CN105858610A - Highly-efficient molecular sieve oxygen generator - Google Patents
Highly-efficient molecular sieve oxygen generator Download PDFInfo
- Publication number
- CN105858610A CN105858610A CN201610179735.4A CN201610179735A CN105858610A CN 105858610 A CN105858610 A CN 105858610A CN 201610179735 A CN201610179735 A CN 201610179735A CN 105858610 A CN105858610 A CN 105858610A
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- China
- Prior art keywords
- adsorption tower
- molecular sieve
- valve
- oxygen
- gas
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
- C01B13/0262—Physical processing only by adsorption on solids characterised by the adsorbent
- C01B13/027—Zeolites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0001—Separation or purification processing
- C01B2210/0009—Physical processing
- C01B2210/0014—Physical processing by adsorption in solids
- C01B2210/0015—Physical processing by adsorption in solids characterised by the adsorbent
- C01B2210/0018—Zeolites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0046—Nitrogen
Abstract
The invention discloses a highly-efficient molecular sieve oxygen generator. The highly-efficient molecular sieve oxygen generator comprises an air inlet, an adsorption tower group connected with the air inlet, a purity analyzer and a gas recovery system, wherein the purity analyzer and the gas recovery system are in parallel connection; one end of the purity analyzer in parallel connection with the gas recovery system is connected with a gas output pipeline of the adsorption tower group; the other end of the purity analyzer is connected with an oxygen outlet; and the pipeline of the oxygen outlet is provided with a gas outlet control valve. The highly-efficient molecular sieve oxygen generator provided by the invention can continuously release oxygen, is highly-efficient and rapid, and can timely detect the purity of generated oxygen, wherein the oxygen with inadequate purity is timely recycled and returns to a tower for purification again, so the purity of the generated oxygen is guaranteed to achieve standards; meanwhile, continuous gas supply can be realized; resources are saved; and production efficiency is further improved at the same time.
Description
Technical field
The disclosure relates generally to oxygenerator, particularly relates to efficient molecular sieve oxygenerator.
Background technology
Molecular-sieve oxygen generator is with air as raw material, using 5A zeolite molecular sieve as adsorbent,
Use pressure-variable adsorption principle to purify oxygen, specifically utilize molecular sieve to oxygen and the selection of oxygen
Property absorption and make oxygen and oxygen separating method extract highly purified oxygen.
Traditional method is, when purity analysis instrument detects that oxygen is defective, i.e. closes and gives vent to anger
Valve, opens atmospheric valve simultaneously, by underproof for surge tank oxygen emptying.This method exists such as
Lower deficiency, first is that oxygen emptying causes huge energy waste；Second is during emptying
Consume substantial amounts of man-hour；3rd is to cause potential safety hazard.Therefore, the same of raw material is being wasted
Time reduce again production efficiency.
The most universal technique is to extract defective oxygen from the outlet of oxygen surge tank to return to absorption
Tower system processes again, owing to needing to block the defeated of the qualified oxygen of purity during processing
Supply gas stream, after purity is up to standard, opens the delivery air of oxygen again.The most in process of production
It cannot be guaranteed that the seriality that system is given vent to anger.
Summary of the invention
In view of drawbacks described above of the prior art or deficiency, it is desirable to provide a kind of efficient molecular sieve system
Oxygen machine.
On the one hand a kind of efficient molecular sieve oxygenerator is provided, including: air inlet, with described
The absorption tower system that air inlet connects, purity analysis instrument, gas recovery system, described purity
Analyser is in parallel with described gas recovery system,
Described purity analysis instrument one end in parallel with described gas recovery system is connected to described absorption
The gas outlet duct of tower system, the other end is connected to oxygen gas outlet；
It is also equipped with gas outlet control valve on the pipeline of described oxygen gas outlet.
The efficient molecular sieve oxygenerator that the present invention provides can releasing oxygen continuously, the most quickly,
And the purity producing oxygen can be detected in time, oxygen inadequate for purity is carried out timely
Reclaim, return tower weight and newly purify, it is ensured that produce the up to standard of oxygen purity, and can supply continuously
Gas, further increases production efficiency while economizing on resources.
Accompanying drawing explanation
By reading retouching in detail with reference to made non-limiting example is made of the following drawings
Stating, other features, purpose and advantage will become more apparent upon:
Fig. 1 is efficient molecular sieve oxygenerator structural representation in the embodiment of the present invention.
Detailed description of the invention
With embodiment, the application is described in further detail below in conjunction with the accompanying drawings.It is appreciated that
, specific embodiment described herein is used only for explaining related invention, rather than to this
Bright restriction.It also should be noted that, for the ease of describe, accompanying drawing illustrate only with
The part that invention is relevant.
It should be noted that in the case of not conflicting, the embodiment in the application and embodiment
In feature can be mutually combined.Describe this below with reference to the accompanying drawings and in conjunction with the embodiments in detail
Application.
Refer to Fig. 1, the embodiment of the present invention provides a kind of efficient molecular sieve oxygenerator, including:
Air inlet 1, the absorption tower system being connected with air inlet 1, purity analysis instrument 2, gas
Recovery system, purity analysis instrument 2 is in parallel with gas recovery system,
Purity analysis instrument 2 one end in parallel with gas recovery system is connected to adsorb the gas of tower system
Output channel 12, the other end is connected to oxygen gas outlet 6；
Gas outlet control valve it is also equipped with on the pipeline of oxygen gas outlet 6.
The efficient molecular sieve oxygenerator that the embodiment of the present invention provides can releasing oxygen continuously, efficiently
Quickly；The oxygen purity of the oxygen outlet of purity analysis instrument detection simultaneously, when oxygen purity is defective
Time, the closedown of gas outlet control valve, oxygenerator now the most outwards carries oxygen, and gas reclaims system
System is started working, and underproof for purity oxygen recovery is purified to adsorption tower, due to not
Outwards supply, oxygenerator is in low load condition, sheaf space very high purity on adsorption tower, passes through
Experiment measurement reaches 99.995%, and molecular sieve adsorption is very capable, therefore returns in adsorption tower not
Qualified oxygen, by Fast Purification, comes back in the surge tank neutralization buffer tank in recovery system surplus
Remaining defective oxygen mix, to improve the total purity of oxygen, typically can be extensive through 2-3 cycle
Supply, an and cycle time again is 150 seconds, has stopped the waste caused due to oxygen emptying
With the shortcoming that original system recovers service life length, save resource and improve efficiency.
Further, absorption tower system includes the first adsorption tower 3 and the second adsorption tower 4, and first inhales
It is connected between attached tower 3 with the second adsorption tower 4 and has valve system.
The embodiment of the present invention provides two adsorption towers, by controller control, two adsorption towers
Alternate cycles works, to realize producing continuously the purpose of high-quality oxygen.
Further, " connect between the first adsorption tower and the second adsorption tower and have valve system " specifically
For: the first adsorption tower top and the second adsorption tower top are connected to absorption by the first valve respectively
Tower system gas outlet duct；Second is passed through respectively with in the middle of the second adsorption tower in the middle of first adsorption tower
Valve is connected to air inlet；First adsorption tower bottom is passed through respectively with the second adsorption tower bottom
3rd valve is connected to air inlet and the 4th valve is connected to acoustic filter.
Further, the first adsorption tower top and described second adsorption tower top are also associated with the 3rd
Stop valve.Connect between the first adsorption tower and the second adsorption tower and have a lot of valves, control respectively
System enters adsorption tower and leaves the gas flow of adsorption tower, it is ensured that the accuracy of oxygenerator work.
Further, the first adsorption tower 3 and described second adsorption tower 4 are respectively provided with 5A boiling
Stone molecular sieve.Equipped with the 5A zeolite molecular sieve of high-quality as adsorbent in adsorption tower, one
Under fixed pressure, oxygen producing from air.The specifically compression through purge drying is empty
Gas, carries out pressurized adsorbent, decompression desorption in adsorber.The crystal of 5A zeolite molecular sieve is cage
Type structure, has the strongest cation and negative oxygen ion in bug hole, constitute the pole that polarity is extremely strong
Property molecular sieve, under polar molecule sieve effect, oxygen nitrogen creates the even level of induction, and the luring of oxygen nitrogen
The polarity of conductive coupling level and 5A zeolite molecular sieve produces a kind of induction force, and the nitrogen easily polarized produces
Raw induction force is far longer than the induction force that oxygen produces, therefore molecular sieve energy in the case of pressurization
Enough a large amount of absorption nitrogens, when absorption reaches balance, oxygen is enriched with discharge；Then reduce pressure
To other impurity such as normal pressure, the nitrogen that adsorbent desorption is adsorbed, it is achieved regeneration.In systems
Arranging two adsorption towers, a tower absorption produces another tower desorption and regeneration while oxygen, by PLC journey
Sequence automatically controls, and makes two tower alternate cycles work, to realize producing continuously the mesh of high-quality oxygen
's.
Further, purity analysis instrument 2 two ends are separately installed with the first electromagnetic valve 11 and the second electricity
Magnet valve 13.Purity analysis instrument needs the oxygen flowing out oxygenerator to carry out purity detecting by collection,
Connect electromagnetic valve at purity analysis instrument two ends respectively and can control to pass in and out the oxygen of purity analysis instrument
Amount, it is ensured that the accuracy of purity analysis instrument detection.
Further, gas recovery system includes: tubing, is connected with described tubing
Surge tank 5, described tubing include parallel connection gas flow to pipeline and gas effuser road.
Further, gas flows to the first stop valve 7 and the first check valve that pipeline includes being connected
9, described gas flows out the second stop valve 8 and the second check valve 10, institute that pipeline includes being connected
State the first check valve 9 and described second check valve 10 gas flow is contrary.In the embodiment of the present invention
Gas recovery system include surge tank, wherein equipped with through processing the oxygen that will flow out,
The air inlet of surge tank is connected with tubing；Wherein gas piping is when oxygen purity deficiency
Carry out what gas recovery purified again, therefore, two branch roads in parallel in gas piping are installed
Having check valve in opposite direction, a branch road air inlet, another branch road is by oxygen inadequate for purity
It is recycled in adsorption tower.
Further, one end that tubing is not connected with described surge tank 5 is connected to through valve
The gas outlet duct of described absorption tower system.The tubing other end is also connected with a valve so that
The work of this gas recovery system is more accurate.
The efficient molecular sieve oxygenerator that the embodiment of the present invention provides can releasing oxygen continuously, efficiently
Quickly, and can detect in time produce oxygen purity, by timely for oxygen inadequate for purity
Carrying out reclaim, return tower weight and newly purify, it is ensured that produce the up to standard of oxygen purity, and can
Supply, further increases production efficiency while economizing on resources continuously.
Above description is only the preferred embodiment of the application and saying institute's application technology principle
Bright.It will be appreciated by those skilled in the art that invention scope involved in the application, do not limit
In the technical scheme of the particular combination of above-mentioned technical characteristic, also should contain simultaneously without departing from
In the case of described inventive concept, above-mentioned technical characteristic or its equivalent feature carry out combination in any
And other technical scheme formed.Such as features described above and (but not limited to) disclosed herein
The technical characteristic with similar functions is replaced mutually and the technical scheme that formed.
Claims (9)
1. an efficient molecular sieve oxygenerator, it is characterised in that including: air inlet, with
The absorption tower system that described air inlet connects, purity analysis instrument, gas recovery system, described
Purity analysis instrument is in parallel with described gas recovery system,
Described purity analysis instrument one end in parallel with described gas recovery system is connected to described absorption
The gas outlet duct of tower system, the other end is connected to oxygen gas outlet；
It is also equipped with gas outlet control valve on the pipeline of described oxygen gas outlet.
Efficient molecular sieve oxygenerator the most according to claim 1, it is characterised in that described
Absorption tower system includes the first adsorption tower and the second adsorption tower, described first adsorption tower and described second
Connect between adsorption tower and have valve system.
Efficient molecular sieve oxygenerator the most according to claim 2, it is characterised in that described
" be connected between described first adsorption tower with described second adsorption tower and have valve system " particularly as follows:
Described first adsorption tower top is connected to by the first valve respectively with described second adsorption tower top
Described absorption tower system gas outlet duct；With described second adsorption tower in the middle of described first adsorption tower
Centre is connected to described air inlet by the second valve respectively；Described first adsorption tower bottom
With described second adsorption tower bottom respectively by the 3rd valve be connected to described air inlet and
4th valve is connected to acoustic filter.
Efficient molecular sieve oxygenerator the most according to claim 2, it is characterised in that described
First adsorption tower and described second adsorption tower are respectively provided with 5A zeolite molecular sieve.
Efficient molecular sieve oxygenerator the most according to claim 1, it is characterised in that described
Purity analysis instrument two ends are separately installed with the first electromagnetic valve and the second electromagnetic valve.
Efficient molecular sieve oxygenerator the most according to claim 1, it is characterised in that described
Gas recovery system includes: tubing, the surge tank being connected with described tubing, described
Tubing includes that the gas of parallel connection flows to pipeline and gas effuser road.
Efficient molecular sieve oxygenerator the most according to claim 6, it is characterised in that described
Gas flows to the first stop valve and the first check valve that pipeline includes being connected, described gas effuser
Road includes the second stop valve and the second check valve being connected, described first check valve and described second
Check valve gas flow is contrary.
Efficient molecular sieve oxygenerator the most according to claim 6, it is characterised in that described
Not tank connected with the described buffering one end of tubing is connected to the gas of described absorption tower system through valve
Body output channel.
Efficient molecular sieve oxygenerator the most according to claim 3, it is characterised in that described
First adsorption tower top and described second adsorption tower top are also associated with the 3rd stop valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610179735.4A CN105858610A (en) | 2016-03-25 | 2016-03-25 | Highly-efficient molecular sieve oxygen generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610179735.4A CN105858610A (en) | 2016-03-25 | 2016-03-25 | Highly-efficient molecular sieve oxygen generator |
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| Publication Number | Publication Date |
|---|---|
| CN105858610A true CN105858610A (en) | 2016-08-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610179735.4A Pending CN105858610A (en) | 2016-03-25 | 2016-03-25 | Highly-efficient molecular sieve oxygen generator |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145067A (en) * | 2016-08-31 | 2016-11-23 | 江苏嘉宇特种装备股份有限公司 | Plasma cutting special nitrogen making machine |
| CN109368597A (en) * | 2018-12-18 | 2019-02-22 | 上海穗杉实业股份有限公司 | A kind of oxygen generation system recycling unqualified oxygen and method |
| CN111659228A (en) * | 2020-06-30 | 2020-09-15 | 浙江勤策空分设备有限公司 | Working method of pressure swing adsorption oxygen equipment |
| CN112516749A (en) * | 2020-06-30 | 2021-03-19 | 浙江勤策空分设备有限公司 | Pressure swing adsorption oxygen equipment |
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| US5122164A (en) * | 1990-03-29 | 1992-06-16 | The Boc Group, Inc. | Process for producing oxygen enriched product stream |
| JP2000210525A (en) * | 1999-01-25 | 2000-08-02 | Ikiken:Kk | Operation control device in oxygen enriching device |
| CN1861246A (en) * | 2006-02-17 | 2006-11-15 | 成都安普环境技术有限公司 | Method for producing oxygen by using air as raw material |
| CN102502511A (en) * | 2011-11-01 | 2012-06-20 | 济南宝丰电气有限公司 | High-concentration oxygen generating plant with molecular sieves |
| CN104291280A (en) * | 2014-09-25 | 2015-01-21 | 江苏嘉宇流体装备有限公司 | High-efficiency molecular sieve nitrogen making machine |
| CN205556097U (en) * | 2016-03-25 | 2016-09-07 | 江苏嘉宇特种装备股份有限公司 | High -efficient molecular sieve oxygen generation machine |
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2016
- 2016-03-25 CN CN201610179735.4A patent/CN105858610A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5122164A (en) * | 1990-03-29 | 1992-06-16 | The Boc Group, Inc. | Process for producing oxygen enriched product stream |
| JP2000210525A (en) * | 1999-01-25 | 2000-08-02 | Ikiken:Kk | Operation control device in oxygen enriching device |
| CN1861246A (en) * | 2006-02-17 | 2006-11-15 | 成都安普环境技术有限公司 | Method for producing oxygen by using air as raw material |
| CN102502511A (en) * | 2011-11-01 | 2012-06-20 | 济南宝丰电气有限公司 | High-concentration oxygen generating plant with molecular sieves |
| CN104291280A (en) * | 2014-09-25 | 2015-01-21 | 江苏嘉宇流体装备有限公司 | High-efficiency molecular sieve nitrogen making machine |
| CN205556097U (en) * | 2016-03-25 | 2016-09-07 | 江苏嘉宇特种装备股份有限公司 | High -efficient molecular sieve oxygen generation machine |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145067A (en) * | 2016-08-31 | 2016-11-23 | 江苏嘉宇特种装备股份有限公司 | Plasma cutting special nitrogen making machine |
| CN109368597A (en) * | 2018-12-18 | 2019-02-22 | 上海穗杉实业股份有限公司 | A kind of oxygen generation system recycling unqualified oxygen and method |
| CN111659228A (en) * | 2020-06-30 | 2020-09-15 | 浙江勤策空分设备有限公司 | Working method of pressure swing adsorption oxygen equipment |
| CN112516749A (en) * | 2020-06-30 | 2021-03-19 | 浙江勤策空分设备有限公司 | Pressure swing adsorption oxygen equipment |
| CN111659228B (en) * | 2020-06-30 | 2022-05-06 | 佛山市美客医疗科技有限公司 | Working method of pressure swing adsorption oxygen equipment |
| CN112516749B (en) * | 2020-06-30 | 2022-07-05 | 上海海尔医疗科技有限公司 | Pressure swing adsorption oxygen equipment |
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Application publication date: 20160817 |