WO2014053297A3 - Process for the separation of air by cryogenic distillation - Google Patents
Process for the separation of air by cryogenic distillation Download PDFInfo
- Publication number
- WO2014053297A3 WO2014053297A3 PCT/EP2013/068965 EP2013068965W WO2014053297A3 WO 2014053297 A3 WO2014053297 A3 WO 2014053297A3 EP 2013068965 W EP2013068965 W EP 2013068965W WO 2014053297 A3 WO2014053297 A3 WO 2014053297A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- column system
- separation
- air
- cryogenic distillation
- nitrogen enriched
- Prior art date
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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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- 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
- F25J3/04—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 for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04048—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of cold gaseous streams, e.g. intermediate or oxygen enriched (waste) streams
- F25J3/0406—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of cold gaseous streams, e.g. intermediate or oxygen enriched (waste) streams of nitrogen
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- 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
- F25J3/04—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 for air
- F25J3/04151—Purification and (pre-)cooling of the feed air; recuperative heat-exchange with product streams
- F25J3/04163—Hot end purification of the feed air
- F25J3/04169—Hot end purification of the feed air by adsorption of the impurities
- F25J3/04175—Hot end purification of the feed air by adsorption of the impurities at a pressure of substantially more than the highest pressure column
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- 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
- F25J3/04—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 for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04048—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of cold gaseous streams, e.g. intermediate or oxygen enriched (waste) streams
- F25J3/04054—Providing pressurised feed air or process streams within or from the air fractionation unit by compression of cold gaseous streams, e.g. intermediate or oxygen enriched (waste) streams of air
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- 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
- F25J1/0015—Nitrogen
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- 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
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- F25J1/0202—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 only internal refrigeration means, i.e. without external refrigeration in a quasi-closed internal refrigeration loop
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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
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- F25J1/0228—Coupling of the liquefaction unit to other units or processes, so-called integrated processes
- F25J1/0234—Integration with a cryogenic air separation unit
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
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- F25J3/04—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 for air
- F25J3/04006—Providing pressurised feed air or process streams within or from the air fractionation unit
- F25J3/04078—Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression
- F25J3/04084—Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression of nitrogen
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- 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
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
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- F25J3/04—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 for air
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- F25J3/0409—Providing pressurised feed air or process streams within or from the air fractionation unit providing pressurized products by liquid compression and vaporisation with cold recovery, i.e. so-called internal compression of oxygen
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- F25J3/04187—Cooling of the purified feed air by recuperative heat-exchange; Heat-exchange with product streams
- F25J3/04218—Parallel arrangement of the main heat exchange line in cores having different functions, e.g. in low pressure and high pressure cores
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- F25J3/04315—Lowest pressure or impure nitrogen, so-called waste nitrogen expansion
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- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/12—Particular process parameters like pressure, temperature, ratios
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- 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)
Abstract
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP13763036.4A EP2904339A2 (en) | 2012-10-01 | 2013-09-13 | Process for the separation of air by cryogenic distillation |
CN201380051043.6A CN105431698A (en) | 2012-10-01 | 2013-09-13 | Process for the separation of air by cryogenic distillation |
US14/431,918 US20150253075A1 (en) | 2012-10-01 | 2013-09-13 | Process for the separation of air by cryogenic distillation |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP12306195.4A EP2713128A1 (en) | 2012-10-01 | 2012-10-01 | Process for the separation of air by cryogenic distillation |
EP12306195.4 | 2012-10-01 |
Publications (2)
Publication Number | Publication Date |
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WO2014053297A2 WO2014053297A2 (en) | 2014-04-10 |
WO2014053297A3 true WO2014053297A3 (en) | 2015-11-19 |
Family
ID=47022601
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2013/068965 WO2014053297A2 (en) | 2012-10-01 | 2013-09-13 | Process for the separation of air by cryogenic distillation |
Country Status (4)
Country | Link |
---|---|
US (1) | US20150253075A1 (en) |
EP (2) | EP2713128A1 (en) |
CN (1) | CN105431698A (en) |
WO (1) | WO2014053297A2 (en) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR3044747B1 (en) * | 2015-12-07 | 2019-12-20 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | PROCESS FOR LIQUEFACTION OF NATURAL GAS AND NITROGEN |
EP3438585A3 (en) * | 2017-08-03 | 2019-04-17 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Method for defrosting a device for air separation by cryogenic distillation and device adapted to be defrosted using this method |
EP3732415A4 (en) | 2017-12-28 | 2021-08-11 | L'air Liquide, Société Anonyme Pour L'Étude Et L'exploitation Des Procédés Georges Claude | Utilization of nitrogen-enriched streams produced in air separation units comprising split-core main heat exchangers |
CN109059422A (en) * | 2018-07-12 | 2018-12-21 | 北京拓首能源科技股份有限公司 | A kind of device using dirty nitrogen cold energy precooled air |
CN109341193A (en) * | 2018-11-16 | 2019-02-15 | 杭州凯德空分设备有限公司 | A kind of peak-trough electricity production liquid oxygen liquid nitrogen plan and method |
US20220034584A1 (en) * | 2020-07-30 | 2022-02-03 | L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Large liquid oxygen and liquefied natural gas production process |
CN112304027B (en) * | 2020-12-04 | 2025-01-03 | 开封空分集团有限公司 | Air separation device and preparation method for all-liquid production of nitrogen circulation process |
US20220252341A1 (en) * | 2021-02-05 | 2022-08-11 | Air Products And Chemicals, Inc. | Method and system for decarbonized lng production |
US12209802B2 (en) | 2022-07-28 | 2025-01-28 | Praxair Technology, Inc. | System and method for cryogenic air separation using four distillation columns including an intermediate pressure column |
US12055345B2 (en) | 2022-07-28 | 2024-08-06 | Praxair Technology, Inc. | Air separation unit and method for production of nitrogen and argon using a distillation column system with an intermediate pressure kettle column |
US11959701B2 (en) | 2022-07-28 | 2024-04-16 | Praxair Technology, Inc. | Air separation unit and method for production of high purity nitrogen product using a distillation column system with an intermediate pressure kettle column |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5261171A (en) * | 1975-11-17 | 1977-05-20 | Hitachi Ltd | Air separation method to collect liquid product |
DE19803437A1 (en) * | 1998-01-29 | 1999-03-18 | Linde Ag | Oxygen and nitrogen extracted by low-temperature fractional distillation |
FR2819046A1 (en) * | 2001-01-03 | 2002-07-05 | Air Liquide | Cryogenic distillation air separation plant uses compressor to compress nitrogen-rich flow with inlet temperature below that of heat exchanger |
US20050132746A1 (en) * | 2003-12-23 | 2005-06-23 | Jean-Renaud Brugerolle | Cryogenic air separation process and apparatus |
US20060010912A1 (en) * | 2004-07-14 | 2006-01-19 | Jean-Renaud Brugerolle | Low temperature air separation process for producing pressurized gaseous product |
US20080115531A1 (en) * | 2006-11-16 | 2008-05-22 | Bao Ha | Cryogenic Air Separation Process and Apparatus |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2807150B1 (en) * | 2000-04-04 | 2002-10-18 | Air Liquide | PROCESS AND APPARATUS FOR PRODUCING OXYGEN ENRICHED FLUID BY CRYOGENIC DISTILLATION |
FR2915271A1 (en) * | 2007-04-23 | 2008-10-24 | Air Liquide | Air separating method, involves operating extracted nitrogen gas from high pressure column at pressure higher than pressure of systems operating at low pressure, and compressing gas till pressure is higher than high pressure of systems |
-
2012
- 2012-10-01 EP EP12306195.4A patent/EP2713128A1/en not_active Withdrawn
-
2013
- 2013-09-13 CN CN201380051043.6A patent/CN105431698A/en active Pending
- 2013-09-13 EP EP13763036.4A patent/EP2904339A2/en not_active Withdrawn
- 2013-09-13 US US14/431,918 patent/US20150253075A1/en not_active Abandoned
- 2013-09-13 WO PCT/EP2013/068965 patent/WO2014053297A2/en active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5261171A (en) * | 1975-11-17 | 1977-05-20 | Hitachi Ltd | Air separation method to collect liquid product |
DE19803437A1 (en) * | 1998-01-29 | 1999-03-18 | Linde Ag | Oxygen and nitrogen extracted by low-temperature fractional distillation |
FR2819046A1 (en) * | 2001-01-03 | 2002-07-05 | Air Liquide | Cryogenic distillation air separation plant uses compressor to compress nitrogen-rich flow with inlet temperature below that of heat exchanger |
US20050132746A1 (en) * | 2003-12-23 | 2005-06-23 | Jean-Renaud Brugerolle | Cryogenic air separation process and apparatus |
US20060010912A1 (en) * | 2004-07-14 | 2006-01-19 | Jean-Renaud Brugerolle | Low temperature air separation process for producing pressurized gaseous product |
US20080115531A1 (en) * | 2006-11-16 | 2008-05-22 | Bao Ha | Cryogenic Air Separation Process and Apparatus |
Also Published As
Publication number | Publication date |
---|---|
EP2713128A1 (en) | 2014-04-02 |
CN105431698A (en) | 2016-03-23 |
WO2014053297A2 (en) | 2014-04-10 |
EP2904339A2 (en) | 2015-08-12 |
US20150253075A1 (en) | 2015-09-10 |
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