CN206188385U - And controlling devic - Google Patents
And controlling devic Download PDFInfo
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- CN206188385U CN206188385U CN201621247885.6U CN201621247885U CN206188385U CN 206188385 U CN206188385 U CN 206188385U CN 201621247885 U CN201621247885 U CN 201621247885U CN 206188385 U CN206188385 U CN 206188385U
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- separation chamber
- separation
- oxygen
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- air
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- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The utility model relates to an and controlling devic, the device's constitution includes consecutive air inlet, gas flow controller, first order separation chamber, grade separation room and third level separation chamber, wherein, size, the structure of first order separation chamber, grade separation room and third level separation chamber are the same, and the front end of each staging room all is provided with the oxygenation membrane, is the separation passageway of full of liquid after the oxygenation membrane, and the top outer wall of separation passageway all is fixed with the magnet array, and the tail end of separation passageway all is provided with two air ducts from top to bottom respectively, and the air duct on upper portion links to each other with the inlet end of the separation chamber of next stage, and the air duct of lower part is as the nitrogen gas blast pipe. The utility model discloses a multistage separation, combine settings such as molecular sieve layer, oxygenation membrane, magnet array simultaneously to oxygen concentration has been improved effectively.
Description
Technical field
The technical solution of the utility model is related to general physical unit, specifically a kind of Magneto separate collection oxygen device.
Background technology
As energy crisis is further serious with environmental pollution, the mankind while research and development new energy is devoted to,
Making great efforts the efficiency of combustion of raising fuel.Burnt completely by fuel, while producing more multi-energy, reduce imperfect combustion and produce
Raw pollutant, such as carbon monoxide and nitric oxide etc..Research display according to investigations, oxygen content often improves 1%, burning in air
Efficiency can improve 10% or so.Current air separation technology both domestic and external is mainly membrane separation process, cryogenic distillation process, molecular sieve
Method, bacterium method, magnetic separation method.By gas with various, seepage velocity difference realizes that gas is separated to membrane separation process in the film, only
The membrane separation assemblies that air after change is constituted by doughnut, due to the effect of film both sides partial pressure difference, oxygen seepage velocity is fast
And oxygen-enriched air is obtained, the method must have fresh, clean atmospheric environment and the current country of hollow fiber film can't make
Make, thus spread difficulty is larger；Cryogenic distillation process is different using gasless liquefaction point, compresses low by air
Temperature produces gas with various, and the method cannot be used directly in engineering at present；Sieve method is with one by dry compressed air
Constant-pressure and time interval are alternately passed through in adsorption tower, and nitrogen molecular is adsorbed by zeolite molecular sieve, and oxygen molecule is flowed out by adsorption tower
Collect, the method remains unchanged and relies on clean atmosphere environment, dustiness is higher in the oxygen being collected into need to could use and divide through filtering
Son sieve service life is shorter.Wherein magnetic separation method is using the susceptibility difference of nitrogen oxygen, by nitrogen and oxygen separation in air.
There are patent application in day wood, the U.S., the former Soviet Union and Britain etc. successively.
Japan Patent, examined patent publication 42-15361 is using two methods of the combination of permanent-magnetism electromagnetic, in pipe front end first with forever
Magnetic array magnetizes air, the outer wall power-up magnet in pipe back, oxygen rich gas is enriched with near-wall, but the device is needed
Want external energy source and oxygen enrichment percentage is low；Chinese patent, ZLCN1986436A is to improve oxygen in water gas by magnetic field gradient
Concentration, by water treatment agent be placed on produce gradient magnetic V-groove in, using the paramagnetism of oxygen, when the oxygen in water is dense
Different magnetic field forces can be produced to act on when spending uneven so as to the air for driving water surface produces flowing, but this device needs pole
Electrical potential difference high, and increase containing air capacity also results in oxygen concentration rising in water, and nitrogen and oxygen separation are not realized really；
ZLCN201520249654.8, Cryogenic air is separated using superconducting magnetic separator, porous super by Cryogenic air access equipment, contacting
Oxygen is absorbed after leading film, and nitrogen passes through, so that oxygen concentration is improved, but the air that the device is utilized is low after processing
Warm air, and thin film separation nitrogen and oxygen are utilized, not can be visually seen magnetic field separation of nitrogen and oxygen；ZLCN1115260A,
It is to apply non-uniform magnetic-field in the stream of air, its magnetic field intensity gradient direction is not zero with the flow direction of air in a certain
Angle.The magnetic field force induced effect of oxygen is flowed along magnetic field intensity gradient direction, the enrichment region of oxygen is formed, in the enrichment region
Oxygen apply driving force and oxygen is overcome the constraint in magnetic field, flow into collecting region, form the stream of oxygen.But magnetic in the device
Corner dimension between field gradient direction and air-flow direction can not accurately determine, and the driving force for being applied will also consider
Many-side influence, experiment parameter control difficulty is larger；ZLCN2442740Y, the device be one without the hollow inverted conical outer cover of magnetic,
Welded with the outer shell phase of the semicircle for having oxygen cathete on top；Herein it is internal also place one with the upper hollow inverted cone of structure identical,
Multiple electromagnet or permanent magnet are placed around reverse taper.When a branch of air flows bottom-up, in magnetic field force effect
Under, nitrogen and oxygen separation are realized, but separative efficiency is relatively low.
Utility model content
The technical solution of the utility model is intended to improve oxygen concentration, there is provided a kind of Magneto separate collection oxygen device.The device exists
The method such as auxiliary oxygenation film, zeolite molecular sieve increases oxygen content in liquid environment, so as to improve oxygen concentration.
The technical solution of the utility model：
A kind of Magneto separate collection oxygen device, the composition of the device includes the air inlet, gas flow controller, the first order that are sequentially connected
Separation chamber, second level separation chamber and third level separation chamber；
Wherein, first order separation chamber, second level separation chamber are identical with the size of third level separation chamber, structure, are glass
The equilateral triangular prism structure of material, triangular prism horizontal positioned, top is plane；The front end of each grade of separation chamber is provided with oxygenation
Film, is hydraulically full split tunnel after oxygenation film, and the top exterior walls of split tunnel are all fixed with magnet array, split tunnel
Tail end be all respectively arranged with upper and lower two wireways, the wireway on top is connected with the inlet end of the separation chamber of next stage, under
The wireway in portion is used as nitrogen exhaust pipe；Wherein, molecular sieve layer, the third level are additionally provided with before the oxygenation film of first order separation chamber
The upper airway of separation chamber is oxygen collecting pipe；
Liquid in described split tunnel is water, pentane, ethanol, kerosene or organophosphorus ester.
The beneficial effects of the utility model are：
The utility model employs multi-stage separation.In combination with methods such as molecular sieve layer, oxygenation films, so as to effectively improve
Oxygen concentration.It is equal to all fuel and most industrial furnaces the device is mainly used for fields such as combustion-supporting, energy-conservation and environmental protection
It is applicable.It can not only improve the range of application of inferior fuel, and the combustibility of high-grade fuel can be given full play to again.With 22.9%
Air combustion with oxygen enrichment anthracite, efficiency of combustion can improve 19%.It is oxygen-enriched for non-ferrous metal metallurgy, not only can obvious energy-conservation,
Increase yield, but also SO2 concentration can be improved, to reclaim, so as to mitigate environmental pollution, with significant economic benefit and
Social benefit.With 22.9% oxygen-enriched air strengthening smelting process, 17% is can save energy.SO2 concentration improves 30%, and production capacity is carried
It is high by 20%.In addition it is oxygen-enriched to can be additionally used in other fields such as health care, petrochemical industry and fishery cultivating.
Brief description of the drawings
Fig. 1 is the structural representation of the utility model Magneto separate collection oxygen device；
Wherein, 1- air inlets；2- gas flow controllers；3- molecular sieve layers；4 first order oxygenation films, 9 second oxygenation films, 14
Three-level oxygenation film；5 first order separation chambers, 10 second level separation chambers, 15 third level separation chambers；6 first magnet arrays, 11 second magnetic
Volume array, 16 the 3rd magnet arrays；7th, 8,12,13,17,18 wireway.
Specific embodiment
It is as shown below, below in conjunction with the drawings and specific embodiments, further illustrate the utility model.Example is only used
In the present invention is explained, scope of the present utility model is not intended to limit.
Magneto separate collection oxygen device in the utility model is as shown in figure 1, the composition of the device includes the air inlet being sequentially connected
1st, gas flow controller 2, first order separation chamber 5, second level separation chamber 10 and third level separation chamber 15；
Wherein, first order separation chamber 5, second level separation chamber 10 are identical with the size of third level separation chamber 15, structure, are
The equilateral triangular prism structure of glass material, triangular prism horizontal positioned, top is plane；The front end of each grade of separation chamber is provided with
Oxygenation film, is hydraulically full split tunnel after oxygenation film；The top exterior walls of split tunnel are fixed with magnet array, separate logical
The tail end in road is respectively arranged with upper and lower two wireways, and the wireway on top is connected with the inlet end of the separation chamber of next stage, under
The wireway in portion is used as nitrogen exhaust pipe；Wherein, molecular sieve layer 3 is additionally provided with before the oxygenation film 4 of first order separation chamber 2, the
The upper airway of three-level separation chamber is oxygen collecting pipe.
Liquid in described split tunnel is water, pentane, ethanol, kerosene, organophosphorus ester, and the utility model is preferred
It is pentane.
The magnetic field intensity and intensity gradient product 2-3.5T of described magnet array2/m；
Described oxygenation film is polysulfones-composite silicone rubber membrane.
Described molecular sieve is specially zeolite.
Embodiment 1：
The concrete structure of described device is described as follows：
Air inlet 1 is connected with gas flow controller 2, and the other end of gas flow controller 2 is connected with first order separation chamber 5.
The front end of one-level separation chamber 5 sets gradually molecular sieve layer 3 and first order oxygenation film 4, and outer wall sets first order magnet array 6, the
The tail end of one-level separation chamber 5 sets two guide pipelines with pellicle：The air inlet phase of wireway 7 and second level separation chamber 10
Even；Wireway 8 derives nitrogen content gas higher.Second and third grade of separation chamber is set ibid.
The material and parameter of device are specially：
Wherein, gas flow controller (Taiwan An Zhou YCP-902-B) outlet speed is 4.0m3/min；Oxygenation film is public day nation
Rolling polysulfones-the composite silicone rubber membrane of department；Magnet is the magnet of Wenzhou Sheng Ci companies, is bonded with epoxy resin layer between magnet,
The magnetic field intensity and intensity gradient product 3.0T of formation2/m；The material of described pellicle is cellulose acetate；Triangular prism shaped glass
Glass separation chamber makes by oneself for laboratory, is 15 centimetres by rectangle poly (methyl methacrylate) plate and two pieces of length of sides long 35 centimetres wide 15 centimetres
Equilateral triangle poly (methyl methacrylate) plate glass cement is bonded and formed.
The utility model is to use track deflecting method mangneto partition method, and track is hydraulically full, makes gas in bubble mode
Separated, and used multi-stage separation, be effectively improved the oxygen concentration after separating.Air is passed through air inlet, by molecule
Screen layers, into after High-gradient Magnetic field areas, because oxygen is that paramagnetism is moved to magnetic field gradient place high, nitrogen is diamagnetism
Moved to the low place of magnetic field gradient, bubble occurs substantially deformation, and eventually hit tip and be broken into two bubbles.Oxygen concentration compared with
Bubble high enters next stage Disengagement zone through oxygenation film, and nitrogen is discharged from another outlet.
Operation：
When the device is operated, gas pressurized (for example can be by increasing air pump) injection air inlet, is adjusted by gas flow controller
Solar term stream size, air enters the triangular prism shaped glass separation chamber being liquid filled, by zeolite layer and oxygenation film, into ladder high
After degree field region (split tunnel), oxygen in the presence of itself paramagnetism to the place motion that magnetic field gradient is high, nitrogen by
Acted on to the low place motion of magnetic field gradient in diamagnetism, bubble occurs substantially deformation, encounters tip and be broken into two bubbles.Oxygen
Concentration bubble higher enters next stage Disengagement zone through oxygenation film, and nitrogen is discharged from wireway 8,13,18, and final oxygen exists
Collected with drainage at wireway 17, concentration can averagely improve 6.67%.
Oxygen concentration contrast before and after the experimental provision of table 1
Oxygen concentration can averagely be improved 6.67% through the practice detection present apparatus.
The utility model unaccomplished matter is known technology.
Claims (1)
1. a kind of Magneto separate collection oxygen device, it is characterized by the composition of the device include being sequentially connected air inlet, gas flow controller,
First order separation chamber, second level separation chamber and third level separation chamber；
Wherein, first order separation chamber, second level separation chamber are identical with the size of third level separation chamber, structure, are glass material
Equilateral triangular prism structure, triangular prism horizontal positioned, top is plane；The front end of each grade of separation chamber is provided with oxygenation film,
It is hydraulically full split tunnel after oxygenation film, the top exterior walls of split tunnel are all fixed with magnet array, split tunnel
Tail end is all respectively arranged with upper and lower two wireways, and the wireway on top is connected with the inlet end of the separation chamber of next stage, bottom
Wireway as nitrogen exhaust pipe；Wherein, molecular sieve layer, the third level point are additionally provided with before the oxygenation film of first order separation chamber
Upper airway from room is oxygen collecting pipe；
Liquid in described split tunnel is water, pentane, ethanol, kerosene or organophosphorus ester.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621247885.6U CN206188385U (en) | 2016-11-22 | 2016-11-22 | And controlling devic |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621247885.6U CN206188385U (en) | 2016-11-22 | 2016-11-22 | And controlling devic |
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| Publication Number | Publication Date |
|---|---|
| CN206188385U true CN206188385U (en) | 2017-05-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621247885.6U Expired - Fee Related CN206188385U (en) | 2016-11-22 | 2016-11-22 | And controlling devic |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110131718A (en) * | 2019-06-17 | 2019-08-16 | 云南简澜环保科技有限公司 | Microkinetic oxygen-enriching device |
-
2016
- 2016-11-22 CN CN201621247885.6U patent/CN206188385U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110131718A (en) * | 2019-06-17 | 2019-08-16 | 云南简澜环保科技有限公司 | Microkinetic oxygen-enriching device |
| CN110131718B (en) * | 2019-06-17 | 2024-03-19 | 云南简澜环保科技有限公司 | Micro-power oxygen-enriching device |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170524 Termination date: 20171122 |
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| CF01 | Termination of patent right due to non-payment of annual fee |