Efficient energy-saving airflow drying system for modified starch production

Abstract

The utility model discloses a high-efficiency energy-saving pneumatic drying system for modified starch production, and aims to provide a high-efficiency energy-saving pneumatic drying system for modified starch production, which can improve the starch drying speed, and has the technical scheme that the high-efficiency energy-saving pneumatic drying system for modified starch production comprises a machine body which is also provided with a material inlet, and is characterized in that a buffer box is arranged below the material inlet; two cyclone separators are arranged below the buffer box, a heating coil is further arranged on the outer wall of the buffer box, a material distributing device is arranged between the buffer box and the cyclone separators and comprises a material distributor located below the buffer box, two outlets are formed in the material distributor and connected with the cyclone separators respectively, and the heating coil is arranged on the outer wall of the buffer box. An electromagnetic valve is further arranged on an outlet of the distributor, a material storage box is further arranged below the cyclone separator, and a recycling device is further arranged on the material storage box.

Description

Technical Field

[0001] This utility model relates to the field of starch equipment, specifically to a high-efficiency and energy-saving airflow drying system for modified starch production. Background Technology

[0002] Airflow drying refers to the rapid flow of heated air within a pipe. Wet materials enter the pipe and are carried towards the pipe outlet by the high-speed airflow. During this process, water vapor evaporates simultaneously due to convective heat and mass transfer. Because the material is thoroughly mixed by the high-speed airflow after entering the pipe, a cyclone separator is typically used at the pipe outlet to separate the gas and solid phases. Airflow drying generally takes about one second.

[0003] Currently, Chinese patent CN204944127U discloses a corn modified starch airflow drying device, which includes a hot air furnace, a feeder, a drying pipe, a cyclone separator I, an airlock, a material box, a fan, a cyclone separator II, and a bag collector. One end of the drying pipe is connected to the hot air furnace, and the other end is connected to the cyclone separator I. The feeder is installed on the drying pipe, located on the side where the drying pipe connects to the hot air furnace. The bottom of the cyclone separator I is connected to the airlock. A material box is located below the airlock. The cyclone separator I and the cyclone separator II are connected by a pipe. The bag collector is connected to the cyclone separator II by a pipe.

[0004] Although this type of corn modified starch airflow drying equipment adopts a negative pressure suction structure, which not only has high drying intensity, short drying time, and high thermal efficiency, but also a good working environment and low loss of corn modified starch, it often occupies a large area, which is not conducive to space utilization and has low efficiency. Summary of the Invention

[0005] One objective of this invention is to provide a high-efficiency and energy-saving airflow drying system for modified starch production, which has the advantages of effectively saving space and increasing efficiency.

[0006] The above-mentioned technical objective of this utility model is achieved through the following technical solution:

[0007] A high-efficiency and energy-saving airflow drying system for modified starch production includes a machine body with a feed inlet. Below the feed inlet is a buffer tank, and below the buffer tank are two cyclone separators. A heating coil is installed on the outer wall of the buffer tank. A material distribution device is provided between the buffer tank and the cyclone separators. The material distribution device includes a distributor located below the buffer tank, with two outlets connected to the cyclone separators respectively. A solenoid valve is installed at each outlet of the distributor. Below the cyclone separators is a storage tank, and the storage tank is equipped with a recovery device.

[0008] By adopting the above technical solution, the buffer box can be temporarily used to buffer starch, and then the starch is distributed by the distributor and enters the cyclone separator through two outlets to separate starch and water vapor. Then it enters the storage box for temporary storage. The buffer box is equipped with a heating coil, which can effectively increase the temperature of the buffer box and improve the evaporation efficiency of starch.

[0009] Further feature: The cyclone separator is also equipped with a heater.

[0010] By adopting the above technical solution, the heater installed on the cyclone separator can further increase the evaporation during the separation process, thereby improving the evaporation efficiency.

[0011] Further configuration: The recycling device includes a material extractor located on the storage bin, and a one-way valve is provided between the material extractor and the storage bin. The outlet of the material extractor is connected to a distributor.

[0012] By adopting the above technical solution, the installed material extractor can effectively extract the starch from the storage bin back onto the distributor for re-drying.

[0013] Further feature: The bottom of the storage box is also provided with a discharge port.

[0014] By adopting the above technical solution, it is convenient for users to effectively remove the dried starch.

[0015] Further features: The storage box is also equipped with a sampling port, and the sampling port is also equipped with a threaded sealing cap.

[0016] By adopting the above technical solution, the sampling port can be conveniently used by users to take samples, thereby determining whether the drying degree of starch meets the requirements.

[0017] Further feature: The buffer box is also equipped with a temperature indicator.

[0018] By adopting the above technical solution, the temperature indicator provided allows users to easily monitor changes in the internal temperature.

[0019] In summary, this utility model has the following beneficial effects: it adopts a preheating method and effectively separates starch from water vapor through a cyclone separator, thereby ensuring the dryness of the starch. Furthermore, the parallel connection of multiple cyclone separators can better ensure production efficiency. Attached Figure Description

[0020] The present invention will be further described below with reference to the accompanying drawings.

[0021] Figure 1 This is a schematic diagram of the overall structure of a high-efficiency and energy-saving airflow drying system for modified starch production.

[0022] In the diagram, 1. Machine body; 2. Feed inlet; 3. Buffer tank; 4. Cyclone separator; 5. Heating coil; 6. Distributor; 61. Distributor; 62. Solenoid valve; 63. Storage tank; 7. Recycling device; 71. Pump; 72. Check valve; 8. Heater; 9. Discharge port; 10. Sampling port; 11. Sealing cover; 12. Temperature indicator. Detailed Implementation

[0023] The specific embodiments of this utility model will be further described below with reference to the accompanying drawings.

[0024] The technical solution adopted in this utility model is: a high-efficiency and energy-saving airflow drying system for modified starch production, such as... Figure 1 As shown, the device includes a body 1, a feed inlet 2, a buffer tank 3 below the feed inlet 2, a temperature indicator 12 on the buffer tank 3, two cyclone separators 4 below the buffer tank 3, heaters 8 on the cyclone separators 4, a heating coil 5 on the outer wall of the buffer tank 3, and a material distribution device 6 between the buffer tank 3 and the cyclone separators 4. The material distribution device 6 includes a distributor 61 located below the buffer tank 3, with two outlets connected to the cyclone separators 4 respectively. Meanwhile, a solenoid valve 62 is also provided at the outlet of the distributor 61, and a storage box 63 is also provided below the cyclone separator 4. The bottom of the storage box 63 is also provided with a discharge port 9, and the storage box 63 is also provided with a sampling port 10. The sampling port 10 is also provided with a threaded sealing cap 11. At the same time, a recycling device 7 is also provided on the storage box 63. The recycling device 7 includes a material extractor 71 located on the storage box 63. A one-way valve 72 is also provided between the material extractor 71 and the storage box 63, and the outlet of the material extractor 71 is connected to the distributor 61.

[0025] Its main working principle is as follows: During use, the starch to be dried is added into the buffer tank 3 through the feed port 2. The operator can heat the starch in the buffer tank 3 through the heating coil 5, and the temperature indicator 12 can effectively monitor the internal temperature. After reaching a certain temperature and time, the starch can be divided into two pieces by the distributor 61 and sent to two cyclone separators 4 for drying. At the same time, the cyclone separators 4 can be heated by the heater 8 to increase the temperature and speed up the drying. The dried starch can be stored in the storage tank 63 for sampling and testing. If the dryness is found to be unqualified, the feeder 71 can be started to re-dry until the required dryness is achieved.

[0026] The above are merely preferred embodiments of the present utility model and are not intended to limit the present utility model in any way. Any simple modifications, equivalent changes, and alterations made to the above embodiments based on the technical essence of the present utility model shall fall within the scope of the present utility model's technical solution.

Claims

1. A high-efficiency and energy-saving airflow drying system for modified starch production, comprising a body (1), wherein the body (1) is further provided with a feed inlet (2), characterized in that: Below the feed inlet (2) is a buffer tank (3), below the buffer tank (3) are two cyclone separators (4), and the outer wall of the buffer tank (3) is also provided with a heating coil (5). Between the buffer tank (3) and the cyclone separators (4) is a material distribution device (6). The material distribution device (6) includes a material distributor (61) located below the buffer tank (3). The material distributor (61) has two outlets that are respectively connected to the cyclone separators (4). The outlet of the material distributor (61) is also provided with a solenoid valve (62). Below the cyclone separators (4) is a storage tank (63), and the storage tank (63) is also provided with a recycling device (7).

2. The high-efficiency energy-saving pneumatic drying system for modified starch production according to claim 1, characterized in that: The cyclone separator (4) is also equipped with a heater (8).

3. The high-efficiency and energy-saving pneumatic drying system for modified starch production according to claim 2, characterized in that: The recycling device (7) includes a material extractor (71) located on the storage bin (63), and a one-way valve (72) is provided between the material extractor (71) and the storage bin (63). The outlet of the material extractor (71) is connected to the distributor (61).

4. The high-efficiency and energy-saving pneumatic drying system for modified starch production according to claim 3, characterized in that: The bottom of the storage box (63) is also provided with a discharge port (9).

5. The high-efficiency and energy-saving airflow drying system for modified starch production according to claim 4, characterized in that: The storage box (63) is also provided with a sampling port (10), and the sampling port (10) is also provided with a threaded sealing cap (11).

6. The high-efficiency and energy-saving pneumatic drying system for modified starch production according to claim 5, characterized in that: The buffer box (3) is also equipped with a temperature indicator (12).

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