ES2174213T3 - Procedimiento para producir un hidrato de gas. - Google Patents

Procedimiento para producir un hidrato de gas.

Info

Publication number
ES2174213T3
ES2174213T3 ES97900274T ES97900274T ES2174213T3 ES 2174213 T3 ES2174213 T3 ES 2174213T3 ES 97900274 T ES97900274 T ES 97900274T ES 97900274 T ES97900274 T ES 97900274T ES 2174213 T3 ES2174213 T3 ES 2174213T3
Authority
ES
Spain
Prior art keywords
gas
containers
pressure
supplied
hydration
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.)
Expired - Lifetime
Application number
ES97900274T
Other languages
English (en)
Inventor
Andrew Richard Williams
Trevor Smith
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.)
BG Intellectual Property Ltd
Original Assignee
BG Intellectual Property Ltd
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 BG Intellectual Property Ltd filed Critical BG Intellectual Property Ltd
Application granted granted Critical
Publication of ES2174213T3 publication Critical patent/ES2174213T3/es
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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

PLANTA DE PRODUCCION DE HIDRATO DE GAS NATURAL QUE COMPRENDE TRES ETAPAS (I), (II), Y (III). LA ETAPA (I) COMPRENDE TRES RECIPIENTES A PRESION (A1, A2, Y A3), LA ETAPA (II), DOS RECIPIENTES A PRESION (A4 Y A5), Y LA ETAPA (III) UN RECIPIENTE A PRESION (A6). LAS CONDICIONES DE TEMPERATURA Y PRESION EN LOS RECIPIENTES A PRESION SON LAS ADECUADAS PARA QUE SE FORME EL HIDRATO DE GAS EN LOS RECIPIENTES. EL HIDRATO FORMADO SE EXTRAE A TRAVES DE TUBERIAS (E1, E2, E3, E4, E5 Y E6) DE LOS RECIPIENTES A PRESION HASTA UN COLECTOR (34). SE SUMINISTRA AGUA FRIA, QUE ACTUA TANTO DE AGUA DE REACCION COMO DE REFRIGERANTE PARA EL PROCESO, POR MEDIO DE DISPOSITIVOS DE REFRIGERACION (20), DE FORMA SIMULTANEA, A LA PARTE INFERIOR DE CADA RECIPIENTE A PRESION, POR MEDIO DE UNA TUBERIA (22), AL COLECTOR (32) Y A LAS TUBERIAS (B1, B2, B3, B4, B5 Y B6). SE SUMINISTRA GAS NATURAL DESDE UN ALIMENTADOR (26), POR MEDIO DE UNA TUBERIA (30), EL COLECTOR (32) Y LAS TUBERIAS (C1, C2 Y C3) A TOBERAS SITUADAS EN LA PARTE INFERIOR DE CADA DEPOSITO (A1, A2 Y A3), BURBUJEANDO EL GAS DESDE LAS TOBERAS HACIA ARRIBA A TRAVES DE COLUMNAS DE AGUA EN LOS RECIPIENTES (A1, A2 Y A3). SE ALIMENTA GAS SIN REACCIONAR DESDE LOS DEPOSITOS (A1, A2 Y A3) A TOBERAS SIMILARES EN LOS DEPOSITOS (A4 Y A5), DESDE LOS CUALES EL GAS SIN REACCIONAR SE ALIMENTA AL DEPOSITO (A6), DEL CUAL EL GAS SIN REACCIONAR SE EXTRAE A TRAVES DE LA TUBERIA (D6). LA VELOCIDAD MEDIA SUPERFICIAL DE ASCENSO DEL GAS ES SUSTANCIALMENTE LA MISMA EN LAS TRES ETAPAS.
ES97900274T 1996-01-18 1997-01-07 Procedimiento para producir un hidrato de gas. Expired - Lifetime ES2174213T3 (es)

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
ES2174213T3 true ES2174213T3 (es) 2002-11-01

Family

ID=10787218

Family Applications (1)

Application Number Title Priority Date Filing Date
ES97900274T Expired - Lifetime ES2174213T3 (es) 1996-01-18 1997-01-07 Procedimiento para producir un hidrato de gas.

Country Status (24)

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

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GB9906310D0 (en) * 1998-06-15 1999-05-12 Unilever Plc Manufacture of edible frozen products
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
CA2410578A1 (en) * 2001-03-29 2002-11-25 Mitsubishi Heavy Industries, Ltd. Gas hydrate production device and gas hydrate dehydrating device
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
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
AU2006236093B2 (en) * 2003-02-07 2008-12-11 Woodside Energy Ltd. Removing contaminants from natural gas by cooling
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
WO2007063915A1 (ja) * 2005-11-29 2007-06-07 Mitsui Engineering & Shipbuilding Co., Ltd. ガスハイドレートの製造方法
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
WO2018118623A1 (en) 2016-12-22 2018-06-28 Exxonmobil Research And 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 (en) 2017-02-15 2018-08-23 Exxonmobil Research And Engineering Company Sequestration of co2 using 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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US2356407A (en) * 1941-08-15 1944-08-22 Fluor Corp System for forming and storing hydrocarbon hydrates
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US5536893A (en) * 1994-01-07 1996-07-16 Gudmundsson; Jon S. Method for production of gas hydrates for transportation and storage
NO951669L (no) * 1995-04-28 1996-10-29 Statoil As Fremgangsmåte og apparat for fremstilling av et hydrokarbonprodukt
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
GB9626665D0 (en) 1997-02-12
JP3168013B2 (ja) 2001-05-21
DE69710819D1 (de) 2002-04-11
DZ2163A1 (fr) 2002-12-01
DE69710819T2 (de) 2003-06-18
GB9601030D0 (en) 1996-03-20
EG21218A (en) 2001-02-28
AU1386597A (en) 1997-08-11
OA10618A (en) 2002-08-30
TR199700982T1 (xx) 1998-01-21
ATE214146T1 (de) 2002-03-15
EP0820574B1 (en) 2002-03-06
GB2309227A (en) 1997-07-23
CA2214373A1 (en) 1997-07-24
EP0820574A1 (en) 1998-01-28
DK100797A (da) 1997-09-04
US6111155A (en) 2000-08-29
HK1008560A1 (en) 1999-05-14
PL183667B1 (pl) 2002-06-28
TW412586B (en) 2000-11-21
PL322305A1 (en) 1998-01-19
NZ325367A (en) 1999-02-25
CA2214373C (en) 2002-04-02
ZA9778B (en) 1997-09-29
JPH10503971A (ja) 1998-04-14
AU689056B2 (en) 1998-03-19
TNSN97013A1 (fr) 1999-12-31
AR005485A1 (es) 1999-06-23
MX9707070A (es) 1997-11-29
CN1181806A (zh) 1998-05-13
PT820574E (pt) 2002-08-30
WO1997026494A1 (en) 1997-07-24
GB2309227B (en) 1999-09-29

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