Scutellaria baicalensis decoction piece production equipment

Through the continuous production of dry cleaning machines, bubble cleaning dryers and tunnel microwave dryers in the production equipment of scutellaria flakes, combined with the dust removal and recycling technology of the spray absorption tower, the high energy consumption and water use of existing equipment are solved. The problem of large quantities has achieved low-cost and environmentally friendly production results.

CN222218258UActive Publication Date: 2024-12-24ZHUCHENG HAOTIAN PHARMA CO LTD
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Patent Information

Application Number
CN202420774970.6
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-04-15
Publication Date
2024-12-24
Estimated Expiration
2034-04-15

AI Technical Summary

Technical Problem

The existing production equipment of Scutellaria baicalensis tablets has high energy consumption and large water consumption, resulting in high production costs.

Method used

A production equipment for scutellaria decoction tablets including dry cleaning machines, bubble cleaning dryers and tunnel microwave dryers was designed. Through continuous production of conveyor belts, combined with bubble cleaning and microwave drying technology, it reduces water consumption and energy consumption, and adopts Spray absorption towers carry out dust removal and recycling to reduce waste of water resources.

Benefits of technology

It has achieved low water consumption and low energy consumption in the production process of Scutellaria baicalensis, which has reduced production costs, and through the use of circulating pumps and filters, it has ensured dust removal effect and water resource conservation and environmentally friendly.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses scutellaria baicalensis decoction piece production equipment, and relates to the technical field of scutellaria baicalensis processing equipment, the inlet end of a dry cleaning machine is provided with a first conveyor belt, the lower part of the outlet of the dry cleaning machine is provided with a second conveyor belt, the upper part of the second conveyor belt is provided with a bubble cleaning dryer, and one end of the feed opening of the second conveyor belt is provided with a third conveyor belt; a tunnel type microwave dryer is arranged on the outer side of the third conveying belt, and a slicing machine is arranged at one end of a discharging port of the third conveying belt. Scutellaria baicalensis roots are conveyed into the dry cleaning machine through the first conveying belt, enter the bubble cleaning and drying machine through the second conveying belt after being cleaned in the dry cleaning machine, are further cleaned under the action of the bubble spray gun, then enter the tunnel type microwave drying machine through the third conveying belt after being blow-dried through the multiple draught fans, and are dried through the drying machine. And evaporating the surfaces of the scutellaria baicalensis roots to dryness, degrading active enzymes in the scutellaria baicalensis roots, and slicing the scutellaria baicalensis roots in a slicing machine. In the whole process, the water consumption is low, the energy consumption is low, the production cost is reduced, and continuous production is realized.
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Description

Technical Field

[0001] The utility model relates to the technical field of scutellaria baicalensis processing equipment, in particular to scutellaria baicalensis slice production equipment. Background Art

[0002] Scutellaria baicalensis is a Chinese medicine. Also known as Camellia Root and Tujin Tea Root, its root is used as medicine. It tastes bitter and is cold in nature. It has the effects of clearing away heat and dampness, purging fire and detoxifying, stopping bleeding, and calming the fetus. It is mainly used to treat febrile diseases, upper respiratory tract infections, lung heat cough, damp-heat jaundice, pneumonia, dysentery, hemoptysis, red eyes, fetal movement disorders, hypertension, carbuncles, furuncles, etc. The clinical antibacterial activity of Scutellaria baicalensis is better than that of Coptis chinensis, and it does not produce drug resistance. It is mostly processed into flakes for sale and use.

[0003] Most of the scutellariae baicalensis slices are prepared by the processing method, and the scutellariae baicalensis root needs to be steamed during the preparation process to kill the activity of the enzyme that degrades baicalin in the scutellariae baicalensis root. This process equipment has high energy consumption and large water consumption, and the production cost is high. Summary of the invention

[0004] The technical problem to be solved by the utility model is: in view of the deficiencies in the prior art, a production device for scutellariae decoction pieces is provided, which has low energy consumption, small water consumption and low production cost.

[0005] In order to solve the above technical problems, the technical solution of the utility model is:

[0006] The production equipment of Scutellaria baicalensis slices includes a dry-cleaning machine, a first conveyor belt is provided at the inlet end of the dry-cleaning machine, a second conveyor belt is provided at the lower part of the outlet of the dry-cleaning machine, a bubble cleaning and drying machine is provided on the upper part of the second conveyor belt, a third conveyor belt is provided at one end of the unloading port of the second conveyor belt, a tunnel-type microwave drying machine is provided on the outer side of the third conveyor belt, and a slicer is provided at one end of the unloading port of the third conveyor belt.

[0007] As an improved technical solution, the bubble cleaning and drying machine and the tunnel type microwave drying machine are respectively connected to the induced draft fan through pipelines.

[0008] As an improved technical solution, the outlet of the induced draft fan is connected to a spray absorption tower through a pipeline, and an emptying pipeline is provided on the top of the spray absorption tower.

[0009] As an improved technical solution, the bottom of the spray absorption tower is connected to a circulation pump through a pipeline, and the outlet of the circulation pump is connected to the spray absorption tower and the spray liquid temporary storage tank through pipelines respectively.

[0010] As an improved technical solution, a first filter is provided between the circulation pump and the spray liquid temporary storage tank, the outlet of the spray liquid temporary storage tank is connected to a water replenishment pump through a pipeline, and the outlet of the water replenishment pump is connected to the spray absorption tower and the bubble cleaning and drying machine through pipelines respectively.

[0011] As an improved technical solution, the spray absorption tower is provided with a process water replenishment pipeline.

[0012] As a preferred technical solution, a second filter is provided on the exhaust pipe of the spray absorption tower, and the second filter is an activated carbon filter.

[0013] As a preferred technical solution, a first shut-off valve is provided on the process water replenishment pipeline, a second shut-off valve is provided on the pipeline between the circulating pump and the spray liquid temporary storage tank, a liquid level sensor is provided in the spray absorption tower, and the first shut-off valve, the second shut-off valve and the liquid level sensor are interlocked to a control system.

[0014] As a preferred technical solution, the spray absorption tower is provided with a sewage discharge pipe.

[0015] Due to the adoption of the above technical solution, the beneficial effects of the utility model are:

[0016] The utility model provides a production equipment for Radix Scutellariae Radix slices, including a dry cleaning machine, a first conveyor belt is provided at the inlet end of the dry cleaning machine, a second conveyor belt is provided at the lower part of the outlet of the dry cleaning machine, a bubble cleaning and drying machine is provided at the upper part of the second conveyor belt, a third conveyor belt is provided at one end of the feeding port of the second conveyor belt, a tunnel type microwave drying machine is provided outside the third conveyor belt, and a slicer is provided at one end of the feeding port of the third conveyor belt. The root of Radix Scutellariae Radix enters the dry cleaning machine through the conveyance of the first conveyor belt, enters the bubble cleaning and drying machine through the second conveyor belt after being cleaned in the dry cleaning machine, is further cleaned under the action of a water bubble spray gun, and then enters the tunnel type microwave drying machine through the third conveyor belt after being blown dry by a multi-channel fan, evaporates the surface of the root of Radix Scutellariae Radix and degrades the active enzyme inside the root of Radix Scutellariae Radix, and then enters the slicer for slicing. The whole process uses less water and has low energy consumption, reduces production costs, and realizes continuous production.

[0017] The bubble cleaning and drying machine and the tunnel type microwave drying machine of the utility model are respectively connected to the induced draft fan through pipelines, the outlet of the induced draft fan is connected to the spray absorption tower through pipelines, and the top of the spray absorption tower is provided with an emptying pipeline. The dust-containing gas generated during the dry cleaning and microwave drying process is collected and sent to the spray absorption tower for dust removal, so as to avoid the dust-containing air being directly discharged into the air to cause damage to the environment.

[0018] The bottom of the spray absorption tower is connected to a circulation pump through a pipeline, and the outlet of the circulation pump is connected to the spray absorption tower and the spray liquid temporary storage tank through pipelines. The circulation pump can circulate and spray the absorption liquid in the spray absorption tower, and on the other hand, it can discharge and replace the dust-containing absorption liquid in the spray absorption tower to avoid excessive dust content in the absorption liquid in the spray absorption tower affecting the dust removal effect.

[0019] A first filter is provided between the circulation pump and the spray liquid temporary storage tank, the outlet of the spray liquid temporary storage tank is connected to a water replenishment pump through a pipeline, and the outlet of the water replenishment pump is connected to the spray absorption tower and the bubble cleaning and drying machine through pipelines. The dust-containing absorption liquid is purified by the first filter, and the purified water obtained is stored in the spray liquid temporary storage tank and used to replenish water for the spray absorption tower and the bubble spray gun of the bubble cleaning and drying machine, thereby avoiding energy waste and saving costs.

[0020] The spray absorption tower is provided with a process water replenishment pipeline to replenish the liquid level of the spray absorption tower.

[0021] The exhaust pipe of the spray absorption tower is provided with a second filter, which is an activated carbon filter. The gas after spray absorption is filtered again, and the gas discharged into the air has higher purity and is more environmentally friendly.

[0022] A first shut-off valve is provided on the process water replenishment pipeline, a second shut-off valve is provided on the pipeline between the circulation pump and the spray liquid temporary storage tank, a liquid level sensor is provided in the spray absorption tower, and the first shut-off valve, the second shut-off valve and the liquid level sensor are interlocked to a control system. The control system controls the opening and closing of the first shut-off valve and the second shut-off valve according to the value of the liquid level sensor to maintain the balance of the liquid level in the spray absorption tower.

[0023] The spray absorption tower is provided with a sewage pipe, which can better empty and repair the spray absorption tower. BRIEF DESCRIPTION OF THE DRAWINGS

[0024] The utility model is further described below in conjunction with the accompanying drawings and embodiments.

[0025] Figure 1 It is a structural schematic diagram of an embodiment of the utility model;

[0026] Among them: 1. Dry cleaning machine; 2. First conveyor belt; 3. Second conveyor belt; 4. Bubble cleaning and drying machine; 5. Third conveyor belt; 6. Tunnel type microwave drying machine; 7. Slicer; 8. Spray absorption tower; 9. Emptying pipe; 10. Circulation pump; 11. Spray liquid temporary storage tank; 12. First filter; 13. Make-up water pump; 14. Process water make-up water pipeline; 15. Second filter; 16. First shut-off valve; 17. Second shut-off valve; 18. Liquid level sensor; 19. Sewage pipe; 20. induced draft fan. DETAILED DESCRIPTION

[0027] The present invention is further described below in conjunction with the accompanying drawings and embodiments.

[0028] like Figure 1As shown, a production equipment for Radix Scutellariae Radix slices includes a dry cleaning machine 1, a first conveyor belt 2 is provided at the inlet end of the dry cleaning machine 1, a second conveyor belt 3 is provided at the lower part of the outlet of the dry cleaning machine 1, a bubble cleaning and drying machine 4 is provided at the upper part of the second conveyor belt 3, a third conveyor belt 5 is provided at one end of the feeding port of the second conveyor belt 3, a tunnel type microwave drying machine 6 is provided outside the third conveyor belt 5, and a slicer 7 is provided at one end of the feeding port of the third conveyor belt 5. The radix scutellariae Radix enters the dry cleaning machine 1 through the conveyance of the first conveyor belt 2, enters the bubble cleaning and drying machine 4 through the second conveyor belt 3 after being cleaned in the dry cleaning machine 1, is further cleaned under the action of the bubble spray gun in the bubble cleaning and drying machine 4, and then enters the tunnel type microwave drying machine 6 through the third conveyor belt 5 after being blown dry by the multi-channel fan in the bubble cleaning and drying machine 4, evaporates the surface of the radix scutellariae Radix and degrades the active enzyme inside the radix scutellariae Radix, and then enters the slicer 7 for slicing operation. The whole process uses less water and has low energy consumption, which reduces production costs and realizes continuous production.

[0029] The bubble cleaning and drying machine 4 and the tunnel type microwave drying machine 6 are respectively connected to the induced draft fan 20 through pipelines, and the outlet of the induced draft fan 20 is connected to the spray absorption tower 8 through pipelines. The top of the spray absorption tower 8 is provided with an emptying pipeline 9. The dust-containing gas generated during the dry cleaning and microwave drying process is collected and sent to the spray absorption tower 8 for dust removal, so as to avoid the dust-containing air being directly discharged into the air to cause damage to the environment.

[0030] The bottom of the spray absorption tower 8 is connected to a circulation pump 10 through a pipeline, and the outlet of the circulation pump 10 is respectively connected to the spray absorption tower 8 and the spray liquid temporary storage tank 11 through pipelines. The circulation pump 10 circulates and sprays the absorption liquid in the spray absorption tower 8 on the one hand, and on the other hand, it can discharge and replace the dust-containing absorption liquid in the spray absorption tower 8 to avoid excessive dust content in the absorption liquid in the spray absorption tower 8 affecting the dust removal effect.

[0031] A first filter 12 is provided between the circulation pump 10 and the spray liquid temporary storage tank 11, and the outlet of the spray liquid temporary storage tank 11 is connected to a water replenishment pump 13 through a pipeline, and the outlet of the water replenishment pump 13 is respectively connected to the spray absorption tower 8 and the bubble cleaning and drying machine 4 through pipelines. The dust-containing absorption liquid is purified by the first filter 12, and the purified water obtained is stored in the spray liquid temporary storage tank 11, and is used to replenish water for the spray absorption tower 8 and water for the bubble spray gun of the bubble cleaning and drying machine 4, thereby avoiding energy waste and saving costs.

[0032] The spray absorption tower 8 is provided with a process water replenishment pipeline 14 to replenish the liquid level of the spray absorption tower 8 .

[0033] The exhaust pipe 9 of the spray absorption tower 8 is provided with a second filter 15, which is an activated carbon filter. The gas after spray absorption is filtered again, and the gas discharged into the air has higher purity and is more environmentally friendly.

[0034] The process water replenishment pipeline 14 is provided with a first shut-off valve 16, the pipeline between the circulation pump 10 and the spray liquid temporary storage tank 11 is provided with a second shut-off valve 17, and the spray absorption tower 8 is provided with a liquid level sensor 18, and the first shut-off valve 16, the second shut-off valve 17 and the liquid level sensor 18 are interlocked to the control system. The control system controls the opening and closing of the first shut-off valve 16 and the second shut-off valve 17 according to the value of the liquid level sensor 18 to maintain the balance of the liquid level in the spray absorption tower 8.

[0035] The spray absorption tower 8 is provided with a sewage pipe 19, which can better empty and repair the spray absorption tower 8.

[0036] It should be understood that these embodiments are only used to illustrate the present invention and are not used to limit the scope of the present invention. In addition, it should be understood that after reading the content taught by the present invention, those skilled in the art can make various changes or modifications to the present invention, and these equivalent forms also fall within the scope defined by the claims attached to this application.

Claims

1. Scutellaria baicalensis slice production equipment, characterized by: It includes a dry cleaning machine, wherein a first conveyor belt is provided at the inlet end of the dry cleaning machine, a second conveyor belt is provided at the lower part of the outlet of the dry cleaning machine, a bubble cleaning and drying machine is provided on the upper part of the second conveyor belt, a third conveyor belt is provided at one end of the unloading port of the second conveyor belt, a tunnel-type microwave drying machine is provided on the outer side of the third conveyor belt, and a slicer is provided at one end of the unloading port of the third conveyor belt.

2. The equipment for producing Radix Scutellariae Radix slices according to claim 1, characterized in that: The bubble cleaning and drying machine and the tunnel type microwave drying machine are respectively connected to the induced draft fan through pipelines.

3. The equipment for producing Radix Scutellariae Radix slices according to claim 2, characterized in that: The outlet of the induced draft fan is connected to a spray absorption tower through a pipeline, and an emptying pipeline is arranged on the top of the spray absorption tower.

4. The equipment for producing Radix Scutellariae Radix slices according to claim 3, characterized in that: The bottom of the spray absorption tower is connected to a circulation pump through a pipeline, and the outlet of the circulation pump is connected to the spray absorption tower and the spray liquid temporary storage tank through pipelines respectively.

5. The equipment for producing scutellariae decoction pieces according to claim 4, characterized in that: A first filter is provided between the circulation pump and the spray liquid temporary storage tank, the outlet of the spray liquid temporary storage tank is connected to a water replenishment pump through a pipeline, and the outlet of the water replenishment pump is connected to the spray absorption tower and the bubble cleaning and drying machine through pipelines.

6. The equipment for producing scutellariae decoction pieces according to claim 4, characterized in that: The spray absorption tower is provided with a process water replenishment pipeline.

7. The equipment for producing Radix Scutellariae Radix slices according to claim 3, characterized in that: A second filter is provided on the exhaust pipe of the spray absorption tower, and the second filter is an activated carbon filter.

8. The equipment for producing scutellariae baicalensis slices according to claim 6, characterized in that: A first shut-off valve is provided on the process water replenishment pipeline, a second shut-off valve is provided on the pipeline between the circulation pump and the spray liquid temporary storage tank, a liquid level sensor is provided in the spray absorption tower, and the first shut-off valve, the second shut-off valve and the liquid level sensor are interlocked to a control system.

9. The equipment for producing Radix Scutellariae Radix slices according to claim 3, characterized in that: The spray absorption tower is provided with a sewage discharge pipeline.