CN220214438U - Highly integrated oxygenerator molecular sieve adsorption tower - Google Patents
Highly integrated oxygenerator molecular sieve adsorption tower Download PDFInfo
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- CN220214438U CN220214438U CN202321757809.XU CN202321757809U CN220214438U CN 220214438 U CN220214438 U CN 220214438U CN 202321757809 U CN202321757809 U CN 202321757809U CN 220214438 U CN220214438 U CN 220214438U
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- molecular sieve
- adsorption
- adsorption tower
- air inlet
- exhaust pipe
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- 238000001179 sorption measurement Methods 0.000 title claims abstract description 108
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 62
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 239000002245 particle Substances 0.000 claims description 13
- 230000006835 compression Effects 0.000 claims description 8
- 238000007906 compression Methods 0.000 claims description 8
- 238000005192 partition Methods 0.000 claims description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 abstract description 8
- 239000001301 oxygen Substances 0.000 abstract description 8
- 230000010354 integration Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 8
- 239000008187 granular material Substances 0.000 description 5
- 230000007246 mechanism Effects 0.000 description 3
- 238000012856 packing Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model discloses a highly integrated oxygenerator molecular sieve adsorption tower, which relates to the technical field of molecular sieve adsorption towers and aims at solving the problems that two towers are often arranged in the existing molecular sieve adsorption tower, continuous oxygen production operation is realized through alternate work of the two towers, the two towers enable the integration degree of the molecular sieve adsorption tower to be low, and the occupied area of equipment is large. The integration level of the molecular sieve adsorption tower can be improved, the occupied area of equipment is reduced, and the effect of strong practicability is achieved.
Description
Technical Field
The utility model relates to the technical field of molecular sieve adsorption towers, in particular to a highly integrated oxygenerator molecular sieve adsorption tower.
Background
The molecular sieve adsorption tower is an important component in the contemporary oxygen generating equipment, and when air passes through the inside of the molecular sieve adsorption tower, the molecular sieve can absorb specific components in the air, so that the oxygen enrichment concentration of the discharged air is improved, and the molecular sieve adsorption tower is an indispensable part in the contemporary oxygen generating link.
The existing molecular sieve adsorption tower is often provided with two tower bodies, continuous oxygen production operation is realized through alternate work of the two tower bodies, and the arrangement of the two tower bodies enables the integration degree of the molecular sieve adsorption tower to be low, and the occupied area of equipment to be large.
Disclosure of Invention
The utility model aims to provide a highly integrated oxygenerator molecular sieve adsorption tower which can improve the integration degree of the molecular sieve adsorption tower, reduce the occupied area of equipment and has strong practicability.
In order to achieve the above purpose, the present utility model provides the following technical solutions:
the utility model provides a highly integrated oxygenerator molecular sieve adsorption tower, includes the adsorption tower, fixedly connected with inner baffle on the inner wall of adsorption tower, the both sides of inner baffle set up respectively to first absorption chamber and second absorption chamber, the inside in first absorption chamber and second absorption chamber is all fixed mounting has a molecular sieve casing, the inside packing of molecular sieve casing has the molecular sieve granule.
Through adopting above-mentioned technical scheme, can effectively replace current product to carry out efficient adsorption operation, can greatly reduced equipment's area simultaneously.
Further, an air inlet pipe is fixedly connected to the side surface of the adsorption tower, a compression air pump is fixedly arranged at the air inlet end of the air inlet pipe, two air outlet ports are formed in the air inlet pipe, and the two air outlet ports are respectively communicated with the inside of the first adsorption cavity and the inside of the second adsorption cavity.
By adopting the technical scheme, the original air can be ensured to enter the first adsorption cavity or the second adsorption cavity.
Further, an exhaust pipe is fixedly connected to the side surface of the adsorption tower, two air inlet ports are formed in the exhaust pipe and are respectively communicated with the inside of the first adsorption cavity and the inside of the second adsorption cavity, and an electromagnetic valve is respectively installed at the two air inlet ports of the exhaust pipe.
Through adopting above-mentioned technical scheme, can nimble convenient carry out management and control operation to the blast pipe.
Further, an exhaust pipe is fixedly connected to the side surface of the adsorption tower, a vacuum pump is fixedly installed at an air outlet port of the exhaust pipe, two air inlet ports are formed in the exhaust pipe, and the two air inlet ports of the exhaust pipe are respectively communicated with the inside of the first adsorption cavity and the inside of the second adsorption cavity.
Through adopting above-mentioned technical scheme, can effectually carry out the evacuation operation to the inside of first absorption chamber or second absorption chamber.
Further, two air outlet ports of the air inlet pipe are respectively and fixedly provided with an electromagnetic valve.
Through adopting above-mentioned technical scheme, can be nimble convenient carry out management and control operation to the intake pipe.
Further, two air inlet ports of the exhaust pipe are respectively fixedly provided with an electromagnetic valve.
Through adopting above-mentioned technical scheme, can nimble convenient carry out management and control operation to the exhaust tube.
According to the utility model, the interior of the adsorption tower is divided into the first adsorption cavity and the second adsorption cavity by the inner partition plate, the molecular sieve shells are respectively arranged in the first adsorption cavity and the second adsorption cavity, and the molecular sieve particles are filled in the molecular sieve shells, so that the first adsorption cavity and the second adsorption cavity can be alternately connected, the molecular sieve particles in the two molecular sieve shells can alternately work, and the desorption operation is carried out on the molecular sieve particles in the other molecular sieve shell during the working, the adsorption tower can continuously carry out high-efficiency molecular adsorption operation for a long time, the stable and continuous oxygen production operation is ensured, compared with the mode of alternately working by the two adsorption mechanisms, the integration degree of the adsorption tower is greatly improved, the occupied area of equipment is greatly reduced, and the whole practicability is effectively improved.
Drawings
FIG. 1 is a first perspective view of a three-dimensional structure of the present utility model;
FIG. 2 is a second perspective view of the three-dimensional structure of the present utility model;
fig. 3 is an internal structural view of the present utility model.
In the figure: 1. an adsorption tower; 2. an exhaust pipe; 3. an air inlet pipe; 4. a compression air pump; 5. an exhaust pipe; 6. a vacuum pump; 7. a molecular sieve shell; 8. molecular sieve particles; 9. an inner partition; 10. a first adsorption chamber; 11. and a second adsorption chamber.
Detailed Description
The process according to the utility model is described in further detail below with reference to the accompanying drawings.
Referring to fig. 3, a highly integrated oxygenerator molecular sieve adsorption tower, including adsorption tower 1, fixedly connected with inner baffle 9 on the inner wall of adsorption tower 1, the both sides of inner baffle 9 set up respectively to first adsorption chamber 10 and second adsorption chamber 11, the inside of first adsorption chamber 10 and second adsorption chamber 11 is equal fixed mounting has a molecular sieve casing 7, the inside packing of molecular sieve casing 7 has molecular sieve granule 8, wherein separate the inside of adsorption tower 1 into first adsorption chamber 10 and second adsorption chamber 11 through inner baffle 9, and respectively at the internally mounted molecular sieve casing 7 of first adsorption chamber 10 and second adsorption chamber 11, and fill molecular sieve granule 8 in the inside of molecular sieve casing 7, consequently, can switch on first adsorption chamber 10 and second adsorption chamber 11 in turn, make the inside molecular sieve granule 8 of two molecular sieve casings 7 can work in turn, and in the during operation to the inside molecular sieve granule 8 of another molecular sieve casing 7, this adsorption tower 1 can carry out high-efficient molecular adsorption operation for a long time, ensure that oxygen operation carries out the high-efficient adsorption operation in turn, the high-efficient absorption mechanism of the system of the present system has been compared, the high-efficient absorption device of the system has been improved, and the large-scale integrated device has been greatly improved, and the utility has been greatly improved.
Referring to fig. 1 and 2, an air inlet pipe 3 is fixedly connected to a side surface of an adsorption tower 1, a compression air pump 4 is fixedly arranged at an air inlet end of the air inlet pipe 3, two air outlet ports are formed in the air inlet pipe 3 and are respectively communicated with the inside of a first adsorption cavity 10 and the inside of a second adsorption cavity 11, an electromagnetic valve is fixedly arranged at each of the two air outlet ports of the air inlet pipe 3, and the electromagnetic valve on the air inlet pipe 3 can be utilized to control an air flow channel of the air inlet pipe 3, so that air supply operation for the first adsorption cavity 10 or the second adsorption cavity 11 can be ensured independently.
Referring to fig. 1, an exhaust pipe 2 is fixedly connected to a side surface of an adsorption tower 1, two air inlet ports are formed in the exhaust pipe 2 and are respectively communicated with the inside of a first adsorption cavity 10 and a second adsorption cavity 11, an electromagnetic valve is respectively mounted at the two air inlet ports of the exhaust pipe 2, the exhaust pipe 2 can be controlled by the electromagnetic valve on the exhaust pipe 2, and the first adsorption cavity 10 or the second adsorption cavity 11 can perform independent exhaust operation.
Referring to fig. 2, an exhaust pipe 5 is fixedly connected to a side surface of the adsorption tower 1, a vacuum pump 6 is fixedly installed at an air outlet port of the exhaust pipe 5, two air inlet ports of the exhaust pipe 5 are respectively communicated with the inside of the first adsorption cavity 10 and the inside of the second adsorption cavity 11, an electromagnetic valve is fixedly installed at each of the two air inlet ports of the exhaust pipe 5, the electromagnetic valve on the exhaust pipe 5 can be used for controlling the exhaust pipe 5, the vacuum pump 6 can be used for independently vacuumizing the inside of the first adsorption cavity 10 or the inside of the second adsorption cavity 11, and the molecular sieve particles 8 can be stably desorbed.
Working principle: when in use, the device is placed at a designated position, then the air inlet end of the compression air pump 4 is communicated with an external air filtering mechanism, then the electromagnetic valve on one of the pipelines of the air inlet pipe 3 is closed, so that the air outlet end of the compression air pump 4 is communicated with the inside of the first adsorption cavity 10, then the electromagnetic valve on one of the pipelines of the air outlet pipe 2 is closed, so that the first adsorption cavity 10 can stably exhaust, at the moment, the compression air pump 4 guides air into one side of the molecular sieve shell 7 inside the first adsorption cavity 10, high-pressure air passes through the molecular sieve shell 7 and the molecular sieve particles 8 filled inside the molecular sieve shell 7, then is placed on the other side of the molecular sieve shell 7, and then is discharged from the air outlet pipe 2, when the air passes through the inside of the molecular sieve particles 8, the molecular sieve particles 8 can absorb specific components in the air, so as to improve the oxygen-enriched coefficient of the discharged air in the air outlet pipe 2, after a period of adsorption, the air inlet pipe 3 and the other electromagnetic valve on the exhaust pipe 2 are opened, at the same time, so that the high-pressure air generated by the compression air pump 4 can enter the inside the second adsorption cavity 11, the molecular sieve shell 8, the molecular sieve particles 8 are lifted by the use of the molecular sieve shell 8, the air in the air outlet pipe 5, and the air pump 5 can be opened at the same time, and the vacuum-enriched air channel 5 can be opened, and the vacuum-adsorbed by the first electromagnetic valve 5 when the air particles are opened, and the vacuum-enriched air is opened, and the vacuum-phase-separated by the air particles, and the air is opened, and the vacuum-enriched air, and the air is opened, the molecular sieve particles 8 inside the second adsorption chamber 11 are subjected to a disaggregation operation.
The embodiments of the present utility model are all preferred embodiments of the present utility model, and are not intended to limit the scope of the present utility model in this way, therefore: all equivalent changes in structure, shape and principle of the utility model should be covered in the scope of protection of the utility model.
Claims (6)
1. The utility model provides a highly integrated oxygenerator molecular sieve adsorption tower, includes adsorption tower (1), its characterized in that: the adsorption tower is characterized in that an inner partition plate (9) is fixedly connected to the inner wall of the adsorption tower (1), two sides of the inner partition plate (9) are respectively provided with a first adsorption cavity (10) and a second adsorption cavity (11), a molecular sieve shell (7) is fixedly installed in each of the first adsorption cavity (10) and the second adsorption cavity (11), and molecular sieve particles (8) are filled in the molecular sieve shell (7).
2. A highly integrated oxygenerator molecular sieve adsorption column according to claim 1, wherein: the adsorption tower is characterized in that an air inlet pipe (3) is fixedly connected to the side surface of the adsorption tower (1), a compression air pump (4) is fixedly arranged at the air inlet end of the air inlet pipe (3), two air outlet ports are formed in the air inlet pipe (3), and the two air outlet ports are respectively communicated with the interiors of the first adsorption cavity (10) and the second adsorption cavity (11).
3. A highly integrated oxygenerator molecular sieve adsorption column according to claim 1, wherein: the adsorption tower is characterized in that an exhaust pipe (2) is fixedly connected to the side surface of the adsorption tower (1), two air inlet ports are formed in the exhaust pipe (2), the two air inlet ports are respectively communicated with the inside of the first adsorption cavity (10) and the inside of the second adsorption cavity (11), and an electromagnetic valve is respectively arranged at the two air inlet ports of the exhaust pipe (2).
4. A highly integrated oxygenerator molecular sieve adsorption column according to claim 1, wherein: the adsorption tower is characterized in that an exhaust pipe (5) is fixedly connected to the side surface of the adsorption tower (1), a vacuum pump (6) is fixedly installed at an air outlet port of the exhaust pipe (5), two air inlet ports are formed in the exhaust pipe (5), and the two air inlet ports of the exhaust pipe (5) are respectively communicated with the inside of the first adsorption cavity (10) and the inside of the second adsorption cavity (11).
5. A highly integrated oxygenerator molecular sieve adsorption column according to claim 2, wherein: two air outlet ports of the air inlet pipe (3) are respectively and fixedly provided with an electromagnetic valve.
6. The highly integrated oxygenerator molecular sieve adsorption column of claim 4, wherein: two air inlet ports of the air exhaust pipe (5) are respectively and fixedly provided with an electromagnetic valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321757809.XU CN220214438U (en) | 2023-07-06 | 2023-07-06 | Highly integrated oxygenerator molecular sieve adsorption tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321757809.XU CN220214438U (en) | 2023-07-06 | 2023-07-06 | Highly integrated oxygenerator molecular sieve adsorption tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220214438U true CN220214438U (en) | 2023-12-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321757809.XU Active CN220214438U (en) | 2023-07-06 | 2023-07-06 | Highly integrated oxygenerator molecular sieve adsorption tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220214438U (en) |
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2023
- 2023-07-06 CN CN202321757809.XU patent/CN220214438U/en active Active
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