CN203247086U - Oxygen generating equipment - Google Patents
Oxygen generating equipment Download PDFInfo
- Publication number
- CN203247086U CN203247086U CN 201320292436 CN201320292436U CN203247086U CN 203247086 U CN203247086 U CN 203247086U CN 201320292436 CN201320292436 CN 201320292436 CN 201320292436 U CN201320292436 U CN 201320292436U CN 203247086 U CN203247086 U CN 203247086U
- Authority
- CN
- China
- Prior art keywords
- oxygen
- outlet
- cabin
- air inlet
- nitrogen
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Oxygen, Ozone, And Oxides In General (AREA)
- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model provides oxygen generating equipment which comprises a separation container, an air inlet, a zeolitic molecular screen, a nitrogen outlet, a vacuumizer and an oxygen outlet; wherein the air inlet, the nitrogen outlet and the oxygen outlet are formed in the separation container; the inner part of the separation container is divided into an oxygen cabin and a nitrogen cabin through the zeolitic molecular screen; the front part of the oxygen cabin is connected with the air inlet; the rear part of the oxygen cabin is connected with the oxygen outlet; each cabin is divided into 3 to 10 microcavities; the microcavities are communicated through small holes. The oxygen generating equipment can be used to reduce the concentration of the nitrogen step by step, so that more than 97% of highly-purified oxygen can be provided, and the oxygen generating equipment is suitable for middle large-sized hospitals or equipment needling oxygen.
Description
Technical field
The utility model relates to a kind of oxygen generating plant, especially PSA oxygen generator equipment.
Background technology
Present pressure-variable adsorption vacuum desorption (being called for short VPSA) oxygen generating plant, namely penetrate under the atmospheric condition, utilize the impurity such as the airborne nitrogen of the dedicated molecular sieve used selective adsorption of VPSA, carbonic acid gas and water, under the condition that vacuumizes, molecular sieve is carried out desorb, thereby circulation makes the higher oxygen of purity (90 ~ 94%).The VPSA energy consumption is lower, and larger its energy consumption of equipment is lower.
The VPSA oxygen generation system mainly is comprised of gas blower, vacuum pump, switching valve, adsorber and oxygen equilibrium tank.Raw air is pressurized to 0.3-0.5barg by Root's blower and enters wherein in the adsorber after the suction port strainer is removed dust granule.Filled with adsorbent in the adsorber, wherein moisture, carbonic acid gas, and a small amount of other gaseous fraction be loaded in the activated alumina of bottom in the adsorber ingress and adsorb, nitrogen is loaded in the zeolite molecular sieve on activated alumina top and adsorbs subsequently.And oxygen (comprising argon gas) drains into oxygen equilibrium tank from the adsorber top exit as gas product for non-absorbed component.
When this adsorber is adsorbed onto to a certain degree, the state that will reach capacity of sorbent material wherein, utilize vacuum pump that it vacuumized (with absorption opposite direction) by switching valve this moment, and vacuum tightness is 0.65-0.75barg.The moisture that has adsorbed, carbonic acid gas, nitrogen and a small amount of other gaseous fraction are drawn out of and drain into atmosphere, and sorbent material obtains regeneration.
But present structure is still too complicated, and purifying gas output is not very high.
Summary of the invention
The utility model provides a kind of gas yield high oxygen generating plant.
The utility model is achieved through the following technical solutions:
A kind of oxygen generating plant is characterized in that by separation vessel air inlet, the zeolite molecules screen cloth, nitrogen outlet, evacuator, oxygen outlet forms, and air inlet is arranged, nitrogen outlet on the separation vessel, oxygen outlet, separation vessel inside becomes oxygen cabin and nitrogen cabin by the zeolite molecular sieve grid, and the oxygen cabin front connects air inlet, and the back connects oxygen outlet, the cabin is divided into 3-10 microcavity, keeps aperture to be communicated with between the microcavity.
Progressive effect of the present utility model is: can utilize the concentration that reduces step by step nitrogen, thereby highly purified oxygen is provided.
Description of drawings
Accompanying drawing is synoptic diagram of the present utility model.
Wherein: 1, oxygen outlet; 2, the zeolite molecules screen cloth; 3, air inlet; 4, nitrogen outlet; 5, evacuator.
Embodiment
Below in conjunction with accompanying drawing the utility model is described further: oxygen generating plant is by separation vessel, air inlet 3, zeolite molecules screen cloth 2, nitrogen outlet 4, evacuator 5, oxygen outlet 1 forms, and air inlet 3 is arranged, nitrogen outlet 4 on the separation vessel, oxygen outlet 1, connect evacuator 5 on the nitrogen outlet, separation vessel inside becomes oxygen cabin and nitrogen cabin by zeolite molecules screen cloth 2 lattice, and the oxygen cabin front connects air inlet 3, the back connects oxygen outlet 1, the cabin is divided into 3-10 microcavity, keeps aperture UNICOM between the microcavity, connects evacuator 5 on the nitrogen outlet.
Prioritization scheme one, the oxygen outlet cross section is greater than 1/5 of air inlet.
Prioritization scheme two, zeolite molecules screen cloth are made into reciprocation type membrane separation net, improve the gas processing amount.
Adopt oxygen generating plant of the present utility model, can improve oxygen concentration and reach more than 97%, be fit to medium-and-large-sized hospital or oxygen demand equipment.
Claims (3)
1. an oxygen generating plant is characterized in that by separation vessel air inlet, the zeolite molecules screen cloth, nitrogen outlet, evacuator, oxygen outlet forms, and air inlet is arranged, nitrogen outlet on the separation vessel, oxygen outlet, separation vessel inside becomes oxygen cabin and nitrogen cabin by the zeolite molecular sieve grid, and the oxygen cabin front connects air inlet, and the back connects oxygen outlet, the cabin is divided into 3-10 microcavity, keeps aperture to be communicated with between the microcavity.
2. oxygen generating plant according to claim 1 is characterized in that the oxygen outlet cross section is greater than 1/5 of air inlet.
3. oxygen generating plant according to claim 1 is characterized in that the zeolite molecules screen cloth is made into reciprocation type membrane separation net.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320292436 CN203247086U (en) | 2013-05-27 | 2013-05-27 | Oxygen generating equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201320292436 CN203247086U (en) | 2013-05-27 | 2013-05-27 | Oxygen generating equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
CN203247086U true CN203247086U (en) | 2013-10-23 |
Family
ID=49373537
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201320292436 Expired - Fee Related CN203247086U (en) | 2013-05-27 | 2013-05-27 | Oxygen generating equipment |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN203247086U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106582191A (en) * | 2016-11-22 | 2017-04-26 | 杭州激湍流体科技有限公司 | Magnetic separation and oxygenation device |
CN110411147A (en) * | 2019-07-09 | 2019-11-05 | 珠海联创医疗科技有限公司 | A kind of medical oxygen generator with energy saving system |
-
2013
- 2013-05-27 CN CN 201320292436 patent/CN203247086U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106582191A (en) * | 2016-11-22 | 2017-04-26 | 杭州激湍流体科技有限公司 | Magnetic separation and oxygenation device |
CN110411147A (en) * | 2019-07-09 | 2019-11-05 | 珠海联创医疗科技有限公司 | A kind of medical oxygen generator with energy saving system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5221372B2 (en) | Combustible gas concentrating apparatus and combustible gas concentrating method | |
CN201692748U (en) | Emission control and recovery device of organic gases | |
TW436316B (en) | Pressure swing process and system using single adsorber and single blower for separating a gas mixture | |
CN104192807B (en) | A kind of oxygen generating plant system and technical process thereof | |
CN103058144B (en) | Vacuum pressure swing adsorption oxygen generation system and control method thereof | |
JPH0699035A (en) | Method for separating and recovering carbon dioxide in waste gas | |
CN203247086U (en) | Oxygen generating equipment | |
CN201930684U (en) | Non-deep-cold transforming, adsorbing and separating device for oxygen and argon mixture | |
CN101531342B (en) | Device and method for producing oxygen by means of pressure swing adsorption (PSA) by five beds | |
CN102380285B (en) | Method and device for concentrating coal mine exhaust gas by multi-tower vacuum pressure swing adsorption method | |
CN103738924A (en) | Oxygenerator | |
CN102091501A (en) | Upper and lower pressure-equalizing pressure swing adsorption method | |
CN112062095A (en) | Double-air-passage mixed flow oxygen and nitrogen making machine | |
CN117942706A (en) | Device system and method for preparing oxygen by rapid variable-pressure vacuum adsorption | |
CN102600699B (en) | Pressure-variable adsorption gas separation device | |
CN212655467U (en) | Adsorption vacuum desorption oxygen generation equipment | |
WO2023140238A1 (en) | Method and apparatus for manufacturing purified gas | |
CN210764320U (en) | Pressure swing adsorption device for stable negative pressure adsorption oxygen production | |
JPS61230715A (en) | Method for concentrating and recovering gas by using psa apparatus | |
CN210764337U (en) | Negative pressure adsorption high-purity nitrogen making device | |
CN211246029U (en) | Pressure swing adsorption device for negative pressure adsorption oxygen production | |
TWM626483U (en) | Vacuum pressure swing adsorption system for separation of carbon dioxide | |
CN209530468U (en) | A kind of pressure swing adsorption system with jet stream desorption | |
Wawrzyńczak et al. | Effect of desorption pressure on CO2 separation from combustion gas by means of zeolite 13X and activated carbon | |
JP2007277028A (en) | Method of producing high purity gaseous nitrogen |
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 | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131023 Termination date: 20160527 |