A sodium butyrate dust recovery device
By combining large-pore and small-pore filter elements and employing a backflushing cleaning structure, the problem of filter element clogging in dust recovery devices is solved, achieving efficient filtration and automatic dust removal, thereby improving production stability and economy.
Patent Information
- Application Number
- CN202522021269.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-09-19
- Publication Date
- 2026-08-25
- Estimated Expiration
- 2035-09-19
AI Technical Summary
Existing dust recovery devices are prone to filter clogging when processing high-concentration, fine-particle sodium butyrate dust, leading to decreased filtration efficiency, increased system resistance, and impact on production continuity and stability.
It uses a combination of large-pore and small-pore filter elements for filtration, and is equipped with a backflushing cleaning structure to achieve graded filtration and automatic dust removal, preventing filter element clogging.
It improves filtration efficiency, extends filter life, reduces maintenance frequency and operating costs, and ensures production continuity and stability.
Smart Images

Figure CN224672341U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of sodium butyrate recovery technology, specifically to a sodium butyrate dust recovery device. Background Technology
[0002] Sodium butyrate, as an important chemical product and feed additive, easily generates a large amount of dust during its production, processing, and packaging. This dust not only wastes raw materials and results in economic losses, but also poses an explosion risk, seriously threatening the production environment and the health of operators. Therefore, the efficient recovery and treatment of sodium butyrate dust is of significant economic and safety importance.
[0003] Currently, most common dust recovery devices use a single filtration unit, such as a single-stage filter cartridge for dust collection. While this structure is simple, the filter cartridge is prone to rapid clogging when handling high concentrations of fine-particle sodium butyrate dust. This leads to a sharp increase in system resistance, a decrease in filtration efficiency, and frequent shutdowns for cleaning or filter cartridge replacement, severely impacting the continuity and stability of production.
[0004] Therefore, we propose a sodium butyrate dust recovery device. Utility Model Content
[0005] (a) Technical problems to be solved
[0006] To address the shortcomings of existing technologies, this utility model provides a sodium butyrate dust recovery device. It achieves efficient graded filtration by combining large-pore and small-pore filter elements, and automatically cleans dust using a backflushing cleaning structure. This improves filtration efficiency, extends filter element life, and reduces maintenance frequency and operating costs, effectively solving the problems in the background technology.
[0007] (II) Technical Solution
[0008] To achieve the above objectives, the technical solution adopted by this utility model is as follows: a sodium butyrate dust recovery device, comprising a purification box, an exhaust gas inlet installed in the middle of the left outer surface of the purification box, a back-flushing cleaning structure installed in the lower left side of the purification box, the back-flushing cleaning structure comprising a back-flushing main pipe, a first back-flushing branch pipe and a second back-flushing branch pipe, and back-flushing nozzles evenly distributed on the upper outer walls of the first back-flushing branch pipe and the second back-flushing branch pipe, support feet fixedly installed at the four corners of the lower outer surface of the purification box, a maintenance plate installed at the bottom of the front outer surface of the purification box by bolts, and an annular rubber ring provided between the back of the maintenance plate and the front outer surface of the purification box, and an exhaust fan fixedly installed at the right end of the upper outer surface of the purification box. The pump has a vertical partition fixedly installed in the middle of the inner cavity of the purification chamber. A horizontal partition is fixedly installed on the upper left side of the vertical partition. A large-diameter filter element is bolted to the lower end of the horizontal partition. A small-diameter filter element is bolted to the upper right side of the inner cavity of the purification chamber. Both the large-diameter and small-diameter filter elements include a filter cartridge, a connecting flange, and a sealing plate. A through hole is opened in the middle of the lower outer surface of the sealing plate, and the through hole extends to the middle of the upper outer surface of the sealing plate. An arc-shaped air guide pipe is fixedly installed between the middle of the horizontal partition and the upper part of the vertical partition. One end of the arc-shaped air guide pipe extends to the lower outer surface of the horizontal partition, and the other end extends to the upper part of the right outer surface of the vertical partition.
[0009] Preferably, the lower end of the arc-shaped air guide tube is connected to the upper part of the inner cavity of the filter cartridge in the large-pore filter element; the air extraction tube in the air pump extends to the upper part of the inner cavity of the filter cartridge in the small-pore filter element.
[0010] Preferably, the connecting flange is fixed to the outer wall of the upper part of the filter cartridge, and the sealing plate is fixed to the bottom of the inner cavity of the filter cartridge.
[0011] Preferably, the pore size of the filter cartridge in the large-pore filter element is - micrometer; the pore size of the filter cartridge in the small-pore filter element is - micrometer.
[0012] Preferably, the backflush main pipe is located at the bottom of the inner cavity of the purification chamber and penetrates the lower part of the vertical partition; the left end of the backflush main pipe penetrates the shell of the purification chamber and extends to its left side outside.
[0013] Preferably, the first backflush branch pipe and the second backflush branch pipe are both fixedly connected to the upper end of the backflush main pipe; the second backflush branch pipe passes through the through hole and its outer wall is fixedly connected to the sealing plate; the backflush nozzle is located inside the filter cartridge.
[0014] (III) Beneficial Effects
[0015] Compared with the prior art, this utility model provides a sodium butyrate dust recovery device, which has the following beneficial effects:
[0016] 1. This sodium butyrate dust recovery device achieves graded filtration by setting up large-pore filter elements and small-pore filter elements. The dust-laden gas first undergoes primary filtration through the large-pore filter element, intercepting most of the larger dust particles, reducing the filtration load of the subsequent small-pore filter element, effectively avoiding rapid clogging of the small-pore filter element, thereby improving the overall filtration efficiency and processing capacity of the device.
[0017] 2. This sodium butyrate dust recovery device integrates a back-flushing cleaning structure consisting of a back-flushing main pipe, back-flushing branch pipes, and back-flushing nozzles to perform high-pressure gas back-flushing cleaning of large-pore and small-pore filter elements; the back-flushing airflow acts directly on the inside of the filter cartridge, which can effectively remove the dust attached to the filter material and reduce the frequency of downtime maintenance due to filter element clogging. Attached Figure Description
[0018] Figure 1 This is a schematic diagram of the overall structure of a sodium butyrate dust recovery device according to the present invention.
[0019] Figure 2 This is a side cross-sectional view of a sodium butyrate dust recovery device according to the present invention.
[0020] Figure 3 This is a schematic diagram of the bottom structure of the large-pore filter element in the sodium butyrate dust recovery device of this utility model.
[0021] Figure 4 This is a schematic diagram of the backflushing cleaning structure in a sodium butyrate dust recovery device of this utility model.
[0022] In the diagram: 1. Purification box; 2. Exhaust gas inlet; 3. Air pump; 4. Maintenance plate; 5. Backflush cleaning structure; 6. Support legs; 7. Vertical partition; 8. Horizontal partition; 9. Arc-shaped air guide pipe; 10. Large-pore filter element; 11. Small-pore filter element; 12. Filter cartridge; 13. Connecting flange; 14. Sealing plate; 15. Through hole; 16. Backflush main pipe; 17. First backflush branch pipe; 18. Second backflush branch pipe; 19. Backflush nozzle. Detailed Implementation
[0023] To make the technical means, creative features, objectives and effects of this utility model easier to understand, the present utility model will be further described below in conjunction with specific embodiments.
[0024] like Figure 1-4 As shown, a sodium butyrate dust recovery device mainly includes a purification box 1, an exhaust gas inlet 2, an air pump 3, a maintenance plate 4, a backflushing cleaning structure 5, and support legs 6.
[0025] The purification chamber 1 is the main body of the device. An exhaust gas inlet 2 is installed in the middle of its left outer surface for connecting to an external dust-laden gas pipeline to introduce the sodium butyrate dust gas to be treated. Support legs 6 are fixedly installed at the four corners of the bottom of the purification chamber 1 to support and secure the entire device. A maintenance plate 4 is bolted to the bottom of the front outer surface of the purification chamber 1. A ring-shaped rubber seal is provided on the contact surface between the maintenance plate 4 and the chamber body to ensure sealing and prevent dust leakage. Opening the maintenance plate 4 allows for cleaning of the dust accumulated inside the chamber.
[0026] The interior of the purification chamber 1 is divided into two chambers, left and right, by a vertical partition 7. A horizontal partition 8 is fixedly installed on the upper left side of the vertical partition 7, and a large-pore filter element 10 is bolted to the lower part of the horizontal partition 8. A small-pore filter element 11 is bolted to the upper right side of the inner chamber of the purification chamber 1. The filter cartridge 12 of the large-pore filter element 10 has a pore size of 5-10 micrometers and is used for primary filtration to intercept larger dust particles; the filter cartridge 12 of the small-pore filter element 11 has a pore size of 1-3 micrometers and is used for fine filtration to capture fine dust particles.
[0027] Both the large-pore filter element 10 and the small-pore filter element 11 include a filter cartridge 12, a connecting flange 13, and a sealing plate 14. The connecting flange 13 is fixed to the upper outer wall of the filter cartridge 12 for connection and fixation. The sealing plate 14 is fixed to the bottom of the inner cavity of the filter cartridge 12, and a through hole 15 is opened in the middle of the sealing plate 14. An arc-shaped air guide pipe 9 is fixedly installed between the middle of the transverse partition 8 and the upper part of the vertical partition 7. One end of the arc-shaped air guide pipe 9 passes through the transverse partition 8 and communicates with the upper part of the inner cavity of the filter cartridge 12 of the large-pore filter element 10, and the other end passes through the vertical partition 7 and extends to the upper part of the right side chamber, for guiding the gas after primary filtration to the area of the small-pore filter element 11.
[0028] An air pump 3 is fixedly installed on the right side of the upper outer surface of the purification box 1. The air pump 3's air extraction pipe passes through the upper part of the filter cartridge 12 of the small-diameter filter element 11. By extracting air, a negative pressure is formed, driving the gas flow and discharging the finally purified gas.
[0029] A backflush cleaning structure 5 is installed on the lower left side of the purification chamber 1, including a backflush main pipe 16, a first backflush branch pipe 17, and a second backflush branch pipe 18. The backflush main pipe 16 is located at the bottom of the inner cavity of the purification chamber 1 and passes through the lower part of the vertical partition 7. Its left end passes through the shell of the purification chamber 1 and connects to an external high-pressure air source. The first backflush branch pipe 17 and the second backflush branch pipe 18 are both vertically fixed to the upper end of the backflush main pipe 16. The upper end of the first backflush branch pipe 17 extends into the filter cartridge 12 of the large-pore filter element 10, and the second backflush branch pipe 18 extends into the filter cartridge 12 of the small-pore filter element 11. Backflush nozzles 19 are evenly distributed on the upper outer wall of the first backflush branch pipe 17 and the second backflush branch pipe 18, located inside their respective filter cartridges 12. The external high-pressure air source is activated at regular intervals. The backflushing gas is transported through the backflushing main pipe 16 and branch pipes, and finally sprayed out by the backflushing nozzle 19 to blow back the inner wall of the filter cartridge 12, causing the attached dust to fall off and achieving automatic dust removal.
[0030] The working principle of this invention is as follows: Sodium butyrate gas containing dust enters the left chamber of the purification chamber 1 through the exhaust gas inlet 2. It first undergoes primary filtration through the large-pore filter element 10, where larger particles are trapped. The preliminarily purified gas then enters the right chamber through the arc-shaped air guide pipe 9, where it undergoes secondary fine filtration through the small-pore filter element 11, capturing fine dust particles. Finally, the clean gas is drawn out by the suction pump 3. During operation, the backflushing cleaning structure 5 is activated intermittently at regular intervals. High-pressure gas is used to backflush and clean the two filter elements through the backflushing nozzles 19. The detached dust falls to the bottom of the purification chamber 1, and can be cleaned periodically by opening the maintenance plate 4.
[0031] It should be noted that, in this document, relational terms such as first and second (number one, number two), etc., are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such a process, method, article, or apparatus. Without further limitations, an element defined by the phrase "comprising one..." does not exclude the presence of other identical elements in the process, method, article, or apparatus that includes said element.
[0032] The foregoing has shown and described the basic principles, main features, and advantages of this utility model. Those skilled in the art should understand that this utility model is not limited to the above embodiments. The embodiments and descriptions in the specification are merely illustrative of the principles of this utility model. Various changes and modifications can be made to this utility model without departing from its spirit and scope, and all such changes and modifications fall within the scope of the claimed utility model.
Claims
1. A sodium butyrate dust recovery device, comprising a purification chamber (1), characterized in that... A waste gas inlet (2) is installed in the middle of the outer left side of the purification box (1). A back-flushing cleaning structure (5) is installed in the lower left side of the purification box (1). The back-flushing cleaning structure (5) includes a back-flushing main pipe (16), a first back-flushing branch pipe (17), and a second back-flushing branch pipe (18). Back-flushing nozzles (19) are evenly distributed on the outer walls of the upper part of the first back-flushing branch pipe (17) and the second back-flushing branch pipe (18). Support legs (6) are fixedly installed at the four corners of the lower outer surface of the purification box (1). A maintenance plate (4) is installed at the bottom of the front outer surface of the purification box (1) by bolts. An annular rubber ring is provided between the back of the maintenance plate (4) and the front outer surface of the purification box (1). A vacuum pump (3) is fixedly installed at the right end of the upper outer surface of the purification box (1). A vertical partition (7) is fixedly installed in the middle of the inner cavity of the purification box (1). A horizontal partition (8) is fixedly installed on the upper left side of the vertical partition (7). A large-pore filter element (10) is bolted to the lower end of the horizontal partition (8). A small-pore filter element (11) is bolted to the upper right side of the inner cavity of the purification box (1). Both the large-pore filter element (10) and the small-pore filter element (11) include a filter cartridge (12), a connecting flange (13), and a sealing plate (14). The lower end of the sealing plate (14) is externally... A through hole (15) is provided in the middle of the surface, and the through hole (15) extends to the middle of the upper outer surface of the sealing plate (14). An arc-shaped air guide pipe (9) is fixedly installed between the middle of the horizontal partition (8) and the upper part of the vertical partition (7). One end of the arc-shaped air guide pipe (9) extends to the lower outer surface of the horizontal partition (8), and the other end of the arc-shaped air guide pipe (9) extends to the upper part of the right outer surface of the vertical partition (7).
2. The sodium butyrate dust recovery device according to claim 1, characterized in that... The lower end of the arc-shaped air guide tube (9) is connected to the upper part of the inner cavity of the filter cartridge (12) in the large-pore filter element (10); the air extraction tube in the air pump (3) extends to the upper part of the inner cavity of the filter cartridge (12) in the small-pore filter element (11).
3. The sodium butyrate dust recovery device according to claim 2, characterized in that... The connecting flange (13) is fixed to the outer wall of the upper part of the filter cylinder (12), and the sealing plate (14) is fixed to the bottom of the inner cavity of the filter cylinder (12).
4. The sodium butyrate dust recovery device according to claim 3, characterized in that... The filter cartridge (12) in the large-pore filter element (10) has a pore size of 5-10 micrometers; the filter cartridge (12) in the small-pore filter element (11) has a pore size of 1-3 micrometers.
5. A sodium butyrate dust recovery device according to claim 4, characterized in that... The backflush main pipe (16) is located at the bottom of the inner cavity of the purification box (1) and penetrates the lower part of the vertical partition (7); the left end of the backflush main pipe (16) penetrates the shell of the purification box (1) and extends to its left side.
6. A sodium butyrate dust recovery device according to claim 5, characterized in that... The first backflush branch pipe (17) and the second backflush branch pipe (18) are both fixedly connected to the upper end of the backflush main pipe (16); the second backflush branch pipe (18) passes through the through hole (15) and its outer wall is fixedly connected to the sealing plate (14); the backflush nozzle (19) is located inside the filter cartridge (12).