TNSN97013A1 - Une methode de production d'hydrate de gaz - Google Patents

Une methode de production d'hydrate de gaz

Info

Publication number
TNSN97013A1
TNSN97013A1 TNTNSN97013A TNSN97013A TNSN97013A1 TN SN97013 A1 TNSN97013 A1 TN SN97013A1 TN TNSN97013 A TNTNSN97013 A TN TNSN97013A TN SN97013 A TNSN97013 A TN SN97013A TN SN97013 A1 TNSN97013 A1 TN SN97013A1
Authority
TN
Tunisia
Prior art keywords
containers
gas
pressure
until
container
Prior art date
Application number
TNTNSN97013A
Other languages
English (en)
Inventor
Trevor Smith
Andrew Richard Williams
Original Assignee
British Gas Plc
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 British Gas Plc filed Critical British Gas Plc
Publication of TNSN97013A1 publication Critical patent/TNSN97013A1/fr

Links

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
    • C10L3/108—Production of gas hydrates
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

UNE INSTALLATION POUR LA PRODUCTION D'HYDRATE DE GAZ NATUREL SE COMPOSE DE TROIS PHASES (I), (II) ET (III). LA PHASE (I) SE COMPOSE DE TROIS RECIPIENTS SOUS PRESSION A1, A2 ET A3, LA PHASE (II) DE DEUX RECIPIENTS SOUS PRESSION A4 ET A5, ET LA PHASE (III) DU RECIPIENT SOUS PRESSION A6. LES CONDITIONS DE TEMPERATURE ET DE PRESSION DANS LES RECIPIENTS SOUS PRESSION SONT TELLES QUE L'HYDRATE DE GAZ EST FORME DANS LES RECIPIENTS. L'HYDRATE FORME EST EVACUE A TRAVERS LES TUYAUX E1, E2, E3, E4, E5 ET E6 DES RECIPIENTS SOUS PRESSION JUSQU'A UN COLLECTEUR 34. DE L'EAU REFROIDIE QUI EST A LA FOIS L'EAU REACTIVE ET LE LIQUIDE DE REFROIDISSEMENT POUR LE TRAITEMENT EST FOURNIE PAR DES MOYENS DE REFROIDISSEMENT 20 ET AMENEE SIMULTANEMENT JUSQU'A LA PARTIE INFERIEURE DE CHAQUE RECIPIENT SOUS PRESSION A TRAVERS LE TUYAU 22, LE COLLECTEUR 32 ET LES TUYAUX B1,B2,B3,B4,B5 ET B6. LE GAZ NATUREL DE L'ARRIVEE 26 EST AMENE PAR LE TUYAU 30, LE COLLECTEUR 32 ET LES TUYAUX C1, C2, C3 JUSQU'AUX AJUTAGES DANS LA PARTIE INFERIEURE DE CHAQUE RECIPIENT A1, A2 ET A3 A PARTIR DESQUELS AJUTAGES LE GAZ BOUILLONE VERS LE HAUT A TRAVERS LES COLONNES D'EAU DANS LES RECIPIENTS A1, A2 ET A3. LE GAZ NON ENTRE EN REACTION EST AMENE DES RECIPIENTS A1, A2 ET A3 JUSQU'A DES AJUTAGES SIMILAIRES DANS LES RECIPIENTS A4 ET A5 A PARTIR DESQUELS LE GAZ NON ENTRE EN REACTION EST AMENE JUSQU'A UN AJUTAGE DANS LE RECIPIENT A6 A PARTIR DUQUEL LE GAZ ON ENTRE EN REACTION EST EVACUE A TRAVERS LE TUYAU D6. LA VELOCITE SUPERFICIELLE ASCENDANTE MOYENNE DU GAZ EST ESSENTIELLEMENT LA MEME DANS LES TROIS PHASES
TNTNSN97013A 1996-01-18 1997-01-17 Une methode de production d'hydrate de gaz TNSN97013A1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GBGB9601030.1A GB9601030D0 (en) 1996-01-18 1996-01-18 a method of producing gas hydrate

Publications (1)

Publication Number Publication Date
TNSN97013A1 true TNSN97013A1 (fr) 1999-12-31

Family

ID=10787218

Family Applications (1)

Application Number Title Priority Date Filing Date
TNTNSN97013A TNSN97013A1 (fr) 1996-01-18 1997-01-17 Une methode de production d'hydrate de gaz

Country Status (25)

Country Link
US (1) US6111155A (fr)
EP (1) EP0820574B1 (fr)
JP (1) JP3168013B2 (fr)
CN (1) CN1181806A (fr)
AR (1) AR005485A1 (fr)
AT (1) ATE214146T1 (fr)
AU (1) AU689056B2 (fr)
CA (1) CA2214373C (fr)
DE (1) DE69710819T2 (fr)
DK (1) DK100797A (fr)
DZ (1) DZ2163A1 (fr)
EG (1) EG21218A (fr)
ES (1) ES2174213T3 (fr)
GB (2) GB9601030D0 (fr)
HK (1) HK1008560A1 (fr)
MX (1) MX9707070A (fr)
NZ (1) NZ325367A (fr)
OA (1) OA10618A (fr)
PL (1) PL183667B1 (fr)
PT (1) PT820574E (fr)
TN (1) TNSN97013A1 (fr)
TR (1) TR199700982T1 (fr)
TW (1) TW412586B (fr)
WO (1) WO1997026494A1 (fr)
ZA (1) ZA9778B (fr)

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US6245955B1 (en) * 1998-09-01 2001-06-12 Shell Oil Company Method for the sub-sea separation of hydrocarbon liquids from water and gases
AUPQ118899A0 (en) 1999-06-24 1999-07-22 Woodside Energy Limited Natural gas hydrate and method for producing same
AU778742B2 (en) * 1999-06-24 2004-12-16 Metasource Pty Ltd Natural gas hydrates and method of producing same
AU777346B2 (en) * 1999-08-17 2004-10-14 Metasource Pty Ltd Production plant for natural gas hydrate
AUPQ228399A0 (en) * 1999-08-17 1999-09-09 Woodside Energy Limited Production plant
US6296060B1 (en) * 2000-01-10 2001-10-02 Kerr-Mcgee Corporation Methods and systems for producing off-shore deep-water wells
KR20030004434A (ko) * 2001-03-29 2003-01-14 미츠비시 쥬고교 가부시키가이샤 가스 하이드레이트 제조 장치 및 가스 하이드레이트 탈수장치
JP5019683B2 (ja) * 2001-08-31 2012-09-05 三菱重工業株式会社 ガスハイドレートスラリーの脱水装置及び脱水方法
CN1324289C (zh) * 2001-12-28 2007-07-04 中国科学院广州能源研究所 促进气体水合物生长的方法
US6881389B2 (en) * 2002-09-24 2005-04-19 Edg, Inc. Removal of H2S and CO2 from a hydrocarbon fluid stream
AU2006236093B2 (en) * 2003-02-07 2008-12-11 Woodside Energy Ltd. Removing contaminants from natural gas by cooling
AU2003900534A0 (en) * 2003-02-07 2003-02-20 Shell Internationale Research Maatschappij B.V. Process and apparatus for removal of a contaminant from a natural gas feed stream
US20050137432A1 (en) * 2003-12-17 2005-06-23 Chevron U.S.A. Inc. Method and system for preventing clathrate hydrate blockage formation in flow lines by enhancing water cut
CN100387691C (zh) * 2005-02-03 2008-05-14 石油大学(北京) 生成水合物的方法
EP1956071A4 (fr) * 2005-11-29 2010-08-18 Mitsui Shipbuilding Eng Procede de production d un hydrate gazeux
CN101153231B (zh) * 2006-09-25 2010-10-27 上海理工大学 多反应釜喷雾强化天然气水合物连续制备装置及工艺流程
CN101113379B (zh) * 2007-07-11 2010-09-15 哈尔滨工业大学 天然气水合物合成的双级串联反应器
CN101514300B (zh) * 2009-03-23 2012-05-23 江苏工业学院 一种气体水合物促进剂的制备方法
DE102009051277A1 (de) 2009-10-29 2011-05-05 Linde Aktiengesellschaft Verfahren und Vorrichtung zur Erzeugung von Clathrat
US8354565B1 (en) * 2010-06-14 2013-01-15 U.S. Department Of Energy Rapid gas hydrate formation process
CN103571557B (zh) * 2013-11-12 2014-12-24 北京化工大学 一种制造天然气水合物的方法
CN105779049B (zh) * 2015-11-24 2019-03-01 北京化工大学 一种制造煤层气水合物的方法
US10668425B2 (en) 2016-12-22 2020-06-02 Exxonmobil Research & Engineering Company Separation of methane from gas mixtures
US20180178161A1 (en) 2016-12-22 2018-06-28 Exxonmobil Research And Engineering Company Separation of co2 from gas mixtures
WO2018151907A1 (fr) 2017-02-15 2018-08-23 Exxonmobil Research And Engineering Company Séquestration de co2 à l'aide de calthrates
US11292730B2 (en) 2018-04-24 2022-04-05 Exxonmobil Research And Engineering Company Hydrates for water desalination using iso-butane additive
CN108671858B (zh) * 2018-08-06 2023-06-27 西南石油大学 一种水合物快速合成装置及方法
CN112127850B (zh) * 2019-06-24 2021-12-17 南京延长反应技术研究院有限公司 一种开采可燃冰的绿色工艺
CN110387276B (zh) * 2019-08-20 2023-10-27 中国石油化工股份有限公司 一种喷射式页岩气水合物浆液快速合成装置及方法
CN112844275B (zh) * 2020-11-05 2022-06-14 东北石油大学 一种用于分层多级水合物浆制备的反应釜以及制备方法
CN112705132A (zh) * 2020-12-08 2021-04-27 西安石油大学 一种气体水合物快速连续生成及制饼装置和方法

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US5660603A (en) * 1995-09-05 1997-08-26 International Process Services, Inc. Process for separating selected components from multi-component natural gas streams

Also Published As

Publication number Publication date
GB2309227B (en) 1999-09-29
DK100797A (da) 1997-09-04
DZ2163A1 (fr) 2002-12-01
ATE214146T1 (de) 2002-03-15
EG21218A (en) 2001-02-28
AU689056B2 (en) 1998-03-19
DE69710819D1 (de) 2002-04-11
EP0820574B1 (fr) 2002-03-06
TW412586B (en) 2000-11-21
GB9626665D0 (en) 1997-02-12
ES2174213T3 (es) 2002-11-01
HK1008560A1 (en) 1999-05-14
TR199700982T1 (xx) 1998-01-21
AU1386597A (en) 1997-08-11
AR005485A1 (es) 1999-06-23
CA2214373C (fr) 2002-04-02
OA10618A (en) 2002-08-30
DE69710819T2 (de) 2003-06-18
MX9707070A (es) 1997-11-29
PL183667B1 (pl) 2002-06-28
JP3168013B2 (ja) 2001-05-21
CN1181806A (zh) 1998-05-13
ZA9778B (en) 1997-09-29
PT820574E (pt) 2002-08-30
NZ325367A (en) 1999-02-25
GB9601030D0 (en) 1996-03-20
JPH10503971A (ja) 1998-04-14
EP0820574A1 (fr) 1998-01-28
PL322305A1 (en) 1998-01-19
CA2214373A1 (fr) 1997-07-24
US6111155A (en) 2000-08-29
GB2309227A (en) 1997-07-23
WO1997026494A1 (fr) 1997-07-24

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