AU2003238457A1 - Method for liquefying a stream enriched with hydrocarbons and the simultaneous recovery of a high-yield fraction enriched with cless thansbgreater than3+less than/sbgreater than - Google Patents
Method for liquefying a stream enriched with hydrocarbons and the simultaneous recovery of a high-yield fraction enriched with cless thansbgreater than3+less than/sbgreater thanInfo
- Publication number
- AU2003238457A1 AU2003238457A1 AU2003238457A AU2003238457A AU2003238457A1 AU 2003238457 A1 AU2003238457 A1 AU 2003238457A1 AU 2003238457 A AU2003238457 A AU 2003238457A AU 2003238457 A AU2003238457 A AU 2003238457A AU 2003238457 A1 AU2003238457 A1 AU 2003238457A1
- Authority
- AU
- Australia
- Prior art keywords
- enriched
- thansbgreater
- sbgreater
- than3
- cless
- 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.)
- Abandoned
Links
- 229930195733 hydrocarbon Natural products 0.000 title 1
- 150000002430 hydrocarbons Chemical class 0.000 title 1
- 238000000034 method Methods 0.000 title 1
- 238000011084 recovery Methods 0.000 title 1
Classifications
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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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0257—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 characterised by the separated product stream separation of nitrogen
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/005—Processes comprising at least two steps in series
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C7/00—Purification; Separation; Use of additives
- C07C7/09—Purification; Separation; Use of additives by fractional condensation
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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
- 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
- F25J1/0022—Hydrocarbons, e.g. natural gas
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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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
- F25J1/0032—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
- F25J1/0035—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by gas expansion with extraction of work
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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- F25J1/0032—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
- F25J1/004—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by flash gas recovery
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- F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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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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- 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
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- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
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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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- F25J1/0264—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
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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
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- F25J1/0281—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc. characterised by the type of prime driver, e.g. hot gas expander
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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
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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
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- F25J3/0204—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 characterised by the feed stream
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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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/32—Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
-
- 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/40—Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10226596.8 | 2002-06-14 | ||
DE2002126596 DE10226596A1 (en) | 2002-06-14 | 2002-06-14 | Process for liquefying a hydrocarbon-rich stream with simultaneous recovery of a C3 + -rich fraction with high yield |
PCT/EP2003/005808 WO2003106906A1 (en) | 2002-06-14 | 2003-06-03 | Method for liquefying a stream enriched with hydrocarbons and the simultaneous recovery of a high-yield fraction enriched with c<sb>3+</sb> |
Publications (1)
Publication Number | Publication Date |
---|---|
AU2003238457A1 true AU2003238457A1 (en) | 2003-12-31 |
Family
ID=29723166
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU2003238457A Abandoned AU2003238457A1 (en) | 2002-06-14 | 2003-06-03 | Method for liquefying a stream enriched with hydrocarbons and the simultaneous recovery of a high-yield fraction enriched with cless thansbgreater than3+less than/sbgreater than |
Country Status (6)
Country | Link |
---|---|
AU (1) | AU2003238457A1 (en) |
DE (1) | DE10226596A1 (en) |
MY (1) | MY149624A (en) |
NO (1) | NO20050197L (en) |
RU (1) | RU2317497C2 (en) |
WO (1) | WO2003106906A1 (en) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004023814A1 (en) * | 2004-05-13 | 2005-12-01 | Linde Ag | Process and apparatus for liquefying a hydrocarbon-rich stream |
DE102004054674A1 (en) * | 2004-11-12 | 2006-05-24 | Linde Ag | Process for liquefying a hydrocarbon-rich stream |
WO2006108821A1 (en) * | 2005-04-12 | 2006-10-19 | Shell Internationale Research Maatschappij | Method and apparatus for liquefying a natural gas stream |
US8578734B2 (en) | 2006-05-15 | 2013-11-12 | Shell Oil Company | Method and apparatus for liquefying a hydrocarbon stream |
US20090301131A1 (en) * | 2006-05-19 | 2009-12-10 | Shell Oil Company | Method and apparatus for treating a hydrocarbon stream |
US10539363B2 (en) | 2008-02-14 | 2020-01-21 | Shell Oil Company | Method and apparatus for cooling a hydrocarbon stream |
CN101644527B (en) * | 2009-08-26 | 2011-12-28 | 四川空分设备(集团)有限责任公司 | Refrigeration system and liquefaction system for liquefaction process of natural gas |
AU2011273541B2 (en) | 2010-06-30 | 2014-07-31 | Shell Internationale Research Maatschappij B.V. | Method of treating a hydrocarbon stream comprising methane, and an apparatus therefor |
AP3845A (en) * | 2010-06-30 | 2016-09-30 | Shell Int Research | Method of treating a hydrocarbon stream comprising methane, and an apparatus therefor |
US11668522B2 (en) * | 2016-07-21 | 2023-06-06 | Air Products And Chemicals, Inc. | Heavy hydrocarbon removal system for lean natural gas liquefaction |
RU2694337C1 (en) * | 2018-07-02 | 2019-07-11 | Андрей Владиславович Курочкин | Hydrocarbon extraction unit c2+ from natural gas (embodiments) |
RU2696375C1 (en) * | 2018-08-06 | 2019-08-01 | Андрей Владиславович Курочкин | Plant for producing hydrocarbons c2+ from natural gas (versions) |
RU2694746C1 (en) * | 2018-08-06 | 2019-07-16 | Андрей Владиславович Курочкин | Plant for production of hydrocarbons c2+ from natural gas (versions) |
RU2694735C1 (en) * | 2018-08-30 | 2019-07-16 | Андрей Владиславович Курочкин | Plant of low-temperature separation with fractionating absorption ltsfa for processing of natural gas with extraction of hydrocarbons c2+ (versions) |
RU2681897C1 (en) * | 2018-08-30 | 2019-03-13 | Андрей Владиславович Курочкин | Installation of low-temperature separation with ntsd dephlegmation for processing natural gas with extracting hydrocarbons c2+ (options) |
RU2682595C1 (en) * | 2018-08-30 | 2019-03-19 | Андрей Владиславович Курочкин | Low temperature reflux plant for converting natural gas with production of hydrocarbons c2+ (versions) |
RU2694731C1 (en) * | 2018-08-30 | 2019-07-16 | Андрей Владиславович Курочкин | Low-temperature fractionating absorption plant for processing natural gas with extraction of hydrocarbons c2+ (versions) |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4507133A (en) * | 1983-09-29 | 1985-03-26 | Exxon Production Research Co. | Process for LPG recovery |
RU2144556C1 (en) * | 1995-06-07 | 2000-01-20 | Элкор Корпорейшн | Method of gas flow separation and device for its embodiment |
DE19716415C1 (en) * | 1997-04-18 | 1998-10-22 | Linde Ag | Process for liquefying a hydrocarbon-rich stream |
GB9826999D0 (en) * | 1998-12-08 | 1999-02-03 | Costain Oil Gas & Process Limi | Low temperature separation of hydrocarbon gas |
WO2001088447A1 (en) * | 2000-05-18 | 2001-11-22 | Phillips Petroleum Company | Enhanced ngl recovery utilizing refrigeration and reflux from lng plants |
UA76750C2 (en) * | 2001-06-08 | 2006-09-15 | Елккорп | Method for liquefying natural gas (versions) |
-
2002
- 2002-06-14 DE DE2002126596 patent/DE10226596A1/en not_active Withdrawn
-
2003
- 2003-04-15 MY MYPI20031406 patent/MY149624A/en unknown
- 2003-06-03 AU AU2003238457A patent/AU2003238457A1/en not_active Abandoned
- 2003-06-03 WO PCT/EP2003/005808 patent/WO2003106906A1/en not_active Application Discontinuation
- 2003-06-03 RU RU2005100838/06A patent/RU2317497C2/en active
-
2005
- 2005-01-13 NO NO20050197A patent/NO20050197L/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
RU2005100838A (en) | 2006-06-10 |
WO2003106906A1 (en) | 2003-12-24 |
RU2317497C2 (en) | 2008-02-20 |
DE10226596A1 (en) | 2004-01-15 |
MY149624A (en) | 2013-09-13 |
NO20050197D0 (en) | 2005-01-13 |
NO20050197L (en) | 2005-02-04 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK6 | Application lapsed section 142(2)(f)/reg. 8.3(3) - pct applic. not entering national phase |