CA2378679A1 - Procede de deshydratation et de fractionnement d'un gaz naturel basse pression - Google Patents

Procede de deshydratation et de fractionnement d'un gaz naturel basse pression Download PDF

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Publication number
CA2378679A1
CA2378679A1 CA002378679A CA2378679A CA2378679A1 CA 2378679 A1 CA2378679 A1 CA 2378679A1 CA 002378679 A CA002378679 A CA 002378679A CA 2378679 A CA2378679 A CA 2378679A CA 2378679 A1 CA2378679 A1 CA 2378679A1
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CA
Canada
Prior art keywords
ceramic
powder
ceramic powder
low pressure
natural gas
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.)
Granted
Application number
CA002378679A
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English (en)
Other versions
CA2378679C (fr
Inventor
Fabrice Lecomte
Beatrice Fischer
Jean-Charles Viltard
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IFP Energies Nouvelles IFPEN
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IFP Energies Nouvelles IFPEN
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Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of CA2378679A1 publication Critical patent/CA2378679A1/fr
Application granted granted Critical
Publication of CA2378679C publication Critical patent/CA2378679C/fr
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10—Working-up natural gas or synthetic natural gas
    • C10L3/101—Removal of contaminants
    • C10L3/102—Removal of contaminants of acid contaminants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/002—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by condensation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26—Drying gases or vapours
    • B01D53/263—Drying gases or vapours by absorption
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/10—Working-up natural gas or synthetic natural gas
    • 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
    • F25J3/0204—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
    • F25J3/0209—Natural gas or substitute natural gas
    • 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
    • F25J3/0233—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 CnHm with 1 carbon atom or more
    • 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
    • F25J3/0242—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 CnHm with 3 carbon atoms or more
    • 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
    • F25J2200/00—Processes or apparatus using separation by rectification
    • F25J2200/80—Processes or apparatus using separation by rectification using integrated mass and heat exchange, i.e. non-adiabatic rectification in a reflux exchanger or dephlegmator
    • 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
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/02—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum
    • 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
    • F25J2205/00—Processes or apparatus using other separation and/or other processing means
    • F25J2205/50—Processes or apparatus using other separation and/or other processing means using absorption, i.e. with selective solvents or lean oil, heavier CnHm and including generally a regeneration step for the solvent or lean oil
    • 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
    • F25J2220/00—Processes or apparatus involving steps for the removal of impurities
    • F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
    • F25J2220/66—Separating acid gases, e.g. CO2, SO2, H2S or RSH
    • 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
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/04—Internal refrigeration with work-producing gas expansion loop

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Compositions Of Oxide Ceramics (AREA)
  • Glanulating (AREA)

Abstract

A method for manufacturing spherical ceramic powder is provided. The method includes essentially a spray drying step and a sintering step. In the spray drying step, a spray nozzle is used to spray slurry containing powdered raw material consisting essentially of ceramic ingredients to form liquid droplets, and liquid contents in the liquid droplets are heated and removed to obtain ceramic granular powder. In the sintering step, the ceramic granular powder is sintered to form spherical ceramic powder. The method provides ceramic powder having a mean particle site of about 1-50 .mu.m and a sphericity of about 0.8 or higher, which is suited for mixing wi th resin material to form a compound. The ceramic powder has high dispersant and filling properties against the resin material.
CA002378679A 2001-03-29 2002-03-25 Procede de deshydratation et de fractionnement d'un gaz naturel basse pression Expired - Fee Related CA2378679C (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR0104297A FR2822838B1 (fr) 2001-03-29 2001-03-29 Procede de deshydratation et de fractionnement d'un gaz naturel basse pression
FR0104297 2001-03-29

Publications (2)

Publication Number Publication Date
CA2378679A1 true CA2378679A1 (fr) 2002-09-29
CA2378679C CA2378679C (fr) 2009-10-06

Family

ID=8861723

Family Applications (1)

Application Number Title Priority Date Filing Date
CA002378679A Expired - Fee Related CA2378679C (fr) 2001-03-29 2002-03-25 Procede de deshydratation et de fractionnement d'un gaz naturel basse pression

Country Status (6)

Country Link
US (1) US6767388B2 (fr)
CA (1) CA2378679C (fr)
FR (1) FR2822838B1 (fr)
GB (1) GB2376953B (fr)
NL (1) NL1020268C2 (fr)
SA (1) SA02230027B1 (fr)

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* Cited by examiner, † Cited by third party
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US6984257B2 (en) * 2002-02-08 2006-01-10 Heath Rodney T Natural gas dehydrator and system
FR2822838B1 (fr) * 2001-03-29 2005-02-04 Inst Francais Du Petrole Procede de deshydratation et de fractionnement d'un gaz naturel basse pression
FR2822839B1 (fr) * 2001-03-29 2003-05-16 Inst Francais Du Petrole Procede ameliore des deshydratation et de degazolinage d'un gaz naturel humide
US7219512B1 (en) * 2001-05-04 2007-05-22 Battelle Energy Alliance, Llc Apparatus for the liquefaction of natural gas and methods relating to same
US7591150B2 (en) * 2001-05-04 2009-09-22 Battelle Energy Alliance, Llc Apparatus for the liquefaction of natural gas and methods relating to same
US20070137246A1 (en) * 2001-05-04 2007-06-21 Battelle Energy Alliance, Llc Systems and methods for delivering hydrogen and separation of hydrogen from a carrier medium
US7594414B2 (en) * 2001-05-04 2009-09-29 Battelle Energy Alliance, Llc Apparatus for the liquefaction of natural gas and methods relating to same
US7008544B2 (en) * 2002-05-08 2006-03-07 Marine Desalination Systems, L.L.C. Hydrate-based desalination/purification using permeable support member
US6955705B1 (en) * 2004-06-02 2005-10-18 Rdc Research Llc Method and system for compressing and dehydrating wet natural gas produced from low-pressure wells
US9353315B2 (en) 2004-09-22 2016-05-31 Rodney T. Heath Vapor process system
US8061413B2 (en) 2007-09-13 2011-11-22 Battelle Energy Alliance, Llc Heat exchangers comprising at least one porous member positioned within a casing
US9217603B2 (en) 2007-09-13 2015-12-22 Battelle Energy Alliance, Llc Heat exchanger and related methods
US9574713B2 (en) 2007-09-13 2017-02-21 Battelle Energy Alliance, Llc Vaporization chambers and associated methods
US9254448B2 (en) 2007-09-13 2016-02-09 Battelle Energy Alliance, Llc Sublimation systems and associated methods
US8555672B2 (en) * 2009-10-22 2013-10-15 Battelle Energy Alliance, Llc Complete liquefaction methods and apparatus
US8899074B2 (en) 2009-10-22 2014-12-02 Battelle Energy Alliance, Llc Methods of natural gas liquefaction and natural gas liquefaction plants utilizing multiple and varying gas streams
US8529215B2 (en) 2008-03-06 2013-09-10 Rodney T. Heath Liquid hydrocarbon slug containing vapor recovery system
RU2554736C2 (ru) * 2009-07-21 2015-06-27 Шелл Интернэшнл Рисерч Маатсхаппий Б.В. Способ очистки многофазного углеводородного потока и предназначенная для этого установка
CN201768471U (zh) * 2010-07-23 2011-03-23 镇海石化建安工程有限公司 低温甲醇洗原料气冷却器
US8864887B2 (en) * 2010-09-30 2014-10-21 Rodney T. Heath High efficiency slug containing vapor recovery
RU2476789C1 (ru) * 2011-08-24 2013-02-27 Открытое акционерное общество "ВНИПИгаздобыча" Способ низкотемпературной подготовки природного газа и извлечения нестабильного углеводородного конденсата из пластового газа (варианты) и установка для его осуществления
CA2875296C (fr) 2012-05-10 2020-10-27 Rodney T. Heath Unite de combinaison d'unites de traitement
US10655911B2 (en) 2012-06-20 2020-05-19 Battelle Energy Alliance, Llc Natural gas liquefaction employing independent refrigerant path
RU2506505C1 (ru) * 2012-11-21 2014-02-10 Открытое акционерное общество "НОВАТЭК" Установка для подготовки газа с удаленным терминалом управления и использованием программного комплекса автоматического управления технологическим процессом
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US9527786B1 (en) 2013-03-15 2016-12-27 Rodney T. Heath Compressor equipped emissions free dehydrator
US9291409B1 (en) 2013-03-15 2016-03-22 Rodney T. Heath Compressor inter-stage temperature control
US9932989B1 (en) 2013-10-24 2018-04-03 Rodney T. Heath Produced liquids compressor cooler
CN105509413B (zh) * 2016-01-19 2018-05-22 中国科学院理化技术研究所 聚烯烃排火炬气的深冷分离回收系统及方法
RU2685460C1 (ru) * 2018-04-17 2019-04-18 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ автоматического поддержания температурного режима технологических процессов установки низкотемпературной сепарации газа с применением аппаратов воздушного охлаждения в условиях крайнего севера
RU2692164C1 (ru) * 2018-10-08 2019-06-21 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ автоматического поддержания плотности нестабильного газового конденсата, подаваемого в магистральный конденсатопровод, с применением аппарата воздушного охлаждения, на установках низкотемпературной сепарации газа в районах крайнего севера
RU2709045C1 (ru) * 2019-01-09 2019-12-13 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ автоматического управления производительностью установки низкотемпературной сепарации газа
RU2709119C1 (ru) * 2019-06-10 2019-12-16 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ оптимизации процесса отмывки ингибитора из нестабильного газового конденсата на установках низкотемпературной сепарации газа
FR3106136B1 (fr) 2020-01-14 2021-12-31 Axens Procédé de dégazolinage d’un gaz contenant des hydrocarbures condensables
RU2743726C1 (ru) * 2020-07-14 2021-02-25 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ оптимизации процесса отмывки ингибитора из нестабильного газового конденсата на установках низкотемпературной сепарации газа нефтегазоконденсатных месторождений севера рф
RU2743711C1 (ru) * 2020-07-14 2021-02-24 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ оптимизации процесса отмывки ингибитора из нестабильного газового конденсата на установках низкотемпературной сепарации газа нефтегазоконденсатных месторождений севера рф
RU2755099C1 (ru) * 2020-12-09 2021-09-13 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ автоматического управления низкотемпературной сепарацией газа на нефтегазоконденсатных месторождениях севера рф
RU2756966C1 (ru) * 2020-12-09 2021-10-07 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ автоматического поддержания температурного режима технологических процессов установки низкотемпературной сепарации газа турбодетандерными агрегатами в условиях севера рф
RU2765415C1 (ru) * 2021-01-11 2022-01-31 Общество с ограниченной ответственностью "Газпром добыча Уренгой" Способ подготовки углеводородного газа к транспорту методом низкотемпературной сепарации
RU2768837C1 (ru) * 2021-06-02 2022-03-24 Общество с ограниченной ответственностью "Газпром добыча Ямбург" Способ автоматического поддержания плотности нестабильного газового конденсата с применением турбодетандерных агрегатов на выходе установок низкотемпературной сепарации газа северных нефтегазоконденсатных месторождений рф

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FR2740468B1 (fr) * 1995-10-27 1997-12-12 Inst Francais Du Petrole Procede de sechage de gaz au glycol incluant la purification des rejets gazeux
FR2743083B1 (fr) * 1995-12-28 1998-01-30 Inst Francais Du Petrole Procede de deshydratation, de desacidification et de degazolinage d'un gaz naturel, utilisant un melange de solvants
FR2760653B1 (fr) * 1997-03-13 1999-04-30 Inst Francais Du Petrole Procede de desacidification avec production de gaz acides en phase liquide
FR2771653B1 (fr) * 1997-12-02 1999-12-31 Nouvelles Appl Tech Procede de deshydratation d'un gaz humide au moyen d'un dessiccant liquide, avec regeneration poussee dudit dessiccant
FR2787870B1 (fr) * 1998-12-24 2001-02-02 Inst Francais Du Petrole Procede et systeme de fractionnement d'un gaz a haute pression
FR2814378B1 (fr) * 2000-09-26 2002-10-31 Inst Francais Du Petrole Procede de pretraitement d'un gaz naturel contenant des gaz acides
FR2814379B1 (fr) * 2000-09-26 2002-11-01 Inst Francais Du Petrole Procede de desacidification d'un gaz par absorption dans un solvant avec un controle de la temperature
FR2822838B1 (fr) * 2001-03-29 2005-02-04 Inst Francais Du Petrole Procede de deshydratation et de fractionnement d'un gaz naturel basse pression
FR2822839B1 (fr) * 2001-03-29 2003-05-16 Inst Francais Du Petrole Procede ameliore des deshydratation et de degazolinage d'un gaz naturel humide

Also Published As

Publication number Publication date
US6767388B2 (en) 2004-07-27
GB2376953B (en) 2004-10-20
GB0207072D0 (en) 2002-05-08
FR2822838B1 (fr) 2005-02-04
NL1020268C2 (nl) 2002-10-01
CA2378679C (fr) 2009-10-06
US20020185006A1 (en) 2002-12-12
GB2376953A (en) 2002-12-31
SA02230027B1 (ar) 2006-10-31
FR2822838A1 (fr) 2002-10-04

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