NO20071425L - Konfigurasjoner og fremgangsmater for kombinert produksjon av LPG og kraft - Google Patents
Konfigurasjoner og fremgangsmater for kombinert produksjon av LPG og kraftInfo
- Publication number
- NO20071425L NO20071425L NO20071425A NO20071425A NO20071425L NO 20071425 L NO20071425 L NO 20071425L NO 20071425 A NO20071425 A NO 20071425A NO 20071425 A NO20071425 A NO 20071425A NO 20071425 L NO20071425 L NO 20071425L
- Authority
- NO
- Norway
- Prior art keywords
- lng
- column
- power
- lpg
- rich
- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
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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
- F25J3/0228—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
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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
- F25J3/0228—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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
- F17C2265/00—Effects achieved by gas storage or gas handling
- F17C2265/05—Regasification
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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
- 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
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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
- 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
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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
- 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
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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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/62—Ethane or ethylene
-
- 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
- F25J2240/00—Processes or apparatus involving steps for expanding of process streams
- F25J2240/70—Steam turbine, e.g. used in a Rankine 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
- F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
- F25J2290/10—Mathematical formulae, modeling, plot or curves; Design methods
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P80/00—Climate change mitigation technologies for sector-wide applications
- Y02P80/10—Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
- Y02P80/15—On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Et LNG-anlegg er utformet for å motta rik LNG og for å produsere LPG, mager LNG samt kraft ved å benytte minst én fraksjoneringskolonne, hvor fraksjoneringsdelen av anlegget kan eventuelt være termisk koblet til en kraftsyklus som anvender restkjøling fra det behandlete magre LNG. Det er mest foretrukket at en væskedel av den rike LNG pumpes til trykk og oppvarmes, og den trykksatte overhetete delen ekspanderes for å produsere elektrisk energi før den fødes til kolonnen. Toppdampen til kolonnen er delvis kondensert, og sørger for kolonnetilbakeløp for høy NGL-utvinning, og restdampen kondenseres ytterligere ved bruk av kjøleinnholdet til den rike LNG som danner det magre LNG-produktet, som videre pumpes til rørledningstrykk og deretter fordampes ved bruk av oppvarmet arbeidsfluid til kraftsyklusen.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US61247304P | 2004-09-22 | 2004-09-22 | |
PCT/US2005/031005 WO2006036441A1 (en) | 2004-09-22 | 2005-08-30 | Configurations and methods for lpg and power cogeneration |
Publications (1)
Publication Number | Publication Date |
---|---|
NO20071425L true NO20071425L (no) | 2007-04-20 |
Family
ID=36119213
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO20071425A NO20071425L (no) | 2004-09-22 | 2007-03-16 | Konfigurasjoner og fremgangsmater for kombinert produksjon av LPG og kraft |
Country Status (10)
Country | Link |
---|---|
US (1) | US8065890B2 (no) |
EP (1) | EP1792129A1 (no) |
JP (1) | JP4901740B2 (no) |
CN (1) | CN101027526B (no) |
AU (1) | AU2005290036B2 (no) |
CA (1) | CA2578471C (no) |
EA (1) | EA010641B1 (no) |
MX (1) | MX2007003102A (no) |
NO (1) | NO20071425L (no) |
WO (1) | WO2006036441A1 (no) |
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MX2007007021A (es) * | 2004-12-16 | 2007-08-14 | Fluor Tech Corp | Configuraciones y metodos para regasificacion de gas natural licuado y control de valor calorico. |
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CA2552327C (en) | 2006-07-13 | 2014-04-15 | Mackenzie Millar | Method for selective extraction of natural gas liquids from "rich" natural gas |
US9470452B2 (en) * | 2006-07-27 | 2016-10-18 | Cosmodyne, LLC | Imported LNG treatment |
US8132411B2 (en) * | 2008-11-06 | 2012-03-13 | Air Products And Chemicals, Inc. | Rankine cycle for LNG vaporization/power generation process |
CN101832157A (zh) * | 2010-03-08 | 2010-09-15 | 翁志远 | 一种使用低温液体做工质的热机发电技术 |
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. |
RU2495258C1 (ru) * | 2012-07-23 | 2013-10-10 | Общество с ограниченной ответственностью "Горизонт Инжиниринг" | Легкокипящая смесь органических соединений, преимущественно рабочее тело энергетической установки, работающей по циклу ренкина |
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 |
US9835373B2 (en) * | 2013-06-17 | 2017-12-05 | Conocophillips Company | Integrated cascade process for vaporization and recovery of residual LNG in a floating tank application |
CA2958091C (en) | 2014-08-15 | 2021-05-18 | 1304338 Alberta Ltd. | A method of removing carbon dioxide during liquid natural gas production from natural gas at gas pressure letdown stations |
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PL413001A1 (pl) * | 2015-07-06 | 2017-01-16 | Tadeusz Bąk | Sposób regazyfikacji skroplonego gazu ziemnego oraz system regazyfikacji skroplonego gazu ziemnego |
CN105065901B (zh) * | 2015-08-14 | 2017-04-19 | 中国石油化工股份有限公司青岛安全工程研究院 | 用于液化天然气接收站的轻烃回收工艺 |
CN105065900B (zh) * | 2015-08-14 | 2017-04-19 | 中国石油化工股份有限公司青岛安全工程研究院 | Lng接收站轻烃回收工艺 |
WO2017045055A1 (en) | 2015-09-16 | 2017-03-23 | 1304342 Alberta Ltd. | A method of preparing natural gas at a gas pressure reduction stations to produce liquid natural gas (lng) |
US10006701B2 (en) | 2016-01-05 | 2018-06-26 | Fluor Technologies Corporation | Ethane recovery or ethane rejection operation |
RU2629344C1 (ru) * | 2016-11-22 | 2017-08-28 | Андрей Владиславович Курочкин | Установка компримирования попутного нефтяного газа |
US20190003343A1 (en) * | 2017-06-30 | 2019-01-03 | Uop Llc | Process and apparatus for using a waste heat stream in an aromatics complex |
US10662824B2 (en) * | 2017-08-08 | 2020-05-26 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to power using organic Rankine cycle |
US10690407B2 (en) | 2017-08-08 | 2020-06-23 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous power and potable water using organic Rankine cycle and modified multi-effect-distillation systems |
US10436077B2 (en) | 2017-08-08 | 2019-10-08 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to potable water using modified multi-effect distillation system |
US10684079B2 (en) | 2017-08-08 | 2020-06-16 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous power and cooling capacities using modified goswami system |
US10677104B2 (en) | 2017-08-08 | 2020-06-09 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous power, cooling and potable water using integrated mono-refrigerant triple cycle and modified multi-effect-distillation system |
US10487699B2 (en) | 2017-08-08 | 2019-11-26 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to cooling capacity using kalina cycle |
US10480355B2 (en) | 2017-08-08 | 2019-11-19 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous power, cooling and potable water using modified goswami cycle and new modified multi-effect-distillation system |
US10443453B2 (en) | 2017-08-08 | 2019-10-15 | Saudi Araabian Oil Company | Natural gas liquid fractionation plant cooling capacity and potable water generation using integrated vapor compression-ejector cycle and modified multi-effect distillation system |
US10626756B2 (en) * | 2017-08-08 | 2020-04-21 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to power using dual turbines organic Rankine cycle |
US10494958B2 (en) | 2017-08-08 | 2019-12-03 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous power and cooling capacities using integrated organic-based compressor-ejector-expander triple cycles system |
US10451359B2 (en) | 2017-08-08 | 2019-10-22 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to power using Kalina cycle |
US10480354B2 (en) | 2017-08-08 | 2019-11-19 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous power and potable water using Kalina cycle and modified multi-effect-distillation system |
US10663234B2 (en) | 2017-08-08 | 2020-05-26 | Saudi Arabian Oil Company | Natural gas liquid fractionation plant waste heat conversion to simultaneous cooling capacity and potable water using kalina cycle and modified multi-effect distillation system |
JP7084219B2 (ja) * | 2018-06-15 | 2022-06-14 | 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 |
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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 |
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-
2005
- 2005-08-30 AU AU2005290036A patent/AU2005290036B2/en not_active Ceased
- 2005-08-30 JP JP2007532355A patent/JP4901740B2/ja not_active Expired - Fee Related
- 2005-08-30 EA EA200700700A patent/EA010641B1/ru not_active IP Right Cessation
- 2005-08-30 WO PCT/US2005/031005 patent/WO2006036441A1/en active Application Filing
- 2005-08-30 CA CA2578471A patent/CA2578471C/en not_active Expired - Fee Related
- 2005-08-30 EP EP05793897A patent/EP1792129A1/en not_active Withdrawn
- 2005-08-30 CN CN2005800320723A patent/CN101027526B/zh not_active Expired - Fee Related
- 2005-08-30 MX MX2007003102A patent/MX2007003102A/es active IP Right Grant
- 2005-08-30 US US11/574,271 patent/US8065890B2/en not_active Expired - Fee Related
-
2007
- 2007-03-16 NO NO20071425A patent/NO20071425L/no not_active Application Discontinuation
Also Published As
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AU2005290036A1 (en) | 2006-04-06 |
EP1792129A1 (en) | 2007-06-06 |
AU2005290036B2 (en) | 2008-06-12 |
CN101027526A (zh) | 2007-08-29 |
US20080190135A1 (en) | 2008-08-14 |
WO2006036441A1 (en) | 2006-04-06 |
JP4901740B2 (ja) | 2012-03-21 |
EA010641B1 (ru) | 2008-10-30 |
EA200700700A1 (ru) | 2007-10-26 |
MX2007003102A (es) | 2007-05-16 |
CN101027526B (zh) | 2010-12-08 |
JP2008513726A (ja) | 2008-05-01 |
CA2578471C (en) | 2010-09-21 |
CA2578471A1 (en) | 2006-04-06 |
US8065890B2 (en) | 2011-11-29 |
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