BR112016027427B1 - Sistema e método de separação de ar - Google Patents
Sistema e método de separação de ar Download PDFInfo
- Publication number
- BR112016027427B1 BR112016027427B1 BR112016027427-0A BR112016027427A BR112016027427B1 BR 112016027427 B1 BR112016027427 B1 BR 112016027427B1 BR 112016027427 A BR112016027427 A BR 112016027427A BR 112016027427 B1 BR112016027427 B1 BR 112016027427B1
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- stream
- compressed
- air
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- 238000000926 separation method Methods 0.000 title claims abstract description 58
- 238000000034 method Methods 0.000 title claims abstract description 22
- 238000004821 distillation Methods 0.000 claims abstract description 33
- 238000001816 cooling Methods 0.000 claims abstract description 9
- 239000003570 air Substances 0.000 claims description 222
- 239000007788 liquid Substances 0.000 claims description 65
- 238000004519 manufacturing process Methods 0.000 claims description 31
- 230000006835 compression Effects 0.000 claims description 30
- 238000007906 compression Methods 0.000 claims description 30
- 238000010926 purge Methods 0.000 claims description 24
- 238000005057 refrigeration Methods 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 11
- 238000000746 purification Methods 0.000 claims description 7
- 239000012080 ambient air Substances 0.000 claims description 5
- 230000008859 change Effects 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 3
- 230000007704 transition Effects 0.000 claims description 3
- 230000001143 conditioned effect Effects 0.000 claims description 2
- 238000013022 venting Methods 0.000 claims 1
- 238000012546 transfer Methods 0.000 abstract description 4
- 239000000047 product Substances 0.000 description 95
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 91
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 59
- 239000001301 oxygen Substances 0.000 description 59
- 229910052760 oxygen Inorganic materials 0.000 description 59
- 229910052757 nitrogen Inorganic materials 0.000 description 45
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 35
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 20
- 239000007789 gas Substances 0.000 description 15
- 229910052786 argon Inorganic materials 0.000 description 10
- 239000012263 liquid product Substances 0.000 description 10
- 230000005611 electricity Effects 0.000 description 7
- 238000009835 boiling Methods 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 230000009977 dual effect Effects 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 230000001174 ascending effect Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 3
- 239000012808 vapor phase Substances 0.000 description 3
- 238000007792 addition Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000007670 refining Methods 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000819 phase cycle Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
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- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
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- F25J3/04012—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling
- F25J3/04024—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of warm gaseous streams; details of intake or interstage cooling of purified feed air, so-called boosted air
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- F25J2230/40—Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being air
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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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/40—Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval
- F25J2240/46—Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval the fluid being 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
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/40—Processes or apparatus involving steps for recycling of process streams the recycled stream being air
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
- Separation By Low-Temperature Treatments (AREA)
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US14/293,003 US9574821B2 (en) | 2014-06-02 | 2014-06-02 | Air separation system and method |
| PCT/US2014/040456 WO2015187117A1 (en) | 2014-06-02 | 2014-06-02 | Air separation system and method |
| US14/293,003 | 2014-06-02 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| BR112016027427A2 BR112016027427A2 (https=) | 2017-08-15 |
| BR112016027427B1 true BR112016027427B1 (pt) | 2022-07-05 |
Family
ID=51136787
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BR112016027427-0A BR112016027427B1 (pt) | 2014-06-02 | 2014-06-02 | Sistema e método de separação de ar |
Country Status (6)
| Country | Link |
|---|---|
| US (2) | US9574821B2 (https=) |
| EP (1) | EP3149419B1 (https=) |
| CN (1) | CN106415175B (https=) |
| BR (1) | BR112016027427B1 (https=) |
| CA (1) | CA2949450C (https=) |
| WO (1) | WO2015187117A1 (https=) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10948618B2 (en) * | 2016-10-14 | 2021-03-16 | Chevron U.S.A. Inc. | System and method for automated seismic interpretation |
| US10359231B2 (en) * | 2017-04-12 | 2019-07-23 | Praxair Technology, Inc. | Method for controlling production of high pressure gaseous oxygen in an air separation unit |
| EP3438584B1 (fr) * | 2017-08-03 | 2020-03-11 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Procédé et appareil de séparation d'air par distillation cryogénique |
| CN108240734B (zh) * | 2018-03-08 | 2024-03-26 | 李佳晨 | 增压膨胀机供气系统及空分设备 |
| JP7105085B2 (ja) * | 2018-03-30 | 2022-07-22 | 大陽日酸株式会社 | 空気液化分離装置及び空気液化分離装置の運転停止方法 |
| US11029087B2 (en) * | 2018-11-16 | 2021-06-08 | L'air Liquide Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for utilizing waste air to improve the capacity of an existing air separation unit |
| EP3899388B1 (en) * | 2018-12-19 | 2026-03-04 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for starting up a cryogenic air separation unit and associated air separation unit |
| JP7460973B2 (ja) * | 2020-03-05 | 2024-04-03 | 日本エア・リキード合同会社 | 空気分離装置 |
| CN116547488A (zh) * | 2020-11-24 | 2023-08-04 | 林德有限责任公司 | 用于空气低温分离的方法和设备 |
| US12117240B2 (en) * | 2021-07-19 | 2024-10-15 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Integrated multicomponent refrigerant and air separation process for producing liquid oxygen |
| CN113663992A (zh) * | 2021-07-30 | 2021-11-19 | 上海宝冶集团有限公司 | 多级压缩空气管路快速吹扫法 |
| CN113758150A (zh) * | 2021-09-18 | 2021-12-07 | 乔治洛德方法研究和开发液化空气有限公司 | 空气的低温分离方法和空气分离装置 |
Family Cites Families (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3477239A (en) | 1967-05-16 | 1969-11-11 | Messer Griesheim Gmbh | Multistage compression drive in gas separation |
| US4861351A (en) | 1987-09-16 | 1989-08-29 | Air Products And Chemicals, Inc. | Production of hydrogen and carbon monoxide |
| JP2736543B2 (ja) | 1989-04-17 | 1998-04-02 | 日本酸素株式会社 | 空気液化分離方法 |
| US5228296A (en) * | 1992-02-27 | 1993-07-20 | Praxair Technology, Inc. | Cryogenic rectification system with argon heat pump |
| US5924307A (en) | 1997-05-19 | 1999-07-20 | Praxair Technology, Inc. | Turbine/motor (generator) driven booster compressor |
| US5901579A (en) | 1998-04-03 | 1999-05-11 | Praxair Technology, Inc. | Cryogenic air separation system with integrated machine compression |
| FR2784308B1 (fr) * | 1998-10-09 | 2001-11-09 | Air Liquide | Procede et installation de separation de gaz avec production d'un debit gazeux variable |
| US6357258B1 (en) | 2000-09-08 | 2002-03-19 | Praxair Technology, Inc. | Cryogenic air separation system with integrated booster and multicomponent refrigeration compression |
| US6622520B1 (en) * | 2002-12-11 | 2003-09-23 | Praxair Technology, Inc. | Cryogenic rectification system for producing low purity oxygen using shelf vapor turboexpansion |
| DE10339230A1 (de) * | 2003-08-26 | 2005-03-24 | Linde Ag | Verfahren und Vorrichtung zur Tieftemperaturzerlegung von Luft |
| DE102004016931A1 (de) * | 2004-04-06 | 2005-10-27 | Linde Ag | Verfahren und Vorrichtung zur variablen Erzeugung eines Druckproduktes durch Tieftemperaturzerlegung von Luft |
| US7533540B2 (en) * | 2006-03-10 | 2009-05-19 | Praxair Technology, Inc. | Cryogenic air separation system for enhanced liquid production |
| US8020408B2 (en) * | 2006-12-06 | 2011-09-20 | Praxair Technology, Inc. | Separation method and apparatus |
| AU2008287322B2 (en) * | 2007-08-14 | 2012-04-19 | Fluor Technologies Corporation | Configurations and methods for improved natural gas liquids recovery |
| US8191386B2 (en) * | 2008-02-14 | 2012-06-05 | Praxair Technology, Inc. | Distillation method and apparatus |
| US20090241595A1 (en) * | 2008-03-27 | 2009-10-01 | Praxair Technology, Inc. | Distillation method and apparatus |
| JP5643491B2 (ja) | 2009-07-24 | 2014-12-17 | 大陽日酸株式会社 | 空気液化分離方法及び装置 |
| US9279613B2 (en) | 2010-03-19 | 2016-03-08 | Praxair Technology, Inc. | Air separation method and apparatus |
| NO333438B1 (no) | 2010-07-14 | 2013-06-03 | Statoil Asa | Fremgangsmate og apparat for sammensetningsbasert kompressorkontroll og ytelsesovervaking. |
| US9010114B2 (en) * | 2013-02-19 | 2015-04-21 | The Boeing Company | Air charge system and method for an internal combustion engine |
-
2014
- 2014-06-02 BR BR112016027427-0A patent/BR112016027427B1/pt active IP Right Grant
- 2014-06-02 US US14/293,003 patent/US9574821B2/en active Active
- 2014-06-02 CA CA2949450A patent/CA2949450C/en active Active
- 2014-06-02 WO PCT/US2014/040456 patent/WO2015187117A1/en not_active Ceased
- 2014-06-02 EP EP14736516.7A patent/EP3149419B1/en active Active
- 2014-06-02 CN CN201480079131.1A patent/CN106415175B/zh active Active
-
2017
- 2017-01-05 US US15/399,297 patent/US10254040B2/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CA2949450A1 (en) | 2015-12-10 |
| CN106415175B (zh) | 2019-06-04 |
| EP3149419A1 (en) | 2017-04-05 |
| US10254040B2 (en) | 2019-04-09 |
| BR112016027427A2 (https=) | 2017-08-15 |
| US20170115053A1 (en) | 2017-04-27 |
| US9574821B2 (en) | 2017-02-21 |
| CN106415175A (zh) | 2017-02-15 |
| EP3149419B1 (en) | 2019-10-30 |
| CA2949450C (en) | 2018-11-06 |
| US20150345857A1 (en) | 2015-12-03 |
| WO2015187117A1 (en) | 2015-12-10 |
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Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 02/06/2014, OBSERVADAS AS CONDICOES LEGAIS |