EA200700700A1 - Конфигурации и способы для когенерации сжиженного нефтяного газа и энергии - Google Patents

Конфигурации и способы для когенерации сжиженного нефтяного газа и энергии

Info

Publication number
EA200700700A1
EA200700700A1 EA200700700A EA200700700A EA200700700A1 EA 200700700 A1 EA200700700 A1 EA 200700700A1 EA 200700700 A EA200700700 A EA 200700700A EA 200700700 A EA200700700 A EA 200700700A EA 200700700 A1 EA200700700 A1 EA 200700700A1
Authority
EA
Eurasian Patent Office
Prior art keywords
lng
energy
column
lean
cogeneration
Prior art date
Application number
EA200700700A
Other languages
English (en)
Other versions
EA010641B1 (ru
Inventor
Джон Мак
Original Assignee
Флуор Текнолоджиз Корпорейшн
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 Флуор Текнолоджиз Корпорейшн filed Critical Флуор Текнолоджиз Корпорейшн
Publication of EA200700700A1 publication Critical patent/EA200700700A1/ru
Publication of EA010641B1 publication Critical patent/EA010641B1/ru

Links

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
    • 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
    • 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
    • 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
    • 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
    • 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
    • F25J2200/74—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
    • 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
    • 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

Установка СПГ выполнена с возможностью получения обогащенного СПГ и производства СНГ, обедненного СПГ и энергии, с использованием по меньшей мере одной фракционнной колонны, в которой фракционную часть установки можно термически соединить с энергетическим циклом, в котором использовано остаточное охлаждение обработанного обедненного СПГ. Является более предпочтительным, чтобы жидкую часть обогащенного СПГ накачивали до давления и нагревали, а нагнетаемую и перегретую часть перед ее подачей в колонну расширяли для получения электроэнергии. Пар, отводимый с верха колонны, частично конденсируют, обеспечивая колонну флегмой для повышения выхода СПГ, а затем конденсируют остаточный пар, с использованием охлаждающего состава обогащенного СПГ, образуя обедненный продукт СПГ, который затем накачивают до давления в трубопроводе и впоследствии испаряют с использованием нагретой текучей среды энергетического цикла.
EA200700700A 2004-09-22 2005-08-30 Способ обработки спг и получения энергии и установка для его осуществления EA010641B1 (ru)

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 (2)

Publication Number Publication Date
EA200700700A1 true EA200700700A1 (ru) 2007-10-26
EA010641B1 EA010641B1 (ru) 2008-10-30

Family

ID=36119213

Family Applications (1)

Application Number Title Priority Date Filing Date
EA200700700A EA010641B1 (ru) 2004-09-22 2005-08-30 Способ обработки спг и получения энергии и установка для его осуществления

Country Status (10)

Country Link
US (1) US8065890B2 (ru)
EP (1) EP1792129A1 (ru)
JP (1) JP4901740B2 (ru)
CN (1) CN101027526B (ru)
AU (1) AU2005290036B2 (ru)
CA (1) CA2578471C (ru)
EA (1) EA010641B1 (ru)
MX (1) MX2007003102A (ru)
NO (1) NO20071425L (ru)
WO (1) WO2006036441A1 (ru)

Families Citing this family (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4759571B2 (ja) * 2004-12-16 2011-08-31 フルオー・テクノロジーズ・コーポレイシヨン Ｌｎｇ再ガス化とｂｔｕ制御のための構成および方法
EP2032921A2 (en) * 2006-06-27 2009-03-11 Fluor Technologies Corporation Ethane recovery methods and configurations
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
RU2659858C2 (ru) * 2013-06-17 2018-07-04 Конокофиллипс Компани Единый каскадный процесс испарения и извлечения остатка сжиженного природного газа в применении, связанном с плавучими резервуарами
WO2016023098A1 (en) 2014-08-15 2016-02-18 1304338 Alberta Ltd. A method of removing carbon dioxide during liquid natural gas production from natural gas at gas pressure letdown stations
BR112017005575B1 (pt) 2014-09-30 2022-11-08 Dow Global Technologies Llc Processo para a recuperação de componentes c2 e c3 através de um sistema de produção de propileno por encomenda
CA2976071C (en) 2015-02-09 2020-10-27 Fluor Technologies Corporation Methods and configuration of an ngl recovery process for low pressure rich feed gas
PL413001A1 (pl) * 2015-07-06 2017-01-16 Tadeusz Bąk Sposób regazyfikacji skroplonego gazu ziemnego oraz system regazyfikacji skroplonego gazu ziemnego
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
CN109294647B (zh) * 2018-09-17 2021-08-13 广州智光节能有限公司 天然气的提纯系统
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
CN110847987B (zh) * 2019-12-24 2024-04-05 青岛中稷龙源能源科技有限公司 一种混合工质的lng冷能发电和综合利用系统及方法
CN112324530B (zh) * 2020-11-02 2022-07-19 江苏科技大学 船用lng冷能利用冷电联供系统
RU2758364C1 (ru) * 2021-03-10 2021-10-28 Андрей Владиславович Курочкин Способ реконструкции установки низкотемпературной сепарации газа для получения сжиженного природного газа (варианты)

Family Cites Families (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3394555A (en) 1964-11-10 1968-07-30 Mc Donnell Douglas Corp Power-refrigeration system utilizing waste heat
US3837172A (en) * 1972-06-19 1974-09-24 Synergistic Services Inc Processing liquefied natural gas to deliver methane-enriched gas at high pressure
GB1444176A (en) * 1972-11-17 1976-07-28 Garwin L Isotopically enriched helium - 4
DE2523672C3 (de) * 1975-05-28 1980-03-20 Gutehoffnungshuette Sterkrade Ag, 4200 Oberhausen Einrichtung zur Verdampfung von verflüssigtem Erdgas mit Hilfe einer Gasturbinenanlage mit geschlossenem Kreislauf
JPS5491648A (en) * 1977-12-29 1979-07-20 Toyokichi Nozawa Lnggfleon generation system
JPS597001B2 (ja) * 1978-11-25 1984-02-16 三井造船株式会社 液化天然ガス冷熱利用装置
JPS55123306A (en) * 1979-03-14 1980-09-22 Chiyoda Chem Eng & Constr Co Ltd Vaporization of liquefied natural gas and its energy recovering method
EP0043212B1 (en) * 1980-07-01 1985-09-11 Costain Petrocarbon Limited Producing power from a cryogenic liquid
JPS5773299A (en) * 1980-10-24 1982-05-07 Kobe Steel Ltd Gasification of liquefied natural gas
US4444015A (en) * 1981-01-27 1984-04-24 Chiyoda Chemical Engineering & Construction Co., Ltd. Method for recovering power according to a cascaded Rankine cycle by gasifying liquefied natural gas and utilizing the cold potential
US4551979A (en) 1981-05-11 1985-11-12 Soma Kurtis Method and apparatus for a thermodynamic cycle by use of distillation
JPS5822872A (ja) * 1981-07-31 1983-02-10 東洋エンジニアリング株式会社 天燃ガス中のｌｐｇ回収方法
JPS58152128A (ja) * 1982-03-04 1983-09-09 Ishikawajima Harima Heavy Ind Co Ltd 液化天然ガスの冷熱利用発電方法
JPS60205166A (ja) * 1984-03-30 1985-10-16 石川島播磨重工業株式会社 液化天然ガス冷熱発電設備の再生ガス液化方法
US4711651A (en) * 1986-12-19 1987-12-08 The M. W. Kellogg Company Process for separation of hydrocarbon gases
US5114451A (en) * 1990-03-12 1992-05-19 Elcor Corporation Liquefied natural gas processing
US5295350A (en) * 1992-06-26 1994-03-22 Texaco Inc. Combined power cycle with liquefied natural gas (LNG) and synthesis or fuel gas
US5615561A (en) * 1994-11-08 1997-04-01 Williams Field Services Company LNG production in cryogenic natural gas processing plants
JPH08269468A (ja) * 1995-03-30 1996-10-15 Osaka Gas Co Ltd 分留機能付き液化天然ガス気化設備
JP3895386B2 (ja) * 1996-02-29 2007-03-22 シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ 液化天然ガス中低沸点成分量の低減
US5944984A (en) 1996-03-20 1999-08-31 Ormat Industries Ltd. Solvent deasphalting unit and method for using the same
US5890377A (en) * 1997-11-04 1999-04-06 Abb Randall Corporation Hydrocarbon gas separation process
TW432192B (en) * 1998-03-27 2001-05-01 Exxon Production Research Co Producing power from pressurized liquefied natural gas
US6233938B1 (en) * 1998-07-14 2001-05-22 Helios Energy Technologies, Inc. Rankine cycle and working fluid therefor
JP3500081B2 (ja) * 1998-12-21 2004-02-23 三菱重工業株式会社 液化天然ガスの分離装置並びに分離方法、発電方法及び液化天然ガスの使用方法
US6367286B1 (en) * 2000-11-01 2002-04-09 Black & Veatch Pritchard, Inc. System and process for liquefying high pressure natural gas
FR2818365B1 (fr) * 2000-12-18 2003-02-07 Technip Cie Procede de refrigeration d'un gaz liquefie, gaz obtenus par ce procede, et installation mettant en oeuvre celui-ci
WO2002097252A1 (en) * 2001-05-30 2002-12-05 Conoco Inc. Lng regasification process and system
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
US6945075B2 (en) * 2002-10-23 2005-09-20 Elkcorp Natural gas liquefaction
JP4240999B2 (ja) * 2002-10-30 2009-03-18 三菱重工業株式会社 液化天然ガスの分離装置
US7143606B2 (en) 2002-11-01 2006-12-05 L'air Liquide-Societe Anonyme A'directoire Et Conseil De Surveillance Pour L'etide Et L'exploitation Des Procedes Georges Claude Combined air separation natural gas liquefaction plant
US6751959B1 (en) * 2002-12-09 2004-06-22 Tennessee Valley Authority Simple and compact low-temperature power cycle
US7278281B2 (en) * 2003-11-13 2007-10-09 Foster Wheeler Usa Corporation Method and apparatus for reducing C2 and C3 at LNG receiving terminals
US8132411B2 (en) * 2008-11-06 2012-03-13 Air Products And Chemicals, Inc. Rankine cycle for LNG vaporization/power generation process

Also Published As

Publication number Publication date
EP1792129A1 (en) 2007-06-06
MX2007003102A (es) 2007-05-16
EA010641B1 (ru) 2008-10-30
CA2578471A1 (en) 2006-04-06
US20080190135A1 (en) 2008-08-14
NO20071425L (no) 2007-04-20
JP4901740B2 (ja) 2012-03-21
CA2578471C (en) 2010-09-21
US8065890B2 (en) 2011-11-29
CN101027526B (zh) 2010-12-08
JP2008513726A (ja) 2008-05-01
CN101027526A (zh) 2007-08-29
AU2005290036B2 (en) 2008-06-12
AU2005290036A1 (en) 2006-04-06
WO2006036441A1 (en) 2006-04-06

Similar Documents

Publication Publication Date Title
EA200700700A1 (ru) Конфигурации и способы для когенерации сжиженного нефтяного газа и энергии
CA2600155A1 (en) Integrated of lng regasification with refinery and power generation
EA200800893A1 (ru) Объединенные извлечения газоконденсатных жидкостей и сжижение природного газа
NO20055881L (no) Effektsyklus med regassifisering av kondensert naturgass
EA201790092A1 (ru) Комбинированный цикл регазификации топлива и производства энергии
AR032329A1 (es) Procesos y aparatos para recuperar los componentes relativamente menos volatiles de una alimentacion de gas rica en metano para producir un producto de gnl mientras que se rechazan los componentes relativamente mas volatiles los cuales son subsiguientemente licuados para producir gnl
BRPI0515295A (pt) método e sistema para o processamento de gás natural liquefeito
AR094357A1 (es) Proceso integrado para lgn (recuperación de líquidos de gas natural) y gnl (licuefacción de gas natural)
GB2450667B (en) Method for vaporizing and heating a cryogenic fluid
UY28977A1 (es) Sistema de gas natural licuado que emplea columna de extraccion de pesados refuidos con condensacion en la parte superior
PE20060219A1 (es) Tratamiento de gas natural licuado
NO20061001L (no) Fremgangsmate og innretning for gjennomforing av en termodynamisk syklus
GB2487111A (en) Liquefied natural gas and hydrocarbon gas processiing
WO2010143046A3 (en) Multi-level organic rankine cycle power system
PE20041074A1 (es) Produccion de gas natural licuado (gnl) en plantas criogenicas de procesamiento de gas natural
MY161650A (en) Liquefied natural gas and hydrocarbon gas processing
DE602008005791D1 (de) Einheit zur lagerung und regasifizierung von schwimmendem flüssigerdgas sowie verfahren zur regasifizierung von flüssigerdgas mit besagter einheit
UY31371A1 (es) Método para la producción de gas natural licuado
WO2007011921A3 (en) Configurations and methods for power generation in lng regasification terminals
PE20141165A1 (es) Metodo y aparato de producir y utilizar energia termica en una planta de calor y electricidad combinada
RU2009140093A (ru) Усадочный туннель для осуществления процесса усадки термоусаживаемой пленки на упаковках или упаковочных элементах
KR960041990A (ko) Lng로부터 질소 제거 방법
RU2009101148A (ru) Способ и устройство для обработки потока углеводородов и устройство для его осуществления
WO2013135993A3 (fr) Procédé et appareil de séparation d'un mélange contenant du dioxyde de carbone par distillation
EA201592015A1 (ru) Способ и устройство для производства сжиженного потока углеводородов

Legal Events

Date Code Title Description
MM4A Lapse of a eurasian patent due to non-payment of renewal fees within the time limit in the following designated state(s)

Designated state(s): AM AZ BY KZ KG MD TJ TM RU