CN107572482B - A kind of self elevation adaption oxygen generation system and method for producing oxygen through - Google Patents
A kind of self elevation adaption oxygen generation system and method for producing oxygen through Download PDFInfo
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- CN107572482B CN107572482B CN201710910906.0A CN201710910906A CN107572482B CN 107572482 B CN107572482 B CN 107572482B CN 201710910906 A CN201710910906 A CN 201710910906A CN 107572482 B CN107572482 B CN 107572482B
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- 239000001301 oxygen Substances 0.000 title claims abstract description 189
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 189
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 187
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 230000006835 compression Effects 0.000 claims abstract description 33
- 238000007906 compression Methods 0.000 claims abstract description 33
- 239000007789 gas Substances 0.000 claims abstract description 16
- 238000010521 absorption reaction Methods 0.000 claims abstract description 11
- 238000011897 real-time detection Methods 0.000 claims abstract description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 18
- 238000001514 detection method Methods 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 238000012545 processing Methods 0.000 claims description 5
- 239000002808 molecular sieve Substances 0.000 claims description 4
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 238000005516 engineering process Methods 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- 238000007689 inspection Methods 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- 238000013461 design Methods 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- DOTMOQHOJINYBL-UHFFFAOYSA-N molecular nitrogen;molecular oxygen Chemical compound N#N.O=O DOTMOQHOJINYBL-UHFFFAOYSA-N 0.000 description 2
- 150000002926 oxygen Chemical class 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000003044 adaptive effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 230000009916 joint effect Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002640 oxygen therapy Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
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- Separation Of Gases By Adsorption (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The invention discloses a kind of self elevation adaption oxygen generation system and method for producing oxygen through, system includes air compression unit, oxygen absorbing unit processed, control unit, pressure sensing cell, wherein air compression unit is oxygen absorbing unit processed gas supply, control unit is for controlling air compression unit and oxygen absorbing unit processed, the pressure sensor of the pressure sensing cell is installed on oxygen absorbing unit processed, the operating pressure of real-time detection oxygen absorbing unit, after air compression unit is opened, pressure sensing cell real-time detecting system pressure value, control unit starts timing simultaneously, when system pressure value reaches setting value, control unit stops timing and calculates the air compression unit working time, control unit calculates height above sea level according to the air compression unit working time, and absorption and the denitrogen time of oxygen absorbing unit processed are controlled according to height above sea level.The present invention does not use the components such as altitude sensor, frequency converter, and cost is greatly saved, and guarantees that the concentration of oxygen processed reaches 90% or more.
Description
Technical field
The invention belongs to medical instruments fields, and in particular to a kind of self elevation adaption oxygen generation system and method for producing oxygen through.
Background technique
General oxygen generation system can produce 90% or more oxygen in region of no relief use, but because of highlands air
Thin, atmosphere forces down, and causes oxygen generation system in uplift plateau operation irregularity or produces the decline of oxygen ability.Recent domestic is developed extensively
The oxygenerators of various plateau types, some provide gas source by using powerful air compressor and are made into plateau type oxygenerator；
Some detects height above sea level by increasing pressure test device or plateau oxygen concentration detecting apparatus, at the same by increase frequency converter or
The number of compressor improves system dynamic；The portable oxygenerator scheme having is improved using direct current generator by changing motor speed
System dynamic is to improve oxygen concentration.
But this oxygen generating plant that gas source is provided by using powerful air compressor is defined as plateau type
Oxygenerator cannot work normally in plains region, cause the use scope of product to narrow, be limited by use environment.And pass through
Increase pressure test device or plateau oxygen concentration detecting apparatus and detect height above sea level, while by increasing frequency converter or compressor
Number improves system dynamic, considerably increases design and producing cost, while also increasing the volume and weight of machine, increases
The energy consumption of equipment.Using the portable oxygenerator scheme of direct current generator, define that the oxygen flow of output will not be very big, it may not
Meets the needs of oxygen therapy.
Summary of the invention
The technical problem to be solved by the invention is to provide one kind can adapt to operating air pressure environment automatically, and high concentration is made
The self elevation adaption oxygen generation system and method for producing oxygen through of oxygen.
To solve the above problems, the technical solution used in the present invention is:
A kind of self elevation adaption oxygen generation system, including the inspection of air compression unit, oxygen absorbing unit processed, control unit, pressure
Unit is surveyed, wherein air enters oxygen absorbing unit oxygen processed after air compression unit compresses, and control unit is for controlling air
The working condition of compression unit and oxygen absorbing unit processed, the pressure sensor of the pressure sensing cell are installed on oxygen absorption processed
The output end of the output end of unit, the operating pressure of real-time detection oxygen absorbing unit, pressure sensing cell connects control unit
Input terminal, after air compression unit is opened, pressure sensing cell real-time detecting system pressure value, while control unit starts
Timing, when system pressure value reaches setting value, control unit stops timing and calculates the air compression unit working time, controls
Unit calculates height above sea level according to the air compression unit working time, and according to height above sea level control the absorption (gas supply) of oxygen absorbing unit processed with
And denitrogen (exhaust) time, produce high-concentration oxygen.
It further, further include that the absorption of air accumulator and flow concentration detecting unit, wherein air accumulator import and oxygen processed is single
Member connects, and flow concentration detecting unit, the connection control of flow concentration detecting unit output end are installed in reservoir outlet pipeline
Unit input terminal processed.
It further, further include inlet air filtration unit for filtering the air, for being carried out to compressed air
The heat-sink unit of cooling and the noise-reduction unit that noise-reduction is carried out to entire oxygen generation system.
A kind of method for producing oxygen through of self elevation adaption oxygen generation system, this method are based on physics omnibus control system technology, pass through
Air compression unit compresses air, the absorption using the molecular sieve of oxygen absorbing unit processed to oxygen and nitrogen in air
The difference of ability comes oxygen and nitrogen separation, to obtain the oxygen of high concentration；Entire making oxygen by control unit into
Row control, the making oxygen the following steps are included:
1) judge the atmospheric pressure of equipment working environment, that is, determine height above sea level；
Control unit control air compression unit extracts air from external environment and is compressed first, and by compressed air
It is delivered to oxygen absorbing unit processed；Control unit starts timing, and real-time detecting system pressure value simultaneously, i.e., oxygen absorbing unit processed
Operating pressure is compared with setup pressure value, stops timing when system pressure value reaches setup pressure value, calculates timing
Time, the atmospheric pressure of equipment working environment, i.e. height above sea level are determined according to the time of timing；
2) oxygen absorbing unit control parameter processed is determined according to the atmospheric pressure that step 1) measures, controls oxygen absorbing unit oxygen processed
Process；
Different altitude height corresponding to the atmospheric pressure that step 1) is measured carries out segment processing, and different height above sea level sections is corresponding
Different oxygen absorbing unit control parameters processed；The control parameter mainly includes service life and denitrogen time, and height above sea level is higher, is supplied
Gas time and denitrogen time are longer, and control unit controls oxygen absorbing unit processed according to corresponding control parameter and carries out oxygen processed, are made
High-concentration oxygen.
Further, further comprising the steps of:
The oxygen concentration of oxygen made from step 2) is detected, the oxygen concentration obtained by detecting is lower than oxygenerator
When standard value, further oxygen absorbing unit control parameter processed is adjusted, adjustment mode is on the basis of existing control parameter
It is upper further to increase service life and evacuation time.
Wherein, the mode of service life and evacuation time is further increased are as follows: it is full to be not up to system in system working pressure
When with operating pressure, control service life and evacuation time respectively with small size time stepping increase, every stepping increase a step and
Oxygen concentration and system pressure value detection are carried out after 2min, if oxygen concentration not up to requires and pressure is less than system restriction, after
It is continuous to increase service life and evacuation time in a stepping manner, if system pressure value have reached equipment permission maximum value or
Oxygen concentration reaches requirement, then stops the adjusting to service life and evacuation time.Service life stepping amplitude is 0.1s, when exhaust
Between stepping amplitude be 0.085s.
The beneficial effects of adopting the technical scheme are that the present invention reaches setting by calculating system pressure value
The time of pressure value judges the external pressure and height above sea level of equipment local environment, and the gas supply by changing oxygen absorbing unit processed and
The denitrogen time improves system to the adaptability of different altitude height oxygen, easy to operate, easy to control, and does not use
The components such as specific altitude sensor, frequency converter, are greatly saved cost, optimize design, and product on plateau, put down
Former region can be used, and can guarantee that the concentration of oxygen processed reaches 90% or more.
Detailed description of the invention
Fig. 1 is oxygenerator modular construction schematic diagram of the present invention；
Fig. 2 is the atmospheric pressure decision flow chart of present device working environment；
Specific embodiment
Invention is described in further detail with reference to the accompanying drawing:
The present invention is the oxygen generation system and method for producing oxygen through of a kind of self elevation adaption.Oxygen generation system of the present invention passes through to system pressure
The detection of power (operating pressure of oxygen absorbing unit processed) judges the ambient pressure and atmospheric density situation of equipment work, in turn
Gas supply, exhaust (denitrogen) state for controlling oxygen generation system, are realized to the adaptive of different altitude height oxygen.This oxygen generation system and
Method for producing oxygen through can not only carry out oxygen processed in different altitude height, and can guarantee that the concentration of oxygen processed reaches 90% or more, be
Structure of uniting is simple, easy to control.
As shown in Figure 1, a kind of self elevation adaption oxygen generation system, including inlet air filtration unit, air compression unit, heat dissipation list
Member, oxygen absorbing unit, control unit, pressure sensing cell, air accumulator, flow concentration detecting unit and noise-reduction list processed
Member, wherein inlet air filtration unit is for filtering the air, and heat-sink unit is for cooling down to compressed air, noise-reduction
Unit is used to carry out entire oxygen generation system noise-reduction, and oxygen absorbing unit processed is for recycling oxygen processed, including one absorption of control
Nitrogen is discharged in tower absorption nitrogen oxygen producing and another adsorption tower, cleans sifting bed, air accumulator be used to produce oxygen enrichment and
Storage, control unit is for sensed system parameter (such as system pressure, oxygen concentration, flow) and control air compression unit and system
The work of oxygen absorbing unit；Wherein air accumulator import is connect with oxygen absorbing unit processed, and it is dense that flow oxygen is installed in reservoir outlet pipeline
Detection unit is spent, flow concentration detecting unit output end connects control unit input terminal；Air is compressed through air compression unit
Enter oxygen absorbing unit oxygen processed afterwards, control unit is used to control the work shape of air compression unit and oxygen absorbing unit processed
State, the pressure sensor of the pressure sensing cell are installed on oxygen absorbing unit output end processed, real-time detection oxygen absorbing unit
Operating pressure, pressure sensing cell output end connection control unit input terminal, when air compression unit open after, pressure
Detection unit real-time detecting system pressure value, while control unit starts timing, when system pressure value reaches setting value, control
Unit stops timing and calculates the air compression unit working time, and control unit calculates sea according to the air compression unit working time
It pulls out, and controls absorption and the denitrogen time of oxygen absorbing unit processed according to height above sea level, produce high-concentration oxygen.
For user convenience, it is additionally provided with biofilter and humidification bottle, the oxygen in air accumulator is successively dense through flow oxygen
Spend detection unit, biofilter, humidification bottle supply user (patient).Wherein biofilter is used for the filtering of bacterium, molecule
The filtering of dust is sieved, humidification bottle is used for oxygen humidification so as to for users to use.
Based on the method for producing oxygen through of above-mentioned oxygen generation system, this method is based on physics omnibus control system technology, passes through air pressure
Contracting unit compresses air, using the molecular sieve of oxygen absorbing unit processed to the adsorption capacity of oxygen and nitrogen in air
Difference comes oxygen and nitrogen separation, to obtain the oxygen of high concentration；Entire making oxygen is controlled by control unit,
The making oxygen the following steps are included:
1) judge the atmospheric pressure of equipment working environment, that is, determine height above sea level, process is as shown in Figure 2
Control unit control air compression unit extracts air from external environment and is compressed first, and by compressed air
It is delivered to oxygen absorbing unit processed；Control unit starts timing, and real-time detecting system pressure value simultaneously, i.e., oxygen absorbing unit processed
Operating pressure is compared with setup pressure value, stops timing when system pressure value reaches setup pressure value, calculates timing
Time, the atmospheric pressure of equipment working environment, i.e. height above sea level are determined according to the time of timing；
2) oxygen absorbing unit control parameter processed is determined according to the atmospheric pressure that step 1) measures, controls absorbing unit oxygen preparation
Different altitude height corresponding to the atmospheric pressure that step 1) is measured carries out segment processing, and different height above sea level sections is corresponding
Different oxygen absorbing unit control parameters processed；The control parameter mainly includes service life and denitrogen time, and height above sea level is higher, is supplied
Gas time and denitrogen time are longer, and control unit controls oxygen absorbing unit processed according to corresponding control parameter and carries out oxygen processed, are made
High-concentration oxygen.
In order to guarantee that standard that oxygen concentration obtained reaches 90% or more, the present invention are also carried out by oxygen concentration detection
Feedback control adjusts the control parameter of oxygen absorbing unit processed, specifically includes the following steps:
The oxygen concentration of oxygen made from step 2) is detected, the oxygen concentration obtained by detecting is lower than oxygenerator
When standard value, further oxygen absorbing unit control parameter processed is adjusted, adjustment mode is on the basis of existing control parameter
It is upper further to increase service life and evacuation time.
Oxygen workflow explanation processed:
The present invention is after opening oxygen generation system, and oxygen generation system first carries out atmospheric pressure identification, and (height above sea level of working environment is sentenced
It is disconnected).This identifies that work is completed by control unit and pressure sensing cell, and control unit is in control air compression unit work
While start timing, and real-time detecting system pressure value (oxygen absorbing unit operating pressure processed).For the system pressure for guaranteeing detection
Force value is accurate enough, and the sample frequency of pressure value cannot be too slow, and sample frequency, which must assure that, can effectively identify that pressure becomes
Change, meanwhile, for the consistency for reducing sampling error, increasing product, sampled pressure value need to pass through the disposal of gentle filter.When control is single
When member judges that system pressure value after processing reaches setup pressure value, the time of air compression unit work is calculated, no
The same working time corresponds to different external pressure force value (corresponding to different height above sea level).
The atmospheric pressure of equipment working environment in the present invention, the i.e. approximation to function of height above sea level and timing time are following passes
System:
Wherein, H is height above sea level, and T is timing time, and a, b are the coefficient value of function.The coefficient value of above-mentioned function is to pass through
The experiment of simulated high altitude environment or calibration test on the spot obtain the functional relation that data determine.The coefficient value of above-mentioned function is by air
The joint effect of compression unit capacity and oxygen absorbing unit adsorption capacity processed and volume of gas storage tank, therefore when air compression is single
When first gas supply capacity is different, oxygen absorbing unit adsorption capacity difference processed designs volume difference with air accumulator, the coefficient of above-mentioned function
Value all can be different.
The present invention, be to oxygen absorbing unit processed into before normal oxygen process processed after completing atmospheric pressure identification
Running parameter (mainly service life and evacuation time) is adjusted, to guarantee the air total amount entered in oxygen absorbing unit processed
The oxygen of corresponding amount is produced enough, and guarantees that operating pressure is suitable for the operating pressure of interior molecules sieve absorption nitrogen.It is specific to adjust
Adjusting method is as follows:
Control unit external pressure force value according to obtained in above-mentioned atmospheric pressure identification step (height above sea level angle value), is adopted
Segment processing is carried out to different height above sea levels with software program, different height above sea level sections corresponds to different control parameters, and control is single
Member identifies which height above sea level section is equipment be located at using software checking book method first, then carries out assignment to control parameter according to height above sea level section
Adjustment.Control parameter includes service life and the denitrogen time of oxygen absorbing unit processed, to guarantee that pressure is suitable, and is provided
Air capacity produce corresponding oxygen enough, when denitrogen, can sufficiently parse nitrogen.
Assuming that oxygen generation system of the invention sets operating altitude as 0-4000m, the relationship of this height above sea level and atmospheric pressure is herein
It is approximately linear relationship in range, can is that a height above sea level section divides with every increase 800m to height above sea level.Sentence in measurement
When disconnected outside atmospheric pressure, different altitude height, the time T that system pressure reaches preset value space-time air pressure contracting cell operation can not
Together.Assuming that equipment works in height above sea level 300m, height above sea level 3000m and tri- height above sea levels of height above sea level 3800m, then control unit detects
Time can be respectively T1, T2 and T3 (T1 < T2 < T3), control unit can provide according to built-in software program different respectively
Oxygen absorbing unit control parameter (referring to following table) processed: service life G1, G2 and G3 and exhaust (denitrogen) time P1, P2 and P3.
Wherein the relationship of T1, T2 and T3 are T1 < T2 < T3, which can control oxygen absorbing unit parameter processed: service life relationship is
G1 < G2 < G3, denitrogen time relationship are P1 < P2 < P3.
For system of the invention, one group of suitable data is as follows:
| Height above sea level (unit: rice) | 300 | 3000 | 3800 |
| Detection time (unit: second) | 8.0 | 12.5 | 17.4 |
| Service life (unit: second) | 5.6 | 8.4 | 11.0 |
| Evacuation time (unit: second) | 5 | 7 | 9 |
According to above-mentioned data, in the oxygen generation system equally configured, the functional relation of height above sea level and timing time is obtained
Are as follows:
Oxygen absorbing unit processed of the invention is by two identical adsorption tower groups at when adsorption tower gas supply thereto
When, the adsorption tower absorption nitrogen oxygen producing, while another adsorption tower carries out denitrogen so as to internal regenerating molecular sieve.There is electricity
Magnet valve is connected at the air inlet and exhaust (denitrogen) of two adsorption towers, and control unit is by changing the time of solenoid valve on-off to system
The intake and exhaust time of oxygen absorbing unit is accurately controlled.
Flow concentration detecting unit is used to detect the flow and concentration value of obtained oxygen, when detecting obtained oxygen
When concentration still relatively low (being lower than 90%), further the parameter of oxygen absorbing unit processed can be carried out according to current system pressure value
Adjustment, with oxygen effect most preferably processed.Adjustment mode is further increasing gas supply and evacuation time, further increases service life
With the mode of evacuation time are as follows: be not up to system saturation operating pressure (equipment in system working pressure (current system pressure value)
The maximum value of permission) when, service life and evacuation time are controlled respectively with small size time stepping increase, and every stepping increases by a step simultaneously
Oxygen concentration and system pressure value detection are carried out after 2min, if oxygen concentration not up to requires and pressure is less than system restriction,
Continue to increase service life and evacuation time in a stepping manner, if system pressure value have reached equipment permission maximum value or
Person's oxygen concentration reaches requirement, then stops the adjusting to service life and evacuation time.And service life stepping amplitude is 0.1s,
Evacuation time stepping amplitude is 0.085s.
For example, oxygenerator exports oxygen with the flow of 3L/min, if system working pressure distance reaches system saturation work
With 0.1s stepping increase, evacuation time is with 0.085s stepping increase, often there are also when larger surplus, can control service life for pressure
2min is judged according to the oxygen concentration and system pressure parameter value that detect, if oxygen concentration not up to requires and pressure does not surpass
System saturation operating pressure is crossed, continues to increase service life in a stepping manner and evacuation time is stopped if pressure has reached maximum
Only to the adjusting of service life and evacuation time, if oxygen concentration reaches requirement, also stop the tune to service life and evacuation time
Section.
Claims (6)
1. a kind of self elevation adaption oxygen generation system, including air compression unit, oxygen absorbing unit processed, control unit, pressure detecting
Unit, wherein air enters oxygen absorbing unit oxygen processed after air compression unit compresses, and control unit is for controlling air pressure
The working condition of contracting unit and oxygen absorbing unit processed, it is characterised in that: the pressure sensor of the pressure sensing cell is installed
Connect in the output end of the output end of oxygen absorbing unit processed, the operating pressure of real-time detection oxygen absorbing unit, pressure sensing cell
The input terminal for connecing control unit, after air compression unit is opened, pressure sensing cell real-time detecting system pressure value, same to time control
Unit processed starts timing, and when system pressure value reaches setting value, control unit stops timing and calculates air compression unit work
Make the time, control unit calculates height above sea level according to the air compression unit working time, and controls oxygen absorbing unit processed according to height above sea level
Absorption and denitrogen time, produce high-concentration oxygen.
2. self elevation adaption oxygen generation system according to claim 1, it is characterised in that: further include that air accumulator and flow oxygen are dense
Detection unit is spent, wherein air accumulator import is connect with oxygen absorbing unit processed, and the inspection of flow oxygen concentration is installed in reservoir outlet pipeline
Unit is surveyed, flow concentration detecting unit output end connects control unit input terminal.
3. self elevation adaption oxygen generation system according to claim 2, it is characterised in that: further include for being carried out to air
The inlet air filtration unit of filter, heat-sink unit for cooling down to compressed air and carries out noise reduction to entire oxygen generation system and disappears
The noise-reduction unit of sound.
4. a kind of method for producing oxygen through of self elevation adaption oxygen generation system, this method is based on physics omnibus control system technology, passes through sky
Gas compression unit compresses air, using the molecular sieve of oxygen absorbing unit processed to the adsorption energy of oxygen and nitrogen in air
The difference of power comes oxygen and nitrogen separation, to obtain the oxygen of high concentration；Entire making oxygen is carried out by control unit
Control, which is characterized in that the making oxygen the following steps are included:
1) judge the atmospheric pressure of equipment working environment, that is, determine height above sea level；
Control unit control air compression unit extracts air from external environment and is compressed first, and compressed air is conveyed
To oxygen absorbing unit processed；Control unit starts timing, and real-time detecting system pressure value, i.e., the work of oxygen absorbing unit processed simultaneously
Pressure is compared with setup pressure value, stops timing when system pressure value reaches setup pressure value, calculate timing when
Between, the atmospheric pressure of equipment working environment, i.e. height above sea level are determined according to the time of timing；
2) oxygen absorbing unit control parameter processed is determined according to the atmospheric pressure that step 1) measures, controls absorbing unit oxygen preparation；
Different altitude height corresponding to the atmospheric pressure that step 1) is measured carries out segment processing, and different height above sea level sections is corresponding different
Oxygen absorbing unit control parameter processed；The control parameter mainly includes service life and denitrogen time, and height above sea level is higher, when gas supply
Between and the denitrogen time it is longer, control unit controls oxygen absorbing unit processed according to corresponding control parameter and carries out oxygen processed, is made highly concentrated
Spend oxygen.
5. a kind of method for producing oxygen through of self elevation adaption oxygen generation system according to claim 4, it is characterised in that further include with
Lower step:
The oxygen concentration of oxygen made from step 2) is detected, the oxygen concentration obtained by detecting is lower than oxygenerator standard
When value, further oxygen absorbing unit control parameter processed is adjusted, adjustment mode be on the basis of existing control parameter into
One step increases service life and evacuation time.
6. a kind of method for producing oxygen through of self elevation adaption oxygen generation system according to claim 5, it is characterised in that: further plus
The mode of big service life and evacuation time are as follows: when system working pressure is not up to system saturation operating pressure, control gas supply
Respectively with small size time stepping increase, every stepping increases by a step and carries out oxygen concentration and system after 2min for time and evacuation time
Pressure value detection continues to increase gas supply in a stepping manner if oxygen concentration not up to requires and pressure is less than system restriction
Time and evacuation time stop if system pressure value has reached the maximum value of equipment permission or oxygen concentration reaches requirement
Adjusting to service life and evacuation time.
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Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN113195024B (en) * | 2018-12-29 | 2024-04-05 | 青岛精安医疗科技有限责任公司 | Oxygen generation system and method |
| CN109987584A (en) * | 2019-04-28 | 2019-07-09 | 陕西四海测控技术有限公司 | A vehicle-mounted oxygen generator suitable for low temperature and low pressure |
| CN111517281A (en) * | 2020-06-08 | 2020-08-11 | 可孚医疗科技股份有限公司 | Altitude-adaptive portable oxygen generator and oxygen generation method |
| CN112346488B (en) * | 2020-11-06 | 2024-01-30 | 西藏大学 | Highland diffuse type oxygen supply control method |
| CN112357888A (en) * | 2020-11-12 | 2021-02-12 | 中车大连机车车辆有限公司 | Oxygen generation method for plateau locomotive |
| CN112607710B (en) * | 2020-12-30 | 2022-10-28 | 青岛精安医疗科技有限责任公司 | Oxygen generation system and control method thereof |
| CN112675659B (en) * | 2020-12-31 | 2022-09-30 | 青岛精安医疗科技有限责任公司 | Oxygen generation system and molecular sieve health state monitoring method thereof |
| CN112815466A (en) * | 2021-01-27 | 2021-05-18 | 中铁第一勘察设计院集团有限公司 | Construction method of plateau railway oxygen regulation system |
| CN113415238A (en) * | 2021-06-15 | 2021-09-21 | 宁波越凡医疗科技有限公司 | Vehicle-mounted carsickness-prevention electrical stimulation system and method |
| CN113998673B (en) * | 2021-10-27 | 2023-03-07 | 北京科技大学 | A portable oxygen generator |
| CN114028668B (en) * | 2021-10-28 | 2023-06-09 | 中国船舶重工集团公司第七一八研究所 | Pulse gas quantity control method of pulse type oxygen making equipment |
| CN116603362A (en) * | 2023-05-19 | 2023-08-18 | 湖南比扬医疗科技有限公司 | Oxygen generator control system and oxygen generator |
| CN117970970B (en) * | 2024-03-15 | 2024-06-18 | 中山清匠电器科技有限公司 | Vpsa mode-based oxygen-making oil-free compressor and control system thereof |
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|---|---|---|---|---|
| CN105883723B (en) * | 2016-03-31 | 2018-07-24 | 中国人民解放军军事医学科学院卫生装备研究所 | The adaptive pressure swing adsorption oxygen of frequency conversion type height above sea level and method for producing oxygen through |
| CN105984849A (en) * | 2016-07-08 | 2016-10-05 | 上海东方压缩机厂有限公司 | Oxygen generator |
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2017
- 2017-09-29 CN CN201710910906.0A patent/CN107572482B/en active Active
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