Processing device for colistin sulfate soluble powder for poultry and livestock
By installing a circulating drying system with guide tubes and baffles inside the drying tank, the problems of uneven contact between wet particles and drying airflow and the adjustment of wet particle quantity are solved, thus achieving uniform drying and efficient production of colistin sulfate soluble powder for poultry and livestock.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- SHANDONG XINHUIRUI BIOTECHNOLOGY CO LTD
- Filing Date
- 2025-09-12
- Publication Date
- 2026-07-31
AI Technical Summary
In the existing technology, the wet particles of colistin sulfate soluble powder for poultry and livestock do not come into uniform contact with the drying airflow during the drying process, and the amount of wet particles participating in the drying per unit time cannot be adjusted according to the amount of wet particles stored, resulting in low drying efficiency.
The drying tank is vertically arranged and has a fixed plate inside that divides the drying area and the discharge area. The guide tube and baffle form a circulating drying system. Drying air is injected through the blow holes to achieve the circulating drying of wet particles. The amount of wet particles can be adjusted by adjusting the distance between the guide tube and the valve plate. The discharge is controlled by the drive motor through the fan-shaped closed plate.
This achieves uniform contact between wet particles and the drying airflow, improving drying efficiency and uniformity, and ensuring the continuity and high efficiency of the drying process.
Smart Images

Figure CN224580652U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of drying equipment technology, specifically to a processing device for colistin sulfate soluble powder for poultry and livestock. Background Technology
[0002] Colistin sulfate soluble powder for poultry and livestock is widely used in livestock and poultry farming, showing significant effects in preventing and treating intestinal diseases and promoting growth and development. To comply with veterinary drug production standards, ensure consistent and stable product quality, and meet market demand for efficient and high-quality products, it is essential to design an integrated and intelligent processing device. This device encompasses core processes such as crushing, mixing, granulation, drying, and packaging to achieve continuous and automated production. After wet granulation, the wet granules require rapid drying and precise moisture control.
[0003] The prior art discloses a patent with publication number CN106902083A, which includes 10% colistin sulfate, a drug synergist, chlorhexidine acetate, dipropylglutamine, and an active enzyme. The colistin sulfate soluble powder used in exported poultry is made by mixing 10% colistin sulfate, a drug synergist, chlorhexidine acetate, dipropylglutamine, and an active enzyme. This colistin sulfate soluble powder used in exported poultry has a therapeutic effect on air sacculitis caused by Escherichia coli (G-) and pneumococcus (G+), as well as pericarditis and perihepatitis caused by Escherichia coli infection, duck serositis, oviductitis, and peritonitis in laying hens.
[0004] The shortcomings of existing technology have gradually become apparent with use, mainly in the following aspects:
[0005] First, during the production process of colistin sulfate soluble powder for poultry and livestock, when the wet granules are dried, the wet granules cannot come into uniform contact with the drying airflow, which affects the uniformity of drying the wet granules.
[0006] Secondly, in existing drying devices, the contact amount between the drying airflow and the wet particles is fixed, making it impossible to adjust the amount of wet particles participating in drying per unit time according to different wet particle storage conditions, thus reducing drying efficiency.
[0007] In conclusion, the existing technology obviously has inconveniences and defects in practical use, so it is necessary to improve it. Utility Model Content
[0008] To address the shortcomings of existing technologies, this utility model provides a processing device for soluble colistin sulfate powder for poultry and livestock, which solves the problems in traditional technologies where wet particles cannot be uniformly contacted with the drying airflow during drying, and the inability to adjust the amount of wet particles participating in drying per unit time according to different wet particle storage amounts, thus reducing drying efficiency.
[0009] To achieve the above objectives, this utility model provides the following technical solution:
[0010] A processing device for soluble colistin sulfate powder for poultry and livestock includes a vertically arranged drying tank. A fixed plate is horizontally fixed inside the drying tank, and the fixed plate divides the inner cavity of the drying tank into a drying area and a discharge area from top to bottom. The fixed plate is equipped with a control structure for switching the drying area and the discharge area on and off.
[0011] The drying area is provided with a guide tube that slides vertically, and there is a return flow interval between the lower end of the guide tube and the fixed plate. The control structure is provided with an air distribution structure that blows air into the guide tube.
[0012] As an optimized solution, a baffle is fixedly installed above the guide tube in the drying area, and an air passage is provided between the outer edge of the baffle and the inner wall of the drying tank.
[0013] As an optimized solution, the baffle is arranged in an arc-shaped cover, with the open end of the baffle facing downwards.
[0014] As an optimized solution, a feed cylinder is fixedly attached to the outer wall of the drying tank at an angle downwards, and the outlet end of the feed cylinder is connected to the drying area.
[0015] As an optimized solution, a support rod is horizontally fixed to the inner wall of the drying tank, and a support sleeve is fixed between the opposite ends of the two support rods. The guide cylinder is threaded into the support sleeve.
[0016] As an optimized solution, the control structure includes a valve disc rotatably mounted on the fixed disk, the fixed disk having a plurality of fan-shaped material discharge holes around its center, and the valve disc having a plurality of fan-shaped closing plates that match the fan-shaped material discharge holes.
[0017] As an optimized solution, the air distribution structure includes a plurality of spray holes evenly spaced at the center of the valve disc, the spray holes connecting the drying area and the discharge area.
[0018] As an optimized solution, a discharge cylinder that communicates with the discharge area is obliquely fixed to the outer wall of the drying tank, and the inner bottom surface of the drying tank is obliquely arranged, with the discharge cylinder close to the lower side of the bottom surface.
[0019] As an optimized solution, a drying air inlet cylinder that connects to the discharge area is fixedly connected to the outer wall of the drying tank.
[0020] As an optimized solution, a locking sleeve is threaded onto the guide tube, and the lower surface of the locking sleeve abuts against the upper surface of the support sleeve.
[0021] As an optimized solution, the inner holes of the support sleeve and the locking sleeve are respectively provided with internal threads, and the outer wall of the guide tube is provided with an external thread section that matches the internal threads.
[0022] As an optimized solution, the upper surface of the baffle is fixed to the inner top surface of the drying tank by parallel hanging rods.
[0023] As an optimized solution, an exhaust pipe is fixedly connected to the top of the drying tank, and the exhaust pipe is connected to a bag filter dust collector.
[0024] As an optimized solution, the area of the sector-shaped closing plate is larger than the area of the sector-shaped material discharge hole.
[0025] As an optimized solution, a drive motor is fixedly connected to the outer bottom surface of the drying tank, and the output shaft of the drive motor is fixedly connected to the center position of the lower surface of the valve disc.
[0026] As an optimized solution, the fixed disk is provided with a clearance hole to avoid the output shaft of the drive motor.
[0027] As an optimized solution, an operator's manhole is fixedly connected to the outer wall of the drying tank above the support rod.
[0028] Compared with the prior art, the beneficial effects of this utility model are:
[0029] High-pressure drying air is introduced through the dry air inlet cylinder, and wet particles are introduced through the feed cylinder. The wet particles pass through the reflux interval and accumulate above the fixed plate. Due to the introduction of drying air, the drying air is sprayed into the guide cylinder through the blow holes. The material rises with the airflow until it hits the baffle and falls in all directions. Then it passes through the reflux interval and accumulates above the fixed plate, realizing the circulation of the contact spray drying airflow. This achieves the circulation drying of wet particles, increases the mobility of wet particles, and increases the drying uniformity with the drying airflow.
[0030] By rotating the guide tube, the distance between its lower end and the valve disc can be adjusted, the inlet height of the reflux interval can be adjusted, and the amount of wet particles entering the nozzle can be adjusted. This allows for the adjustment of the amount of wet particles participating in drying per unit time, thereby improving drying efficiency.
[0031] After the wet granules are dried, the drive motor rotates the valve disc, and the area between the two fan-shaped closed plates is aligned with the fan-shaped discharge hole, so that the dried granules fall into the discharge area. The dried material is then discharged by opening the discharge cylinder, which is convenient and quick. Attached Figure Description
[0032] To more clearly illustrate the specific embodiments of this utility model or the technical solutions in the prior art, the drawings used in the description of the specific embodiments or the prior art will be briefly introduced below. In all the drawings, similar elements or parts are generally identified by similar reference numerals. In the drawings, the elements or parts are not necessarily drawn to scale.
[0033] Figure 1 This is a schematic diagram of the structure of this utility model;
[0034] Figure 2 This is a schematic diagram of the structure of the fixing disc of this utility model;
[0035] Figure 3 This is a schematic diagram of the valve disc of this utility model.
[0036] In the diagram: 1-Drying tank; 2-Fixed plate; 3-Drying area; 4-Discharge area; 5-Guide cylinder; 6-Support rod; 7-Support sleeve; 8-Locking sleeve; 9-Manhole; 10-Baffle; 11-Hanging rod; 12-Exhaust pipe; 13-Feed cylinder; 14-Discharge cylinder; 15-Drying air inlet cylinder; 16-Recirculation interval; 17-Puffing hole; 18-Fan-shaped discharge hole; 19-Valve disc; 20-Fan-shaped sealing plate; 21-Driver. Detailed Implementation
[0037] The embodiments of the present invention will now be described in detail with reference to the accompanying drawings. These embodiments are merely illustrative of the present invention and should not be construed as limiting the scope of protection of the present invention.
[0038] like Figures 1 to 3 As shown, the device includes a vertically arranged drying tank 1, with a horizontally fixed plate 2 inside the drying tank 1. The fixed plate 2 divides the inner cavity of the drying tank 1 into a drying area 3 and a discharge area 4 from top to bottom. The fixed plate 2 is equipped with a control structure to switch the drying area 3 and the discharge area 4 on and off.
[0039] The drying area 3 is equipped with a guide tube 5 that slides vertically. The lower end of the guide tube 5 is provided with a return interval 16 between it and the fixed plate 2. The control structure is provided with an air distribution structure that blows air into the guide tube 5.
[0040] A baffle 10 is fixedly installed above the guide tube 5 in the drying zone 3, and an air passage is provided between the outer edge of the baffle 10 and the inner wall of the drying tank 1.
[0041] The baffle 10 is set in an arc shape, with the open end of the baffle 10 facing downwards.
[0042] A feed cylinder 13 is fixedly attached to the outer wall of the drying tank 1 at an angle downwards, and the outlet end of the feed cylinder 13 is connected to the drying area 3.
[0043] A support rod 6 is horizontally fixed to the inner wall of the drying tank 1, and a support sleeve 7 is fixed between the opposite ends of the two support rods 6. The guide tube 5 is threaded into the support sleeve 7.
[0044] The control structure includes a valve disc 19 rotatably mounted on a fixed disk 2. The fixed disk 2 has several fan-shaped material discharge holes 18 arranged around its center. The valve disc 19 has several fan-shaped closing plates 20 that match the fan-shaped material discharge holes 18.
[0045] The air distribution structure includes several spray holes 17 evenly distributed at the center of the valve disc 19, and the spray holes 17 connect the drying area 3 and the discharge area 4.
[0046] A discharge cylinder 14, which connects to the discharge area 4, is obliquely fixed to the outer wall of the drying tank 1. The inner bottom surface of the drying tank 1 is obliquely arranged, and the discharge cylinder 14 is close to the lower side of the bottom surface.
[0047] A drying air inlet 15, which connects to the discharge area 4, is fixedly attached to the outer wall of the drying tank 1. The drying air inlet 15 is connected to the drying airflow through an air purification device and high-pressure air delivery is achieved through a centrifugal fan.
[0048] A locking sleeve 8 is threaded onto the guide tube 5, and the lower surface of the locking sleeve 8 abuts against the upper surface of the support sleeve 7.
[0049] The inner holes of the support sleeve 7 and the locking sleeve 8 are respectively provided with internal threads, and the outer wall of the guide tube 5 is provided with an external thread section that matches the internal threads.
[0050] The upper surface of the baffle 10 is fixed to the inner top surface of the drying tank 1 by parallel hanging rods 11.
[0051] An exhaust pipe 12 is fixedly connected to the top of the drying tank 1, and the exhaust pipe 12 is connected to a bag filter dust collector.
[0052] The area of the sector-shaped closing plate 20 is larger than the area of the sector-shaped discharge hole 18.
[0053] A drive motor 21 is fixedly connected to the outer bottom surface of the drying tank 1, and the output shaft of the drive motor 21 is fixedly connected to the center position of the lower surface of the valve disc 19.
[0054] A stepper motor or a servo motor can be connected to the drive motor 21, so that the number of rotation steps of the stepper motor or servo motor can be controlled by sending pulse signals through the controller, thereby precisely controlling the rotation angle (each pulse corresponds to a fixed angle increment).
[0055] The fixed plate 2 has a clearance hole for the output shaft of the drive motor 21.
[0056] An operator manhole 9 is fixed to the outer wall of the drying tank 1 above the support rod 6. Opening the operator manhole 9 makes it easy to adjust the height of the guide tube 5.
[0057] A jacket can be installed on the outer wall of the drying tank 1 to achieve temperature control.
[0058] The working principle of this device is as follows:
[0059] High-pressure drying air is introduced through the dry air inlet cylinder 15, and wet particles are introduced through the feed cylinder 13. The wet particles pass through the return interval 16 and accumulate above the fixed plate 2. Due to the introduction of drying air, the drying air is sprayed into the guide cylinder 5 through the blow hole 17. The material will rise with the airflow until it hits the baffle 10 and then falls in all directions. Then it passes through the return interval 16 and gathers above the fixed plate 2, realizing the circulating contact spray drying airflow, realizing the circulating drying of wet particles, increasing the mobility of wet particles, and increasing the drying uniformity with the drying airflow.
[0060] By rotating the guide tube 5, the distance between its lower end and the valve disc 19 can be adjusted, and the inlet height of the return interval 16 can be adjusted, thereby adjusting the amount of wet particles entering above the spray hole 17. This allows for the adjustment of the amount of wet particles participating in drying per unit time, thus improving drying efficiency.
[0061] After the wet granules are dried, the drive motor 21 drives the valve disc 19 to rotate. The area between the two fan-shaped closed plates 20 is aligned with the fan-shaped discharge hole 18, so that the dried granules fall into the discharge area 4. The dried material is discharged by opening the discharge cylinder 14, which is convenient and quick.
[0062] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of this utility model, and not to limit it. Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that modifications can still be made to the technical solutions described in the foregoing embodiments, or equivalent substitutions can be made to some or all of the technical features. Such modifications or substitutions do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of this utility model, and they should all be covered within the scope of the claims and specification of this utility model.
Claims
1. Apparatus for processing colistin sulfate soluble powder for poultry and livestock, characterized by: The equipment includes a vertically arranged drying tank (1), a horizontally fixed plate (2) is fixed inside the drying tank (1), and the inner cavity of the drying tank (1) is divided from top to bottom into a drying area (3) and a discharge area (4) by the fixed plate (2). The fixed plate (2) is provided with a control structure to open and close the drying area (3) and the discharge area (4). The drying area (3) is provided with a guide tube (5) that slides vertically. A return flow interval (16) is provided between the lower end of the guide tube (5) and the fixed plate (2). The control structure is provided with an air distribution structure that blows air into the guide tube (5).
2. The process for preparing a soluble powder of colistin for poultry and livestock according to claim 1, characterized in that: A baffle (10) is fixedly installed above the guide tube (5) in the drying area (3), and an air passage is provided between the outer edge of the baffle (10) and the inner wall of the drying tank (1).
3. The apparatus for processing soluble colistin sulfate powder for poultry and livestock according to claim 2, characterized in that: The baffle (10) is provided in an arc shape, with the opening end of the baffle (10) facing downwards.
4. The process for preparing a soluble powder of colistin for poultry and livestock according to claim 1, characterized in that: A support rod (6) is horizontally fixed to the inner wall of the drying tank (1), and a support sleeve (7) is fixed between the opposite ends of the two support rods (6). The guide tube (5) is threaded into the support sleeve (7).
5. The apparatus for processing soluble colistin sulfate for poultry as claimed in claim 1 wherein: The control structure includes a valve disc (19) rotatably mounted on the fixed disc (2). The fixed disc (2) has a plurality of fan-shaped material dropping holes (18) around its center. The valve disc (19) has a plurality of fan-shaped closing plates (20) that match the fan-shaped material dropping holes (18).
6. The apparatus for processing soluble sulfisoxazole powder for poultry of claim 5, wherein: The air distribution structure includes a number of spray holes (17) evenly distributed at the center of the valve disc (19), and the spray holes (17) connect the drying area (3) and the discharge area (4).
7. The process for preparing a soluble sulfisoxazole powder for poultry as claimed in claim 1 wherein: The outer wall of the drying tank (1) is inclinedly fixed with a discharge cylinder (14) that connects to the discharge area (4). The inner bottom surface of the drying tank (1) is inclined, and the discharge cylinder (14) is close to the lower side of the bottom surface.
8. The process for preparing a soluble powder of colistin for poultry animals according to claim 1, characterized in that: A drying air inlet cylinder (15) that connects to the discharge area (4) is fixedly connected to the outer wall of the drying tank (1).
9. The process for preparing a soluble powder of colistin for poultry and livestock according to claim 4, characterized in that: The guide tube (5) is threaded with a locking sleeve (8), and the lower surface of the locking sleeve (8) abuts against the upper surface of the support sleeve (7).
10. The process for preparing a soluble powder of colistin for poultry and livestock according to claim 2, characterized in that: The upper surface of the baffle (10) is fixed to the inner top surface of the drying tank (1) by parallel hanging rods (11).