A homogeneous feed mixed reactor
By designing multiple sets of outlets arranged axially and circumferentially in the reactor, combined with heat exchange and stirring mechanisms, the problem of uneven mixing of liquid reaction media in the prior art is solved, and rapid and uniform mixing is achieved.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- 南京伟励技术有限公司
- Filing Date
- 2025-06-30
- Publication Date
- 2026-06-05
AI Technical Summary
In the prior art, mixing two liquid reaction media in a reaction device is time-consuming and difficult to achieve a completely uniform mixture, especially in the initial mixing stage where the effect is poor.
A uniform feed mixing reactor is designed, employing multiple sets of outlets arranged along the axial and circumferential directions of the reactor to ensure that the two reaction media enter the reactor through the spaced outlets respectively. Combined with heat exchange and stirring mechanisms, uniform feeding and mixing are achieved.
This allows for uniform mixing of the two reaction media upon entering the reaction vessel, saving stirring time and improving mixing efficiency.
Smart Images
Figure CN224321392U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of chemical equipment technology, specifically to a uniformly fed mixing reactor. Background Technology
[0002] Mixing two liquid reaction media in a reaction apparatus to facilitate the reaction is typically achieved using a stirring mechanism in existing technologies.
[0003] For example, Chinese invention patent CN120005698A discloses a highly efficient microbial agent preparation device and method for nitrogen and phosphorus removal. The preparation device includes a reaction tank, the top of which is equipped with a feed hopper, a first inlet pipe, a second inlet pipe, and a driving device, while the bottom of the reaction tank is equipped with a discharge pipe. In this prior art, two reaction media enter the reaction tank through the first and second inlet pipes respectively, and a stirring mechanism ensures that the reaction media are fully mixed.
[0004] When two different types of reaction media are injected into the reaction apparatus described above, the two reaction media are mixed by stirring. Firstly, stirring the reaction media is time-consuming, and it is difficult to achieve a completely uniform mixture. Secondly, the existing reaction apparatus is unsuitable when it is necessary for the two reaction media to be uniformly mixed and reacted from the initial stage of entering the reaction vessel. Utility Model Content
[0005] To address the aforementioned problems, the purpose of this invention is to provide a uniformly fed mixing reactor.
[0006] The technical solution provided by this utility model is as follows:
[0007] A uniformly fed mixing reactor includes a reaction vessel, which has a reaction chamber and is connected to an outlet pipe.
[0008] The reaction chamber is equipped with a first reaction medium delivery mechanism and a second reaction medium delivery mechanism.
[0009] The first reaction medium conveying mechanism is provided with multiple sets of first outlets, and the second reaction medium conveying mechanism is provided with multiple sets of second outlets;
[0010] Each group of first outlets and each group of second outlets includes multiple outlets arranged along the axial direction of the reaction vessel;
[0011] In the circumferential direction of the reaction vessel, each group of first outlets and each group of second outlets are arranged alternately;
[0012] The distance between the first outlet and the center line of the reaction vessel is R1, and the distance between the second outlet and the center line of the reaction vessel is R2, where R1 = (0.98~1.02)R2.
[0013] As an optional technical solution, the first reaction medium conveying mechanism includes a first annular pipe, which is connected to a first inlet pipe and a plurality of first branch pipes; the plurality of first branch pipes are evenly arranged along the circumference of the reaction tank; the first branch pipes extend along the axial direction of the reaction tank; and the first outlet is provided on the first branch pipe.
[0014] The second reaction medium conveying mechanism includes a second annular pipe, which is connected to a second inlet pipe and a plurality of second branch pipes; the plurality of second branch pipes are evenly arranged along the circumference of the reaction tank; the second branch pipes extend along the axial direction of the reaction tank; and the second outlet is provided on the second branch pipes.
[0015] Optionally, the diameter D1 of the first annular pipe is larger than the diameter D2 of the second annular pipe; the second branch pipe is connected to the second annular pipe through a transition pipe.
[0016] Optionally, an outer tank is installed on the outside of the reaction vessel, and a heat exchange cavity is formed between the inner wall of the outer tank and the outer wall of the reaction vessel; the outer tank is provided with a heat exchange medium inlet and a heat exchange medium outlet; the heat exchange medium inlet and the heat exchange medium outlet are connected to the heat exchange cavity.
[0017] As an optional technical solution, a first cylinder, a second cylinder, and a third cylinder are sequentially installed from the outside to the inside within the reaction chamber; a first flow channel is formed between the first cylinder and the second cylinder, and a second flow channel is formed between the second cylinder and the third cylinder; both the first and second flow channels are provided with inlets;
[0018] The second outlet is located on the third cylinder and is connected to the second flow channel.
[0019] A connecting pipe is installed between the second cylinder and the third cylinder, and a transition channel is formed inside the connecting pipe; the first outlet is located on the third cylinder and is connected to the transition channel; the second cylinder is provided with a transition outlet, which is used to connect the first channel and the transition channel.
[0020] Optionally, a heat exchanger is installed inside the third cylinder.
[0021] Furthermore, the heat exchanger includes an upper annular tube and a lower annular tube; the upper annular tube and the lower annular tube are connected by a plurality of vertical tubes arranged in a ring; one of the upper annular tube and the lower annular tube is connected to the heat exchange medium inlet and the other is connected to the heat exchange medium outlet.
[0022] As an optional technical solution, it also includes stirring blades and a drive mechanism for driving the stirring blades to rotate; the stirring blades are used to stir the first reaction medium and the second reaction medium in the reaction chamber.
[0023] As an optional technical solution, the diameters of the first outlet and the second outlet are 0.05mm to 0.15mm.
[0024] Compared with the prior art, the technical solution provided by this utility model has the following advantages:
[0025] This invention includes multiple sets of first outlets and multiple sets of second outlets. Each set of first outlets and each set of second outlets includes multiple outlets arranged along the axial direction of the reaction tank. In the circumferential direction of the reaction tank, each set of first outlets and each set of second outlets are arranged alternately, and the distance between the first outlet and the center line of the reaction tank is approximately equal to the distance between the second outlet and the center line of the reaction tank. When the two reaction media enter the reaction tank through the first outlet and the second outlet respectively, uniform feeding and uniform mixing can be achieved. Attached Figure Description
[0026] Figure 1 This is a schematic diagram of a uniformly fed mixing reactor in one embodiment of this application;
[0027] Figure 2 for Figure 1 Enlarged view of point A in the middle;
[0028] Figure 3 This is a schematic diagram of the arrangement of the first annular tube and the second annular tube in one embodiment of this application;
[0029] Figure 4 This is a schematic diagram of the arrangement of the first branch pipe and the second branch pipe in one embodiment of this application;
[0030] Figure 5 This is a schematic diagram showing the arrangement of the first cylinder, the second cylinder, and the third cylinder in one embodiment of this application;
[0031] Figure 6 This is a schematic diagram showing the flow direction of the first and second reaction media in one embodiment of this application;
[0032] Figure 7 This is a schematic diagram showing the connection between the upper annular pipe, the vertical pipe, and the lower annular pipe in one embodiment of this application.
[0033] Explanation of the labels in the diagram:
[0034] Reaction tank 101, reaction chamber 102, reaction tank outlet pipe 103, second outlet 104, first outlet 105, first annular pipe 201, first inlet pipe 202, first branch pipe 203, second annular pipe 301, second inlet pipe 302, second branch pipe 303, transition pipe 303-1, outer tank 401, heat exchange chamber 402, heat exchange medium inlet 403, heat exchange medium outlet 404, upper annular pipe 405, lower annular pipe 406, vertical pipe 407, first cylinder 501, second cylinder 502, third cylinder 503, connecting pipe 504, transition outlet 505, first flow channel 506, second flow channel 507, transition flow channel 508. Detailed Implementation
[0035] To further understand the content of this utility model, a detailed description of this utility model will be provided in conjunction with the accompanying drawings and embodiments.
[0036] The structures, proportions, and sizes illustrated in the accompanying drawings are merely for illustrative purposes and to aid those skilled in the art in understanding and reading the invention. They are not intended to limit the scope of the invention and therefore have no substantial technical significance. Any modifications to the structure, changes in proportions, or adjustments to size, without affecting the effectiveness and purpose of the invention, should still fall within the scope of the technical content disclosed in this utility model. Furthermore, terms such as "upper," "lower," "left," "right," and "middle" used in this specification are merely for clarity and not intended to limit the scope of implementation. Changes or adjustments to their relative relationships, without substantially altering the technical content, should also be considered within the scope of the invention's implementation.
[0037] In one embodiment, this application proposes a uniform feed mixing reactor, including a reaction vessel 101, wherein the reaction vessel 101 is provided with a reaction chamber 102, and the reaction media are mixed in the reaction chamber 102. After the two reaction media are mixed and reacted in the reaction chamber 102, the product is discharged through a reaction vessel outlet pipe 103 provided with the reaction vessel.
[0038] A first reaction medium delivery mechanism and a second reaction medium delivery mechanism are installed in the reaction chamber 102. The first reaction medium is delivered into the reaction chamber 102 through the first reaction medium delivery mechanism, and the second reaction medium is delivered into the reaction chamber 102 through the second reaction medium delivery mechanism. In this embodiment, both the first reaction medium and the second reaction medium are liquids.
[0039] The first reaction medium conveying mechanism is provided with multiple sets of first outlets, and the second reaction medium conveying mechanism is provided with multiple sets of second outlets. The arrangement of the first and second outlets simultaneously satisfies the following conditions: (1) Each set of first outlets and each set of second outlets includes multiple outlets arranged along the axial direction of the reaction tank; (2) In the circumferential direction of the reaction tank 101, each set of first outlets and each set of second outlets are arranged alternately; (3) ... Figure 4 , 6 As shown, the distance between the first outlet and the center line of the reaction tank is R1, and the distance between the second outlet and the center line of the reaction tank is R2, where R1 = (0.98~1.02)R2. This arrangement facilitates reactor manufacturing and enables uniform feeding and mixing of the two reaction media upon entering the reaction tank, while saving stirring time.
[0040] For the implementation of the first outlet and the second outlet, please refer to the following embodiments.
[0041] Example 1
[0042] like Figure 1-4 As shown, the first reaction medium conveying mechanism includes a first annular pipe 201, which is connected to a first inlet pipe 202 and multiple first branch pipes 203. The first reaction medium can be conveyed into the first annular pipe 201 through the first inlet pipe 202, and then enter each of the first branch pipes 203 through the first annular pipe 201. The multiple first branch pipes 203 are evenly arranged around the circumference of the reaction tank 101, with a gap between each first branch pipe 203. The first branch pipes 203 extend axially along the reaction tank 101, and each first branch pipe 203 has a first outlet (not shown in the figure) provided at intervals along the extension direction of the first branch pipe 203.
[0043] Similarly, the second reaction medium conveying mechanism includes a second annular pipe 301, which is connected to a second inlet pipe 302 and multiple second branch pipes 303. The second reaction medium can be conveyed into the second annular pipe 301 through the second inlet pipe 302, and then into each of the second branch pipes 303 through the second annular pipe 301. The multiple second branch pipes 303 are evenly arranged around the circumference of the reaction tank 101, with a gap between each second branch pipe 303. Figure 4 As shown, the first branch pipe 203 and the second branch pipe 303 are arranged alternately. The second branch pipe 303 extends axially along the reaction vessel 101, and a second outlet 104 is provided alternately on each second branch pipe 303 along the extension direction of the second branch pipe 303.
[0044] To ensure that the distances from the first outlet to the centerline of the reactor are approximately equal to those from the second outlet, the distances from the first branch pipe 203 to the centerline of the reactor must also be approximately equal to those from the second branch pipe 303. As an optional implementation, the diameter D1 of the first annular pipe 201 is larger than the diameter D2 of the second annular pipe 301. Furthermore, the second branch pipe 303 is connected to the second annular pipe 301 via a transition pipe 303-1. This ensures that the distances from the first branch pipe 203 to the centerline of the reactor are also approximately equal to those from the second branch pipe 303.
[0045] As an optional embodiment, a heat exchange mechanism can also be provided to utilize the heat generated during the mixing and reaction of the two reaction media. Specifically, such as Figure 1As shown, an outer tank 401 is installed on the outside of the reaction tank 101, and a heat exchange cavity 402 is formed between the inner wall of the outer tank 401 and the outer wall of the reaction tank 101. The outer tank 401 is provided with a heat exchange medium inlet 403 and a heat exchange medium outlet 404, which are connected to the heat exchange cavity 402. The heat exchange medium enters the heat exchange cavity 402 through the heat exchange medium inlet 403. The heat generated by the reaction in the reaction cavity 102 is exchanged with the heat exchange medium through the tank body of the reflective tank 101, and the heat exchange medium flows out through the heat exchange medium outlet 404 after heat exchange.
[0046] Preferably, the reaction vessel outlet pipe 103 is located at the bottom of the reaction vessel 101, while the heat exchange medium inlet 403 is located at the bottom and the heat exchange medium outlet 404 is located at the top, thereby improving the heat exchange efficiency.
[0047] Example 2
[0048] like Figure 5-6 As shown, a first cylinder 501, a second cylinder 502, and a third cylinder 503 are sequentially installed from the outside to the inside within the reaction chamber 102. The bottoms of the first cylinder 501, the second cylinder 502, and the third cylinder 503 are sealed to the inner wall of the reaction chamber 102, thereby forming a first flow channel 506 between the first cylinder 501 and the second cylinder 502, and a second flow channel 507 between the second cylinder 502 and the third cylinder 503. Both the first flow channel 506 and the second flow channel 507 are provided with inlets, through which the first reaction medium and the second reaction medium enter the first flow channel 506 and the second flow channel 507, respectively.
[0049] The second outlet 104 is located on the third cylinder 503 and is connected to the second flow channel 507. The second reaction medium in the second flow channel 507 can enter the reaction chamber 102 through the second outlet 104. Multiple sets of second outlets 104 are provided on the third cylinder 503, with each set of second outlets 104 arranged circumferentially around the third cylinder 503. Each outlet in each set of second outlets 104 is arranged axially around the third cylinder 503.
[0050] A connecting pipe 504 is installed between the second cylinder 502 and the third cylinder 503, and a transition channel 508 is formed inside the connecting pipe 504. A first outlet 105 is located on the third cylinder 503 and communicates with the transition channel 508. A transition outlet 505 is provided on the second cylinder 502, connecting the first channel 506 and the transition channel 508. The first reaction medium in the first channel 506 enters the transition channel 508 through the transition outlet 506, and then flows into the reaction chamber 102 through the first outlet 105. Multiple sets of first outlets 105 are provided on the third cylinder 503, with each set of first outlets 105 arranged alternately along the circumference of the third cylinder 503. Each outlet in each set of first outlets 105 is arranged alternately along the axial direction of the third cylinder 503.
[0051] In the circumference of the third cylinder 503, the first outlet 105 and the second outlet 104 are arranged alternately, so that the two reaction media can be fed and mixed evenly when they enter the reaction tank, while saving stirring time.
[0052] As an optional embodiment, a heat exchanger is installed inside the third cylinder 503, thereby utilizing the heat generated during the mixing and reaction of the two reaction media in the reaction chamber 102 for heat exchange. Specifically, as Figure 6-7 As shown, the heat exchanger includes an upper annular tube 405 and a lower annular tube 406, which are connected by multiple vertical tubes 407 arranged in a ring. One of the upper annular tube 405 and the lower annular tube 406 is connected to the heat exchange medium inlet, and the other is connected to the heat exchange medium outlet. The heat exchange medium enters from the heat exchange medium inlet and flows out from the heat exchange medium outlet.
[0053] As an optional embodiment, in order to further improve the reaction rate, a stirring blade and a driving mechanism for driving the stirring blade to rotate can also be provided. The driving mechanism can drive the stirring blade to rotate, thereby stirring the first reaction medium and the second reaction medium in the reaction chamber 102 through the stirring blade.
[0054] As an optional implementation, the diameters of the first outlet and the second outlet are 0.05 mm to 0.15 mm, for example, 0.1 mm, so that the flow rates of the first reaction medium and the second reaction medium can be controlled, which is beneficial to the uniform mixing and reaction of the two reaction media.
[0055] The present invention and its embodiments have been described above illustratively. This description is not restrictive, and the figures shown are only one embodiment of the present invention; the actual structure is not limited thereto. Therefore, if those skilled in the art are inspired by this description and design similar structures and embodiments without departing from the inventive spirit of the present invention, such designs should fall within the protection scope of the present invention.
Claims
1. A uniformly fed mixing reactor, comprising a reaction vessel (101), the reaction vessel (101) being provided with a reaction chamber (102) and connected to a reaction vessel outlet pipe (103); Its features are: The reaction chamber (102) is equipped with a first reaction medium conveying mechanism and a second reaction medium conveying mechanism; The first reaction medium conveying mechanism is provided with multiple sets of first outlets, and the second reaction medium conveying mechanism is provided with multiple sets of second outlets; Each group of first outlets and each group of second outlets includes multiple outlets arranged along the axial direction of the reaction vessel; In the circumferential direction of the reaction vessel (101), each group of first outlets and each group of second outlets are arranged alternately; The distance between the first outlet and the center line of the reaction vessel is R1, and the distance between the second outlet and the center line of the reaction vessel is R2, where R1 = (0.98~1.02)R2.
2. The uniformly fed mixing reactor according to claim 1, characterized in that: The first reaction medium conveying mechanism includes a first annular pipe (201), which is connected to a first inlet pipe (202) and a plurality of first branch pipes (203); the plurality of first branch pipes (203) are evenly arranged around the reaction tank (101); the first branch pipes (203) extend axially along the reaction tank (101); and the first outlet is provided on the first branch pipes (203). The second reaction medium conveying mechanism includes a second annular pipe (301), which is connected to a second inlet pipe (302) and a plurality of second branch pipes (303); the plurality of second branch pipes (303) are evenly arranged around the reaction tank (101); the second branch pipes (303) extend axially along the reaction tank (101); and the second branch pipes (303) are provided with a second outlet (104).
3. The uniformly fed mixing reactor according to claim 2, characterized in that: The diameter D1 of the first annular tube (201) is larger than the diameter D2 of the second annular tube (301); The second branch pipe (303) is connected to the second annular pipe (301) through the transition pipe (303-1).
4. The uniformly fed mixing reactor according to claim 2, characterized in that: An outer tank (401) is installed on the outside of the reaction vessel (101), and a heat exchange chamber (402) is formed between the inner wall of the outer tank (401) and the outer wall of the reaction vessel (101); the outer tank (401) is provided with a heat exchange medium inlet (403) and a heat exchange medium outlet (404); The heat exchange medium inlet (403) and heat exchange medium outlet (404) are connected to the heat exchange cavity (402).
5. The uniformly fed mixing reactor according to claim 1, characterized in that: Inside the reaction chamber (102), a first cylinder (501), a second cylinder (502), and a third cylinder (503) are installed sequentially from the outside to the inside; a first flow channel (506) is formed between the first cylinder (501) and the second cylinder (502), and a second flow channel (507) is formed between the second cylinder (502) and the third cylinder (503); both the first flow channel (506) and the second flow channel (507) are provided with inlets; The second outlet (104) is located on the third cylinder (503), and the second outlet (104) is connected to the second flow channel (507); A connecting pipe (504) is also installed between the second cylinder (502) and the third cylinder (503), and a transition channel (508) is formed inside the connecting pipe (504); a first outlet (105) is provided on the third cylinder (503), and the first outlet (105) is connected to the transition channel (508); a transition outlet (505) is provided on the second cylinder (502), and the transition outlet (505) is used to connect the first channel (506) and the transition channel (508).
6. The uniformly fed mixing reactor according to claim 5, characterized in that: A heat exchanger is installed inside the third cylinder (503).
7. The uniformly fed mixing reactor according to claim 6, characterized in that: The heat exchanger includes an upper annular tube (405) and a lower annular tube (406); the upper annular tube (405) and the lower annular tube (406) are connected by a plurality of vertical tubes (407) arranged in a ring. One of the upper annular pipe (405) and the lower annular pipe (406) is connected to the heat exchange medium inlet, and the other is connected to the heat exchange medium outlet.
8. The uniformly fed mixing reactor according to any one of claims 1-5 and 7, characterized in that: It also includes stirring blades and a drive mechanism for rotating the stirring blades; The stirring blades are used to stir the first reaction medium and the second reaction medium in the reaction chamber (102).
9. The uniformly fed mixing reactor according to claim 1, characterized in that: The diameters of the first and second outlets are 0.05 mm to 0.15 mm.