EA200201126A1 - Управление производством потока продукта сжиженного природного газа - Google Patents
Управление производством потока продукта сжиженного природного газаInfo
- Publication number
- EA200201126A1 EA200201126A1 EA200201126A EA200201126A EA200201126A1 EA 200201126 A1 EA200201126 A1 EA 200201126A1 EA 200201126 A EA200201126 A EA 200201126A EA 200201126 A EA200201126 A EA 200201126A EA 200201126 A1 EA200201126 A1 EA 200201126A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- flow rate
- natural gas
- liquefied natural
- mixed refrigerant
- set point
- Prior art date
Links
- 239000003949 liquefied natural gas Substances 0.000 title abstract 8
- 239000003507 refrigerant Substances 0.000 abstract 10
- 230000001419 dependent effect Effects 0.000 abstract 4
Classifications
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0244—Operation; Control and regulation; Instrumentation
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
- F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
- F25J1/0052—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream
- F25J1/0055—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by vaporising a liquid refrigerant stream originating from an incorporated cascade
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0211—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle
- F25J1/0212—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a multi-component refrigerant [MCR] fluid in a closed vapor compression cycle as a single flow MCR cycle
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0258—Construction and layout of liquefaction equipments, e.g. valves, machines vertical layout of the equipments within in the cold box
-
- 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
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
- F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
- F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
- F25J1/0269—Arrangement of liquefaction units or equipments fulfilling the same process step, e.g. multiple "trains" concept
- F25J1/0271—Inter-connecting multiple cold equipments within or downstream of the cold box
- F25J1/0272—Multiple identical heat exchangers in parallel
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Chemical & Material Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Bakery Products And Manufacturing Methods Therefor (AREA)
- Alcoholic Beverages (AREA)
Abstract
При управлении производством сжиженного природного газа (31) измеряют температуру (50) и скорость (55) потока сжиженного природного газа (31); поддерживают скорость потока тяжелого смешанного хладагента (60а) на установленном оператором заданном значении (80) и определяют скорость потока легкого смешанного хладагента (86) по (i) скорости потока тяжелого смешанного хладагента (80) и (ii) установленном оператором заданном значении для отношения скорости потока тяжелого смешанного хладагента к скорости потока легкого смешанного хладагента (81); определяют зависимое установочное значение (91) для отношения скорости потока сжиженного природного газа к скорости потока тяжелого смешанного хладагента так, чтобы температура (50) сжиженного природного газа поддерживалась на установленном оператором заданном значении (90); определяют зависимое установочное значение (95) для скорости потока сжиженного природного газа (95) по (i) зависимому установочному значению (91) для отношения скорости потока продукта сжиженного природного газа к скорости потока тяжелого смешанного хладагента и (ii) скорости потока тяжелого смешанного хладагента (60с); и поддерживают скорость (55а) потока сжиженного природного газа на ее зависимом установочном значении (95).Международная заявка была опубликована вместе с отчетом о международном поиске.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP00201470 | 2000-04-25 | ||
PCT/EP2001/004661 WO2001081845A1 (en) | 2000-04-25 | 2001-04-24 | Controlling the production of a liquefied natural gas product stream |
Publications (2)
Publication Number | Publication Date |
---|---|
EA200201126A1 true EA200201126A1 (ru) | 2003-04-24 |
EA004468B1 EA004468B1 (ru) | 2004-04-29 |
Family
ID=8171392
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA200201126A EA004468B1 (ru) | 2000-04-25 | 2001-04-24 | Управление производством потока продукта сжиженного природного газа |
Country Status (18)
Country | Link |
---|---|
US (2) | US6725688B2 (ru) |
EP (1) | EP1281033B1 (ru) |
JP (1) | JP4990461B2 (ru) |
KR (1) | KR100830075B1 (ru) |
CN (1) | CN1211629C (ru) |
AT (1) | ATE317536T1 (ru) |
AU (2) | AU5481601A (ru) |
DE (1) | DE60117136D1 (ru) |
DZ (1) | DZ3339A1 (ru) |
EA (1) | EA004468B1 (ru) |
EG (1) | EG23193A (ru) |
ES (1) | ES2258081T3 (ru) |
GC (1) | GC0000279A (ru) |
MY (1) | MY128820A (ru) |
NO (1) | NO334586B1 (ru) |
PT (1) | PT1281033E (ru) |
TW (1) | TW500906B (ru) |
WO (1) | WO2001081845A1 (ru) |
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US7074322B2 (en) | 2002-09-30 | 2006-07-11 | Bp Corporation North America Inc. | System and method for liquefying variable selected quantities of light hydrocarbon gas with a plurality of light hydrocarbon gas liquefaction trains |
US7047764B2 (en) | 2002-09-30 | 2006-05-23 | Bp Corporation North America Inc. | Modular LNG process |
KR100486641B1 (ko) * | 2002-11-20 | 2005-04-29 | 태산엘시디 주식회사 | 아날로그 게인 조정을 이용한 질량유량 제어기 및 동작방법 |
TWI314637B (en) * | 2003-01-31 | 2009-09-11 | Shell Int Research | Process of liquefying a gaseous, methane-rich feed to obtain liquefied natural gas |
US6964180B1 (en) * | 2003-10-13 | 2005-11-15 | Atp Oil & Gas Corporation | Method and system for loading pressurized compressed natural gas on a floating vessel |
MXPA06014854A (es) * | 2004-06-18 | 2008-03-11 | Exxonmobil Upstream Res Co | Planta de gas natural licuado de capacidad escalable. |
CN101163772A (zh) * | 2005-02-28 | 2008-04-16 | 霍尼韦尔国际公司 | 掺混制冷剂的改进方法 |
US20060260330A1 (en) | 2005-05-19 | 2006-11-23 | Rosetta Martin J | Air vaporizor |
MX2008015056A (es) * | 2006-06-27 | 2008-12-10 | Fluor Tech Corp | Configuraciones y metodos de recuperacion de etano. |
US20090241593A1 (en) * | 2006-07-14 | 2009-10-01 | Marco Dick Jager | Method and apparatus for cooling a hydrocarbon stream |
EP1921406A1 (en) * | 2006-11-08 | 2008-05-14 | Honeywell Control Systems Ltd. | A process of liquefying a gaseous methane-rich feed for obtaining liquid natural gas |
US8650906B2 (en) * | 2007-04-25 | 2014-02-18 | Black & Veatch Corporation | System and method for recovering and liquefying boil-off gas |
US8783061B2 (en) * | 2007-06-12 | 2014-07-22 | Honeywell International Inc. | Apparatus and method for optimizing a natural gas liquefaction train having a nitrogen cooling loop |
EP2165138A2 (en) * | 2007-07-12 | 2010-03-24 | Shell Internationale Research Maatschappij B.V. | Method and apparatus for cooling a hydrocarbon stream |
US20090025422A1 (en) * | 2007-07-25 | 2009-01-29 | Air Products And Chemicals, Inc. | Controlling Liquefaction of Natural Gas |
US9243842B2 (en) * | 2008-02-15 | 2016-01-26 | Black & Veatch Corporation | Combined synthesis gas separation and LNG production method and system |
CA2732653C (en) * | 2008-09-08 | 2014-10-14 | Conocophillips Company | System for incondensable component separation in a liquefied natural gas facility |
MY161121A (en) * | 2008-09-19 | 2017-04-14 | Shell Int Research | Method for cooling a hydrocarbon stream and an apparatus therefor |
JP5191969B2 (ja) * | 2009-09-30 | 2013-05-08 | 三菱重工コンプレッサ株式会社 | ガス処理装置 |
WO2011051226A2 (en) * | 2009-10-27 | 2011-05-05 | Shell Internationale Research Maatschappij B.V. | Apparatus and method for cooling and liquefying a fluid |
US9441877B2 (en) | 2010-03-17 | 2016-09-13 | Chart Inc. | Integrated pre-cooled mixed refrigerant system and method |
US9562717B2 (en) | 2010-03-25 | 2017-02-07 | The University Of Manchester | Refrigeration process |
US9982951B2 (en) * | 2010-03-31 | 2018-05-29 | Linde Aktiengesellschaft | Main heat exchanger and a process for cooling a tube side stream |
US10113127B2 (en) | 2010-04-16 | 2018-10-30 | Black & Veatch Holding Company | Process for separating nitrogen from a natural gas stream with nitrogen stripping in the production of liquefied natural gas |
WO2012075266A2 (en) | 2010-12-01 | 2012-06-07 | Black & Veatch Corporation | Ngl recovery from natural gas using a mixed refrigerant |
US10139157B2 (en) | 2012-02-22 | 2018-11-27 | Black & Veatch Holding Company | NGL recovery from natural gas using a mixed refrigerant |
US11428463B2 (en) | 2013-03-15 | 2022-08-30 | Chart Energy & Chemicals, Inc. | Mixed refrigerant system and method |
US11408673B2 (en) | 2013-03-15 | 2022-08-09 | Chart Energy & Chemicals, Inc. | Mixed refrigerant system and method |
CA3140415A1 (en) | 2013-03-15 | 2014-09-18 | Chart Energy & Chemicals, Inc. | Mixed refrigerant system and method |
US10563913B2 (en) | 2013-11-15 | 2020-02-18 | Black & Veatch Holding Company | Systems and methods for hydrocarbon refrigeration with a mixed refrigerant cycle |
US9574822B2 (en) | 2014-03-17 | 2017-02-21 | Black & Veatch Corporation | Liquefied natural gas facility employing an optimized mixed refrigerant system |
EP2977431A1 (en) | 2014-07-24 | 2016-01-27 | Shell Internationale Research Maatschappij B.V. | A hydrocarbon condensate stabilizer and a method for producing a stabilized hydrocarbon condenstate stream |
EP2977430A1 (en) | 2014-07-24 | 2016-01-27 | Shell Internationale Research Maatschappij B.V. | A hydrocarbon condensate stabilizer and a method for producing a stabilized hydrocarbon condenstate stream |
AR105277A1 (es) | 2015-07-08 | 2017-09-20 | Chart Energy & Chemicals Inc | Sistema y método de refrigeración mixta |
WO2017097764A1 (en) | 2015-12-08 | 2017-06-15 | Shell Internationale Research Maatschappij B.V. | Controlling refrigerant compression power in a natural gas liquefaction process |
US10393429B2 (en) * | 2016-04-06 | 2019-08-27 | Air Products And Chemicals, Inc. | Method of operating natural gas liquefaction facility |
US10571189B2 (en) | 2017-12-21 | 2020-02-25 | Shell Oil Company | System and method for operating a liquefaction train |
US10935312B2 (en) | 2018-08-02 | 2021-03-02 | Air Products And Chemicals, Inc. | Balancing power in split mixed refrigerant liquefaction system |
CN111090294B (zh) * | 2019-12-31 | 2024-06-07 | 合肥万豪能源设备有限责任公司 | 一种冷箱自适应控制装置和控制方法 |
US20220074654A1 (en) * | 2020-09-04 | 2022-03-10 | Air Products And Chemicals, Inc. | Method to control the cooldown of main heat exchangers in liquefied natural gas plant |
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US3929438A (en) | 1970-09-28 | 1975-12-30 | Phillips Petroleum Co | Refrigeration process |
JPS56105284A (en) * | 1980-01-23 | 1981-08-21 | Hitachi Ltd | Method of liquefying and storing gas |
US4381814A (en) * | 1980-10-01 | 1983-05-03 | Phillips Petroleum Company | Control of heat transfer from heat exchangers in parallel |
US4901533A (en) * | 1986-03-21 | 1990-02-20 | Linde Aktiengesellschaft | Process and apparatus for the liquefaction of a natural gas stream utilizing a single mixed refrigerant |
US4809154A (en) * | 1986-07-10 | 1989-02-28 | Air Products And Chemicals, Inc. | Automated control system for a multicomponent refrigeration system |
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US5746066A (en) * | 1996-09-17 | 1998-05-05 | Manley; David B. | Pre-fractionation of cracked gas or olefins fractionation by one or two mixed refrigerant loops and cooling water |
DE29713045U1 (de) * | 1997-07-23 | 1998-01-08 | Theod. Mahr Söhne GmbH, 52068 Aachen | Wärmestation für eine Warmluft-Kirchenheizung |
US5791160A (en) * | 1997-07-24 | 1998-08-11 | Air Products And Chemicals, Inc. | Method and apparatus for regulatory control of production and temperature in a mixed refrigerant liquefied natural gas facility |
EG22293A (en) * | 1997-12-12 | 2002-12-31 | Shell Int Research | Process ofliquefying a gaseous methane-rich feed to obtain liquefied natural gas |
TW421704B (en) * | 1998-11-18 | 2001-02-11 | Shell Internattonale Res Mij B | Plant for liquefying natural gas |
US6647744B2 (en) * | 2002-01-30 | 2003-11-18 | Exxonmobil Upstream Research Company | Processes and systems for liquefying natural gas |
-
2001
- 2001-04-23 EG EG20010399A patent/EG23193A/xx active
- 2001-04-23 MY MYPI20011902A patent/MY128820A/en unknown
- 2001-04-23 GC GCP20011304 patent/GC0000279A/en active
- 2001-04-24 PT PT01927923T patent/PT1281033E/pt unknown
- 2001-04-24 AT AT01927923T patent/ATE317536T1/de not_active IP Right Cessation
- 2001-04-24 WO PCT/EP2001/004661 patent/WO2001081845A1/en active IP Right Grant
- 2001-04-24 DE DE60117136T patent/DE60117136D1/de not_active Expired - Lifetime
- 2001-04-24 CN CNB018085350A patent/CN1211629C/zh not_active Expired - Fee Related
- 2001-04-24 AU AU5481601A patent/AU5481601A/xx active Pending
- 2001-04-24 AU AU2001254816A patent/AU2001254816B2/en not_active Expired
- 2001-04-24 EA EA200201126A patent/EA004468B1/ru not_active IP Right Cessation
- 2001-04-24 DZ DZ013339A patent/DZ3339A1/fr active
- 2001-04-24 EP EP01927923A patent/EP1281033B1/en not_active Expired - Lifetime
- 2001-04-24 JP JP2001578888A patent/JP4990461B2/ja not_active Expired - Fee Related
- 2001-04-24 US US10/258,636 patent/US6725688B2/en not_active Expired - Lifetime
- 2001-04-24 ES ES01927923T patent/ES2258081T3/es not_active Expired - Lifetime
- 2001-04-24 KR KR1020027014280A patent/KR100830075B1/ko not_active IP Right Cessation
- 2001-08-21 TW TW090120476A patent/TW500906B/zh active
-
2002
- 2002-10-24 NO NO20025103A patent/NO334586B1/no not_active IP Right Cessation
-
2003
- 2003-11-12 US US10/706,409 patent/US6789394B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
ATE317536T1 (de) | 2006-02-15 |
EA004468B1 (ru) | 2004-04-29 |
TW500906B (en) | 2002-09-01 |
CN1211629C (zh) | 2005-07-20 |
EP1281033B1 (en) | 2006-02-08 |
ES2258081T3 (es) | 2006-08-16 |
GC0000279A (en) | 2006-11-01 |
KR20030001449A (ko) | 2003-01-06 |
NO20025103D0 (no) | 2002-10-24 |
US20030046953A1 (en) | 2003-03-13 |
JP4990461B2 (ja) | 2012-08-01 |
AU2001254816B2 (en) | 2004-04-22 |
PT1281033E (pt) | 2006-06-30 |
NO334586B1 (no) | 2014-04-14 |
WO2001081845A1 (en) | 2001-11-01 |
CN1426524A (zh) | 2003-06-25 |
NO20025103L (no) | 2002-12-18 |
MY128820A (en) | 2007-02-28 |
US6789394B2 (en) | 2004-09-14 |
DE60117136D1 (de) | 2006-04-20 |
EG23193A (en) | 2001-07-31 |
DZ3339A1 (fr) | 2001-11-01 |
US20040093896A1 (en) | 2004-05-20 |
KR100830075B1 (ko) | 2008-05-16 |
US6725688B2 (en) | 2004-04-27 |
EP1281033A1 (en) | 2003-02-05 |
AU5481601A (en) | 2001-11-07 |
JP2003532047A (ja) | 2003-10-28 |
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