaft, and the hollow rotating shaft is driven to rotate by a motor.
[0014] Compared with the prior art, the utility model has the following advantages: the utility model can not only make the feed syrup form a thin film with uniform texture, improve its evaporation efficiency, shorten the concentration time, and prevent the occurrence of thermal decomposition of sugar flavor substances, discoloration of syrup, etc., but also can fully clean the concentrator after production is completed by adding cleaning water, automatic water spray cleaning, etc., to prevent the syrup from sticking to the inner wall and causing contamination of the next batch, thereby ensuring stability between batches. BRIEF DESCRIPTION OF THE DRAWINGS
[0015] Figure 1 It is a schematic diagram of the system structure of the utility model;
[0016] Figure 2It is a schematic diagram of the specific structure of the arc-shaped flow distributor described in the utility model (the conical discharge pipe is not drawn).
[0017] Among them: 1. Concentrator body; 2. Jacket; 3. Feed inlet; 4. Arc-shaped flow distributor; 4a. Middle connecting port; 4b. Outlet; 5. Rotating scraper cylinder; 6. Arc-shaped corrugated plate; 7. Hollow rotating shaft; 8. Connecting pipe; 9. Conical discharge pipe; 10. Steam inlet; 11. Drain outlet; 12. Thermometer socket; 13. Discharge port; 14. Condenser; 14a. Refrigerant inlet; 14b. Refrigerant outlet; 14c. Evaporating solvent inlet; 15. Receiving tank; 16. Circulation pipe; 17. Vacuum interface; 18. Injection nozzle; 19. Motor. DETAILED DESCRIPTION
[0018] The specific implementation of the utility model is described in detail below with reference to the accompanying drawings.
[0019] Example:
[0020] The accompanying drawings show a specific implementation of a flavor syrup production and concentration system of the utility model, as shown in FIG. Figure 1 It mainly includes a concentrator body 1. A feed port 3 is provided on the top of the concentrator body 1. The feed port 3 is connected to an arc-shaped flow distributor 4. The syrup enters from the feed port 3 and is evenly sprayed on the inner wall of the concentrator body 1 through the arc-shaped flow distributor 4 to initially form a film on the wall.
[0021] Structural combination of arc flow distributor 4 Figure 2 As shown, a middle connection port 4a is provided in the middle thereof, and the middle connection port 4a is connected to the feed port 3 through a connecting pipe 8. Two outlets 4b are respectively provided on both sides of the middle connection port 4a on the arc-shaped flow distributor 4, and each outlet 4b is connected to a conical discharge pipe 9. The arc of the arc-shaped flow distributor 4 is arranged along the inner wall of the concentrator body 1, and the outlet 4b is arranged toward the inner wall of the concentrator body 1, so that the syrup can be fully sprayed on the inner wall.
[0022] The interior of the concentrator body 1 is provided with a rotating scraper cylinder 5, and a circle of inclined arc-shaped corrugated plates 6 are provided around the outer wall of the rotating scraper cylinder 5, and the arc-shaped corrugated plates 6 have a plurality of pieces and are evenly spaced. The rotating scraper cylinder 5 is driven to rotate by the hollow rotating shaft 7, and the syrup flowing down the inner wall can be more evenly smeared into a thin film driven by the arc-shaped corrugated plates 6. Compared with the straight scraper of the traditional scraper evaporator, the rotating scraper cylinder 5 of the utility model adopts a cylindrical structure of multiple groups of arc-shaped corrugated plates 6, which can enable the syrup to be continuously and evenly smeared on the wall, further forming a thin film with uniform texture, greatly improving the evaporation efficiency.
[0023] A jacket 2 is provided outside the concentrator body 1 , a steam inlet 10 is provided at the top of the jacket 2 , and a drain outlet 11 is provided at the bottom. Steam enters the jacket 2 from the steam inlet 10 , evaporates and concentrates the syrup, and is discharged from the drain outlet 11 .
[0024] The concentrator body 1 is provided with a thermometer socket 12 for assembling a thermometer to detect the concentrating temperature.
[0025] A discharge port 13 is provided at the bottom of the concentrator body 1 , and the concentrated syrup is collected at the bottom and discharged from the discharge port 13 after concentration is completed.
[0026] The top of the concentrator body 1 is connected to a condenser 14, and the condenser 14 is also connected to a receiving tank 15. The condenser 14 is provided with a refrigerant inlet 14a, a refrigerant outlet 14b, an evaporation solvent inlet 14c, and a cooling material outlet. The refrigerant inlet 14a and the refrigerant outlet 14b are used to transport the refrigerant, the evaporation solvent inlet 14c is connected to the concentrator body 1 through a circulation pipe 16, and the cooling material outlet is connected to the receiving tank 15. The evaporated solvent in the concentrator body 1 enters the condenser 14 through the circulation pipe 16, and is collected in the receiving tank 15 after cooling. The condenser 14 is also provided with a vacuum interface 17, and the vacuum interface 17 is connected to a vacuum pump to extract air and drive the evaporated solvent to enter the condenser 14 for condensation.
[0027] In addition, not shown in the figure, the hollow rotating shaft 7 is also connected to a water supply device, which includes a water pipe rotatably sealed and connected to the bottom of the hollow rotating shaft 7, and the water pipe is connected to an external water source through a water pump, and is used to pump water into the hollow rotating shaft 7. The upper part of the hollow rotating shaft 7 is provided with a spray nozzle 18, and a plurality of spray nozzles 18 are evenly arranged around the hollow rotating shaft 7, and are used to spray water onto the inner wall of the concentrator body 1.
[0028] In this embodiment, the hollow rotating shaft 7 is driven to rotate by a motor 19 .
[0029] The feed port 3 can also be used to add cleaning water into the concentrator body 1 , and cooperate with the injection nozzle 18 to fully clean the concentrator body 1 , and the cleaning water is discharged from the discharge port 13 .
[0030] When the present embodiment is in operation, the whole system is cleaned and dried in advance, and a thermometer is installed in the thermometer socket 12 for standby use. When the operation starts, the vacuum pump connected to the vacuum interface 17 is turned on, the condenser 14 is turned on to deliver the refrigerant, and steam is introduced into the jacket 2. After the thermometer displays the specified temperature, the flavor syrup to be concentrated is fed into the concentrator body 1 from the feed port 3, and the syrup is evenly sprayed on the wall through the arc-shaped flow distributor 4, so that the syrup is initially formed into a film on the wall. When the initially formed film syrup flows down the wall, the motor 19 drives the hollow shaft 7 to rotate, driving the rotating scraper cylinder 5 to rotate, and under the action of the arc-shaped corrugated plate 6, the syrup flowing down the wall can be continuously and evenly smeared on the wall, further forming a uniform film, and performing rapid evaporation and concentration.
[0031] The concentrated flavor syrup is collected at the bottom of the concentrator body 1, and is discharged from the discharge port 13 when the whole batch concentration is completed. During the concentration process, the evaporated solvent in the concentrator body 1 is discharged from the circulation pipe 16, cooled by the condenser 14, and collected in the receiving tank 15.
[0032] After the concentration is completed, a certain amount of washing water is added to the concentrator body 1 through the feed port 3, and the water pump is started at the same time to send the water into the hollow shaft 7 through the water pipe and spray it out through the spray nozzle 18. During cleaning, the hollow shaft 7 drives the rotating scraper tube 5 and the spray nozzle 18 to rotate synchronously, and the rotating scraper tube 5 is used to stir the washing water added from the feed port 3 to clean the concentrator body 1, and the rotating spray nozzle 18 is used to fully rinse the inner wall of the concentrator body 1 to achieve a thorough cleaning effect. The spray angle and water spray flow rate of the spray nozzle 18 can be adjusted. After cleaning, the washing water is discharged from the discharge port 13 and dried for the next use.
[0033] Of course, the above embodiments are only for illustrating the technical concept and features of the utility model, and their purpose is to enable people familiar with the technology to understand the content of the utility model and implement it accordingly, and they cannot be used to limit the protection scope of the utility model. Any modifications made according to the spirit of the main technical solution of the utility model should be included in the protection scope of the utility model.
Claims
1. A flavor syrup production and concentration system, characterized in that: The invention comprises a concentrator body (1) with a jacket (2) on the outside, a feed inlet (3) on the top of the concentrator body (1), the feed inlet (3) being connected to an arc-shaped flow distributor (4), a rotating scraper cylinder (5) being provided inside the concentrator body (1), a circle of inclined arc-shaped corrugated plates (6) being provided around the outer wall of the rotating scraper cylinder (5), the rotating scraper cylinder (5) being driven to rotate by a hollow rotating shaft (7), the syrup is evenly sprayed on the inner wall of the concentrator body (1) from the feed inlet (3) through the arc-shaped flow distributor (4), the rotating scraper cylinder (5) being driven by the hollow rotating shaft (7) to utilize the arc-shaped flow distributor (4) to distribute the syrup to the concentrator body (1), and the rotating scraper cylinder (5) is driven by the hollow rotating shaft (7) to utilize the arc-shaped flow distributor (4) to distribute the syrup to the concentrator body (1). The corrugated plate (6) continuously and evenly spreads the flowing syrup into a thin film; the upper part of the jacket (2) is provided with a steam inlet (10) and the bottom is provided with a sewage outlet (11); the steam is passed into the jacket (2) from the steam inlet (10) to evaporate and concentrate the syrup and then discharged from the sewage outlet (11); the bottom of the concentrator body (1) is provided with a discharge port (13) and the top is connected with a condenser (14); the condenser (14) is also connected with a receiving tank (15); the concentrated syrup is discharged from the discharge port (13), and the evaporated solvent is cooled by the condenser (14) and then collected in the receiving tank (15); The hollow shaft (7) is connected to a water supply device. A spray nozzle (18) is provided on the upper part of the hollow shaft (7). The water supply device can draw water into the hollow shaft (7) and spray it out through the spray nozzle (18). The feed port (3) can be used to add cleaning water into the concentrator body (1). The concentrator body (1) is fully cleaned in cooperation with the spray nozzle (18). The washing water is discharged from the discharge port (13).
2. A flavor syrup production and concentration system according to claim 1, characterized in that: The arc-shaped flow distributor (4) is provided with an intermediate connecting port (4a) in the middle, and the intermediate connecting port (4a) is connected to the feed port (3) through a connecting pipe (8). The arc-shaped flow distributor (4) is provided with a plurality of outlets (4b) on both sides of the intermediate connecting port (4a). The arc of the arc-shaped flow distributor (4) is arranged along the inner wall of the concentrator body (1), and the outlets (4b) are arranged toward the inner wall of the concentrator body (1).
3. A flavor syrup production and concentration system according to claim 2, characterized in that: The outlet (4b) is connected to a conical discharge pipe (9).
4. The flavor syrup production and concentration system according to claim 1, characterized in that: The arc-shaped corrugated plates (6) have a plurality of pieces and are distributed at equal intervals.
5. The flavor syrup production and concentration system according to claim 1, characterized in that: The concentrator body (1) is provided with a thermometer socket (12) for assembling a thermometer to detect the concentrating temperature.
6. The flavor syrup production and concentration system according to claim 1, characterized in that: The condenser (14) is provided with a refrigerant inlet (14a), a refrigerant outlet (14b), an evaporating solvent inlet (14c), and a cooling material outlet. The evaporating solvent inlet (14c) is connected to the concentrator body (1) through a circulation pipe (16), and the cooling material outlet is connected to a receiving tank (15). The condenser (14) is also provided with a vacuum interface (17), and the vacuum interface (17) is connected to a vacuum pump for extracting air.
7. The flavor syrup production and concentration system according to claim 1, characterized in that: The water supply device comprises a water delivery pipe which is rotatably sealed and connected to the bottom of the hollow rotating shaft (7); the water delivery pipe is connected to an external water source via a water pump.
8. The flavor syrup production and concentration system according to claim 1, characterized in that: A plurality of injection nozzles (18) are evenly arranged around the hollow rotating shaft (7), and the hollow rotating shaft (7) is driven to rotate by a motor (19).