WO2011039682A1 - Gas concentration arrangement - Google Patents
Gas concentration arrangement Download PDFInfo
- Publication number
- WO2011039682A1 WO2011039682A1 PCT/IB2010/054289 IB2010054289W WO2011039682A1 WO 2011039682 A1 WO2011039682 A1 WO 2011039682A1 IB 2010054289 W IB2010054289 W IB 2010054289W WO 2011039682 A1 WO2011039682 A1 WO 2011039682A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas
- discharge
- discharge chamber
- outlet
- output side
- Prior art date
Links
- 239000007789 gas Substances 0.000 claims abstract description 239
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000001301 oxygen Substances 0.000 claims abstract description 32
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 32
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 15
- 230000008878 coupling Effects 0.000 claims description 12
- 238000010168 coupling process Methods 0.000 claims description 12
- 238000005859 coupling reaction Methods 0.000 claims description 12
- 239000002808 molecular sieve Substances 0.000 claims description 8
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 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 8
- 239000012528 membrane Substances 0.000 claims description 5
- 230000001939 inductive effect Effects 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 2
- 230000001965 increasing effect Effects 0.000 abstract description 7
- 239000000203 mixture Substances 0.000 abstract description 5
- 238000010943 off-gassing Methods 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000008901 benefit Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910021536 Zeolite Inorganic materials 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 3
- 230000004907 flux Effects 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 238000002640 oxygen therapy Methods 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- 239000010457 zeolite Substances 0.000 description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 208000006545 Chronic Obstructive Pulmonary Disease Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 230000000306 recurrent effect Effects 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/0407—Constructional details of adsorbing systems
- B01D53/0438—Cooling or heating systems
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/12—Oxygen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/102—Nitrogen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40083—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
- B01D2259/40088—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating
- B01D2259/40098—Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by heating with other heating means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/45—Gas separation or purification devices adapted for specific applications
- B01D2259/4541—Gas separation or purification devices adapted for specific applications for portable use, e.g. gas masks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/818—Employing electrical discharges or the generation of a plasma
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2313/00—Details relating to membrane modules or apparatus
- B01D2313/18—Specific valves
Definitions
- the invention relates to the field of increasing the amount of a gas component in a gas mixture, especially of enriching air with oxygen.
- Oxygen therapy is the administration of Oxygen as a therapeutic modality. Oxygen therapy benefits the patient by increasing the supply of Oxygen to the lungs and thereby increasing the availability of Oxygen to the body tissues.
- the main homecare application of Oxygen therapy is for patients with severe chronic obstructive pulmonary disease (COPD), a disease that affects more than 13 million patients in the US.
- COPD chronic obstructive pulmonary disease
- W098/56488 discloses an oxygen concentrator, which has a first molecular sieve bed connected to a four- way valve, which either joins the sieve bed to a pressurized air source or alternatively vents it to atmosphere.
- a second molecular sieve bed is also joined to the four- way valve in a corresponding manner.
- the first and the second molecular sieve bed adsorb gas components like nitrogen, carbon monoxide, carbon dioxide and water vapor.
- One bed is joined to the compressed air to produce oxygen-enriched air while the other is vented to atmosphere to cause evacuation.
- the sieve beds are joined at the outlet end to a product reservoir.
- the oxygen-enriched product gas passes from the reservoir to the patient.
- the oxygen concentrator comprises a compressor unit.
- the gas arrangement comprises:
- a discharge chamber including an input side and an output side, a gas discharge device for generating a gas discharge inside the discharge chamber for generating a pressure gradient on the output side and/or the input side of the discharge chamber, and
- a gas selection device which is arranged on the input side or the output side of the chamber and which is exposable to a gas flow generated by the pressure gradient.
- the gas concentration arrangement according to the invention comprises a gas discharge device for generating pressurized gas by generating a plasma.
- a pressure in the discharge chamber can be increased during high power-operation of the plasma, and the pressure can be decreased during low power operation or turning off the plasma.
- a pressure swing can be obtained by running a power-modulated discharge in the discharge chamber.
- Generating pressurized gas by a discharge device in a discharge chamber has advantages with respect to cost price, servicing and noise.
- a further advantage is that the pressurized air is intrinsically disinfected and sterilized.
- the gas selection device selects one or more gas components of a gas mixture, preferably air, for example by adsorption or by absorption of this one or more gas
- gas selection device Such gas components are hindered by the gas selection device to flow through. Therefore, the gas mixture, which flows through the gas selection device, is enriched with those one or more gas components, which may easily flow through the gas selection device.
- the gas selection device is nitrogen selective and oxygen non-selective.
- the gas mixture, which exits the gas selection device is enriched with oxygen.
- the gas selection device comprises at least one selective molecular sieve and/or one selective membrane.
- Preferred materials, which can be used for a molecular sieve or a selective membrane, are zeolite, carbon or polyamid. These materials select gas components mainly by adsorption.
- the gas discharge device comprises a coupling device to generate a gas discharge by capacitive, inductive, surface wave and/or microwave coupling.
- the coupling device is arranged outside the gas discharge chamber.
- the wearing down of parts of the coupling device, especially of electrodes, can be significantly reduced.
- the gas concentration arrangement comprises, in addition, an inlet valve, which is arranged on the input side of the discharge chamber, and an outlet valve, which is arranged on the output side.
- an inlet valve which is arranged on the input side of the discharge chamber
- an outlet valve which is arranged on the output side.
- the gas concentration arrangement comprises, in addition, a gas reservoir, which is arranged on the output side or on the input side of the discharge chamber. Even if operating the gas discharge device with a power-modulated discharge, a nearly constant over pressure or under pressure can be generated in the reservoir, which can be used for producing a continuous gas flow, preferably by using a valve or an orifice on an outlet or an inlet of the reservoir.
- the gas concentration arrangement comprises, in addition, an exhaust gas outlet device to blow of exhaust gas generated by the gas selection device.
- the discharge chamber comprises a gas inlet, a first gas outlet and a second gas outlet, wherein the gas outlet device is connected to the first gas outlet and the gas discharge device is connected to the second gas outlet.
- the gas concentration system according to the invention comprises at least two inventive gas concentration arrangements, wherein the two arrangements are joined on their output side.
- Such a gas concentration system is able to provide a nearly continuous gas flow by operating a first arrangement and a second arrangement phase shifted, especially in an antiparallel manner.
- the gas pump according to the invention comprises a discharge chamber including an input side and an output side, a gas discharge device for generating a gas discharge inside the discharge chamber for generating a pressure gradient on the output side and/or the input side of the discharge chamber, and an inlet valve, which is arranged on the input side of the discharge chamber, and an outlet valve, which is arranged on the output side.
- Fig. 1 is a schematic view of a first embodiment of a gas concentration arrangement in a state of generating a gas flow through the gas selection device by use of a high-power plasma;
- Fig. 2 is a schematic view of the first embodiment of a gas concentration arrangement in a state of outgassing of the gas selection device;
- Fig. 3 is a schematic view of the first embodiment of a gas concentration arrangement in a state of filling the discharge chamber with fresh gas;
- Fig. 4 is a schematic view of a second embodiment of a gas concentration arrangement
- Fig. 5 is a schematic view of a third embodiment of a gas concentration arrangement
- Fig. 6 is a schematic view of a fourth embodiment of a gas concentration arrangement
- Fig. 7 is another schematic view of the first embodiment of a gas concentration arrangement
- Fig. 8 is a schematic view of a fifth embodiment of a gas concentration system
- Fig. 9 is a schematic view of a sixth embodiment of a gas concentration arrangement
- Fig. 10 is a diagram displaying a rms-current in dependence of time
- Figs. 1 to 3 display a first embodiment of a gas concentration arrangement according to the invention. This first embodiment is also displayed in Fig. 7.
- the gas concentration arrangement comprises a discharge chamber 1 including an input side and an output side, a gas discharge device 2 for generating a gas discharge inside the discharge chamber 1 for generating a pressure gradient on the output side of the discharge chamber 1, and a gas selection device 3, which is arranged on the output side of the chamber 1 and which is exposable to a gas flow generated by the pressure gradient.
- the "input side” of the discharge chamber 1 is the side of the discharge chamber 1 from which gas flows into the chamber 1
- the "output side” of the discharge chamber 1 is the side of the discharge chamber 1 , where gas flows out of the discharge chamber 1.
- the gas discharge device comprises a coupling device to generate a gas discharge by capacitive, inductive, surface wave and/or microwave coupling, and an energy source 10 to provide the coupling device with an alternating current.
- the coupling device comprises two electrodes 1 la, 1 lb, which are arranged outside the gas discharge chamber 1 for capacitive coupling.
- the energy source 10 a voltage could be applied between the two electrodes 1 la, 1 lb, leading to a gas discharge and to the generation of a plasma 13 inside the discharge chamber 1.
- An alternating current allows to sustain the plasma 13 over time, by changing of the amplitude of the alternating current the power of the plasma 13 can be modulated.
- the discharge chamber 1 comprises a gas inlet 7, a first gas outlet 8a and a second gas outlet 8b.
- a gas outlet device 4 Connected to the first gas outlet 8a is a gas outlet device 4 to blow of exhaust gas generated by the gas selection device 3, see Fig. 7.
- the outlet device 4 can be a simple two way valve, which is on one side connected to the discharge chamber 1 and on the other side connected to the atmosphere 12 or a reservoir for exhaust gas.
- the gas discharge device 2 is connected to the second gas outlet 8b.
- an inlet valve 5 is connected with the gas inlet 7 and an outlet valve 6 is connected with the second gas outlet 8b, wherein the gas selection device 3 is arranged between the second gas outlet 8b and the outlet valve 6.
- inlet valve 5 and outlet valve 6 non-return valves or two-way valves can be used, for example. Non-return valves are preferred because they do not need controlling.
- the gas selection device 3 comprises at least one selective molecular sieve and/or one selective membrane, which is nitrogen selective and oxygen non-selective.
- the molecular sieve or the membrane comprises zeolite.
- Zeolite adsorbs nitrogen, carbon, carbon monoxide, carbon dioxide, water vapor and other significant components of air, but is non-selective for oxygen.
- a first step compression and oxygen diffusion
- air in the discharge chamber 1 is compressed due to generating and sustaining a high-power plasma 13 inside the discharge chamber 1, see Fig. 1.
- the plasma leads to an increase in gas temperature, which results in an increased pressure due to the fact that the discharge chamber 1 is closed against the surrounding air.
- the air inside the chamber 1 especially oxygen and nitrogen, can only leave the chamber 1 by diffusing through the gas selection device 3 (0 2 ) or diffusing into the gas selection device 3 by adsorption (N 2 ).
- the oxygen enriched air flows through the outlet valve 6.
- the oxygen enriched air can be passed to a patient or stored in a reservoir.
- the gas exhaust device 4 is opened to the surrounding air and the outlet valve 6 closes or is closed, see Fig. 2.
- the pressure in the discharge chamber 1 goes down to atmospheric pressure.
- the plasma 13 is kept at high power for significantly reducing the particle density. Therefore, nitrogen that is adsorbed in the gas selection device 3 diffuses out of the gas selection device 3 through the discharge chamber 1 and through the gas exhaust device 4 towards the atmosphere 12.
- a third step see Fig. 3, the discharge power is reduced significantly or switched off, the gas exhaust device 4 is closed, the outlet valve 6 closes or is closed and the inlet valve 5 opens or is opened. The gas temperature with it the pressure inside the discharge chamber 1 drops. Fresh air flows into the discharge chamber 1 through the gas inlet 7.
- the cycle is finished.
- the power- modulated gas discharge device 2 starts again with the first step. If the plasma 13 has been not switched off, igniting the plasma in the following step can be omitted.
- the gas concentration arrangement can be operated without an overlapping of the first, the second and the third step. Alternatively, the gas concentration arrangement can be operated with one or more steps overlapping.
- the discharge chamber 1, the discharge device 2, the inlet valve 5 and the outlet valve 6 function as a gas pump, producing a directed flow of gas.
- Fig. 4 displays a second embodiment of a gas concentration arrangement.
- the gas concentration arrangement according to the second embodiment comprises an inlet valve 5, a gas discharge chamber 1, a gas discharge device 2, an outlet valve 6, a gas exhaust device 4, a gas selection device 3 and a third valve 14, which are connected to each other in the order as stated.
- the third valve 14 is, for example, a two-way valve or, preferably, a non-return valve.
- the discharge chamber 1 is a glass sphere, for example a hard glass, with an inner diameter of 4 cm
- the electrodes 11a, 1 lb of the discharge device 2 are inner carbon rod electrodes, for example with an electrode diameter of 4 mm and an electrode distance of ⁇ 10 mm.
- the discharge chamber 1 has two glass pipes (not shown) as gas inlet 7 and as gas outlet 8a. In contrast to the first embodiment, a second gas outlet 8a is not provided.
- non-return valves 5, 6 are mounted at the gas inlet 7 and at the outlet 8b. Due to these non-return valves 5, 6, gas can flow only from the inlet 7 to the outlet 8b. Gas flow measurements have been performed by putting suited flow meters into the inlet and outlet pipes in front or behind of the non-return valves 5, 6.
- Currents I mea n up to several amperes and powers of several hundred watts are feasible with the electronic driver.
- the energy source 10 also delivers peak voltages of up to 20 kV for start phase to obtain a gas breakdown / igniting the plasma 13.
- the arrangement according to the second embodiment can be operated in the following manner.
- a first step fresh air is pumped by modulated gas discharge inside the chamber 1 from the surroundings or an reservoir through the inlet valve 5, the discharge chamber 1 and the outlet valve 6, the gas exhaust device 4 and the gas selection device 3, leading to a flow of oxygen enriched air passing the open valve 14.
- the gas exhaust device 4 which is, for example, a three-way valve, is closed to the surrounding air 12.
- the gas exhaust device 4 opens a connection between the gas selection device 3 and the surrounding air 12 and closes the connection to the outlet valve 6. After outgassing of the gas selection device 3, which can be supported by a purge gas (not shown), the cycle can continue with the first step.
- Fig. 5 displays a third embodiment of a gas concentration arrangement.
- the third embodiment comprises a second gas selection device 3, a further third valve 14 and a fourth valve 15, wherein the second gas selection device 3 and the further third valve 14 are connected to the exhaust gas device 4 parallel to the first gas selection device 3 and valve 14. Between the gas selection devices 3 and the third valves 14, the fourth valve 15 is connected parallel to these two lines. After the third valves 14, both lines are joined. Alternatively, fourth valve 15 could be substituted by an orifice.
- the arrangement can be operated in the following manner.
- a first step fresh air is pumped by modulated gas discharge inside the chamber 1 from the surroundings or an reservoir through the inlet valve 5, the discharge chamber 1 , the outlet valve 6 and the gas exhaust device 4 to one of the two gas selection devices 3, leading to a flow of oxygen enriched air passing one of the two open valves 14.
- the other gas selection device 3 is disconnected from outlet valve 6 but connected by gas exhaust device 4 to the surroundings 12.
- the gas exhaust device 4 closes the connection of the other gas selection device 3 to the surroundings 12 and opens the connection to the outlet valve 6, so that fresh air is pumped through the other gas selection device 3, leading to a flow of oxygen enriched air passing the second open valve 14. Furthermore, the connection between the outlet valve 6 and the first gas selection device 3 is closed by gas exhaust device 4 and the connection to the surroundings 12 is opened, enabling outgassing of the first gas selection device 3.
- the cycle can continue with the first step. Due to the fourth valve 15 an amount of the oxygen enriched air can be lead as purge gas through the gas selection device 3, which is connected to the surroundings 12, supporting the outgassing of this gas selection device 3.
- the third valves 14 are preferably non-return valves, preventing a back flow of oxygen enriched air.
- gas exhaust device 4 a four-way valve can be used, for example.
- Fig. 6 displays a fourth embodiment of a gas concentration arrangement.
- the fourth embodiment comprises a gas reservoir 9 and a reservoir- valve 16.
- the valve 16 can be substituted by an orifice.
- the gas reservoir 9 is arranged between the outlet valve 6 and the gas exhaust device 4.
- an over pressure inside the reservoir 9 can be generated, preferably by increasing the flow resistance after the gas reservoir 9 by using the valve 16 or, alternatively, an orifice.
- a constant or nearly constant over pressure can be used to produce a continuous or nearly continuous gas flow.
- a constant or nearly constant oxygen enriched air flow can be generated at the output of the arrangement.
- Fig. 8 displays a fifth embodiment of a gas concentration arrangement.
- two gas concentration arrangements according to the first embodiment are connected in parallel and joined behind their outlet valves 6.
- a continuous or nearly continuous flow of oxygen enriched air can be generated at the output of the arrangement.
- Fig. 9 displays a sixth embodiment of a gas concentration arrangement.
- the gas concentration arrangement comprises two gas discharge chambers 1 and two gas discharge devices 2, which are arranged in two different lines of the arrangement.
- the two lines are joined on the input side of the two gas discharge chambers 1 and connected via an inlet valve 17, for example, a two- way valve, to fresh air or a gas reservoir.
- an inlet valve 17 for example, a two- way valve
- one of the lines is connected via an output valve 6 to the surroundings 12; the other line is connected via an output valve 6 to, for example, a gas reservoir or a patient.
- output valves 6 non-return valves or two-way valves are preferred.
- a valve 18, for example, a two-way valve is arranged on the input side of the gas discharge chamber 1.
- a gas selection device 3 is provided on the input side of the gas discharge chamber 1.
- valve 17 is open and valve 18 is closed. Pressure at the output side of the gas selection device 3 is reduced by modulated gas discharge inside the gas discharge chamber 1 being arranged in the same line as the gas selection device 3. Fresh air from the surroundings or an reservoir flows through the open valve 17 to the gas selection device 3, leading to a flow of oxygen enriched air passing the discharge chamber 1 and the open outlet valve 6.
- valve 17 is closed and valve 18 is opened.
- pressure at the input side of the gas selection device 3 is reduced by modulated gas discharge inside the chamber 1 being arranged in the other line. Especially nitrogen desorbs from the gas selection device 3 and flows through the open valve 18, through the discharge chamber 1 and the open outlet valve 6 into the surrounding air 12.
- the cycle can now continue with the first step.
- This principle according to which the gas selection device is provided on the input side of the discharge chamber 1 , can be transferred to the first to fifth embodiments shown in Figs. 4-8.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Separation Of Gases By Adsorption (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BR112012006823A BR112012006823A2 (en) | 2009-09-30 | 2010-09-23 | gas concentration arrangement, gas concentration system and gas pump for gas pumping |
CN2010800438961A CN102548652A (en) | 2009-09-30 | 2010-09-23 | Gas concentration arrangement |
AU2010302301A AU2010302301B2 (en) | 2009-09-30 | 2010-09-23 | Gas concentration arrangement |
US13/387,511 US20120177546A1 (en) | 2009-09-30 | 2010-09-23 | Gas concentration arrangement |
EP10765517A EP2482968A1 (en) | 2009-09-30 | 2010-09-23 | Gas concentration arrangement |
JP2012531528A JP2013506544A (en) | 2009-09-30 | 2010-09-23 | Gas concentrator |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP09171845.2 | 2009-09-30 | ||
EP09171845 | 2009-09-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2011039682A1 true WO2011039682A1 (en) | 2011-04-07 |
Family
ID=43468160
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IB2010/054289 WO2011039682A1 (en) | 2009-09-30 | 2010-09-23 | Gas concentration arrangement |
Country Status (7)
Country | Link |
---|---|
US (1) | US20120177546A1 (en) |
EP (1) | EP2482968A1 (en) |
JP (1) | JP2013506544A (en) |
CN (1) | CN102548652A (en) |
AU (1) | AU2010302301B2 (en) |
BR (1) | BR112012006823A2 (en) |
WO (1) | WO2011039682A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8696795B2 (en) * | 2009-12-17 | 2014-04-15 | Koninklijke Philips N.V. | Oxygen separation method and system with a plasma pump and a membrane |
US11247015B2 (en) | 2015-03-24 | 2022-02-15 | Ventec Life Systems, Inc. | Ventilator with integrated oxygen production |
US10315002B2 (en) | 2015-03-24 | 2019-06-11 | Ventec Life Systems, Inc. | Ventilator with integrated oxygen production |
US10773049B2 (en) | 2016-06-21 | 2020-09-15 | Ventec Life Systems, Inc. | Cough-assist systems with humidifier bypass |
EP3781244A4 (en) | 2018-05-13 | 2022-01-19 | Ventec Life Systems, Inc. | Portable medical ventilator system using portable oxygen concentrators |
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US3903891A (en) * | 1968-01-12 | 1975-09-09 | Hogle Kearns Int | Method and apparatus for generating plasma |
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- 2010-09-23 AU AU2010302301A patent/AU2010302301B2/en not_active Expired - Fee Related
- 2010-09-23 US US13/387,511 patent/US20120177546A1/en not_active Abandoned
- 2010-09-23 WO PCT/IB2010/054289 patent/WO2011039682A1/en active Application Filing
- 2010-09-23 BR BR112012006823A patent/BR112012006823A2/en not_active IP Right Cessation
- 2010-09-23 JP JP2012531528A patent/JP2013506544A/en active Pending
- 2010-09-23 CN CN2010800438961A patent/CN102548652A/en active Pending
- 2010-09-23 EP EP10765517A patent/EP2482968A1/en not_active Withdrawn
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Also Published As
Publication number | Publication date |
---|---|
EP2482968A1 (en) | 2012-08-08 |
CN102548652A (en) | 2012-07-04 |
US20120177546A1 (en) | 2012-07-12 |
BR112012006823A2 (en) | 2019-09-24 |
AU2010302301B2 (en) | 2015-05-07 |
JP2013506544A (en) | 2013-02-28 |
AU2010302301A1 (en) | 2012-05-24 |
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