AR005485A1 - Metodo para producir hidrato de gas - Google Patents
Metodo para producir hidrato de gasInfo
- Publication number
- AR005485A1 AR005485A1 ARP970100170A ARP970100170A AR005485A1 AR 005485 A1 AR005485 A1 AR 005485A1 AR P970100170 A ARP970100170 A AR P970100170A AR P970100170 A ARP970100170 A AR P970100170A AR 005485 A1 AR005485 A1 AR 005485A1
- Authority
- AR
- Argentina
- Prior art keywords
- gas
- pressurized
- vessels
- manifold
- containers
- Prior art date
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)
- Carbon And Carbon Compounds (AREA)
Abstract
Una planta para producir hidrato de gas natural comprende tres etapas (i), (ii) y (iii). La etapa (i) comprende tres recipientes presurizados A1, A2 y A3;la etapa (ii) comprende dos recipientes presurizados A4 y AA5 y la etapa (iii) comprende unre cipiente presurizado A6. Las condiciones de temperatura ypresión en los recipientes presurizados son tales que el hidrato de gas se forma dentro de dichos recipientes. El hidrato formado se retira de losrecipientes presurizados por canos e1,e2, e3, e4, e5 y e6 hacia un múltiple 34. El agua enfriada que es tanto agua de reacción como de refrigeración parael proceso, es provista por el medio refrigerante 20 y suministrado simultáneamente a la parte inferior de cadarecipiente presurizado por el cano22, el múltiple 32 y los canos b1, b2, b3, b4, b5 y b6. Desde el suministro 26 se alimenta gas natural por el cano 30, el múltiple 32 y los canos c1,c2 y c3,a las boquillas situadas en la parte inferior de cadarecipiente, A2, A2 y A3, desde cuyas boquillas el gas burbujea hacia arriba a través de las columnas deagua de los recipientes A1, A2 y A3. El gas sin reaccionar se alimenta desde los recipientes A1, A2 y A3 a boquillas similares de losrecipientes A4 y A5,desd e donde dicho gas sin reaccionar se alimenta a una boquilla del recipiente A6, y finalmente se retira de allí a través del cano d6. La velocidadsuperficial superior media del gas es sustancialmente la misma en las tresetapas. Equilibrio de hid rato calculado, Curva para una composición de gascaracterística del Mar del Norte, Temperatura (C°) Presiones (barg=)
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 |
|---|---|
| AR005485A1 true AR005485A1 (es) | 1999-06-23 |
Family
ID=10787218
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP970100170A AR005485A1 (es) | 1996-01-18 | 1997-01-16 | Metodo para producir hidrato de gas |
Country Status (25)
| 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) |
| HK (1) | HK1008560A1 (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) |
Families Citing this family (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| AUPQ228399A0 (en) * | 1999-08-17 | 1999-09-09 | Woodside Energy Limited | Production plant |
| AU777346B2 (en) * | 1999-08-17 | 2004-10-14 | Metasource Pty Ltd | Production plant for natural gas hydrate |
| 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 |
| 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 |
| EP1956071A4 (en) * | 2005-11-29 | 2010-08-18 | Mitsui Shipbuilding Eng | METHOD FOR PRODUCING A GAS HYDROTH |
| 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 |
| US20180178161A1 (en) | 2016-12-22 | 2018-06-28 | Exxonmobil Research And Engineering Company | Separation of co2 from gas mixtures |
| US10668425B2 (en) | 2016-12-22 | 2020-06-02 | Exxonmobil Research & Engineering Company | Separation of methane 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 |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2399723A (en) * | 1941-06-28 | 1946-05-07 | Kellogg M W Co | Gas hydration |
| US2356407A (en) * | 1941-08-15 | 1944-08-22 | Fluor Corp | System for forming and storing hydrocarbon hydrates |
| US2410583A (en) * | 1943-07-10 | 1946-11-05 | Fluor Corp | Separation of hydrate-forming components of gaseous mixtures |
| US2528028A (en) * | 1950-03-20 | 1950-10-31 | Arthur F Barry | Method and means for separating hydrocarbon liquids and water from high-pressure gasstreams |
| US2904511A (en) * | 1955-06-17 | 1959-09-15 | Koppers Co Inc | Method and apparatus for producing purified water from aqueous saline solutions |
| US2943124A (en) * | 1957-02-25 | 1960-06-28 | Nat Tank Co | Hydrocarbon hydrate separation process and separation unit therefor |
| US2974102A (en) * | 1959-11-09 | 1961-03-07 | Projex Engineering Corp | Hydrate forming saline water conversion process |
| US3354663A (en) * | 1961-06-13 | 1967-11-28 | Atlantic Richfield Co | Hydrate removal from wet natural gas |
| US4393660A (en) * | 1981-06-29 | 1983-07-19 | General Foods Corporation | Quiescent formation of gasified ice product and process |
| CH677618A5 (es) * | 1988-01-14 | 1991-06-14 | Sulzer Ag | |
| NO172080C (no) * | 1990-01-29 | 1993-06-02 | Gudmundsson Jon Steinar | Framgangsmaate for framstilling av gasshydrater og apparattil utfoerelse av samme |
| US5473904A (en) * | 1993-11-12 | 1995-12-12 | New Mexico Tech Research Foundation | Method and apparatus for generating, transporting and dissociating gas hydrates |
| 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 |
-
1996
- 1996-01-18 GB GBGB9601030.1A patent/GB9601030D0/en active Pending
- 1996-12-23 GB GB9626665A patent/GB2309227B/en not_active Expired - Fee Related
-
1997
- 1997-01-06 ZA ZA9700078A patent/ZA9778B/xx unknown
- 1997-01-07 CN CN97190182A patent/CN1181806A/zh active Pending
- 1997-01-07 AT AT97900274T patent/ATE214146T1/de not_active IP Right Cessation
- 1997-01-07 JP JP52576497A patent/JP3168013B2/ja not_active Expired - Fee Related
- 1997-01-07 PT PT97900274T patent/PT820574E/pt unknown
- 1997-01-07 PL PL97322305A patent/PL183667B1/pl not_active IP Right Cessation
- 1997-01-07 TR TR97/00982T patent/TR199700982T1/xx unknown
- 1997-01-07 ES ES97900274T patent/ES2174213T3/es not_active Expired - Lifetime
- 1997-01-07 MX MX9707070A patent/MX9707070A/es not_active IP Right Cessation
- 1997-01-07 US US08/913,412 patent/US6111155A/en not_active Expired - Fee Related
- 1997-01-07 AU AU13865/97A patent/AU689056B2/en not_active Ceased
- 1997-01-07 EP EP97900274A patent/EP0820574B1/en not_active Expired - Lifetime
- 1997-01-07 NZ NZ325367A patent/NZ325367A/xx unknown
- 1997-01-07 WO PCT/GB1997/000021 patent/WO1997026494A1/en active IP Right Grant
- 1997-01-07 DE DE69710819T patent/DE69710819T2/de not_active Expired - Fee Related
- 1997-01-07 CA CA002214373A patent/CA2214373C/en not_active Expired - Fee Related
- 1997-01-13 EG EG4497A patent/EG21218A/xx active
- 1997-01-15 DZ DZ970008A patent/DZ2163A1/fr active
- 1997-01-16 AR ARP970100170A patent/AR005485A1/es unknown
- 1997-01-17 TN TNTNSN97013A patent/TNSN97013A1/fr unknown
- 1997-01-20 TW TW086100557A patent/TW412586B/zh not_active IP Right Cessation
- 1997-09-04 DK DK100797A patent/DK100797A/da not_active Application Discontinuation
- 1997-09-18 OA OA70080A patent/OA10618A/en unknown
-
1998
- 1998-07-28 HK HK98109477A patent/HK1008560A1/xx not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| GB9601030D0 (en) | 1996-03-20 |
| PL322305A1 (en) | 1998-01-19 |
| EG21218A (en) | 2001-02-28 |
| WO1997026494A1 (en) | 1997-07-24 |
| CA2214373C (en) | 2002-04-02 |
| TR199700982T1 (xx) | 1998-01-21 |
| CA2214373A1 (en) | 1997-07-24 |
| TW412586B (en) | 2000-11-21 |
| PT820574E (pt) | 2002-08-30 |
| PL183667B1 (pl) | 2002-06-28 |
| GB2309227A (en) | 1997-07-23 |
| CN1181806A (zh) | 1998-05-13 |
| DE69710819T2 (de) | 2003-06-18 |
| AU1386597A (en) | 1997-08-11 |
| GB9626665D0 (en) | 1997-02-12 |
| DE69710819D1 (de) | 2002-04-11 |
| HK1008560A1 (en) | 1999-05-14 |
| NZ325367A (en) | 1999-02-25 |
| EP0820574A1 (en) | 1998-01-28 |
| DK100797A (da) | 1997-09-04 |
| AU689056B2 (en) | 1998-03-19 |
| MX9707070A (es) | 1997-11-29 |
| ZA9778B (en) | 1997-09-29 |
| TNSN97013A1 (fr) | 1999-12-31 |
| ATE214146T1 (de) | 2002-03-15 |
| GB2309227B (en) | 1999-09-29 |
| JPH10503971A (ja) | 1998-04-14 |
| ES2174213T3 (es) | 2002-11-01 |
| JP3168013B2 (ja) | 2001-05-21 |
| OA10618A (en) | 2002-08-30 |
| DZ2163A1 (fr) | 2002-12-01 |
| EP0820574B1 (en) | 2002-03-06 |
| US6111155A (en) | 2000-08-29 |
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