CN1554466A - Variable pressure adsorptive oxygen making device suitable for high altitude area - Google Patents

Variable pressure adsorptive oxygen making device suitable for high altitude area Download PDF

Info

Publication number
CN1554466A
CN1554466A CNA2003101224707A CN200310122470A CN1554466A CN 1554466 A CN1554466 A CN 1554466A CN A2003101224707 A CNA2003101224707 A CN A2003101224707A CN 200310122470 A CN200310122470 A CN 200310122470A CN 1554466 A CN1554466 A CN 1554466A
Authority
CN
China
Prior art keywords
gas
adsorption tower
pressure
valve
adsorption
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.)
Granted
Application number
CNA2003101224707A
Other languages
Chinese (zh)
Other versions
CN1228128C (en
Inventor
刘应书
况成明
冯俊小
丁守全
崔红社
乐恺
侯庆文
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing University of Technology
University of Science and Technology Beijing USTB
Original Assignee
University of Science and Technology Beijing USTB
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by University of Science and Technology Beijing USTB filed Critical University of Science and Technology Beijing USTB
Priority to CN 200310122470 priority Critical patent/CN1228128C/en
Publication of CN1554466A publication Critical patent/CN1554466A/en
Application granted granted Critical
Publication of CN1228128C publication Critical patent/CN1228128C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The present invention relates to one variable pressure adsorbing oxygen making apparatus used in air separating field. The apparatus consists of oil-less air compressor, air cooler, adsorption tower, product oxygen storage tank, pneumatic valve, reducing valve, needle valve, flow meter, flow regulating valve and other parts. The present invention features the material air storage tank for stabilizing the pressure in the outlet of the adsorption bed, storing the exhausted air of the compressor during homogenizing pressure, reducing the fluctuation of product oxygen flow and reducing the influence of environment pressure on the performance of the apparatus. The present invention may be used in high altitude area over 4000 m to provide oxygen for breath of people, medical health care and industrial use.

Description

A kind ofly be suitable for the pressure swing adsorption oxygen making device that the high altitude localities is used
Technical field
The present invention relates to a kind of pressure swing adsorption oxygen making device in air separation field, be specially adapted to the high altitude localities.
Background technology
Pressure swing adsorption is proposed by people such as Skarstrom the earliest, its ultimate principle is to utilize the difference of different components equilibrium adsorption capacity, rate of diffusion on sorbent material in the mixed gas and adsorptive capacity to increase, reduce with pressure the characteristic that reduces with the pressure rising, under pressurized conditions, finish the adsorption separation process of mixed gas, the gaseous fraction desorb that is adsorbed under the pressure-lowering condition, adsorbent reactivation, thus the separation and the sorbent circulation of each component of realization mixed gas are used.Eighties of last century is since the eighties, and pressure swing adsorption has obtained using widely in the gas delivery industry.As sorbent material, utilizing the pressure-swing adsorption process separation of air can produce concentration is about 95% oxygen with zeolite molecular sieve.According to the difference of working pressure range, pressure-swing adsorption process can be divided into two kinds: (1) PSA flow process promptly has the absorption of pressure, normal pressure desorb flow process.General adsorptive pressure is 0.2~0.6MPa, adsorption bed desorb under the standard atmosphere pressure condition.This flow process is mainly used in the less separation of air oxygenerator of scale, and characteristics are that equipment is simple, but product recovery rate is low, energy consumption is higher.(2) VSA flow process, i.e. normal pressure absorption, vacuum desorption flow process.Adsorptive pressure is a normal pressure or a little more than barometric point, utilizes vacuum pump to vacuumize desorb.Be mainly used in larger gas separation unit, characteristics are product recovery rate height, and energy consumption is lower, but the equipment relative complex, the initial cost height.The barometric point of high altitude localities (refering in particular to height above sea level here above the area more than 4000 meters) is well below standard atmosphere pressure.Owing to be subjected to the influence of environmental stress, adopt the transformation fractionation by adsorption air oxygenerator of PSA flow process and VSA flow process often can not normally move or efficiently operation in the high altitude localities.But along with extensively carrying out of development of the West Regions and construction, grow with each passing day to the demand of oxygen in the high altitude localities.Therefore, be necessary to develop a kind of pressure swing adsorption oxygen making device that is applicable to the high altitude localities.
Summary of the invention
The object of the invention is to provide that a kind of equipment is simple, product recovery rate is high, energy consumption is lower, is applicable to the pressure swing adsorption oxygen making device of high altitude localities that being called has the pressure swing adsorption oxygen making device of pressing absorption low pressure desorb (being called for short LPSA) flow process.
A kind ofly be suitable for the pressure swing adsorption oxygen making device that the high altitude localities is used, by oil-free air compressor 1, air-cooler 2, adsorption tower 4, adsorption tower 5, product gas gas-holder 6, operated pneumatic valve 7,8,9,10,12,13,14, reducing valve 15, needle type valve 11, under meter 16, flow control valve 17 parts such as grade constitute, it is characterized in that being provided with in the device unstripped gas gas-holder 3, the effect of unstripped gas gas-holder 3 is a pressure of stablizing the adsorption bed outlet, store the compressor air-discharging in the pressure equalizing, reduce the influence of the fluctuation of product airshed and environmental stress device performance.Surpass area more than 4000 meters for height above sea level, because high altitude localities air rarefaction, system normally moves for assurance, the exhaust pressure of air compressor is 0.1~0.7Mpa, the volume of unstripped gas gas-holder is 1.1~3 times of adsorption tower volumetrical, and required raw material source of the gas capacity coupling is 21~50 times of product tolerance.
Whole prod making processes is: air enters air-cooler 2 coolings, the incoming stock gas gas-holder 3 of cooled gas after oil free compressor 1 compression.Pneumavalve 7,10 and 13 leaves, and valve 8,9,12,14 cuts out.This moment, adsorption tower 4 was in absorption phase, and adsorption tower 5 is in desorption phase.Enter adsorption tower 4 from the high pressure mixed gas of unstripped gas gas-holder 3 through valve 7, the adsorptive pressure in the adsorption tower is 0.2MPa~0.5MPa.In adsorption tower 4, the strong absorbed component-nitrogen in the unstripped gas is adsorbed the zeolite molecular sieve absorption in the tower.Weak absorbed component-oxygen in the unstripped gas is discharged from adsorption tower 4 outlets.Wherein a part enters product gas gas-holder 6 as product gas through pneumavalve 13, reducing valve 15.And another part oxygen reverse adsorption tower 5 that enters after needle type valve 11 step-downs that adsorption tower 4 produces cleans the molecular sieve bed that is in desorption state.The waste gas of the desorb of adsorption tower 5 directly is discharged in the surrounding environment through valve 10.Because the high altitude localities environmental stress is far below standard atmosphere pressure, this moment, adsorption tower 5 was equivalent to desorb under vacuum condition.Molecular sieve bed in adsorption tower 4 is near before saturated, and valve 7,8,9,10,13,14 cuts out, and valve 12 leaves.Adsorption tower 4 is finished absorption phase, and adsorption tower 5 is finished the desorption and regeneration stage.Subsequently, a part of gas in the adsorption tower 4 enters 5, two adsorption towers of adsorption tower through equalizing valve 12 and carries out pressure equalizing.Adsorption tower 4 pressure reduce, and adsorption tower 5 pressure raise, the oxygen components that recovery part mechanical energy and concentration are higher.In the pressure equalizing, two adsorption towers 4 and 5 all stop into unstripped gas.At this moment, the compressor expellant gas stores at unstripped gas gas-holder 3.After all the pressure stage finished, valve 8,9,14 left, and valve 7,10,12,13 cuts out, adsorption tower 4 decompression desorbs, adsorption tower 5 absorption of boosting.Before adsorption bed 5 reaches capacity, stop air inlet.Thereby finish a transformation sorption cycle cycle.Two adsorption towers are alternately finished absorption and desorption process just can produce oxygen continuously from the product end.Pressure in the absorption phase, adsorption tower is 0.2MPa~0.5MPa.Directly desorb under local barometric point (absolute pressure is less than 0.1MPa) condition did not adopt vacuum pump to vacuumize after adsorption tower reached capacity.When sea level elevation was 5000m, the desorption pressures of adsorption tower was (absolute pressure) about 0.05MPa.The product gas that obtains from the adsorption bed outlet enters product gas gas-holder 6 after reducing valve 15 decompressions.According to the actual needs, the oxygen concentration of product gas can be regulated between 80%-95%.
The present invention had both solved the problem that the source of the gas deficiency that the high altitude localities environment atmospheric pressure is low, air rarefaction caused and adsorptive pressure do not reach design load, made full use of the characteristics that subatmospheric helps the pressure-swing adsorption process desorb again, reached with vacuum pump and to vacuumize obtained effect.This pressure swing adsorption oxygen making device can be breathed and health care usefulness oxygen and relevant industrial oxygen for the construction of high altitude localities and staff provide, and has that equipment is simple, easy to adjust, the level of automation advantages of higher.
Description of drawings
Fig. 1 is a LPSA flow process making oxygen synoptic diagram.
Wherein: 1-compressor, 2-air-cooler, 3-unstripped gas gas-holder, 4, the 5-adsorption tower, 6-product gas gas-holder, 7,8,9,10,13, the 14-operated pneumatic valve, 12-equalizing valve, 15-reducing valve, 11-needle type valve, 16-under meter, 17-flow control valve
Embodiment
Embodiment 1, and air enters air-cooler 2 coolings after oil free compressor 1 compression.The incoming stock gas gas-holder 3 of cooled gas, the volume of unstripped gas gas-holder 3 are 1.2 times of adsorption tower volumetrical, and required raw material source of the gas capacity coupling is 25 times of product tolerance.Open pneumavalve 7,10 and 13, valve 8,9,12,14 cuts out, and this moment, adsorption tower 4 was in absorption phase, and adsorption tower 5 is in desorption phase.Enter adsorption tower 4 from the high pressure mixed gas of unstripped gas gas-holder 3 through valve 7, the adsorptive pressure in the adsorption tower is 0.2MPa.In adsorption tower 4, the strong absorbed component-nitrogen in the unstripped gas is adsorbed the zeolite molecular sieve absorption in the bed.Weak absorbed component-oxygen in the unstripped gas is discharged from the adsorption tower outlet.Wherein a part enters product gas gas-holder 6 as product gas through pneumavalve 13, reducing valve 15.And another part oxygen reverse adsorption tower 5 that enters after needle type valve 11 step-downs that adsorption tower 4 produces cleans the molecular sieve bed that is in desorption state.The waste gas of the desorb of adsorption tower 5 directly is discharged in the surrounding environment through valve 10.Molecular sieve bed in adsorption tower 4 is near before saturated, and valve 7,8,9,10,13,14 cuts out, and valve 12 leaves.Adsorption tower 4 is finished absorption phase, and adsorption tower 5 is finished the desorption and regeneration stage.Subsequently, a part of gas in the adsorption tower 4 enters 5, two adsorption towers of adsorption tower through equalizing valve 12 and carries out pressure equalizing.Adsorption tower 4 pressure reduce, and adsorption tower 5 pressure raise, the oxygen components that recovery part mechanical energy and concentration are higher.In the pressure equalizing, two adsorption towers 4 and 5 all stop into unstripped gas.At this moment, the compressor expellant gas stores at unstripped gas gas-holder 3.After all the pressure stage finished, valve 8,9,14 left, and valve 7,10,12,13 cuts out, adsorption tower 4 decompression desorbs, adsorption tower 5 absorption of boosting.Before adsorption bed 5 reaches capacity, stop air inlet.Thereby finish a transformation sorption cycle cycle.Two adsorption towers are alternately finished absorption and desorption process just can produce oxygen continuously from the product end.The product gas that obtains from the adsorption tower outlet enters product gas gas-holder 6 after the reducing valve decompression.According to actual needs, the oxygen concentration of product gas can be regulated between 80%-95%.
Embodiment 2, and air enters air-cooler 2 coolings after oil free compressor 1 compression.The incoming stock gas gas-holder 3 of cooled gas.The volume of unstripped gas gas-holder 3 is 1.5 times of adsorption tower volumetrical, and required raw material source of the gas capacity coupling is 30 times of product tolerance.Open pneumavalve 7,10 and 13, valve 8,9,12,14 cuts out.This moment, adsorption tower 4 was in absorption phase, and adsorption tower 5 is in desorption phase.Enter adsorption tower 4 from the high pressure mixed gas of unstripped gas gas-holder 3 through valve 7, the adsorptive pressure in the adsorption tower is 0.3MPa.In adsorption tower 4, the strong absorbed component-nitrogen in the unstripped gas is adsorbed the zeolite molecular sieve absorption in the tower.Weak absorbed component-oxygen in the unstripped gas is discharged from the adsorption tower outlet.Wherein a part enters product gas gas-holder 6 as product gas through pneumavalve 13, reducing valve 15.And another part oxygen reverse adsorption bed 5 that enters after needle type valve 11 step-downs that adsorption tower 4 produces cleans the molecular sieve bed that is in desorption state.The waste gas of the desorb of adsorption tower 5 directly is discharged in the surrounding environment through valve 10.Molecular sieve bed in adsorption tower 4 is near before saturated, and valve 7,8,9,10,13,14 cuts out, and valve 12 leaves.Adsorption tower 4 is finished absorption phase, and adsorption tower 5 is finished the desorption and regeneration stage.Subsequently, a part of gas in the adsorption tower 4 enters 5, two adsorption towers of adsorption tower through equalizing valve 12 and carries out pressure equalizing.Adsorption tower 4 pressure reduce, and adsorption tower 5 pressure raise, the oxygen components that recovery part mechanical energy and concentration are higher.In the pressure equalizing, two adsorption towers 4 and 5 all stop into unstripped gas.At this moment, the compressor expellant gas stores at unstripped gas gas-holder 3.After all the pressure stage finished, valve 8,9,14 left, and valve 7,10,12,13 cuts out, adsorption tower 4 decompression desorbs, adsorption tower 5 absorption of boosting.Before adsorption bed 5 reaches capacity, stop air inlet.Thereby finish a transformation sorption cycle cycle.Two adsorption towers are alternately finished absorption and desorption process just can produce oxygen continuously from the product end.The product gas that obtains from the adsorption tower outlet enters product gas gas-holder 6 after the reducing valve decompression.
Embodiment 3, and air enters air-cooler 2 coolings after oil free compressor 1 compression.The incoming stock gas gas-holder 3 of cooled gas.The volume of unstripped gas gas-holder 3 is 2 times of adsorption tower volumetrical, and required raw material source of the gas capacity coupling is 40 times of product tolerance.Open pneumavalve 7,10 and 13, valve 8,9,12,14 cuts out.This moment, adsorption tower 4 was in absorption phase, and adsorption tower 5 is in desorption phase.Enter adsorption tower 4 from the high pressure mixed gas of unstripped gas gas-holder 3 through valve 7, the adsorptive pressure in the adsorption tower is 0.5MPa.In adsorption tower 4, the strong absorbed component-nitrogen in the unstripped gas is adsorbed the zeolite molecular sieve absorption in the bed.Weak absorbed component-oxygen in the unstripped gas is discharged from the adsorption tower outlet.Wherein a part enters product gas gas-holder 6 as product gas through pneumavalve 13, reducing valve 15.And another part oxygen reverse adsorption tower 5 that enters after needle type valve 11 step-downs that adsorption tower 4 produces cleans the molecular sieve bed that is in desorption state.The waste gas of the desorb of adsorption tower 5 directly is discharged in the surrounding environment through valve 10.Molecular sieve bed in adsorption tower 4 is near before saturated, and valve 7,8,9,10,13,14 cuts out, and valve 12 leaves.Adsorption tower 4 is finished absorption phase, and adsorption tower 5 is finished the desorption and regeneration stage.Subsequently, a part of gas in the adsorption tower 4 enters 5, two adsorption towers of adsorption tower through equalizing valve 12 and carries out pressure equalizing.Adsorption tower 4 pressure reduce, and adsorption tower 5 pressure raise, the oxygen components that recovery part mechanical energy and concentration are higher.In the pressure equalizing, two adsorption towers 4 and 5 all stop into unstripped gas.At this moment, the compressor expellant gas stores at unstripped gas gas-holder 3.After all the pressure stage finished, valve 8,9,14 left, and valve 7,10,12,13 cuts out, adsorption tower 4 decompression desorbs, adsorption tower 5 absorption of boosting.Before adsorption bed 5 reaches capacity, stop air inlet.Thereby finish a transformation sorption cycle cycle.Two adsorption towers are alternately finished absorption and desorption process just can produce oxygen continuously from the product end.The product gas that obtains from the adsorption tower outlet enters product gas gas-holder 6 after the reducing valve decompression.
Embodiment 4, and air enters air-cooler 2 coolings after oil free compressor 1 compression.The incoming stock gas gas-holder 3 of cooled gas.The volume of unstripped gas gas-holder 3 is 3 times of adsorption tower volumetrical, and required raw material source of the gas capacity coupling is 50 times of product tolerance.Open pneumavalve 7,10 and 13, valve 8,9,12,14 cuts out.This moment, adsorption tower 4 was in absorption phase, and adsorption tower 5 is in desorption phase.Enter adsorption tower 4 from the high pressure mixed gas of unstripped gas gas-holder 3 through valve 7, the adsorptive pressure in the adsorption tower is 0.5MPa.In adsorption tower 4, the strong absorbed component-nitrogen in the unstripped gas is adsorbed the zeolite molecular sieve absorption in the bed.Weak absorbed component-oxygen in the unstripped gas is discharged from the adsorption tower outlet.Wherein a part enters product gas gas-holder 6 as product gas through pneumavalve 13, reducing valve 15.And another part oxygen reverse adsorption tower 5 that enters after needle type valve 11 step-downs that adsorption tower 4 produces cleans the molecular sieve bed that is in desorption state.The waste gas of the desorb of adsorption tower 5 directly is discharged in the surrounding environment through valve 10.Molecular sieve bed in adsorption tower 4 is near before saturated, and valve 7,8,9,10,13,14 cuts out, and valve 12 leaves.Adsorption tower 4 is finished absorption phase, and adsorption tower 5 is finished the desorption and regeneration stage.Subsequently, a part of gas in the adsorption tower 4 enters 5, two adsorption towers of adsorption tower through equalizing valve 12 and carries out pressure equalizing.Adsorption tower 4 pressure reduce, and adsorption tower 5 pressure raise, the oxygen components that recovery part mechanical energy and concentration are higher.In the pressure equalizing, two adsorption towers 4 and 5 all stop into unstripped gas.At this moment, the compressor expellant gas stores at unstripped gas gas-holder 3.After all the pressure stage finished, valve 8,9,14 left, and valve 7,10,12,13 cuts out, adsorption tower 4 decompression desorbs, adsorption tower 5 absorption of boosting.Before adsorption bed 5 reaches capacity, stop air inlet.Thereby finish a transformation sorption cycle cycle.Two adsorption towers are alternately finished absorption and desorption process just can produce oxygen continuously from the product end.The product gas that obtains from the adsorption tower outlet enters product gas gas-holder 6 after the reducing valve decompression.

Claims (2)

1. one kind is suitable for the pressure swing adsorption oxygen making device that the high altitude localities is used, by oil-free air compressor (1), air-cooler (2), adsorption tower (4), adsorption tower (5), product gas gas-holder (6), operated pneumatic valve (7), (8), (9), (10), (12), (13), (14), reducing valve (15), needle type valve (11), under meter (16), flow control valve parts such as (17) constitute, it is characterized in that being provided with in the device unstripped gas gas-holder (3), the effect of unstripped gas gas-holder (3) is a pressure of stablizing the adsorption bed outlet, store the compressor air-discharging in the pressure equalizing, reduce the influence of the fluctuation of product airshed and environmental stress device performance.
2. a kind of pressure swing adsorption oxygen making device as claimed in claim 1, the exhaust pressure that it is characterized in that air compressor (1) is 0.1~0.7Mpa, the volume of unstripped gas gas-holder (3) is 1.1~3 times of adsorption tower volumetrical, absorption phase, pressure in the adsorption tower is 0.2MPa~0.5Mpa, and required raw material source of the gas capacity coupling is 21~50 times of product tolerance.
CN 200310122470 2003-12-25 2003-12-25 Variable pressure adsorptive oxygen making device suitable for high altitude area Expired - Fee Related CN1228128C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200310122470 CN1228128C (en) 2003-12-25 2003-12-25 Variable pressure adsorptive oxygen making device suitable for high altitude area

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200310122470 CN1228128C (en) 2003-12-25 2003-12-25 Variable pressure adsorptive oxygen making device suitable for high altitude area

Publications (2)

Publication Number Publication Date
CN1554466A true CN1554466A (en) 2004-12-15
CN1228128C CN1228128C (en) 2005-11-23

Family

ID=34338664

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200310122470 Expired - Fee Related CN1228128C (en) 2003-12-25 2003-12-25 Variable pressure adsorptive oxygen making device suitable for high altitude area

Country Status (1)

Country Link
CN (1) CN1228128C (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103827021A (en) * 2011-09-13 2014-05-28 皇家飞利浦有限公司 Portable oxygen concentrator
CN110980651A (en) * 2019-12-27 2020-04-10 广西珂深威医疗科技有限公司 Oxygen generation system based on bidirectional complementary oxygen pressure equalization
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
CN114949647A (en) * 2022-06-06 2022-08-30 北京航空航天大学 System and method for extracting oxygen to prepare respiratory gas

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103827021A (en) * 2011-09-13 2014-05-28 皇家飞利浦有限公司 Portable oxygen concentrator
CN110980651A (en) * 2019-12-27 2020-04-10 广西珂深威医疗科技有限公司 Oxygen generation system based on bidirectional complementary oxygen pressure equalization
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
CN114949647A (en) * 2022-06-06 2022-08-30 北京航空航天大学 System and method for extracting oxygen to prepare respiratory gas

Also Published As

Publication number Publication date
CN1228128C (en) 2005-11-23

Similar Documents

Publication Publication Date Title
CN104066493B (en) Nitrogen-rich gas preparation method, gas separating method and nitrogen-rich gas preparation facilities
CN203144108U (en) Small pressure-swing adsorption nitrogen-making device
US9908078B2 (en) Methods and systems of enhanced carbon dioxide recovery
JP2008501514A (en) Gas separation method by two-stage full recovery transformer adsorption
WO2010129329A2 (en) Miniature oxygen concentrators and methods
JP5184885B2 (en) Production method of oxygen by three-stage transformer adsorption device
CN104058371A (en) Pressure swing adsorption gas production system and pressure swing adsorption gas production method
CN102133498A (en) Pressure swing adsorption method for simultaneously preparing high-purity hydrogen and carbon monoxide
RU101646U1 (en) PLANT FOR PRODUCING OXYGEN FROM ATMOSPHERIC AIR
CN201930684U (en) Non-deep-cold transforming, adsorbing and separating device for oxygen and argon mixture
CN100444933C (en) Pressure-changing adsorption method for recovering low-partial-pressure gas
CN1228128C (en) Variable pressure adsorptive oxygen making device suitable for high altitude area
CN203724982U (en) Two-stage series pressure swing adsorption oxygen generation system capable of improving oxygen recovery rate
CN103738925B (en) A kind of oxygenerator
CN2643985Y (en) Transformation and absorption device for high concentration oxygen by use of air separation
CN102976291A (en) Variable pressure adsorption nitrogen production equipment and method thereof
CN104418312A (en) Method for producing nitrogen through pressure swing adsorption (PSA)
CN101531342B (en) Device and method for producing oxygen by means of pressure swing adsorption (PSA) by five beds
CN100355484C (en) Pressure swing absorption decarbonization process and apparatus
WO2021207909A1 (en) Method of movable pressure swing adsorption oxygen production device
CN206328151U (en) Plasma cut special nitrogen making machine
CN101891154A (en) Indoor oxygen regulating equipment
CN100469686C (en) Method and equipment for separating oxygen from air
CN103801171A (en) Two-stage-tandem PSA (pressure swing adsorption) oxygen production system capable of increasing recovery rate of oxygen and operating method of two-stage PSA oxygen production system
CN103768891B (en) A kind of two-stage series connection swing adsorption oxygen generating system and method for operating thereof that can improve oxygen recovery rate

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee