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 than

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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
Application number
AU2003238457A
Inventor
Heinz Bauer
Hubert Franke
Rainer Sapper
Thilo Schiewe
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Linde GmbH
Original Assignee
Linde GmbH
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Filing date
Publication date
Application filed by Linde GmbH filed Critical Linde GmbH
Publication of AU2003238457A1 publication Critical patent/AU2003238457A1/en
Abandoned legal-status Critical Current

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes 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
    • F25J3/0228Processes 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
    • F25J3/0257Processes 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/005Processes comprising at least two steps in series
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/09Purification; Separation; Use of additives by fractional condensation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022Hydrocarbons, e.g. natural gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003Processes 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
    • F25J1/0032Processes 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"
    • F25J1/0035Processes 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25J1/003Processes 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
    • F25J1/0032Processes 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"
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    • F25J1/0217Processes 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 a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as at least a three level refrigeration cascade with at least one MCR cycle
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    • F25J1/0243Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244Operation; Control and regulation; Instrumentation
    • F25J1/0245Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0248Stopping of the process, e.g. defrosting or deriming, maintenance; Back-up mode or systems
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    • F25J1/0257Construction and layout of liquefaction equipments, e.g. valves, machines
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    • F25J1/0257Construction and layout of liquefaction equipments, e.g. valves, machines
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    • F25J1/0264Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
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    • F25J1/0279Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0281Compression 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
    • F25J1/0283Gas turbine as the prime mechanical driver
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    • F25J1/0291Refrigerant compression by combined gas compression and liquid pumping
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    • F25J1/0292Refrigerant compression by cold or cryogenic suction of the refrigerant gas
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    • F25J3/0204Processes 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
    • F25J3/0209Natural gas or substitute natural gas
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    • F25J3/0228Processes 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
    • F25J3/0233Processes 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 CnHm with 1 carbon atom or more
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F25J3/0228Processes 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
    • F25J3/0242Processes 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 CnHm with 3 carbon atoms or more
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    • F25J2240/02Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/32Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/40Vertical layout or arrangement of cold equipments within in the cold box, e.g. columns, condensers, heat exchangers etc.
AU2003238457A 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 Abandoned AU2003238457A1 (en)

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>

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DE (1) DE10226596A1 (en)
MY (1) MY149624A (en)
NO (1) NO20050197L (en)
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WO (1) WO2003106906A1 (en)

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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)

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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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