Novel stepped mixer

By designing a novel stepped mixer, utilizing an O-ring and bolt connection structure, combined with flow-blocking blocks and turbulence-disrupting columns, the problems of inconvenient loading, unloading, and cleaning of micro mixers and low mixing efficiency are solved, achieving a highly efficient and uniform mixing effect.

CN223861727UActive Publication Date: 2026-02-03SHANDONG FLOW-CHEM SILO CHEM TECH CO LTD
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Patent Information

Application Number
CN202520164363.2
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-01-23
Publication Date
2026-02-03
Estimated Expiration
2035-01-23

AI Technical Summary

Technical Problem

Existing micro mixers have complex structures, are inconvenient to install, disassemble, and clean, and have low mixing efficiency and uneven mixing.

Method used

A novel stepped mixer is adopted, which fixes the first heat exchange plate, baffle and mixing plate by O-ring and bolt connection. It is designed with mixing channel and heat exchange channel, and set flow blocking block and turbulence column in the channel to achieve multiple mixing and efficient heat exchange.

Benefits of technology

With its simple structure, it is easy to install, disassemble and clean, significantly improving mixing efficiency, avoiding uneven mixing, and achieving high-efficiency mixing.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a novel stepped mixer and relates to the technical field of mixers. The stepped mixer comprises a first heat exchange plate, a partition plate, a mixing plate and a second heat exchange plate, and the adjacent parts are connected through O-shaped rings and bolts; a first heat exchange channel is arranged on one face of the first heat exchange plate, a mixing channel is arranged on one face of the mixing plate, and a second heat exchange channel is arranged on the other face of the mixing plate. The mixing channel is divided into a plurality of mixing units, and a mixing part is arranged in each mixing unit. All the components are sealed through the O-shaped rings and detachably and fixedly connected through the bolts, the structure is simple, mounting and dismounting are convenient, the first mixing unit, the second mixing unit and the third mixing unit are matched, two liquid materials can be mixed for multiple times through the mixing part and the flow guide column, and the mixing efficiency is improved. Meanwhile, the first heat exchange channel and the second heat exchange channel are used for efficient heat exchange, so that the mixing efficiency is remarkably improved, and the problem of non-uniform mixing is avoided.
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Description

Technical Field

[0001] This utility model relates to the field of mixer technology, and in particular to a novel stepped mixer. Background Technology

[0002] Micromixers can effectively mix and emulsify two immiscible liquids, and they have wide applications in chemical synthesis. However, current micromixers have relatively complex structures, making them inconvenient to install, remove, clean, and adjust, and they also suffer from low mixing efficiency and uneven mixing. Utility Model Content

[0003] In view of the problems of complex structure, inconvenience in installation, disassembly, cleaning and debugging, low mixing efficiency and uneven mixing of the existing micro mixers, this utility model provides a new type of stepped mixer.

[0004] To solve the above-mentioned technical problems, the present invention adopts the following technical solution:

[0005] A novel stepped mixer includes a first heat exchange plate, a partition plate, a mixing plate, and a second heat exchange plate, with adjacent components connected by O-rings and bolts. A first heat exchange channel is provided on one side of the first heat exchange plate, a mixing channel is provided on one side of the mixing plate, and a second heat exchange channel is provided on the other side. The mixing channel is divided into several mixing units, each containing a mixing section.

[0006] Furthermore, the first heat exchange plate, the partition plate, the mixing plate, and the second heat exchange plate are sequentially bonded together, with the first heat exchange channel located on the bottom surface of the first heat exchange plate and the second heat exchange channel located on the bottom surface of the mixing plate.

[0007] Furthermore, both the first heat exchange channel and the second heat exchange channel have several flow-blocking blocks.

[0008] Furthermore, one side of the first heat exchange channel is connected to the first heat exchange inlet, and the other side is connected to the first heat exchange outlet; one side of the second heat exchange channel is connected to the second heat exchange inlet, and the other side is connected to the second heat exchange outlet.

[0009] Furthermore, each of the flow-blocking blocks is triangular in shape and arranged in an alternating pattern, with one corner of each flow-blocking block facing either the first heat exchange inlet or the second heat exchange inlet.

[0010] Furthermore, the mixing unit includes a first mixing unit, a second mixing unit, and a third mixing unit connected in sequence. One side of the first mixing unit is connected to a first feed inlet, and the other side is connected to a second feed inlet. The mixing part is located between the first feed inlet and the second feed inlet.

[0011] Furthermore, the mixing section is formed by an S-shaped first partition, and the top of the mixing section is lower than the top surface of the mixing plate.

[0012] Furthermore, each of the first mixing unit, the second mixing unit, and the third mixing unit is connected to a dispensing plate on one side, and each dispensing plate is provided with a few interfering flow columns. A second partition is provided between each dispensing plate and the first mixing unit, the second mixing unit, and the third mixing unit.

[0013] Furthermore, the dispensing plate adjacent to the first mixing unit is connected to both sides of the second mixing unit via a curved connecting groove; the dispensing plate adjacent to the second mixing unit is connected to both sides of the third mixing unit via a curved connecting groove; and the dispensing plate adjacent to the third mixing unit is connected to a discharge port.

[0014] Furthermore, both sides of the second and third mixing units are provided with several interference flow columns.

[0015] The beneficial effects of this utility model are: the components of this utility model are sealed with O-rings and fixedly connected by bolts, the structure is simple, and it is easy to install, disassemble, clean and debug. Furthermore, the first mixing unit, the second mixing unit and the third mixing unit cooperate to mix the two liquid materials multiple times using the mixing part and the guide column. At the same time, the first heat exchange channel and the second heat exchange channel are used for efficient heat exchange, which significantly improves the mixing efficiency and avoids the problem of uneven mixing. Attached Figure Description

[0016] Figure 1 The image shown is an exploded view of the structure of this utility model.

[0017] Figure 2 As shown Figure 1 A sectional view.

[0018] Figure 3 As shown Figure 1 A schematic diagram of the structure of the hybrid plate.

[0019] Figure 4 As shown Figure 3 Top view.

[0020] Figure 5 The diagram shown is a schematic of the structure of the first heat exchange plate.

[0021] Figure 6 As shown Figure 5 Top view.

[0022] Explanation of reference numerals in the attached drawings: 1. First heat exchange plate; 2. Baffle plate; 3. Mixing plate; 4. Second heat exchange plate; 5. Mixing channel (5); 6. First heat exchange inlet; 7. First heat exchange outlet; 8. First heat exchange channel; 9. Second feed inlet; 10. Discharge outlet; 11. Second heat exchange inlet; 12. Second heat exchange outlet; 13. Second heat exchange channel; 14. Sealing groove; 15. First mixing unit; 16. Second mixing unit; 17. Third mixing unit; 18. Mixing section; 19. Second partition; 20. First distribution plate; 21. Connecting groove; 22. Second distribution plate; 23. Third distribution plate; 24. Baffle column; 25. Flow blocking block; 26. Support component. Detailed Implementation

[0023] This utility model discloses a novel stepped mixer. The following describes one embodiment of this utility model in detail with reference to the accompanying drawings.

[0024] Combination Figure 1 and Figure 2 As shown, a novel stepped mixer includes a first heat exchange plate 1, a partition plate 2, a mixing plate 3, and a second heat exchange plate 4. The first heat exchange plate 1, partition plate 2, mixing plate 3, and second heat exchange plate 4 are sequentially and tightly fitted together, and adjacent components are detachably fixed together by bolts. A mixing channel 5 is provided on the bottom surface of the mixing plate 3, and a sealing groove 14 is formed on the outer periphery of the mixing channel 5. An O-ring is disposed within the sealing groove 14, and the mixing plate 3 and partition plate 2 are sealed together by the O-ring. The mixing channel 5 is divided into a first mixing unit 15, a second mixing unit 16, and a third mixing unit 17, which are sequentially connected and each has a mixing section 18 inside. The mixing section 18 is formed by an S-shaped first partition plate 2. The top of the mixing section 18 is lower than the top surface of the mixing plate 3, and a support member 26 protrudes upward at the corner of each first partition plate 2. The bottom surface of the support member 26 is at the same height as the top surface of the mixing plate 3. In this embodiment, the thickness of the partition 2 is no more than 1 mm, which is used to ensure the effective transfer of heat between the reaction fluid and the heat exchange fluid.

[0025] Combination Figure 3 and Figure 4As shown, a first feed inlet is provided on the left side wall of the mixing plate 3, and a second feed inlet 9 is provided on the right side wall. The first feed inlet is connected to the bottom left side of the first mixing unit 15, and the second feed inlet 9 is connected to the bottom right side of the first mixing unit 15. The first mixing unit 15, the second mixing unit 16, and the third mixing unit 17 all have a mixing section 18. A first distribution plate 20 is provided between the first mixing unit 15 and the second mixing unit 16, a second distribution plate 22 is provided between the second mixing unit 16 and the third mixing unit 17, and the third mixing unit 17 is connected to a third distribution plate 23. The first distribution plate 20, the second distribution plate 22, and the third distribution plate 23 all have several staggered turbulence columns 24.

[0026] A second partition 19 is provided between one side of the first dispensing plate 20 and the first mixing unit 15, and the other side is connected to both sides of the second mixing unit 16 through a curved connecting groove 21. A second partition 19 is also provided between one side of the second dispensing plate 22 and the second mixing unit 16, and the other side is connected to both sides of the third mixing unit 17 through a curved connecting groove 21. A third partition is provided between one side of the third dispensing plate 23 and the third mixing unit 17, and the other side is connected to the discharge port 10 opened on the rear side wall of the mixing plate 3.

[0027] Combination Figure 5 and Figure 6 As shown, a first heat exchange channel 8 is provided on the bottom surface of the first heat exchange plate 1, and a second heat exchange channel 13 is provided on the bottom surface of the mixing plate 3. Sealing grooves 14 are provided on the outer periphery of both the first and second heat exchange channels 8 and 13, and O-rings are disposed within the sealing grooves 14. The first heat exchange plate 1 and the partition plate 2 are sealed by O-rings, and the mixing plate 3 and the second heat exchange plate 4 are also sealed by O-rings. Both the first and second heat exchange channels 8 and 13 are hexagonal, and each contains several staggered flow-blocking blocks 25, each with an isosceles triangular cross-section. A first heat exchange inlet 6 is provided on the front sidewall of the first heat exchange plate 1, and the first heat exchange inlet 6 communicates with the front side of the bottom of the first heat exchange channel 8. A first heat exchange outlet 7 is provided on the rear sidewall of the first heat exchange plate 1, and the first heat exchange outlet 7 communicates with the rear side of the bottom of the first heat exchange channel 8. A second heat exchange inlet 11 is provided on the front side wall of the second heat exchange plate 4, and the second heat exchange inlet 11 is connected to the front side of the second heat exchange channel 13. A second heat exchange outlet 12 is provided on the rear side wall of the second heat exchange plate 4, and the second heat exchange outlet 12 is connected to the rear side of the second heat exchange channel 13. In the first heat exchange channel 8, the apex of each flow-blocking block 25 faces the first heat exchange inlet 6; in the second heat exchange channel 13, the apex of each flow-blocking block 25 faces the second heat exchange inlet 11. Each flow-blocking block 25 can effectively prevent the partition plate 2 from deforming while ensuring heat exchange efficiency through its dense and uniform arrangement.

[0028] In use, the first heat exchange plate 1, partition plate 2, mixing plate 3, and second heat exchange plate 4 are arranged and installed sequentially from top to bottom. The first heat exchange inlet 6, the first heat exchange outlet 7, the second heat exchange inlet 11, and the second heat exchange outlet 12 are respectively connected to external heat exchange pipes. The first feed inlet is connected to the first feed pipe, the second feed inlet 9 is connected to the second feed pipe, and the discharge outlet 10 is connected to the discharge pipe. Operators use the first and second feed pipes to introduce different liquid materials into the mixing channel 5. The two different liquid materials are separated into several thin streams by the S-shaped first partition, and the two different liquid materials interweave. As the liquid materials are continuously introduced, the two different liquid materials will undergo preliminary mixing at the top of the first partition, and the preliminarily mixed liquid enters the first distribution plate 20 through the second partition 19. The first dispensing plate 20 has several turbulent flow columns 24, which further mix the initially mixed liquid. The initially mixed liquid then enters the left and right sides of the second mixing unit 16 through the connecting groove 21. Both sides of the second mixing unit 16 are provided with several turbulent flow columns 24, which further mix the initially mixed liquid. The liquid entering the left and right sides of the second mixing unit 16 then undergoes a second mixing through the mixing section 18. The liquid after the second mixing passes through the second partition 19 into the second dispensing plate 22, where the several turbulent flow columns 24 further mix the liquid. The liquid after the second mixing then enters the left and right sides of the third mixing unit 17 through the connecting groove 21. The structure and material mixing process of the third mixing unit 17 are approximately the same as those of the second mixing unit 16. The liquid after the second mixing undergoes a third mixing in the mixing section 18 within the third mixing unit 17. After the third mixing, the liquid enters the third distribution plate 23 through the second partition 19. The turbulent flow column 24 located in the third distribution plate 23 further mixes the liquid after the third mixing. Then, the liquid after the third mixing flows out of the mixing plate 3 through the discharge port 10.

[0029] There is no specific limit to the number of mixing units; staff can flexibly increase the number of mixing units according to the difficulty of mixing the liquid materials.

[0030] Of course, the above description is not intended to limit the present utility model, and the present utility model is not limited to the examples given above. Any changes, modifications, additions or substitutions made by those skilled in the art within the scope of the present utility model should also fall within the protection scope of the present utility model.

Claims

1. A novel stepped mixer, characterized in that: It includes a first heat exchange plate (1), a partition plate (2), a mixing plate (3) and a second heat exchange plate (4), and adjacent components are connected by O-rings and bolts; a first heat exchange channel (8) is provided on one side of the first heat exchange plate (1), a mixing channel (5) is provided on one side of the mixing plate (3), and a second heat exchange channel (13) is provided on the other side; the mixing channel (5) is divided into several mixing units, and each mixing unit has a mixing part (18).

2. The novel stepped mixer according to claim 1, characterized in that: The first heat exchange plate (1), the partition plate (2), the mixing plate (3) and the second heat exchange plate (4) are sequentially attached to each other. The first heat exchange channel (8) is located on the bottom surface of the first heat exchange plate (1) and the second heat exchange channel (13) is located on the bottom surface of the mixing plate (3).

3. A novel stepped mixer according to claim 2, characterized in that: Both the first heat exchange channel (8) and the second heat exchange channel (13) have several flow-blocking blocks (25).

4. A novel stepped mixer according to claim 3, characterized in that: One side of the first heat exchange channel (8) is connected to the first heat exchange inlet (6), and the other side is connected to the first heat exchange outlet (7); one side of the second heat exchange channel (13) is connected to the second heat exchange inlet (11), and the other side is connected to the second heat exchange outlet (12).

5. A novel stepped mixer according to claim 4, characterized in that: Each of the flow-blocking blocks (25) is triangular and arranged in an alternating pattern, with one corner of each flow-blocking block (25) facing the first heat exchange inlet (6) or the second heat exchange inlet (11).

6. A novel stepped mixer according to claim 1, characterized in that: The mixing unit includes a first mixing unit (15), a second mixing unit (16), and a third mixing unit (17) connected in sequence. The first mixing unit (15) has a first feed port connected to one side and a second feed port (9) connected to the other side. The mixing part (18) is located between the first feed port and the second feed port (9).

7. A novel stepped mixer according to claim 6, characterized in that: The mixing section (18) is formed by an S-shaped first partition, and the top of the mixing section (18) is lower than the top surface of the mixing plate (3).

8. A novel stepped mixer according to claim 6, characterized in that: One side of each of the first mixing unit (15), the second mixing unit (16), and the third mixing unit (17) is connected to a liquid distribution plate. Each liquid distribution plate is provided with a few turbulent flow columns (24). A second partition (19) is provided between each liquid distribution plate and the first mixing unit (15), the second mixing unit (16), and the third mixing unit (17).

9. A novel stepped mixer according to claim 8, characterized in that: The liquid distribution plate adjacent to the first mixing unit (15) is connected to both sides of the second mixing unit (16) via a curved connecting groove (21); the liquid distribution plate adjacent to the second mixing unit (16) is connected to both sides of the third mixing unit (17) via a curved connecting groove (21); the liquid distribution plate adjacent to the third mixing unit (17) is connected to a discharge port (10).

10. A novel stepped mixer according to claim 8, characterized in that: Both sides of the second mixing unit (16) and the third mixing unit (17) are provided with some interference flow columns (24).