WO2011004123A3 - Procédé de production d'un courant riche en méthane et d'un courant riche en hydrocarbures en c2+, et installation associée - Google Patents

Procédé de production d'un courant riche en méthane et d'un courant riche en hydrocarbures en c2+, et installation associée Download PDF

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Publication number
WO2011004123A3
WO2011004123A3 PCT/FR2010/051437 FR2010051437W WO2011004123A3 WO 2011004123 A3 WO2011004123 A3 WO 2011004123A3 FR 2010051437 W FR2010051437 W FR 2010051437W WO 2011004123 A3 WO2011004123 A3 WO 2011004123A3
Authority
WO
WIPO (PCT)
Prior art keywords
stream
rich stream
hydrocarbon
cooled
heat exchanger
Prior art date
Application number
PCT/FR2010/051437
Other languages
English (en)
Other versions
WO2011004123A2 (fr
Inventor
Vanessa Gahier
Julie Gouriou
Loïc BARTHE
Sandra Thiebault
Original Assignee
Technip France
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 Technip France filed Critical Technip France
Priority to MX2012000474A priority Critical patent/MX353746B/es
Priority to BR112012000404-2A priority patent/BR112012000404B1/pt
Priority to EP10742221.4A priority patent/EP2452140B1/fr
Priority to CA2767502A priority patent/CA2767502C/fr
Publication of WO2011004123A2 publication Critical patent/WO2011004123A2/fr
Publication of WO2011004123A3 publication Critical patent/WO2011004123A3/fr

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Classifications

    • 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
    • F25J3/0204Processes 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
    • 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
    • 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
    • F25J3/0238Processes 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 2 carbon atoms or more
    • 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
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/02Processes or apparatus using separation by rectification in a single pressure main column system
    • 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
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/30Processes or apparatus using separation by rectification using a side column in a single pressure column system
    • 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
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/50Processes or apparatus using separation by rectification using multiple (re-)boiler-condensers at different heights of the column
    • 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
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/76Refluxing the column with condensed overhead gas being cycled in a quasi-closed loop refrigeration cycle
    • 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
    • F25J2205/04Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
    • 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
    • F25J2230/00Processes or apparatus involving steps for increasing the pressure of gaseous process streams
    • F25J2230/24Multiple compressors or compressor stages in parallel
    • 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
    • F25J2230/00Processes or apparatus involving steps for increasing the pressure of gaseous process streams
    • F25J2230/60Processes or apparatus involving steps for increasing the pressure of gaseous process streams the fluid being hydrocarbons or a mixture of hydrocarbons
    • 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
    • F25J2240/02Expansion 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
    • F25J2245/00Processes or apparatus involving steps for recycling of process streams
    • F25J2245/02Recycle of a stream in general, e.g. a by-pass 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
    • F25J2270/00Refrigeration techniques used
    • F25J2270/02Internal refrigeration with liquid vaporising 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
    • F25J2270/04Internal 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
    • F25J2270/04Internal refrigeration with work-producing gas expansion loop
    • F25J2270/06Internal refrigeration with work-producing gas expansion loop with multiple gas expansion loops
    • 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
    • F25J2270/88Quasi-closed internal refrigeration or heat pump cycle, if not otherwise provided
    • 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
    • F25J2290/80Retrofitting, revamping or debottlenecking of existing plant

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Ce procédé comprend le refroidissement du courant d'alimentation dans un premier échangeur thermique (20), la séparation dans un premier ballon séparateur (22) pour produire un courant léger (44) de tête et un courant lourd (45) de pied et la division du courant léger (44) de tête en une fraction (48) d'alimentation d'une turbine de détente dynamique et en une fraction (46) d'alimentation d'une première colonne de distillation (30). Le procédé comprend la formation d'un courant de reflux refroidi (56) à partir d'un effluent (54) issu d'une turbine de détente dynamique (26), la partie de l'effluent étant refroidie et au moins partiellement liquéfiée dans un échangeur thermique (28). Il comprend l'introduction du courant de reflux refroidi (56) issu de l'échangeur thermique (28) dans la première colonne de distillation (30).
PCT/FR2010/051437 2009-07-09 2010-07-07 Procédé de production d'un courant riche en méthane et d'un courant riche en hydrocarbures en c2+, et installation associée WO2011004123A2 (fr)

Priority Applications (4)

Application Number Priority Date Filing Date Title
MX2012000474A MX353746B (es) 2009-07-09 2010-07-07 Metodo para producir un flujo rico en metano y un flujo rico en hidrocarburos de c2+, e instalaciones asociadas.
BR112012000404-2A BR112012000404B1 (pt) 2009-07-09 2010-07-07 Processo e instalação de produção de uma corrente rica em metano e de uma corrente rica em hidrocarbonetos em c2+ a partir de uma corrente de alimentação contendo hidrocarbonetos
EP10742221.4A EP2452140B1 (fr) 2009-07-09 2010-07-07 Procédé de production d'un courant riche en méthane et d'un courant riche en hydrocarbures en c2+, et installation associée
CA2767502A CA2767502C (fr) 2009-07-09 2010-07-07 Procede de production d'un courant riche en methane et d'un courant riche en hydrocarbures en c2+, et installation associee

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0954781 2009-07-09
FR0954781A FR2947897B1 (fr) 2009-07-09 2009-07-09 Procede de production d'un courant riche en methane et d'un courant riche en hydrocarbures en c2+, et installation associee.

Publications (2)

Publication Number Publication Date
WO2011004123A2 WO2011004123A2 (fr) 2011-01-13
WO2011004123A3 true WO2011004123A3 (fr) 2014-05-01

Family

ID=42123187

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/FR2010/051437 WO2011004123A2 (fr) 2009-07-09 2010-07-07 Procédé de production d'un courant riche en méthane et d'un courant riche en hydrocarbures en c2+, et installation associée

Country Status (9)

Country Link
US (2) US9310128B2 (fr)
EP (1) EP2452140B1 (fr)
AR (1) AR077652A1 (fr)
BR (1) BR112012000404B1 (fr)
CA (1) CA2767502C (fr)
DK (1) DK201070320A (fr)
FR (1) FR2947897B1 (fr)
MX (1) MX353746B (fr)
WO (1) WO2011004123A2 (fr)

Families Citing this family (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2966578B1 (fr) * 2010-10-20 2014-11-28 Technip France Procede simplifie de production d'un courant riche en methane et d'une coupe riche en hydrocarbures en c2+ a partir d'un courant de gaz naturel de charge, et installation associee.
FR2969745B1 (fr) 2010-12-27 2013-01-25 Technip France Procede de production d'un courant riche en methane et d'un courant riche en hydrocarbures en c2+ et installation associee.
FR2970258B1 (fr) * 2011-01-06 2014-02-07 Technip France Procede de production d'une coupe riche en hydrocarbures en c3+ et d'un courant riche en methane et ethane a partir d'un courant d'alimentation riche en hydrocarbures et installation associee.
US20130074542A1 (en) * 2011-09-25 2013-03-28 Mehdi Mehrpooya System and method for recovering natural gas liquids with auto refrigeration system
DE102013013883A1 (de) * 2013-08-20 2015-02-26 Linde Aktiengesellschaft Kombinierte Abtrennung von Schwer- und Leichtsiedern aus Erdgas
FR3012150B1 (fr) 2013-10-23 2016-09-02 Technip France Procede de fractionnement d'un courant de gaz craque, mettant en oeuvre un courant de recycle intermediaire, et installation associee
EP3060865A1 (fr) * 2013-10-25 2016-08-31 Air Products and Chemicals, Inc. Purification de dioxyde de carbone
WO2015158395A1 (fr) * 2014-04-17 2015-10-22 Statoil Petroleum As Extraction de liquides de gaz naturel et refroidissement de gaz recomprimé traité
RU2570736C1 (ru) * 2014-07-18 2015-12-10 Публичное акционерное общество "Газпром" Способ переработки природного или попутного нефтяного газа
US20160069610A1 (en) * 2014-09-04 2016-03-10 Ortloff Engineers, Ltd. Hydrocarbon gas processing
US10808999B2 (en) 2014-09-30 2020-10-20 Dow Global Technologies Llc Process for increasing ethylene and propylene yield from a propylene plant
EP3040405A1 (fr) 2014-12-30 2016-07-06 Technip France Procédé pour améliorer la récupération de propylène, à partir d'unité de craquage catalytique fluide
FR3042983B1 (fr) * 2015-11-03 2017-10-27 Air Liquide Reflux de colonnes de demethanisation
EP3389807A4 (fr) * 2015-12-18 2019-08-14 Bechtel Hydrocarbon Technology Solutions, Inc. Systèmes et procédés de récupération d'hydrocarbures légers désirés à partir de déchets gazeux de raffinerie au moyen d'un turbodétendeur aval
DE102016003305A1 (de) * 2016-03-17 2017-09-21 Linde Aktiengesellschaft Verfahren zum Abtrennen einer ethanreichen Fraktion aus Erdgas
CN105797417B (zh) * 2016-04-29 2018-07-06 大连德泽药业有限公司 监控温度制备高纯度馏分的分馏装置、方法以及系统
GB2562692B (en) * 2016-11-18 2022-07-13 Costain Oil Gas & Process Ltd Hydrocarbon separation process and apparatus
MX2020002413A (es) * 2017-09-06 2020-09-17 Linde Eng North America Inc Metodos para proporcionar refrigeracion en plantas de recuperacion de liquidos del gas natural.
EP4031820A1 (fr) * 2019-09-19 2022-07-27 Exxonmobil Upstream Research Company (EMHC-N1-4A-607) Prétraitement, pré-refroidissement et récupération de condensat de gaz naturel par compression et détente à haute pression
EP4031821A1 (fr) * 2019-09-19 2022-07-27 ExxonMobil Upstream Research Company Pré-traitement et pré-refroidissement de gaz naturel par compression et détente à haute pression
JP7453952B2 (ja) 2021-11-10 2024-03-21 一哉 上原 アスピレータ減圧手段を用いる減圧タービン発電システム

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US3213631A (en) * 1961-09-22 1965-10-26 Lummus Co Separated from a gas mixture on a refrigeration medium
US4687499A (en) * 1986-04-01 1987-08-18 Mcdermott International Inc. Process for separating hydrocarbon gas constituents
US5983664A (en) * 1997-04-09 1999-11-16 Elcor Corporation Hydrocarbon gas processing
US6244070B1 (en) * 1999-12-03 2001-06-12 Ipsi, L.L.C. Lean reflux process for high recovery of ethane and heavier components
US20010008073A1 (en) * 2000-01-07 2001-07-19 Finn Adrian Joseph Hydrocarbon separation process and apparatus
US6526777B1 (en) * 2001-04-20 2003-03-04 Elcor Corporation LNG production in cryogenic natural gas processing plants
US6578379B2 (en) * 2000-12-13 2003-06-17 Technip-Coflexip Process and installation for separation of a gas mixture containing methane by distillation

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US2823523A (en) * 1956-03-26 1958-02-18 Inst Gas Technology Separation of nitrogen from methane
US5265427A (en) * 1992-06-26 1993-11-30 Exxon Production Research Company Refrigerant recovery scheme
US5555748A (en) * 1995-06-07 1996-09-17 Elcor Corporation Hydrocarbon gas processing
US9316433B2 (en) * 2006-06-27 2016-04-19 Fluor Technologies Corporation Ethane recovery methods and configurations

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3213631A (en) * 1961-09-22 1965-10-26 Lummus Co Separated from a gas mixture on a refrigeration medium
US4687499A (en) * 1986-04-01 1987-08-18 Mcdermott International Inc. Process for separating hydrocarbon gas constituents
US5983664A (en) * 1997-04-09 1999-11-16 Elcor Corporation Hydrocarbon gas processing
US6244070B1 (en) * 1999-12-03 2001-06-12 Ipsi, L.L.C. Lean reflux process for high recovery of ethane and heavier components
US20010008073A1 (en) * 2000-01-07 2001-07-19 Finn Adrian Joseph Hydrocarbon separation process and apparatus
US6578379B2 (en) * 2000-12-13 2003-06-17 Technip-Coflexip Process and installation for separation of a gas mixture containing methane by distillation
US6526777B1 (en) * 2001-04-20 2003-03-04 Elcor Corporation LNG production in cryogenic natural gas processing plants

Also Published As

Publication number Publication date
FR2947897B1 (fr) 2014-05-09
US20160370109A9 (en) 2016-12-22
MX353746B (es) 2018-01-26
FR2947897A1 (fr) 2011-01-14
BR112012000404A2 (pt) 2016-04-05
CA2767502C (fr) 2017-09-12
AR077652A1 (es) 2011-09-14
MX2012000474A (es) 2012-01-27
US9310128B2 (en) 2016-04-12
US9823015B2 (en) 2017-11-21
WO2011004123A2 (fr) 2011-01-13
DK201070320A (en) 2011-01-10
US20150292798A1 (en) 2015-10-15
EP2452140A2 (fr) 2012-05-16
EP2452140B1 (fr) 2019-04-10
US20110005273A1 (en) 2011-01-13
BR112012000404B1 (pt) 2023-10-31
CA2767502A1 (fr) 2011-01-13

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