Barium sulfate micro-reaction device for chemical fibers

By designing a rotary reaction tank and stirring mechanism, the problems of stirring hazards and uneven drying in barium sulfate production devices were solved, thus achieving a safe and efficient barium sulfate production process.

CN223969950UActive Publication Date: 2026-03-06XINJI XIBO CHEM IND CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-02-27
Publication Date
2026-03-06

AI Technical Summary

Technical Problem

Existing barium sulfate production equipment suffers from problems such as high risk of stirring and uneven drying.

Method used

A barium sulfate microreactor for chemical fibers was designed, which adopts a rotary reaction tank and a stirring mechanism. The reaction tank is driven to rotate by a snap-fit ​​gear, and combined with nozzle heating and stirring blades, the barium sulfate is prevented from sticking together.

Benefits of technology

It achieves safe and efficient mixing and uniform drying, reduces the danger of manual operation, and improves the safety and quality uniformity of barium sulfate production.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of barium sulfate preparation, in particular to a barium sulfate micro-reaction device for chemical fiber, which comprises four groups of supporting legs, the middle parts of the upper ends of the four groups of supporting legs are jointly and fixedly connected with a limiting ring, the upper end of the supporting leg at the right part of the front side is fixedly connected with a motor, and the output end of the motor is fixedly connected with a clamping gear. A rectangular plate is jointly and fixedly connected to the lower portions of the two supporting legs on the left side of the front end and the right side of the rear end, a gas storage pipe is fixedly connected to the middle of the upper end of the rectangular plate, a plurality of nozzles are fixedly connected to the upper end of the gas storage pipe at equal intervals, and a ventilation pipe is fixedly connected to the left end of the gas storage pipe; the upper ends of the two supporting legs on the left side of the front end and the right side of the rear end are jointly and fixedly connected with a stirring mechanism. According to the barium sulfate micro-reaction device for the chemical fibers, automatic stirring can be achieved in the reaction process, manual stirring is not needed, the reaction barrel can be comprehensively heated and dried, and barium sulfate can be conveniently prepared.
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Description

Technical Field

[0001] This utility model relates to the field of barium sulfate production technology, and in particular to a barium sulfate microreactor for chemical fibers. Background Technology

[0002] Barium sulfate is used in the production of synthetic fibers to improve fiber performance. However, barium sulfate requires a specialized reaction apparatus, which has some defects and shortcomings. Specific areas for improvement are as follows: 1. The conventional method of producing barium sulfate involves mixing sulfuric acid and barium hydroxide to produce barium sulfate precipitate and water. However, this reaction requires constant stirring, which increases labor costs. Furthermore, sulfuric acid and barium hydroxide are acidic and alkaline solutions, respectively, making manual stirring dangerous. 2. After production, barium sulfate needs to be dried. Conventional drying equipment is often inconveniently located, leading to uneven drying of the barium sulfate inside the reaction tank. Therefore, we propose a micro-reaction apparatus for barium sulfate used in synthetic fibers. Utility Model Content

[0003] The main objective of this invention is to provide a barium sulfate microreactor for chemical fibers, which can effectively solve the problems in the background art.

[0004] To achieve the above objectives, the technical solution adopted by this utility model is as follows:

[0005] A barium sulfate microreactor for chemical fibers includes four sets of support legs. A limiting ring is fixedly connected to the upper center of each of the four sets of support legs. A motor is fixedly connected to the upper end of the front right support leg, and a locking gear is fixedly connected to the output end of the motor. A rectangular plate is fixedly connected to the lower part of the two sets of support legs on the front left and rear right sides. A gas storage pipe is fixedly connected to the upper center of the rectangular plate. Several sets of nozzles are fixedly connected at equal intervals to the upper end of the gas storage pipe. A vent pipe is fixedly connected to the left end of the gas storage pipe. A stirring mechanism is fixedly connected to the upper end of the two sets of support legs on the front left and rear right sides. A reaction mechanism is movably locked inside the limiting ring.

[0006] Preferably, the reaction mechanism includes a reaction barrel, with two sets of limiting rings fixedly connected to the upper outer surface of the reaction barrel. The ends of the two sets of limiting rings that are close to each other are movably connected to several sets of movable rollers through a U-shaped rod at equal intervals. Several sets of snap-fit ​​teeth are fixedly connected at equal intervals to the upper part of the outer surface of the reaction barrel. Drainage pipes are fixedly connected to the lower left and lower right ends of the reaction barrel, and a filter screen is fixedly connected inside the drain pipe on the right side.

[0007] By adopting the above technical solution, the reaction vessel is made of metal and the interior is made of ceramic, which can effectively prevent acid and alkali and withstand high temperature.

[0008] Preferably, the reaction vessel is located inside the limiting ring, the limiting ring is located inside two sets of limiting rings, and several sets of moving rollers are in contact with the limiting ring but not fixed.

[0009] By adopting the above technical solution, the movable roller can facilitate the rotation of the reaction tank, which is located above several sets of nozzles.

[0010] Preferably, the stirring mechanism includes a support frame, an extension tube is fixedly connected to the middle of the lower inner wall of the support frame, an extension rod is inserted and fixedly arranged in the middle of the support frame, a number of connecting rods are fixedly connected at equal intervals on the outer surface of the extension rod, a stirring blade is fixedly connected to the end of the number of connecting rods that do not contact the extension rod, and a scraping plate is fixedly connected to the lower left and lower right ends of the extension rod.

[0011] By adopting the above technical solution—that is, extending the round rod through the extension tube—control over the extended round rod can be increased.

[0012] Preferably, the stirring blade and the scraper are both located inside the reaction vessel, the scraper is in contact with but not fixed to the lower inner wall of the reaction vessel, and the support frame is fixedly connected to the support leg.

[0013] By adopting the above technical solution, the scraping plate can prevent barium sulfate from sticking to the bottom during drying.

[0014] Preferably, several sets of the engaging teeth mesh with the engaging gear.

[0015] By adopting the above technical solution, the snap-fit ​​teeth and snap-fit ​​gears can be engaged and locked together, which can drive the reaction tank to rotate.

[0016] Compared with the prior art, the present invention has the following beneficial effects:

[0017] 1. By setting up a stirring mechanism, a spiral stirring blade is fixedly connected to the extension rod of the stirring structure via a connecting rod. This can stir and mix the sulfuric acid and barium hydroxide solution inside, facilitating their reaction to produce barium sulfate. Additionally, the scraping plate at the bottom can scrape the lower inner wall of the reaction tank when it rotates, preventing the generated barium sulfate from sticking to the bottom during drying.

[0018] 2. By setting up a reaction mechanism, the two sets of limiting rings on the reaction barrel can easily support the reaction barrel, and the movable rollers set on the limiting rings can reduce friction when the reaction barrel rotates. The upper locking teeth mesh with the locking gear at the motor output end, which can drive the reaction barrel to rotate, so that the lower nozzle can fully heat the lower part of the reaction barrel and dry the barium sulfate. Attached Figure Description

[0019] Figure 1This is a partial structural schematic diagram of a barium sulfate microreactor for chemical fibers according to this utility model;

[0020] Figure 2 This is a partial structural schematic diagram of a barium sulfate microreactor for chemical fibers according to this utility model;

[0021] Figure 3 This is a schematic diagram of the reaction mechanism of a barium sulfate microreactor for chemical fibers according to this utility model;

[0022] Figure 4 This is a schematic diagram of the stirring mechanism of a barium sulfate microreactor for chemical fibers according to this utility model.

[0023] In the diagram: 1. Support leg; 2. Limiting ring; 3. Motor; 4. Snap-fit ​​gear; 5. Rectangular plate; 6. Gas storage pipe; 7. Nozzle; 8. Vent pipe; 9. Stirring mechanism; 10. Reaction mechanism; 11. Reaction tank; 12. Limiting ring; 13. Moving roller; 14. Snap-fit ​​tooth; 15. Drain pipe; 16. Filter screen; 91. Support frame; 92. Extension pipe; 93. Extension rod; 94. Connecting rod; 95. Stirring blade; 96. Scratching plate. Detailed Implementation

[0024] 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.

[0025] In the description of this utility model, it should be noted that the terms "upper," "lower," "inner," "outer," "front end," "rear end," "both ends," "one end," and "the other end," etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are used only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model. In addition, the terms "first" and "second" are used for descriptive purposes only and should not be construed as indicating or implying relative importance.

[0026] In the description of this utility model, it should be noted that, unless otherwise explicitly specified and limited, the terms "installed," "equipped with," and "connected," etc., should be interpreted broadly. For example, "connected" can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium; it can be a connection within two components. Those skilled in the art can understand the specific meaning of the above terms in this utility model based on the specific circumstances.

[0027] Please see Figure 1-4This utility model provides a technical solution:

[0028] A barium sulfate microreactor for chemical fibers includes four sets of support legs 1. A limiting ring 2 is fixedly connected to the middle of the upper part of the four sets of support legs 1. A motor 3 is fixedly connected to the upper part of the support leg 1 on the front right side. A snap-fit ​​gear 4 is fixedly connected to the output end of the motor 3. A rectangular plate 5 is fixedly connected to the lower part of the two sets of support legs 1 on the front left and rear right sides. A gas storage pipe 6 is fixedly connected to the middle of the upper part of the rectangular plate 5. Several sets of nozzles 7 are fixedly connected at equal intervals to the upper part of the gas storage pipe 6. A vent pipe 8 is fixedly connected to the left end of the gas storage pipe 6. A stirring mechanism 9 is fixedly connected to the upper part of the two sets of support legs 1 on the front left and rear right sides. A reaction mechanism 10 is movably snap-fitted inside the limiting ring 2.

[0029] In this embodiment, the reaction mechanism 10 includes a reaction tank 11. Two sets of limiting rings 12 are fixedly connected to the upper outer surface of the reaction tank 11. Several sets of movable rollers 13 are movably connected to the near ends of the two sets of limiting rings 12 through a U-shaped rod at equal intervals. Several sets of snap-fit ​​teeth 14 are fixedly connected at equal intervals to the upper outer surface of the reaction tank 11. Drain pipes 15 are fixedly connected to the lower left and lower right ends of the reaction tank 11. A filter screen 16 is fixedly connected inside the drain pipe 15 on the right side. The reaction tank 11 is located inside the limiting ring 2. The limiting ring 2 is located inside the two sets of limiting rings 12, and the several sets of movable rollers 13 are in contact with the limiting ring 2 but are not fixed.

[0030] Through the above scheme: the upper part of the reaction tank 11 is fixedly connected with a snap-fit ​​protrusion 14, which meshes with the snap-fit ​​gear 4 at the output end of the motor 3, so as to drive the reaction tank 11 to rotate, so that the flame sprayed from the nozzle 7 at the bottom can evenly heat the lower part of the reaction tank 11 and evenly dry the barium sulfate inside.

[0031] In this embodiment, the stirring mechanism 9 includes a support frame 91. An extension tube 92 is fixedly connected to the middle of the lower inner wall of the support frame 91. An extension rod 93 is inserted and fixedly arranged in the middle of the support frame 91. Several sets of connecting rods 94 are fixedly connected at equal intervals on the outer surface of the extension rod 93. The ends of the several sets of connecting rods 94 that do not contact the extension rod 93 are fixedly connected to a stirring blade 95. The lower left and lower right ends of the extension rod 93 are both fixedly connected to a scraping plate 96. The stirring blade 95 and the scraping plate 96 are both located inside the reaction tank 11. The scraping plate 96 contacts the lower inner wall of the reaction tank 11 but is not fixed. Several sets of snap-fit ​​teeth 14 are fixedly connected to the support leg 1 and are engaged with the snap-fit ​​gear 4.

[0032] With the above scheme: the extended round rod 93 on the stirring mechanism 9 has a stirring blade 95 fixedly connected by a connecting rod 94. The extended round rod 93 and the stirring blade 95 are stationary, but the reaction tank 11 is driven to rotate, so the internal contents can be stirred. In addition, during the subsequent drying, the scraping plate 96 at the bottom can scrape the inner wall of the reaction tank 11 to prevent barium sulfate from sticking to the inner wall.

[0033] It should be noted that this utility model is a barium sulfate microreactor for chemical fibers. During use, a proportioned sulfuric acid solution and barium hydroxide solution are first injected into the reaction tank 11. Then, the motor 3 is driven. The output end of the motor 3 is fixedly connected to a snap-fit ​​gear 4, which engages with a snap-fit ​​protrusion 14 fixedly connected to the upper outer surface of the reaction tank 11. This allows the reaction tank 11 to rotate. Furthermore, a movable roller 13, movably connected to a limiting ring 12 fixedly connected to the outer surface of the reaction tank 11 via a U-shaped rod, reduces friction during the rotation of the reaction tank 11, facilitating its rotation. The upper part of the support leg 1 is fixed... The connecting rod 94 and stirring blade 95, which are connected by the extension rod 93, are fixed on the support frame 91. When the reaction tank 11 rotates, the solution inside is mixed and stirred to facilitate the reaction. After the reaction is completed, the solution inside is discharged through the drain pipe 15 with a filter screen 16, leaving only moist barium sulfate inside the reaction tank 11. As the reaction tank 11 continues to rotate, the gas pipe 8 at the bottom is supplied with gas, which is sprayed out from the nozzle 7. The gas is ignited and heats the lower end of the reaction tank 11 evenly, which facilitates the drying of barium sulfate. The scraping plate 96 can scrape the inner wall of the reaction tank 11 to prevent barium sulfate from sticking together.

[0034] 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 claims. The scope of protection of this utility model is defined by the appended claims and their equivalents.

Claims

1. A barium sulfate micro-reactor for chemical fibers, comprising four sets of supporting legs (1), characterized in that: The upper end of the four groups of support legs (1) is fixedly connected with a limiting ring (2), the upper end of the front right support leg (1) is fixedly connected with a motor (3), the output end of the motor (3) is fixedly connected with a clamping gear (4), the lower part of the two groups of support legs (1) between the front left end and the rear right end is fixedly connected with a rectangular plate (5), the upper end of the rectangular plate (5) is fixedly connected with a gas storage pipe (6), the upper end of the gas storage pipe (6) is fixedly connected with a plurality of groups of nozzles (7), the left end of the gas storage pipe (6) is fixedly connected with an air pipe (8), the upper end of the two groups of support legs (1) between the front left end and the rear right end is fixedly connected with a stirring mechanism (9), and the inside of the limiting ring (2) is movably clamped with a reaction mechanism (10).

2. A barium sulfate micro-reactor for chemical fibers according to claim 1, characterized in that: The reaction mechanism (10) comprises a reaction bucket (11), the upper outer surface of the reaction bucket (11) is fixedly connected with two groups of limiting rings (12), the ends close to each other of the two groups of limiting rings (12) are movably connected with a plurality of groups of movable rollers (13) through meandering rods at equal distances, the outer surface of the reaction bucket (11) is fixedly connected with a plurality of groups of clamping convex teeth (14) at equal distances, and the left lower part and the right lower part of the reaction bucket (11) are fixedly connected with a drain pipe (15). The inside of the right drain pipe (15) is fixedly connected with a filter screen (16).

3. A barium sulfate micro-reactor for chemical fibers according to claim 2, characterized in that: The reaction bucket (11) is located in the inside of the limiting ring (2), the limiting ring (2) is located in the inside of the two groups of limiting rings (12), and the plurality of groups of movable rollers (13) are in contact with the limiting ring (2) but are not fixed.

4. The barium sulfate micro-reactor for chemical fibers according to claim 2, characterized in that: The stirring mechanism (9) comprises a support frame (91), the lower inner wall of the support frame (91) is fixedly connected with an extension pipe (92), the support frame (91) is movably fixedly provided with an extension round rod (93), the outer surface of the extension round rod (93) is fixedly connected with a plurality of groups of connecting rods (94) at equal distances, the ends of the plurality of groups of connecting rods (94) not in contact with the extension round rod (93) are fixedly connected with stirring blades (95), and the left lower part and the right lower part of the extension round rod (93) are fixedly connected with scraping plates (96).

5. A barium sulfate micro-reactor for chemical fibers according to claim 4, characterized in that: The stirring blades (95) and the scraping plates (96) are located in the inside of the reaction bucket (11), the scraping plates (96) are in contact with the lower inner wall of the reaction bucket (11) but are not fixed, and the support frame (91) is fixedly connected with the support leg (1).

6. A barium sulfate micro-reactor for chemical fibers according to claim 2, characterized in that: The plurality of groups of clamping convex teeth (14) are in meshing clamping with the clamping gear (4).