Catalytic reaction module for producing hydrogen from methanol

By designing a catalytic reaction module in the methanol hydrogen production equipment, the catalyst is placed in multiple parallel reaction chambers, and the replacement process is simplified through modular design, which solves the problem of difficult catalyst replacement, achieving longer equipment operation time and higher economic benefits.

CN119656987APending Publication Date: 2025-03-21SICHUAN HEYI NEW ENERGY TECH CO LTD
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Patent Information

Application Number
CN202411114285.1
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2024-08-14
Publication Date
2025-03-21

AI Technical Summary

Technical Problem

It is difficult to replace catalysts in existing methanol hydrogen production equipment, resulting in unstable operation of the equipment and requires frequent catalyst replacement.

Method used

A catalytic reaction module is designed, and the catalyst is placed in multiple reaction chambers arranged in parallel. By controlling the flow direction of methanol steam and water vapor, the working state of the reaction chamber is switched, the catalyst replacement cycle is extended, and the catalyst replacement process is simplified through modular design.

Benefits of technology

It effectively extends the catalyst replacement cycle, reduces the difficulty of replacement, and improves the continuous working time and economic benefits of the equipment.

✦ Generated by Eureka AI based on patent content.

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Abstract

The catalytic reaction module comprises a supporting frame, a plurality of supporting plates are arranged on the supporting frame, and the supporting plates are arranged on the supporting frame; a reaction box is arranged on each supporting frame in a sliding manner, and a locking assembly matched with the reaction box is further arranged on each supporting plate; the reaction module further comprises an air inlet pipe and an exhaust pipe, one end of the air inlet pipe is communicated with an external air source, and the other end of the air inlet pipe is connected with the inlet end of each reaction box in parallel; one end of the exhaust pipe is connected with the hydrogen storage device, and the other end is connected in parallel with the outlet end of each reactor; a hydrogen sensor and a flow sensor are also arranged at the outlet end of each reaction box and are electrically connected with the controller respectively; independent packaging of the catalyst is achieved through the modularized reaction box, the catalyst can be replaced by replacing the whole reaction box, the reaction box can be filled with the catalyst again, reutilization is achieved, and the replacement efficiency of the catalyst is effectively improved.
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Description

Technical Field

[0001] The present application relates to the technical field of methanol hydrogen production equipment, and specifically to a catalytic reaction module for methanol hydrogen production. Background Art

[0002] Methanol hydrogen production is an important technical means for hydrogen production. In the prior art, methanol vapor and water vapor are generally generated by heating, and then the mixture of methanol vapor and water vapor is introduced into a reactor. A large number of reaction tubes are arranged in the reactor, and the reaction tubes are filled with catalysts. At the same time, heating oil is filled between the reaction tubes. Methanol vapor and water vapor enter from one end of the reaction tube and are converted into hydrogen under the action of the catalyst, and tail gas is discharged from the other end of the reaction tube.

[0003] After the equipment has been working for a period of time, some catalysts will begin to fail. In order to ensure the normal operation of the equipment, the failed catalysts need to be replaced regularly. However, in the prior art, the structure of the reaction tank is relatively closed, which makes it difficult to replace the catalyst. Summary of the invention

[0004] The main purpose of the present application is to provide a catalytic reaction module for producing hydrogen from methanol, aiming to solve the defect of the difficulty in replacing the catalyst in the prior art.

[0005] This application achieves the above objectives through the following technical solutions: A catalytic reaction module for producing hydrogen from methanol, comprising a support frame; A plurality of support plates, each of which is sequentially arranged on the support frame along the height direction of the support frame; a reaction box is slidably arranged on each of the support frames, and each of the support plates is also provided with a locking assembly adapted to the reaction box; An air inlet pipe, one end of which is connected to an external air source, and the other end of which is connected in parallel to the inlet ends of the reaction boxes; An exhaust pipe, one end of which is connected to the hydrogen storage device, and the other end of which is connected in parallel to the outlet ends of the reactors; A plurality of hydrogen sensors, each of which is disposed at the outlet end of each of the reaction boxes; a flow sensor is also disposed at the outlet end of each of the reaction boxes; A controller is electrically connected to each of the hydrogen sensors and each of the flow sensors.

[0006] Optionally, each of the support plates is provided with a plurality of slide rails, each of the slide rails is provided with a slide groove, and the reaction box is provided with rollers adapted to the slide groove.

[0007] Optionally, the locking assembly includes a locking rod and a locking sleeve, and along the sliding direction of the reaction box, limit frames are provided on both sides of the reaction box, and the locking rod is threadedly connected to the limit frames; the locking sleeve is provided on the reaction box.

[0008] Optionally, both the air inlet pipe and the exhaust pipe are sleeved with insulation pipes, and spiral guide plates are provided between the insulation pipe and the air inlet pipe, and between the insulation pipe and the exhaust pipe.

[0009] Optionally, the reaction box includes a box body, which is provided with an air inlet and an air outlet, and a plurality of guide plates are provided in the box body, each of the guide plates has an arc-shaped structure, and each of the guide plates is arranged in a concentric circle structure in the box body, and a filling cavity for placing a catalyst is provided between any two adjacent guide plates; a partition plate for separating the air inlet and the air outlet is also provided in the box body.

[0010] Optionally, a plurality of adjustment plates are provided in the filling cavity located on the inner side, each of the adjustment plates is provided with a vent hole, and the vent holes are staggered along the airflow direction.

[0011] Optionally, the support frame includes a plurality of support rods, and a connecting frame is provided on the top and bottom of each of the support rods; at least one of the support rods is provided with a plurality of adjustment seats for adjusting the height of the support plate, and the remaining support rods are provided with a sliding seat, and the sliding seat is provided with a fixing component.

[0012] Optionally, the adjustment seat includes a lifting sleeve and a support seat, the lifting sleeve is threadedly connected to the support rod; the lifting sleeve and the support seat are rotatably connected via a thrust ball bearing; and a limiting rod and a limiting hole that cooperate with each other are arranged between the support plate and the support seat.

[0013] Optionally, the fixing assembly includes a fixing screw, which is threadedly connected to the sliding seat, and the support rod is provided with a fixing groove adapted to the fixing screw.

[0014] Optionally, the reaction box further comprises a cover plate, the cover plate is provided with a plug-in slot, and the top of the box body is provided with a plug-in ring adapted to the plug-in slot; and a matching flange plate is further provided between the box body and the cover plate.

[0015] Compared with the prior art, this application has the following beneficial effects: The present application includes a support frame, on which a plurality of support plates are arranged, each of which is arranged in sequence on the support frame along the height direction of the support frame; a reaction box is slidably arranged on each of the support frames, and each of the support plates is also provided with a locking assembly adapted to the reaction box; the reaction module also includes an air inlet pipe and an exhaust pipe, one end of the air inlet pipe is connected to an external air source, and the other end of the air inlet pipe is respectively connected in parallel with the inlet end of each of the reaction boxes; one end of the exhaust pipe is connected to a hydrogen storage device, and the other end thereof is respectively connected in parallel with the outlet end of each of the reactors; at the same time, a hydrogen sensor and a flow sensor are also provided at the outlet end of each of the reaction boxes, and each of the hydrogen sensor and the flow sensor is respectively electrically connected to the controller.

[0016] Compared with the prior art, since the present application places the catalyst in several parallel-connected reaction boxes, the working state of the reaction boxes can be switched by controlling the flow direction of methanol vapor and water vapor, that is, in a low flow state, methanol vapor and water vapor are concentrated in some reaction boxes for catalytic hydrogen production, thereby protecting other reaction boxes, staggering the failure time of the catalysts, avoiding the synchronous failure of all catalysts, and effectively extending the catalyst replacement cycle, thereby extending the continuous working time of the equipment and improving the economic benefits of the equipment; Secondly, all catalysts are encapsulated in a modular reaction box, and the reaction box is a detachable structure. In the prior art, the reaction tube filled with catalysts is fixed in the reaction tank, and the catalyst can only be replaced by hollowing out the reaction tube by a drill or other equipment. However, in the present application, when replacing the catalyst, the reaction box is replaced together, which makes the replacement of the catalyst more convenient, reduces the difficulty of replacing the catalyst, improves the replacement efficiency, avoids the long-term shutdown of the equipment for replacing the catalyst, and is conducive to improving the operation time of the equipment and the economic efficiency of the equipment; Finally, for the replaced reaction boxes, the present application can centrally remove and reload the catalysts without causing the catalysts to scatter, which is not only beneficial to improving the environmental sanitation of the working area, but also reduces the difficulty of reloading the catalysts, which is beneficial to improving the efficiency of catalyst replacement, avoiding long-term shutdown of equipment for catalyst replacement, and improving the operating time of the equipment and the economic efficiency of the equipment. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] Figure 1 A schematic structural diagram of a catalytic reaction module for producing hydrogen from methanol provided in Embodiment 1 of the present application; Figure 2 A front view of a catalytic reaction module for producing hydrogen from methanol provided in Embodiment 1 of the present application; Figure 3 This is an exploded view of the reaction box; Figure 4 is a cross-sectional view of a reaction box; Figure 5 It is a schematic diagram of the structure of an intake pipe or an exhaust pipe; Figure 6 This is a schematic diagram of the assembly of the adjustment seat;

[0018] Figure numerals: 1-support frame, 2-support plate, 3-reaction box, 4-intake pipe, 5-exhaust pipe, 6-hydrogen sensor, 7-flow sensor, 8-controller, 9-slide rail, 10-slide groove, 11-roller, 12-locking rod, 13-locking sleeve, 14-limiting frame, 15-insulation pipe, 16-spiral guide plate, 17-slide seat, 18-lifting sleeve, 19-support seat, 20- Thrust ball bearing, 21-limit rod, 22-limit hole, 23-fixing screw, 24-fixing groove, 101-support rod, 102-connecting frame, 301-box, 302-air inlet, 303-air outlet, 304-guide plate, 305-filling cavity, 306-dividing plate, 307-adjusting plate, 308-vent, 309-cover plate, 310-plug-in groove, 311-plug-in ring.

[0019] The purpose, features and advantages of this application will be further described in conjunction with embodiments and with reference to the accompanying drawings. DETAILED DESCRIPTION

[0020] The following will be combined with the drawings in the embodiments of the present invention to clearly and completely describe the technical solutions in the embodiments of the present invention. Obviously, the described embodiments are only part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

[0021] It should be noted that all directional indications (such as up, down, left, right, front, back, etc.) in the embodiments of the present invention are only used to explain the relative position relationship, movement status, etc. between the components under a certain specific posture (as shown in the accompanying drawings). If the specific posture changes, the directional indication will also change accordingly.

[0022] In the present invention, unless otherwise clearly specified and limited, the terms "connection", "fixation", etc. should be understood in a broad sense. For example, "fixation" 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 the internal connection of two elements or the interaction relationship between two elements, unless otherwise clearly defined. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0023] In addition, if there are descriptions involving "first", "second", etc. in the embodiments of the present invention, the descriptions of "first", "second", etc. are only used for descriptive purposes and cannot be understood as indicating or implying their relative importance or implicitly indicating the number of technical features indicated. Therefore, the features defined as "first" and "second" may explicitly or implicitly include at least one of the features. In addition, the meaning of "and / or" appearing in the full text includes three parallel schemes. Taking "A and / or B" as an example, it includes scheme A, or scheme B, or a scheme that satisfies both A and B. In addition, the technical solutions between the various embodiments can be combined with each other, but it must be based on the ability of ordinary technicians in the field to implement. When the combination of technical solutions is contradictory or cannot be implemented, it should be deemed that such a combination of technical solutions does not exist and is not within the scope of protection required by the present invention.

[0024] Implementation Method 1 Reference Figures 1 to 6 This embodiment is an optional embodiment of the present application, which discloses a catalytic reaction module for producing hydrogen from methanol, including a support frame 1, wherein the support frame 1 includes a plurality of support rods 101, preferably, three support rods 101 are preferably used, and each support rod 101 is arranged in a triangular structure, and a connecting frame 102 is also provided at the top and bottom of the support rod 101, and each support rod 101 is connected by the connecting frame 102 to ensure the stability of the structure; The support frame 1 further includes a plurality of support plates 2, which are distributed in sequence along the height direction of the support frame 1 and are respectively connected to the frame body; It should be noted that the number of support plates 2 can be flexibly adjusted as needed to more fully utilize the internal space of the tank; In the above structure, each reaction box 3 is arranged in sequence in the height direction, which not only makes higher use of the space in the tank body, but also can effectively control the length of the airflow path, thereby avoiding the occurrence of long-distance invalid paths, ensuring that the hydrogen produced by catalysis can be discharged at the fastest speed, thereby improving the hydrogen production efficiency of the equipment.

[0025] An adjustment seat is provided on at least one support rod 101, and a slide seat 17 is slidably provided on the other support rods 101, wherein the adjustment seat includes a lifting sleeve 18 and a support seat 19, and the lifting sleeve 18 is threadedly connected to the support rod 101; the lifting sleeve 18 is rotatably connected to the support seat 19 through a thrust ball bearing 20; a mounting hole is provided on the support plate 2, and the support seat 19 is inserted into the mounting hole, and a limiting rod 21 is provided on the support plate 2, and a limiting hole 22 is provided on the support seat 19, and the limiting rod 21 is inserted into the limiting hole 22; The slide 17 is a round structure, and the slide 17 is slidably sleeved on the support rod 101. A fixing assembly is also provided between the slide 17 and the support rod 101, and the fixing assembly includes a fixing screw 23, and the fixing screw 23 is threadedly connected to the slide 17. A fixing groove 24 adapted to the fixing screw 23 is provided on the support rod 101; When in use, loosen the fastening screw, and then rotate the lifting sleeve 18 to control the height of the entire adjustment seat, and the change in the height position of the adjustment seat will drive the support plate 2 to rise or fall. After adjusting to the right position, the support plate 2 can be fixed by the fixing screw 23; The above structure can facilitate the staff to adjust the position of the support plate 2 according to the needs, especially when assembling the equipment, the position of the support plate 2 can be quickly adjusted through the above device, thereby improving the assembly accuracy and reducing the requirements for the equipment production accuracy; Secondly, through the above arrangement, the arrangement of the support plate 2 can be made more compact, and during the disassembly and assembly process, the gap between two adjacent support plates 2 can be effectively expanded, which facilitates the removal and installation of the reaction box 3 to accommodate more reaction boxes 3; Finally, since the position of the support plate 2 can be adjusted, in actual use, the reaction boxes 3 of different specifications can be replaced according to needs, thereby providing reaction boxes 3 with different catalytic capabilities to meet different usage requirements.

[0026] A reaction box 3 is disposed on each of the support plates 2. The reaction box 3 includes a box body 301 and a cover plate 309. An air inlet 302 and an air outlet 303 are also disposed on the box body 301. The reaction box 3 is an annular structure as a whole, and the central cavity is a heating chamber. The setting of the heating chamber can, on the one hand, expand the contact surface between the reaction box 3 and the heat exchange medium such as heating oil, thereby improving the heat transfer efficiency; on the other hand, the heating chamber can guide the heat exchange medium such as heating oil to enter the middle area of ​​the reaction box 3, thereby heating the heating box of the annular structure in both the inner and outer directions, which can effectively avoid the heating blind area, improve the uniformity of the temperature in the reaction box 3, and ensure the efficiency of catalytic hydrogen production; A plurality of guide plates 304 are also arranged in the box body 301. The guide plates 304 are arranged in an arc-shaped structure. The arc of each guide plate 304 is preferably 250°-270°. The radius of each guide plate 304 increases successively. With the center of the box body 301 as the center point, each guide ring is arranged in a concentric circle structure. Between two adjacent guide plates 304 is a filling area, which is filled with a catalyst. The arc of 250°-270° can ensure that an empty area is formed in the box body 301. A partition is arranged in the above-mentioned empty area. The two ends of the partition are respectively connected to the inner walls of the two sides of the box body 301. The box body 301 is also provided with an air inlet 302 and an air outlet 303. The air inlet 302 and the air outlet 303 are both connected to the air pipe. At the same time, the air inlet pipe 4 and the air outlet pipe are respectively arranged on both sides of the partition; The above-mentioned vacant area is divided into two parts separated from each other by a partition, and the two areas are respectively connected to the inlet and outlet of each filling area; at the same time, the air inlet 302 is isolated from the air outlet 303 by the setting of the partition, so that the gas can only be discharged after rotating around the axis of the box body 301 for one circle, thereby ensuring that the methanol vapor and water vapor can only flow along the prescribed path in the box body 301, ensuring their retention time, and preventing a large amount of methanol vapor and water vapor from mixing into the tail gas, thereby ensuring the recovery rate of hydrogen; In the above structure, the guide plates 304 arranged in a concentric circle structure can be used to set up several airflow channels in parallel in the box 301. On the one hand, the contact area between the catalyst and the methanol vapor is increased, which is beneficial to improving the catalytic reaction efficiency; on the other hand, the airflow can be more reasonably distributed to ensure that the catalysts in different areas have high-concentration methanol vapor passing through, thereby avoiding the accumulation of methanol vapor at the inlet end. Finally, the above structural arrangement can more reasonably utilize the space in the reaction box 3 and improve the efficiency of catalytic hydrogen production.

[0027] It should be noted that in the above technical solution, one or two filling areas can be combined by setting a closed outlet and setting a new opening, so as to form a maze-like airflow path in the box 301, thereby ensuring the retention time of the airflow in the box 301 and ensuring the recovery rate of hydrogen; The cover plate 309 is provided with a plug-in slot 310 on one side that is in contact with the box body 301. The top surface of the box body 301 is provided with a plug-in ring 311 that matches the plug-in slot 310. The plug-in ring 311 is inserted into the plug-in slot 310. A filling rubber sealing ring is also provided in the plug-in slot 310 to achieve sealing of small gaps. A matching flange plate is also provided between the cover plate 309 and the box body 301, and the flange plates are connected by connecting bolts; At the same time, a sealing gasket is also arranged inside the plug-in slot 310. The shape of the sealing gasket is exactly the same as the distribution of the guide plate 304. After installation, the sealing gasket is located between the cover plate 309 and the guide plate 304, thereby sealing the gap between the cover plate 309 and the guide plate 304 to prevent gas from flowing from the top of the guide plate 304, ensuring that gases such as methanol vapor can only move along a specified route; Furthermore, in the filling area located on the inner side, since it is close to the center of the box body 301, its radius is smaller and its path is shorter. Therefore, in order to ensure the catalytic conversion efficiency, baffles can be further provided in the above-mentioned filling area. The baffles are staggered to form an S-shaped airflow path, thereby ensuring that the airflow paths in different channels are basically equal and the hydrogen recovery rate is ensured. The above-mentioned arrangement has a simple structure and low cost.

[0028] Two mutually parallel slide rails 9 are arranged on each of the support plates 2, and a slide groove 10 is arranged on each of the two slide rails 9. A roller 11 is arranged at the bottom of the box body 301 of the reaction box 3, and the roller 11 is inserted into the slide groove 10. At the same time, a guide block is also arranged at the outlet end of the slide groove 10, and the top surface of the guide block is arranged obliquely; A locking assembly is also provided between the reaction box 3 and the support plate 2, and the locking assembly includes a locking rod 12 and a locking sleeve 13. Along the sliding direction of the reaction box 3, both sides of the reaction box 3 are provided with a limiting frame 14, and the locking rod 12 is threadedly connected to the limiting frame 14; the locking sleeve 13 is provided on the reaction box 3; The above-mentioned structural setting enables the reaction box 3 to have a certain sliding ability. When removing the reaction box 3 or reinstalling the reaction box 3, the reaction box 3 can be pulled or pushed, which makes the installation easier and labor-saving, and is conducive to improving work efficiency.

[0029] Furthermore, the catalytic reaction module further includes an air inlet pipe 4 and an air outlet pipe, one end of the air inlet pipe 4 is connected to an external gas source, and the other end of the air inlet pipe 4 is respectively connected in parallel with the inlet end of each of the reaction boxes 3; one end of the exhaust pipe 5 is connected to a hydrogen storage device, and the other end thereof is respectively connected in parallel with the outlet end of each of the reactors; A hydrogen sensor 6 and a flow sensor 7 are provided at the outlet end of the reaction box 3 . The catalytic reaction module further comprises a controller 8 . The controller 8 is electrically connected to each of the hydrogen sensors 6 and each of the flow sensors 7 .

[0030] At the same time, an insulation pipe 15 is sleeved on the air inlet pipe 4 and the air outlet pipe, and a spiral guide plate 16 is arranged between the insulation pipe 15 and the air inlet pipe 4, and between the insulation pipe 15 and the exhaust pipe 5; With the above-mentioned structural arrangement, the air inlet pipe 4 and the air outlet pipe can be arranged outside the tank body, and the hydrogen sensor 6 and the flow sensor 7 can also be arranged outside the tank body, thereby avoiding the adverse effect of the heat exchange medium on the sensor; At the same time, the above arrangement can also avoid too many pipelines inside the tank, reducing the difficulty of equipment maintenance and disassembly; At the same time, the heat preservation pipe 15 can be used to insulate the external air inlet pipe 4 and the air outlet pipe and recover heat, which is not only beneficial to ensure the temperature of the mixed gas, but also beneficial to reduce the energy consumption of the equipment; The parameters of the hydrogen sensor 6 and the flow sensor 7 can accurately monitor the hydrogen recovery rate at the outlet, which is not only conducive to improving the monitoring capability of the working state of the equipment; at the same time, under the condition of uninterrupted mixed gas at the inlet, if the hydrogen recovery rate at the outlet is significantly reduced, it can be determined that the catalyst in the reaction box 3 is invalid and needs to be replaced; At this time, the controller 8 will issue an instruction to replace the catalyst, and quickly determine the specific reaction box 3 according to the position of the hydrogen sensor 6, helping the staff to quickly locate the failed reaction box 3 and improve the maintenance efficiency; Secondly, while issuing an alarm, the controller 8 can also shut down the reaction box 3, on the one hand to avoid the waste of reaction raw gases such as methanol vapor and water vapor, and on the other hand to avoid a large amount of methanol vapor and water vapor being directly discharged into the tail gas without conversion, thereby ensuring the stability of the hydrogen recovery rate.

[0031] The above are only preferred embodiments of the present application, and are not intended to limit the patent scope of the present application. Any equivalent structure or equivalent process transformation made using the contents of the present application specification and drawings, or directly or indirectly applied in other related technical fields, are also included in the patent protection scope of the present application.

Claims

1. A catalytic reaction module for producing hydrogen from methanol, characterized in that: It comprises a support frame (1); A plurality of support plates (2), each of the support plates (2) being arranged on the support frame (1) in sequence along the height direction of the support frame (1); a reaction box (3) being slidably arranged on each of the support frames (1), and a locking assembly adapted to the reaction box (3) being also arranged on each of the support plates (2); An air inlet pipe (4), one end of the air inlet pipe (4) being in communication with an external air source, and the other end of the air inlet pipe (4) being respectively connected in parallel with the inlet ends of the reaction boxes (3); An exhaust pipe (5), one end of which is connected to the hydrogen storage device, and the other end of which is connected in parallel to the outlet ends of each of the reactors; A plurality of hydrogen sensors (6), each of the hydrogen sensors (6) being arranged at an outlet end of each of the reaction boxes (3); a flow sensor (7) is also arranged at the outlet end of each of the reaction boxes (3); A controller (8), wherein the controller (8) is electrically connected to each of the hydrogen sensors (6) and each of the flow sensors (7).

2. A catalytic reaction module for producing hydrogen from methanol according to claim 1, characterized in that: A plurality of slide rails (9) are arranged on each of the support plates (2), a slide groove (10) is arranged on each of the slide rails (9), and a roller (11) adapted to the slide groove (10) is arranged on the reaction box (3).

3. A catalytic reaction module for producing hydrogen from methanol according to claim 1 or 2, characterized in that: The locking assembly comprises a locking rod (12) and a locking sleeve (13); along the sliding direction of the reaction box (3), both sides of the reaction box (3) are provided with limiting frames (14); the locking rod (12) is threadedly connected to the limiting frames (14); and the locking sleeve (13) is arranged on the reaction box (3).

4. A catalytic reaction module for producing hydrogen from methanol according to claim 1, characterized in that: The air intake pipe (4) and the exhaust pipe (5) are both sleeved with an insulation pipe (15), and a spiral guide plate (16) is provided between the insulation pipe (15) and the air intake pipe (4), and between the insulation pipe (15) and the exhaust pipe (5).

5. The catalytic reaction module for producing hydrogen from methanol according to claim 1, characterized in that: The reaction box (3) comprises a box body (301), the box body (301) is provided with an air inlet (302) and an air outlet (303), a plurality of guide plates (304) are provided in the box body (301), each of the guide plates (304) is in an arc-shaped structure, and each of the guide plates (304) is arranged in a concentric circle structure in the box body (301), and a filling cavity (305) for placing a catalyst is provided between any two adjacent guide plates (304); a partition plate (306) for separating the air inlet (302) and the air outlet (303) is also provided in the box body (301).

6. A catalytic reaction module for producing hydrogen from methanol according to claim 5, characterized in that: A plurality of adjustment plates (307) are arranged in the filling cavity (305) located on the inner side, and each of the adjustment plates (307) is provided with a vent hole (308). The vent holes (308) are arranged in a staggered manner along the airflow direction.

7. The catalytic reaction module for producing hydrogen from methanol according to claim 1, characterized in that: The support frame (1) comprises a plurality of support rods (101), and a connecting frame (102) is provided at the top and the bottom of each of the support rods (101); at least one of the support rods (101) is provided with a plurality of adjustment seats for adjusting the height of the support plate (2), and the remaining support rods (101) are provided with a sliding seat (17), and a fixing component is provided on the sliding seat (17).

8. A catalytic reaction module for producing hydrogen from methanol according to claim 7, characterized in that: The adjustment seat comprises a lifting sleeve (18) and a support seat (19); the lifting sleeve (18) is threadedly connected to the support rod (101); the lifting sleeve (18) and the support seat (19) are rotatably connected via a thrust ball bearing (20); and a limiting rod (21) and a limiting hole (22) that cooperate with each other are provided between the support plate (2) and the support seat (19).

9. A catalytic reaction module for producing hydrogen from methanol according to claim 7, characterized in that: The fixing assembly comprises a fixing screw (23), the fixing screw (23) being threadedly connected to the slide seat (17), and a fixing groove (24) adapted to the fixing screw (23) is provided on the support rod (101).

10. The catalytic reaction module for producing hydrogen from methanol according to claim 5, characterized in that: The reaction box (3) further comprises a cover plate (309), a plug-in slot (310) is arranged on the cover plate (309), and a plug-in ring (311) adapted to the plug-in slot (310) is arranged on the top of the box body (301); a flange plate which cooperates with each other is also arranged between the box body (301) and the cover plate (309).