Gas purification equipment

By introducing automatically switching adsorption containers and components into the gas purification equipment, the problem of continuous production after the adsorption material becomes saturated is solved, improving the efficiency of gas purification and the lifespan of the adsorbent, and ensuring the stability of the system and the durability of the materials.

CN223980310UActive Publication Date: 2026-03-10SHANGHAI VISION ENERGY TECH CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2025-04-07
Publication Date
2026-03-10

AI Technical Summary

Technical Problem

Existing gas purification equipment requires shutdown after the adsorption material becomes saturated, making continuous production impossible. Furthermore, the adsorption material is easily pulverized under the impact of airflow, resulting in low molecular sieve utilization and reduced purification performance.

Method used

A gas purification device comprising first and second adsorption containers is designed. The saturation state of the adsorption material is monitored by a flow meter, and the container is switched for regeneration and purification. The automatic switching of the container is achieved by using adjustable inlet, purified gas and exhaust gas discharge components. Combined with energy release and compression components, the friction and pulverization of the adsorption material are reduced.

Benefits of technology

This technology enables efficient switching and regeneration of the adsorption container, improves the recovery efficiency of gas purification and the service life of the adsorbent, and ensures stable system operation and material durability.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses gas purification equipment, which belongs to the technical field of gas purification and comprises a first pipeline, a flow meter and an analyzer are mounted on the first pipeline; the first pipeline is connected with an adjustable air inlet assembly; the air outlet end of the adjustable air inlet assembly is connected with a first adsorption container and a second adsorption container, and the first adsorption container and the second adsorption container are the same in structure; the input ends of the first adsorption container and the second adsorption container are both connected with an adjustable regeneration gas assembly for regeneration gas to enter; the gas outlet ends of the first adsorption container and the second adsorption container are connected with an adjustable purified gas discharge assembly for discharging purified gas and a waste gas discharge assembly for discharging waste gas. According to the mode, the system is simple in structure, convenient to operate, suitable for various industrial gas production scenes and capable of achieving efficient and accurate operation, and the operation stability of the system is improved.
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Description

Technical Field

[0001] This utility model relates to the field of gas purification technology, and specifically to a gas purification device. Background Technology

[0002] Nitrogen, oxygen, argon, and helium purification is a process achieved through gas purification devices, designed to remove impurities, impurities, or harmful substances from nitrogen, oxygen, argon, and helium to obtain high-purity hydrogen.

[0003] For example, Chinese patent CN219186389U discloses a purification device for nitrogen, oxygen, argon, and helium, relating to the field of chemical gas purification technology. Specifically, it describes a purification device for nitrogen, oxygen, argon, and helium, comprising a cylindrical box with a semi-circular rectangular tube at the top. This purification device, through the setting of a limiting rod, prevents the sixth support block from shaking with the semi-circular rectangular tube. The coordinated arrangement of the semi-circular rectangular tube, support shaft, and sixth support block improves the utilization rate of the molecular sieve adsorbent. The convex column prevents the third support column from detaching. The coordinated arrangement of the third, first, and second support columns enhances purification performance.

[0004] However, the above-mentioned simple purification equipment requires shutdown after the adsorption material is saturated, making continuous production impossible. The adsorption material is also subject to strong impact and friction from the airflow, which can easily cause the molecular sieve to pulverize.

[0005] Based on this, the present invention designs a gas purification device to solve the above problems. Utility Model Content

[0006] In view of the above-mentioned shortcomings of the existing technology, the present invention provides a gas purification device.

[0007] To achieve the above objectives, this utility model provides the following technical solution:

[0008] A gas purification device, including a first conduit;

[0009] A flow meter and analyzer are installed on the first pipeline;

[0010] The first pipe is connected to an adjustable air intake assembly;

[0011] The outlet end of the adjustable air intake assembly is connected to a first adsorption container and a second adsorption container, and the first adsorption container and the second adsorption container have the same structure.

[0012] The inlet ends of both the first and second adsorption containers are connected to a regulating regeneration gas assembly for regeneration gas entry.

[0013] The first and second adsorption containers are connected to an adjustable purified gas discharge assembly for discharging purified gas and an exhaust gas discharge assembly for discharging waste gas.

[0014] Furthermore, the adjustable intake assembly includes a first control valve, a second pipe, a third control valve, and a fifth pipe. The first pipe is connected to the fifth pipe and the second pipe via a tee pipe. The first control valve is installed on the fifth pipe, and the third control valve is fixedly installed on the second pipe. The fifth pipe is connected to the input end of the first adsorption container, and the second pipe is connected to the input end of the second adsorption container.

[0015] Furthermore, the adjustable regeneration gas assembly includes a second control valve, a fourth control valve, a fifth control valve, a third pipe, a fourth pipe, and an eleventh pipe. The third pipe is connected to the regeneration gas source, and the fifth control valve is installed on the third pipe. The third pipe is connected to the fourth and eleventh pipes via a tee pipe. The eleventh pipe is equipped with a second control valve, and the fourth pipe is equipped with a fourth control valve. The eleventh pipe is connected to the first adsorption container, and the fourth pipe is connected to the second adsorption container.

[0016] Furthermore, the adjustable purified gas discharge assembly includes a tenth pipe, a sixth control valve, a seventh pipe, an eighth control valve, and an eighth pipe. The tenth pipe is fixedly connected to the output end of the first adsorption container, and the sixth control valve is installed on the tenth pipe. The eighth pipe is fixedly connected to the output end of the second adsorption container, and the eighth control valve is fixedly connected to the eighth pipe. The eighth control valve and the tenth pipe are fixedly connected to the seventh pipe through a three-way pipe.

[0017] Furthermore, the exhaust gas discharge assembly includes a sixth pipe, a seventh control valve, a vent pipe, a ninth pipe, and a ninth control valve. The output end of the second adsorption container is connected to the ninth pipe, and the ninth control valve is installed on the ninth pipe. The output end of the first adsorption container is connected to the sixth pipe, and the seventh control valve is fixedly connected to the sixth pipe. The seventh control valve and the ninth pipe are fixedly connected to the vent pipe through a three-way pipe.

[0018] Furthermore, the second adsorption container includes a tank body and a tank cover. The tank cover is fixedly installed on the top of the tank body. An energy-relieving component for reducing the energy consumption of the purified gas is connected to the upper end of the tank body. A clamping component for compacting the adsorption material is provided below the energy-relieving component of the tank body. A feeding pipe for feeding is opened below the clamping component of the tank body. A conical hollow hopper for supporting the adsorption material is fixedly connected to the lower end of the inner wall of the tank body. A discharge pipe is fixedly connected to the discharge end of the conical hollow hopper, and the discharge pipe is located at the outer end of the tank body.

[0019] The lid of the second adsorption container is connected to the fourth and second pipes, and the lid of the first adsorption container is connected to the fifth and eleventh pipes.

[0020] The tank of the second adsorption container is connected to the eighth and ninth pipes, and the tank of the first adsorption container is connected to the sixth and tenth pipes.

[0021] Furthermore, the energy dissipation component includes a follower-type rotating component and an energy-consuming component, both of which are connected to the flow meter and are movably connected.

[0022] Furthermore, the clamping assembly includes a rocker arm, a palm pad, a crankshaft, and a second spring. The inner wall of the tank rotates with the crankshaft via a bearing. The bent part of the crankshaft is fixedly connected to the top of the second spring via a rotating ring. The bottom of the second spring is fixedly connected to a palm pad that slides in contact with the inner wall of the tank. One end of the crankshaft is fixedly connected to a rocker arm, which is located on the outside of the tank.

[0023] Beneficial effects

[0024] This utility model's flow meter performs flow statistics. When the adsorbent material in the second adsorption container reaches saturation, the first adsorption container purifies, and the second adsorption container regenerates. The adjustable inlet assembly and the adjustable purified gas outlet assembly are connected to the first adsorption container. The gas to be purified enters the first adsorption container through the adjustable inlet assembly, where it undergoes purification. The purified gas is then discharged through the adjustable purified gas outlet assembly. Simultaneously, the adjustable regeneration gas assembly and the exhaust gas outlet assembly are connected to the second adsorption container. The regeneration gas from the adjustable regeneration gas assembly enters the second adsorption container, removing impurities such as water, carbon monoxide, carbon dioxide, and hydrocarbons. Finally, the gas is discharged from the exhaust gas outlet assembly. The flow meter then performs flow statistics on the adsorption material in the first adsorption container reaching saturation. When saturation is reached, the second adsorption container purifies while the first adsorption container regenerates. The adjustable inlet assembly and the adjustable purified gas outlet assembly are connected to the second adsorption container, allowing the gas to be purified to enter through the adjustable inlet assembly. The second adsorption container then purifies the gas, and the purified gas is discharged through the adjustable purified gas outlet assembly. Simultaneously, the adjustable regeneration gas assembly and the exhaust gas outlet assembly are connected to the first adsorption container, allowing the regeneration gas from the adjustable regeneration gas assembly to enter the first adsorption container, removing impurities such as water, carbon monoxide, carbon dioxide, and hydrocarbons. Finally, the regeneration gas is discharged through the exhaust gas outlet assembly. This system effectively controls the adsorption and switching between the first and second adsorption containers, improving the recovery efficiency of the purified gas and the lifespan of the adsorbent. It also allows for accurate calculation of the adsorption capacity of both the first and second adsorption containers. The system is simple in structure, easy to operate, and suitable for various industrial gas production scenarios, enabling efficient and precise operation and improving system stability. Attached Figure Description

[0025] To more clearly illustrate the technical solutions in the embodiments of this utility model or the prior art, the drawings used in the description of the embodiments or the prior art will be briefly introduced below. Obviously, the drawings described below are only some embodiments of this utility model. For those skilled in the art, other drawings can be obtained based on these drawings without creative effort.

[0026] Figure 1 This is a schematic diagram of the structure of a gas purification device according to the present invention;

[0027] Figure 2 The second adsorption container structure of this utility model is three-dimensional. Figure 1 ;

[0028] Figure 3 This is a front view of the second adsorption container structure of this utility model;

[0029] Figure 4 The second adsorption container structure of this utility model is three-dimensional. Figure 2 ;

[0030] Figure 5 This is a partial schematic diagram of the second adsorption part of the present invention;

[0031] Figure 6 The second adsorption container structure of this utility model is three-dimensional. Figure 3 ;

[0032] Figure 7 For along Figure 3 A sectional view along the AA direction.

[0033] The labels in the diagram represent:

[0034] 1. Flow meter 2. First adsorption container 3. Second adsorption container 31. Tank body 32. Tank cover 33. Energy release assembly 331. Rotating cam 332. Horizontal shaft 333. Bearing 334. Mounting bracket 335. First spring 336. Horizontal support plate 337. Horizontal plate 337. Slide rod 338. Blade 34. Injection pipe 35. Pressing assembly 351. Rocker arm 352. Palm pad 353. Crankshaft 354. Second spring 36. Discharge pipe 37. Conical hollow bucket 4. Analyzer 5. First Pipeline 6. First Control Valve 7. Second Control Valve 8. Second Pipeline 9. Third Control Valve 10. Fourth Control Valve 11. Fifth Control Valve 12. Third Pipeline 13. Fourth Pipeline 14. Fifth Pipeline 15. Eleventh Pipeline 16. Sixth Pipeline 17. Tenth Pipeline 18. Sixth Control Valve 19. Seventh Control Valve 20. Vent Pipe 21. Seventh Pipeline 22. Eighth Control Valve 23. Eighth Pipeline 24. Ninth Pipeline 25. Ninth Control Valve. Detailed Implementation

[0035] To make the objectives, technical solutions, and advantages of the embodiments of this utility model clearer, the technical solutions of the embodiments of this utility model will be clearly and completely described below with reference to the accompanying drawings. Obviously, the described embodiments are only some, not all, of the embodiments of this utility model. All other embodiments obtained by those skilled in the art based on the embodiments of this utility model without creative effort are within the scope of protection of this utility model.

[0036] The present invention will be further described below with reference to the embodiments.

[0037] Example 1

[0038] Please refer to the instruction manual appendix. Figure 1 A gas purification device, including a first conduit 5;

[0039] A flow meter 1 and an analyzer 4 are installed on the first pipeline 5;

[0040] The first pipe 5 is connected to an adjustable air intake assembly;

[0041] The outlet end of the adjustable air intake assembly is connected to a first adsorption container 2 and a second adsorption container 3, and the first adsorption container 2 and the second adsorption container 3 have the same structure.

[0042] The input ends of both the first adsorption container 2 and the second adsorption container 3 are connected to a regulating regeneration gas assembly for regeneration gas entry.

[0043] The first adsorption container 2 and the second adsorption container 3 are connected to an adjustable purified gas discharge assembly for the discharge of purified gas and an exhaust gas discharge assembly for the discharge of waste gas.

[0044] When the adsorption material in the second adsorption container 3 reaches saturation, the first adsorption container 2 purifies and the second adsorption container 3 regenerates. The regulating inlet assembly and the regulating purified gas outlet assembly are connected to the first adsorption container 2, allowing the gas to be purified to enter through the regulating inlet assembly. The first adsorption container 2 then purifies the gas, which is then discharged through the regulating purified gas outlet assembly. Simultaneously, the regulating regeneration gas assembly and the exhaust gas outlet assembly are connected to the second adsorption container 3, allowing the regeneration gas from the regulating regeneration gas assembly to enter the second adsorption container 3, removing impurities such as water, carbon monoxide, carbon dioxide, and hydrocarbons. Finally, the gas is discharged through the exhaust gas outlet assembly. The flow meter 1 then records the flow rate, indicating that the adsorption material in the first adsorption container 2 has reached saturation. Simultaneously, the second adsorption container 3 purifies while the first adsorption container 2 regenerates. The adjustable inlet assembly and the adjustable purified gas outlet assembly are connected to the second adsorption container 3. The gas to be purified enters the second adsorption container 3 through the adjustable inlet assembly, where it undergoes purification. The purified gas is then discharged through the adjustable purified gas outlet assembly. At the same time, the adjustable regeneration gas assembly and the exhaust gas outlet assembly are connected to the first adsorption container 2. The regeneration gas from the adjustable regeneration gas assembly enters the first adsorption container 2, removing impurities such as water, carbon monoxide, carbon dioxide, and hydrocarbons. Finally, the regeneration gas is discharged through the exhaust gas outlet assembly. This system effectively controls the adsorption and switching between the first adsorption container 2 and the second adsorption container 3, improving the recovery efficiency of the purified gas and the lifespan of the adsorbent. It also allows for accurate calculation of the adsorption capacity of the first adsorption container 2 and the second adsorption container 3. With its simple structure and convenient operation, it is suitable for various industrial gas production scenarios, achieving efficient and precise operation and improving system stability.

[0045] The adjustable intake assembly includes a first control valve 6, a second pipe 8, a third control valve 9, and a fifth pipe 14. The first pipe 5 is connected to the fifth pipe 14 and the second pipe 8 through a three-way pipe. The first control valve 6 is installed on the fifth pipe 14. The third control valve 9 is fixedly installed on the second pipe 8. The fifth pipe 14 is connected to the input end of the first adsorption container 2, and the second pipe 8 is connected to the input end of the second adsorption container 3.

[0046] The adjustable regeneration gas assembly includes a second control valve 7, a fourth control valve 10, a fifth control valve 11, a third pipe 12, a fourth pipe 13, and an eleventh pipe 15. The third pipe 12 is connected to the regeneration gas source. The fifth control valve 11 is installed on the third pipe 12. The third pipe 12 is connected to the fourth pipe 13 and the eleventh pipe 15 through a three-way pipe. The second control valve 7 is installed on the eleventh pipe 15. The fourth control valve 10 is installed on the fourth pipe 13. The eleventh pipe 15 is connected to the first adsorption container 2. The fourth pipe 13 is connected to the second adsorption container 3.

[0047] The adjustable purified gas discharge assembly includes a tenth pipe 17, a sixth control valve 18, a seventh pipe 21, an eighth control valve 22, and an eighth pipe 23. The output end of the first adsorption container 2 is fixedly connected to the tenth pipe 17, and the sixth control valve 18 is installed on the tenth pipe 17. The output end of the second adsorption container 3 is fixedly connected to the eighth pipe 23, and the eighth control valve 22 is fixedly connected to the eighth pipe 23. The eighth control valve 22 and the tenth pipe 17 are fixedly connected to the seventh pipe 21 through a three-way pipe.

[0048] The exhaust gas discharge assembly includes a sixth pipe 16, a seventh control valve 19, a vent pipe 20, a ninth pipe 24, and a ninth control valve 25. The output end of the second adsorption container 3 is connected to the ninth pipe 24, and the ninth control valve 25 is installed on the ninth pipe 24. The output end of the first adsorption container 2 is connected to the sixth pipe 16, and the seventh control valve 19 is fixedly connected to the sixth pipe 16. The seventh control valve 19 and the ninth pipe 24 are fixedly connected to the vent pipe 20 through a three-way pipe.

[0049] The first adsorption container 2 purifies, the second adsorption container 3 regenerates, the first control valve 6 of the regulating air intake assembly and the sixth control valve 18 of the regulating purified gas discharge assembly are opened, the fifth pipe 14, the tenth pipe 17, and the seventh pipe 21 are connected to the first adsorption container 2, and the third control valve 9, the second control valve 7, the seventh control valve 19, and the eighth control valve 22 are closed. The gas to be purified enters the first adsorption container 2 through the fifth pipe 14 of the regulating air intake assembly, the first adsorption container 2 purifies, and the purified gas passes through the regulating purified gas discharge assembly. The tenth pipe 17 and the seventh pipe 21 discharge. At the same time, the fifth control valve 11 and the fourth control valve 10 of the regulating regeneration gas assembly and the ninth control valve 25 of the exhaust gas discharge assembly are opened. The third pipe 12, the fourth pipe 13 and the ninth pipe 24 are connected to the second adsorption container 3. The regeneration gas of the regulating regeneration gas assembly enters the second adsorption container 3 through the third pipe 12 and the fourth pipe 13 to remove impurities such as water, carbon monoxide, carbon dioxide and hydrocarbons in the second adsorption container 3. Finally, it is discharged from the ninth pipe 24 and the vent pipe 20 of the exhaust gas discharge assembly.

[0050] When the adsorbent material in the first adsorption container 2 reaches saturation, the second adsorption container 3 purifies and the first adsorption container 2 regenerates. The third control valve 9 of the regulating air intake assembly and the eighth control valve 22 of the regulating purified gas discharge assembly open. The second pipe 8, the eighth pipe 23, and the seventh pipe 21 are connected to the second adsorption container 3, and the first control valve 6, the fourth control valve 10, the ninth control valve 25, and the sixth control valve 18 are closed. The gas to be purified enters the second adsorption container 3 through the second pipe 8 of the regulating air intake assembly, where it is purified. The purified gas is then discharged through the eighth pipe 23 and the seventh pipe 21 of the regulating purified gas discharge assembly. Simultaneously, the second control valve 7 of the regulating regeneration gas assembly and the seventh control valve 19 of the exhaust gas discharge assembly are opened, and the third pipe 12, the eleventh pipe 15, the sixth pipe 16, and the vent pipe 20 are connected to the first adsorption container 2. The regeneration gas from the regulating regeneration gas assembly enters the first adsorption container 2 through the third pipe 12 and the eleventh pipe 15, removing impurities such as water, carbon monoxide, carbon dioxide, and hydrocarbons from the first adsorption container 2. Finally, it is discharged from the sixth pipe 16 and the vent pipe 20 of the exhaust gas discharge assembly. This effectively controls the adsorption and switching of the first adsorption container 2 or the second adsorption container 3, improving the recovery efficiency of the purified gas and the service life of the adsorbent.

[0051] Please refer to the instruction manual appendix. Figure 2-7 The second adsorption container 3 includes a tank body 31 and a tank cover 32. The tank cover 32 is fixedly installed on the top of the tank body 31. The upper end of the tank body 31 is connected to an energy-dissipating component 33 for reducing the energy consumption of the purified gas. The tank body 31 is provided with a pressing component 35 for compacting the adsorption material below the energy-dissipating component 33. The tank body 31 is provided with a feeding pipe 34 below the pressing component 35. The lower end of the inner wall of the tank body 31 is fixedly connected to a conical hollow hopper 37 for supporting the adsorption material. The discharge end of the conical hollow hopper 37 is fixedly connected to a discharge pipe 36, and the discharge pipe 36 is located at the outer end of the tank body 31.

[0052] The lid 32 of the second adsorption container 3 is connected to the fourth pipe 13 and the second pipe 8, and the lid 32 of the first adsorption container 2 is connected to the fifth pipe 14 and the eleventh pipe 15.

[0053] The tank 31 of the second adsorption container 3 is connected to the eighth pipe 23 and the ninth pipe 24, and the tank 31 of the first adsorption container 2 is connected to the sixth pipe 16 and the tenth pipe 17.

[0054] Both the injection pipe 34 and the discharge pipe 36 are equipped with control valves at their outer ends for controlling the sealing of the injection pipe 34 and the discharge pipe 36.

[0055] The energy dissipation component 33 includes a follower-type rotating component and an energy-consuming component. Both the follower-type rotating component and the energy-consuming component are connected to the flow meter 1, and the follower-type rotating component and the energy-consuming component are movably connected.

[0056] The follow-up rotating component includes a rotating cam 331, a horizontal shaft 332, and blades 338. The tank body 31 is rotatably connected to the horizontal shaft 332 via a bearing. Blades 338 are fixedly connected at equal intervals along the circumference on the part of the tank body 31 located inside the tank body 31. The rotating cam 331 is fixedly connected to the outer end of the horizontal shaft 332. The rotating cam 331 is movably connected to the energy-consuming component.

[0057] The energy-consuming components include a bearing 333, a mounting bracket 334, a first spring 335, a horizontal support plate 336, and a sliding rod 337. The horizontal support plate 336 is fixedly installed on the outer wall of the tank 31. The first spring 335 is fixedly connected to the top of the horizontal support plate 336. The mounting bracket 334 is fixedly connected to the top of the first spring 335. The bearing 333 is rotatably connected to the mounting bracket 334. The bearing 333 is movably connected to the rotating cam 331. The sliding rod 337 is fixedly connected to the bottom of the mounting bracket 334. The bottom of the sliding rod 337 is in contact with and slidably connected to the straight hole opened in the horizontal support plate 336.

[0058] When the rotating cam 331 is separated from the bearing 333 and the first spring 335 is in its normal state, the top of the bearing 333 is 2cm higher than the bottom of the rotating cam 331 at its lowest point.

[0059] Gas enters the tank body 31 through the can lid 32. The gas drives the blades 338 of the follower rotating component of the energy dissipation component 33 to rotate. The blades 338 drive the horizontal shaft 332 to rotate. The horizontal shaft 332 drives the rotating cam 331 to rotate. The rotating cam 331 contacts the bearing 333 of the energy dissipation component and pushes the bearing 333 to move downward. The bearing 333 drives the mounting bracket 334 to move downward. The mounting bracket 334 drives the first spring 335 to compress downward. After the rotating cam 331 separates from the bearing 333, the restoring force of the first spring 335 pushes the mounting bracket 334 upward and pushes the bearing 333 upward. During this process, the energy required for the compression of the first spring 335 is not reused. This part of the energy is the energy of the gas flow, which reduces the impact on the adsorbent material, reduces the friction between the adsorbent materials, and reduces the possibility of adsorbent material pulverization.

[0060] The clamping assembly 35 includes a rocker arm 351, a palm pad 352, a crankshaft 353, and a second spring 354. The inner wall of the can 31 rotates with the crankshaft 353 via a bearing. The bent part of the crankshaft 353 is fixedly connected to the top of the second spring 354 via a rotating ring. The bottom of the second spring 354 is fixedly connected to the palm pad 352, which is in close contact with and slidably connected to the inner wall of the can 31. One end of the crankshaft 353 is fixedly connected to the rocker arm 351, and the rocker arm 351 is located on the outside of the can 31.

[0061] When the adsorbent material needs to be replaced, rotate the rocker arm 351 of the clamping assembly 35. The rocker arm 351 causes the curved part of the crankshaft 353 to face upwards. The crankshaft 353 causes the second spring 354 to move upwards. The second spring 354 causes the palm pad 352 to move upwards until it is higher than the injection pipe 34, opening the valve on the discharge pipe 36. The adsorbent material on the conical hollow bucket 37 is discharged through the discharge pipe 36. After contact, the discharge pipe 36 is blocked, and the adsorbent material enters the tank 31 through the injection pipe 34. Finally, rotate the rocker arm 351. The rocker arm 351 causes the curved part of the crankshaft 353 to face downwards. The crankshaft 353 causes the second spring 354 to move downwards. The second spring 354 causes the palm pad 352 to move into contact with the adsorbent, pressing the adsorbent material on the conical hollow bucket 37 tightly to prevent the adsorbent material from loosening or rubbing, further reducing the possibility of adsorbent material pulverization and extending the service life of the adsorbent material.

[0062] The above embodiments are only used to illustrate the technical solutions of this utility model, and are not intended to limit it. Although this utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that modifications can still be made to the technical solutions described in the foregoing embodiments, or equivalent substitutions can be made to some of the technical features. Such modifications or substitutions will not cause the essence of the corresponding technical solutions to deviate from the spirit and scope of the technical solutions of the embodiments of this utility model.

Claims

1. A gas purification device comprising a first pipeline (5), characterized in that: a flow meter (1) and an analyzer (4) are installed on the first pipeline (5); a regulating air inlet assembly is connected to the first pipeline (5); a first adsorption container (2) and a second adsorption container (3) are connected to the air outlet end of the regulating air inlet assembly, and the first adsorption container (2) and the second adsorption container (3) are the same in structure; the input ends of the first adsorption container (2) and the second adsorption container (3) are connected to a regulating regeneration gas assembly for the regeneration gas inlet; the air outlet ends of the first adsorption container (2) and the second adsorption container (3) are connected to a regulating purified gas discharge assembly for discharging the purified gas and a waste gas discharge assembly for discharging the waste gas.

2. The gas purification apparatus according to claim 1, characterized by, The regulating air inlet assembly comprises a first control valve (6), a second pipeline (8), a third control valve (9), and a fifth pipeline (14), the first pipeline (5) is connected to the fifth pipeline (14) and the second pipeline (8) through a three-way pipeline, the first control valve (6) is installed on the fifth pipeline (14), the third control valve (9) is fixedly installed on the second pipeline (8), the fifth pipeline (14) is connected to the input end of the first adsorption container (2), and the second pipeline (8) is connected to the input end of the second adsorption container (3).

3. The gas purification apparatus according to claim 2, characterized by, The regulating regeneration gas assembly comprises a second control valve (7), a fourth control valve (10), a fifth control valve (11), a third pipeline (12), a fourth pipeline (13), and an eleventh pipeline (15), the third pipeline (12) is connected to a regeneration gas source, the fifth control valve (11) is installed on the third pipeline (12), the third pipeline (12) is connected to the fourth pipeline (13) and the eleventh pipeline (15) through a three-way pipeline, the second control valve (7) is installed on the eleventh pipeline (15), the fourth control valve (10) is installed on the fourth pipeline (13), the eleventh pipeline (15) is connected to the first adsorption container (2), and the fourth pipeline (13) is connected to the second adsorption container (3).

4. The gas purification apparatus according to claim 3, characterized by The regulating purified gas discharge assembly comprises a tenth pipeline (17), a sixth control valve (18), a seventh pipeline (21), an eighth control valve (22), and an eighth pipeline (23), the output end of the first adsorption container (2) is fixedly connected to the tenth pipeline (17), the sixth control valve (18) is installed on the tenth pipeline (17), the output end of the second adsorption container (3) is fixedly connected to the eighth pipeline (23), the eighth control valve (22) is fixedly connected to the eighth pipeline (23), and the eighth control valve (22) and the tenth pipeline (17) are fixedly connected to the seventh pipeline (21) through a three-way pipeline.

5. The gas purification apparatus according to claim 4, characterized by The exhaust gas discharge assembly comprises a sixth pipeline (16), a seventh control valve (19), a vent pipe (20), a ninth pipeline (24) and a ninth control valve (25), the second adsorption container (3) is connected with the ninth pipeline (24) at the output end, the ninth control valve (25) is installed on the ninth pipeline (24), the first adsorption container (2) is connected with the sixth pipeline (16) at the output end, the seventh control valve (19) is fixedly connected on the sixth pipeline (16), and the seventh control valve (19) and the ninth pipeline (24) are fixedly connected with the vent pipe (20) through a three-way pipe.

6. The gas purification apparatus according to claim 5, characterized by The second adsorption container (3) comprises a tank body (31) and a tank cover (32), the tank cover (32) is fixedly installed on the top of the tank body (31), the tank body (31) is connected with an energy dissipation assembly (33) for energy consumption reduction of purified gas at the upper end, the tank body (31) is provided with a compaction assembly (35) for compacting adsorption material below the energy dissipation assembly (33), the tank body (31) is provided with a feeding pipe (34) for feeding below the compaction assembly (35), the inner wall of the tank body (31) is fixedly connected with a conical hollow hopper (37) for supporting adsorption material at the lower end, the conical hollow hopper (37) is fixedly connected with a discharge pipe (36) at the discharge end, and the discharge pipe (36) is located at the outer end of the tank body (31); The tank cover (32) of the second adsorption container (3) is connected with the fourth pipeline (13) and the second pipeline (8), and the tank cover (32) of the first adsorption container (2) is connected with the fifth pipeline (14) and the eleventh pipeline (15); The tank body (31) of the second adsorption container (3) is connected with the eighth pipeline (23) and the ninth pipeline (24), and the tank body (31) of the first adsorption container (2) is connected with the sixth pipeline (16) and the tenth pipeline (17).

7. The gas purification apparatus according to claim 6, characterized by The energy dissipation assembly (33) comprises a follow-up rotating assembly and an energy consumption assembly, and the follow-up rotating assembly and the energy consumption assembly are connected with the flow meter (1) and movably connected.

8. A gas purification apparatus according to any one of claims 6-7, characterized in that, The compaction assembly (35) comprises a rocker (351), a palm pad (352), a crankshaft (353) and a second spring (354), the inner wall of the tank body (31) is rotatably connected with the crankshaft (353) through a bearing, the curved part of the crankshaft (353) is fixedly connected with the top of the second spring (354) through a rotating ring, the bottom of the second spring (354) is fixedly connected with the palm pad (352) which is slidably connected with the inner wall of the tank body (31), one end of the crankshaft (353) is fixedly connected with the rocker (351), and the rocker (351) is located outside the tank body (31).

Citation Information

Patent Citations

  • Purification device for nitrogen, oxygen, argon and helium

    CN219186389U