Equipment for efficiently purifying oxygen
By introducing gasification components and heating and drying technology into the oxygen purification device, the problems of low oxygen purification efficiency and low cost in the existing technology are solved, equipment for efficient oxygen purification is realized, and the purity and purification efficiency of oxygen are improved.
Patent Information
- Application Number
- CN202420251857.X
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-02-01
- Publication Date
- 2025-01-21
- Estimated Expiration
- 2034-02-01
AI Technical Summary
When the existing oxygen purification device performs preliminary purification and refined purification of oxygen, the gas flows slowly in the adsorption tank, resulting in wasted time and the purification efficiency and cost are not efficient enough.
An equipment for efficient oxygen purification is designed. It uses gasification components to separate water and gas impurities in the air through compression and decompression, and uses molecular sieves to separate oxygen. Combined with heating and drying technology, it improves oxygen purification efficiency.
Efficient preliminary purification of oxygen is achieved, the purification efficiency is improved, time and cost are reduced, and the purity of oxygen is improved.
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Figure CN222368731U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of equipment for efficiently purifying oxygen, and specifically, to equipment for efficiently purifying oxygen. Background Art
[0002] With the development of social sciences, industrial technology has gradually developed into high-precision manufacturing, and the demand for high-purity gases has become increasingly greater. High-purity oxygen is widely used in electronics, crystalline silicon and other industries.
[0003] In the prior art, an oxygen purification device for bulk gas supply with application number 'CN202122423339.0' comprises a base, an adsorption tank and a processing tank, a fixed plate is provided on the top of the base, support columns are fixedly connected at the four corners of the bottom of the fixed plate, a support plate is fixedly connected between the plurality of support columns, an insulating layer is provided on the inner wall of the adsorption tank, sieve plates are fixedly connected on both sides of the inner wall of the adsorption tank, a filter plate is provided on one side of the outer wall of the sieve plate, an insulating layer is provided between the two sieve plates, a guide plate is fixedly connected to the outer wall of the insulating layer, the number of the guide plates is set to be multiple, an adsorbent is provided on the outer wall of the insulating layer, an activated carbon adsorption plate is provided on the top of the guide plate, an electric heating pipe is provided on the inner wall of the insulating layer, a vacuum layer is provided on the inner wall of the processing tank, partitions are fixedly connected on both sides of the inner wall of the processing tank, a drainage pipe is provided between the two partitions, a desiccant is provided on the outer wall of the drainage pipe, an activated carbon filter is provided at the bottom of one of the partitions, and a first filter is provided at the bottom of the activated carbon filter.
[0004] The above technology contains the following technical problems: the raw gas enters the adsorption tank from the air inlet pipe, and then the contact time between the gas and the adsorbent is prolonged so that the raw gas can be purified under the contact with the activated carbon plate. Although the purification effect is improved, the preliminary purification and fine purification of oxygen are carried out simultaneously, and the gas flows slowly in the adsorption tank. By increasing the contact time between the gas and the adsorbent, a lot of time is wasted in the preliminary treatment of the raw gas, making the overall oxygen purification work inefficient and increasing the time cost of the purification cost. Utility Model Content
[0005] The utility model provides a device for efficiently purifying oxygen, which makes the initial purification of oxygen more efficient, increases the purification efficiency of oxygen, and further reduces the time cost of oxygen purification.
[0006] The technical solution of the utility model is as follows:
[0007] A device for efficiently purifying oxygen comprises a pure gas shell, a plurality of first gas outlet holes for transferring purified gas are provided on the side wall of the pure gas shell, a second gas outlet hole is provided on the other side of the first gas outlet hole, a sealing cover is connected to the pure gas shell to ensure that the pure gas shell is sealed and the gas is preliminarily filtered, a gasification component for accelerating the purification of the preliminarily filtered gas is connected between the sealing cover and the second gas outlet hole, a limiting plate for piston movement with the inner wall of the pure gas shell is connected to the lower side of the gasification component, a driving component for driving the gasification component is connected to the lower side of the limiting plate, a plurality of heating tubes for heating the gas in the pure gas shell are fixedly connected to the pure gas shell in an annular manner, and a limiting block for cooperating with the gasification component to complete the function is fixedly connected to the inner wall of the pure gas shell.
[0008] Furthermore, the gasification component includes a limiting sleeve, which is fixedly connected to the limiting plate, and a pressure column is slidably connected to the limiting sleeve, and the end of the pressure column away from the limiting sleeve is fixedly connected to the first sealing plate, and a pressure spring is sleeved on the pressure column, and the two ends of the pressure spring are respectively abutted against the outer wall of the limiting sleeve and the first sealing plate, and the limiting sleeve is slidably connected inside, and a negative pressure column is fixedly connected to the limiting plate, and the end of the negative pressure column away from the limiting plate is fixedly connected to the second sealing plate, and a negative pressure spring is sleeved on the negative pressure column, and the two ends of the negative pressure spring are respectively abutted against the inner wall of the limiting sleeve.
[0009] Furthermore, the outer wall of the negative pressure column is tightly fitted with the inner wall of the first sealing plate and the inner wall of the pressure column and is slidably connected, the upper side of the first sealing plate abuts against the lower side of the limit block, and the lower side of the second sealing plate abuts against the upper side of the limit block.
[0010] Furthermore, the driving assembly includes a flip block and a motor, the flip block is fixedly connected to the side of the limit plate facing the bottom of the pure gas shell, the flip block is rotatably connected to a flip plate, the end of the flip plate away from the flip block is rotatably connected to a shaking column, both ends of the shaking column are rotatably connected to the pure gas shell, the motor is fixedly connected to the outer wall of the pure gas shell, and the driving shaft of the motor passes through the pure gas shell and is fixedly connected to one end of the shaking column.
[0011] Furthermore, a heat preservation groove is provided in a ring shape on the pure gas shell, the heating pipe is fixedly connected to the inner wall of the heat preservation groove, a gas gathering groove is provided on the pure gas shell, each of the first gas outlet holes is connected to the gas gathering groove, the second gas outlet holes is connected to the gas gathering groove, the second gas outlet holes are fixedly connected to an gas outlet pipe toward the outside, and a molecular sieve for separating oxygen is fixedly connected in the gas outlet pipe.
[0012] Furthermore, a plurality of desiccant blocks are fixedly connected to the limiting plate, a sealing block is fixedly connected to the upper side of each desiccant block, an air leakage hole is opened on each desiccant block, and each sealing block abuts against the inner wall of the pure gas housing.
[0013] Furthermore, the sealing cover is threadedly connected to the pure gas housing, a polymer filter element is fixedly connected inside the sealing cover, and an air inlet pipe is fixedly connected to the upper side of the sealing cover.
[0014] Furthermore, a plurality of supporting legs for supporting the pure gas housing are fixedly connected to the lower side of the pure gas housing.
[0015] The working principle and beneficial effects of the utility model are:
[0016] In the utility model, the gasification component can continuously compress and decompress the gas injected into the pure gas shell. The air is first decompressed, and the water vapor impurities in the air can be separated by the decompression effect, and the water content in the air is reduced to improve the efficiency of oxygen purification. Then, the compressed gas is brought into contact with the molecular sieve through the compression effect, and is used to separate the oxygen in the air to achieve the purpose of purifying the oxygen. The heating pipe can heat and dry the air in the pure gas shell by heating, increase the speed of water vapor separation, and further improve the oxygen purification efficiency. BRIEF DESCRIPTION OF THE DRAWINGS
[0017] The utility model is further described in detail below in conjunction with the accompanying drawings and specific implementation methods.
[0018] Figure 1 is an isometric schematic diagram of the prior art;
[0019] Figure 2 It is an isometric schematic diagram of the utility model;
[0020] Figure 3 It is a partial half-section isometric schematic diagram of the utility model;
[0021] Figure 4 for Figure 3 A is an enlarged schematic diagram;
[0022] Figure 5 It is a partially cutaway enlarged schematic diagram of the utility model;
[0023] Figure 6 It is an isometric perspective view of the pure gas shell of the utility model.
[0024] In the figure: 11. Support foot; 12. Pure gas shell; 121. First air outlet; 122. Gas gathering tank; 123. Insulation tank; 124. Second air outlet; 13. Air outlet pipe; 14. Sealing cover; 15. Air inlet pipe; 16. Polymer filter element; 17. Limit block; 2. Gasification component; 21. Limit sleeve; 22. Negative pressure spring; 23. Pressurization spring; 24. First sealing plate; 25. Second sealing plate; 26. Negative pressure column; 27. Pressurization column; 28. Limit disk; 3. Sealing block; 31. Desiccant block; 32. Air vent; 41. Turning block; 42. Shaking column; 43. Turning plate; 5. Motor; 6. Heating tube. DETAILED DESCRIPTION
[0025] The following will be combined with the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments of the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.
[0026] Example 1
[0027] like Figure 2 to Figure 6 As shown, this embodiment proposes an efficient oxygen purification device, including a pure gas housing 12, a plurality of first gas outlets 121 for transferring the purified gas are all opened on the side wall of the pure gas housing 12, and a second gas outlet 124 is opened on the other side of the first gas outlet 121. The pure gas housing 12 is connected to a cover 14 that ensures that the pure gas housing 12 is sealed and performs preliminary filtering on the gas. A gasification component 2 that accelerates the purification of the gas after preliminary filtering is connected between the cover 14 and the second gas outlet 124. The gasification component 2 can continuously compress and decompress the gas injected into the pure gas housing 12. The air is first decompressed, and the water vapor impurities in the air can be separated by the decompression effect, thereby reducing the content of the air. The amount of water is increased to improve the efficiency of oxygen purification, and then the compressed gas is brought into contact with the molecular sieve through compression to separate the oxygen in the air to achieve the purpose of purifying the oxygen. The limit plate 28 that makes piston motion with the inner wall of the pure gas shell 12 is connected to the lower side of the gasification component 2, and the driving component for driving the gasification component 2 is connected to the lower side of the limit plate 28. A number of heating pipes 6 for heating the gas in the pure gas shell 12 are annularly fixedly connected to the pure gas shell 12. The heating pipes 6 can heat and dry the air in the pure gas shell 12 by heating, increase the speed of water vapor separation, and further improve the oxygen purification efficiency. The limit block 17 that cooperates with the gasification component 2 to complete the function is fixedly connected to the inner wall of the pure gas shell 12.
[0028] like Figure 3 to Figure 5As shown, the gasification component 2 includes a limiting sleeve 21, the limiting sleeve 21 is fixedly connected to the limiting disk 28, the pressure column 27 is slidably connected to the limiting sleeve 21, and the end of the pressure column 27 away from the limiting sleeve 21 is fixedly connected to the first sealing plate 24, and the pressure spring 23 is sleeved on the pressure column 27, and the two ends of the pressure spring 23 are respectively abutted against the outer wall of the limiting sleeve 21 and the first sealing plate 24. When the limiting disk 28 moves up, the first sealing plate 24 will abut against the limiting block 17 on the lower side. Under the action of the pressure spring 23, the continued movement of the limiting disk 28 will cause the first sealing plate 24 to be completely closed. The limiting block 17 is pressed against the first sealing plate 24 so that the hole groove on the limiting block 17 is completely blocked, so that a closed cavity is formed between the first sealing plate 24 and the limiting plate 28, and then the limiting plate 28 continues to move upward to continuously compress the gas in the cavity until the vent hole 32 is connected to the first air outlet 121, and this part of the compressed gas contacts the molecular sieve through the first air outlet 121, so that oxygen is separated from the air, and the limiting plate 28 is slidably connected in the limiting sleeve 21, and the negative pressure column 26 is fixedly connected to the limiting plate 28, and the negative pressure column 26 is away from the limiting plate 28. One end of the positioning plate 28 is fixedly connected to the second sealing plate 25, and the negative pressure spring 22 is sleeved on the negative pressure column 26. The two ends of the negative pressure spring 22 are respectively connected to the inner wall of the limiting sleeve 21. When the limiting plate 28 moves downward, the desiccant block 31 will block the first air outlet 121 and drive the second sealing plate 25 to move downward. When the second sealing plate 25 contacts the limiting block 17, the second sealing plate 25 will press the air on the upper side of the limiting block 17 into the cavity between the limiting plate 28 and the second sealing plate 25. As the limiting plate 28 continues to move downward, under the action of the negative pressure spring 22, the second sealing plate 25 will gradually It gradually comes into close contact with the limit block 17, and then blocks the hole groove in the limit block 17, so that the air in the cavity between the limit plate 28 and the second sealing plate 25 is continuously decompressed. During the decompression process, the moisture inside the gas will also decrease as the pressure decreases. This is because moisture usually exists in liquid form under high pressure, but in the decompression process, moisture may be released in gaseous form. Therefore, the decompression treatment can reduce the moisture in the gas to a lower level. At the same time, the desiccant block 31 will absorb and dry this part of the separated water vapor, further improving the air purification efficiency.
[0029] like Figure 3 to Figure 5 As shown, the outer walls of the negative pressure column 26 are tightly fitted with the inner walls of the first sealing plate 24 and the inner walls of the pressure column 27 and are slidably connected. Cylinders and other related manufacturing processes can be used to ensure that air does not escape from the connection between the negative pressure column 26 and the pressure column 27. The upper side surface of the first sealing plate 24 abuts against the lower side surface of the limit block 17, and the lower side surface of the second sealing plate 25 abuts against the upper side surface of the limit block 17, so that the negative pressure column 26 and the pressure column 27 will not interfere with each other during relative movement.
[0030] like Figure 2 and Figure 3As shown, the driving assembly includes a flip block 41 and a motor 5. The flip block 41 is fixedly connected to the side of the limit plate 28 facing the bottom of the pure gas shell 12. The flip block 41 is rotatably connected to the flip plate 43. The end of the flip plate 43 away from the flip block 41 is rotatably connected to the shaking column 42. Both ends of the shaking column 42 are rotatably connected to the pure gas shell 12. The motor 5 is fixedly connected to the outer wall of the pure gas shell 12. The driving shaft of the motor 5 passes through the pure gas shell 12 and is fixedly connected to one end of the shaking column 42. The shaking column 42 is directly driven to rotate by the motor 5, so that the limit plate 28 makes continuous piston motion in the pure gas shell 12, so that the air in the pure gas shell 12 can be repeatedly pressurized and depressurized.
[0031] like Figure 3 to Figure 6 As shown, the insulation tank 123 is opened on the pure gas shell 12, the heating pipe 6 is fixedly connected to the inner wall of the insulation tank 123, and the heating pipe 6 is close to the inner wall of the insulation tank 123 on the side of the axis of the pure gas shell 12. The air in the pure gas shell 12 is dried by heating the pure gas shell 12, so that the water vapor in the air can be absorbed by the desiccant block 31. The gas gathering tank 122 is opened on the pure gas shell 12, and each first air outlet hole 121 is connected with the gas gathering tank 122, so that the gas flowing out of each first air outlet hole 121 is gathered from the gas gathering tank 122 and finally flows out from the second air outlet hole 124. The second air outlet hole 124 is connected with the gas gathering tank 122, and the second air outlet hole 124 is fixedly connected to the air outlet pipe 13 toward the outside. A molecular sieve for separating oxygen is fixedly connected in the air outlet pipe 13, and the oxygen in the air is separated by the molecular sieve.
[0032] like Figure 5 and Figure 6 As shown, several desiccant blocks 31 are fixedly connected to the limiting plate 28, and each sealing block 3 is fixedly connected to the upper side of each desiccant block 31. The desiccant block 31 can absorb the water separated from the oxygen to achieve the purpose of oxygen purification. Each leak hole 32 is respectively opened on each desiccant block 31. When the desiccant block 31 moves up to a certain distance, the leak hole 32 will be connected with the first air outlet 121, so that the gas in the pure gas shell 12 can be converted from a closed state to a flowing state. Each sealing block 3 is in contact with the inner wall of the pure gas shell 12, so that the sealing block 3 can block the first air outlet 121 most of the time, thereby forming a closed space between the limiting plate 28 and the cover 14.
[0033] like Figure 3 and Figure 5 As shown, the cover 14 is threadedly connected to the pure gas housing 12, so that after the pure gas housing 12 is disassembled through the cover 14, the remaining components can be easily replaced to increase the service life of the entire components. The polymer filter element 16 is fixedly connected in the cover 14 to remove impurities and moisture in the oxygen, and the air inlet pipe 15 is fixedly connected to the upper side of the cover 14.
[0034] like Figure 2 and Figure 3 As shown, a plurality of support legs 11 for supporting the pure gas housing 12 are fixedly connected to the lower side of the pure gas housing 12 to support the entire pure gas housing 12 so as to ensure that the temperature inside the pure gas housing 12 is stable and will not be excessively disturbed by the outside world.
[0035] The working principle of this embodiment is:
[0036] First, tighten the cover 14 on the pure gas housing 12, and then inject the raw gas from the gas inlet pipe 15. The raw gas can be pre-processed by the polymer filter element 16, that is, the impurities such as water are initially removed, and then the preliminarily cleaned raw gas is accumulated in the cavity between the cover 14 and the second sealing plate 25. The motor 5 is started to drive the shaking column 42 to rotate, and then the flip plate 43 drives the limit plate 28 to move up and down like a piston on the inner wall of the pure gas housing 12;
[0037] When the limit plate 28 is at the highest point and moves downward: at this time, the second sealing plate 25 has not yet abutted against the side wall of the limit block 17, so the cavity between the cover 14 and the second sealing plate 25 becomes the cavity between the cover 14 and the first sealing plate 24. As the limit plate 28 moves downward, the limit plate 28 gradually abuts against the side wall of the limit block 17, and even abuts against the bottom wall of the limit block 17, which will press a part of the raw gas downward until the limit plate 28 moves down to a length exceeding the length of the pressurizing column 27, the first sealing plate 24 will separate from the limit block 17, so that the raw gas is transferred into the cavity between the second sealing plate 25 and the limit plate 28. Under the action of the negative pressure spring 22, the limit plate 28 can continue to move downward. At this time, the raw gas will be decompressed and dried. The water vapor further separated from the raw gas will be absorbed by the desiccant block 31, so that the impurities in the raw gas will be further removed.
[0038] When the limit plate 28 is at the lowest point and moves upward: the gas that has been decompressed and dried in the previous process moves upward with the limit plate 28. After the first sealing plate 24 abuts against the limit block 17, the air pressure returns to normal. At this time, the cavity is transformed from the cavity between the second sealing plate 25 and the limit plate 28 to the cavity between the first sealing plate 24 and the limit plate 28. The limit plate 28 continues to move upward to pressurize the raw gas in the cavity, and the second sealing plate 25 is gradually reset to facilitate the subsequent replenishment of the raw gas. Until it is compressed to a certain pressure, the sealing block 3 moves to the highest position with the limit plate 28, so that the vent hole 32 is connected to the first outlet hole 121, so that the compressed gas will quickly flow through the first outlet hole 121 and contact with the outlet pipe 13 with a molecular sieve, so that the oxygen in the raw gas is separated. The outlet pipe 13 can be connected with a hose to connect with other higher precision refining equipment to improve the oxygen purity.
[0039] The above are only preferred embodiments of the present invention and are not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the protection scope of the present invention.
Claims
1. An apparatus for efficiently purifying oxygen, comprising a pure gas housing (12), characterized in that: The side wall of the pure gas shell (12) is provided with a plurality of first gas outlet holes (121) for transferring the purified gas, and the other side of the first gas outlet hole (121) is provided with a second gas outlet hole (124). The pure gas shell (12) is connected with a sealing cover (14) for ensuring that the pure gas shell (12) is sealed and performs preliminary filtering on the gas. A gasification component (2) for accelerating the purification of the gas after preliminary filtering is connected between the sealing cover (14) and the second gas outlet hole (124). The lower side of the gasification component (2) is connected with a limit plate (28) for piston movement with the inner wall of the pure gas shell (12), and the lower side of the limit plate (28) is connected with a driving component for driving the gasification component (2). The pure gas shell (12) is annularly fixedly connected with a plurality of heating pipes (6) for heating the gas in the pure gas shell (12), and the inner wall of the pure gas shell (12) is fixedly connected with a limit block (17) for cooperating with the gasification component (2) to complete the function.
2. The device for highly efficient oxygen purification according to claim 1, characterized in that: The gasification component (2) comprises a limiting sleeve (21), the limiting sleeve (21) is fixedly connected to the limiting plate (28), a pressure column (27) is slidably connected to the limiting sleeve (21), one end of the pressure column (27) away from the limiting sleeve (21) is fixedly connected to a first sealing plate (24), a pressure spring (23) is sleeved on the pressure column (27), and both ends of the pressure spring (23) are respectively connected to the limiting sleeve (28). The outer wall of the limit sleeve (21) is in contact with the first sealing plate (24), and the limit sleeve (21) is slidably connected with a limit plate (28), and the limit plate (28) is fixedly connected with a negative pressure column (26), and one end of the negative pressure column (26) away from the limit plate (28) is fixedly connected with a second sealing plate (25), and a negative pressure spring (22) is sleeved on the negative pressure column (26), and the two ends of the negative pressure spring (22) are respectively connected with the inner wall of the limit sleeve (21).
3. The device for highly efficient oxygen purification according to claim 2, characterized in that: The outer wall of the negative pressure column (26) is tightly fitted with the inner wall of the first sealing plate (24) and the inner wall of the pressure column (27) and is slidably connected. The upper side surface of the first sealing plate (24) abuts against the lower side surface of the limit block (17), and the lower side surface of the second sealing plate (25) abuts against the upper side surface of the limit block (17).
4. The device for highly efficient oxygen purification according to claim 1, characterized in that: The driving assembly comprises a flip block (41) and a motor (5); the flip block (41) is fixedly connected to the side of the limit plate (28) facing the bottom of the pure gas shell (12); the flip block (41) is rotatably connected to a flip plate (43); one end of the flip plate (43) away from the flip block (41) is rotatably connected to a shaking column (42); both ends of the shaking column (42) are rotatably connected to the pure gas shell (12); the motor (5) is fixedly connected to the outer wall of the pure gas shell (12); the driving shaft of the motor (5) passes through the pure gas shell (12) and is fixedly connected to one end of the shaking column (42).
5. The device for highly efficient oxygen purification according to claim 1, characterized in that: The pure gas shell (12) is provided with a heat preservation groove (123) in an annular shape, the heating pipe (6) is fixedly connected to the inner wall of the heat preservation groove (123), the pure gas shell (12) is provided with a gas gathering groove (122), each of the first gas outlet holes (121) is connected to the gas gathering groove (122), the second gas outlet holes (124) are connected to the gas gathering groove (122), the second gas outlet holes (124) are fixedly connected to a gas outlet pipe (13) facing outward, and a molecular sieve for separating oxygen is fixedly connected inside the gas outlet pipe (13).
6. The device for highly efficient oxygen purification according to claim 1, characterized in that: A plurality of desiccant blocks (31) are fixedly connected to the limiting plate (28), a sealing block (3) is fixedly connected to the upper side of each desiccant block (31), an air leakage hole (32) is provided on each desiccant block (31), and each sealing block (3) abuts against the inner wall of the pure gas housing (12).
7. The device for highly efficient oxygen purification according to claim 1, characterized in that: The sealing cover (14) is threadedly connected to the pure gas housing (12); a polymer filter element (16) is fixedly connected inside the sealing cover (14); and an air inlet pipe (15) is fixedly connected to the upper side of the sealing cover (14).
8. The device for highly efficient oxygen purification according to claim 1, characterized in that: A plurality of supporting legs (11) for supporting the pure gas housing (12) are fixedly connected to the lower side of the pure gas housing (12).
Citation Information
Patent Citations
Oxygen purification device for bulk gas supply
CN216259688U