Double-tower reactor for hydrogen production process

Abstract

The utility model provides a double-tower reactor for a hydrogen production process, which comprises two reaction towers, the reaction towers on two sides are symmetrically arranged in position, two supporting bottom plates are fixedly arranged at the bottoms of the reaction towers, the supporting bottom plates on two sides are symmetrically arranged in position, and the supporting bottom plates on two sides play a role in stable supporting. According to the scheme, the production efficiency of the hydrogen production process can be improved by switching the serial connection mode and the parallel connection mode of the double towers, the hydrogen quality in hydrogen production is improved, the supporting control stability of the adjusting control pipe can be improved through the supporting plate, the adjusting control pipe can be conveniently and directly disassembled after use, and the production cost is reduced. At the moment, the reaction towers on the two sides can be directly and independently used after being disassembled, and assembling and disassembling are very convenient and fast.

Description

Technical Field

[0001] The utility model relates to the technical field of hydrogen production reaction towers, in particular to a double-tower reactor for a hydrogen production process. Background Art

[0002] Double-tower parallel reaction tower hydrogen production is an advanced hydrogen production process that uses two reaction towers to achieve efficient and low-cost hydrogen production.

[0003] The existing dual-tower parallel reaction towers can only carry out synchronous hydrogen production in parallel. If the hydrogen production reaction efficiency is low, the synchronous dual-tower hydrogen production will instead cause poor-quality hydrogen to be produced and exported, which leads to a waste of resources. Utility Model Content

[0004] 1. Technical issues to be solved

[0005] In view of the deficiencies in the prior art, the utility model provides a double-tower reactor for a hydrogen production process, which solves the problems raised in the above-mentioned background technology.

[0006] (II) Technical solution

[0007] To achieve the above objectives, the utility model is implemented through the following technical solutions: a double-tower reactor for a hydrogen production process, comprising two reaction towers, the reaction towers on both sides are symmetrically arranged, two supporting bottom plates are fixedly provided at the bottom of the reaction towers, the supporting bottom plates on both sides are symmetrically arranged, and the supporting bottom plates on both sides have a stable supporting effect, a material interface is fixedly provided at the top of the reaction tower, and a pressure gauge is fixedly provided at the top of the reaction tower and on one side of the material interface.

[0008] Preferably, the top and side surfaces of the material interface are respectively connected with material input pipelines.

[0009] Preferably, the outer walls of the reaction towers on both sides are connected to each other and are provided with two heat pipe interfaces, and the positions of the heat pipe interfaces on both sides are symmetrical up and down.

[0010] Preferably, a reaction chamber is provided in the reaction tower, and a plurality of reaction tubes are vertically installed in the reaction chamber, and the reaction tubes are arranged in a matrix.

[0011] Preferably, an output pipe opening is connected to the lower wall of the reaction chamber, and output pipes are connected to the bottom and side surfaces of the output pipe opening.

[0012] Preferably, a support plate is horizontally arranged between the tops of the reaction towers on both sides, an adjusting control tube is vertically installed in the support plate, and the upper and lower end surfaces of the adjusting control tube are respectively connected with diversion interfaces.

[0013] Preferably, both sides of the diversion interface at the top are connected to the material input pipeline at one side, and both sides of the diversion interface at the bottom are connected to the output pipeline at one side.

[0014] (III) Beneficial effects

[0015] The utility model provides a double-tower reactor for hydrogen production process, which has the following beneficial effects:

[0016] 1. This solution can improve the efficiency of hydrogen production process and the quality of hydrogen in hydrogen production by switching the series and parallel modes of the double towers.

[0017] 2. This solution can improve the support and control stability of the regulating control tube through the support plate, and can facilitate the direct disassembly of the regulating control tube after use. At this time, the reaction towers on both sides can also be directly disassembled and used independently, and assembly and disassembly are very convenient. BRIEF DESCRIPTION OF THE DRAWINGS

[0018] Figure 1 This is a schematic diagram of the appearance structure of the utility model;

[0019] Figure 2 This is a schematic diagram of the main structure of the utility model;

[0020] Figure 3 It is a side view structural schematic diagram of the utility model;

[0021] Figure 4 For this utility model Figure 3 Cross-sectional view along the AA direction.

[0022] In the figure: 101, reaction tower; 102, heat pipe interface; 103, support base plate; 104, adjustment control tube; 105, pressure gauge; 106, material interface; 107, diversion interface; 108, support plate; 109, material input pipeline; 110, output pipe outlet; 111, reaction chamber; 112, reaction tube; 113, output pipeline. DETAILED DESCRIPTION

[0023] The utility model embodiment provides a double tower reactor for hydrogen production process, such as Figure 1-4 As shown, two reaction towers 101 are included. The reaction towers 101 on both sides are symmetrically arranged. Two supporting bottom plates 103 are fixedly arranged at the bottom of the reaction tower 101. The supporting bottom plates 103 on both sides are symmetrically arranged. The supporting bottom plates 103 on both sides have the effect of stable support. A material interface 106 is fixedly arranged at the top of the reaction tower 101. A barometer 105 is fixedly arranged at the top of the reaction tower 101 and located on one side of the material interface 106.

[0024] It should be further explained that the barometer 105 is a barometer in the prior art, which is used to detect the air pressure value in the reaction tower 101.

[0025] Furthermore, the top and side of the material interface 106 are respectively connected to material input pipelines 109, and the material input pipelines 109 on both sides are inlets for different hydrogen production raw materials.

[0026] Furthermore, two heat pipe interfaces 102 are provided on the outer walls of the reaction towers 101 on both sides, and the positions of the heat pipe interfaces 102 on both sides are symmetrical up and down.

[0027] It should be further explained that a shell side module is provided in the shell of the reaction tower 101, the shell side module inlet is connected to the lower heat pipe interface 102, and the shell side module outlet is connected to the upper heat pipe interface 102.

[0028] Furthermore, a reaction chamber 111 is provided in the reaction tower 101 , and a plurality of reaction tubes 112 are vertically installed in the reaction chamber 111 , and the reaction tubes 112 are arranged in a matrix.

[0029] Furthermore, an output nozzle 110 is connected to the lower wall of the reaction chamber 111 , and an output pipe 113 is connected to the bottom and the side of the output nozzle 110 .

[0030] Furthermore, a support plate 108 is horizontally arranged between the tops of the reaction towers 101 on both sides, and an adjustment control tube 104 is vertically installed in the support plate 108 . The upper and lower end surfaces of the adjustment control tube 104 are respectively connected with diversion interfaces 107 .

[0031] Furthermore, both sides of the top flow diversion interface 107 are connected to the material input pipeline 109 on one side, and both sides of the bottom flow diversion interface 107 are connected to the output pipeline 113 on one side.

[0032] It should be further explained that the connecting pipes on each side are controlled by control valves.

[0033] When using this solution, first move the reaction towers 101 on both sides to a reasonable working position, and use the supporting base plate 103 at the bottom to provide a stable support effect. At this time, connect the two sides of the top diversion interface 107 with the material input pipeline 109 on one side, and connect the two sides of the bottom diversion interface 107 with the output pipeline 113 on one side. At this time, connect the heat pipe interface 102 on one side of the reaction towers 101 on both sides to the workshop heat transfer oil pipe. The lower heat pipe interface 102 is the heat transfer oil pipe input port, and the upper heat pipe interface 102 is the heat transfer oil pipe output port.

[0034] Subsequently, the top of the material input pipeline 109 is connected to the material input pipeline, and the material is input into the reaction tube 112 in the reaction chamber 111. At the same time, the heat transfer oil enters 101 through the heat pipe interface 102, and after passing through the shell side in 101, heat exchange is performed and output to the outside. After the reaction, the produced hydrogen is discharged to the outside through the output pipe port 110.

[0035] At this time, when the efficiency of the hydrogen production reaction is low, the control valve in the control tube 104 is switched, and the material gas output through the output pipe port 110 at the bottom is refluxed to the material interface 106 at the top of the reaction tower 101 on one side through the diversion interface 107, and continues to be input into the reaction chamber 111 for secondary reaction, and then the reaction towers 101 on both sides are connected in series to complete the series tower reaction, thereby improving the quality of the output hydrogen and meeting the requirements of the production process.

[0036] After a period of reaction, when it is detected that the reaction efficiency is high, the control valve in the control tube 104 is adjusted to switch. At this time, the reaction towers 101 on both sides form a parallel mode and carry out hydrogen production reaction at the same time, thereby improving the efficiency of the hydrogen production process in the reaction tower.

[0037] At the same time, by switching control of the adjustment control tube 104, the series-parallel relationship between the reaction towers 101 on both sides can be better completed, the process production of the hydrogen production reaction can be completed more reasonably and intelligently, and the support and control stability of the adjustment control tube 104 can be improved through the support plate 108. After use, the adjustment control tube 104 can be directly disassembled. At this time, the reaction towers 101 on both sides can also be directly disassembled and used independently, and assembly and disassembly are very convenient.

[0038] Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and variations may be made to the embodiments without departing from the principles and spirit of the present invention, and that the scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A double tower reactor for a hydrogen production process, characterized in that: The invention comprises two reaction towers (101), wherein the reaction towers (101) on both sides are symmetrically arranged, two supporting bottom plates (103) are fixedly arranged at the bottom of the reaction tower (101), and the supporting bottom plates (103) on both sides are symmetrically arranged, a material interface (106) is fixedly arranged at the top of the reaction tower (101), and a pressure gauge (105) is fixedly arranged at the top of the reaction tower (101) and located on one side of the material interface (106); A support plate (108) is horizontally arranged between the tops of the reaction towers (101) on both sides, an adjustment control tube (104) is vertically installed in the support plate (108), and the upper and lower end surfaces of the adjustment control tube (104) are respectively connected to flow diversion interfaces (107).

2. A double tower reactor for hydrogen production process according to claim 1, characterized in that: The top and side of the material interface (106) are respectively connected to a material input pipeline (109).

3. A double tower reactor for hydrogen production process according to claim 1, characterized in that: The outer walls of the reaction towers (101) on both sides are connected to each other and are provided with two heat pipe interfaces (102), and the positions of the heat pipe interfaces (102) on both sides are symmetrical up and down.

4. A double tower reactor for hydrogen production process according to claim 2, characterized in that: A reaction chamber (111) is provided in the reaction tower (101), and a plurality of reaction tubes (112) are vertically installed in the reaction chamber (111), wherein the reaction tubes (112) are arranged in a matrix.

5. A double tower reactor for hydrogen production process according to claim 4, characterized in that: The lower wall of the reaction chamber (111) is connected to an output pipe opening (110), and the bottom and side surfaces of the output pipe opening (110) are respectively connected to output pipes (113).

6. A double tower reactor for hydrogen production process according to claim 5, characterized in that: Both sides of the flow diversion interface (107) at the top are in communication with the material input pipeline (109) at one side, and both sides of the flow diversion interface (107) at the bottom are in communication with the output pipeline (113) at one side.

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