CN203392857U - Novel air separation oxygen production device - Google Patents
Novel air separation oxygen production device Download PDFInfo
- Publication number
- CN203392857U CN203392857U CN201320417611.7U CN201320417611U CN203392857U CN 203392857 U CN203392857 U CN 203392857U CN 201320417611 U CN201320417611 U CN 201320417611U CN 203392857 U CN203392857 U CN 203392857U
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- air
- oxygen
- dish
- air separation
- molecular sieve
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- Separation Of Gases By Adsorption (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The utility model discloses a novel air separation oxygen production device. The novel air separation oxygen production device comprises an air separation disc, an oxygen collecting disc and at least two molecular sieve pipelines which are communicated between the air separation disc and the oxygen collecting disc, wherein an air inlet is formed in the air separation disc, an air distribution valve connected to the air inlet is arranged on the air separation disc, an oxygen cavity is formed in the oxygen collecting disc, the two molecular sieve pipelines are of fan-shaped tubular structures and are arrayed into a cylindrical structure, and an oxygen guiding pipe is arranged in the oxygen cavity and is communicated to an oxygen outlet formed in the air separation disc. The novel air separation oxygen production device has the advantages that the size of the complete device is greatly reduced, the structure is relatively compact and firm, oxygen separated out is guided by the oxygen guiding pipe to the side where the air inlet is arranged, so that the connection and the air conveying are convenient, the whole device is generous and attractive in appearance and reasonable in structure.
Description
Technical field
The utility model relates to a kind of oxygenerator, the separated oxygenerator of especially a kind of novel air.
Background technology
Molecular-sieve oxygen generator generally adopts pressurization absorption normal pressure desorb (HP) method, carries out respectively identical working cycle, thereby realize continuous air feed by two adsorption towers.ZL200620062940.4 discloses a kind of molecular sieve oxygen generator, molecular sieve pipeline in this device is circular tube structure, be evenly arranged between air separation dish and oxygen set dish, but its circular tube structure is difficult to rational deployment, can not close-packed arrays, the oxygenerator volume of making is larger, structural instability, and its air inlet and oxygen outlet are distributed in the two ends of body, use inconvenient.
Utility model content
In order to solve the problems of the technologies described above, the utility model provides a kind of novel air separated oxygenerator, adopts fan-shaped molecular sieve pipeline arrangement architecture close to each other, and simple and practical, outward appearance is more attractive in appearance.
To achieve these goals, the technical scheme that the utility model adopts is:
The separated oxygenerator of a kind of novel air, comprise air separation dish, oxygen set dish and be communicated with the molecular sieve pipeline between air separation dish and oxygen set dish, described air separation dish is provided with inlet mouth and connected air slide valve, in described oxygen set dish, be provided with oxygen chamber, described molecular sieve pipeline is fan-shaped tubular structure, at least comprise two molecular sieve pipelines and rearrange cylindrical structure, in described oxygen chamber, being provided with airway and being communicated to the oxygen outlet arranging on air separation dish.
Further improvement as technique scheme, the card of described air separation dish and oxygen set dish is respectively equipped with the dish groove embedding for each molecular sieve pipe end, on described air separation dish, respectively coil trench bottom and be respectively equipped with uptake and be communicated with the valve block air outlet arranging in air slide valve, the dish trench bottom of oxygen set dish is respectively equipped with the gas off-take being communicated with oxygen chamber.
As the further improvement of technique scheme, the gas port of described gas off-take is periphery in oxygen chamber surrounding, and is provided with sealing-ring in described dish groove.
As the further improvement of technique scheme, the central task end face of described air slide valve is provided with pressurized air mouth and is communicated with air amount with the inlet mouth on air separation dish.
As the further improvement of technique scheme, the number of described molecular sieve pipeline is 6-12 bar.
The further improvement of technique scheme, described molecular sieve pipeline is provided with for importing the through hole of molecular sieve.
As the further improvement of technique scheme, on described air separation dish, be also provided with nitrogen relief outlet, and utilize the tripping device arranging on air separation dish that oxygen outlet, air inlet and the setting of nitrogen relief outlet are positioned to the same side.
The beneficial effects of the utility model: the utility model utilizes the molecular sieve pipeline of sector structure to replace traditional pipe, be arranged in right cylinder, arranging of each molecular sieve pipeline is tightr, improve space availability ratio, greatly reduce the volume of complete machine, structure is more stable firmly, cost-saving, and by airway, the oxygen of separating is led back, by tripping device, oxygen outlet, air inlet and the setting of nitrogen relief outlet are positioned to the same side, designs simplification, easy to use and flexible, generous attractive in appearance, the more reasonable structure of overall design.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, embodiment of the present utility model is described further.
Fig. 1 is one-piece construction schematic diagram of the present utility model.
Fig. 2 is the sectional view of Fig. 1.
Fig. 3 is the structural representation of molecular sieve pipeline in the utility model.
Fig. 4 is the combination assumption diagram of molecular sieve pipeline in the utility model.
Fig. 5 is the sectional view of Fig. 3.
Embodiment
Referring to figs. 1 through Fig. 4, the separated oxygenerator of a kind of novel air that the utility model provides, comprise air separation dish 1, oxygen set dish 2 and be communicated with the molecular sieve pipeline 3 between air separation dish 1 and oxygen set dish 2, described air separation dish 1 is provided with air intlet 11 and connected air slide valve 13, also be provided with nitrogen relief outlet to get rid of through separated nitrogen simultaneously, in described oxygen set dish 2, be provided with oxygen chamber 21, described molecular sieve pipeline 3 is fan-shaped tubular structure, at least comprises two molecular sieve pipelines 3 and rearranges cylindrical structure.In described oxygen chamber 21, be provided with airway 4 and be communicated to the oxygen outlet 12 arranging on air separation dish 1.In said structure, on described air separation dish 1, be also provided with nitrogen relief outlet, and utilize the tripping device arranging on air separation dish 1 that oxygen outlet, air inlet and the setting of nitrogen relief outlet are positioned to the same side, the right cylinder mid-way that described airway 4 is formed by arrangement connects, and structure is firmly practical.
In order to make structure close and firm more, the card of described air separation dish 1 and oxygen set dish 2 is respectively equipped with the dish groove embedding for each molecular sieve pipeline 3 ends, on described air separation dish 1, respectively coiling trench bottom is respectively equipped with uptake and is communicated with the valve block air outlet arranging in air slide valve 13, the dish trench bottom of oxygen set dish 2 is respectively equipped with the gas off-take being communicated with oxygen chamber 21, and the gas port of described gas off-take is periphery in oxygen chamber 21 surroundings.In described dish groove, be provided with sealing-ring, make structure tightr.
Preferably, the central task end face of described air slide valve 13 is provided with pressurized air mouth and is communicated with air amount with the air intlet 11 on air separation dish 1, and the air of suction is evenly distributed in each molecular sieve pipeline 3 by the rotation of air slide valve 13.
The number that adopts molecular sieve pipeline 3 in the present embodiment is 6 to 12, and on molecular sieve pipeline 3, be also provided with through hole 31, shown in Fig. 5, utilize conduit to insert in through hole 31 and pour into molecular sieve, after packing molecular sieve into, by piston, through hole 31 is sealed, without dismounting pipeline configuration, easy to use while changing molecular sieve.Owing to adopting the molecular sieve pipeline 3 of sector structure to replace traditional pipe, make to arrange between pipeline tightr, greatly reduce the volume of complete machine, structure is more firm, and generous attractive in appearance, the more reasonable structure of complete machine outward appearance.
The above, be preferred embodiment of the present utility model, and the utility model is not limited to above-mentioned embodiment, as long as it reaches technique effect of the present utility model with identical means, all should belong to protection domain of the present utility model.
Claims (8)
1. the separated oxygenerator of a novel air, comprise air separation dish (1), molecular sieve pipeline (3) between oxygen set dish (2) and connection air separation dish (1) and oxygen set dish (2), described air separation dish (1) is provided with air intlet (11) and connected air slide valve (13), in described oxygen set dish (2), be provided with oxygen chamber (21), it is characterized in that: described molecular sieve pipeline (3) is fan-shaped tubular structure, at least comprise two molecular sieve pipelines (3) and rearrange cylindrical structure, in described oxygen chamber (21), be provided with airway (4) and be communicated to the upper oxygen outlet (12) arranging of air separation dish (1).
2. the separated oxygenerator of a kind of novel air according to claim 1, it is characterized in that: the card of described air separation dish (1) and oxygen set dish (2) is respectively equipped with the dish groove embedding for each molecular sieve pipeline (3) end, on described air separation dish (1), respectively coil trench bottom and be respectively equipped with the valve block air outlet arranging in uptake and air slide valve (13) and be communicated with, the dish trench bottom of oxygen set dish (2) is respectively equipped with the gas off-take being communicated with oxygen chamber (21).
3. the separated oxygenerator of a kind of novel air according to claim 2, is characterized in that: the gas port of described gas off-take is periphery in oxygen chamber (21) surrounding.
4. the separated oxygenerator of a kind of novel air according to claim 2, is characterized in that: in described dish groove, be provided with sealing-ring.
5. the separated oxygenerator of a kind of novel air according to claim 1, is characterized in that: the central task end face of described air slide valve (13) is provided with pressurized air mouth and is communicated with air amount with the air intlet (11) on air separation dish (1).
6. the separated oxygenerator of a kind of novel air according to claim 1, is characterized in that: the number of described molecular sieve pipeline (3) is 6-12 bar.
7. according to the separated oxygenerator of a kind of novel air described in claim 1 or 6, it is characterized in that: described molecular sieve pipeline (3) is provided with the through hole (31) for importing molecular sieve.
8. the separated oxygenerator of a kind of novel air according to claim 1, it is characterized in that: on described air separation dish (1), be also provided with nitrogen relief outlet, and utilize the upper tripping device arranging of air separation dish (1) that oxygen outlet, air inlet and the setting of nitrogen relief outlet are positioned to the same side.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320417611.7U CN203392857U (en) | 2013-07-12 | 2013-07-12 | Novel air separation oxygen production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320417611.7U CN203392857U (en) | 2013-07-12 | 2013-07-12 | Novel air separation oxygen production device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203392857U true CN203392857U (en) | 2014-01-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320417611.7U Expired - Fee Related CN203392857U (en) | 2013-07-12 | 2013-07-12 | Novel air separation oxygen production device |
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| CN (1) | CN203392857U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106976842A (en) * | 2017-05-17 | 2017-07-25 | 崔泽龙 | Oxygenerator nitrogen oxygen separating shell |
| CN106984136A (en) * | 2017-05-17 | 2017-07-28 | 崔泽龙 | Oxygenerator nitrogen oxygen separating tower |
| CN113501501A (en) * | 2021-07-08 | 2021-10-15 | 合肥康居人智能科技有限公司 | Analysis sieve jar for oxygenerator |
-
2013
- 2013-07-12 CN CN201320417611.7U patent/CN203392857U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106976842A (en) * | 2017-05-17 | 2017-07-25 | 崔泽龙 | Oxygenerator nitrogen oxygen separating shell |
| CN106984136A (en) * | 2017-05-17 | 2017-07-28 | 崔泽龙 | Oxygenerator nitrogen oxygen separating tower |
| CN113501501A (en) * | 2021-07-08 | 2021-10-15 | 合肥康居人智能科技有限公司 | Analysis sieve jar for oxygenerator |
| CN113501501B (en) * | 2021-07-08 | 2023-10-13 | 合肥康居人医疗器械科技股份有限公司 | Analytical screen cylinder for oxygenerator |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140115 Termination date: 20140712 |
|
| EXPY | Termination of patent right or utility model |