EA200700221A1 - Установка (варианты) и способ регазификации сжиженного природного газа - Google Patents
Установка (варианты) и способ регазификации сжиженного природного газаInfo
- Publication number
- EA200700221A1 EA200700221A1 EA200700221A EA200700221A EA200700221A1 EA 200700221 A1 EA200700221 A1 EA 200700221A1 EA 200700221 A EA200700221 A EA 200700221A EA 200700221 A EA200700221 A EA 200700221A EA 200700221 A1 EA200700221 A1 EA 200700221A1
- Authority
- EA
- Eurasian Patent Office
- Prior art keywords
- lng
- pressure
- regasification
- variants
- installation
- Prior art date
Links
Classifications
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- 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
- F25J3/0214—Liquefied 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
- F25J3/0238—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 2 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
- 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
- F25J2200/02—Processes or apparatus using separation by rectification in a single pressure main column system
-
- 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
- F25J2200/04—Processes or apparatus using separation by rectification in a dual pressure main column system
-
- 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
- F25J2200/72—Refluxing the column with at least a part of the totally condensed overhead 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/74—Refluxing the column with at least a part of the partially condensed overhead 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
- 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
- F25J2205/04—Processes or apparatus using other separation and/or other processing means using simple phase separation in a vessel or drum in the feed line, i.e. upstream of the fractionation step
-
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/62—Ethane or ethylene
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- 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
- F25J2235/00—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams
- F25J2235/60—Processes or apparatus involving steps for increasing the pressure or for conveying of liquid process streams the fluid being (a mixture of) hydrocarbons
-
- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/02—Expansion of a process fluid in a work-extracting turbine (i.e. isentropic expansion), e.g. of the feed stream
-
- 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
- F25J2245/00—Processes or apparatus involving steps for recycling of process streams
- F25J2245/02—Recycle of a stream in general, e.g. a by-pass stream
-
- 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
- F25J2270/02—Internal refrigeration with liquid vaporising loop
-
- 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/10—Mathematical formulae, modeling, plot or curves; Design methods
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (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)
Abstract
Состав СПГ из резервуара для хранения СПГ или другого источника модифицируется в процессе, в котором СПГ нагнетается до первого давления и разделяется на две части. Давление одной части сжатого СПГ затем понижается, и более тяжелые компоненты отделяются от СПГ с пониженным давлением, чтобы посредством этого образовать бедный СПГ. Бедный СПГ затем нагнетается до более высокого давления и объединяется с другой частью, чтобы образовать более бедный СПГ. Предпочтительно, разделение осуществляется с использованием деметанизатора, в котором часть продукта верхнего погона деметанизатора конденсируется, чтобы образовать бедный СПГ, в то время как другая часть используется для орошения колонны. В более предпочтительной конфигурации извлечение этана является изменяемым, и в еще других конфигурациях пропан или этан могут поставляться посредством дозирующего трубопровода.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US58461104P | 2004-06-30 | 2004-06-30 | |
US68318105P | 2005-05-20 | 2005-05-20 | |
PCT/US2005/022880 WO2006004723A1 (en) | 2004-06-30 | 2005-06-27 | Lng regasification configurations and methods |
Publications (2)
Publication Number | Publication Date |
---|---|
EA200700221A1 true EA200700221A1 (ru) | 2007-08-31 |
EA010743B1 EA010743B1 (ru) | 2008-10-30 |
Family
ID=35783200
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EA200700221A EA010743B1 (ru) | 2004-06-30 | 2005-06-27 | Установка (варианты) и способ регазификации сжиженного природного газа |
Country Status (8)
Country | Link |
---|---|
US (1) | US20080264100A1 (ru) |
EP (1) | EP1782010A4 (ru) |
AU (1) | AU2005259965B2 (ru) |
CA (1) | CA2574601C (ru) |
EA (1) | EA010743B1 (ru) |
MX (1) | MX2007000929A (ru) |
NO (1) | NO334716B1 (ru) |
WO (1) | WO2006004723A1 (ru) |
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EP1756496B1 (en) | 2004-01-16 | 2017-09-13 | Aker Kvaerner, Inc. | Gas conditioning process for the recovery of lpg/ngl (c2+) from lng |
FR2893627B1 (fr) * | 2005-11-18 | 2007-12-28 | Total Sa | Procede pour l'ajustement du pouvoir calorifique superieur du gaz dans la chaine du gnl. |
EP2024699A4 (en) * | 2006-05-23 | 2017-09-20 | Fluor Technologies Corporation | High ethane recovery configurations and methods in lng regasification facilities |
US9470452B2 (en) * | 2006-07-27 | 2016-10-18 | Cosmodyne, LLC | Imported LNG treatment |
US20100000234A1 (en) * | 2006-08-23 | 2010-01-07 | Eduard Coenraad Bras | Method and apparatus for the vaporization of a liquid hydrocarbon stream |
US8499581B2 (en) | 2006-10-06 | 2013-08-06 | Ihi E&C International Corporation | Gas conditioning method and apparatus for the recovery of LPG/NGL(C2+) from LNG |
WO2008070017A2 (en) * | 2006-12-04 | 2008-06-12 | Kellogg Brown & Root Llc | Method for adjusting heating value of lng |
US8695376B2 (en) * | 2007-04-13 | 2014-04-15 | Fluor Technologies Corporation | Configurations and methods for offshore LNG regasification and heating value conditioning |
US20080264099A1 (en) * | 2007-04-24 | 2008-10-30 | Conocophillips Company | Domestic gas product from an lng facility |
US8973398B2 (en) * | 2008-02-27 | 2015-03-10 | Kellogg Brown & Root Llc | Apparatus and method for regasification of liquefied natural gas |
KR20090107805A (ko) * | 2008-04-10 | 2009-10-14 | 대우조선해양 주식회사 | 천연가스 발열량 저감방법 및 장치 |
US20100122542A1 (en) * | 2008-11-17 | 2010-05-20 | Daewoo Shipbuilding & Marine Engineering Co., Ltd. | Method and apparatus for adjusting heating value of natural gas |
US9683703B2 (en) * | 2009-08-18 | 2017-06-20 | Charles Edward Matar | Method of storing and transporting light gases |
US8707730B2 (en) * | 2009-12-07 | 2014-04-29 | Alkane, Llc | Conditioning an ethane-rich stream for storage and transportation |
CA2805271A1 (en) * | 2010-07-21 | 2012-01-26 | Synfuels International, Inc. | Methods and systems for storing and transporting gases |
EA201390572A1 (ru) * | 2010-10-20 | 2013-11-29 | Киртикумар Натубхай Пател | Способ сепарации и извлечения этана и более тяжелых углеводородов из lng |
DE102010056581B4 (de) * | 2010-12-30 | 2013-04-04 | Gea Batignolles Technologies Thermiques | Anordnung zur Verdampfung von flüssigem Erdgas |
US10852060B2 (en) * | 2011-04-08 | 2020-12-01 | Pilot Energy Solutions, Llc | Single-unit gas separation process having expanded, post-separation vent stream |
CA2763081C (en) | 2011-12-20 | 2019-08-13 | Jose Lourenco | Method to produce liquefied natural gas (lng) at midstream natural gas liquids (ngls) recovery plants. |
CA2772479C (en) | 2012-03-21 | 2020-01-07 | Mackenzie Millar | Temperature controlled method to liquefy gas and a production plant using the method. |
CA2790961C (en) | 2012-05-11 | 2019-09-03 | Jose Lourenco | A method to recover lpg and condensates from refineries fuel gas streams. |
CA2787746C (en) | 2012-08-27 | 2019-08-13 | Mackenzie Millar | Method of producing and distributing liquid natural gas |
CA2798057C (en) | 2012-12-04 | 2019-11-26 | Mackenzie Millar | A method to produce lng at gas pressure letdown stations in natural gas transmission pipeline systems |
CA2813260C (en) | 2013-04-15 | 2021-07-06 | Mackenzie Millar | A method to produce lng |
US20140338393A1 (en) * | 2013-05-13 | 2014-11-20 | Rustam H. Sethna | Methods for blending liquefied natural gas |
US10288347B2 (en) | 2014-08-15 | 2019-05-14 | 1304338 Alberta Ltd. | Method of removing carbon dioxide during liquid natural gas production from natural gas at gas pressure letdown stations |
JP6527714B2 (ja) * | 2015-02-25 | 2019-06-05 | レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 液体燃料ガスの供給装置および供給方法 |
CN108431184B (zh) | 2015-09-16 | 2021-03-30 | 1304342阿尔伯塔有限公司 | 在气体减压站制备天然气以生产液体天然气(lng)的方法 |
RU170011U1 (ru) * | 2016-11-22 | 2017-04-11 | федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королева" | Криогенный насос-газификатор |
EP3600611A4 (en) * | 2017-03-20 | 2020-12-16 | ConocoPhillips Company | ALTERNATIVE DESIGN TO TWO RICH REFLUX HRU COLUMNS |
JP7026470B2 (ja) * | 2017-09-29 | 2022-02-28 | レール・リキード-ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード | 天然ガスの製造装置および天然ガスの製造方法 |
JP7051372B2 (ja) * | 2017-11-01 | 2022-04-11 | 東洋エンジニアリング株式会社 | 炭化水素の分離方法及び装置 |
JP7246285B2 (ja) * | 2019-08-28 | 2023-03-27 | 東洋エンジニアリング株式会社 | リーンlngの処理方法及び装置 |
CN112344204A (zh) * | 2020-10-23 | 2021-02-09 | 中国石油化工股份有限公司 | 一种低温乙烷装车方法 |
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GB1002566A (en) * | 1964-08-10 | 1965-08-25 | Conch Int Methane Ltd | Improved method of processing natural gas |
FR1501013A (fr) * | 1966-09-13 | 1967-11-10 | Air Liquide | Procédé de production d'un gaz riche en méthane, sous pression élevée à partirde gaz naturel liquide sous basse pression |
US3405530A (en) * | 1966-09-23 | 1968-10-15 | Exxon Research Engineering Co | Regasification and separation of liquefied natural gas |
US5114451A (en) * | 1990-03-12 | 1992-05-19 | Elcor Corporation | Liquefied natural gas processing |
US6581409B2 (en) * | 2001-05-04 | 2003-06-24 | Bechtel Bwxt Idaho, Llc | Apparatus for the liquefaction of natural gas and methods related to same |
US7069743B2 (en) * | 2002-02-20 | 2006-07-04 | Eric Prim | System and method for recovery of C2+ hydrocarbons contained in liquefied natural gas |
US6941771B2 (en) * | 2002-04-03 | 2005-09-13 | Howe-Baker Engineers, Ltd. | Liquid natural gas processing |
US6564579B1 (en) * | 2002-05-13 | 2003-05-20 | Black & Veatch Pritchard Inc. | Method for vaporizing and recovery of natural gas liquids from liquefied natural gas |
US6907752B2 (en) * | 2003-07-07 | 2005-06-21 | Howe-Baker Engineers, Ltd. | Cryogenic liquid natural gas recovery process |
US7155931B2 (en) * | 2003-09-30 | 2007-01-02 | Ortloff Engineers, Ltd. | Liquefied natural gas processing |
US7278281B2 (en) * | 2003-11-13 | 2007-10-09 | Foster Wheeler Usa Corporation | Method and apparatus for reducing C2 and C3 at LNG receiving terminals |
EP1861671B1 (en) * | 2005-03-22 | 2015-12-23 | Shell Internationale Research Maatschappij B.V. | Process and apparatus for extracting natural gas liquids from a stream of liquefied natural gas |
US7530236B2 (en) * | 2006-03-01 | 2009-05-12 | Rajeev Nanda | Natural gas liquid recovery |
WO2008070017A2 (en) * | 2006-12-04 | 2008-06-12 | Kellogg Brown & Root Llc | Method for adjusting heating value of lng |
-
2005
- 2005-06-27 WO PCT/US2005/022880 patent/WO2006004723A1/en active Application Filing
- 2005-06-27 CA CA002574601A patent/CA2574601C/en not_active Expired - Fee Related
- 2005-06-27 US US11/658,110 patent/US20080264100A1/en not_active Abandoned
- 2005-06-27 AU AU2005259965A patent/AU2005259965B2/en not_active Ceased
- 2005-06-27 EA EA200700221A patent/EA010743B1/ru not_active IP Right Cessation
- 2005-06-27 MX MX2007000929A patent/MX2007000929A/es unknown
- 2005-06-27 EP EP05763868.6A patent/EP1782010A4/en not_active Withdrawn
-
2007
- 2007-01-29 NO NO20070553A patent/NO334716B1/no not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
CA2574601C (en) | 2009-08-11 |
MX2007000929A (es) | 2007-04-16 |
CA2574601A1 (en) | 2006-01-12 |
US20080264100A1 (en) | 2008-10-30 |
EP1782010A1 (en) | 2007-05-09 |
AU2005259965A1 (en) | 2006-01-12 |
NO20070553L (no) | 2007-03-12 |
WO2006004723B1 (en) | 2006-08-17 |
EA010743B1 (ru) | 2008-10-30 |
EP1782010A4 (en) | 2014-08-13 |
WO2006004723A1 (en) | 2006-01-12 |
NO334716B1 (no) | 2014-05-12 |
AU2005259965B2 (en) | 2009-09-10 |
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