JP5906089B2 - 液体酸素製造装置及び方法 - Google Patents
液体酸素製造装置及び方法 Download PDFInfo
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- 238000000034 method Methods 0.000 title claims description 20
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 title claims description 12
- 238000004519 manufacturing process Methods 0.000 title description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 70
- 239000001301 oxygen Substances 0.000 claims description 70
- 229910052760 oxygen Inorganic materials 0.000 claims description 70
- 239000007789 gas Substances 0.000 claims description 28
- 239000000047 product Substances 0.000 claims description 22
- 238000003860 storage Methods 0.000 claims description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 14
- 239000012530 fluid Substances 0.000 claims description 13
- 239000012263 liquid product Substances 0.000 claims description 13
- 238000004891 communication Methods 0.000 claims description 12
- 230000008859 change Effects 0.000 claims description 9
- 239000002808 molecular sieve Substances 0.000 claims description 9
- 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 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 238000001179 sorption measurement Methods 0.000 claims description 7
- 238000005259 measurement Methods 0.000 claims description 6
- 230000004044 response Effects 0.000 claims description 5
- 238000010926 purge Methods 0.000 claims description 4
- 230000008020 evaporation Effects 0.000 claims 1
- 238000001704 evaporation Methods 0.000 claims 1
- 239000003570 air Substances 0.000 description 12
- 238000004364 calculation method Methods 0.000 description 4
- 238000012790 confirmation Methods 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 239000012080 ambient air Substances 0.000 description 2
- 238000012937 correction Methods 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000000241 respiratory effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 238000013459 approach Methods 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000000875 corresponding effect Effects 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
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 238000002640 oxygen therapy Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
-
- 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
-
- 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
- B01D53/047—Pressure swing adsorption
- B01D53/053—Pressure swing adsorption with storage or buffer vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0012—Primary atmospheric gases, e.g. air
- F25J1/0017—Oxygen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0225—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using other external refrigeration means not provided before, e.g. heat driven absorption chillers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0275—Construction and layout of liquefaction equipments, e.g. valves, machines adapted for special use of the liquefaction unit, e.g. portable or transportable devices
-
- 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
- B01D2259/40007—Controlling pressure or temperature swing adsorption
-
- 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
- B01D2259/416—Further details for adsorption processes and devices involving cryogenic temperature treatment
-
- 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
- B01D2259/4533—Gas separation or purification devices adapted for specific applications for medical purposes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0046—Nitrogen
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/40—Air or oxygen enriched air, i.e. generally less than 30mol% of O2
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
- F25J2270/908—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by regenerative chillers, i.e. oscillating or dynamic systems, e.g. Stirling refrigerator, thermoelectric ("Peltier") or magnetic refrigeration
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- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Separation Of Gases By Adsorption (AREA)
Description
Claims (16)
- 液体酸素を製造するシステムを制御する方法において、
液化サイクルがアクティブであるかどうかを決定するステップと、
酸素濃縮サブシステムから液化サブシステムへの流量を測定するステップであって、前記酸素濃縮サブシステムの生成物タンク内の圧力を測定するステップを有する前記ステップと、
前記流量を流量セットポイントと比較するステップと、
前記液化サイクルがアクティブであるという決定に応答して前記比較に従って、前記圧力及び前記流量が特定の範囲内に保たれるように、前記酸素濃縮サブシステムのサイクルタイミングを調節するステップと、
を有する方法。 - 前記測定するステップが、前記生成物タンク内の圧力の変化のレートを決定するステップを有する、請求項1に記載の方法。
- 前記測定するステップが、前記生成物タンク内の圧力の変化に基づいて流量を推定するステップを有する、請求項1に記載の方法。
- 前記セットポイントが、選択された流量を有する、請求項1に記載の方法。
- 前記セットポイントが、前記酸素濃縮サブシステムの生成物タンク内の圧力の変化のレートを有する、請求項1に記載の方法。
- 前記サイクルタイミングを調節するステップは、
前記流量が前記セットポイントより高い場合に、バルブフィード時間をデクリメントするステップと、
前記流量が前記セットポイントより低い場合に、前記バルブフィード時間をインクリメントするステップと、
前記流量が前記セットポイントに等しい場合に、前記バルブフィード時間を維持するステップと、
を有する、請求項1に記載の方法。 - 前記調節するステップの後に、遅延時間により遅延するステップと、
前記遅延するステップの後に、前記測定、比較及び調節を繰り返すステップと、
を有する、請求項1に記載の方法。 - 前記調節するステップが、バルブフィード時間又はバルブパージ時間を調節するステップを有する、請求項1に記載の方法。
- 前記方法が、前記比較に基づいて、前記調節を修正するステップを有し、前記調節を修正するステップが、前記測定、比較及び調節の反復の合間の遅延、並びに前記サイクルタイミングの変化の大きさの一方又は両方を変更するステップを有する、請求項1に記載の方法。
- 液体酸素を製造する装置において、
酸素濃縮サブシステムと、
前記酸素濃縮サブシステムと流体連通し、前記酸素濃縮サブシステムから酸素濃縮ガスを受け取り、液体生成物を製造するように前記酸素濃縮ガスを凝縮する液化サブシステムと、
前記液化サブシステムと流体連通し、前記液化サブシステムから前記液体生成物を受け取る液体生成物貯蔵タンクと、
前記酸素濃縮サブシステムから前記液化サブシステムへの流量を測定するセンサであって、前記酸素濃縮サブシステムの少なくとも一部における圧力を測定し、前記測定された圧力に基づいて前記測定された流量を決定するように配置された圧力センサを有する前記センサと、
液化サイクルがアクティブであるかどうかを決定し、前記測定された流量を流量セットポイントと比較し、前記液化サイクルがアクティブであるという決定に応答して前記比較に基づいて、前記圧力及び前記流量が特定の範囲内に保たれるように、前記酸素濃縮サブシステム内の酸素濃縮サイクル時間を制御するコントローラと、
を有する装置。 - 前記酸素濃度サブシステムが、前記酸素濃縮サブシステムの酸素生成要素から酸素濃縮ガスを収集し、前記酸素濃縮ガスを前記液化サブシステムに供給する生成ガス貯蔵タンクを有し、前記圧力センサが、前記生成ガス貯蔵タンク内の圧力を測定するように配置される、請求項10に記載の装置。
- 前記液体酸素貯蔵タンクは、着脱可能であり、ユーザが前記液体酸素貯蔵タンク内に貯蔵された液体生成物の蒸発により製造される酸素濃縮ガスに対する供給レートを選択することを可能にする制御可能なバルブを有する、請求項10に記載の装置。
- 前記酸素濃縮サブシステムが、圧力スイング吸着濃縮器を有し、前記コントローラは、
前記流量が前記セットポイントより高い場合に、バルブフィード時間がデクリメントされ、
前記流量が前記セットポイントより低い場合に、前記バルブフィード時間がインクリメントされ、
前記流量が前記セットポイントに等しい場合に、前記バルブフィード時間が維持される、
ように前記酸素濃縮サブシステムのバルブフィード時間を制御する、請求項10に記載の装置。 - 前記セットポイントが、選択された流量を有する、請求項10に記載の装置。
- 前記セットポイントが、前記酸素濃縮サブシステムの生成物タンク内の圧力の変化のレートを有する、請求項10に記載の装置。
- 液体酸素を製造する装置において、
(a)圧力スイング吸着酸素濃縮サブシステムであって、
(1)圧縮空気を受け取り、酸素濃縮ガスを製造するように前記圧縮空気から窒素を吸着する分子篩、
(2)前記圧縮空気が前記分子篩により受け取られるように流れることを可能にされるフィードサイクルに対して開かれるように制御可能なフィードバルブ、
(3)前記分子篩と流体連通し、前記分子篩から前記酸素濃縮ガスを受け取る生成物タンク、及び
(4)前記生成物タンクと流体連通し、前記生成物タンク内の圧力を測定するセンサ、
を有する前記圧力スイング吸着酸素濃縮サブシステムと、
(b)前記酸素濃縮サブシステムと流体連通し、前記酸素濃縮サブシステムから前記酸素濃縮ガスを受け取り、液体生成物を製造するように前記酸素濃縮ガスを凝縮する液化サブシステムと、
(c)前記液化サブシステムと流体連通し、前記液化サブシステムから前記液体生成物を受け取る液体生成物貯蔵タンクと、
(d)前記測定された圧力に基づいて測定された流量を決定するプロセッサと、
(e)液化サイクルがアクティブであるかどうかを決定し、前記測定された流量を流量セットポイントと比較し、前記液化サイクルがアクティブであるという決定に応答して前記比較に基づいて、前記圧力及び前記流量が特定の範囲内に保たれるように、前記フィードサイクルの持続時間を制御するコントローラと、
を有する装置。
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US13974108P | 2008-12-22 | 2008-12-22 | |
US61/139,741 | 2008-12-22 | ||
PCT/IB2009/055263 WO2010073141A1 (en) | 2008-12-22 | 2009-11-21 | Liquid oxygen production device and method |
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JP2012513230A JP2012513230A (ja) | 2012-06-14 |
JP5906089B2 true JP5906089B2 (ja) | 2016-04-20 |
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US (1) | US9556029B2 (ja) |
EP (1) | EP2379202A1 (ja) |
JP (1) | JP5906089B2 (ja) |
CN (1) | CN102256684A (ja) |
BR (1) | BRPI0918102A2 (ja) |
WO (1) | WO2010073141A1 (ja) |
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CN102269979A (zh) * | 2010-12-31 | 2011-12-07 | 北京谊安医疗系统股份有限公司 | 制氧机气路切换机构的控制方法及装置 |
CN102366647B (zh) * | 2011-10-28 | 2014-02-26 | 北京神鹿腾飞医疗科技有限公司 | 一种带双气源的cpap给氧仪 |
CN203123774U (zh) * | 2012-11-19 | 2013-08-14 | 黄卫文 | 用于psa装置的节能装置 |
DE102014017600A1 (de) * | 2014-11-27 | 2016-06-02 | Linde Aktiengesellschaft | Verfahren und Vorrichtung zur Mengen- und Reinheitskontrolle bei Druckwechseladsorptionsanlagen |
JP6454611B2 (ja) * | 2015-06-19 | 2019-01-16 | 株式会社ジェイ・イー・ティ | 基板処理システム及び基板処理方法 |
WO2018006157A1 (en) * | 2016-07-08 | 2018-01-11 | Cpap Direct Ltd. | Apparatus and methods for cleaning and oxygen-enriching air |
JP7028694B2 (ja) * | 2018-04-03 | 2022-03-02 | トヨタ自動車株式会社 | 蒸発燃料処理装置 |
EP3880344B1 (en) * | 2018-11-16 | 2022-07-06 | Koninklijke Philips N.V. | Portable oxygen concentration |
CN112495137B (zh) * | 2020-11-12 | 2022-04-19 | 杭州汉德空分设备有限公司 | 一种变压吸附制氧设备 |
CN114326874B (zh) * | 2021-12-13 | 2023-12-01 | 天津怡和嘉业医疗科技有限公司 | 一种制氧设备的控制方法、控制设备及控制系统 |
CN115617104B (zh) * | 2022-12-15 | 2023-09-15 | 湖南一特医疗股份有限公司 | 医用分子筛制氧设备的远程监控系统、方法和计算机设备 |
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JP4257256B2 (ja) * | 2004-04-30 | 2009-04-22 | 日本特殊陶業株式会社 | 酸素濃縮器 |
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US7370651B2 (en) * | 2005-04-01 | 2008-05-13 | Ric Investments, Llc | Gas conserving device |
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US8753435B2 (en) * | 2006-04-03 | 2014-06-17 | Ric Investments, Llc | Portable oxygen concentrator |
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WO2008047435A1 (fr) | 2006-10-19 | 2008-04-24 | Husqvarna Zenoah Co.,Ltd. | Isolateur |
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2009
- 2009-11-21 EP EP09768422A patent/EP2379202A1/en not_active Withdrawn
- 2009-11-21 WO PCT/IB2009/055263 patent/WO2010073141A1/en active Application Filing
- 2009-11-21 JP JP2011541654A patent/JP5906089B2/ja not_active Expired - Fee Related
- 2009-11-21 CN CN2009801516715A patent/CN102256684A/zh active Pending
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US20110239698A1 (en) | 2011-10-06 |
EP2379202A1 (en) | 2011-10-26 |
US9556029B2 (en) | 2017-01-31 |
JP2012513230A (ja) | 2012-06-14 |
WO2010073141A1 (en) | 2010-07-01 |
CN102256684A (zh) | 2011-11-23 |
BRPI0918102A2 (pt) | 2015-11-24 |
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