CN202968101U - Oxygen generation system - Google Patents
Oxygen generation system Download PDFInfo
- Publication number
- CN202968101U CN202968101U CN 201220629025 CN201220629025U CN202968101U CN 202968101 U CN202968101 U CN 202968101U CN 201220629025 CN201220629025 CN 201220629025 CN 201220629025 U CN201220629025 U CN 201220629025U CN 202968101 U CN202968101 U CN 202968101U
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- oxygen
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- generation system
- oxygen generation
- air
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- Separation Of Gases By Adsorption (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The utility model belongs to the technical field of oxygen generation equipment, and particularly relates to an oxygen generation system. The problems of low work efficiency, low throughput of oxygen, short service life and the like of the existing oxygen generation device are solved. The oxygen generation system comprises an air compressor, an air tank, a dryer, an active carbon tower, an air buffer tank and an adsorption plant, which are sequentially connected. The oxygen generation system is characterized by also comprising an oxygen tank and an oxygen buffer tank, which are mutually connected; the adsorption plant is respectively connected with the oxygen tank and the oxygen buffer tank; and the oxygen tank is connected to the air tank for a product. The oxygen generation system has the advantages of reasonable design, simple structure, high adsorption efficiency, long service life, good oxygen generation effect and the like.
Description
Technical field
The utility model belongs to the oxygen generating plant technical field, especially relates to a kind of oxygen generation system.
Background technology
The assemblies such as existing oxygen generation system mainly divides air filter, gas blower, sound damper and valve and pipeline, watercooler, oxygen cleaner, oxygen buffer, automatic emptying device, and be linked in sequence with pipeline.The working process of oxygen generation system is roughly: raw air is through gas blower supercharging, watercooler cooling, enter the oxygen cleaner, in the oxygen cleaner, first remove moisture content by the active oxidation aluminium lamination of adsorption tower bottom, molecular sieve layer by adsorption tower top absorption nitrogen optionally again, with oxygen separation out, then, oxygen with finished product gas from the adsorption tower top by the finished product gas outlet pipe output that is provided with.This system is complex structure not only, and environmental pollution is serious, and the effect of regenerated molecular sieve is not ideal enough, and has affected the working efficiency of adsorption tower and the turnout of oxygen.
The problem that exists in order to improve prior art, people have carried out long-term exploration, have proposed various solutions.For example, Chinese patent literature discloses a kind of gas membrane separation type oxygen producing system [application number: 201020270774.3], comprise oxygen-enriching device, oxygen-enriching device comprises oxygen permeable membrane or hollow-fibre membrane, the pressure pump, the Power Drive Unit that also comprise unpowered part, described Power Drive Unit is connected with the pressure pump of unpowered part by friction wheel, and the pressure pump of described unpowered part is connected with oxygen-enriching device.
Such scheme has improved prior art to a certain extent, can be connected with multiple drive, does not use electric power, reaches the effect of energy-conserving and environment-protective.The defectives such as yet such scheme still exists the working efficiency of adsorption tower low, and the turnout of oxygen is low.
Summary of the invention
The purpose of this utility model is for the problems referred to above, provides a kind of reasonable in design, simple in structure, and adsorption efficiency is high, and long service life is produced the effective oxygen generation system of oxygen.
For achieving the above object, the utility model has adopted following technical proposal: this oxygen generation system, comprise the air compressor machine, air vessel, drying machine, activated carbon tower, air cushioning tank and the adsorption unit that connect successively, it is characterized in that, native system also comprises interconnective oxygen canister and oxygen surge tank, described adsorption unit and oxygen canister and oxygen surge tank are connected respectively, and described oxygen canister is connected to the product gas tank.
Further, in above-mentioned oxygen generation system, described oxygen canister and product are with being connected with the oxygen pressing device between gas tank.
Further, in above-mentioned oxygen generation system, described oxygen pressing device comprises at least two interconnective oxygen pressing machines.
In above-mentioned oxygen generation system, described adsorption unit comprises interconnective the first adsorption tower and the second adsorption tower, described the first adsorption tower be connected adsorption tower and be connected with the oxygen surge tank with oxygen canister respectively.
As a kind of technical scheme of comparatively optimizing, in above-mentioned oxygen generation system, described drying machine is freezing type drier.
Compared with prior art, the advantage of this oxygen generation system is: reasonable in design, simple in structure, adsorption efficiency is high, and long service life is produced oxygen effective.
Description of drawings
Fig. 1 is the structural representation that the utility model provides.
In figure, air compressor machine 1, air vessel 2, drying machine 3, activated carbon tower 4, air cushioning tank 5, adsorption unit 6, the first adsorption tower 61, the second adsorption tower 62, oxygen canister 7, oxygen surge tank 8, oxygen pressing device 9, oxygen pressing machine 91, product gas tank 10.
Embodiment
As shown in Figure 1, this oxygen generation system, comprise the air compressor machine 1, air vessel 2, drying machine 3, activated carbon tower 4, air cushioning tank 5 and the adsorption unit 6 that connect successively, also comprise interconnective oxygen canister 7 and oxygen surge tank 8, described adsorption unit 6 is connected with the oxygen surge tank with oxygen canister 7 and is connected respectively, and described oxygen canister 7 is connected to product with gas tank 10.
As a kind of technical scheme of comparatively optimizing, in the present embodiment, oxygen canister 7 and product are with being connected with oxygen pressing device 9 between gas tank 10, oxygen pressing device 9 comprises at least two interconnective oxygen pressing machines 91, adsorption unit 6 comprises interconnective the first adsorption tower 61 and the second adsorption tower 62, the first adsorption tower 61 be connected adsorption tower 62 and be connected with the oxygen surge tank with oxygen canister 7 respectively and be connected, drying machine 3 is freezing type drier.
Specific embodiment described herein is only to the explanation for example of the utility model spirit.The utility model person of ordinary skill in the field can make various modifications or replenishes or adopt similar mode to substitute described specific embodiment, but can't depart from spirit of the present utility model or surmount the defined scope of appended claims.
Although this paper has more used air compressor machine 1, air vessel 2, drying machine 3, activated carbon tower 4, air cushioning tank 5, adsorption unit 6, the first adsorption tower 61, the second adsorption tower 62, oxygen canister 7, oxygen surge tank 8, oxygen pressing device 9, oxygen pressing machine 91, product with terms such as gas tanks 10, do not get rid of the possibility of using other term.Using these terms is only in order to describe more easily and explain essence of the present utility model, and they are construed to any additional restriction is all contrary with the utility model spirit.
Claims (5)
1. oxygen generation system, comprise the air compressor machine (1), air vessel (2), drying machine (3), activated carbon tower (4), air cushioning tank (5) and the adsorption unit (6) that connect successively, it is characterized in that, native system also comprises interconnective oxygen canister (7) and oxygen surge tank (8), described adsorption unit (6) is connected 8 with oxygen canister (7) with the oxygen surge tank) be connected respectively, described oxygen canister (7) is connected to product gas tank (10).
2. oxygen generation system according to claim 1, is characterized in that, described oxygen canister (7) and product are with being connected with oxygen pressing device (9) between gas tank (10).
3. oxygen generation system according to claim 2, is characterized in that, described oxygen pressing device (9) comprises at least two interconnective oxygen pressing machines (91).
4. oxygen generation system according to claim 1, it is characterized in that, described adsorption unit (6) comprises interconnective the first adsorption tower (61) and the second adsorption tower (62), described the first adsorption tower (61) be connected adsorption tower (62) and be connected 8 with oxygen canister (7) with the oxygen surge tank respectively) be connected.
5. according to claim 1 and 2 or 3 or 4 described oxygen generation systems, is characterized in that, described drying machine (3) is freezing type drier.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220629025 CN202968101U (en) | 2012-11-23 | 2012-11-23 | Oxygen generation system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220629025 CN202968101U (en) | 2012-11-23 | 2012-11-23 | Oxygen generation system |
Publications (1)
Publication Number | Publication Date |
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CN202968101U true CN202968101U (en) | 2013-06-05 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 201220629025 Expired - Fee Related CN202968101U (en) | 2012-11-23 | 2012-11-23 | Oxygen generation system |
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CN (1) | CN202968101U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106006564A (en) * | 2016-06-30 | 2016-10-12 | 广州惠临空气分离设备有限公司 | Energy-saving type domestic oxygen generator with multi-stage air purification system |
CN106115626A (en) * | 2016-06-30 | 2016-11-16 | 广州惠临空气分离设备有限公司 | Household type mute oxygen generator containing multi-staged air cleaning system |
-
2012
- 2012-11-23 CN CN 201220629025 patent/CN202968101U/en not_active Expired - Fee Related
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106006564A (en) * | 2016-06-30 | 2016-10-12 | 广州惠临空气分离设备有限公司 | Energy-saving type domestic oxygen generator with multi-stage air purification system |
CN106115626A (en) * | 2016-06-30 | 2016-11-16 | 广州惠临空气分离设备有限公司 | Household type mute oxygen generator containing multi-staged air cleaning system |
CN106006564B (en) * | 2016-06-30 | 2018-11-30 | 广州惠临空气分离设备有限公司 | The energy-saving household oxygenerator of the purification system containing multi-staged air |
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Legal Events
Date | Code | Title | Description |
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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: 20130605 Termination date: 20151123 |