WO2010060735A3 - Procede de rejet d'azote d'un flux d'hydrocarbure pour produire un flux de gaz combustible et appareil associe method of rejecting nitrogen from a hydrocarbon stream to provide a fuel gas stream and an apparatus therefor - Google Patents

Procede de rejet d'azote d'un flux d'hydrocarbure pour produire un flux de gaz combustible et appareil associe method of rejecting nitrogen from a hydrocarbon stream to provide a fuel gas stream and an apparatus therefor Download PDF

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Publication number
WO2010060735A3
WO2010060735A3 PCT/EP2009/064423 EP2009064423W WO2010060735A3 WO 2010060735 A3 WO2010060735 A3 WO 2010060735A3 EP 2009064423 W EP2009064423 W EP 2009064423W WO 2010060735 A3 WO2010060735 A3 WO 2010060735A3
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WO
WIPO (PCT)
Prior art keywords
nitrogen
stream
hydrocarbon stream
fuel gas
lean
Prior art date
Application number
PCT/EP2009/064423
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English (en)
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WO2010060735A2 (fr
Inventor
Sander Kaart
Marco Dick Jager
Original Assignee
Shell Internationale Research Maatschappij B.V.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shell Internationale Research Maatschappij B.V. filed Critical Shell Internationale Research Maatschappij B.V.
Priority to EP09744404A priority Critical patent/EP2342517A2/fr
Priority to JP2011533751A priority patent/JP2012514050A/ja
Priority to US13/126,476 priority patent/US20110239701A1/en
Priority to CA2741970A priority patent/CA2741970A1/fr
Priority to AU2009319191A priority patent/AU2009319191B2/en
Priority to CN2009801428220A priority patent/CN102713479A/zh
Publication of WO2010060735A2 publication Critical patent/WO2010060735A2/fr
Publication of WO2010060735A3 publication Critical patent/WO2010060735A3/fr

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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
    • F25J3/0233Processes 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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    • 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
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    • 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
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    • 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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    • F25J1/0037Processes 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 of a return stream
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    • F25J1/0052Processes 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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    • F25J1/0055Processes 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 originating from an incorporated cascade
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    • F25J1/0072Nitrogen
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    • F25J1/0211Processes 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
    • 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
    • F25J1/0218Processes 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 with one or more SCR cycles, e.g. with a C3 pre-cooling cycle
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    • F25J1/0264Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
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    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/74Refluxing the column with at least a part of the partially condensed overhead gas
    • 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
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/02Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
    • 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
    • F25J2210/00Processes characterised by the type or other details of the feed stream
    • F25J2210/06Splitting of the feed stream, e.g. for treating or cooling in different ways
    • 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
    • F25J2215/00Processes characterised by the type or other details of the product stream
    • F25J2215/04Recovery of liquid products
    • 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
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/30Dynamic liquid or hydraulic expansion with extraction of work, e.g. single phase or two-phase turbine
    • 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
    • F25J2240/00Processes or apparatus involving steps for expanding of process streams
    • F25J2240/40Expansion without extracting work, i.e. isenthalpic throttling, e.g. JT valve, regulating valve or venturi, or isentropic nozzle, e.g. Laval
    • 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
    • F25J2270/00Refrigeration techniques used
    • F25J2270/14External refrigeration with work-producing gas expansion loop
    • 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
    • F25J2270/00Refrigeration techniques used
    • F25J2270/42Quasi-closed internal or closed external nitrogen refrigeration cycle

Abstract

L'invention concerne un procédé et un appareil (1) permettant de rejeter l'azote d'un flux d'hydrocarbure (10) pour produire un flux de gaz combustible (510). Un flux d'hydrocarbure (10) est au moins partiellement liquéfié et, par la suite, détendu. Le flux d'hydrocarbure détendu (110) est fractionné dans une colonne de fractionnement (150) pour produire un flux d'hydrocarbure riche en azote (160) et un flux d'hydrocarbure pauvre en azote (170). Le flux d'hydrocarbure riche en azote (160) est partiellement condensé dans un condenseur (200) par refroidissement contre un réfrigérant que l'on fait circuler dans un premier circuit réfrigérant spécialisé (800), et qui est séparé en phase pour produire un flux de rejet d'azote (260) et un flux de reflux pauvre en azote (270) que l'on retourne vers la colonne de fractionnement (150). Le flux d'hydrocarbure pauvre en azote (170) est partiellement vaporisé et séparé en phase pour produire un flux de vapeur que l'on retourne à la colonne de fractionnement (150) et un flux d'hydrocarbure pauvre en azote (370) que l'on soumet à un sous-refroidissement. Le flux de gaz combustible (510) est généré à partir du flux d'hydrocarbure pauvre en azote (410).
PCT/EP2009/064423 2008-11-03 2009-11-02 Procede de rejet d'azote d'un flux d'hydrocarbure pour produire un flux de gaz combustible et appareil associe method of rejecting nitrogen from a hydrocarbon stream to provide a fuel gas stream and an apparatus therefor WO2010060735A2 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP09744404A EP2342517A2 (fr) 2008-11-03 2009-11-02 Procede de rejet d'azote d'un flux d'hydrocarbure pour produire un flux de gaz combustible et appareil associemethod of rejecting nitrogen from a hydrocarbon stream to provide a fuel gas stream and an apparatus therefor
JP2011533751A JP2012514050A (ja) 2008-11-03 2009-11-02 炭化水素流から窒素を排除して燃料ガス流を提供する方法およびそのための装置
US13/126,476 US20110239701A1 (en) 2008-11-03 2009-11-02 Method of rejecting nitrogen from a hydrocarbon stream to provide a fuel gas stream and an apparatus therefor
CA2741970A CA2741970A1 (fr) 2008-11-03 2009-11-02 Procede de rejet d'azote d'un flux d'hydrocarbure pour produire un flux de gaz combustible et appareil associe method of rejecting nitrogen from a hydrocarbon stream to provide afuel gas stream and an apparatus therefor
AU2009319191A AU2009319191B2 (en) 2008-11-03 2009-11-02 Method of rejecting nitrogen from a hydrocarbon stream to provide a fuel gas stream and an apparatus therefor
CN2009801428220A CN102713479A (zh) 2008-11-03 2009-11-02 从烃流除去氮以提供燃料气体流的方法和用于该方法的设备

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP08168159.5 2008-11-03
EP08168159 2008-11-03

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WO2010060735A2 WO2010060735A2 (fr) 2010-06-03
WO2010060735A3 true WO2010060735A3 (fr) 2012-08-30

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Country Link
US (1) US20110239701A1 (fr)
EP (1) EP2342517A2 (fr)
JP (1) JP2012514050A (fr)
CN (1) CN102713479A (fr)
AU (1) AU2009319191B2 (fr)
CA (1) CA2741970A1 (fr)
WO (1) WO2010060735A2 (fr)

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US20110239701A1 (en) 2011-10-06
EP2342517A2 (fr) 2011-07-13
JP2012514050A (ja) 2012-06-21
CA2741970A1 (fr) 2010-06-03
CN102713479A (zh) 2012-10-03
AU2009319191A1 (en) 2010-06-03
WO2010060735A2 (fr) 2010-06-03
AU2009319191B2 (en) 2013-05-02

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